EPA-60Q/2-77-187b
September 1977
Environmental Protection Technology Series
EMISSION TESTING AND EVALUATION
OF FORD/KOPPERS'COKE
PUSHING CONTROL SYSTEM;
VOLUME II. APPENDICES
Industrial Environmental Research Labor?
Office of Research and Oevelopm
U.S. Environmental Protection Agency
Research Triangle Park, North Carolina 27711
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RESEARCH REPORTING SERIES
Research reports of the Office of Research and Development, U.S. Environmental Protection
Agency, have been grouped into five series. These five broad categories were established to
facilitate further development and application of environmental technology. Elimination of
traditional grouping was consciously planned to foster technology transfer and a maximum
interface in related fields. The five series are:
1. Environmental Health Effects Research
2. Environmental Protection Technology
3. Ecological Research
4. Environmental Monitoring
5. Socioeconomic Environmental Studies
This report has been assigned to the ENVIRONMENTAL PROTECTION TECHNOLOGY
series. This series describes research performed to develop and demonstrate instrumenta-
tion, equipment, and methodology to repair or prevent environmental degradation from point
and non-point sources of pollution. This work provides the new or improved technology
required for the control and treatment of pollution sources to meet environmental quality
standards
EPA REVIEW NOTICE
This report has been reviewed by the U.S. Environmental Protection Agency, and approved
for publication. Approval does not signify that the contents necessarily reflect the views and
policy of the Agency, nor does mention of trade names or commercial products constitute
endorsement or recommendation for use.
This document is available to the public through the National Technical Information Service,
Springfield, Virginia 22161.
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EPA-600/2-77-187b
September 1977
EMISSION TESTING AND EVALUATION
OF FORD/KOPPERS COKE
PUSHING CONTROL SYSTEM;
VOLUME II. APPENDICES
by
Fred Cooper, Thomas Loch,
John Mutchler, and Janet Vecchio
(Clayton Environmental Consultants, Inc.)
Ford Motor Company
The American Road
Dearborn, Michigan 48121
Contract No 68-02-0630
Program Element No. 1AB604
EPA Project Officer Norman Plaks
Industrial Environmental Research Laboratory
Office of Energy, Minerals, and Industry
Research Triangle Park, N C. 27711
Prepared for
U.S. ENVIRONMENTAL PROTECTION AGENCY
Office of Research and Development
Washington, D.C. 20460
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VOLUME II APPENDICES
A. Summary of Maintenance and Operations Department
Logbooks Pertaining to the Ford/Koppers Control
System
B. Summary of EPA Methods
C. Source Sampling Field Data Sheets
D. Calibrations
E. Sample Calculations
F. Project Participants
G. Daily Log of Fume Hood Performance
H. Daily Log of Scrubber System Performance
I. Summaries of Process and Control System Data
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APPENDIX A
SUMMARY OF MAINTENANCE AND
OPERATIONS DEPARTMENT LOGBOOKS
PERTAINING TO THE
FORD/KOPPERS CONTROL SYSTEM
This appendix contains a list of nearly-verbatum extractions
from the logbooks. To the extent possible, the original log entry
is presented unless the original writer's sentence was clearly
misleading or unintelligible; in such cases an interpretation was
made based upon experience with the control system and the stand-
ard terminology presented in the design manual or the Glossary of
Terms in this report. In many cases, the entries are insuffi-
ciently detailed to provide an estimate of downtime. However,
the list is useful in that it provides an overview of typical
system failures or inadequacies.
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A-l
MAINTENANCE DEPARTMENT LOGBOOK ENTRIES
FOR SMOKELESS COKE PUSHING SYSTEM
7-1-72 The A-door machine went down at approximately 3:45 PM.
Operations started using machine at 8PM and took It out
of service again at 9:05.
Large blower motor bearing hot and had to be shut down.
Motor and machines still out of service at 10:45 PM.
7-2-72 A-door machine was down at start of Number 3 shift.
Trouble was found In disconnect switch for Femco signal
to butterfly. Was repaired and given to operations at
6:20.
7-7-72 A-door machine will be In service. But they do not
want south hood (fume collection hood) In operation.
7-8-72 A-door machine down at beginning of shift ... would not
travel. Found trouble in top Rayco cylinder. FM-7
connection burned off at terminal inside motor housing.
7-16-72 A-door machine out of service. Removed top louvre in
smoke emission stack, it was warped from heat and was
catching damper.
7-18-72 A-door machine out of service entire shift. Main fan
damper limits (were) reset and chain installed. We
tried to operate machine once and damper opened only
two-thirds of the way but when we tried to close it
the motor would not move...there is quite a bit of
bind in the damper.
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A-2
7-22-72 A-battery pollution fan kicked off twice at 3:45 PM and
6:10 PM. Reason unknown. All lights on panel indicated
it should have run. Had to wait from 6:10 to 9:25 until
power people reset the breaker. There was a time relay
lock-out which we had to wait for.
7-24-72 A-battery scrubber fan ... low water pressure alarm
went off a couple of times and could not find anything
wrong except there is a leak at the pressure switch.
7-30-72 A-battery pollution scrubber ... water to scrubber
dropped about 25 6PM at 5:45 and alarm went off, we
switched from the south pump to the north pump and lost
another 25 to 50 GPM. Tightened packing gland on south
pump, switched back over to south pump and GPM came
back up to 750 while the north pump was on the gauge
and the north pump showed 0. There is about three
inches of sludge on the ground between pumps indi-
cating a possible blockage.
9-4-72 A-battery scrubber... fan motor bearings low on oil.
Scrubber spray pumps oiler cups empty of oil. South
pump seal leaking badly.
10-23-72 A-door machine that opens doors on suction main was
stuck at No. 28 oven. Could not travel north or south.
Pin on south side of hood does not line up. Machine
was out of service for repair from 10 PM to 12 midnight.
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A-3
10-23-72 Fume seal that fits against main at south channel was
(Continued)
bent in and pin head inside was catching. Would not
allow seal to retract. Burned one side of pin head
off that was lapped over inner seal to get clearance
to move machine to south end and straighten the steel
work. Downtime 10 FM to 5 AM total.
10-25-72 A-door machine was used to push an oven north of fume
main. Fume seal did not retract and machine was
unable to travel. Hood struck end of main when operator
moved south to put door back on. Pulled coke guide off
track and did extensive damage to the hood. South
upright channel will have to be replaced. The rest
can probably be straightened on the job. Got machine
moved to south end at 5:30 so production could start
on A-battery. Total downtime 3:00 to 5:30.
11-2-72 Fan at south end of A-battery stopped with power failure,
We were notified at 1:50 and had it running at 2:10 AM.
11-17-72 A-door machine ...the Rayco cylinder that controls the
butterfly works intermittently. It started acting up
at 2:00 and we have been working it on manual. A fan
scrubber pump (north) makes noise..switched to south
pump. No downtime. A-battery smoke suction fan ...
installed Rayco cylinder and hooked up. Started up
fan at 7:00. Still is not working and have not had
time to check out. Electrical please follow up.
A-battery suction butterly Rayco cylinder is completed
and there is a lock on it.
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A-4
11-19-72 A-battery fume emission butterfly Rayco cylinder...
installed a jumper on wire FB-4 to FB-5 in control
station in A-stack draft room. This jumps out the
butterfly Rayco cylinder internal forward stop limit
thermal protection and hand wheel crank limit.
The Rayco travel is still protected by external stop
limits. The reason for this was when you use the
manual push-button, the external limits are not in
the circuit and you could overtravel and jam the Rayco.
11-26-72 A-battery fume fan...motor reducer unit that operates
louvres ahead of fan, motor winding is burned open due
to oil leakage on reducer. Please follow-up on removing.
A-battery recirculating water to pollution fan. One
water recirculating pump is running even though fan is
off. There is no heat around pumps. So we want to
avoid a freeze-up. The other pump has inlet and out-
let valves closed and drain valve open. In any case,
for the pump that is down leave the drain valve at
the bottom of pump open as other valves are not holding.
There is some leakage.
11-29-72 A-battery fume fan main board reset and we started up
at 1:1-5 AM ... was getting low scrubber water preseure
alarm. Switched over to No. 2 pump. The pollution
fan louvre motor brake coil burned up. The brake
guts have been removed. The motor is still in operation
and there doesn't seem to be any excessive drifting.
Check operation during your shift by observing the
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A-5
11-29-72 movement of the mechanical mechanism at the external
(Continued)
limit switch area. If any trouble develops or louvres
bind in extreme open or closed position shut the main
fan down.
11-30-72 A-battery scrubber water pumps were getting alarm at
low water pressure to scrubber. Found both pumps running,
South one had the valves closed yet. Opened valves and
let both pumps operate. 45 psi at pumps and 35 psi at
spray headers. We replaced the gauge at the north pump
and spray header.
12-1-72 Scrubber pump still getting low water flow alarm with
one pump running 40 psi.
12-2-72 A-battery emission A-door machine left out all shift
and did not shut off fan. Purpose to avert start-up
problems in cold weather* Alternated operation of
scrubber pumps.
12-5-72 A-battery scrubber-recorder in office shows no flow,
pump shows pressure and sprays are working. Will
need instrument repairman. A-battery fume control
in operation all shift...we have some questions about
louvre motor searching at closed area. Need possible
cause of motor trouble.
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A-6
12-10-72 A-battery scrubber both pumps were running, surge
tank was empty. Checked and found 4-Inch gate valve
In quench station shut-off and 4-inch drain on south
eide of tank open. Closed drain and opened supply
and put sprays in service but recorder in anunciator
panel does not work.
12-12-72 A-battery fume controls, damper was not operating
because butterfly Rayco limit was shorted. Jumpered
out internal back limit (FB-5a and FB-4), operating
OK now except Rayco blew a fuse once.
12-17-72 A-butterfly Rayco Code 31-25-363 not in yet. Left fan
running but system is not in operation.
12-21-72 A-battery pollution fan shut down at 9:45 AM, louvre
motor burned out. Repaired motor is expected back
on 12-22-72.
12-24-72 A-battery fume control, installed louvre motor and ran
same. It pulls 1/2 amp in both directions on all three
legs. Number 3 shift to check over—all operation between
door machine and fan.
12-26-72 Checked out butterfly for pollution fan and it is
working correctly.
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A-7
12-28-72 A-battery pollution fan louvre motor disconnect switch
is pulled and is to be left off until Femco signal
is repaired. Number 3 shift to requisition spare
parts and we will follow-up in the morning.
12-29-72 A-battery pollution fan shut down at 3 PM due to bad
regulating instruments for louvre motor.
1-2-73 A-battery pollution fan back in service at 1 PM.
2-11-73 A-pollution fan... tried working between calls but
still no suction. Butterfly not working. Got call at
end of shift that it seems to be working.
2-17-73 A-battery pollution fan went down at 10 AM (high)
motor bearing temperature. Called power-house to have
control relay reset. Left motor down until damper
motor chain is repaired. A-battery fan repaired chain
drive on louvres; located No. RC 60 chain. But louvres
seem to be frozen bound up inside of duct. Made up
some salamanders to get some heat in the area. This
will help on fan start-up.
2-18-73 A-battery fan...removed inspection plate and busted
ice away from bottom louvre to free-up. There is about
two inches of ice on the bottom. One and a half-inch
drain west of louvres is frozen, the valve was closed.
Ice must have frozen back again because louvres will
not make bottom limit.
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A-8
2-19-73 A-battery fan...replaced broken section of drain line
and drained. Louvres are freed and making both limits.
But could not get damper-closed light in the control
room. Had to stop working on it at 12:50 AH for break-
downs.
3-11-73 Big fan at south end of A-battery kicked off at 1:10 PM
Circulating water pump blew a fuse shutting down big
fan motor. Called power-house to reset fan motor.
They said the three-hour timer had started and that
t« i -.
it would be 4 PM before it could be reset.
3-19-73 A-battery fume fan shut down. Replaced fuses and put
fan back on. Follow-up: check controls and see why
both pumps stay on. Note both packings are leaking
badly. May be why both pumps had to run to get pressure
4-3-73 A-door machine fume pick-up (hood) was hung up on door
that would not close because of bent lever. Pulled
lever over with chain fall to straighten. Also
straightened two more levers that were bent same area.
4-7-73 A-fume hood hung up on door that would not close
because of bent lever. Straightened lever and returned
to operation. Note: there are about five levers toward
north end that are bent.
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A-9
4-8-73 A-fume hood... straightened door levers but machine
bent them again. Started to remove some shim on the
east side because east track had been raised. Also
fume main track is sagging near No.. 25 oven.
4-19-73 Started A-fan at 7:20 PM.
4-20-73 A-battery pollution fan went down at 11:40 AM. Inboard
motor bearing temperature high. Drained oil and
flushed and added 3-1/2 quarts to about 3/4 level on
sight gauge. Started up at 2:55.
4-21-73 A-fan motor shut down at 3:45 PM. Inboard motor bearing
temperature 175°. Drained oil and refilled. Started
up again at 8 PM and put fume system in operation.
Bearing temperature went up to 170° and holding.
Ambient air is cooler, will probably kick off in the
morning when the sun comes out. Informed main board
of conditions. Note: it did not make it, 1:20 PM
fan shut down. By the time I got over to the room
from the office the readout showed 150°F was the
reading and 170°F while running.
4-22-73 Leave pollution fan down until tomorrow. Drained oil
and checked oil rings.
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A-10
4-24-73 Main pollution fan on at 2 PM. Main bearing tempera-
tures at 3:15 (were) 120 to 150°. Keep check on your
shifts.
A-battery fan...the oil dripped at outboard end of
motor, I think Is coming from Inboard bearings, too
much oil. Temperature holding at 145° to 150°.
A-door machine hood Rayco has a burned out coll and
wire on field loss relay. Running with jumper.
4-25-73 Inboard A-pollution fan motor bearing temperature
holding at 125° to 150°.
A-door machine...changed field loss relay for hood
Rayco cylinder and repaired wiring around It that had
burned also replaced resistor. Rayco motor Is shorted
and will have to be changed. It Is disconnected.
4-26-73 A-door machine Rayco hooked up electrical and checked
out. Put In service at 4:50 PM.
4-29-73 A-door machine hung up on the last two fume door handles
at 6:50 AM. Freed up and took to the south end.
5-3-73 A-battery,..straightened arms on fume main (doors)
46,47,48,49.
5-9-73 A-door machine...relocated fume hood limit to the upper
channel. As soon as the Rayco moves the slide 1-1/2
Inches, the machine cannot move.
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A-ll
5-26-73 A-door machine coke guide became hung up on fume main
door handle. It seems that fume main door actuator
over-traveled on open and handles became tangled in
the opening mechanism. We had to burn them off to
get the fume main door actuator into the retracted
position. They need to be welded back on.
5-29-73 Pollution fan south end battery went down.
6-1-73 Changed burned coil on FLR relay. A-door machine fume
main damper: after completion found open shunt field
circuit to Rayco motor. Did not isolate problem to
motor as operations wanted to use machine. We have
one out for repair now.
6-2-73 In checking A-door machine, the Rayco shunt circuit is
opened.
6-4-73 5:10 AM, A-battery pollution fan went down.
5:20 AM, A-fan kicked off. Called main board. As of
10:40 had not reset. A-door machine fume hood hit
bumper at north end, sheared the coupling bolts and
ripped out cables and receptacles; fortunately not the
two multi-cables.
6-5-73 A-pollution fan put in service at 12:30.
A-battery fan started up at 7:30 FM.
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A-12
6-6-73 A-battery fan...power maintenance requested shut down
on motor for service; changed oil; started up at 7:30.
Shut down at 8:23 with hot inboard bearing. We'll
have to wait three hours to restart; power maintenance
check oil looks like low level.
6-7-73 A-battery fan started at 1:20 AM; took temperature
reading at 2:55,temperatures 135° to 165°.
6-8-73 12:45 PM started A-battery pollution fan. 2 PM A-battery
pollution control fan stopped.
6-19-73 Finally got fan started at 11:10 PM.
6-21-73 Fume fan down from 10 AM to the end of the shift
installing temperature recorder. No. 3 shift to
receive coupling guard, install sun shield, and put
fan back in operation. A-battery fan motor in service
at 8:15 PM.
6-26-73 Air pollution fan damper: we checked and found ampere
recorder in heater room at A-and B-bunker to be non-
functioning. Have instrument repairman fix it.
I checked with power maintenance on A-fan motor and was
told by No. 4 sub-attendant that motor is out for bearing
check.
6-30-73 A-battery pollution fan started at 3:45 PM.
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A-13
7-5-73 Fay attention to A-battery pollution fan current draw.
When it exceeds 250 amps either find the trouble or
get it shut down. This motor current is to be controlled
at 240 or less. When damper louvres are left open and
fume main door closed water is pulled into fan and
could damage the fan badly.
7-8-73 A-battery fan went down at 3:05 PM, inboard motor
bearing temperature 180°. A-battery fan started up
at 9:00.
7-14-73 A-battery fan shut down at 12:15 PM approximately;
high inboard motor bearing temperature. Started back
up at 1:30 PM. Vibration was noted as fan current
began to subside when current came all the way down
to normal, fan running good.
8/2/73 A-door machine fume main hood jamming mechanically and
not going in all the way. It probably happened when
machine derailed.
8-27-73 A-battery stack motor kicked out at 3:40 with hot
inboard bearing. Put on line again at 6:45.
8-31-73 Air pollution fan back in service at 6:30 PM at which
time inboard bearing was a little low on oil. Shut
fan off to allow power maintenance to put oil in and
fan will not start (3-hour time tripped) fan back in
service at 8:50. All systems go.
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A-14
11-1-73 We checked A-door machine fume hood and found Rayco
cylinder will have to be changed. Grounded field.
A forward relay may have to be changed also.
11-2-73 A<-door machine fume hood cylinder back in service at
1:30 PM. Changed zelay and cleared ground in Rayco
cylinder.
11-3-73 A-door machine...changed Rayco.
11-4-73 A-door machine fume hood seal ring is not going all the
way to main. Relays drop off before it gets there.
Please check.
We repaired fume hood on door machine. No downtime.
11-26-73 4:00 PM...A-battery pollution fan butterfly wouldn't
operate. We checked door machine and controls at south
end of A and on fume main butterfly valve motor.
Worked contact and it started working. OK at 4:00.
Stopped working again at 5:30. Didn't locate problem.
Locked butterfly partially open and put back in service,
12-2-73 Kinpactor tank was overflowing. The valve far south
that is supposed to be open five turns was closed.
Opened valve but this was late in the shift. Should
have helped, please check.
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A-15
12-14-73 Replaced fuse on No. 1 Klnpactor pump.
12-22-73 A-battery pollution fan main dampers were not giving
suction. Check system. Transmitters and receivers
were OK. Believe problem to be in the instrument
panel at A-and B-heater room. We would get a 200-amp
reading only occasionally when relay in instrument
panel had been chattering. We would get a full 240-
amp reading when we operated the dampers manually.
A-battery pollution fan was accidentally tripped off
as electricians were locating control switches in
A-stack draft room for heating cables in that area.
The pressure switch for main fan, water-cooled
bearings ia frozen upright at the pressure switch.
Put fan back on line at 11:30 AM. Thawed pressure
switch line.
12-23-73 We replaced one-inch water line to Kinpactor pump
bearing.
1-8-74 A-battery pollution fan control from bunker Instrument
is out of adjustment.
1-16-74 Air pollution fan maintenance off for one and one-half
shifts.
1-17-74 Air pollution fan off for repair.
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A-16
1-25-74 A-door machine fume hood requires mechanical work on
couplings.
3-22-74 We repaired the Kinpactor and put north pump and fan in
service at 6:30. Had call at 10:00 PM that system was
not working. Checked out and found cause for kicking
off was high temperature on inboard bearing. Notified
dispatchers and called power to have it checked.
A-battery pollution fan in service at 1:15 AM, gas
dispatcher notified. Motor inboard bearing is leaking
oil around shaft. A-door machine and coke guide...
fume hood would not work on automatic from fan when
the fan was put back on at 1:15 AM. Back on automatic
at 6:15.
3-27-74 A-coke guide (fume hood) straightened outside member
by use of heat and cutting brace member to relieve
strain, welded braces back in.
3-31-74 A-coke guide: the same 6-inch channel is bent again.
Doesn't interfere with operating the fume hood although
there is as much as four inches to six inches difference
in alignment between the No. 1 oven and the No. 49 oven.
4-18-74 A-battery pollution fan down at 1:30 FM due to repairs
being made to a broken city water line.
A-battery fan back on at 7:45 FM.
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A-17
5-14-74 A-battery fan kicked off at 7PM, showed vibration.
Called power and was told to try at 10:00 PH. We
tried at this time, it would not reset and showed
high temperature on inboard bearing.
5-15-74 Started air pollution fan, took temperature readings
at 2:15, 3:30, and 5:00-- all were same.
5-18-74 A-battery air pollution fan damper...replaced brake
coil and welded up cracks in metal brake disc. Back
in service at 2 PM. Still need instrument repair to
adjust current regulating instrument.
5-22-74 A-battery pollution fan...found everthing operating
normally. A-battery pollution fan kicked off at 3:40,
high inboard bearing temperature and fan motor back
in service at 7:25.
5-31-74 A-battery pollution fan motor kicked off at 3:23 due
to high inboard bearing temperature. Back in service
at 8:00 PH. This motor has kicked off at least five
times in the past two weeks for the same reason.
Checked into power. Found that they had installed a
new Babbitt bearing on 6-27-73. Bearing temperature
has been kicking fan off at closer intervals. Sounds
like it is starting to wipe out.
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A-18
6-2-74 Air pollution fan kicked off at 2:55 and went back on
line at 6:45 PM. High temperature on inboard bearing,
oil OK.
6-3-74 Air pollution fan kicked off at 1:20 PM. Do not reset
unless myself or someone else from power-house OK's it.
Brewer tried air pollution fan at 5:00 PM would not go
on line, power reset on line at 5:20 PM, running normal
6- .4-74 Power house pulled inboard bearing found bottom half
wiped slightly, changed bearing.
6-5-74 Power-house checked alignment, found motor was 0.012
high, 0.001 out on coupling faces. Decided to change
fan bearings.
6-6-74 Started changing bearings, outboard bearing wiped.
Noticed strange lines in journal areas of shaft
resembling cracks or where shaft had been welded and
machined.
6-7-74 (Above) stated lines in shaft were obviously shrink
lines from shaft being welded. Would cause no problem.
6-8-74 Air pollution fan, completed change at south bearing.
6-9-74 Completed north bearing change.
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A-19
6-10-74 Air pollution (fan) on line at 9:15 AM, recording
bearing temperatures.
6-14-74 Air pollution fan kicked out at 6:38 and was reset back
on line at 10:10 PM. High temperature and vibration
on inboard bearing.
6-17-74 Air pollution fan kicked off at 3:10 on high inboard
bearing temperature. As of 6:50 , power could not be
reset, maintenance to check bearing alignment.
Power-house working on A-battery pollution fan. Is
left down until No. 2 shift 6-18.
6-18-74 Checking bearing temperatures on fan.
6-19-74 Fan kicked off at 7:40 due to high temperature inboard
motor bearing.
6-20-74 A-battery pollution fan...we switched over from city
water to mill water due to low pressure for bearings.
We repaired some loose solder joints on master module.
We reset all modules to kick out at 170° bearing tempera-
tures .
Fan be-aring temperatures monitored. Notify dispatcher
of a kick-off and was reset.
6-22-74 Pollution fan: completed polishing shaft. Installed
bearing housings. Took indicator readings vertical
and horizontal of periphery. Will align shafts.
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A-20
6-24-74 We shimmed bearing pedestals. Found that the spacer
support between the bearing housing and foundation
support was secured only by bearing hold down bolt
which was very poor since bearing was dolled to it.
Fan is completed,filled with oil.
New carbon seals both sides of air pollution fan.
Took apart and cleaned water seals. All set for
morning start-up.
7-1-74 A-battery pollution fan kicked off at 6:15 PM. Hot
inboard motor bearing temperature. Back on line
9:25. Went down again.
7-2-74 Fan kicked off at 3:15 with hot Inboard motor bearing
temperature; on line at 5:30 AM.
We made up and installed two-inch dsain line on bearing
of pollution fan. Dampers working but indicator light
does not show it. Temperature on inboard bearing of
motor has been holding at 170°.
7-4-74 We put pollution fan on line at 8:10.
7-6-74 Pollution fan still running.
7-7-74 Pollution fan back in service 6:50 PM, it kicked out
at 1:50 PM.
7-10-74 We shut down fan at 10:30 PM.
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A-21
7-11-74 I signed out 26-205 feeder fan, air pollution fan, at
4:05 PM, took inboard coupling apart, removed doors
and covers, fixed fan on back of motor, and signed
service back in at 7:15. Motor would not start
because timer being tripped. Started at 7:56 and
ran until 8:45 and signed out again. Left covers
off fan and motor. Inboard bearing appears to be
wiped out and fan has some buildup of debris.
7-12-74 Fan completed and coupling together; ready to try out
7-13-74 We started up fan; made test, and closed doors.
7-14-74 Ran and checked pollution fan motor until 7 :'00 PM and
shut down. Temperatures ranged from 135° to 175°.
Note: water to Kinpactor shut off at south point
station. Both pumps are shut off.
7-15-74 Removed north Kinpactor pump motor to floor and south
motor installed on north pump. In service at 9:45.
7-16-74 A-battery pollution fan ran all shift.
7-17-74 Pulled coupling off old Kinpactor pump and installed
on good motor. Hooked up suction and discharge lines,
7-18-74 Made three checks on temperature and pollution motor
and fan.
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A-22
7-21-74 A-door machine...drive wheel for hood is broken.
Wheel runs on upper rail.
7-22-74 Put A-battery pollution fan motor back in service at
6:10 PM. A-door machine out of service from 8:00 AM
to 10:10 AM to change fume hood travel drive wheel.
8-29-74 Fume damper handle at oven 32, A-battery needs
straightening.
8-31-74 A-battery fume main door arms (on oven) numbers 39,
41, 43, 48, and 49 need to be straightened.
9-1-74 We straightened the fume main door arm at 39.
9-30-74 A-battery pollution fan is down for repair for two
days.
10-18-74 Angle clips were installed...on A-battery fume main.
South beam was slightly twisted at top so we had to
drive wedges...gave machine to operations at 4:45 PM.
A-battery emissions control fan in service at 5:00 PM.
All covers were installed on Kinpactor.
11-5-74 A-door machine fume hood is not operating all the time.
We found that the hood carriage doesn't move far enough
to trip LSDO located on the south side of the Rayco
platform. The door is opened and the hood opening is
-------
A-23
11-5-75 against the main but the bracket to trip the limit
(Continued)
switch is 2-1/2 to three inches away from limit
switch arm. It does make contact on the northern-
most ovens.
11-7-74 A-battery fume hood started acting up so we elongated
the holes for the dog for LSDO and moved it forward
on the carriage. The fume (hood) works well on all
of A-battery but on AX (that is, ovens 53 through 64)
the hood doesn't seal around the door enough. Leaves
about a 3/4-inch gap.
A-coke guide derailed at 4:50. Had back on track
and in service at 5:15. Also repaired No. 8 fume
door from south and adjusted Rayco limit on A-hood.
11-22-74 Wayne County to take noise level readings tonight
between 9:00 and 11:00 PM. After their first reading^
they will contact operations to shut down main pollu-
tion fan...we tried to start fume fan at 11:00 and it
didn't start at 3:30.
11-28-74 Moved Goulds pump from SS (Building) to A-battery
Kinpactor.
1-1-29-74 Completed south Kinpactor pump installation.
12-11-74 Pollution fan was back on at 3:20 PM.
-------
A-24
12-12-74 A-door machine indicating light does not work because
wire No. FT25 is open between limit and panel...we
repaired all indicator lights in the control room at
south end of A-battery.
12-28-74 Shut off air pollution main fan at 11:15. Noise level
too high. Plant personnel called operations; shut off
until after the holidays.
1-7-75 Air pollution fan back in service at 2:00 PM.
1-9-75 A-door machine: hooked up Rayco cylinder but could
not operate...also found limit switch which drops CR2
out was not opening due to the stationary contacts
being badly bent...operating at 9:00 PM.
A-battery pollution fan was shut down at 10:15 PM per
EPA due to noise.
1-10-75 Turned A-battery fan back on.
1-14-75 The north Kinpactor pump was shut down at 5:45 due
to noise. A-door machine fume hood binding mechanically,
1-16-75 A-door machine out of service at 8:00 PM to change
Rayco cylinder on fume hood.
1-27-75 Fan damper motor is out of service; damper is set so
that motor pulls 180-200 amps. Took damper apart...was
not able to free up.
-------
A-25
2-5-75 A-door machine and coke guide out of service at 7:30 AM
to end of No. 2 shift; follow-up for No. 3 shift to
patch door machine hood.
2-16-75 Kinpactor unit at A-battery over flow drain was only
partially open...please follow-up, line may be plugged.
3-7-75 Mounted pollution fan damper motor, did not get it
hooked up electrically.
A-door machine was not opening fume hood doors. We
took it to the south end and checked it out (7:30 «
8:30)...after thorough lube job, no more trouble.
3-8-75 A-battery pollution fan and door machine worked at
1:30 PM.
3-20-75 A-door machine fume hood is down; there is a mechanical
bind that doesn't allow it to go out all the way. It
is missing the door by 6 to 8 inches. Rayco was pulling
30 amps so we turned it off rather than damage it.
4-2-75 There will be a power shutdown this evening...this
feeds A-battery pollution fan and pumps. Shut this
equipment down at 3:30.
4-3-75 Pollution fan in service.
-------
A-26
4-20-75 A-scrubber: could not get water to stop coming out
of the hole at the bottom. Had water and pumps off
fiom 10:00 to 2:30.
5-2-75 We picked up the wheel assembly for A-door machine
fume hood and put it on the south end. A-door machine
would not retract; cleaned up carriage limit.
5-8-75 A-door machine: rang out wires for fume hood Rayco;
hooked up.
5-9-75 Changed Rayco field loss relay at 6:00. Hood would
not return due to time TR10A not working.
5-10-75 A-coke guide fume hood is not sealing. Please check
and repair.
5-13-75 A-fume hood would not operate; found contact stuck
closed on LSDRO not allowing CR2 to come in.
5-21-75 Kinpactor piping: we made up gaskets and tried to
pack pipe joints but could not get up to proper height;
will need a sky hook or a cherry picker.
5-30-75 2:30 to 4:00 A-fume hood would not return; the dampers
were open and power shut off to draw 150 amps on main
fan...replaced a broken wire.
-------
A-27
6-13-75 A-fame hood has an open (wire) between panel and Rayco
cylinder. Took out of service from 4:45 to 5:00 to
check out.
6-14-75 A-door machine...we still have an open in the shunt
field.
A-door machine fume hood, found broken wire in a box
at the Rayco. Everthing comes in but armature is
shorted. Returned to service at 5:15 without hood
working. Hood worked out some way and knocked off
three doors on main.
A-battery pollution fan was shut down at 7:40 FM.
6-15-75 Fume collector... installed five doors that had
been knocked (off) due to operator's using machine
when we had pin out of Rayco unit for fume hood causing
hood to move. A-door machine Rayco unit changed. Had
problems locating trouble in Rayco...would go out but
would not return...after extending one foot we could
not extend or return. We welded clip so that it
cannot move.
6-20-75 A-battery fan kicked off at 12:30 PM. High temperature
at inboard fan bearing. Control timer times out at
3:30 PM.
A-door machine: millwrights located bind in roller
at northeast side of fume hood, there is no grease
fitting and it cannot be lubricated properly. Fume
hood is going in and out manually. We did not check
to see if fan damper is open or not. Follow-up.
-------
A-28
6-21-75 A-door machine out of service to trim hoods on north
and south sides. Frame broke, rewelded.
6-22-75 A-door machine: repaired ground in fume hood control
and put in service at 7:15...fume hood will go out
only a few inches and then will not return. Machine
down entire shift as far as hood is concerned...worked
on fume hood from 11:30 to 1:00 PM, could find nothing.
6-23-75 A-fume hood: Rayco and Femco circuit is OK now.
We have some side pull on Rayco to hood hookup causing
internal bind in cylinder.
6-24-75 Checked at beginning of shift and hood would not
operate without tripping overload at approximately 20
amps. Replaced control reed contacts and greased hood
slide bars. Returned to service at 2:30 PM. Fume
hood stopped working during rain. Overloads not
holding. Started troubleshooting after rain...and
found open circuit to limits in Rayco.
6-25-75 A-door machine fume hood: returned to service at
4:30 AM installed jumper wire.
6-26-75 A-door machine fume hood: during entire shift according
to amp meter...hood has not been going out for every
oven since 12:30 PM. Checked out and found it was
working properly. Seems to be an alignment problem.
-------
A-29
6-27-75 Took A-door machine out of service and greased the
sides,,,kept kicking out...two wheels not turning on
hood carriage. Either door hinges are rusty or doors
are binding inside of the hood when they are open...at
end of battery it worked fine but up against the door,
it stops from going in 6-8 inches, kicking overload.
6-29-75 A-door machine fume hood is binding up. Rollers
won't turn and have no grease fittings to lubricate
them. When doors open, they bind on the corrugated
liner inside the hood.
6-30-75 A-door machine: at lunchtime checked out fume,hood,
oiled Rayco shaft. Started working.
7-11-75 A-fan on at 11:40 off 3:00j on 4:20, off 6:25. Each
time, panel indicated motor inboard bearing. However
temperature was only 125°F, when A-fan was running
fume hood was not going in all the way. There is a
mechnical bind because it is operating properly
without opening doors.
-------
A-30
OPERATIONS DEPARTMENT
LOGBOOK ENTRIES FOR SMOKELESS COKE PUSHING SYSTEM
3-9-75 Replaced Femco converter on A-door machine, suction
fan is now working properly.
3-20-75 Fume fan damper not operating. Maintenance stated
that the door machine hood does not open all the way
to make the limit.
No. 2 has to check out...found a side wear plate on
inside fume hood bent over not allowing fume main
doors to open.
A-door machine out of service 8:00-8:15 removed bent
plate from fume hood.
3-26-75 Shut off power to pollution fan so electrical tie-in
could be made at gate.
4-18-75 Pollution system back in service 2:40 PM.
4-20-75 Pollution system out of service at 10:00 AM. Mainte-
nance patched holes in Kinpactor. Back at 2:50 PM.
4-26-75 A-door machine out of service 9:50 to 10:20, Rayco
wouldn't come out due to blown fuse.
5-1-75 A-door machine out of service from beginning of shift
until end. Not to use unless absolutely necessary.
Wheel on trolley machine for pollution device in very
bad shape.
-------
A-31
5-3-75 The control limit on A-door machine collector fume
slides. The hood would not come back once in position.
5-8-75 Maintenance changed Rayco on A-door machine. Failed
to return on No. 59AX oven. Out of service at lunch,
to be completed on No. 3 shift.
A-door machine out of service to 7:15 working on Rayco
wiring.
5-9-75 Adjusted limit on A-door machine coke guide for Rayco.
5-13-75 Maintenance repaired limit on A-door machine Rayco for
smokeless pushing.
5-14-75 A-door machine out at 12:00 PM until 2:40 PM replacing
Rayco cylinder.
5-15-75 Notified maintenance that the smokeless pushing system
is not retracting after the push on automatic; told
them about it at 6:00.
5-16-75 Started bypassing the Smokeless Pushing System on A-
door machine because the smoke boot wouldn't retract..
north side pumps need to be replaced. Maintenance noti-
field at 6:30.
A-door machine out from 7:30 to 9:00 maintenance
repaired the smoke boot but it will only work on manual.
-------
A-32
5-17-75 Had to remove A-door machine hood twice with manual
button.
5-19-75 Did not use Rayco unit on A-door machine. Kinpactor out
of service. Expected to be out all week.
5-30-75 Kinpactor pump kicked off twice. Changed over to south
pump.
6-13-75 Maintenance worked on Smokeless Pushing System; out of
service from 12:00 to 8:00. The Rayco wasn't working
on auto or manual, maintenance found an open wire to
Rayco.
A-door machine out of service 8:00 to 11:30 there is a
temporary hook-up.
6-14-75 A-door machine out 8:00 to 2:40 Ryaco still out of
service.
A-door machine back in service at 5:30 minus the Rayco
unit - armature burned up and will have to be replaced.
Started moving machine north to A-44 oven and hood
made contact with three fume collector doors knocking
them to the ground. Upon investigation, hood (was)
found extended two inches farther west than normally.
Pulled the hood back by hand and continued using the
machine. Southwest channel on hood torn slightly-
no other apparent damage. Shut down pollution fan at
7:40 PM.
-------
A-33
6-15-75 Removed Rayco cylinder from A-door machine and replaced
five doors on fume collector...in service at 2:20.
6-21-75 A-door machine out 12:00 until end of shift due to
Rayco not working.
6-22-75 A-door machine, Smokeless Pushing System Rayco out of
order from 12:00. A-door machine out from 11:30 till
1:15 vorking on Rayco.
6-23-75 A-door machine out of service from 10:15 to 2:30.
Maintenance vorking on fume collector Rayco.
6-24-75 A-door machine out of service from 12:00 to 2:45.
Electricians working on Rayco. Back at 8:45 AM
Maintenance worked on Rayco. A-door machine Rayco
cylinder quit working at 5:45 PM, notified proper
authorities of its not working.
6-25-75 A-door machine out of service 12:00 to 4:30, mainte-
nance working on Rayco wiring. A-door machine out of
service 8:30 to 9:00. Maintenance greased rollers on
Rayco, from fume hood.
A-door machine out of service 12:00 to 12:30, electri-
cians repaired short in limit switch on coke side that
controls Rayco.
-------
A-34
6-26-75 Greased the rollers on the Rayco unit. A-door machine
out of service 9:40 to 10:15 maintenance making adjust-
ments to overload limit for Rayco fume hood.
6-27-75 A-door machine out of service from 8:00 to 8:30
maintenance working on fume collector, Rayco, and hood.
A-door machine out of service 12:40 to 1:45, working on
Rayco again.
7-1-75 A-door machine out of service 11:30 to 2:00, working on
Rayco rylinder.
7-3-75 Fume collector down at 4:37 FM due to substation 46A
going out. Back on at 9:00 PM.
7-7-75 A-door machine out of service 11:45 to 1:00, maintenance
replaced flume hood extension.
7-8-75 A-door machine out from beginning of shift through 9:15;
maintenance worked on flume collector hood slide.
7-11-75 Fan motor tripped out 2:45 AM; back on for first oven
after lunch at 4:10 AM but it's not working very well.
The extension is going against the main also it is
tripping the Rayco reset...fan motor tripped out again
at 6:15.
-------
A-35
7-20-75 Fume hood out of service 11:35 to 2:45, needed greasing,
Overload kept kicking out.
7-23-75 A-door machine out of service 8:00 to 8:30;greased
Rayco shaft.
-------
APPENDIX B
SUMMARY OF EPA METHODS
-------
B-l
111:0400
FEDERAL REGULATIONS
by UM
•• RKII.KINCK MI-TIIODS
|S»IK 20790. June 14. l»74|
MLTHOO I— UUPM AND VHjOCIT* 1BMCUM
I. frtnnplt tint
1.1 Principle. A HnpHr-: ill* Mid tM
number erf tnrcm pmiiu n . x>.46>.tHl to Mil
In III* wmeilmt of • repn juiuilv* Mmple.
14 AppllcabUlir nil mtthod •hoold
to appIM only «h<«
pracvdran ft* tfctennlninti compumce wi
Uw Now Boum IMfanrnncn Wnmtanfi. Un-
ICM ellMiwlM cpwIOrd. thta ntlhnd Ir ii'.l
InwndM l« »p|il)f u> ra« rtmum Mhur Hum
UMM anltud diracUy la UM rtmuip>cr»
•lilmul further piaMalni.
9. MoMriiin.
•.I BciceilenefaumpllngiluamlmlDU
mum number
-------
B-2
STATIONARY SOURCES
it-io.1
121:0407
•.1J
enurta can b* net. toe
of travtn* polnu I* twain (12).
S.IJ Borne sampling situations render the
abov* lampllng siu criteria Impractical.
Whan this Is th* caw. ehooao a eoBvtnltnt
sampling location and use Plgur* 1-1 to de-
termine the minimum number of tra»*is»
point*. Trader no condition* should • earn-
plug point be nlected within 1 Inch at tb*
stack wall. Tb obtain th* number of travm*
polnu tor «Uck* or ducU with a diameter
lem than • fort, multiply the number of
point* ebtalMd tram Flpuo t-1 by 0«T.
j.j.4 TO UK pigure 1-1 nrst moamir* HM
dUUncr tram tb* chosen tampllng location
ta ta* uvijes* upstream and downstream dis-
turbance]. DoterniliM the comtpondlag
nnmbtr of travtn* polnu for eich dlitanco
from Flgu.-» l-l. Select tho blfhtr of tb*
two numben of tiaven* potato, or a greater
value, tueb tbat tor clreular ttaeka Iho nnm-
btr to a multiple of 4. and for rectangular
•tack* tfco numbir foUowi tht ertUrta of
U C?n»i *>aUonalUyeut and location of
traven* polnu.
1X1 Par circular etaeks loeaU th* tr*.
van* polnu on at lout two dlamiUn ae-
oordlnf to Plfun 1-3 and Tab!* 1-1. Th*
traven* an* mall diiid* the itaek em*
notion into equal part*.
T.|
(*»rcr-t of ttK< «lr»ttr frn If-.Ki mil l» Ir4iint [-'".I
Figure 1-2. Cross section of circular start divided Into 12 •qu«l
voat. shaving location of traverse) points at centroM ol each area.
0
0
0
| . j , i ;
.Jj. j j
"i" I """!
1 a | • J •
--j— — r— — -T— —
| . ( . .
! 1 i
Figmo 1-3. Cross scchon of rectangular slack divided Into 12 equal
areas, with iravciso points at cenlrpld ol each area.
Triwrie
"."* i
'£~l* ^_ »» Str »f Intent Mint* M • <
:14.4' 1.7
i
M.I il.O
I.I
11.7
1.1 : Ml M
10.1
' 71.0 ' 11.1 . 19.4
1.1
l.tl 1.7 1 1.7
14.4 i 11.4; 0.0
' 01.1 ' 70.1 ! 11. 1 II.I
, . !«..
10
II
It
11
14
10
14
17
IS
1*
10
n
it
ti
14
.H.I
i I
i
1
1
M.7 i M.t
Uijll.0
II.I
N.7
77.1
41.1
01.1
07.1
17.71 14.1
is.o
11.1
64.1
71.0
IM
U.t
M.I
07.0
H.I
Il.O
Ml
II .1
71.1
70.1
N.I
00.1
01.1
00.1
1.1
4.1
I.I
IM
11.1
Il.O
It.)
17.1
U.I
11.7
71.0
11.1
17.1
II.I
M.I
N.4
lirtli
1.4
I.I
7.1
10.0
14.1
III
11.4
».4
».!
11.1
70.4
71.1
11.1
11.4
11.1
OM
H.I
N.4
r __
1.1
1.0
1.7
0.7
1>.0
U.I
1.1
:.!
i.i ! i :
1.0 I 1.5
0.7 1 7.1
H.I 11: i
14.1
11.1
10.4 14.3 l!» 1
11.0
19.1
11.1
11.1 |(0.l
H.I •« :
11.!
ii.i ; ».i
M.I
71.0
71.1
M.I
17.1
10.1
01.1
M.1
01.1
"
40.7
17.1
U 1
II.I
U.S.U.I
71.0 | (7.7
70.1.71.1
Il.O
41.4
11.4
01.1
04.0
M.1
04.0
77.0
10.6
II.I
41.1
(0.1
U.I
M.i
01.1
01.0
3 33 Pur rectangular Mack* dlvid* the
ehM* icctlon Into 01 many equal rectangular
•re.il a* trarerw polnu. luch that the ratio
of the length to the width of th* elemental
areoa la between one and two. Locate the
•.ravene point* at the centrold of each equal
urea according ta Figure 1-3.
3. Jtr/rrenee*.
Determining Diut Concentration In a Ou
Si ream. A8MK Performance Test Cod* «37.
New York. N.V.. 1DST.
Dovorkln. Howard, et •!.. Air Pollution
S.urco Tesllng Manual. Air Pollution.Control
Uhlrlet. Los Angeles. Calif. November 1003.
Method* for Determination of Velocity.
V-Jiime. Diut and Mint Content of reciplinllon Dhtolon of Joy Mnnu-
tacturinK Co.. Los Angeln, Calif. Bulletin
WP-30. 1008.
HlniKlurd Method for Sampling Slnrki !•*
Paniculate Matter. In: 11)71 Hook of A8TM
Standard*. Part S3. Philadelphia. Pa. 1071,
A8TM Oe*lgnatlaii D-102B-71.
umioo i—DnnuiNiTtoH or arncic OA*
VILOCITT AND tOLVMKniC MOW IATK ITTPC
• mot TUBII
1. frtnelf'e and applicability.
1 1 Principle. Black cm velnelty U deler-
mlnril from the giu derully and from menu.
uremeiit of the velocity bead tiling a Type 8
(Slauiehelbe or revena type) pltot tube.
1 a Applicability. Thl* method ihould be
applied only wben fpedned by the test pro-
cedure* for determining eompUano* with the
Mew Source Performance "-—••-IT
9. ^pporolw.
3.1 Pilot tube—Type 8 (Plgur* 8-1). or
equivalent, with a coefficient within ±»»
m*r th* working rang*.
ta Differential preaure gauge—Inclined
manometer, or equivalent, to meaoure velo-
city head to within 10% of the minimum
value.
SJ Tcmperatur«g»uge—Thermocouple or
equlralent attached to the pilot tube to
meanir* *taek Umperatura to within Utt of
tlie minimum absolute Mack temperature.
2 4 Pressure gauge—Mercury-nlled u-tub*
manonieur, or equivalent, to measure clock
prr-miira lo wlihln 0.1 In. Hg.
2A Darometer—To meoaure aimoapherle
prvuure to within 0.1 In. Hg.
20 da* analyzer—Ta analyxo gai composi-
tion far determining molecular weight.
2.7 Pltot tube—Standard type, to cali-
brate Type 8 pilot tube.
S. Procedure.
3.1 Get up th* apparatus a* shewn In Pig-
tire 9-1. Hake euro oil connection* are tight
and leak free. Measure the velocity head and
temperature at the travcne polnu specified
by Method l. ^^
8.2 Measure the sUUe pressure In the
•tack.
8.3 Detcrmlue the stack gai molecular
weight by gas analyst* and appropriate cal-
culation* a* Indicated In Method. 8.
4. Calibration.
4.1 To calibrate th* pltot tub*, measure
the velocity head at some point In a flowing
go* stream with both a Type 8 pltot tube and
•eundard type pltot tube with known co-
efOclent. Calibration ihould be done In the
laboratory and the velocity of tbe Honing gas
•ireaiii should be varied over the iiorinal
where:
CP,,., -Pltot tube coefficient of Type 3
pltot tub*.
Cr.14-l'itot tube coefficient of standard
type pitot tube (if unknown, use
000).
Ap.i<=Velo<.i head measured by stand-
ard i. ,ie pltot tuba.
Api..i= Velocity head measured by Type r
pilot tub*.
(Appendix)
19
-------
B-3
1X1:0406
FEDERAL REGULATIONS
ss
polaUd
irtlwtw
vllb MM ttm
OM •wuttoa W to etfmihte UM MM* (M
I
BqiuU*n2-S
firms-S
Mp»MM4 OMJ. •» wlotttf tiMtm data. UM ttw »«H*n§ PMI
.!7 ^^ UitMlMttmeeliimiMofFliana-Btote-
tf
Umpntun •! Mute* Mo4Ulm,
tt Mote* i
PIPE coun.il
TUiINO ADAPTER
TtPlSPITOT
'Flfluno M. pilot tube-manometer assembly.
Environment R«poit*r
20
-------
B-4
STATIONARY SOURCES
•-in
121:0409
Mark. U fl, Kaehaaleal
Iruw&iaDoekOe,
Mew York,
M.T.
P*nr. t. H, .
book. MeOraw-Bill
M.T, 1MO.
Shlfebara. B. T. W. F. TBdd, and W. &
- - i of Enron IB Stack Saov
mUMon*
in.Ina.Mti
MewTork,
pllni McttumntnU. Piper pmantad •! tin
AnniMl UMUnf of tb* Air FMlntloD Centre!
AoaoUtlon. 8V Lftuto. Mo.. Jun* 14-10.1P70.
Stondsrd Method for Sampling SUeta for
FBrtloulaU IfMMt. IB: IB7I Book of ABTM
8Und>rti. Part », PhUadelphla. Pa, 1871.
ABTM DciltnaUan D-SBS"-?!.
Vomwrd. l. B, Btmnitarr Fluid Median.
la. John WUtr * Bom, Inc.. N*v Tort. M.T.
194T.
PUNT
DATE
RUN NO.
STACK DIAMETER, In.
BAROMETRIC PRESSURE. In. HO._
STATIC PRESSURE IN STACK (P,). in. Mj._
OPERATORS
SCHEMATIC OF STACK
CROSS SECTION
Travon* point
Velocity (Mid,
In.HjO
Stick Ttrnparatiira
AVERAGE:
Flggre 2-8. Velocity traverse data.
-------
B-5
121:0410
FEDERAL REGULATIONS
U lategreled mmfU {Hfun»-»t
U.I Prob*—StaliilOB) atoal ar
equipped with • an** to
ifta HriBiMaw
•J
. - to atmetod fMm a
•od analyzed lev
Onatvnalyaer.
ij Appiioabuuy. nil
r or equivalent—
ahouldte
tettpro-
wlththe
any em
U4 Meedl* valve—TB adjust now Ml*.
ta.4 Pump—Uak-fre*. diaphragm typ*.
01equivalent, to pull gas.
up tho •qulpmrat M ihown la
«-l. mrttaf MIT* ill oonawttam *n
Ptoct tho prate la tho tuek tt •
arotedure will ladlcat* whether a grab i
pi* or an Integrated Mmple to to b* ueed.
S.4PFOTIIU.
S.I Or*beampte(Plgar*»-l,.
ft.1.1 Probe Btalalete eteel or Pyres'
glass, equipped with • Biter to remove partto-
S.IJ Pump On* way *qu**s* bulb, or
equivalent, to transport ga* aampi* to
b«t—T*dltr.> or •qulTCln*,
with a opMlty of 1 to S eu. ft. Lnk t«l tko
DM in tiio Ubontory befei* atnf.
U.T Pilot tub*—Type 8. or Mulmlmt.
*ttMh*d to the pntx w Uurt tto tarapllaf
Bow ntt cut b* mutatod proporUonil to
UM BtMk fM vdooltr wben vuoelty to «uy>
lag with Urn* or » Hmpto tnvno to
Intofnted umpUny.
•At B*MintoUMMbtektc.Mu»tlM
IB Plfara »-t with tht
i tlw piwte !• Uii
i iim. Orannt
M.I OMM MMljmr. or •a.uiratent.
TOMMLTZH
futua
taunioou
stack and purg* th* ^mmtfuuf no*, vwnwn
tb* bag. making aim that all •rantetlon* are
tight and that thm an no leak*.
S.U Sarapl* at a rat* proportional u the
•tack velocity.
M Aaaiytto.
U.1 Determln* the «>„ Of and CO con-
centration* u soon a* poulbl*. ICak* M mr.ny
pa**** a* are n*ceo*ary to giro eonitant read-
ing*. If men than ton paam ar* neetiury.
replace th* abeorblng nlutlon.
IJJ Per grab campling, repeet the ••tri-
pling and analyal* until three •oainutlv*
aample* vary no aun than OJ percent by
volume for each component being analysed.
MJ Per Integrated aunpllng. repeat the
analieto of th* aample until three eomeeu-
tlv* aaalyac* vary no more than oa percent
by volume for each component being
analysed.
4. Calculation*.
4.1 Carbon dl«dde.AT*ng* the thm con-
•atsuttva rune and report the mult to tb*
aeamt0.1%OOr
4J •see** air. UM Bquattoa 0-1 to calcu-
late exeat* sir, and averag* th* rum. Report
the mult to tho ntamt 0.1% «C*M air.
%EA-
(%0i)-()..*(% CO)
"c Nt) - (
FsuroM. Ora>Mmel|ng tnln.
MR I
So,xioo
equation 3-1
«BA=Pereent exeee* air.
%O.=P*n*at oxygen by volume, dry bail*.
%K,—Percent nitrogen by volume, dry
bail*.
%OO=rere*nt carbon monoxide by vol-
ume, dry beat*.
•JM=Ratlo of oxygen to nitrogen la air
by volume.
44 Dry molMUlar weight. UM Equation
B-4 to calculate dry molecular weight and
average th* rune. Beport th* mult to th*
; tenth.
•quatlon 3-2
tb-Ory molecular w*l|ht. Ib./lb-mol*.
%OOa-Pero*nt carbon dloxld* by volum*.
dry baala.
%Oy*P»mnt o«yf*n by volum*. dry
«N«-P*miit nltrogm by volum*. dry
Figure 3-2. IntograM gu • eampltng Inht.
0.«4-Mel*oulBr weight of carbon dioxide
divided by 100.
Oja-Uoleeular weight of oxjcea divided
by 100.
03».Moleeular welfht of nitrogen and
CO divided by 100.
Environment Reporter
10
-------
Altahuller. A. P, «t ml, Storage « <>••»»
and Vapors In Plastic Bags, tat. J. Air *
Water Pollution, •zTS-Bl. 1963.
Conner. William D, and t. & Nader. Air
Sampling with Rattle Bag*. Journal of the
American Industrial Hygiene Anodatton.
39:391-397. May-June 1984.
Devorkln. Howard, et aL. Air FoUnUon
Source Testing Manual. Air Pollution Con-
trol District, Lot Angeles, Calif, November
196S.
UITHOO «—ecntmuTioic or KOOTUKS
and equipped with a mtcr to i
late matter.
U Inmlngeia-Twi
each with 80 mL capadty. or <
3.3 be bath, container—To
moisture In Implngera.
Silica, gel tube (optional)—To protect
end dry gas mirtiT-
. Needle valve—To regulate gas now
Ate.
34 pump—Leak-free, diaphragm type, or
equivalent, to pull gaa through train.
3.T Dry gaa meter—To measure to within
1-- of the total sample volume.
3A Botameter—To measure a
1. Prfmetnl* and appUeabttlty.
1.1 Principle. Koliture Is removed from
the gaa stream, condensed, and detennlnod
volumetrlcally.
13 Applicability. This method la appli-
cable for the determination of moisture IB
stack gaa only when specified by test pro-
cedures fer determining compliance with New
Source Performance Standards. This method
don not apply when liquid droplets an pres-
ent In the fas stream' and the moisture U
subsequently used in the determination of
stack gas molecular weight.
Other methods such as drying tubes, wet
bulb-dry bulb techniques, and volumetric
condensation techniques may be mod.
3. Apparatus.
3.1 Probe—Stainless steel or Pyrex* glass
suffldentlv heated to prevent
'If liquid droplets are present In the gaa
stream, assume the stream to bo saturated.
determine the average stack gas temperature
by travertins, according to Method l. and
use a psychrometiie chart to obtain an ap-
proximation of the moisture percentage.
• Trade name.
from 0 to 0.1
3 9 Graduated cylinder 38 mL
3.10 Barometer—sufficient to read to
within 0.1 inch Rg.
3.11 Pitot tube—Type 8. or equivalent.
attached to probe so that the *»-T""I **v
rate can bo regulated proportional to the
suck gas velocity when velocity la varying
with time or a sample liaveiie la conducted.
3. Procedure.
3.1 Place exactly 5 ml. distilled water In
each implngcr. Assemble the apparatus with-
out the probe as shown In Figure 4-1. Leak
cheek by plugging the inlet to the flrst Im-
plngcr and drawing a vacuum. Ins " '
flow through the dry gee meter la I
l y. of the sampling race.
3.3 Connect the probe and sample at a
constant rate of 04174 c Jjn. or at • rate |
poruonal to the stack gas velocity.»
•""P""g unta the dry gaa meter registers 1
cubic foot or until visible liquid drapleu are
earned over from the flrst Imprager to the
HEATED
FILTER'(GLASS WOOL)
ICCUTH
LOCATION.
TBT
DATE.
OKMTM.
Flgun4>l. Metttum gmpllng Umtn.
ca
I
dry gas meter readings aa required hy Ylguro
oolleetlng the eamnle, BMBim
the volume mcreaet to the nearest OS mL
4. CUoIattont.
4.1 Volume
VvrsVol
Vt
Vi
of water vapor ecUeetad
(standard conditions). eu. ft.
*lnal volume of Implnger eontente.
equation 4-1
•B.
pibo-Denslty of water. 1 gVml.
T.M=Abeoluto temperature at standard
Inltlsl volume
tents, ml.
Bsldeal gas constant.
of uopmgei
3133 Inches
sjo* R.
P.M=Abeolnto pressure at standard eon-
dlttons.39M Inches Hg.
Megeaafoleenlar weight of water. U B*y
""IV
-------
B-7
1X1:0412
FEDERAL REGULATIONS
i temperature of99VF.
•era eonnected IB **rtea with gtaee ball Joint
fittings. Tte fin*, third, and fourth tmpln-
g*ra are of tte Oreenburg^nlth - '
KU OUaswashbuMla* Tw»>
8U4 OlaataampMi
U Analyst*.
modlflod by replacing tte Up with a K-lneh
D gUta* tote Mttadlng to oat-half Inch
from tta bottom of tte Bask. Tte osoond Im.
laeteeBg.
conditions. AM* R.
T. BAbedototemperatana*
4JQ)
. V.
. _ to of tte Oraenburg-Smlth
with tto -*™fir< Up. A eondMMir
«Md In ptaM of UM Implnger* provided thai
tte motetur* •MUM* of tte ataok gs* aa
•ua b> determined.
94J Metering lyftem—Vacuum
_; temperature «o within •• F, dry
•M meter with a% accuracy, and Mated
equipment, or equivalent, aa required to
malnUta aa IsoklneUo campling rate aad to
mJ.T
SJJ
•X* Analytical MUBOI T
±0.1 mf.
•J.4 Trip batanoa-MO o>
measure to ±048*,
9. Jt*ap»te.
U Sampling.
9.1 J Plt
and preweJghed.
9.IJ Blltea ft—Indicating typt.
Bwab. drlod at 1W a (HO* 7.) lor I
*.1J wator.
i.1.4 Crusted tea.
aampl* raeowy.
•-W
In tte
V..BVOIUBO of water
(att
equation «-S
of water
U
to ±04
B*.
•J
•J.t Wator.
a).eii.tt.
I. Mnalpte «id oppKeaMHty.
1.1 PrlBdpto. ParUeulato mauer l» with-
drawn laoklntueaiiy from tte aoureo and Ma
weight U determined gn*imetrleally kftor n-
moval of imeomblned wator.
13 Applicability. TbU method to ippllcm-
Mo for the dotenalnatloa of parUeuiaU omb-
•tont from itaUonary aouroM only wten
•paeiaad by the U»t proeeduni for dttcrmln-
Ing eeapllanco with New aourct Perform-
ance Standard*.
9. Apparetut.
3.1 Sampling train. The deilgn epeelflca-
tlone of the paniculate nmpllng train uwd
hy EPA (Figure 5-1) arc described In AFTD-
OMI. CommtrcUl model* of thl* train an
avaiiaoio.
9.1.1 Neulo—Stalnlo* elect (310) with
aharp. tapered leading edge.
9.13 Probe ryre«' glacj with a healing
•jr»tem capable of maintaining • minimum
pw lempemture of 990* P. at the nit end
during campling to prevent condensation
from occurring. When length limitations
l«Tr4ter than about g f I) are encountered at
. Irmpcratum less than 600* P.. Incoloy S23'.
or equivalent, may be used. Probe* for sam-
pllni pjaa stream* at temperature* In excess
of One- p. must hare been approved by tte
Administrator.
9.IJ Pilot tube—Type 8. or equivalent.
attached to probe to monitor stack gas
velocity.
•Trade nan*.
TUHOPTIOML HtKKrlMCO
•YMEQUVAUMTC
collected
.en. ft.
BncApproxlmat* volumetrle proportloi
of water vapor la tte gat (beam
l*avlagttelmplngen.0«8.
g. Jb/erencct.
Air PeUvUon Xnglneertng Manual. Danld-
aoa, J. A. (ed.). OA DHBW. PBS. HaUonal
Oenltr for Air Pollution Control. Cincinnati.
Ohio. PBS Publication No. 9BB-4P-M. 100T.
Otvorkln. Howard. *t al. Air Pollution
Aeoree Testing Manual. Air Pollution Con-
trol Dtotrtst, Los Angeles. Calif.. November
Methods for Determination of Velocity.
Volume. Dust and Mist Content of Oases.
Western Precipitation Division of;
factoring Co.. Lo* Angeles. Cs
WF-M.106B.
Mknteo 8—DcTBuuM*noM or FMneutaixi
FBOM STATIOM** BODBCSO
^VACUUM
AKA nLTBHOUHI / THEsMOHEIBI CMKI
M nn ma
Plain 5-1. PMIeuUbMMpllno tain.
3JJ Dnleeant—Drlerlte.1 Indicating.
v> anPOCttfaWefe
4.1 Sampling
4.1.1 After selecting the ssmpllng site and
tte minimum number of campUng point*.
dotormln* tte stack pressure, temperature,
moisture, and rang* of velocity head.
4.1.9 Preparation of coUecUon train.
Weigh to tte nearest gram approximately 900
I. of silica gel. Label a niter oT proper diam-
eter, desiccate* for at least 94 hour* and
weigh to the nearest O.B mg. In a room where
the relative humidity I* leu than 80%. Plaoe
100 ml. of water In each of tte first two
Unplngen. leave tte third Implnger empty,
and place approximately 900 g. of proweighed
silica gel In the fourth liaplnger. Set up tte
train without the probe a* IB Figure 8-1.
Lent cheik tte sampling train at tte aam-
pllKg alto by plugging up the Inlet to the ni-
ter holder *:id pulling a 18 In. llg vacuum. A
leakage rate not In excess of 0.09 e.f jn. at a
vacuum of 18 In. Kg la acceptable. Attach
the probe and adjust tte beater to prorld* a
gas temperature oT about 950* F. at tte probe
outlet Turn on tte Alter beating system.
Place crusted le* around the Unplngen. Add
•Dry using DMerlt*' at TO* F.±10* F. 4J.
more lee during tte run to keep tte temper-
ature of tte gate* leaving tte last Implnger
a* low a* possible and preferably at 70* >,
or lest. Temperatures above 10* F. may result
In damag* to the dry gas meter from either
molatura condensation or excessive teat.
4.14 Paniculate train operation. For each
run. record the data required on tte example
sheet shown in Figure 8-3. Take reading* at
each sampling point, at least every 6 minute*.
and wten significant changes IB stack con-
ditions necessitate additional adjustment*
In flow rate. To begin sampling, position tte
nonde at the first traverse point with the
tip pointing directly Into the gas stream.
Immediately start tte pump and adjust the
flow to lacklneuo conditions. Sample for at
least 8 minutes at each traverse point; sam-
pling time must be tte same for each point.
Maintain taoklnetlo sampling throughout the
sampling period. Nomographs are available
which aid in the rapid adjustment of the
sampling rale without other computations.
AFTD-0576 details tte procedure for using
these nomograph*. Turn oft the pump at the
conclusion of each run and record tte final
readings. Remove the prate and Bead* from
tte stack and handle In accordance with the
sample recovery piousm described la eectlon
Environment Ropoilor
12
-------
B-8
STATIONARY SOURCES
•.ITT
121-0413
«*.u-Vblum* of watir
"
eoaditioM).
Vi.-1Mal volume of UoaM ooOeetod IB
implant* aaddUoa Ml (M*Flf
TflM •?••)• BL
MuIualMular wneht •Twatar. II »y
• • TUMI IM eoacUnt, *Ut laeh**
•V-BQ. ffc/lb^mote-'B.
T.M-Ab*otata taimmatiiM •» itandMd
* a
at
4J aaBtpt*rwoT*ty.XnielMcf*lamoT. Omteftur Wo. I. Weigh tb* MOB* illlea Ml B^-
tag th* oolleeuoa trala Horn tb* tart Hta to and report to thi - -
the e*mpl* noorcrr en*, to mlntmteo tb* •. OurbraMoa.
torn of oolloitod Mmpto or th* Mia ct o** method* at
•JrtnaoMM ptrtlovlata m*tt*r. B*t MM* a b**a approvod by th* Admlatatrator to whwis
portion of Ih* aeMoa* uofl la tb* auaplo oaUbnto th* oriflw mttar. pltot tab*, dry BM -r
I mm A liiMilt §ftm •nalwrfa M«««ii»a «i^ MM ****m» aiMi moh* hflattf. RMBllBfal* H •
of watar tram tb* CM tan* im- aftelaA'tortMrMr v'M-V.b...(wito;kilMBiOT.l.. Plae* loon " ' '
eqiwllon 6-3
m*!83£ttiimlSXmln>" *"* ** ******
matter and aottoa* waihlBM from all volume meiniiwl by th* dry MI mur to «• Total Mtttoalato wetaht. itetomiM
Mmpte emond raTton prior to th* fiber ateadmrd oondlttaBt (TO* K. MJUnehM HM _.. to..! fmwUeaSataSASm ^T^^S
lathtooDBUIaeraBde^.Uieanr'.rbUd*. by nriaf B(iutlon ft-L S ^SfflflSflSlES? dato^lM
(or*M).
OoBteiner Wo. I. Traneter the
fe?oi& ^Itf ffourtta luiplnMT to MM irrlfll'til CTI
wtttiur iU*4 icftl* Vts) •*• rubTMr prttVinIBM SMI
an aid In removing elllea gel from th*
AndyiU. Bword th* d>U no^ilnd on
cntopl* *b**t mown la rlfon g-t.
~~ i «ok wmpto eoateltttr M follow*:
OOntotacr Wo. 1. 1ku*f*r th* BlUr *ad
•ay loon putJeulat* mmttar f*
to • Urad gam
dorieoit*. utd dry to • ooniUat
port mult* to th* nmwjt OJt BIB,
CtmMntr He. t. Itmtw tb*
wuhlBft to • t*r*d b*mk*r and cvrnpanU to
dijiiioj •» unbuilt temptnttir* utd
•nr*. DoalecaU utd dry to • oomUnt
B*port mtuu to UM nwiwrt OJ mf.
•qnmUon 5-4
V..H-Volume of CM i
dry gee meter
ttoDe).en.n.
V.-Volume of gM eunpl* thrsugh the
dry gee meter (meter eoadl-
T.u-Abeolate' tomptratnre at Maadarl
lAppmdlic]
-------
B-9
121:0414
FEDERAL REGULATIONS
PLANT.
DATf_
•UN NO..
CONTAINER
•BOm OF 'ARTICULATE COUfCTEO.
FINAL WEIGHT
TARE WEIGHT
WEIGHT GAIN
•4 •oetptablt nralta.
MBit wu UM limit oa ttTt
eampllnf reralta:
Tho fanowln»
£I£IIO%.UMI
the reran* ead repeav
forbelnoretor
IB* HUM,
T. Mtftrtmet.
MOnoum to
Iwjttaff M
DM.a.lMT.
MMIa, Bobtrt H. O
FINAL
INITIAL
LIQUID COLLECTED •
TOTAL VOLUME COLLECTED
VaUME OF LIQUID
WATER COLLECTED
IMPINGE*
VOLUME.
ml
SILICA GEL
•EIGHT.
0
fl*| ml
vtooamental Protection
Bom. Jerome J- »»-'«
ead Donation of
pilot
Annoy. APTD-OU1.
. B, «. T.
TMd. A Krthed of Intarpro
pUn( Data. Piptr pimnttd
niul MMUBI of UM Air Pi
tad w.
Slack
w.
. . MthoeMAa-
MMUBf of UM Air PaUnHan Oontrol
Irtlon, at. touto. Mo, AIM M-M. ino.
Smith. W. S» M •!. auek OM
Blmplin»d wttb HMT Cqulp-
PV HO. m-iit. tan.
CONVERT WEIGHT OF WATER TO VOLUME BY DIVIDING TOTAL WEIGHT
INCREASE BY DENSITY OF WATER. (1 g ml):
INCREASE, g
0 •'"••I
Flgure5-3. Analytical data.
644 eoneentraUoB la Ib Jeu. ft
VOLUME WATER, ml
, APOA PB
OpteUukUon* far Ino1n«imlnr IMIai
Mdtnl FMUIUM, PH* IfOAPO. 1991.
1. PrlMlpto end •ppHooMICty.
14 Principle. A (M eamjde to extracted
from the •ampllat pomt In the stack. The
MU mtot, Including nilfur UtoxUi. to etpo-
rated from the ralror dkndde. The •olfur
dkadde fraction to meaturta by the barium-
thorla Ulratloa method.
14 AppUeaMlUy. Tab method to appU-
eable tor the dftenalaatloa of aulfur dioxide
•mluloai fromctatloaary nureie only whoa
tpeolfled by the MM procedures for deUrmln-
~ looinpllaaeewlthmwaouieePiertamaaoe
'•2.203X10-^-
C"*HMleVd eondtttou). en. A.
4VT XtoktiwUc ' ' "
•quatlooft-e
JpMfBtM.
M Sunpllos. Sot Plfw* t-l.
«4.l rrobi ..fyio»» turn, •n
I to 6 mm. ID. with » hnuat »yiUm to
PNvmt ronrtniMthm ud • fUtcrtni mMlum
to runov* putieulBU outur nviirfm. «ul-
(Urto add mlit.
J.14 «od|« bubbiw^-on*. with ilMi
wool pMted In top to pvmat nilMite Mid
mitt cuiyonr.
3.14 Olu* wool.
1.1.4 Mldeet Implann-niM.
UJt Drying tubo—PMkod with • to Ifl
mah udleatlnftyM dllea «U or oqulnknt,
to dry the nrnplo.
1.14 V«l*o-NMdu nlTO. or oqulnlnt,
toMUuctflownU.
a.1.7 Pump—Lnk-frao. «Muum typo.
M4 Rau uettr—Bottmotor or oaulTft-
tont, to maamiM a 0-10 uaJb. flow ntnn.
a.14 Diy tat mMtr—aumdeauy Meurato
to moMuro tht tamplo volumo within 1%.
a.1.18 Pttot tube-Type a, or oqulnleat.
• Trade
Cftvi
RfjpoitM
16
-------
' only If & eampl* ttama It i*-
quired, or It ataek ga* velocity *atfa with
34.1
8JLB
24, Bampl* recovery.
•MHrENDPACIOjD
Vim QUARTZ OR
pmn
nFssfnor
PolyethyleB* enrag*
Man aaplnger ampl«*
2J Aailyrta.
mlanta and when ngninrant
r to calibrate the i
soJCAoannrtmnnE
justmeatt la Sow rat*. To begin sampling, U standards* th* berlun
portion th* «p ef tb* probe at th* am against t> mL ef standard euttl
sampling palm end ittrt th* pump. 8am- taming 100 mL ef IsopropanoL
pie proportionally throughout the run. At a. CtlrafirHttttt
the conclusion ef each ran. turn off tb* 94 Dry gat volume, i
pomp aad record the final readings. Remove volant measured by the <
ta* prate from th* eteck and dimming it standard eamUttoa* no* V.
from th* train. Draia the lot bath and porg* Hsl bi udag equatloa 3-1.
th* remaining part of the Mia by drawing ^ ' ^^ ^
dean ambient air through tb* astern for IS »• i
U Bampl* recovery. Disconnect th* ha-
of th* midget
th*
bottlt.
«al th*
Poor th* watcnt* of
Into a potpMfejfeM
&M th* thn* mtfftt 1m-
tata* with 01*-
6-1
aptouulp
•fc
of th* *tonc« cootBtaur to • 80 ml. *ola-
mrtrto fluk. Dllut* to tin rank with O»-
lontnd. dtMIled water. Flpttt* • 10 ml.
aliquot et ihli *olutton IBM a ill ml. nea-
" , «dd«0 Btt. Of f
Off MS
FIgmM.
two to tone drop* of thorla lodleater. TMraU
to a pink tndpotnt mat OM JT bartom
pnealonu. Boa • hUak with **eh
B.
»J. TA*
dry gas metsr (eoncM
tuns), en. ft,
V_-Volum*af gas
dry gas raeter
ttta*).ca.ft.
TlM-Ahtatat* tempemtoj*
coiMllcons. 630* B.
T.-Aiaiegs dry ga
09
I
to mL sta* (04 mL divisions) and 30 aL
eta (04 mL divisions).
S44 Volamrarto tlstwe 80 ml, 109 mL.
aadlMOmL
2A3 Burette*—• mL and SO mL
U4 Xrtenmeyer flask—lasml.
3. Bespcntt.
in-
to jtOJXXB If
which ba* pmleBir/
3.1.1 Water—Oeloalagd. dlstuted.
3.14 IsoprapanoL 30«—Mix SO mL at Iso-
pnpaaol with M mL of jlsMlted water.
mL of 30% hydrogen peroxide to l liter with.
distilled water. Prepare fresh dolly.
U Sample recoveiy.
34.1 Water—Pelonlaed. distilled.
34J IcopropuoL. 80».
pbthalate (primary standard gnde).
4. ~
4.1
4.1.1
U mL of 00% Isopnpanol Into th*
bubbler aad 10 mL of 3« hydrogen pennd*
Into each of tb* arst two midget Implngere.
i to* final midget uaprager dry. ~
Analysts.
1 Water—Da
dlatllUd.
fy^puMmifll
Tttorln indicator—l-(o-*noaapaea-
vuco|4-aenhthol-3«-dls(dfoale add. dleo-
dtam alt (or equivalent), maaorie 040 g. la
100 mL distilled water.
34.4 Barium perehlorata (9.01 fr>—Dla-
•olve 14V g. of barium percnlorat*
ISs(OOJ,.3H10) la 300 mL dtotUM water
bl* th* tnta aa ihown la ngur* 0-1.
check th* -"-|r""t trala at ta* T»~r"nt
Hi* by pluvial th* prota latot aad puUlat
a 10 lachc* Bg vacuum. A Makif* rat* not
la men of 1% of th* ——r"-l rat* li ac-
ceptable. Canfally nleaai th* probe rnlvt
and torn off th* pomp. Ptew emthed
around th* latplnftn. Add more let dur-
ing th* raa to k*ep th* tempcrator* of th*
gjuea iMTlng th* lait Imptagcr at W F. or
tan.
4.14 Bampl* conecttoa. Ad]o* th* OB-
ple flow rate proparaanal to U» «tack gai
1M X 10-«- Convemaa faetor.-taeradlBg the
number of gram* per gram
oaulvaleat of sulfur dlosn*
(33 gVg.-eq.). 4W.8 g./lb, aad
1400 ml/L. lb.-Ug.-nu.
V,-volume of banum perchlorat*
for the sample.
Vlt—Vohua* of barlam perchlerate
Utraot and for th* blank, ml.
H-NonuaUty of barium perehlorat*
Utrant. g.^qyi.
V_..—Ttoul aolutloa volttm* of ndfar
dloUd*. M ml
V,—Velum* «t aampl* aliquot tl-
V».,,—Volume cf gas cample through
th* dry gat meter (standard
conditions). cu. ft, we E)us>
ttcao-l.
Itaaufaetunng Puincsee. OA. BOBW. fHB.
Dlvtslea of Ah- PoOutloa. PuSUe Bealth Bsrv-
N* rnbUcaaon Mo. IMVAtVU. Clndaaatl.
Onto. 10g».
Corbett. P. P. ft» Oetermlaatlan at 80,
end 00, IB «u* Qasa. Journal of th* Insti-
tute Of Fuel. 34:331-843. 1301.
Matty, R. B, and r K. out .
Flua-Oas SO, aad 8O, Power WttOwwT. 1
vember. IBS/.
Pattoa. W. F. aad X* A. Brlak. it. t
Bqul^nent and Tecnalqnce for Be tripling
OtiBiiilcal Procea Oases, J. AVMlatkaa r
trat Aooelatlen. U. 1U (1*31).
1. Frlnctple
-------
B-ll
121:0*16
FEDERAL REGULATIONS
(FOB)
8.14
valve Tbor*
14 Applicability. Tata method to _
Mt for Uw measurement of altrogen
from atatkmary
nly whoa
by the test procedure* for determining
nuance with Mnr
Standards.
fl. J
M Sampling. Bee Figure VI.
•.1.1 Fiubs fjiei' glass. heated. with
fUUr to NBIOM paniculate matter. Beating
to iianeeesury Iftheprobe remain* dry dnr.
LlVcMtetlai flask— Two-liter. Fyrex.'
imwd bottom with short aMk and 14/40
standard taper opening. protected •(•Hut
g.J4 Temperature gauge Dial type ther.
BMtneter. or aejulvaieat. eaaahlo of n
lag g* P. Intervals from »• to 138* P.
3.14 Vacuum line Tnblng oapahto of
withstanding a vaouum of g Inch**
lute procure, with T"o
stopcock, or equivalent.
8.14
laches, with OJ.laea
•setllone.
tnehetRgo
valve to Itt
t* at
the
"veaf pedtten aad tuna aft* the
f tbsreisavM'
Of O*M n|IIU**)g
•Men la the meraury level. It then
Me change ever the spaa of one
Baeord the Initial volume.
temperature, and b
the flask wive to Ita
then do the
. TUra
8.1.T IMmp-Oapable of producing a vac.
warn of g Inches Bg abeoiute i
3.14 SqueeasbuIb-OBoway.
84 Sample leooverr.
84.1 Pipette or dropper.
rometrlo pre
•pivgaXposltloa. and
with MM pump valve.
Forge the probe aad the vacuum tube using
the squeeze bulb. If eondeneatlaa occurs la
the probo and flask valre area, heat the probe
^•ifl purgw uatll the oondeassjtloa vUsappoan.
Then turn the pump valve to It* "vent" posi-
tion. Turn the flask valve to Me temple-
poollton and allow aampls to eater the flask
to about II seoonda. After ooUeeUng the
•ample, turn the Baft valve to It* "purge-
position and dtssonaeet the flask from the
sampling train. Shake the flask for g
minutes.
•UIU.I
simian* •»,«/•
'!*•• M. tM(l«S till*. IMk OH*. MM IIMk.
UJ Qlin with bottt*.
M Aaelyde.
34.1 Steam bkth.
MJ Beekne or ounraln—ISO ml, one
for ewb nmpto «nd eteadwd (blank).
UJ VoluiMtile pipette*—1.9. end 10 ml.
1*4 Transfer pipette—10 ml with 0.1 ml.
dlvMon*.
UJ VolumetrlD fluk—100 ml. one for
each cample, and 1.000 mL for the etaadard
(Blank).
U.6 Bpoctrophotometer—To mauure ab-
•ofbaaee at 430 urn.
U.7 Graduated cylinder—100 mt with
Ij0ml.dlv!iloiu.
93* Analytical bnlanee—Ta meaiure to
0.1 rag.
3. Ktagciti.
S.1 Sanipllng.
•.I I AbMvblng solution—Add 34 ml. of
concentrated BJBO. to I liter of dlcUUed
water. MU well and add • ml. of a percent
hydrogen peroxide. Prepare a fnih solution
.weekly and do nut moose to eureme beat or
direct sunlight.
3.3 Sample recovery.
3J.1 Sodium hydroxide (1»>—DUtoIre
40 g. HaOH In dimmed water and dilute to 1
liter.
SJJ ttcd lltn.u« pspsr.
MJ Water—TMonlied, distilled.
•4 AaalyHa.
M.l Fuming eulfttrte eeld—16 to Ig* by
weight free sulfur trwdde.
»»S Phenol—White eolld reagent grade.
•*J» Snlfurle add—Concentrated reagent
34.4 Standard eolutloa-OlaMlteOMMg.
potaeslum nitrate (KrTO.) in diettlled water
and dilute to 1 liter. Par the working stand.
ard solution, dilute 10 ml. of the resulting
eolation to 100 ml. with dlctllled water. One
ml. of the working standard solution to
equlrslent to as «g. nltrogei
*»t Water—DdoahMd.
844 Fhanoldlaulfonle ««IH solution—
DlnolTe 35 g. or pure white phenol In ISO ml.
concentrated suirurtc add on a eteam bath.
Oool. add 75 ml. fuming eulfurlo add. and
heat at 100- O. for 9 hours. Store la a dark.
stoppered bottle.
4i Procedure.
4.1 Sampllag.
4.1.1 Pipette aa ml. of absorbing solution
late a sample flask. Insert the flask *alre
stopper into the flask with the valve In the
•purge- pealltaa. Assemble the sampling
train aa shown la Figure T-l and place the
probe at the sampling point. Turn the flask
valve and the pump valve to their "evacuate"
44.1 Let the flaek set for. • minimum of
M hours and then shake the contents for 3
minutes. Oonnset the flask to a mercury
fined V'tub* manometer, open the valve
from the flask to the manometer, aad record
the flask pressure and temperature along
with the barometric pressure. Transfer the
flask contents to a container for shipment
or to a 380 ml. beaker for analysis. Bine* the
flask with two portions of distilled water
(approslmatelr 10 ml.) and add Has* water
to the sample. Far a blank use 91 ml. of ab-
aorblng eolation and the same volume of dla>
tilled water aa used in rinsing the flask. Prior
to shipping or analysts, add sodium hydrox-
ide (1W) dropwtae Into both the sample and
the blank until alkaline to litmus paper
(about 3S to 36 drops In each).
44-Aaalyils.
44.1 If the sample he* been shipped la
a container, transfer the content* to a 360
ml. beaker using a email amount of distilled
water. Evaporate the solution to drynees en a
steam bath and then oool. Add 3 ml. phenol-
dlsulfoale add solution to the dried residue
and triturate thoroughly with a glass rod.
Make aura the eolation contacts all the resi-
due. Add 1 nU. dictated water and four drop*
of eonontrated sulfurlo add. Beat the solu-
tion on a eteam bath for a minutes with oc-
casional stirring. Oool. add 80 ml. distilled '
water. mU wall by etlrrlag. and add ooneea.
trated ammonium hydroxide dropwiae with
constant stirring unto alkaline to litmus
paper. Transfer the solution to a 100 ml.
volumetrte flaek and wash the beaker three
time* with 4 to 8 ml. portions of distilled
water. Dilate to the mark aad mix thor-
oughly. If the sample contains eollds, trans-
fer a portion of the solution to a clean, dry
centrifuge tube, aad centrifuge, or fllter a
portion of the Mutton. Measure the absorb-
anoa of each sample at 490 nm. using the
blank solution aa a aero. Dilute the sample
aad the blank with a suitable amount of
distilled water If abaorbanco fall* outside the
range of calibration.
8. OBIfbreltoa.
8.1 Flask volume. Assemble the flask aad
flask valve and all with water to the stop-
ooek. Measure the volume of water to ±10
ml. Number aad record the volume on the
64 Bpeetropnotometer. Add0.0tol6.0ml.
of standard solution to a *erles of beaker*. To
each beaker add 86 ml. of absorbing solution
aad add Mdium hydroxide (1W) dropwlse
uatu alkaline to litmus paper (about 36 to
86 drops). Follow the analyst* procedure of
section 44 to collect enough date to draw a
calibration curve of concentration In ft. NOe
per cample versus abaorbaaoo.
0. OaleulaMoas.
6.1 Sample volume.
Environment Reporter
16
-------
B-12
STATIONARY SOURCES
••HI
121:0417
844
WashbotUse-Tvo.
Graduated eyltndcn-atO ad. MO
V..-8*mDl* VOlUlM U Stand**
ttan* (dry bests). mL
T.M-Absolut* temperature at
•(M"Pramn at standard conditions.
8848 rache* Hg.
V,—Volume of flaik and valve, ml.
V.- VOIVUM or absorbing toiutlon.» mL
Inches Hg.
P.-Initial absolute pnasur* of flask.
Inch** Hg.
T,-Final absolute temperature of Bask.
T, - Initial absolute temperature of flask.
844 Olas* sample stowage eentalcars.
144 Graduated cylinder-380ml.
84 Analysla. '
84.1 Pipette—a> ml, 100 ml.
844 Burette—M ml.
844 Brleumeyer flask—880ml.
84.4 Graduated cylinder— 108ml.
844 Trip balance 808 g. capacity, to
6J Bamul* concmtMUon. Mad ft- "Ok
for weft sampl* from the plot of «g. HO,
versus absorbane*.
-16.2X10--
O-Concentration of MO. a* MO, (dry ai
m— Man of NO, In (M lamplt. «g.
V..-Samplo volume at itandard condi-
tions (dry basis), ml.
T Befemce*.
Standard Methods of Olramleal Analysis,
•th «d. New York, D. Van Noatimnd Co.. Inc,
Ma*. vol. i. p. 888-310.
atandmid Method of Test for OUdct o(
Nitrogen In OIMOUI OombuitloB Products
(Phenoldliulfonlo Add Procedure). In: IBM
Book of A8TM Standard*, part 23. Philadel-
phia, Pa. iocs. ASTM Designation D-1608-<0.
p. 788-788.
Jacob, If. B.. The Chtmlcal Analysis of Air
Polliiuuiu. New Tort. N.Y.. Intenclence Pub-
lUhm. Inc.. 1880. vol. 10. p. U1-8M.
atsTKoe a— eamanuMTiON or atnwaic «cu
tan AMD avtrum now HUSSIONS raou
sovscxs
1.
I.I Principle. A |U sample U extracted
from a lampllng point In the ataek and tb*
add mlit lncUidln| aulfur trljild* I* icpa-
ratcd from sulfur dioxide. Potb fnetloni an
meuurad atparatalj by the barlum-thorln
tttratlon method.
13 AppllcabUlty. Thte method U applica-
ble to determination of ralforlc acid mitt
(Indudlng eulfur trloalde) and aulfur diox-
ide from stationary source* only when spe-
cUUd by the tot procedural for determining
compliance with tbe Mew Source Psifuiui-
Mt 8t*\l)Cl*V4aV
8. Apparatiu.
81 aampllng. Bee Figure 8-1. Many of
tbe design specifications of this sampling
train an described In APTD-OM1.
8.1.1 Nozsle—atalnlese steel (818) with
sharp, tapered leading «dge.
8.14 Probe—Pynf gnu with a heating
system to prevent visible cnndansatlon dur-
ing sampling.
8.14 Pilot tube—Type a, or equivalent,
attached to probe to monitor stack gae
velocity.
8.1.4 Filter holder—Pyrex' glees.
8.14 Implnger*—Pour as Shown In Figure
8-1. The ant and third an of the Oreenburg-
Bmlth design with standard tip. The second
and fourth are of th* Onenburg-Smlth de-
sign, modified by replacing th* standard Up
with a tt-lncb ID glass tub* extending to
one-half Inch from the bottom of the Im-
plnger flask, similar collection
which have been approved by th*
trator. may be used.
8.14 Metering system—Vecu
leak-free pump, tharmoowten capable of
measuring temperatun to within 8* F, dry
gas meter with 8% accuracy, and mated
equipment, or equivalent, as required to
maintain an uoklneue sampling rate and
to determine sampl* volume.
8.1.7 Barometer—Tb measure atmospheric
pressure to ±0.1 Incb Hg.
•Trad* name.
84.8 Dropping bottle-to add Indicator
solution.
8. ***•*»<«.
8.1 Bampllng.
8.1.1 Paters Olsss fiber. USA type 1108
BH. or equivalent, of a suitable els* to fit
In the fllter holder.
equation 7-2 a.ij aillea gel—Indicating type. 0-18
•"i""""" mesh, dried at ITS' O. (880* P.) for 8 hours.
8.14 Water—Mounted. dUtllled.
8.1.4 Isopropenol. 00%—Mix 800 ad. of
ml with 800 ml. of detonlseo. dls-
taopropanol
ttltodwatar.
.VACUUM
LINE
•VACUUM
GAUGE
DRTTcSTI
Flfliira 8-1. SuKurie acid mi»l sampling train.
Hydrogen peroxide. 8«— Dilute 100
ml. of 904 hydrogen peroxide to 1 liter with
delonlnd. distilled water.
8.14 Crushed Ice.
8.8.1 Water— Delonlxed. distilled.
8.8.8 bopiapamd. 80«.
84 Analysla.
84.1 Water— Detanlsed. distilled.
844 iBOpropanol.
844 Thorln Indicator— l-(o-ar*onophtn-
TU8o)-a-nspbtbol-8. e-dlsulfonle add. dl-
aodlum salt (or equivalent). Dissolve 040 g.
In 100 ml. dinuled water.
84.4 Barium perehlorate (0.01W)— DU-
ectve 148 g. of barium perehlorate I Be
-------
rapid aaiactmant of tb*
oat otter r^npr*-t1i~
tb* procedure tor aatng
At the eoadnOoa of each run. turn'off tb*
pump aad record tb* Anal readlnga. B
t-1
from the train. Drain tbe toe batb aad pan*
dry pi meter (ttandard
tun*), cafe
V,.-Volume at (u
dry fa*
ttoB*).«a.R.
temperature
of raUtnle MM
_ ..
mL/U Ib.-Uc.-CDl.
at
ttbwtt «Md tar
V.t-Volum* at barium perehlorate
far tto bUnk. nO.
bulnm ptrehlonte to
to record
ttea with • mead
at iiflfur
oondltlons. dry
naaber of pama per tram
4J Sunple moicry.
4J.1 Timniftr th* Uoprapuial
flnt loptnftr to • 3SO mL
UM pfote. Ont ImpiBiCT. wad an oon-
' - - tb* filter «ltb BO%
UoprapanoL Add tb» rum ootuUon to to*
dllBder. OUnw to 200 mL wttb 80* taopnx
puwL Add U>« Oltcr to tli* aolattaa. mix,
•ad umaiter to a suitable itoraf* eoatalmv.
Ttanafer the colutloii (ram the aceoad and
tatal Implncen to a 500 mL gndnatad cfl-
tador. BIDM all Haoware betomit the Alter
•ad mica |*l implagcr wltt detoabad. dla-
toted water aad add tab rlnat water to tb*
cjlladir. Dilute to a volume or BOO mL wltb
ililnnlieil (linmed water. Ttaatfer tb* eola-
tion to a mutable storage container.
44 Aaalyaia,
44J fffc^fc^ tbe ooatalaer
prapaaM and tbe Altar. It tbe Alter
00. allow tbe fragment* to aetOe for a few
Biimitts befuie remorlac a aample. Pipette
a 100 mL aliquot of mmple Into a ISO mL
Zneamejw Aeak and add 9 to 4 drop* of
tbona uutteator. Titrate tbe eample wttb
. _ Pipette a 91 mL
aliquot at eampte into a 980 mL ~ ~
flaak. Add 100 mL of laopropanol and 9 to 4
drop* ot tbortn Indicator. Titrate
wltb bartom perebtarate to • pink end pout.
Repeat tbe UtraUoa with a aeeoad aliquot at
•ample. Titrate to* blanka la tb*
manner as the
B.C«HDraf
-------
B-14
STATIONARY SOURCES
S-2U
121:0410
*., Hal
of IsokuuUo Aource
Ageney, Air Pollution Control OOet Fubu-
cation NO. AFTtVOflTa.
The peatttve nhetnUloiial trror aaeedatoa
with aa avenge of twenty-five reading* to
tbOMfon Mtabltohad. ne eeeuncy of tho
method man bt taken Into eooount when
~ ~ mstalng poxalhlo vtolatloM of anpllp
.epatltyr^^ — ^"^
SJ Data Reduction. Opacity ahall ba de-
i* aa avenge of M consecutive
i recorded at lt-ateoad Interval*.
Divide the obttrveUor.e recorded on the rec-
ord abort Into otto ef M eoiteouUve obaer-
vatleaa. A set to composed of any 24 eon-
ment, Determination of Buifur Dioxide and
•altar Trknlde in Stack Daces. Emeryville
, 4010/BOa.
§ ••dnMJwMM ... t •••.ti-at.iin..
». . . ._ ^n* •»» oypnaiBuny.
Principle. TIM opacity of
aeentlve la "*•*• f~1 In BO
«**-" two
1.1 Applicability. This method to appu>
„, n, eabto for the determination ef the opacity
Utny
vtdblo
> Into the atmosphere; theaa emls-
etooa an uaaally la tho ahapt of a plume.
Thla method Involves tht determination of
pSume opaelty by qualified obttrvera. Tho
method indudee proceduree for tht training
and certification of observer*, and procedure*
to bo used la the field for determination of
plume opaelty. The appearance of a plume a*
viewed by an observer depeada upon a num-
ber ef variable*, toot of which may be eon-
tnttabto and earn* of which may not bt
controllable la the Bold. Variables which f^*i
bo eoatnlled to an extent to which they no
it to I BUI (b) and for'quaWyiuf'ob-
•**•» for Unadly tfttannlnlas optolty of
-
B. FrooadiirM. no obaeiiai qualified to
accordance with parigraph * of thla method
ahall net the following proosduna for vto-
ually determining the opacity of tmlaaicat:
tele overlap. For each art of M observation a.
caleulata the average by euaunlng the opacity
of the M oboes lalluns tad dividing thai turn
by 24. U an appll.^ble atandard epeelftea aa
averaging time requiring more than 14 ob-
servation*, calculate the avangt for all ob-
aarvatlona ••"'« during the apadfled **m*
period. Record the average opacity on a record
chest. (Sea Figure 9-1 for ea example.)
B.i
avenge opacity determined tram
benmtnti to 26 tflfltra&t tttaek
ek pl
with
__ __ _
plomaappeanneaTnclude: Anatoof thoob-
08nerwlthnapecttothapIUBHi;aB|laafU»
ebttnor with ranoet to tha anaTpolBt ef
obaerottoa ef Bttoehad and dataebedatoua
pluma; and angle of the obaerver with re-
apeetto.plunVa^ttadfromaiaetangubr
ataok with a large length to width ntloTne
Bethod inelBdea apoeUo erlteite anplteabla
to
Position. Tho qi
ttand at a distance tuffletont to provide _
clear view of tht emissions with the tun
oriented la the 140* sector to alt back. Con-
not to exceed IB percent opacity on any one
reading and an average error not to espied
TJ percent opacity In each category. Candi-
dates ahall be tested according to the pro-
cedure* described In paragraph 1.9. Smoke
generatora used punuant to paragraph U
ahall be equipped with a amoke mater which
matte the requirement* of paragraph M.
The eertlfleatlon ahaU be valid for a pertod
of a month*, at which time the qualification
procedure must be repeated by any observer
la order to retain eerUaeatloB,
U Certification procedure. The oerUfioa-
tton teat oonalata ef ahowlng the candidate i
luminescence and color
contrast between the plume and the back'
ground against which the plume as viewed.
These variables exert aa Influence upon the
appearance of a plume aa viewed by an ob-
aerver. and can affect the ability ef the ob-
server to accurately assign opacity valuta
to the observed plume. Studies of the theory
of plume opacity and field atudlee have dem-
onstrated that a plume U moat visible and
presents tha greatest apparent opaelty when
viewed against a eontnatlng background. It
followa from this, and la confirmed by field
Mala, that the opaelty ef a plume, viewed
under conditions where a contrasting back-
ground la present can b* assigned with the
greatest degree of accuracy. However, the:
tcntlal for a positive error la also the i
to the emission
dlnotto
Uma. eatlmated dlataaea
id
• __J epttd, deicrtptton
of the sky condition (presence end color ef
clouds), and plume background an recorded
on a field date abort at the time opaelty read-
ing* are Initiated and completed.
2.1 Observation*. Opacity obeervattana
a lisa eontnatlng background, the apparent
opaelty of a plume la lea* and approaches
tore aa the color and luminescence contrast
decrease toward cere. As a mult, significant
negative blaa and negative errors can be
made when a plume la viewed under leaa
contrasting condition*. A negative bias do-
ereans rather than Increases the possibility
that a plant operator will be cited for a vio-
lation of opacity atandarda due to obearver
Studies have been undertaken to determine.
the magnitude of positive errora which can
bt made by qualified obetrven while read-
ing plumes under contrasting conditions aad
using the procedure* set forth In this
method Tht results of these ttudlea (field
trills) which Involve a total of 769 sets of
26 readlnga eacb an aa follows:
(I) For black plumes (las seta at a amoke
genentor). 100 percent ef tht seta wen
read with a positive error* of leaa than "A
percent opaelty: 99 percent were read with
a positive error of leu than B percent opacity.
(2) For white plumes (170 sets at a amoke
generator. 1KB aela at a coal-fired power plant,
298 sets at a aulfurla add plant). 99 percent
of tha seta wen read with a positive error of
less than 7A percent opacity: OS percent wen
read with a positive error of leas than S per-
cent opaelty.
—- -—er™ — —»J pMMBw* ^%O O*V*
server ahall not took continuously at the
plume, but Instead dull absent the plum*
momentarily at IB-second Intervale.
2.84 Attached eteam plumes. Whan eon-
denied water vapor to present within the
Plume aa It emerge* from the — «-rlim out-
let, opaelty obaervatlona shall be made be-
yond tht point In tht pluma at which con-
densed water vapor to no longer visible. The
observer ahall record the approximate dis-
tance from the tmuokm outlet to the point
la the plume at which tht observation* an
a.3.2 Detached ateam plume. When water
vapor la the plume oonderaes and btcomet
visible at a distinct distance from the emla-
atoa outlet, tha opacity of emtodont should
be evaluated at the emlaalon outlet prior to
tht oondeneatlon of water vapor and tht for-
matlon of the steam plume.
2.4 Recording observation. Opacity ob-
serrations shall bt recorded to the nearest 6
percent at IB-aaoond Intervale on an ob.
serrations! record sheet. (Bee Figure a-9 for
an example.) A minimum of 24 obaervatlona
ahall ba recorded. Etch momentary observe-
tton recorded ahall bt deemed u represent
the average opacity ef emissions for a IB-
second period.
generato'. Plume* within each sot of 28 black
and 28 wnlte run* ahall be presented in ran-
dom order. The candidate aaalgna an opacity
value to each plume and record* his obser-
vation on a suitable form. At tht completion
of each run of 80 reading*, the acore of the
candidate la determined. If a candidate fans
to qualify, tht complete run ef BO readlnp
most ba repeated la any reteet. The amoke
teat may be administered aa part of e amoke
eohool or training program, and may be pre-
ceded by training or familiarisation runt of
tht amoke generator during which candidate*
an ahown black and while plumes of known
opacity.
u smoke genentor epeelfleatlona. Any
amoke gaaeratar used for the purpose* of
paragraph u ahall be equipped with a smoke
natter ««••*«*••* to meaaun opacity aoroe*
the diameter of the amoke generator stack.
The smoke meter cutput ahall display in-
atack opacity baaed upon a pathlength equal
to tht etaok exit diameter, on a full 0 to 100
percent chart recorder scale. The amoke
mater optical design and performance ahall
meet the specifications shown in Table 1-1.
The amoke meter ahall be calibrated as nre-
acrtbed In paragraph 1.1.1 prior to the eon-
duet of each amake reading teat. At the
completion of each test, the ctro and span
drift shall be cheeked and if tht drift ex-
eaeds ±1 percent opaelty. the condition shall
be corrected prior to conducting any subse-
quent test runs. The amoke meter ahaU bt
demonatrated. at the time of Installation, to
meet tht apeotncatlons listed In Table 9-1.
Thla demonatratlon than be nptated fol-
lowing any subsequent repair or replacement
of the photocell or associated electronic cir-
cuitry Including the chart recorder or output
meter, or every 0 months, whichever oceun
Apaetjleatbm
Incandescent
operated at nominal
rated voltage.
MO-75
-------
B-15
121:0420 FEDERAL REGULATIONS
MraiMter: l*euljte.n»» MAS Spectral respone* of photocea. monlna-deatlty Alter, of nominal opacity of
b. Spectral rimn*ni Photoplo (daylight Verify from manufacturer* d*U that tto Mr 10. and W penent IB tto smoke meter
of photocell. apMtnl rmpon*. of photocell to* . photopla MPOBH: U, tto pathtength. Filter* Minuted within ±s per-
tto human oyo— *p*ctral otnsltmty of tto Mil stall dooeiy out shall to used. Car* should to takem
reference «J). approximate tto standard epoetral-lumlno*- wton lamrtlng tto Alter* to pm.ni stray
o. Angle of vlow.... U* maaimnm total Uy curw for photoplc vumn which to refer- U|ht from affecting tto meter. Make • total
MJJ Angle of view. Check eonitruetloa Alter. The maximum error oa any on*
*. Calibration error- ±*% opacity, mail- **""«try to eniure that tto total angl* of tog shall Dei pw»nt opacity.
»l*w of tto amok* plume. M nm by tto MM Zero and epan drift. Determine
I. two tat apan si* opacity. M PtatoMll. do*, not exceed U*. Tto lout tto wro and span drift by eolibraUng and
drift minute*. •"•to ^ llmr ""V "• calculated from: l=» operattog tto amok* generator IB a normal
Urn*.-. 55 SMonda. Un'1 d/al* wblr» '"total angle of rtew; moaner ow a 1-hour period. The drift to
dstto mm of tto photocell diameter+the maMured by cheeking tto tero and span ot
amok* meter U dtatt»tar ** »»• limiting aperture; sad the end of this period.
. minimum of M L=UM «"»'"»«• •*• Th» «^*> *• *•/*•"«*»•
ea udoa white tto •mok.pamter lamp aumuit + th* dlamttn oftto limiting
U not producing mate. t*ortur»: and L= tto dtotwe. from tto Ump
MA 8BMKOBMttronlu*tlan.n.BieKo to tto limiting apntun. ~
m*Ur dolgn and ptrfonuae* an to b* 3 J J J Oallbratlen onor. Odaf neutral- ua •"«"«&*«* Manual for Air. VM. Knvl-
omlu.ud M fallow.: duulty Olun of known opacity, otoek tto MBBMBUI Protoetlon Afnoy. Bionnh Trl-
3.844 Llcht MON*. Verify fnm manu- tnor-betwon tto Mhul mpoBM ud tto •"•'• ^rk. WO. APID-1100. Aagust 1*78.
nutuml d«u ud from *oiu«. BMUUM- ttoomieu linear retponte of tto emoke PP.«.i-«M.
meat* made M tbe Unp, M UUUlled. th.t »»ter. Thto chock to acoompllihed by ore* ** Condon, HT, and OdUhaw.H,«and-
tto Ump to opercted within ±6 percent of etUbntU? tto emoke meter accord!!* to "ook el Phyii« lleOimv^OlI Oo, H.T, N.T,
tto nominal raul Mllafl^ UJ "* °>»n laewtlBf a otrta. of thro* UHLTIabteU.p.*4>.
Environment Reporter
-------
FIGURE 9*1
RECORD OF VISUAL DETERMINATION OF OPACITY
pA6E__of_
COMPANY
LOCATION
TEST NUMBER.
DATE
TYPE FACILITY_
CONTROL DEVICE
HOURS OF OBSERVATION.
OBSERVER
I
•<
OBSERVER CERTIFICATION DATE.
OBSERVER AFFILIATION
POINT OF EMISSIONS
HEIGHT OF DISCHARGE POINT
CLOCK THE
£» OBSERVER LOCATION
Distance to Discharge
Direction from Discharge
Height of Observation Point
BACKGROUND DESCRIPTION
WEATHER CONDITIONS
Hind Direction
Wind Speed
Ambient Temperature
SKY CONDITIONS (clear.
overcast, X clouds, etc.)
PLUME DESCRIPTION
Color
Distance Visible
OTIO IHFOIC'JVTIOH
Initial
Final
SUKHARY OF AVERAGE OPACITY
Set
Number
Tim
Start— End
Opaclti
Sum
*verage
M
f
o>
Readings ranged from
to
(opacity
The source was/was not 'In conpllance with
the time evaluation Mas made.
-------
m
FIGURE 9-2 OBSERVATK* RECOBO
PAGE Of .
COMPANY
LOCATION
TEST KUMBBT
MTE
OBSERVER
TYPE FAClllTV
POIKT OF ENISSTOnr
Mr.
Htn.
,
i
i
i
£5
i !
i '
\
u
Second*
'ii
30
«s
STEW) PLUHE
(check If applicable)
Attache?"
oeucned
COWENTS
COMPACT
UCATIOtf
TEST WK8QT
BATE '
ff
34
35
41
•£
(Continued)
OBSEWEt
TYPE FACIllTl
FOOT tf EMISSIONS"
Seconds
1 STEM! PLIffK
((check ff applicable)
-------
B-18
STATIONARY SOURCES
MM
121:04200
I to extract* j. ram a eampUat petiBt
md tor uorboB ^oauOOt (OO)
teat otlus a Xnfl.typo i
iodan«lymr(KDlB)or<
tJ AppAeoMlfly* This ••"* "• to epatl*
table far the determlaaUoB of earboa moo-
eaMo emtatloBS from statlMiary tourooi o&ty
whoa epoelBOd by tbo tort procedures for
- - - - " with aew man
itod aunpto to to M used.
•4 *•*»*. 0 to 1AOO ppm,
•J «m*HM per
Tppmooead 10 nemat OO, per rtppm
1.600 to IMO ppm raage Por devlom moae-
ariBg to tbo 0 to too ppm range. laterfMaos
ralloe ean b* as high as U psntBt RjO per
Si ppm 00 and 10 patient OO, per Mppm
00. The wj* of siiloa got andescarKo traps
wm altotlato th* major Interference prob-
lems. The measured gas volume murt be
oornsttd If thsee traps art
Bttt*lyto**p*ra*at*ndMp*MeBtspeB.
oftbecpeeU
•J mtfco go. todtoattog type, • to U i
dried at lTfOj«4T»P)forlbfun.
T.I tampMa*.
7.1.1 oonttMMaf esmpltBy. art up th*
equipment M shown la fliun 10-1 mekl&t
mm ill ooaaoetleat an took KM. Plate the
you* IB tht MMk at a campUni point and-
purge the mmpunt line. Ooonoet UM aae-i
iyaer and taala drawn* aunpto Into th<
Allow • adautai for tl»
B J.T Wot tab*. Tfp» B. or
joboa to tbt prob» M th
KM can ta niulatad praporttowl to tho
rnlooltj whn mlooltr U
tuner • ' •
lag u nqulnd by tbo tort i
113 and 8). OO, ooatrnt of tho >u awr b»
• tht lltthod • lato-
drtanataMd by ndo« tht Ifttbi
ntM wapi* proeotao (M IB
67 vit|hln| tho uotnt* OO, rn
I.'
BJ ^laolrMi (firm lO-«).
• Mention of trad*
noto dots not coartitato
end eompatlng OO, oonotntreUon from the
of tbo tube.
T.1.9 Integrated sampimf. Bvanmto tho
flexible bag. art up tht equipment M shewn
IB Plgun 10-9 wltt th* bag disconnected,
Plaet the prob* IB tbe stack and purge tho
I line. Connect the bag. making •
by the
ttot oil eoBBOrtloa* in taok fro*.
a nto proportloBtl to th* itoek
o>l Prooteloa. The pnowoa of meet. •. i
aaalysen to approximately ±* peneat of
•J AMuraqr. The aonmey of mart mm
to epproBlmately ±1 peraent at
•J.I OBI
rive Infrared
lit*
a.
M
Profto. 8Ulntao> rtod. or ibn *d
tiaokicjvippidwtth*, altar ton >to
thndoto aattor.
or equivalent
should bo demonstrated.
preferably by tbe manufacturer, to meet or
exoied manufacturer* epeemoatlon* aad
thow deeerlbed la thla method.
BJJ Dnttf tab*. To contain appraxt-
matolyaoogofsllleagal.
•JJ CejibroMoa eat. Befer to paragraph
•J.
niter. As reonrmnenrteH by
00, ooatnit of th* (U any bo i .
by otlaf tho Ilothod • latagntad auaplo
prondon* (M IB 9MM). or by wolabla*
th* ueorlt* OO, nmeml tab* and eompaU
lag 00. ooaeiBirattoa (Mm tho tot volume
tad th* wolfht s*lB of th* taho.
U CO A
la PUvro 10-a. eaUbmt*
BMBtlBd " "
B.1J 4»oeolsd eotXtnttr or
*w ftflBOTS) Uiy dCMS BMoMllTC*
lesmplf (Plgonio-a)
•>•••• errej^iPBs* »amMW*awma ajimwM ojtr *
Pyrex gltst, equipped with a alter to
BJJ Veto*. Needle valve, or equivalent, to
to adjust flow rat*.
•J.« Pump. Leak-free diaphragm typo, or
equivalent, to transport gas.
BJJ JM* meler. Botemeter. or equivalent.
to measure a flow range from 0 to 14 liter
per mta. (O.OSB efm).
UA Flesfble bd removal tube, to ensure
that oath fiMnpftiifirt to to good oaeratlttv
oondlUoB. Eero end calibrate th* Instrument
aooordlag to the manufaetunrt procedures
using, respectively, nitrogen tad the calibre.
1-10-78
-------
B-19
121:04200 FEDERAL REGULATIONS
fllmb flflmmai
•»>—W»..tM— Ht ta
(MMs Ad IMT IHflra'fffl
OMiMt. Calculate th. oonosntretton at carbo*
•quuIoB 10-1
Cfe0.u.i-ocneenUaUon of CO la stack, ppm by votauo (dry biatQ.
CfcoND1R-ecmeentratIon of CO mcacurad by NDIB analyMf, ppm by volume (dry
fco,-volum; fraction of COi In sample, Lo, percent COi from Orsat i
divided by 100.
(39FR13776. April 17.1974)
10. WWtoffropJkf. Analyser mitraotioo Book. IHn. ,
1(U MeXlror.mak.ThelDt«rUebMDIR-cX> ApplUnea Oo. Tvohntel Pradaoto «-
AnalfMr. Frwented at llth kfethodi «taton.Plttaburgh.Pa.
Onafweace oa Air Pollution. UntTtnitr 10.4 •fedtU ailA, SIM. and 41IA Infnrot
or California, BuMity. Calif, Aprtt 1. Analrun. Mekmam ttitrananti. IM.
10TC. nxfcW.... inctruettani ifJB-B.
104 Jaeoba, H. B, et aL. OoaUnuoui Deter- tea. Calif. Oetobar IOOT.
mlnatton of drbon Uonoxlde and By- 104 Continuous CO Ifoaltortnf _. .
dnearboai la Air by a ilodlBed Infra. Modal AMU. mterteoh Oorp7l>rlneeton.
nd AnaliHT. J. Air PoIlutloB Control If J. ^^
AMoetatlon. •(» :110-114. Aarut IBM. 104 DMOB Zfttnrtd Oat tutjwm. .
104 MBA UBA Infrmd Oai and UquM Corp.. Bonomrta. Wort VtrHaU.
A. Performance aptelfoatltnu far HDIM Carbon Jttmaxhte Anutfun.
Output (minimum) _ 0-10mV.
UiBimam deteotable Moiltmtjr . 80 ppm.
HIM Ume. 90 peroent (maximum) 80 seconds.
Fall time. 00 peroent (maximum) ._... SOseoontfs.
Zero drift (maslmum) ........._ 10% In • heun.
Span drift (maximum).....-............... 10% InOhoun.
Precision (minimum) ±9% of full seal*.
None (maximum) ± 1% of full seals.
Unearltr (maximum deviation).—... . •% of full scale.
laterfinno* rejection ratio OOr-1000 to 1. BiO—600 to 1.
Environment Reporter
-------
3-20
STATIONARY SOURCES
S-IM
121:0421
B. Defnltlmu of Ptr/pnMui tpecf/ka)-
lira*.
Jtasov—The minimum ind muUmuu
mrunrement llmlU.
Ovlpal—metrical slgwl wfcMi U proonr-
- . . . . in,,,,,.
S.I A let talk
sterner—To
alntalnab-
Uenitl to the measurement: Intended I
Mellon to mdout or ffr— The
smallest (mount of Input concentration that
can be deleeltd at Uw concentration ap-
accuracy— The degree of agreement be-
tween a meuured value and the truo value:
uiually expressed ai ± percent of full tcato.
Time to 10 pcmnt response— The Umt In-
terval from a etep change In the Input con-
centration at UM Initrument Inlet to a read-
Inf of M> percent of the ultimate recorded
concentration.
JMsa Tint (M percent)— The Interval be-
tween Initial mponae time and time to 90
percent reiponu after a step Incnaea In the
inlet concentration.
fall Time (M percent)— Tht Intervel be-
tween Initial mponee time and time to 90
percent naponeo after a itep decreaM In the
Inlet concentration.
Zero l»rl/i— The change In Initrument out-
put over a etated time period, usually 34
noun, of unadjusted continuous operation
when the Input concentration U zero: usually
expressed aa percent full eeala.
Span Drijt— The chance In Instrument out-
put over a elated time period, usually M
houn, of unadjusted continuous operation
when the Input concentration Is a itated
upscale value; uiually eipnued a* percent
full scale.
PreeMoii— The degree of agreement be-
tween repeated measurements of the same
concentration, expressed ae the average de-
viation of the single results from the mean.
Nolle— Spontaneous deviations from a
mean output not caused by Input concen-
tration changes.
Linearity— The maximum deviation to-
tween an actual Instrument reading and the
raiding predicted by a straight line drawn
between upper and lower calibration points.
METHOD II— DrmUDtATtOlf OF HTMOOCM BWf
rroi iHisstoHs raOM annoiuaT souscxs
1. Principle and applicability.
I.I Principle. Hydrogen milfldi (RJB) U
collected from the source In a series of midget
Implngrrs and reacted with alkaline cad-
mium hydroxide |Cd(OH).| to form cad-
mium sulAde (CdS). The precipitated CdS
Is then dissolved In hydrochloric sold and
absorbed In a known volume of Iodine solu-
tion. The iodine consumed la a measure of
the HjB content of the gas An Implnger con.
talnlni! hydrogen peroxide Is Included to re-
more :-O, as on Interfering species
1 3 Applicability. This method Is applica-
ble for the determination of hydrogen sul-
nde emissions from stationary sources only
when specified by the test procedures for
determining compliance with the new source
performance standards
3. Apparatus.
2.1 Sampling train
1 I.I Sampling line— 8- to 7-mrn |'4-lncb)
Teflon * tubing to connect sampling train to
aamplliiR valve, with provisions for healing
to prevent condensation A pressure reduc-
ing TAlie prior to the Teflon sampling line
may be required depending on sampling
stream pressure.
2 1 2 Impingtrt— Five midget Implngen.
each with 30-nil capacity, or equivalent.
earning solution at • constant temperature.
•.1.4 Silica f«l dryfno tub*—To protect
puti f and dry gas meter.
a14 Weed/a twin*, or evutoefmt-OtaJnleas
steel or other corraaloa realatent material, to
aa just gas flow me.
S.i 0 Pump—lM* urn. diaphragm type, or
equivalent, to transport gas. (Not required
If sampling stream under positive pressure.)
S.I.T Dry got meter—Sufficiently accurate
to measure sample volume to within I per-
cent.
3.1» Halt meler—Botameur. or equivalent,
to measure a flow rat* of 0 to 3 liters per
minute (0.1 ff/mln).
1.1.0 Graduate* cylinder—35 ml.
3.1.10 fiaroBMler—To measure atmospheric
pressure within *M mm (0.1 In.) Hg.
93 Cample JUcotwry.
3.3.1 Sample container—800-ml glass-stop-
pered Iodine flask.
3.3.3 Jtpelfe—oO-ml volumetric type.
3.2.3 Btakcri> ago ml.
9.3.4 Wesk bottle Olaee
3J.1 nose—500-ml glass-stoppered
> Mention of trade names or specific prod-
ucts don not constitute endonoment by the
environmental Protection Agency.
3.3.3 Burette—One M ml.
9 3 3 flask—136-ml conical.
8. Reagent*.
8 1 Sampling.
8.1.1 Abmrting solution—Cadmium hy-
droxide (Cd(OH).l— Mix 4.8 g cadmium sul-
fate hydrate (» CtaOJOJO) and 0* g of
sodium hydroxide (NaOH) in 1 liter of dis-
tilled water (H.O). Mix well.
Wote: The cadmium hydroxide formed In
this mixture will precipitate as a white sus-
pension Therefore, this solution must be
thoroughly mixed before using to ensure an
even distribution of the cadmium hydroxide.
3.13 Hydrogen peroxide. I percent—Dilute
SO percent hydrogen peroxide to 3 percent
aa needed Prepare fresh dally:
8.3 Sample recovery.
3J.l Hydrochloric aeid solution (HCI). 10
percent ay teefont—Ml* 230 ml of concen-
trated HCI (specific gravity 1.19) and 770 ml
of distilled HjO.
3.2.2 lodttie Mlutlen. oj M—Dissolve 34 g
potassium Iodide (Kl) In 80 ml of distilled
H.O In a l-liur graduated cylinder. Weigh
13.7 B of reaubllmed Iodine (I,) Into a weigh-
ing bottle and add to the potassium Iodide
solution. Shske the mixture until the Iodine
ls completely dissolved. Slowly dilute the so-
lution to 1 liter with distilled H.O. with
swirling, niter the solution. If cloudy, and
store In a brown flats-stoppered bottle.
3.33 Standard todlne solution. OOI H—Di-
lute 100 ml of the 0.1 M Iodine solution In a
volumetric flask to I liter with distilled
water
Standardize dally as folKiws: Pipette 35 ml
of the 0 01 H Iodine solution Into a ISS-ml
conical flask. Titrate with standard 0.01 M
thlosulfate solution (see paragraph 333) un-
til the solution U a light yellow. Add a few
drops of the starch solution and continue
titrating until the blue color Just disap-
pears Prom the results of this tltratlon. cal-
culate the exact normality ol the lodl-ie
solution (see paragraph B.I).
3.34 Dill Ittrd. defended Baler.
3 3 Analytii.
3 3 I Sodium fliloral/afe solution, standard
OJ H—rat each liter of solution, dissolve
34 8 g of sodium thlosulfate (NA.Sp. 8H.O)
In distilled water and add 0 01 g of anhydrous
sodium carbonate (NaOO,) and 0.4 ml of
chloroform (CHCI.) to' atablllze. Mix thor-
oughly by shaking or by aerating with nitro-
gen for approximately 15 minutes, and store
In a glass-stoppered glass bottle.
Standardize frequently as follows: Weigh
Into a MO-ml volumetric flask about 3 g of
potsulum dlchromato (ftv.Cr.O,) weighed
to Uie nearest milligram and dilute to the
MO-ml mark with distilled H,O Use dl-
chromato which has been crystallised from
distilled water and even-dried at liS'O to
IBB'O (tWP to aWF). Dissolve sppruxl-
matelyagof potassium Iodide (KI) In 80 ml
of distilled water In a grsas-stoppered. 600-ml
conical flask, then add S ml of 30-percent
hydrochloric add eoluttoa. Pipette 60 ml of
the dtebromate solution Into this mixture.
Gently swM the solution once and allow It
to aland In the dark for ft minutes. Dilute
the solution with 100 to 300 ml of distilled
water, washing down the aides of the flask
with part of the water. Bwlrl the solution
slowly and titrate with Uw ihimuitaie solu-
tion until the solution to light yellow. Add
• ml of starch solution and continue with a
alow tllratlon with the thlosulfate until the
bright blue color has disappeared and only
the pale green color of the chromlo ton re-
mains. Pram this tltratton, calculate the ex-
act normality of the eodlum thlosulfate solu-
tion (set paragraph 8.3).
|J9IR 13776. April 17. I974|
8.3.3 Sodium tolorm/atesoJ«Mo», standard
041 N-Plpetto 100 ml of the standard 0.1 M
thlosulfate solution Into a volumetric flask
and dilute to one liter with distilled water.
Starch Indicator *gfuNon_6uspend
ml of distilled water, and tot stand 1 hour.
Reutralls* the alkali with concentrated hy-
drochloric acid, using an Indicator paper
similar to Alkacld test ribbon, then add a ml
of glacial acetic add as a preservative.
Test for decomposition by titrating 4 ml of
atareh solution In 300 ml of distilled water
with 0.01 * Iodine solution. If more than 4
drops of the 0.01 H Iodine solution are re-
quired to obtain the blue color, make up a
fresh starch solution.
4. PfOCCdlaTsl.
4.1 Ssmplua.
4.1.1 Assemble the sampling train as shown
In Figure 11-1. connecting the flve midget
Implnger* In series. Place 18 ml of 8 percent
hydrogen peroxide in the flrst Implnger. Place
U ml of the absorbing solution m each of
the next three Implngen, leaving the fifth
dry. Place crushed lee around the Implngen.
Add more ice during the run to keep tbe
teraperaturo of the gases leaving t&o last
Implnger at about 30'C (70*F). or lees.
4.1J Purge the connecting line bttweeu
the sampling valve and the flrst Implnger.
Connect the sample line to the train. Beeord
the Initial readme on the dry gas meter M
shown In Table 11-1.
10 g of soluble starch in 100 ml of dlstllitd
water end add IB g of potassium hydroxide
peltate. Stir until dissolved, dilute with BOO
TASUI ll-l.—field data
Location Comments:
Date
Operator .. ....
Barometric pressure..
_ OM volume Bolameler
Clock Ihrouith soUlnc. Lpa
Hot* mtUMV.). (euHe kei
Men CeaUi per mlnnle)
[Sec. 60.85(011
17
-------
B-21
121:0422
FEDERAL REGULATIONS
to us men per
UNI
minute («M elm).
atm and raOOrd CD Tabl* 11-4.
CIA OanUnu* sampling a minimum of IB
mmnlM. If UM yellow color at cadmium sul-
•d* to visible tn UM third Implngtr. analysis
should oonnrm that UM app
8. CslmiofMM.
1.1
11-1
i exceeded. At UM end of the sample
time, dose UM flow control varw and read
UM Anal meter volume and temperature.
444 DbMtnnset the Implnger train from
tne sampling line. Purge the train with dean
ambient air for U minutes to ensure that all
Hji is removed from the hydrogen peroxide.
(J9IRI3776. April IT. 1974)
when:
•quktlon 11-a
4JJ
"Pt»
4J.1 npette w ml of 0.01 » lodliM solution
Into a aJO-ral braker. Add M ml of 10 percent
BOI to Wi* solution. Mi well.
4JM 1/Uckrd UM content* of UM hydrogen
peroxide Imping*. Carefully transTri ttit con-
tent* of Uw remaining lour Implngcr* to a
IT-wriiht of X,Cr,a mod. g.
Vr- volume of NaAd, untS, nL
fVr-Donn«IHy of itandwd UiiMulfate MluUon, req/llter.
a.M-eoovendaa factor
(• eq fr/mole K,CrM) (1.000 mM)
*™ ' ' "' (10 alii
4AI BUM th* four absorbing Implngers
Md connecting gUsswars with ton* porUoot
el UM addlned Iodine lotoUon. VM UK en-
tlr» 100 ml at •adWed tadlnt for thU pur-
POM. Xmrntdtetely «fter pourloi UM Rddlntd
iadln* Into in Implagtr. itopptr It cod dwk*
far • law momentt bttora tnunterrlni UM
rlnw to UM todlnt fluk. Do not tnnifer Mir
iliut porUon from on* Implnger to knothci:
tnufn it dlneUr ta th* lodln* fluk. One*
•eUUwd BdUm loluUon hi* ham pound Into
•nf itaHwin wnlmlnlng Mdmlum mind*
Mmpw. Ui* container muit he tlgbUy stop-
pered •* ill Umei except when iddlnt mar*
MluUon, ud thl* must be don* u qulekly
Wd einfullj H poulMe. After •adlnf inf
•ddlfted lodUM MluUon to UM Iodine flirt.
•Dow • lew minute* for itoorptwn of the RJB
mto UM Iadln* belor* *ddln| 107 further
.3 g AiOrWinolo) (10 aliquot factor).
8.8 Dry gat selum*. Correct the sample volume measured by the dry eas
standard conditions |21*C(70*F)| and 7fl6 mm (29.93 Inches) HgThy usto?equal
V.....-V
meter to
wherei
oqoMloB 11-3
K.,u-volume at standard conditions of gas sample through the dry gas meter,
standard Uteri (ecf).
-volume of gas sample through the dry gae meter (meter conditions), liters
(eu. ft.).
r.u-abiolute temperature at itandard eondlUaiu, 9M*K
n,-aven«e dry gu meter temperature, »K pSf.
P^-barometrle prcnure at the orlflee meter, mm Hg On. Bg).
14 ?Ci"'f*?'ute ?1%yn JS*.8*""11*^ condition* 7flO mm Hg (39.99 In. Bg).
8.4 OnMn^oJMn •/ Ht8.—Caleulnle the eonecntratton of B»8 to ttu gu itroam t4
etaadard eouditlont nalng equation ll-4t »-—.»«. ••««• •.
4J.4 PMlow tbl* rlnw with two more itnoM
tmng dUUUed water. Add the dMIUed water
runei to the Iodine flask. Stopper UM Ha*k
and shake well. Allow about M minutes for
absorption of too BJB Into UM Iodine, then
eonpiew the analyiis Utrauon.
Csstlon: Keep the lodln* fluk itoppered
except when adding simple or utrant.
13* Prepare a blank In » Iodine fluk
using 45 ml of the absorbing solution. W ml
of Ml M tadln* soluUon. and M ml of 10
percent HOI. Stopper the Bask, shake well
and analyn with UM samples.
«J Awlyrli.
Hate: nil analysis tttraUon Should be
conducted at the sampling location in order
to prevent MM of Iodine from the sample.
TltraUon should never be made In direct
where f metric units):
Cn,i-eonc*ntntlon of 1IJB at standard eoniUUonti, mg/dsem
X-oonv«nion factor- 17.0X 10*
(I.OCO mg/g)
(1,000 ml/l)(an,S eq/molel
ViBVolume of standard Iodine solution, ml.
AriBnnrniallty of standard Iodine solution, g-cq/lllor.
Vr=vi.luinc of standard radium thlomilfnte solution, ml
Arr-nonimllly of standard radium thlomilfate solution, g-eq/ntez.
V-.^^drj' giw volume at standard cunditluns liter*.
where (English unite):
4.3.1 Titrate the eolutton In the flask with
0.01 H sodium thlosuUate sduUon until the
solution la light yellow. Add 4 ml of the
starch Indicator aoliiUon and continue
Utratlng unUl the blue color Just disappears.
433 Tttrile the blink* In UM same man-
ner is the simples.
(391-R 1)776. April 17. 19741
(1.000 l/mjl
In;
|39I'R 13776. April 17. I974|
6. Ae/errMes.
rogcn Sulflde, Ammonlaral Cadmium Chloride Method.
anual on Dtaposal of Iteflanr Wiurtos. Vert V- Hamiillnc
n. ^-^TM"*^ A^erieaTRliolleum Insu'lute!
i.*i? , "!*>.iv" i!rthod!f'w nrtwnitanUoa of Hydrogen SuMde and MereapUn Sulfur
N™ WM-05.T905. PfoeBWWI A«ocl»Uon,*l\,l«, OkUhnm.. N«JPA
Envnonmenl Repoiler
(Sec. 60.BS(*||
-------
APPENDIX C
SOURCE SAMPLING FIELD DATA SHEETS
-------
C-l
OI01GI D. CLAYTOH & ASSOCIATES
BIHAD8T GAS VILOCITY AID FLOW 1ATI
PROJBCT_ Ford Motor Company
Sampling
Tett Ho.
CRBW RJP. CMS
UOKB o«n.ery~Tt"~~ mi»^imM.
Station Scrubber Inlet Date 7/30/74
Prelim.Traverse-1 Pitot Tuba Ho.
Tim* 10:05
.Manometer Ho.
Sampling
Point
B-l
B-2
B-3
B-4
B-5
B-6
B-7
B-8
B-9
B-10
Velocity
Pressure
(In.H20)
0.89
1
1.05
1.2
1.2
1.3
1.4
1.4
1.5
1.2
DB
Temp
CP)
80
80
80
80
80
80
80
80
80
80
Uneorreeted
Velocity
(Ft/sec)
63.6
67.4
69.1
73.8
73.8
76.8
79.7
79.7
82.5
73.8
Sampling
Point
B-ll
B-12
B-13
B-14
B-15
B-16
B-17
B-18
B-19
B-20
Velocity
Pressure
(In.H20)
1.2
1.3
1.5
1.3
1.5
1.5
1.6
1.6
1.5
1.4
DB
Temp
CF)
80
80
80
80
80
80
80
80
80
80
Uneorreeted
Velocity
(Ft/sec)
73.8
76.8
82.5
76.8
82.5
82.5
85.2
85.2
82.5
79.7
Stack Net Bulb Temperature, (°F)
A. Barometric Pressure, (In.Bg)
B. Static Pressure of Stack Gases, (In.HjO)^
C. Pitot Tube Correction Factor
Stack Dimensions
66" I.D.
29.85
-3.7
(0.84)
(1.0)
29.58
D. Specific Gravity of Stack Gases Relative to Dry Air
B. Absolute Pressure of Stack Gases • A + (B/13.6),(In.Hg)
F. Average Uneorreeted Velocity, (ft/see) 77.4 or 60 * F,(ft/min) 4644
Corrected Velocity - F *
G.
^•^'.
-------
C-2
GEORGE D. CLAYTON & ASSOCIATES
EXHAUST GAS VELOCITY AND FLOW RATE
PROJECT Ford Motor Company
Sampling Station
"T.
CREW
Date 7-30- M
RJP. GMS
Time 10:05
Teat Ho. Prelim. Traverse-KCont. )Pitoc 'lube No.
Manometer No.
Sampling
Point
T-l
T-2
T-3
T-4
T-5
T-6
T-7
T-8
T-9
T-10
Velocity
Pressure
(In.H20)
1.2
1.0
1.2
1.1
1.2
1.3
1.3
1.4
1.4
1.3
DB
Temp
(°F)
80
80
80
80
80
80
80
80
80
80
Oneorreeted
Velocity
(Ft/sec)
73.8
67.4
73.8
70.7
73.8
76.8
76.8
79.7
79.7
76.8
Sampling
Point
T-ll
T-12
T-13
T-14
T-15
T-16
T-17
T-18
T-19
T-20
Velocity
Pressure
(ln.H20)
1.2
1.4
1.4
1.3
1.5
1.6
1.6
1.4
1.5
1.2
DB
Temp
<°F)
80
80
80
80
80
80
80
80
80
80
Uncorrected
Velocity
(Ft/sec)
73.8
79.7
79.7
76.8
82.5
85.2
85.2
79.7
82.5
73.8
Stack Wet Bulb Temperature, (°F)
A. Barometric Pressure, (In.Hg)
B. Static Pressure of Stack Gases, (In.H2<>)
C. Pitot Tube Correction Factor
Stack Dimensions
D. Specific Gravity of Stack Gases Relative to Dry Air
B. Absolute Pressure of Stack Gases - A -I- (B/13.6), (In.Hg)
F. Average Dncorrected Velocity, (ft/sec) or 60 * F,(ft/min)
G. Corrected Velocity • F * C
H. Area of Stack, (ft2)
^97*
VT
92 ... 1.00 '
(ft/min)
I. Actual Gas Flow Rate - G * H, (ACFM)
J. Average Stack Temperature, (°F)
K. Standard Gas Flow Rate • I
where TBt& m standard temperature,
<— >.
F
GDC-2
-------
C-3
GBOEGB D. CLAYTOH & AS8OCXATIS
BXHADST 6A8 VELOCITY AHD FLOW RATE
PlOJBCt Ford Motor Company
CRBW
RJP. RJG
Sampling Station
Date
1-11.7S
Time lit 10
Teat Ho. Prelim.Traverse-2 Pitot Tube Ho. 18 Manometer No.
Sampling
Point
B-l
B-2
B-3
B-4
B-5
B-6
B-7
B-8
B-9
B-10
B.ll
B-12
Velocity
Pressure
(In.H20)
1.81
2.06
1.56
1.01
0.96
1.19
1.66
1.61
1.51
1.56
1.66
1.71
DB
leap
CF)
58
58
58
58
58
58
58
58
58
58
58
58
Uncorreeted
Velocity
(Ft/aec)
88.8
94.7
82.4
66.3
64.7
72.0
85.0
83.7
81.1
82.4
85.0
86.3
Sampling
Point
B-13
B-14
B-15
B-16
B-17
B-18
Velocity
Preaaure
(Zn.l20)
1.76
1.86
1.61
1.36
1.16
1.16
DB
Temp
CF)
58
58
58
58
58
58
Uncorrected
Velocity
(Ft/aec)
87.6
90.0
83.7
77.0
71.1
71.1
Stack Wet Bulb Temperature, (°F)
A. Barometric Pressure, (In.Hg)
B. Static Pressure of Stack Gases, (In.H20)
C. Pitot Tube Correction Factor
Stack Dimensions
66" I.D.
28.9
-3.7
0.84
1.0
28.63
D. Specific Gravity of Stack Gases Relative to Dry Air
B. Absolute Pressure of Stack Gases - A •»• (B/13.6) , (In.Hg)
F. Average Uncorreeted Velocity, (ft/sec) 78.4 or 60 * F,(ft/min) 4706
Corrected Velocity • F * C*/29'
G.
92
E D
H. Area of Stack, (ft2)
I. Actual Gas Flow Rate • G * H, (ACFM)
J. Average Stack Temperature, (°F)
, (ft/min)
4041
23.8
34
K.
Standard Gas Flow Rate -
where T8t(j • standard temperature,
GDC-2
68
98366
°F Dry SCFM
98100
-------
C-4
GEPRGB D. CLAYTOH & ASSOCIATES
EXHAUST GAS VELOCITY AND PLOW RATE
PROJECT Ford Motor Company
I!
CREW RJP. RJG
Sampllog Station Scrubber Inlet Date 1-11-75 Time 11;10
Test Ho.Prelim. TMMBrae-2(Pans) Pltot Tube Ho. 18 Manometer Ho. MA
Sampling
Point
T-l
T-2
T-3
T-4
T-5
T-6
T-7
T-8
T-9
T-10
T-ll
T-12
Velocity
Pressure
(In.H20)
2.18
2.08
1.28
1.08
1.28
1.38
1.43
1.38
1.53
1.38
1.48
1.48
DB
Temp
10
10
10
10
10
10
10
10
10
10
10
10
Uncorrected
Velocity
(Pt/sec)
92.8
90.7
71.1
65.3
71.1
73.9
75.2
73.9
77.8
73.9
76.5
76.5
Sampling
Point
T-13
T-14
T-15
T-16
T-17
T-18
Velocity
Pressure
(In.H20)
1.48
1.68
1.38
1.38
1.38
1.33
DB
Temp
CP)
10
10
10
10
10
10
Dncorrected
Velocity
(Pt/sec)
76.5
81.5
73.9
73.9
73.9
72.5
Stack Wet Bulb Temperature, <°P)
A. Barometric Pressure, (In.Eg)
B. Static Pressure of Stack Gases, (In.H20)
C. Pltot Tube Correction Factor
Stack Dimensions
D. Specific Gravity of Stack Gases Relative to Dry Air
B. Absolute Pressure of Stack Gases - A + (B/13.6),(In.Hg)
P. Average Uncorrected Velocity, (ft/sec) or 60 * P,(ft/mln)
G. Corrected Velocity - F * C./^J
H. Area of Stack, (ft2)
* lj££- , (ft/mln)
I. Actual Gas Flow Rate - G * H, (ACPM)
J. Average Stack Temperature, (°F)
K. Standard Gas Plow Rate • I
where T8td " standard temperature,
-
°P
GDC-2
-------
C-5
GBOROI D. CLAYTOH & ASSOCIATES
EXHAUST OA8 VELOCITY AHD PLOW RATE
PROJECT Pord Motor Company CREW RJP. MRP
coke Betcerv A
Sampling Station Scrubber Inlet Pate 1-16-75
Test Ho.Pr«ll«. Tr«v«ra«-3 Pltot Tube Ho. 18 Manometer Ho.
Time 14iOO
Sampling
Point
B-l
B-2
B-3
B-4
B-5
B-6
B-7
B-8
B-9
B-10
B-ll
B-12
Velocity
Pressure
(In.H20)
1.30
1.30
1.10
1.25
1.10
1.50
1.45
1.25
1.30
1.40
1.57
1.50
DB
leap
CF)
60
60
60
60
60
60
60
60
60
60
60
60
Dncorrected
Velocity
(Ft/sec)
75.4
75.4
69.4
73.9
69.4
81.0
79.6
73.9
75.4
78.2
82.9
81.0
Sampling
Point
B-13
B-l 4
B-15
B-16
B-17
B-18
Velocity
Pressure
(In.H20)
1.65
1.70
1.80
1.50
1.40
1.50
DB
leap
CF)
60
60
60
60
60
60
Uncorrected
Velocity
(Ft/sec)
84.9
86.2
88.7
81.0
78.2
81.0
Stack Wet Bulb Temperature, (°P)
A. Barometric Pressure, (In.Hg)
B. Static Pressure of Stack Gases, (In.H20)
C. Pltot Tube Correction Factor
Stack Dimensions
66" I.D,
30.0
-4.2
0.84
1.0
29.69
D. Specific Gravity of Stack Gases Relative to Dry Air
B. Absolute Pressure of Stack Gases - A + (B/13.6),(In.Hg)
P. Average Dncorrected Velocity, (ft/see) 78.7 or 60 * P,(ft/mln) 4724
G. Corrected Velocity • P * C./*9'92 * -^-^ ', (ft/mln) 3983
H. Area of Stack, (ft2)
23.76
I. Actual Gas Flow Rate - G * H, (ACPM)
J. Average Stack Temperature, (°F)
K. Standard Gas Plow Rate • I
94807
wbere T8td • standard temperature,.
68
99347
°F Dry SCPM
99000
GDC-2
-------
C-6
GBORGB D. CLAYTOH & ASSOCIATES
EXHAUST GAS VELOCITY AHD FLOW KATE
PROJECT Ford Motor Company CREW RJP, MRP
Sampling Static*. SlrSblt^fSIet Data 1-16-75
Teat Ho. PreUm.rraverse-3(Oant)f 1 tot Tube Ho. 18 Manometer No.
Time 14:00
Sampling
Point
T-l
T-2
T-3
T-4
T-5
T-6
T-7
T-8
T-9
T-10
T-ll
T-12
Velocity
Pressure
(In.R20)
2.70
1.80
1.20
1.30
1.60
1.50
1.50
1.50
1.50
1.40
1.45
1.40
DB
Temp
CF)
20
20
20
20
20
20
20
20
20
20
20
20
Oneorreeted
Velocity
(Ft/sec)
104
85.2
69.6
72.4
80.4
77.8
77.8
77.8
77.8
75.2
76.5
75.2
Sampling
Point
T-13
T-14
T-15
T-16
T-17
T-18
Velocity
Pressure
(In.H20)
1.70
1.50
1.50
1.50
1.50
1.40
DB
Temp
CF)
20
20
20
20
20
20
Oncorrectedj
Velocity
(Ft/sec)
82.8
77.8
77.8
77.8
77.8
75.2
Stack Wet Bulb Temperature, (°F)
A. Barometric Pressure, (In.Hg)
B. Static Pressure of Stack Gases,
C. Pitot Tube Correction Factor
Stack Dimensions
D. Specific Gravity of Stack Gases Relative to Dry Air _
B. Absolute Pressure of Stack Gases - A -f (B/13. 6) , (In.Hg) _
F. Average Dncorrected Velocity, (ft/sec) _ or 60 * F, (ft/mln)
G. Corrected Velocity - F *
H. Area of Stack, (ft2)
1^2
E
1.00 '
(ft/min)
I. Actual Gas Flow Rate - G * H, (ACFM)
J. Average Stack Temperature, (°F)
K. Standard Gas Flow Rate - I
where T8td • standard temperature,
GDC-2
-------
C-7
GEOEOB D. CLAYTOB & ASSOCXATIS
IXBAD8T 648 VELOCITT AND FLOW IATI
PtOJICT Ford Motor Company
CRIH ROM
Data 2-6-75
Time 15:00
Sampling Station Scrubber Inlet
Teat Ho. Prelim.Traverae-4 P|.tot Tuba Ho. 18 Manama tar Ho..
Sampling
Point
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Velocity
Preaaure
(In.H20)
0.60
1.0
0.95
0.90
0.80
0.80
0.75
0.72
0.78
0.78
0.80
0.82
0.87
0.87
0.78
DB
Temp
CF)
36*
36*
36*
36*
36*
36*
36*
36*
36*
36*
36*
36*
36*
36*
36*
Dneorracted
Velocity
(Ft/aec)
50.0
64.6
63.0
61.3
57.8
57.8
55.9
54.8
57.0
57.0
57.8
58.5
60.2
60.2
57.0
Sampling
Point
16
17
18
*Average
Velocity
Preeaure
(In.H20)
0.74
0.68
0.68
of ambient
DB
Temp
C»)
36*
36*
36*
Uncorr acted
Velocity
(Pt/iec)
55.6
53.3
53.3
tempera turea
Stack Wet Bulb Temperature, (°F)
A. Barometric Pressure, (Zn.Rg)
B. Static Preasure of Stack Gases, (In.R20)
C. Pltot Tube Correction Factor
D.
B.
F.
G.
Stack Dimension*
66" I.D.
29.28
-3.0
0.84
(1.0)
29.06
Specific Gravity of Stack Gases Relative to Dry Air
Absolute Pressure of Stack Gases - A + (B/13. 6) , (In.Rg)
Average Uncorreeted Velocity, (ft/sec) 57.5 or 60 * F,(ft/min) 3450
Corrected Velocity - F * C./29'
92
(ft/min)
2941
B. Area of Stack, (ft2)
I. Actual Gaa Flow Rate • G * H, (ACFM)
J. Average Stack Temperature, (°F)
K. Standard Gas Flow Rate -
23.8
69873
where T8td • standard temperature
( Jf 4- 460 )* f2T79Tj»
perature, 68 _F
36
(SCFM)
72243
(Dry SCFM) 71882
GDC-2
-------
C-8
GEORGE D. CLAYTON & ASSOCIATES
EXHAUST GAS VELOCITY AND PLOD RATE
PROJECT Ford Motor Company
CREW
RJG
tone uactery A
Sampling Station Scrubber Inlet Date 2-12-75
Teat Ho Jrellm.Travarae-5 Pltot Tube Ho. 18 Manometer Ho.
Time 14:15
Sampling
Point
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Velocity
Preaaure
(In.H20)
0.45
0.77
0.90
0.79
0.75
0.80
0.83
0.85
0.78
0.72
0.72
0.72
0.75
0.72
0.68
OB
Temp
<"F)
45
45
45
45
45
45
45
45
45
45
45
45
45
45
45
Uneorreeted
Velocity
(Pt/aac)
43.7
57.2
61.8
57.9
56.4
58.3
59.4 '
60.1
57.6
55.3
55.3
55.3
56.4
55.3
53.7
Sampling
Point
16
17
18
Velocity
Preaaure
(In.H20)
0.80
0.85
0.68
DB
Temp
CP)
45
45
45
Dncorrected
Velocity
(Ft/sec)
58.3
60.1
53.7
Stack Wet Bulb Temperature, (°F)
A. Barometric Pressure, (In.Hg)
B.
C.
D.
E.
P.
Stack Dimensions
Static Preaaure of Stack Gases, (In.H20)
Pltot Tube Correction Pactor
66-1.D.
29.52
-3.0
0.84
(1.0)
Specific Gravity of Stack Gases Relative to Dry Air
Absolute Pressure of Stack Gases - A + (B/13.6),(In.Hg)
Average Uneorreeted Velocity, (ft/aec) 56.4 or 60 * F.(ft/mtn) 3386
29.30
G. Corrected Velocity - F * c A9.92 « j^JW '^ (£t/mln)
v E D
H. Area of Stack, (ft2)
I. Actual Gas Plow Rate - G * H, (ACPM)
2874
23.8
68281
J. Average Stack Temperature, (°F)
K. Standard Gas Flow Rate • I
45
where TBt
-------
C-9
GEORGE D. CLAYTON & ASSOCIATES
EXHAUST GAS VELOCITY AHD FLOW 1ATE
PROJECT
Sampling
Test Ho.
Ford Motor Company
Station
coke Battery A
Scrubber Inlet
Prelim. Traverae-6 Pi tot
CRBV
Data
Tuba Ho.
RGK, GEH
4-9-75
Time
12:17-12:36
10 Manometer Ho.
Sampling
Point
T-l
T-2
T-3
T-4
T-5
T-6
T-7
T-8
T-9
T-10
T-ll
T-12
CL
Velocity
Pressure
(In.H20)
0.68
1.2
1.5
1.4
1.4
1.3
1.3
1.3
1.4
1.3
1.4
1.1
1.3
DB
Tamp
CF)
65
65
65
65
65
65
65
65
65
65
65
65
Uneorraoted
Velocity
(Ft/sec)
54.8
72.8
81.4
78.6
78.6
75.8
75.8
75.8
78.6
75.8
78.6
69.7
75.8
Sampling
Point
B-l
B-2
B-3
B-4
B-5
B-6
B-7
B-8
B-9
B-10
B-ll
B-12
CL
•
Velocity
Pressure
(In.H20)
0.92
1.1
1.3
1.4
1.3
1.4
1.5
1.5
1.7
1.7
1.7
1.6
1.4
DB
Temp
CF)
65
65
65
65
65
65
65
65
65
65
65
65
Uncorrected
Velocity
(Ft/sec)
63.7
69.7
75.8
78.6
75.8
78.6
81.4
81.4
86.6
86.6
86.6
84.0
78.6
Stack Wet Bulb Temperature, (°F)
A. Barometric Pressure, (In.Hg)
B. Static Pressure of Stack Gases, (In.H20)
C. Pitot Tube Correction Factor
Stack Dimensions
66" I.D.
29.40
-5.8
0.836
1.0
28.97
D. Specific Gravity of Stack Gases Relative to Dry Air
B. Absolute Pressure of Stack Gases • A + (B/13.6),(In.Hg)
F. Average Uncorrected Velocity, (ft/sec) 76.9 or 60 * F.(ft/min) 4613
G. Corrected Velocity - F * C./29'92 * i^°- ', (fe/min) 3919
E. Area of Stack, (ft*)
23.8
I. Actual Gas Flow Rate - G * H, (ACFM)
J. Average Stack Temperature, (°F)
K. Standard Gas Flow Rate • I
93109
65
where TBtd m standard temperature,
68
90668
•F Dry SCFM 90215
GDC-2
-------
C-10
CBORGB D. CLAYTOH 6 ASSOCIATES
EXHAUST GAS VELOCITY AND FLOW RATE
PROJECT^
Sampling
Test No.
Ford Motor Company
S ft ion gggSbiePfnleS Date
Prelim.Traverse-7 Pitot Tube No.
CREW ROE. GBH
4-10-75
10 Manometer No..
Sampling
Point
T-l
T-2
T-3
T-4
T-5
T-6
T-7
T-8
T-9
T-10
T-ll
T-12
CL
Velocity
Pressure
(Xn.H20)
1.0
1.05
1.2
1.3
1.3
1.3
1.3
1.4
1.5
1.5
1.6
1.3
1.3
DB
Temp
CP)
64
64
64
64
64
64
64
64
64
64
64
64
Dneorreeted
Velocity
(Ft/sec)
66.4
68.0
72.7
75.7
75.7
75.7
75.7 '
78.5
81.3
81.3
84.0
75.7
75.7
Sampling
Point
B-l
B-2
B-3
B-4
B-5
B-6
B-7
B-8
B-9
B-10
B-ll
B-12
CL
Velocity
Pressure
(In.H20)
1.4
1.4
1.3
1.6
1.6
1.4
1.3
1.4
1.2
1.3
1.2
1.05
1.6
DB
Temp
<°P>
64
64
64
64
64
64
64
64
64
64
64
64
Uncorreetedl
Velocity
(Ft/sec) j
f
78.5
78.5
75.7
84.0
84.0
78.5
75.7
78.5
72.7
75.7
72.7
68.0
84.0
Stack Wet Bulb Temperature, (°F) Stack Dimensions 66" I.D.
A.
B.
C.
D.
E.
F.
G.
H.
I.
J.
K.
Barometric Pressure, (In.Hg)
Static Pressure of Stack Gases, (In.H20)
Pitot Tube Correcti.on Factor
Specific Gravity of Stack Gases Relative to Dry
Absolute Pressure of Stack Gases - A + (B/13.6),
Average Uncorrected Velocity, (ft/sec) 76.4 or
Corrected Velocity - F * C./29'92 * i^. , (ft/a
Area of Stack, (ft?)
Actual Gas Flow Rate • G * H, (ACFM)
Average Stack Temperature, (°F)
Standard Gas Flow Rate - I */*std + *°°\*/ B \
where Tatd • standard temperature, 68
Air
(In.Hg)
60 * F, (ft/min)
iln)
i, (SCFM)
8F Dry SCFM
29.38
-5.0
0.836
1.0
29.01
4583
3891
23.8
92444
64
90316
89864
GDC-2
-------
C-ll
GB01GB D. CLAYTON & ASSOCIATES
BXBAUST GAS VBLOCZTT AMD FLOW RATI
PROJBCT_
Sampling
Test Ho.
Ford Motor Company
otpr Cempi
Coke. Batci
CRBV RJG
Station jgrSbSSr lifla* Pata 4-11-75
P_ra 1 im.Tra ver.se-8 Pitot Tube Ho.
Tlma 10;45
10
Manometer No,
Sampling
Point
B-l
B-2
B-3
B-4
B-S
B-6
B-7
B-8
B-9
B-10
B-ll
B-12
Velocity
Pressure
(Zn.R20)
0.62
1.10
1.30
1.30
1.40
1.20
1.20
1.10
1.20
1.40
1.30
1.10
DB
Te»p
CP)
70
70
70
70
70
70
70
70
70
70
70
70
Dneorraetad
Velocity
(Pt/iec)
52.6
70.0
76.1
76.1
79.0
73.1
73.1
70.0
73.1
79.0
76.1
70.0
Sampling
Point
T-l
T-2
T-3
T-4
T-5
T-6
T-7
T-8
T-9
T-10
T-ll
T-12
Velocity
Pressure
(In.H20)
0.78
1.30
1.50
1.40
1.30
1.20
1.30
1.20
1.20
1.10
1.10
0.95
DB
Temp
CP)
70
70
70
70
70
70
70
70
70
70
70
70
Uncorrected]
Velocity 1
(Pt/sec) j
1
59.0
76.1
81.8
79.0
76.1
73.1
76.1
73.1
73.1
70.0
70.0
65.1
Stack Vet Bulb Temperature, (°P)
A. Barometric Pressure, (In.Hg)
B. Static Pressure of Stack Gases, (In.R20)
C. Pitot Tube Correction Paetor
Stack Dimensions
66"I.D.
29.6
-4.3
0.842
1.0
29.28
D. Specific Gravity of Stack Gases Relative to Dry Air
B. Absolute Pressure of Stack Gases - A -f (B/13.6),(In.Hg)
P. Average Uncorrected Velocity, (ft/sec) 72.5 or 60 * F,(£t/mtn) 4352
G. Corrected Velocity • P * G^J^-£
H. Area of Stack, (ft2)
92 * iiPJL , (ft/min)
3704
23.8
I. Actual Gas Plow Rate • G * H, (ACPM)
J. Average Stack Temperature, (*P)
R. Standard Gas Plow Rate • I
88001
70
where T8td • standard temperature,
68
85794
°P Dry SCPM 85365
GDC -2
-------
C-12
GEORGE D. CLAYTON & ASSOCIATES
EXHAUST GAS VELOCITY AND FLOW BATE
PROJECT^
Sampling
Test Ho.
Ford Motor Company
CREW
RJG
Station jglSbiSr^nlet Date 4-14-75
Prelim.Traverse-9 Pltot Tuba Ho. 10 Manometer Ho.
Time 15:35
Sampling
Point
B-l
B-2
B-3
B-4
B-5
B-6
B-7
B-8
B-9
B-10
B-ll
B-12
Velocity
Pressure
(In.H20)
0.85
1.15
1.20
1.20
1.20
1.25
1.35
1.40
1.50
1.60
1.35
1.50
DB
Temp
<°F)
62
62
62
62
62
62
62
62
62
62
62
62
Uneorreeted
Velocity
(Ft/aec)
61.1
71.1
72.6
72.6
72.6
74.1
77.0
78.4
81.1
83.8
77.0
81.1
Sampling
Point
T-l
T-2
T-3
T-4
T-5
T-6
T-7
T-8
T-9
T-10
T-ll
T-12
Velocity
Pressure
(In.H20)
0.55
1.15
1.35
1.45
1.45
1.40
1.45
1.40
1.45
1.40
1.30
1.25
DB
Temp
<'F)
62
62
62
62
62
62
62
62
62
62
62
62
Dncorrected]
Velocity
(Ft/sec)
49.1
71.1
77.0
79.8
79.8
78.4
79.8
78.4
79.8
78.4
75.5
74.1
Stack Dimensions
66"I.D.
29.8
-6.0
0.842
Stack Wet Bulb Temperature, (°F)_
A. Barometric Pressure, .(I°«Hg)
B. Static Pressure of Stack Gases, (In.H20)
C. Pitot Tube Correction Factor
D. Specific Gravity of Stack Gases Relative to Dry Air
E. Absolute Pressure of Stack Gases - A + (B/13.6),(In.Hg)
F. Average Uneorreeted Velocity, (ft/sec) 75.2 or 60 * F,(ft/min) 4509
G. Corrected Velocity
1.0
29.36
F *
H. Area of Stack, (ft2)
I. Actual Gas Flow Rate - G * H, (ACFM)
J. Average Stack Temperature, (°F)
K. Standard Gas Flow Rate - I
^*^', (ft/min).
E D
3833
23.8
91066
62
where Tstd • standard temperature,
68
(SCFM)
90388
F
GDC-2
-------
C-13
GB01GI B. CLAYTOH & ASSOCIATES
EXHAUST CAS VELOCITY ABO PLOD RATE
ttOJBCT Ford Motor Company
•••piing Station
CRBif RCM
Bata 7/23/75
12:15-12:30
Test Ho.pj«HaJraverga-10 Pltot Tuba Ho. 10 Manomatar Ho. —
Sampling
Point
T-12
T-ll
T-10
T-9
T-8
T-7
T-6
T-5
T-4
T-3
T-2
T-l
Velocity
Pressure
(In.B20)
0.070
0.090
0.085
0.080
0.080
0.085
0.090
0.085
0.065
0.065
0.075
0.060
BB
Temp
CF)
85
85
85
65
85
85
85
85
85
85
85
85
Dacorrected
Velocity
(Pt/sec)
17.9
20.3
19.7
19.1
19.1
19.7
20.3
19.7
17.3
17.3
18.5
16.6
Sampling
Point
S-12
S-ll
S-10
S-9
S-B
S-7
S-6
S-5
S-4
S-3
S-2
S-l
Velocity
Pressure
(In.H20)
0.065
0.090
0.085
0.085
0.090
0.080
0.070
0.065
0.055
0.060
0.060
0.060
OB
Temp
CP)
85
85
85
85
85
85
85
85
85
85
85
85
Uncorracted
Velocity
(Pt/sec)
17.3
20.3
19.7
19.7
20.3
19.1
17.9
17.3
• 15.,
16.6
16.6
16.6
Stsck Wet Bulb Temperature, (eP) ..
A. Barometric Pressure, (In.Hg)
B. Static Pressure of Stack Gases, (In.H20)
C. Pitot Tube Correction Factor
Stack Dimensions
66" I.D.
29.50
-0.55
0.846
B. Specific Gravity of Stack Gases Relative to Dry Air 1.0
B. Absolute Pressure of Stack Gases • A + (B/13.6), (In.Hg) 29.46
P. Average Uncorrected Velocity, (ft/sec) 18.4 or 60 * F,(ft/min) 1107
G. Corrected Velocity - F * C./*9'92 * ii^P. , (ft/min) 944
H. Area of Stack, (ft2) 23.8
I. Actual Gas Flow Rate - G * H, (ACFM) 22.428
J. Average Stack Temperature, (°P) 55
K. Standard Gas Plow Rate • I *A«td +
\ J + 460
wbere T8£d • standard temperature,
GDC-2 NOTE: Doors' end louvers closed
68
21.394
-------
C-14
GEORGE D. CLAYTON & ASSOCIATES
EXHAUST GAS VELOCITY AND FLOW RATE
PROJECT Ford Motor Company
_ , . " ~~ coke Battery A
Sampling Station Scrubber Outlet
_ CREW RJP. MRP
_Date 1-11-75
Teat Ho. Prelim. Traverse-1 pitot Tube No. 12
Time 09:30-10:00
.Manometer No.
Sampling
Point
NE-1
NE-2
NE-3
NE-4
NE-5
HE -6
HE-7
NK.8
HE. 9
Velocity
Pressure
(In.H20)
0.32
0.42
0.48
0.57
0.48
0.50
0.48
Or55
0.49
DB
Temp
CF)
104
104
104
104
104
104
104
104
104
Dncorrected
Velocity
(Ft/sec)
39.0
44.6
47.7
52.0
47.7
48.7
47.7
51.1
48.2
Sampling
Point
NW-1
NW-2
NW-3
NW-4
NW-5
NW-6
NW-7
NW-8
NW-9
Velocity
Pressure
(In.H20)
0.37
0.47
0.48
0.61
0.60
0.55
0.60
0.52
0.57
DB
Temp
<°F)
105
105
105
105
105
105
105
105
105
Dncorrected]
Velocity |
(Ft/sec)
41.9
47.3
47.8
53,8
53.4
51.1
53.4
49.7
52.0
Stack Wet Bulb Temperature, (°F) — Stack Dimensions 90" I. D.
A.
B.
C.
D.
B.
F.
G.
H.
I.
J.
K.
Barometric Pressure, (In.Hg)
Static Pressure of Stack Gases, (In.H20)
Pltot Tube Correction Factor
Specific Gravity of Stack Gases Relative to Dry Air
Absolute Pressure of Stack Gases - A + (B/13. 6) , (In.Hg)
Average Uncorrected Velocity, (ft/sec) 42.9 or 60 * F,(ft/min)
Corrected Velocity - F * Cv/29.!92 * ^^- , (ft/min)
V E D
Area of Stack, (ft2)
Actual Gas Flow Rate - G * H, (ACFM)
Average Stack Temperature, (°F)
Standard Gas Flow Rate • I */Tstd * \ . / B \ *„,-,.%
where T8td " standard temperature, 68 '°F Dry SCFM
28.9
_
0 Kit.
1.0
28.9
2575
2201
44.2
97237
102
88240
88000
GDC-2
-------
C-15
GBOEGB D. CLAYTOH & ASSOCIATES
IZHAD8T GAS VELOCITY AHD FLOW RATE
PROJECT Ford Mot
8SlcS°SIgKry A
CREW
RJP. MED
Sampling Station Scrubber Pullet Date 1-11-75 Time 09; 30-10; 00
I«it Ho. Prelim. Trs0qrse-!l(!Ctti.)»itat Tub* Ho. 12 Manometer Mo.
Sampling
Point
SE-1
8E-2
8E-3
SE-4
SB -5
BE -6
BE -7
BE -8
SE-9
Velocity
Pressure
(Zn.H20)
0.36
0.40
0.46
0.48
0.48
0.51
0.50
0.50
0.51
DB
Temp
CP)
100
100
100
100
100
100
100
100
100
Dneorreeted
Velocity
(Ft/sec)
41.2
43.4
46.5
47.5
47.5
49.0
48.5
48.5
49.0
Sampling
Point
SW-1
SW-2
Stf-3
SV-4
SV-5
SW-6
SH-7
SW-8
SW-p
Velocity
Pressure
(In.H20)
0.32
0.43
0.48
0.52
0.48
0.50
0.48
0.46
0.48
DB
Temp
CF)
100
100
100
100
100
100
100
100
100
Dneorreeted]
Velocity
(Ft/sec) ]
1
38.8
45.0
47.5
49.5
47.5
48.5
47.5
46.5
47.5
Stack Wet Bulb Temperature, (°F)
A. Barometric Pressure, (In.Hg)
B. Static Pressure of Stack Gases, (Zn.H20)
C. Pitot Tube Correction Factor
Stack Dimensions
D. Specific Gravity of Stack Gases Relative to Dry Air _
B. Absolute Pressure of Stack Gases - A + (B/13.6), (In.Hg) _
F. Average Uncorrected Velocity, (ft/sec) _ or 60 * F,(ft/min)
G. Corrected Velocity - F *
H.' Area of Stack, (ft2)
, (ft/min).
I. Actual Gas Flow Rate - G * H, (ACFM)
J. Average Stack Temperature, (°F)
K. Standard Gas Flow Rate - I
wbere T8td • standard temperature,
GDC-2
-------
C-16
SAMPLING TRAIN DATA
(Page 1 of 3)
Companyt Ford Motor Company
Source Designation; Coke Battery A Scrubber Inlet
Date: 4-11-75 Filter Heater Setting:
Teat Number; Prelim. EPA Method 5 Sample-! Probe Heater Setting:
Field Person; RJG Nozzle Number: tDia.(tn.); 3/16
Filter Number:
Barometric Pressure ("Hg); 29.6
Stack Static Pressure <"H?0); -4.3
Stack Dimensions: 66" I»D»
Plume Appearance:
Pitot Tube No. 18 iCorr.Factor;
Meter Box No .MAC-2 ,Corr. Factor; 0.973
Meter Isokinetic Factor:
Assumed Moisture (1): j
Condensate Volume(ml); 0
Ambient Temperature(°F):
Record all Data Every
Silica Gel Weight Gain(g):
Minutes Leak Rate CFM at
"Hg
Trav-
erse
Point
No.
B-8
B-7
B-6
B-5
B-4
B-3
Time
Samp-
ling
<8CC)
0
60
0
148
0
81
0
88
0
60
137
0
50
114
0
160
215
Clock
11:05
11:12
11:24
11:37
12:12
12:29
12:43
Velocity
Pressure
("H20)
1.25
1.60
0.15
1.45
1.45
1.45
1.40
1.40
1.30
1.60
AVERAGE (TOTAL)
Stack
Temp
(°F>
96
166
168
80
70
128
80
130
75
197
Dry Gas Meter
Volume
(ft3)
626.907
627.550
629.427
629.757
630.776
632.461
633.577
636.268
( )
Temp(°F)
Inlet
51
50
50
51
50
50
51
51
51
51
Outle t
45
44
44
45
44
44
45
45
45
45
Orifice
Pressure
Differ.
ential
("H20)
1.50
2.00
0.20
1.60
1.90
1.80
1.80
1.70
1.70
1.45
••liter
Box
Temp
(°F)
Last
Imp.
Gas
Temp
(°F)
Sampling
Train
Static
Pressure
("Hg)
2.0
•*
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
Clayton Environmental Consultants, Inc.
-------
C-17
SAMPLING TRAIN DATA
Company; Ford Motor Company
(Page 2 of 3)
Coke Batterv A Serubbar Inlat
Source Designation:^
Date: 4-11-75 Filter Heater Setting:
Teat Numberr Prelim*.EPA Method 5 Sample-1 Probe Heater Settlng:_
Field Peraon; RJG
Filter Number:
Barometric Pressure ("Hg); 29.6
Stack Static Pressure ("H20) :_^
Stack Dimensions; 66" I»D«
Flume Appearance:
Ambient Temperature (*F):_
Record all Data Every
Noetic Number: .Dia. (in.); 3/16
Pitot Tube No. is jCorr.Factor;
Meter lex No.MAC-2 .Corr.FactottQ.97i
Meter Isokinetic Factor:
Assumed Moisture (1): 1
Condensate Volume(ml); 0
Silica Gel Weight Gain(g):
Minutes Leak Rate CFM at
"Hg
trav-
erse
Point
No.
B-2
B-l
T-8
T-7
T-6
T-5
Time
Samp-
ling
(sec)
0
45
73
0
110
179
0
110
143
0
95
161
0
28
68
0
10
Clock
12:55
13:15
13:40
13:54
14:05
14:20
(Telocity
Pressure
("H20>
1.20
1.35
1.10
1.20
0.13
0.15
1.60
1.60
1.50
1.90
1.50
1.80
AVERAGE (TOTAL)
Stack
Temp
(°F)
75
163
68
147
78
139
70
129
70
210
70
310
Dry Gas Meter
Volume
(ft3)
636.268
637.098
638.992
639.575
641.654
642.552
( )
Temp(-F)
Inlet
51
51
52
52
52
52
52
52
52
52
52
52
Outlet
45
45
46
46
46
46
46
46
46
46
46
46
Orifice
pressure
Differ-
ential
("H20)
1.55
1.40
1.40
1.30
0.17
0.19
2.10
1.95
2.00
2.30
2.00
1.80
filter
Box
Temp
CF)
Last
Imp.
Gas
Temp
CF)
Sampling
Train
Static
Pressure
("Hg)
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
Clayton Environmental Consultants, Inc.
-------
C-18
SAMPLING TRAIN DATA
Company:
Source Designation:
Date: 4-11-75
Ford Motor Company
(Page 3 of 3)
Coke Battery A Scrubber Inlet
Filter Heater Setting:
Teat Number.prelim. BPAMfcfhod5 Sampla-1 Probe Heater Setting:
RJG
Field Person;
Filter Number:
Barometric Pressure ("Hg); 29.6
Stack Static Pressure ("HgO); -4.3
Stack Dimensions: 66"I«D»
Plume Appearance:
Noezle Number: .Dia. (in.);j/16
Pitot Tube No. 18,Corr.Factor;
Meter Box No .MAC-2 ,Corr.Factonp.978
Meter Isokinetic Factor;
Assumed Moisture(Z): 1
Condensate Volume (ml): 0
Ambient Temperature(°F):
Record all Data Every
Silica Gel Weight Gain(g):
Minutes Leak Rate CFM at
"Hg
Trav-
erse
Point
No.
T-4
T-3
T-2
T-l
Time
Samp-
ling
(sec)
62
0
35
92
0
170
231
0
180
240
0
25
74
Clock
14:30
14:50
15:04
15:28
Velocity
Pressure
("H20)
0.11
0.13
1.50
1.60
1.40
1.45
1.05
1.05
AVERAGE (TOTAL)
Stack
Temp
(°P)
70
173
70
138
70
128
70
104
111
Dry Gas Meter
Vo lume
(ft3)
643.333
643.333
643.653
646.632
649.586
650.342
( 22.919 )
TempCF)
Inlet
52
52
52
52
52
52
52
52
51
Outlet
46
46
46
46
46
46
46
46
45
Orifice
Pressure
Differ-
ential
<"H20)
0.15
0.15
2.00
2.00
1.85
1.75
1.40
1.30
1.5
(Filter
Box
Temp
(•F)
Last
Imp.
Gas
Temp
(DF)
Sampling
Train
Static
Pressure
("Hg)
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
Clayton Environmental Consultants, Inc.
-------
C-19
SAMPLING TRAIN DATA
(Page 1 of 3)
Companyt Ford Motor Company
Source Designation; Coke Battery A Scrubber Inlet
Date: 4-14-75 Filter Heater Setting:
Teat Number; prelim.KPAMethod 5 Sample-2 Probe Heater Setting:
Field Person; RJG Nocxle Number: .Die. (In.); 3/16
Filter Number: A-098-39
Barometric Pressure ("Hg); 29.8
Stack Static Pressure ("H?0)t -6.0
Stack Dimensions; 66" I.D.
Plume Appearance:
Ambient Temperature(°F):
Record all Data Every
Pltot Tube No. 18 ,Corr.Factor:
Meter Box No.MAC-2'iCorr. Factor; 0.978
Meter Isoklnetlc Factor:
Assumed Moisture(I); 1
Condensate Volume(ml): 5
Silica Gel Weight Gain(g):
Minutes Leak Rate CFM at
"Hg
Trav-
erse
Point
No.
T-8
T-7
T-6
T-5
T-4
T-3
•
Time
Samp-
ling
pee.)
0
60
100
0
60
0
20
75
0
20
53
0
180
234
0
227
Clock
13:18
13:30
13:42
14:00
14:15
14:28
Velocity
Pressure
("H20)
1.45
1.70
0.40
1.50
1.80
1.55
1.70
1.60
1.80
1.50
•
AVERAGE (TOTAL)
Stack
Temp
(°F)
70
310
185
70
153
70
150
70
165
70
Dry Gas Meter
Vo lurae
(ft3)
654.861
656.062
656.376
657.187
657.829
660.888
663.780
( )
Temp(-P)
Inlet
52
52
52
52
52
52
52
52
52
52
Outlet
46
46
46
46
46
46
46
46
46
46
[Orifice
Pressure
Differ-
ential
("H20)
1.95
1.70
0.56
1.70
2.00
2.00
1.90
2.10
2.20
2.00
Filter
Box
Temp
CF)
90
90
90
100
100
100
100
100
100
100
Last
Imp.
Gas
Temp
CF>
Sampling
Train
Static
Pressure
("Hg)
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
Clayton Environmental Consultants, Inc.
-------
C-20
SAMPLING TRAIN DATA
Ford Motor Company
(Page 2 of 3)
Coke Battery A Scrubber Inlet
Company:
Source Designation:^
Date: 4-14-75 Filter Heater Setting:
Teat Number:prelim. EPA Method 5 Samole-2 Probe Heater Setting:^
Field Person: RJG
Filter Number: A-098-39
Barometric Pressure ("Hg); 29.8
Stack Static Pressure ("H?0); -6.0
Stack Dimensions: 66" I.D.
Plume Appearance:
Nozzle Number: .Dia. (in.);j/i6
Pitot Tube No. 18 ,Corr.Factor;
Meter Box No MAC-2 tCorr.Factor Q.978
Meter Isokinetic Factor:
Assumed Moisture(I); i
Condensate Volume(ml); 5
Ambient Temperature(°F):
Record all Data Every
Silica Gel Weight Gain(g):
Minutes Leak Rate CFM at
"Hg
Trav-
erse
Point
No.
T-3
T-2
T-l
B-8
B-7
B-6
Time
Samp-
ling
<8ec?
0
60
110
0
120
245
0
70
107
0
85
130
0
25
74
0
30
Clock
14:39
14:48
15:01
15:16
15:22
16:19
Velocity
Pressure
<"H20)
1.50
1.70
1.40
1.50
1.10
1.10
1.80
2.00
1.70
1.90
0.13
0.15
AVERAGE (TOTAL)
Stack
Temp
(°F)
70
160
65
70
62
81
65
160
163
70
130
Dry Gas Meter
Volume
(ft3)
663.780
665.183
668.153
669.325
671.163
672.144
( )
Temp(°F)
Inlet
52
52
52
52
52
52
52
52
52
52
51
51
Outlet
46
46
46
46
46
46
46
46
46
46
45
45
Orifice
Pressure
Differ-
ential
C'H2b)
2.00
1.90
1.90
1.80
1.50
1.45
2.40
2.50
2.30
2.20
0.17
0.17
filter
Box
Temp
CF)
100
100
100
100
100
100
100
100
100
100
100
100
Last
Imp.
Gas
Temp
<"F)
Sampling
Train
Static
Pressure
("Hg)
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
Clayton Environmental Consultants, Inc.
-------
C-21
SAMPLING TRAIN DATA
Ford Motor Company
(Page 3 of 3)
Coke Battery A Scrubber Imlet
Company:_
Source Designation^
Date: 4-14-75 Pllter Heater Setting:
Teat Number;prelim. BgA Method 3 Sample-2 Probe Heater Setting:_
Field Peraon; RJG
Filter Number; A-098-39
Barometric Presaure ("Hg); 29.8
Stack Static Pressure ("HgO); -6.0
Stack Dimensions: 66" I»D»
Plume Appearance:
Noztle Number: .Dla. (in.); 3/16
Pitot Tube No. 18,Corr.Factor;
Meter Box No .MAC-2 .Corr.Pacton 0.978
Meter Isokinetlc Factor:
Assumed Moisture (1): 1
Condensate Volume (ml): 5
Ambient Temperature(°F):
Record all Data Every
Silica Gel Weight Galn(g):
Minutes Leak Rate CFM at
"Hg
Trav-
erae
Point
No.
B-5
B-4
B-3
B-2
B-l
Time
Samp-
ling
(aec)
71
0
60
111
0
75
112
0
90
120
0
90
125
0
45
80
Clock
16:33
16:47
17:01
17:13
17:28
"
(Telocity
Pressure
("H20)
1.60
1.80
1.40
1.50
1.30
1.30
1.50
1.70
1.10
1.30
•
AVERAGE (TOTAL)
Stack
Temp
(•F)
70
158
70
158
70
70
70
185
62
156
98
Dry Gas Meter
Volume
(ft3)
672.422
672.422
673.867
675.274
676.664
678.237
679.102
( 23.7 )
Temp(°F)
Inlet
51
51
51
51
51
51
51
51
51
51
52
Outlet
45
45
45
45
45
45
45
45
45
45
46
Orifice
Pressure
Differ-
ential
("H20)
2.15
2.05
1.85
1.75
1.70
1.55
2.00
1.80
1.45
1.45
1.84
tllter
Box
Temp
CF)
100
100
100
100
100
100
100
100
100
100
99
Last
Imp.
Gas
Temp
CF)
Sampling
Train
Static
Pressure
("Hg)
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
Clayton Environmental Consultants, Inc.
-------
C-22
SAMPLING TRAIN DATA
Company: Ford Motor Company
(Page 1 of 6)
Source Deaignatton; Coke Battery A Scrubber Inlet
Date: 6/24/75 Filter Heater Setting; 250°F
Test Number; EPA Method 5 Samale-1 Probe Heater Setting; 2Q00F
Field Person; RGK Nozcle Number; __ ,Pla.(in.); p. 189
Filter Number; A-147-25 & 26 Pitot Tube No. 18 ,Corr.Factor;p.838
Barometric Pressure ("Hg); 29.78 (avg) Meter Box No. RAC-UCorr.Factor; 0.974
Stack Static Pressure ("H;0); -5.0 Meter Isokinetic Factor; 1720
Stack Dimensions; 66" I.D. Assumed Moisture (I); 1
Plume Appearance;
Ambient Temperature(°F); 80
Record all Data Every 0.5
Condensate Volume(ml); 0
Silica Gel Weight Galn(g); 12
Minutes Leak Rate 0.0
CFM at 16.0 "Hg
Trav-
erse
Point
No.
T-12
T-ll
T-10
T-9
Time
Samp-
ling
(see}
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
09:43
10:36
10:52
11:03
Velocity
Pressure
("H20)
1.5
1.5
(1.5)
(1.5)
1.3
1.6
(1.5)
(1.6)
1.5
1.7
(1.6)
(1.7).
1.3
1.6
(1.3)
(1.7)
AVERAGE (TOTAL)
Stack
Temp
<°F)
80
250
(150)
(350)
83
150
(150)
(250)
87
200
(150)
(225)
90
150
(125)
(150)
Dry Gas Meter
Volume
(ft3)
445.592
446.577
447.317
447.925
( )
Temp(°F)
Inlet
80
82
82
82
Outlet
80
82
82
82
Orifice
Pressure
Differ-
ential
UU120)
1.7
1.7
(1.7)
2.0
2.1
(2.0)
2.2
2.0
(2.0)
1.85
2.1
(2.1)
?liter
Box
Temp
(°F)
130
230
230
230
Last
Imp.
Gas
Temp
(°F)
80
80
80
80
Sampling
Train
Static
Pressure
("Hg)
4.0
4.5
4.5
4.5
Clayton Environmental Consultants, Inc.
-------
C-23
SAMPLING TRAIN DATA
Companyi Ford Motor Company
(Pag* 2 of 6)
Source Designation:
Data: 6/24/75
Coke Battery A Scrubber Inlet
Test number; BPA Method 5 Sample-1
Field Person: RGK
Filter Heater Setting; 250T
Probe Heater Setting; 200*P
Filter Number; A-147-25 & 26
Nocsle Number; -- .Dia,(in.);.0.189
Pitot Tube No.18 .Corr.rector;0.838
Barometric Pressure ("Hg); 29.78 (avg) Meter Box No. RAC-l.Corr.Factor; 0.974
Stack Static pressure ("H?0); .5.0 Meter Isokinetic Factor; 1720
Stack Dimensions: 66" I.D. Assumed Moisture (I); 1
Plume Appearance: --
Ambient Temperature(*F)t 80
Record all Data Every 0.5
Condensate Volume(ml); 0
Silica Gel Weight Gain(g); 12
CPM at
Minutes Leak Rate
"Hg
Trav-
erse
Point
No.
T-8
T-7
T-6
T-5
Time
Samp-
ling
( sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
11:17
11:32
11:46
11:58
Velocity
Pressure
("H20)
1.3
1.5
(1.3)
(1.3)
1.2
1.5
(1.5)
(1.6)
1.2
1.4
(1.2)
(1.4) .
1.3
1.6
(1.6)
•
AVERAGE (TOTAL)
Stack
Temp
(•P)
88
130
(100)
(135)
90
200
(200)
(350)
96
260
(150)
(275)
95
400
(>600)
(>600)
Dry Gas Meter
Volume
(ft3)
448.725
449.527
450.210
450.928
( )
Temp('P)
Inlet
82
83
83
83
Outlet
82
83
83
83
Orifice
Pressure
Differ-
ential
("H20)
1.95
2.0
(2.0)
1.7
1.8
(1.8)
1.7
1.6
(1.6)
1.9
1.9
'liter
Box
Temp
CF)
235
235
235
235
Last
Imp.
Gas
temp
CF)
80
80
80
80
Sampling
Train
Static
Pressure
("HR)
4.5
4.5
4.5
4.5
Clayton Environmental Consultants, Inc.
-------
Company:
Source Designation:^
Date: 6/24/75
C-24
SAMPLING TRAIN DATA
Ford Motor Company
(Page 3 of 6)
Coke Battery A Scrubber Inlet
Filter Heater Setting; 250'P
Probe Heater Setting; 200"F
Test Number; EPA Method 5 Sample-1
Field Person; RGK Nozzle Number; -. ,Dia.(in.); p.189
Filter Number; A-147-25 & 26 Pitot Tube No. IS.Corr.Factor; 0.838
Barometric Pressure ("Hg): 29.78(avg) Meter Box No. RAC-l.Corr.Factor; p.974
Stack Static Pressure ("H20) :_=JLtO___ Meter Isokinetic Factor; 1720
Stack Dimensions; 66" I.D. Assumed Moisture (I); 1
Plume Appearance: --
Ambient Temperature(°F); 80
Record all Data Every 0.5
Condensate Volume(ml); 0
Silica Gel Weight Gain(g); 12
CFM at
Minutes Leak Rate
"Kg
Trav-
erse
Point
No.
T-4
T-3
T-2
T-l
Time
Samp-
ling
( sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
13:30
13:40
14:26
14:38
Velocity
Pressure
<"H20)
1.3
1.5
(1.4)
(1.5)
1.3
1.3
(1.3)
(1.3)
1.1
1.1
(1.1)
(1.1>
1.1
1.1
(1.1)
(1.2)
AVERAGE (TOTAL)
Stack
Temp
(6F)
95
200
(100)
(200)
95
150
(150)
(150)
100
200
(150)
(200)
100
150
(125)
(170)
Dry Gas Meter
Volume
(ft3)
451.665
452.323
452.982
453.693
( )
Temp(°F)
Inlet
86
86
76
—
Outlet
86
86
76
—
Orifice
Pressure
Differ-
ential
("H20)
1.85
1.85
1.8
2.0
(2.0)
1.6
1.3
(1.4)
1.6
1.6
(1.6)
[filter
Box
Temp
CF)
230
230
230
230
Last
Imp.
Gas
Temp
(°F)
83
83
83
83
Sampling
Train
Static
Pressure
("Hg)
4.5
4.5
3.0
3.0
Clayton Environmental Consultants, Inc.
-------
C-25
SAMPLING TRAIN DATA
Ford Motor Company
Company:_
Source Designation; Coke Battarv A Sert
Date: 6/25/75
Teat Number; BPA Method 5 Sample-1
Field Person: JBS
Filter Number: A-1A7-2S & 2ft
Barometric Pressure ("Hg); 29*78
Stack Static Pressure ("HgO); .5.0
Stack Dimensions: 66" I.D.
Plume Appearance: --
(Page 4 of 6)
Tnlat
Filter Heater Setting; 25Q*F
Probe Heater Setting; 250*F
Ambient Temperature(°F);gp
Record all Data Every 0.5
Nossle Number; .- .Dia. (in.);j.189
Pitot Tube No. 18 .Corr.Factor to.838
Meter Box No. RAC-IiCorr.FactonQ.974
Meter Isokinetic Factor; 1720
Assumed Moisture(I); 1
Condensate Volume(ml):0
Minutes
Silica Gel Weight Gatn(g); 12
Leak Rate 0.005 CFM at 16.5
"Hf
trav-
erse
Point
No.
S-12
S-ll
S-10
S-9
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
10:05
10:18
10:29
10:40
Velocity
Pressure
("H20)
1.2
1.6
(1.5)
1.5
1.5
(1.2)
(1.5)
1.3
1.6
(1.6)
1.1
1.5
(1.5)
AVERAGE (TOTAL)
Stack
Temp
(°F)
100
150
(125)
(250)
100
155
(125)
(160)
95
130
(125)
100
170
(125)
(200)
Dry Gas Meter
Vo lume
(ft3)
454.604
455.568
455.672
456.417
456.419
456.906
456.907
457.107
•
( )
TempCP)
Inlet
77
78
84
^_
Outlet
77
78
84
^^
Orifice
Pressure
Differ-
ential
(HH20)
1.7
2.1
2.1
2.1
1.8
2.2
(0.1)
0.1
0.1
(0.1)
filter
Box
Temp
CF)
250
250
250
.^
Last
Imp.
Gas
Temp
CFJ
68
70
70
_
Sampling
Train
Static
Pressure
("Hg)
M
_
4.0
16.0
16.0
16.0
(16.0)
Clayton Environmental Consultants, Inc.
-------
C-26
SAMPLING TRAIN DATA
Ford Motor Company
Companyt
Source Designation; Coke Battery A Scrubber inlet
(Page 5 of 6)
6/25/75
Date:
Test Number; EPA Method 5 Samnle-I
Field Person: JBS
Filter Heater Setting; 2SO*P
Probe Heater Setting; 250*P
Filter Number: A-147-25 & 26
Barometric Pressure <"Hg); 29.78(avg)
Stack Static Pressure ("HgO); .5.0
Stack Dimensions:
Plume Appearance:
66" I.D.
Nozxle Number; -- ,Dia.(in.);0.189
Pitot Tube No. 18 ,Corr.Factor; 0.838
Meter Box Ho. RAC-IiCorr.Factor; Q.974
Meter Isokinetic Pactor; 1720
Assumed Moisture(Z): 1
Condensate Volume(ml): 0
Ambient Temperature(°F); 80
Record all Data Every p.5
Minutes
Silica Gel Weight Cain(g):_l2
Leak Rate 0.005 CFM at 16.5 "Hg
Trav^
erse
Point
No.
S-8
S-7
S-6
S-5
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
12:53
13:10
13:32
13:42
Velocity
Pressure
<"H20)
1.5
1.5
(1.5)
1.3
1.6
1.3
1.6
1.3
1.6
AVERAGE (TOTAL)
Stack
Temp
CF)
110
475
(250)
(475)
110
280
(160)
(280)
105
225
(150)
(240)
95
175
(145)
(200)
Dry Gas Meter
Volume
(ft3)
459.169
459.951
459.957
460.702
460.707
461.457
461.458
462.250
< )
Temp(°F)
Inle
94
94
94
94
Outlet
93
93
93
93
Orifice
Pressure
Differ.
ential
("H20)
2.0
1.6
1.9
1.7
1.9
1.85
1.9
'liter
Box
Temp
(°F)
250
250
250
250
Last
Imp.
Gas
Temp
CF)
70
72
75
75
Sampling
Train
Static
Pressure
("Hg)
3.0
3.0
3.0
3.0
Clayton Environmental Consultants, Inc.
-------
C-27
SAHPLING TRAIN DATA
Companyt Ford Motor Company
(Page 6 of 6)
Source Designation:
Date: 6/25/75
Coke Battery A Scrubber Inlet
Teat Humbert BPA Method 5 Saaole-l
Field Person: JBS
Filter Heater Setting; 250T
Probe Heater Setting; 250*F
Filter Number; A-147-25 & 26
Nossle Number; -- .Die, (in.); 0.189
Pitot Tube No. 18 .Corr.Factor;0.838
Barometric Pressure ("Hg); 29.78 (ivt\ Meter Box No. RAC-1.Corr.Factor; 0.974
Stack Static Pressure ("H;0); -5.0 Meter Isokinetic Factor; 1720
Stack Dimensions: 66" I.D.
Plume Appearance: __
Assumed Moisture (I);
Ambient Temperature(°F); 80
Record all Data Every 0.5
Condensate Volume(ml); 0
Silica Gel Weight Gain(g); 12
Minutes Leak Rate 0.005 CFM at 16.5
"Hg
Trav-
erse
Point
No.
S-4
S-3
S-2
S-l
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
13:53
14:03
14:17
14:28
"
Velocity
Pressure
<"H20)
1.3
1.4
1.3
1.4
1.2
1.3
1.2
1.6
•
AVERAGE (TOTAL)
Stack
Temp
(°F>
100
160
(140)
(165)
100
145
(150)
(170)
110
225
(190)
(275)
110
500
(250)
(550)
158
Dry Gas Meter
Volume
(ft3)
462.252
463.023
463.027
463.758
463.762
464.452
464.453
465.132
( 16.897 )
Temp(°F)
Inlet
94
94
94
94
86
Outlet
94
94
94
94
86
Orifice
Pressure
Differ-
ential
("H20)
1.9
1.8
1.9
1.8
1.6
1.5
1.6
1.4
1.75
niter
Box
Temp
CF)
250
250
250
250
236
Last
Imp.
Gas
Temp
CD
75
75
75
75
77
Sampling
Train
Static
Pressure
("HB)
3.0
3.0
3.0
3.0
4.3
Clayton Environmental Consultants, Inc.
-------
C-28
SAMPLING TRAIN DATA
(Page 1 of 6)
Company: Ford Motor Company
Source Designation;
Date: 6/26/75
Coke Battery A Scrubber Inlet
Test Number; EPA Method .5 Sample-2
Field Person; JBS
Filter Heater Setting; 250"F
Probe Heater Setting; 250°F
_ Noztle Number; -- ,Dta. (In. ) ; 0.189
_ Pitot Tube No. 18 .Corr. Factor ;0. 838
Barometric pressure ("Hg); 29.54 (avg) Meter Box No. RAC-1. Corr. FactorsQ. 974
Filter Number: A-147-30
Stack Static pressure ("HgO); -5.Q
Stack Dimensions: 66" I.D.
Plume Appearance: --
Meter Isokinetic Factor:_
Assumed Moisture(Z): 1
1720
Condensate Volume(ml); 1
Ambient Temperature(°F); 80
Record all Data Every 0.5
Silica Gel Weight Cain(g); 12.5
Minutes Leak Rate 0.018 CFM at 16.0 "Hg
Trav-
erse
Point
No.
T-12
T-ll
T-10
T-9
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
09:25
10:16
10:39
10:49
Velocity
Pressure
("H20)
1.4
1.7
1.4
1.6
1.4
1.7
.
1.6
2.4
•
AVERAGE (TOTAL)
Stack
Temp
(•F)
105
225
(225)
100
300
(180)
(325)
90
175
(140)
(200)
100
375
(IBS)
(400)
Dry Gas Meter
Volume
(ft3)
465.324
466.112
466.128
466.878
466.886
467.680
467.682
468.502
( )
Temp(°F)
Inlet
70
84
92
93
Outlet
69
82
90
91
Orifice
pressure
Differ-
ential
("H20)
2.0
1.9
2.0
1.7
2.0
2.2
2.3
2.0
filter
Box
Temp
(°F)
170
190
265
260
Last
Imp.
Gas
Temp
(8F)
70
70
72
72
Sampling
Train
Static
Pressure
("HR)
3.0
3.0
3.0
3.0
Clayton Environmental Consultants, Inc.
-------
C-29
SAMPLING TRAIN DATA
(Pag* 2 of 6)
Company; Ford Motor Company
Source Designation; Coke Battery A Scrubber Inlet
fi/26/75
Date:
Teat Number; EPA Method 5 Sample.2
Field Person: JBS
Filter Number:
Filter Heater Setting:
Probe Heater Setting:
25Q*F
250'F
A-147-30
Barometric Pressure ("Hg)r 29.54 («vg)
Stack Static Pressure ("H;0); -5.0
Stack Dimensions:
Flume Appearance:
66" I.D.
Noccle Number; -- .Bia. (in. ) ; 0.189
Pitot Tube No. 18,Corr.Factor; 0.838
Meter Box No. RAG-1. Corr.Factor; 0.974
Meter Isokinetic Factor; 1720
Assumed Moisture(I); 1
Condensate Volume(ml); 1
80
Ambient Temperature(°F):
Record all Data Every 0.5
Minutes
Silica Gel Weight Gain(g); 12.5
Leak Rate — CFM at - "Hg
Trav-
erse
Point
No.
T-8
T-7
T-6
T-5
•
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
11:02
11:25
11:39
12:55
Velocity
Pressure
("H20)
1.4
1.7
1.5
1.6
1.4
1.5
1.4
1.8
AVERAGE (TOTAL)
Stack
Temp
(«F)
110
175
(160)
(220)
95
155
(135)
(195)
95
145
(120)
(160)
105
605
(260)
(605)
Dry Gas Meter
Volume
(ft3)
468.508
469.300
469.305
470.113
470.115
470.921
470.932
471.682
( )
Temp('F)
Inlet
94
95
95
95
Outlet
92
93
93
93
Orifice
Pressure
Differ-
ential
("H20)
2.0
2.1
2.2
2.1
2.0
2.0
2.0
1.6
filter
Box
Temp
CF)
260
265
265
265
Last
Imp.
Gas
Temp
CF)
73
70
70
70
Sampling
Train
Static
Pressure
("Hg)
3.0
3.0
3.0
3.0
Clayton Environmental Consultants, Inc.
-------
C-30
SAHPLINC TRAIN DATA
Company:
Source Designation:
Date: 6/26/75
Ford Motor Company
(Page 3 of 6)
Coke Batterv A Scrubber Inlet
Teat Humbert RPA Method S Samol«-2
Field Person:___JBS
Filter Number; A-147-30
Filter Heater Setting; 250"P
Probe Heater Setting; 250'P
Nozzle Number; -- ,Dia.(in.); 0.189
Pitot Tube No. 18 .Corr.Factor: 0.838
Barometric Pressure ("Hg); 29.54 (avg) Meter Box No. RAC-!• Co rr. Factor; p.974
Stack Static Pressure ("H;0); -5.0 Meter Isokinetic Factor: 1720
Stack Dimensions: 66" I.D.
Plume Appearance: --
Assumed Moisture(X): 1
Ambient Temperature("F): 80
Record all Data Every 0.5
Condensate Volume(ml); 1
Silica Gel Weight Gain(g); 12.5
Minutes Leak Rate — CFM at — "Hg
Trav-
erse
Point
No.
T-4
T-3
T-2
T-l
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
13:10
13:32
13:37
13:45
Velocity
Pressure
<"H20)
1.2
1.4
1.1
1.3
0.85
1.0
0.85
0.90
•
AVERAGE (TOTAL)
Stack
Temp
(°F)
110
270
(175)
(280)
100
175
(145)
(185)
100
150
(125)
(165)
100
130
(120)
(140)
Dry Gas Meter
Volume
(ft3)
471.683
472.387
472.388
473.082
473.083
473.718
473.718
474.350
( )
Temp(°F)
Inlet
95
96
96
97
Outlet
93
94
94
95
Orifice
Pressure
Differ-
ential
("H20)
1.6
1.6
1.6
1.6
1.2
1.3
1.2
1.2
?ilter
Box
Temp
CF)
260
260
260
260
Last
Imp.
Gas
Temp
CF)
75
75
75
75
Sampling
Train
Static
Pressure
("Hg)
3.0
3.0
3.0
3.0
Clayton Environmental Consultants, Inc.
-------
C-31
SAMPLING TRAIN DATA
Company; Ford Motor Company
(Page 4 of 6)
Source Designation; Coke Battery A Scrubber Inlet
Date: 6/26/75
Teat Number; BPA Method 5 Samole-2
Field Person! JBS
Filter Heater Setting; 250*7
probe Heater Setting; 250*P
Filter Number: A-147-30
_ Noesle Number; -- .Die,(in.);0.189
Pitot Tube No. 18 .Cerr.Factor;0;838
Barometric Pressure ("Hg); 29.54 C«Tg) Meter Box Ho.RAC-l.Corr. Factor; Jk_9JL4
Stack Static Pressure ("H?0); -5.0 Meter Isoklnetic Factor; 1720
Stack Dimensions; 66" I.D.
Flume Appearance: -.
Assumed Moisture(I):1
Ambient Temperature(°F); 80
Record all Data Every Q.S
Condensate Volume(ml); 1
Silica Gel Weight Gain(g); 12.5
Minutes Leak Rate 0.015 CFM at 16.5 "Hg
Trav-
erse
Point
No.
S-12
S-ll
S-10
S-9
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
14:08
14:38
14:58
15:04
(Telocity
Pressure
<"H20)
1.5
1.8
1.3
1.6
0.75
0.85
0.65
0.75
•
AVERAGE (TOTAL)
Stack
Temp
(°P>
105
245
(160)
(245)
95
260
(155)
(280)
100
225
(210)
(290)
100
150
(140)
(160)
Dry Gas Meter
Volume
(£t3)
474.353
475.160
475.166
475.929
475.936
476.545
476.548
477.118
( )
Temp('F)
Inlet
96
96
96
96
Outlet
94
94
94
94
Orifice
Pressure
Differ-
ential
("HzO)
2.2
2.0
1.9
1.7
1.0
1.1
1.0
1.05
'liter
Box
Temp
(•F)
260
260
260
260
Last
Imp.
Gas
Temp
(•F)
75
75
75
75
Sampling
Train
Static
pressure
("Hg)
4.0
4.0
4.0
4.0
Clayton Environmental Consultants, Inc.
-------
C-32
SAMPLING TRAIN DATA
(Page 5 of 6)
Company; Ford Motor Company
Source Designation:
Date: 6/27/75
Coke Battery A Scrubber Inlet
Filter Heater Setting; 250'F
Test Number; EPA Method 5 Samole-2
Field Person: JBS
Probe Heater Setting; 250"F
Nozzle Number; -- ,Dia.(in.); Q.189
Pltot Tube No.18 .Corr.FactortQ.838
Barometric Pressure ("Hg); 29.54 (avg) Meter Box No.RAC-1.Corr.Factor; 0.974
Filter Number; A-147-30
Stack Static Pressure ("H?0); -5.0
Stack Dimensions! 66" I.D.
Plume Appearance: -_
Meter Isokinetic Factor; 1720
Assumed Moisture(I); 1
Condensate Volume(ml); 1
Ambient Temperature(°F); 80
Record all Data Every 0.5
Silica Gel Weight Gain(g); 12.5
Minutes Leak Rate 0.010 CFM at 16.0 "Hg
Trav-
erse
Point
No.
S-8
S-7
S-6
S-5
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
10:56
11:08
11:35
11:58
Velocity
Pressure
("H20)
1.4
1.6
1.4
1.6
1.5
1.8
1.3
1.4
•
AVERAGE (TOTAL)
Stack
Temp
(°F)
105
175
(160)
(210)
105
170
(135)
(175)
105
450
(250)
(460)
110
400
(220)
(500)
Dry Gas Meter
Volume
(£t3)
477.325
478.112
478.114
478.902
478.908
479.700
479.703
480.448
( )
Temp(eF)
Inlet
96
96
96
96
Outlet
94
94
94
94
Orifice
Pressure
Differ-
ential
("H20)
2.0
2.0
2.0
2.0
2.2
1.7
1.9
filter
Box
Temp
(°F)
260
260
260
260
Last
Imp.
Gas
Temp
(°F)
75
75
75
75
Sampling
Train
Static
Pressure
("Hg)
3.0
3.5
3.5
3.5
Clayton Environmental Consultants, Inc.
-------
C-33
SAMPLING TRAIN DATA
(Pag* 6 of 6)
Company8 Ford Mbtor Company
Source Designation:
Data: 6/27/75
Coke Batterv A Scrubber Inlet
Teat Number: KPA Method 5 Sampla-2
Field Peraon; JBS
Filter Heater Setting; 250*t
Probe Heater Setting; 25Q*P
Filter Number: A-147-30
Noccle Number; -- .Dia.(in.); 0.189
____________________u Pitot Tube No. 18.Corr.Factor;'0.838
Barometric Preaaura ("Hg); 29.54 («V8> Meter Box Ho, RAC-l.Corr.FactonA.974
Stack Static Pressure ("H?0); -5.0 Meter Isokinetic Factor; 1720
Stack Dimensions: 66" I.D.
Plume Appearance: --
Assumed Moisture(I):
Ambient Temperature(°F); 85
Record all Data Every 0.5
Condensate Volume(ml); 1
Silica Gel Weight Gain(g); 12.5
Minutes Leak Rate —- CFM at — "Hg
Trav-
erse
Point
No.
S-4
S-3
S-2
S-l
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
13:25
13:40
14:05
14:24
(Telocity
Pressure
("H20)
1.2
1.7
1.2
1.4
1.2
1.4
1.0
1.3
AVERAGE (TOTAL)
Stack
Temp
(•F)
95
700
(275)
(850)
110
210
(155)
(225)
100
170
(210)
(270)
100
325
(170)
(325)
181
Dry Gas Meter
Volume
(ft3)
480.461
481.165
481.167
481.879
481.882
482.612
482.615
483.268
( 17.175)
Temp('F)
Inlet
96
96
96
96
94
Outlet
94
94
94
94
92
Orifice
Pressure
Differ-
ential
("H20)
1.7
1.4
1.7
1.7
1.7
1.8
1.4
1.4
1.7
? liter
Box
Temp
CF)
260
260
260
260
254
Last
Imp.
Gas
Temp
CF)
75
75
75
75
74
Sampling
Train
Static
Pressure
("Hg)
3.5
3.5
3.5
3.5
3.3
Clayton Environmental Consultants, Inc,
-------
C-34
SAMPLING TRAIN DATA
(Page 1 of 6)
Company:_
Source Designation:^
Date: 6/30/75
Ford Motor Company
Coke Battery A Scrubber Inlet
Teat Number; EPA Method 5 Sample-3
Field person: JBS
Filter Heater Setting; 250°F
Probe Heater Setting; 250*P
Filter Number; A-147-34
Nozzle Number; .. ,Dla.(In.); 0.189
Pitot Tube No.18 .Corr.Factor; Q.838
Barometric Pressure ("Hg); 29.70(avg) Meter Box No. RAC-l.Corr.Factor; 0.974
Stack Static Pressure ("HgO): -5.0 Meter Isokinetic Factor; 1720
Stack Dimensions; 66" I.D. Assumed Moisture (I); 1
Plume Appearance:
Ambient Temperature(°F); 83
Record all Data Every 0.5
Condensate Volume(ml); 0
Silica Gel Height Gain(g): 17
0.015 CFM at
Minutes Leak Rate
15.5 "Hg
Trav-
erse
Point
No.
T-12
T-ll
T-10
T-9
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
08:54
09:05
09:20
09:43
Velocity
Pressure
<"H20)
1.4
1.4
1.4
1.5
1.4
1.6
1.4
1.7
AVERAGE (TOTAL)
Stack
Temp
<°F)
100
150
(130)
(160)
100
495
(245)
(495)
105
320
(180)
(325)
100
260
(200)
(280)
Dry Gas Meter
Volume
(ft3)
483.442
484.202
484.207
484.932
484.933
485.683
485.686
486.446
( )
Temp(°F)
Inlet
80
88
94
95
Outlet
78
86
92
93
•
Orifice
Pressure
Differ-
ential
("H20)
2.0
1.8
2.0
1.3
2.0
1.7
2.0
1.9
filter
Box
Temp
(°F)
240
240
250
260
Last
Imp.
Gas
Temp
(°F)
78
78
78
78
Sampling
Train
Static
Pressure
("Hg)
2.5
2.5
2.5
2.5
Clayton Environmental Consultants, Inc.
-------
C-35
SAMPLING TRAIN DATA
Company; Ford Motor Company
(Pag* 2 of 6)
Source Designation; Coke Battery A Scrubber Inlet
Dat«: 6/30/75 •
Teat Humbert EPA Method 5 Sample.3
Field Person: JBS
Filter Heater Settlnit 250T
Probe Heater Setting; 250*P
Filter Number: A-147'-34
Nozzle Humbert -- yDla.(in.); 0.189
Pitot 'Tube No. 18 Afdfcr. Factor; 0.838
Barometric Pressure ("Hg); 29.70 (avg) Meter Box No. RAC-t.Corr.Factor 0.974
Stack Static Pressure ("HjO); -5.0 Meter Isokinetic Factor; 1720
Stack Dimensions: 66"' I.D. Assumed Moisture (I) : 1
Plume Appearance: --
Ambient Temperature(*F); 85
Record all Data Every O.S
Condensate Volume(ml); 0
Silica Gel Weight Gain(g); 17 .
.- CPM at
Minutes Leak Rate
- "Hg
Trav-
erae
Point
No.
T-8
T-7
T-6
T-5
Time
Samp-
ling*
(eec.)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
09:54
10:03
10:11
10:27
Velocity
Pressure
("H20)
1.4
1.6
1.4
1.6
1.4
1.5
.
1.4
1.6
AVERAGE (TOTAL)
Stapk
Temp
(°F)
100
210
(160)
(225)
100
170
(185)
(250)
105
160
(145}
(180)
105
575
(305)
(605)
Dry Gas Meter
Vo lume
(ft3)
486.446
487.209
.487.212
487.978
487.978
488.761
488.761
489.489
•
( )
Temp('F)
Inlet
95
95
96
96
Outlet
94
94
95
95
Orifice
pressure
Differ-
ential
("H20)
2.0
1.9
2.0
2.0
2.0
1.9
2.0
1.3
niter
Box
Temp
CF)
260
260
260
260
•
Last
Imp.
Gas
Temp
CF)
78
78
78
78
Sampling
Train
Static
Pressure
("Hg)
3.0
3.0
3.0
3.0
Clayton Environmental Consultants, Inc.
-------
C-36
8AHPLXMG TRAIN DATA
Companyt Ford Motor Company
(Page 3 of 6)
Source Designation^
D«t«: 6/30/75
Coke Batterv A Scxubbf
Inlet
Teat Humbert BPA Method 5 Samnla-3
Field Person: JBS
Filter Heater Setting; 250*.P
Probe Heater Setting; 250*F
Filter Humbert A-1A7-3A
Barometric Pressure ("Hg); 29.70 (avg)
Stack Static Pressure ("HgO); -5.0
Stack Dimensionst 66" I.D.
Plume Appearance: »_
Ambient Temperature (*P): gjj
Record all Data Every 0.5
NocEle Number; -- .Dia.(in.); 0.189
Pitot Tube No.IB .Corr.Factor; 0.838
Meter Box Ho. RAG-l.Corr.Factor; 0.974
Meter Isokinetic Factor; 1720
Assumed Moisture (Z) : j,
Condenaate Volume(ml): 0
Minutes
Silica Gel Weight Gain(g):JL7
Leak Rate - CPM at - "Hg
r rev-
erse
Point
Ho.
T-4
T-3
T-2
T-l
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
10i45
10:56
12:20
12:47
"
Velocity
treasure
("H20)
1.4
1.6
1.4
1.6
1.0
1.0
0.85
1.0
•
AVERAGE (TOTAL)
Stack
Temp
CF)
100
340
(175)
(340)
105
520
(260)
(530)
110
200
(160)
(220)
100
265
(155)
(265)
Dry Gas Meter
Volume
(ft3)
489.489
490.221
490.221
490.938
490.938
491.592
491.594
492.198
•
( )
Temp('F)
Inlet
96
99
99
99
Outlet
95
97
97
97
Orifice
treasure
Differ.
ential
("H20)
2.0
1.5
2.0
1.3
1.4
1.2
1.2
1.0
filter
Box
Temp
(°F)
260
250
250
250
•
Last
Imp.
Gas
Femp
rp?
78
78
78
78
Sampling
Train
Static
Pressure
("Hg)
3.0
3.0
2.0
2.0
Clayton Environmental Consultants, Inc.
-------
Company:
Source Designation;
Date: 6/30/75
C-37
SAMPLING TRAIN DATA
Ford Motor Company
(Page 4 of 6)
Coke Battery A Scrubber Inlet
Test Number; EPA Method 5 Samole-3
Field Person: JBS
Filter Number:
Filter Heater Setting; 250*r
probe Heater Setting; 250*F
A-147-34
Number; -- .Dia,(in.); 0.189
Pitot Tube No. 18 .Corr.Factor; 0.838
Barometric Pressure ("Hg); 29.70 (avj) Meter Box No. RAG-IiCorr.Factor; p.974
Stack Static Pressure ("H?0); -5.0 Meter Isokinetic Factor; 1720
Stack Dimensions:
Plume Appearance:
Ambient Temperature(°F):
Record all Data Every 0.5
66" I.D.
85
Aaaumed Moisture (X) : I
Condensate Volume(ml): 0
Silica Gel Weight Gain(g): 17
Minutes Leak Rate 0.015 CFM at 16.0 "Hg
Trav-
erse
Point
No.
S-12
S-ll
S-10
S-9
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
13:30
13:50
14:02
14:15
Velocity
Pressure
("H20)
1.2
1.6
1.4
1.7
1.5
1.5
.
1.2
1.2
•
AVERAGE (TOTAL)
Stack
Temp
(•F)
110
270
(170)
(270)
120
170
(165)
(190)
115
165
(155)
(185)
110
700
(350)
(BOO)
-
Dry Gas Meter
Volume
(ft3)
492.198
492.924
492.924
493.701
493.701
494.484
494.484
495.178
( )
Temp(°F)
Inlet
99
99
99
99
Outlet
97
97
97
97
Orifice
Pressure
Differ-
ential
("H20)
1.7
1.7
1.9
2.2
2.1
1.8
2.1
1.2
'liter
Box
Temp
CF)
250
250
250
250
Last
Imp.
Gas
Temp
rp?
78
78
78
78
Sampling
Train
Static
Pressure
("Hg)
3.0
3.0
3.0
3.0
Clayton Environmental Consultants, Inc.
-------
C-38
SAMPLING TRAIN DATA
Componyi Ford Motor Company
(Page 5 of 6)
Source Designation:^
Date: 6/30/75' - 7/1/75
Coke Battery A Scrubber Inlet
Filter Heater Setting; 250*P
Probe Heater Setting; 250*P
Test Number; RPA Method 5 Samnle-3
Field Person: JBS
Filter Number; A-147-34
Barometric Pressure ("Hg); 29.70 (avg)Meter Box No. RAC-I.Corr.Factor; 0.974
Stack Static Pressure ("H20): -5.0 Meter Isokinetic Factor; 1720
Stack Dimensions: 66" I.D.
Plume Appearance: --
Nozzle Humbert -- ,Dia.(in.); Q.189
Pitot Tube No. 18 .Corr.Factor;0.838
Assumed Moisture(I):
Ambient Temperature(°F);
Record all Data Every 0.5
85
Condensate Volume(ml); 0
Silica Gel Weight Cain(g); 17
Minutes Leak Rate 0.015 CFM at 16.0 "Hg
Trav-
erse
Point
No.
S-8
S-7
S-6
7/1/75
S-5
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
14:23
14:48
15:13
08:51
(Telocity
Pressure
("H20>
1.4
1.6
1.4
1.5
1.4
1.7
1.2
1.2
•
AVERAGE (TOTAL)
Stack
Temp
(°F)
125
305
(180)
(315)
100
255
(185)
(275)
120
380
(210)
(380)
90
145
(135)
(160)
Dry Gas Meter
Volume
(ft3)
495.178
495.925
495.925
496.680
496.680
497.420
497.428
498.137
( )
TempCF)
Inlet
99
99
99
90
Outlet
97
97
97
88
Orifice
Pressure
Differ-
ential
("H20)
2.0
1.7
2.0
1.7
1.9
1.6
1.7
1.6
filter
Box
Temp
CF)
250
250
250
250
Last
Imp.
Gas
Temp
CF}
78
78
78
75
Sampling
Train
Static
Pressure
("Hg)
3.0
3.0
3.0
3.0
Clayton Environmental Consultants, Inc.
-------
C-39
SAMPLING TRAIN DATA
Ford Motor Company
Company:
Source Deaignatlon; Coke Battery A Scrubber Inlet
Data: 7/1/75 - 7/2/75
(Page 6 of 6)
Taat Number; BPA Method 5 Sample-3
Field Pereon; JBS
Filter Number:
Filter Heater Setting; 250T
Probe Heater Setting: 250*F
Noccle Number; -- .Dia.(in.); 0.189
Pitot Tube No, 18 .Corr.Factor;'0.838
Barometric Preaaure ("Hg); 29.70 (avi)Meter lex No. RAC-I.Cerr.Factor; 0.974
A-147-34
Stack Static Pressure ("H;0)t -5.0
Stack Dimensions: 66" I.D.
Plume Appearance: --
Meter laokinetic Factor:_
Assumed Moisture(1): 1
1720
Condensate Volume(ml):0
Ambient Temperature(*F); 95
Record all Data Every 0.5
Silica Gel Weight Cain(g); 17
Minutes Leak Rate 0.015 CPM at
16.5 "Hg
Trav-
erse
Point
No.
S-4
7/375
S-3
S-2
S-l
Time
Samp-
ling
(sec)
0
30
60
Max ,
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
09:35
09:21
09:28
09:46
Velocity
Preaaure
("H20)
1.2
1.6
1.1
1.7
1.2
1.4
1.2
1.0
AVERAGE (TOTAL)
Stack
Temp
CF)
100
440
(205)
(440)
90
410
(350)
(410)
110
410
(185)
(415)
105
170
(180)
(190)
209
Dry Gas Meter
Volume
(ft3)
498.142
498.853
498.858
499.619
499.619
500.361
500.362
501.041
( 17.109)
TempCF)
Inlet
97
98
98
99
96
Outlet
95
96
96
97
94
Orifice
Pressure
Differ-
ential
("H20)
1.7
1.5
1.6
1.6
1.7
1.6
1.7
1.3
1.7
'liter
Box
Temp
CF)
250
250
250
250
252
Last
Imp.
Gas
Temp
CF)
75
70
70
70
77
Sampling
Train
Static
Preaaure
("HR)
3.0
3.0
3.0
3.0
2.8
Clayton Environmental Consultants, Inc.
-------
C-40
SAMPLING TRAIN DATA
Conpnny: Ford Motor Company
(Page 1 of 4)
Source Designation^
7/2/75
_Cake Batterv A Scrubber Tnlat
Test Number; EPA Method 5 Sample-4
Field Person: JBS
Filter Heater Setting; 250*F
Probe Heater Setting; 250°F
Filter Number: A-147-12
Barometric Pressure ("Hg); 29.46 (avg)
Stack Static Pressure ("H?0); -5.0
Stack Dimensions: 66" I.D.
Plume Appearance:
Nozzle Number; — ,Dia. (In.);0.189
Pitot Tube No.18 ,Corr.Factor;0.838
Meter Box No. RAC-l.Corr.Factor; p.974
Meter Isokinetic Factor; 1720
Assumed Moisture(I); 1
Condensate Volume (ml): -2
Ambient Temperature (°7) : -_.
Record all Data Every 0.5
Minutes
Silica Gel Weight Gatn(g); 17
Leak Rate 0.020 CFM at 17.0 "Hg
Trav-
erse
Point
No.
T-8
T-7
T-6
T-5
Time
Samp-
ling
Ufifi?
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
13:27
13:35
13:45
13:55
Velocity
Pressure
("H20)
1.4
1.5
1.4
1.6
0.8
0.9
1.0
1.5
•
AVERAGE (TOTAL)
Stack
Temp
(•F)
110
180
U55)
(195)
110
155
(130)
(165)
110
200
(140)
(240)
110
200
(155)
(225)
Dry Gas Meter
Volume
(ft3)
501.338
502.125
502.128
502.928
502.928
503.553
503.553
504.263
( )
Temp(°F)
Inlet
94
95
?6
97
Outlet
92
93
94
95
Orifice
Pressure
Differ-
ential
("H20)
2.0
1.8
2.0
2.1
1.1
1.1
1.4
1.8
Filter
Box
Temp
(°F)
250
250
250
250
Last
Imp.
Gas
Temp
(°F)
70
70
70
70
Sampling
Train
Static
Pressure
("Hg)
2.5
2.5
2.5
2.5
Clayton Environmental Consultants, Inc.
-------
C-41
SAMPLING TRAIN DATA
Company; Ford Motor Company
(Page 2 of 4)
Source Designation; Coke Battery A Scrubber Inlet
7/2/75
Date: _
Test Number; EPA Method 5 Sample-4
Field Person: JBS _
Filter Heater Setting; 250'F
Probe Heater Setting! 250"F
Filter Number: A-147-12
66" I.D.
Barometric Pressure ("Hg); 29.46(avg)
Stack Static Pressure ('^0): -5.0
Stack Dimensions;
Plume Appearance:
Ambient Temperature(°F): •
Record all Data Every 0.5
Noccle Number; -- .Dia.(in.); 0.189
Pitot Tube No. 18 ,Corr.Factor*; 0.838
Meter Box No. RAC-I.Corr.Factor!0.974
Meter Isokinetic Factor; 1720
Assumed Moisture(X) : 1
Condensate Volume(ml); -2
Minutes
Silica Gel Weight Gain(g); 17
Leak Rate
CFM at
"Hg
Trav-
erse
Point
No.
T-4
T-3
T-2
T-l
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
14:15
14:42
14:55
15:05
(Telocity
Pressure
("H20>
1.3
1.7
1.2
1.7
1.2
1.5
1.2
1.4
•
AVERAGE (TOTAL)
Stack
Temp
(•F)
110
380
(200)
(380)
105
260
(155)
(260)
110
200
(150)
(220)
110
170
(135)
(185)
.
Dry Gas Meter
Volume
(ft3)
504.265
505.004
505.008
505.749
505.749
506.503
506.503
507.254
( )
Temp(°F)
Inlet
99
101
102
102
Outlet
97
98
100
100
Orifice
Pressure
Differ-
ential
("H20)
1.8
1.6
1.7
1.9
1.7
1.8
1.7
1.75
'liter
Box
Temp
CF)
250
250
250
250
Last
Imp.
Gas
Temp
CF)
70
70
70
70
Sampling
Train
Static
Pressure
("Hg)
2.5
2.5
2.5
2.5
Clayton Environmental Consultants, Inc.
-------
C-42
SAMPLING TRAIN DATA
(Page 3 of 4)
Company; Pord Motor Company
Source Designation:^
Date: 7/2/75 - 7/3/75
Coke Battery A Scrubber Inlet
Teat Number; EPA Method 5 Sample -
Field Person: _ JBS
Filter Number;
Filter Heater Setting; 250"P
Probe Heater Setting; 250'F
Nozzle Number; -- .Dia.(in.); 0.189
Pitot Tube No. 18 .Corr.Factor: 0.838
Barometric Pressure ("Kg): 29.46 (avg) Meter Box NoJUC-1 .Corr.Factor 0.974
A- 147- 12
Stack Static Pressure ("HgO); -5.0
Stack Dimensions: 66" I.D.
Plume Appearance: _-
Ambient Temperature (°F) : ..
Record all Data Every Q.S
Meter Isokinetic Factor;
Assumed Moi»ture(I); 1
1720
Condenaate Volume (ml); -2
Minutes Leak Rate
Silica Gel Weight Galn(g):17 _
0.020 CFM at 16.5 "Hg
Trav-
erse
Point
No.
S-8
S-7
//3
S-6
S-5
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
15:35
15:45
08:38
09:03
Velocity
Pressure
("H20)
1.3
1.6
1.4
1.7
1.4
1.6
1.4
1.4
AVERAGE (TOTAL)
Stack
Temp
CF)
100
200
(190)
(310)
105
200
(220)
(280)
80
175
(130)
(200)
85
130
(155)
(170)
Dry Gas Meter
Volume
(£t3)
507.256
508.028
508.031
508.842
509.318
510.120
510.120
510.902
( )
TempCF)
Inlet
102
102
98
98
Outlet
100
100
96
96
Orifice
pressure
Differ-
ential
("H20)
1.9
2.0
2.1
1.95
2.05
1.9
filter
Box
Temp
(°F)
250
250
250
250
Last
Imp.
Gas
Temp
(°F)
70
70
70
70
Sampling
Train
Static
Pressure
("Hg)
2.5
2.5
2.5
2.5
Clayton Environmental Consultants, Inc.
-------
C-43
SAMPLING TRAIN DATA
(Page 4 of 4)
Company: Pord Mot
Source Designation:
Date: 7/3/75
Coke Batterv A Scrubber Inlet
Teat Number; EPA Method 5 Sample.4
Field Peraon: JB3
Filter Heater Setting; 25Q°g
Probe Heater Setting; 25Q°P
Noccle Number; ,Dia.(in.);ji. 199
Pltot Tube No. 18,Corr.Factor; 0.838
Barometric Pressure ("Hg); 29.46 (avg) Meter Box No.RAC-l'«Cerr.Factor 0.974
Filter Humbert A-147-12
Stack Static Pressure ("H?0); -5.0
Stack Dimensions; 66" I.D.
Plume Appearance:
Meter Isokinetic Factor;
Assumed Moisture (I); i
1720
Condensate Volume (ml); -2
Ambient Temperature(*F);--
Record all Data Every
0.5 Minutes
Silica Gel Weight Cain(g); 17
Leak Rate
CFM at
"Hg
trav-
erse
Point
No.
S-4
S-3
S-2
S.I
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
09:39
09:54
10:06
10:27
'
(Telocity
Pressure
("H20)
1.4
1.6
1.2
1.4
1.2
1.3
1.0
1.4
•
AVERAGE (TOTAL)
Stack
Temp
(°P)
90
160
(120)
(170)
90
140
(120)
(160)
90
195
(140)
(210)
90
325
(160)
(330)
152
Dry Gas Meter
Volume
(ft3)
510.902
511.700
511.700
512.434
512.434
513.177
513.177
513.872
•
( 11.731)
Temp(°F)
Inlet
98
98
98
98
99
Outlet
96
96
96
96
97
Orifice
Pressure
Differ-
ential
("H20)
2.0
2.1
1.75
1.8
1.75
1.6
1.5
1.5
1.8
niter
Box
Temp
(•F)
250
250
250
250
250
Last
Imp.
Gas
Temp
CF)
70
70
70
70
70
Sampling
Train
Static
Pressure
("Hg)
2.5
2.5
2.5
2.5
2.5
Clayton Environmental Consultants, Inc.
-------
C-44
SAMPLING TRAIN DATA
(Page 1 of 4)
Company; Ford Motor Company „
Source Designation: Coke Battery A Scrubber Inlet
Date: 7/8/75
Test Number:EPA Method 5 -ffaaple-5
Field Person: RCM
Filter Number:
Filter Heater Setting; 250?F
Probe Heater Setting: 250°F
A-147-13
Barometric pressure ("Hg); 29.31
Stack Static Pressure ("H20) :___4_t
Stack Dimensions:
Plume Appearance:
66" I.p.
Nozzle Number; -- ,Dia.(in.) ; 0.189
Pitot Tube No. IB,Corr.Factor; p.838
Meter Box No.RAC-1 jCorr.Factor; 0.974
Meter Isokinetic Factor; 1720
Assumed Moisture(X) : 1
Condensate Volume(ml); 8
Ambient Temperature(°F);--
Record all Data Every p. 5
Minutes
Silica Gel Weight Gain(g): §_
Leak Rate 0.022 CFM at
"Hg
Trav-
erse
Point
No.
T-8
T-7
T-6
T-5
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
09:28
10:17
10:33
10:43
Velocity
Pressure
("H20)
1.25
1.45
(0.30)
(1.50)
1.45
1.55
(1.40)
(1.60)
1.40
1.45
(1.35)
(1.50.)
1.40
1.50
(0.5)
(1.55)
AVERAGE (TOTAL)
Stack
Temp
(°F>
90
.160
(150)
(175)
92
150
(125)
(160)
95
140
(125)
(155)
95
185
(140)
(205)
Dry Gas Meter
Volume
(ft3)
515.018
515.783
515.785
516.618
516.618
517.417
517.418
518.210
( )
Temp(°F)
Inlet
88
88
100
98
Outle t
82
85
98
98
Orifice
Pressure
Differ-
ential
("H20)
1.85
1.90
2.14
2.08
2.10
2.01
2.09
1.93
?ilter
Box
Temp
(°F)
200
225
205
205
Last
Imp.
Gas
Temp
CF)
73
74
75
76
Sampling
Train
Static
Pressure
("Hg)
3.0
3.0
3.3
3.5
Clayton Environmental Consultants,
-------
C-45
SAMPLING TRAIN DATA
Ford Motor Company
(Page 2 of 4)
Company:
Source Designation; Coke Battery A Scrubber Inlet
7/8/75
Date:
Test Number;EPA Method 5 Sample-5
Field Person: RCM
Filter Heater Setting; 250*F
Probe Heoter Setting; 250°F
Filter Number: A-147-13
Barometric Pressure ("Hg); 29.31
Stack Static pressure ("H?0): -4.2
Stack Dimensions; 66" I.D.
Plume Appearance;
NoBile Number; -- .Dta.(In.): 0.189
Pitot Tube No. 18 ,Corr.Factor;0.838
Meter Box No.RAC-l,Corr.Factor; 0.974
Meter Isokinetic Factor; 1720
Assumed Moisture(I); 1
Condensate Volume(ml); 8
Ambient Temperature(°P);
Record all Data Every 0.5
Minutes
Silica Gel Weight Cain(g); 5
Leak Rate
CFM at
"Hg
Trav-
erse
Point
No.
T-4
T-3
T-2
T-l
Time
Samp-
ling
fsfic}
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
10:56
11:41
12:13
12:45
Velocity
Pressure
("H20>
1.30
1.55
(1.30)
(1.65)
1.35
1.45
(1.35)
(1.45)
1.30
1.4
(0.2)
(1.45)
1.05
1.15
(0.8)
(1.20)
AVERAGE (TOTAL)
Stack
Temp
(°P)
94
225
(140)
(235)
96
175
(130)
(185)
98
170
(145)
(180)
95
150
(130)
(165)
•
Dry Gas Meter
Volume
(ft3)
518.211
519.019
519.021
519.802
519.802
520.605
520.605
521.304
( )
Temp(°P)
Inlet
98
101
101
101
Outle t
98
98
98
99
Orifice
Pressure
Differ-
ential
("H20)
1.95
1.88
2.02
1.90
1.94
1.85
1.58
1.56
filter
Box
Temp
(°F)
200
205
185
175
Last
Imp.
Gas
Temp
CF)
74
75
76
78
Sampling
Train
Static
Pressure
("Hg)
3.5
3.5
3.5
3.5
Clayton Environmental Consultants, Znc,
-------
C-46
SAMPLING TRAIN DATA
Ford Motor Company
(Page 3 of 4)
Company;
Source Designation: Coke Battery A Scrubber Inlet
7/8/75
Date: _
Test Humbert EPA Method 5 Sample-5
Field Person: ROM
Filter Number; A-147-13
Barometric Pressure ("Hg); 29.31
Filter Heater Setting; 250'P
Probe Heater Setting; 250"F
Stack Static Pressure ("HgO); -4.2
Stack Dimensions: 66" I.D. |_
Plume Appearance: --
Ambient Temperature(*F); --
Record all Data Every
0.5 Minutes
Nozzle Number:_-- .Dia. (in.); 0.189
Pitot Tube No. 18,Corr.Factor; 0.838
Meter Box No. RAC-ltCorr.Factor; 0.974
Meter Isoklnetic Factor; 1?20
Assumed Moisture (X) : i
Condensate Volume(ml); 8
Silica Gel Weight Gain(g):5
Leak Rate
CFM at
"Hg
Trav-
erse
Point
No.
S-8
S-7
S-6
S-5
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
13:05
13:20
13:35
13:45
Velocity
Pressure
("H20)
1.35
1.45
(1.30)
(1.50)
1.40
1.7
(1.35)
(1.7)
1.3
1.45
(1.3)
(1.45)
1.35
1.45
(1.30)
(1.55)
AVERAGE (TOTAL)
Stack
Temp
(°F)
98
210
(145)
(225)
102
200
(150)
(225)
100
190
(145)
(210)
103
175
(155)
(215)
Dry Gas Meter
Volume
(ft*)
521.305
522.085
522.086
522.902
522.902
523.671
523.672
524.452
( )
Temp(°F)
Inlet
101
101
101
101
Outle t
99
99
99
99
Orifice
Pressure
Differ-
ential
("H20)
2.02
1.81
2.08
2.16
1.94
1.85
2.00
1.90
filter
Box
Temp
CF)
215
205
215
215
Last
Imp.
Gas
[emp
(°F)
78
79
81
82
Sampling
Train
Static
Pressure
("Hg)
3.5
4.0
4.0
4.0
Clayton Environmental Consultants, Inc.
-------
Company:
Source Designation:
Date: 7/8/75
C-47
SAMPLING TRAIN DATA
Ford Motor Company
(Page 4 of 4)
Coke Battery A Scrubber Inlet
Teat Number;BPA Method 5 Samnle-5
Field Person: ROM
Filter Heater Setting; 250*p
Probe Heater Setting; 250*F
Filter Number: A-147-13
Barometric Pressure ("Hg); 29.31
Stack Static Pressure ("H?0)t -4.2
Stack Dimensions: 66" I.D.
Plume Appearance: --
Ambient Temperature(°F):
Nozsle Number; -- ,Dta.(in.); 0,189
Pitot Tube No. 18,Corr.Factor;'0.838
Meter Box No. RAC-1'iCorr.Factor; Q.974
Meter Isokinetic Factor; 1720
Assumed Moisture(1); 1
Condensate Volume(ml); 8
Silica Cel Weight Gain(g): 5
Record all Data Every 0.5 Minutes Leak Rate 0.015 CFM at
"Hg
Trav-
erse
Point
No.
S-4
S-3
S-2
S-l
Time
Samp-
ling
(s«c}
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
14:03
14:21
14:40
14:49
Velocity
Pressure
<"H20>
1.30
1.45
(1.30)
(1.45)
1.25
1.35
(1.30)
(1.40)
1.15
1.45
(1.3)
(1.45;
1.05
1.25
(0.2)
(1.30)
AVERAGE (TOTAL)
Stack
Temp
<°F>
105
170
(135)
(195)
104
135
(170)
(185)
100
200
(150)
(215)
100
180
(145)
(205)
137
Dry Gas Meter
Volume
(ft3)
524.452
525.235
525.237
526.027
526.029
526.786
526.804
527.538
( 12.164)
Temp(°F)
Inlet
101
101
101
102
99
Outlet
99
99
99
101
97
Orifice
pressure
Differ-
ential
("H20)
1.92
1.92
1.85
1.89
1.72
1.82
1.56
1.63
1.90
'liter
Box
Temp
<°F)
210
210
200
215
205
Last
Imp.
Gas
Temp
<-F)
82
82
83
83
78
Sampling
Train
Static
Pressure
("Hg)
4.0
4.0
4.5
4.5
3.7
Clayton Environmental Consultants, Inc.
-------
C-48
SAMPLING TRAIN DATA
Company:
Source Designation:
Ford Motor Company
(Page 1 of 4)
Coke Battery A Scrubber Inlet
7/10/75
Date:
Test Number^PA Method 5 Sample-6
Field Person: ROM
Filter Number; A-190-14
Barometric Pressure ("Hg); 29.33.
Stack Static Pressure _ _
Stack Dimensions: 66""l.D.
Plume Appearance: --
Filter Heater Setting; 250°F
Probe Heater Setting: 250*F
-4.7
Nozzle Number; -- .Dia.(in.); 0*187
Pitot Tube No. 18.Corr.Factor; 0.838
Meter Box No. RAC-1.Corr.Factor; 0.974
Meter Isokinetic Factor; 1720
Assumed Moisture(X): l
Condensate Volume (ml): p_
Ambient Temperature (°F) : -_;
Record all Data Every 0.5
Minutes
Silica Gel Weight Gain(g); 14.5
Leak Rate 0.005 CFM at 16.0 "Hg
Trav-
erse
Point
No.
T-8
T-7
T-6
T-5
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
09:40
09:53
10:17
10:45
Velocity
Pressure
("H20)
1.20
1.50
(1.20)
(1.60)
1.60
1.95
(1.60)
(2.05)
1.30
1.60
(1.30)
(1.65)
1.25
1.45
(1.25)
(1.50)
•
AVERAGE (TOTAL)
Stack
Temp
(°F)
78
175
(140)
(215)
83
450
(175)
(470)
85
190
(130)
(205)
80
150
(125)
(175)
Dry Gas Meter
Volume
(ft3)
540.605
541.347
541.348
542.141
542.143
542.919
542.923
543.676
( )
Temp(eF)
Inlet
72
80
82
82
Outle t
70
75
78
82
Orifice
Pressure
Differ-
ential
("H20)
1.76
1.86
2.36
1.72
1.92
1.98
1.87
1.92
?ilter
Box
Temp
CF)
200
210
215
215
Last
Imp.
Gas
Temp
CF)
68
70
71
73
Sampling
Train
Static
pressure
("Hg)
3.0
3.0
3.0
3.2
Clayton Environmental Consultants, Inc,
-------
C-49
SAMPLING TRAIN DATA
Company:__
Source Designation:^
Date: 7/10/75
Ford Motor Company
(Page 2 of 4)
Coke Battery A Scrubber Inlet
Teat Number; EPA Method 5 Sample-6
Field Person: ROM
Filter Number:
Filter Heater Setting; 250°F
Probe Heater Setting; 250*F
A-190-14
Barometric Pressure ("Hg); 29.33
Stack Static Pressure ("HgO): .4.7
Stack Dimensions: 66" I.D.
Plume Appearance: -_-
Ambient Temperature(°F);
Record all Data Every
Notcle Number; -- ,Dia.(in.); 0.187
Pitot Tube No. is «Corr.Factor;-o.838
Meter Box No. RAC-1,Corr.Factor; 0.974
Meter Isokinetic Factor; 1720
Assumed Moisture(I); 1
Condenaate Volume(ml); 0
Silica Gel Weight Gain(g); 14.5
0.5 Minutes Leak Rate
CPM at
"Hg
Irav-
eree
Point
No.
T-4
T-3
T-2
T-l
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
10:57
11:07
11:20
.
12:42
(Telocity
Pressure
("H20)
1.20
1.40
(1.25)
(1.40)
1.25
1.4
(1.25)
_ _
1.20
1.45
(1.20)
(1.45)
1.05
1.30
(1.05)
(1.35)
AVERAGE (TOTAL)
Stack
Temp
(«F)
80
135
(110)
(145)
80
135
(105)
__
82
170
(140)
(200)
80
130
(110)
(150)
.
Dry Gas Meter
Volume
(£t3)
543.678
544.437
544.438
545.200
545.200
545.964
545.965
546.733
•
( )
Temp(°F)
Inlet
90
90
92
83
Outlet
90
90
92
83
Orifice
Pressure
Differ-
ential
("H20)
1.82
1.93
1.90
1.93
1.82
1.89
1.57
1.78
filter
Box
Temp
(•F)
215
225
220
225
Last
Imp.
Gas
Temp
(•F)
76
78
78
80
Sampling
Train
Static
Pressure
("Hg)
3.3
3.5
3.5
3.5
Clayton Environmental Consultants, Inc.
-------
C-50
SAMPLING TRAIN DATA
Company * Ford Motor Company
(Page 3 of 4)
Source Designation:
Date: 7/10/75
Test Number;EPA Method 5 Sample-6
Field Person: RCM
Filter Number:
Coke Battery A Scrubber Inlet
Filter Heater Setting; 250*7
Probe Heater Setting; 250*F
A-190-14
Barometric Pressure ("Hg); 29.33
Stack Static Pressure ("H?0); .4.7
Stack Dimensions:
Plume Appearance:
66" I.P.
Ambient Temperature("F):
Record all Data Every 0.5
Minutes
Nozzle Number; -- ,Dia.(in.)• p.187
Pitot Tube No. IS.Corr.Factor; p.838
Meter Box No. RAC-I»Corr.Factor; 0,974
Meter Isokinetic Factor; 1720
Assumed Moisture(I); 1
Condensate Volume (ml): 0
Silica Gel Height Gain(g):
Leak Rate CFM at
14.5
"Hg
rrav
erse
Point
No.
S-8
fi-7
S-6
S-5
Time
Samp-
ling
(sec)
0
30
60
Max
fl
,,30
60
Max_
o
30
60
Max
0
30
60
Max
Clock
12:52
13-37
13;58
14:10
Velocity
pressure
("H20)
1.60
1.75
(1.55)
(1.75)
1.60
2.2
fl.6S\
>
1.5
1.7
(1.40)
(1.755
1.35
1.55
(1.35)
(1.6)
AVERAGE (TOTAL)
Stack
Temp
CF)
90
140
(115)
(160)
92
300
ri7tn
n40*
95
200
(145)
(230)
95
155
(130)
(175)
Dry Gas Meter
Volume
(ft3)
546.733
547.582
5A7.5H1
548. &46
548.447
549.269
549.270
550.050
)
TempCF)
Inle
84
05
90
90
Outle
80
90
90
90
Orifice
Pressur
Differ.
ential
("H20>
2.35
2.36
2.39
2.39
2.21
2.11
1.99
2.07
?ilte
Box
Temp
(•F)
220
215
205
205
Las
Imp
Gas
Tern
(DF
76
76
7«
79
Sampling
Train
Static
Pressure
("Hg)
4.0
k.a
4.0
4.0
Clayton Environmental Consultants, Inc.
-------
C-51
SAMPLING TRAIN DATA
Ford Motor Company
(Page 4 of 4)
Company:
Source Designation; Coke Battery A Scrubber inlet
7/10/75
Date: _
Teat Number; EPA Method 5 Sample-6
Field Person: ROM
Filter Heater Setting; 250°P
Probe Heater Setting; 250"F
Filter Number; A-190-14
Barometric Pressure ("Hg); 29.33
Stack Static Pressure ("H;0); -4.7
Stack Dimensions: 66" I.P.
Flume Appearance: --
Ambient Temperature("P);
Record all Data Every 0.5
Minutes
Nocsle Number; -- .Dia.(in.); 0.187
Pitot Tube No. 18,Corr.Factor;'o,838
Meter Box Ho. RAC-l'»Corr.Factor; 0.974
Meter Isoklnetlc Factor; 1720
Assumed Moisture(I); 1
Condensate Volume(ml); p
Silica Gel Weight Gatn(g); 14.5
Leak Rate 0.001 CPM at 15.0 "Hg
Trav-
erae
Point
No.
S-4
S-3
S-2
S-l
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
14:24
14:36
14:52
15:05
'
Velocity
pressure
("H20)
1.20
1.40
(1.20)
(1.40)
1.2
1.55
(1.2)
(1.6)
1.15
1.4
(1.2)
(1.4).
0.95
1.2
(0.92)
(1.25)
AVERAGE (TOTAL)
Stack
Temp
(•F)
95
145
(120)
(155)
90
320
(170)
(345)
95
170
(140)
(180)
95
170
(140)
(185)
142
Dry Gas Meter
Volume
(ft3)
550.050
550.781
550.781
551.521
551.523
552.251
552.252
552.919
( 11.977)
Temp(°F)
Inlet
90
91
92
92
87
Outlet
90
90
90
90
86
Orifice L j
PressurefV"1
Differ- _B°XB
ential *«'
("H20) | ( F)
1.77
1.89
1.79
1.63
1.70
1.82
1.41
1.56
1.92
205
210
210
210
213
Last
Imp.
Gas
Temp
CF)
79
79
79
80
76
Sampling
Train
Static
Pressure
("Hg)
4.0
4.0
4.0
4.0
3.6
Clayton Environmental Consultants, Xne,
-------
Company:_
Source Designation:^
Date: 7/14/75"
C-52
SAMPLING TRAIN DATA
Ford Hotor Company
(Page 1 of 4)
Coke Battery A Scrubber Inlet
Test MumbortEPA Method 5 Sample-7
Pleld Person: RCM/FIC
Filter Heater Setting; 250*F
Probe Heater Setting; 250°P
Filter Number; A-190-08
Barometric Pressure ("Hg)t 29.63
Stack Static Pressure <"HgO); -4.5
Stack Dimensions: 66" I.D.
Plume Appearance:
Ambient Temperature (°F) : __.
Record all Data Every 0.5
Nozzle Kumber; -- ,Dta.(in.): 0.187
Pitot Tube No. IB ,Corr.Factor; Q.838
Meter Box Mo. RAG-1»Corr.Factor; 0.974
Meter Isoklnetlc Factor; 1720
Assumed Moisture(I); 1
Condensate Volume(ml); -1
Minutes
Silica Gel Weight Gatn(g); 14,5
Leak Rate O.QQS CFM at 17.0 "Hg
Trav-
erse
Point
No.
T-8
T-7
T-6
T-5
Time
Samp-
ling
(a*c)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
06:40
09:23
09:32
09:50
Velocity
Pressure
("H20)
1.30
1.70
(1.30)
(1.75)
1.40
1.55
(1.35)
(1.55)
1.35
1.75
(0.3)
(1.75)
1.25
1.45
(1.25)
(1.50)
AVERAGE (TOTAL)
Stack
Temp
<*F)
70
170
(80)
(180)
70
130
(65)
(135)
73
340
(95)
(365)
70
190
(75)
(205)
Dry Gas Meter
Volume
(ft3)
554.153
554.922
554.925
555.735
555.737
556.509
556.512
557.272
( )
Temp(-F)
Inle
70
(70)
(70)
78
80
80
Outle
70
(70)
(70)
74
"
80
80
Orifice
Pressure
Differ-
ential
("HzO)
1.95
2.13
2,11
2.09
2.04
1.76
1.90
1.80
Filter
Box
Temp
CF)
195
(195)
(195)
200
200
215
Las
imp
Gas
Temp
(°F
68
(68
(68}
66
68
68
Samplin;
Train
Static
Pressure
("Hg)
3.2
(3.2)
(3.2)
3,2
3.2
3.3
Clayton Environmental Consultants, Inc.
-------
Company:_
Source Designation^
Date: 7/14/75
C-53
SAMPLING TRAIN DATA
Ford Motor Company
(Page 2 of 4)
Coke Battery A Serubbar Inlet
Teat Number; RPA Meyhod 5 Samnle-7
Pield Person: RCM
Filter Number; A-190-08
Barometric Pressure ("Hg); 29.63
Stack Static Pressure <"H;0); -4.5
Stack Dimensions: 66" I.D.
Plume Appearance: --
Filter Heater Setting; 2SO*F
Probe Heater Setting! 25Q°F
Ambient Temperature (°F) : -_-
Record all Data Every 0.5
Notsle Number; -- ,Dia.(in.); 0.187
Pitot Tube No. 18.Corr.Factor; 0.838
Meter Box No. RAC-l.Corr.Factor 0.974
Meter Isokinetic Factor; 1720
Assumed Moisture(X): 1
Condensate Volume(ml); -1
Minutes
Silica Cel Weight Cain(g); 14.5
Leak Rate CFM at "HB
Trav-
erse
Point
No.
T-4
T-3
T-2
T-i
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
10:22
10:33
10:58
11:10
Velocity
Pressure
<"H20)
1.20
1.45
(1.25)
(1.50)
1.20
1.45
(1.20)
(1.45)
1.15
1.35
(1.10)
(1.35).
1.00
1.30
(1.0)
(1.30)
•
AVERAGE (TOTAL)
Stack
Temp
(°P)
65
180
(75)
(190)
62
155
(72)
(155)
70
165
(85)
(175)
67
240
(85)
(245)
Dry Gas Meter
Volume
(ft*)
557.273
558.020
558.023
558.773
558.773.
559.497
559.499
560.183
C )
Temp(°F)
Inle
74
80
80
80
Outlet
72
78
78
80
Orifice
Pressure
Differ-
ential
("HaO)
1.82
1.80
1.85
1.89
1.74
1.73
1.53
1.49
filter
Box
Temp
CF)
215
210
205
205
Las
Imp
Gas
remn
(°F
70
71
72
71
Sampling
Train
Static
Pr e s s u r e
("Hg)
3.5
3.5
3.5
3.5
Clayton Environmental Consultants, Inc.
-------
C-54
SAMPLING TRAIN DATA
Company; Ford Motor Company
(Page 3 of 4)
Source Designation; Coke Battery A Scrubber inlet
7/14/75
Date:
Teat Number; EPA Method 5 Sampie-7
Field person: ROM
Filter Number:
Filter Heater Setting; 250°F
Probe Heater Setting; 250"P
A-190-08
Barometric Pressure ("Hg)t 29.63
Stack Static Pressure ("HgO); -4.5
66" I.D.
Stack Dimensions:_
Plume Appearance: --
Ambient Temperature(*F): --
Record all Data Every 0.5
Hinutes
Nozzle Number; -- ,Dia.(in.);p.187
Pitot Tube No. 18 ,Corr.Factor;0.838
Meter Box No. RAC-IiCorr.FactonQ.974
Meter Isokinetic Factor; 1720
Assumed Moisture (I): i
Condensate Volume (ml): _j.
Silica Gel Weight Gain(g); 14.5
Leak Rate CFM at "Hg
Trav-
erse
Point
No.
S-8
S-7
S-6
S-5
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
12:45
12:55
13:18
13:38
Velocity
Pressure
("H20)
1.45
1.65
(1.45)
(1.70)
1.40
1.55
(1.40)
(1.60)
1.35
1.6
(0.2)
(1.6)
1.25
1.45
(1.30)
(1.50)
•
AVERAGE (TOTAL)
Stack
Temp
(•F)
77
175
( 90)
(185)
80
155
(100)
(180)
80
180
( 90)
(185)
80
250
( 90)
(260)
Dry Gas Meter
Volume
(ft3)
560.186
560.999
561.000
561.770
561.773
562.554
562.555
563.298
( )
Temp("F)
Inlet
80
80
80
80
Outlet
80
80
80
80
Orifice
Pressure
Differ-
ential
("H20)
2.17
2.09
2.08
2.03
2.01
2.01
1.86
1.64
Filter
Box
Temp
(°F)
210
215
200
205
Last
Imp.
Gas
Temp
(°F)
68
66
68
68
Sampling
Train
Static
Pressure
("Hg)
3.5
3.5
3.5
3.5
Clayton Environmental Consultants, Inc.
-------
C-55
SAHPLING TRAIN DATA
Companyi Ford Motor Company
(Page 4 of 4)
Source Designation! Coke Battery A Scrubber Inlet
7/14/75
Date:
Teat Humbert PA Method 5 Sample-7
Field Person: ROM
TllCez Number: A-190-08
Barometric Pressure ("Hg); 29.63
Filter Heater Setting:,
Probe Heater Setting;
250T
250«F
Stack Static Pressure ("H?0); -4.5
Stack Dimensionst 66" I.D.
Pluae Appearance: —
Hocsle Number; -- .Die.(in.);0.187
Pitot Tube Mo. 18 tCorr.Factor ;"0.838
Meter Box No. RAC-LCert.Paeton p.974
Meter Isokinetic Factor; 1720
Assumed Moisture (X): j
Condenaate Volume (ml): _i
Ambient Temperature(*F):
Record all Data Every 0.5
Minutes
Silica Gel Weight Catn(g); 14.5
Leak Rate p.005 CFM at 15.p
"Hg
trav-
erse
Point
Mo.
6-4
S-3
S-2
S-l
Time
Samp-
ling
(•ec}
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
13:47
13:58
14:10
14:24
Velocity
Pressure
("H20)
1.15
1.30
(1.15)
(1.30)
1.15
1,40
(1.15)
(1.45)
1.15
1.35
(1.1)
(1.40)
0.95
1.15
(0.98)
(1.1)
AVERAGE (TOTAL)
Stack
Temp
CF)
80
170
( 85)
(185)
80
210
( 85)
(220)
75
180
( 95)
(195)
83
100
( 95)
(100)
130
Dry Gas Meter
Volume
(ft3)
563.300
564.021
564.022
564.735
564.737
565.474
565.475
566.146
C 11.654)
TempCF)
Inle
80
80
80
80
79
Outlet
80
80
80
80
78
Orifice
Pressure
Differ.
ential
("H20)
1.71
1.66
1.71
1.68
1.73
1.70
1.41
1.51
1.83
filter
Box
Temp
CF)
215
215
215
215
208
Last
Imp.
Gas
Temp
CF)
70
72
73
72
69
Sampling
Train
Static
Pressure
("Hg)
3.8
3.8
4.0
4.0
3.5
Clayton Environmental Consultants, Inc.
-------
C-56
SAMPLING TRAIN DATA
Ford Motor Company
Company j
Source Designation; Coka Battary A Scrubber inlet
(Page 1 of 4)
7/13/75
Date:
Teat Humbert EPA Method 5 Sample-8
Field Peraon: FIC/GMS
Filter Heater Setting; 230°P
Probe Heater Setting; 230°g
Filter Number; A-190-01
Barometric Pressure ("Hg); 29.60
Stack Static Pressure ("H,0); -4.5
Stack Dimensions ;J 66" I.D.
Plume Appearance: --
Ambient Temperature(*F);
Nocile Number;., .Dia.(in.); 0.187
Pitot Tube No. 18 .Corr.Factor;o.838
Meter Box No. RAC-IiCorr.Factor; Q.974
Meter Isokinetic Factor; 1720
Assumed Moisture (Z): i
Condensate Volume (ml): -1
Silica Gel Weight Cain(g); 17.6
Record all Data Every 0.5 Minutes Leak Rate
70
140
(120)
(140)
80
130
(130)
(140)
80
260
(110)
(270)
110
180
(110)
(180)
Dry Gas Meter
Volume
(ft3)
566.482
566.9
567.426
567.426
567.8
568.248
568.248
568.6
569.050
569.050
569.3
569.777
( )
Temp('F)
Inlet
74
74
(74)
84
84
(84)
94
94
(94)
94
94
(94)
Outlet
72
72
(72)
76
76
(76)
84
84
(84)
84
84.
(84)
[Orifice
Pressure
{Differ-
ential
(MH20)
2.0
2.1
(2.0)
2.0
2.1
(2.1)
1.6
1.7
(1.6)
1.5
1.6
(1.6)
Filter
Box
Temp
CF)
250
250
(250)
250
250
(250)
250
250
(250)
250
250
(250)
Last
Imp.
GSi
Temp
CF>
68
68
(68)
68
68
(68)
68
68
(68)
68
68
(68)
Sampling
Train
Static
Pressure
("Hg)
Clayton Environmental Consultants, Inc.
-------
C-57
SAMPLING TRAIN DATA
Companyt Ford Motor Company
(Page 2 of 4)
Source Designation! Coke Battery A Scrubber Inlet
Date: 7/15/75
Filter Heater Setting.; 2SO*F
Test Number; EPA Method 5 Sample-8
Field Person! FIG/CMS
Filter Number: A-190-01
Barometric Pressure ("Hg); 29.60
Stack Static Pressure ("H?0); -4.5
Stack Dimensions: 66" I.D.
Plume Appearance: --
Ambient Temperature(*F):
Record all Data Every
Probe Heater Setting; 250°F
Noccle Number; — .Dia,(in.);0.187
Pitot Tube No. 18 ,Corr.Factor;Q.836
Meter Box No. RAC-liCorr.Factor; 0.974
Meter Isokinetic Factor: 1720
Assumed Moisture (X): ],
Condensate Volume (ml): -1
Silica Gel Weight Gain(g); 17.6
0.5 Minutes Leak Rate
CFM at
"Hg
Trav-
erse
Point
No.
T-4
T-3
T-2
T-l
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
09:58
10:54
11:04
11:25
Velocity
Pressure
<"H20)
1.1
1.4
(1.1)
(1.4)
1.1
1.6
(1.2)
(1.6)
1.1
1.5
(1.3)
(1.5.)
1.0
1.2
(1.1)
(1.2)
AVERAGE (TOTAL)
Stack
Temp
(°F)
80
140
(110)
(140)
90
200
( 90)
(220)
90
240
(120)
(240)
90
190
(100)
(190]
Dry Gas Meter
Volume
72
72
76
76
(76]
76
76
(76]
Sampling
Train
Static
Pressure
("HR)
2.2
2.2
Clayton Environmental Consultants, Inc.
-------
C-58
SAHPLINC TRAIN DATA
Company; Ford Motor Company
(Page 3 of 4)
Source Designation; Coke Battery A Scrubber Inlet
7/15/75
Date:
Teat Number; EPA Method 5 Sample-8,
Field Person; FIC/GMS
Filter Number: A-190-01
Barometric Pressure ("Hg); 29.60
Stack Static Pressure
Stack Dimensions; 66" I.D.
Plume Appearance: -
Filter Heater Setting:
Probe Heater Setting:
250°F-
25Q°F
: -4.5
Nozzle Number; — .Dia.(in.);0.187
Pitot Tube No.18 ,Corr.Factor; 0.838
Meter Box No. RAC-I,Corr.Factor; 0.974
Meter Isokinetic Factor; 1720
Assumed Moisture(1): 1
Condensate Volume (ml): -1
Ambient Temperature(°F):
Record all Data Every Q.5
Minutes
Silica Gel Weight Gain(g); 17.6
Leak Rate CFM at "Hg
Trav-
erse
Point
No.
S-8
S-7
S-6
S-5
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Clock
11:40
11:56
13:00
13:25
1
Velocity
Pressure
("H20)
1.4
1.9
(1.3)
(1.9)
1.5
1.8
(1.5)
(1.8)
1.4
1.5
(1.4)
1.1
1.4
(1.3)
AVERAGE (TOTAL)
Stack
Temp
(°F)
90
190
(110)
(190)
90
220
(110)
(220)
90
150
(110)
90
220
(120)
Dry Gas Meter
Volume
(ft3)
572.620
573.0
573.362
573.362
573.8
574.188
574.188
574.5
574.963
574.963
575.3
575.732
( )
Temp(°F)
Inlet
100
100
aoo)
100
100
(100)
100
100
(100)
100
100
(100)
Outlet
94
96
(94)
94
94
(94)
98
98
(98)
98
98
(98)
Orifice
Pressure
Differ-
ential
("H20)
1.9
2.0
(1.8)
2.1
2.8
(2.3)
2.1
2.2
(2.1)
1.6
1.7
(1.6)
Filter
Box
Temp
(°F)
250
250
(250)
250
250
(250)
250
250
(250)
250
200
(250)
Last
Imp.
Gas
Temp
(°F)
76
76
W
76
76
(76)
76
76
(76)
76
76
(76)
Sampling
Train
Static
Pressure
("Hg)
2.2
2.4
2.4
2.4
Clayton Environmental Consultants, Inc.
-------
C-59
SAMPLING TRAIN DATA
Conpony; Pord Motor Company
(Page 4 of 4)
Source Designation:
Date: 7/15/75
Coke Battery A Scrubber Inlet
Teat Number;EPA Method 5 Sample-8..
Field Person; FIC/GMS
Filter Number; A-190-01
Barometric pressure ("Hg)t 29.60
Stack Static Pressure ("H;0); -4.5
Stack Dimensions; 66" I.D.
Plume Appearance: --
Filter Heater Setting; 250"F
Probe Heater Setting; 250°F
Noisle Number; -- .Dla.(In.);Q.187
Pltot Tube Me.18 .Corr.Factor;p.838
Meter Box No. RAG-1,Corr.Factor: 0.974
Meter Isoklnetlc Factor; 1720
Assumed Moisture(I); 1
Condensate Volume(ml); -1
Ambient Temperature(°F):
Silica Gel Weight Caln(g); 17.6
Record all Data Every 0.5 Minutes Leak Rate<0-005_ CFM at
"Hg
Trav-
erse
Point
No.
S-4
S-3
S-2
S-l
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
13:33
13:45
14:04
14:09
'
Velocity
Pressure
("H20)
1.1
1.5
(1.2)
(1.5)
1.1
1.5
(1.2)
(1.5)
1.1
1.4
(1.1)
(1.4.)
0.85
1.0
(0.90)
(1.1)
•
AVERAGE (TOTAL)
Stack
Temp
(°F)
90
220
(110)
(240)
90
220
(110)
(220)
100
240
(100)
(240)
100
210
(110)
(210)
143
Dry Gas Meter
Volume
(£t3)
575.733
576.0
576.480
576.480
576.8
577.180
577.180
577.5
577.890
577.890
578.1
578.544
•
< 11.747 )
Temp(°F)
Inlet
100
100
(100)
104
104
<104?
104
104
(104)
104
104
(104>
96
Outlet
98
98
(98)
100
100
£iqoj
100
100
(100)
100
100
(100)
92
Orifice
Pressure
Differ-
ential
("H20)
1.6
1.7
(1.6)
1.6
1.7
(1.6)
1.6
1.7
(1.6)
1.2
1.3
(1.2)
1.8
filter
Box
Temp
(°F)
250
250
(250)
250
250
(250)
250
250
(250)
250
200
(250)
245
Last
Imp.
Gas
Temp
CF)
81
81
(81)
81
81
(81)
81
81
<81)
81
81
(81)
75
Sampling
Train
Static
Pressure
("Hg)
2.4
2.4
2.3
Clayton Environmental Consultants, Inc.
-------
C-60
SAMPLING TRAIN DATA
Company; Ford Motor Company
(Page 1 of 4)
Source Designation:^
Date: 7/16/75
Coke Battery A Scrubber Inlet
Teat Number;EPA Method 5 Samole-9
Pleld Person; PIC/GMS
Pilter Number:
Pilter Heater Setting; 250°F
Probe Heater Setting; 250°P
A-190-12
Barometric Pressure ("Hg): 29.60
Stack Static Pressure ("HgO); -4.5
Stack Dimensions:_
Plume Appearance:
66" I.D.
Nozzle Number; -, ,Dia.(in.);Q.187
Pltot Tube No. 18 ,Corr.Factor; 0.838
Meter Box No. RAC-l.Corr.Factor; 0.974
Meter Isoklnetlc Factor; 1720
Assumed Moisture(Z): 1
Condensate Volume (ml): -1
Ambient Temperature(°F):
Silica Gel Weight Galn(g); 16
Record all Data Every 0.5 Minutes Leak Rate
CFM at
"Hg
Trav-
erse
Point
No.
T-8
T-7
T-6
T-5
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
08:24
08:40
08:53
09:34
Velocity
Pressure
("H20)
1.05
1.3
(1.1)
(1.3)
1.4
1.5
(1.4)
(1.6)
1.3
1.6
(1.5)
(1.6) .
1.3
1.5
(1-2)
(1.5)
•
AVERAGE (TOTAL)
Stack
Temp
<«F)
70
160
(100)
(160)
80
150
(110)
(160)
90
300
(100)
(420)
80
220
(120)
(220)
Dry Gas Meter
Volume
(ft3)
578.956
579.3
579.700
579.700
580.1
580.500
580.500
580.8
581.271
581.271
581.6
582.05
( )
Temp(°F)
Inlet
80
80
(80)
86
86
(86)
90
90
(90)
94
94
(94)
Outlet
80
80
(80)
85
85
(85)
88
88
(88)
92
92
(92)
Orifice
Pressure
Differ-
ential
("H20)
1.5
1.6
(1.5)
2.1
2.2
(2.1)
1.9
1.8
(1.9)
2.0
2.1
(2.0)
Filter
Box
Temp
CF)
250
250
(250)
250
250
(250)
250
250
(250)
250
250
(250)
Last
Imp.
Gas
Temp
(°F)
68
68
(68)
68
68
(68)
• •
68
68
(68)
68
68
(68)
Sampling
Train
Static
Pressure
("Hg)
2.8
2.8
2.4
Clayton Environmental Consultants, Inc.
-------
Company:
Source Designation:
Date: 7/16/75
C-61
SAMPLING TRAIN DATA
Ford Motor Company
(Page 2 of 4)
Coke Battery A Scrubber Inlet
Teat Number;EPA Method 5 Sample.9
Field Person: PIC/GMS
Filter Number:
Filter Heater Setting; 250'F
Probe Heater Setting; 250*F
A-190-12
Barometric Preaaure ("Hg); 29.60
Stack Static Pressure ("HgO); -4.5
Stack Dimensions; 66" I.D.
Plume Appearance: --
Ambient Temperature(°P):
Record all Data Every 0.5
Minutes
Noccle Number; -- .Dia.(in.);0.187
Pitot Tube No. 18,Corr.Faetort0.838
Meter Box No. RAC-I.Corr.Factor 0.974
Meter laokinetic Factor; 1720
Assumed Moisture (X): 1
Condenaate Volume (ml): -I
Silica Gel Weight Galn(g); 16
Leak Rate CFM at "Hg
rrav-
erae
Point
No.
T-4
U-3
T-2
T-l
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
09:41
09:52
10:06
10:35
(Telocity
Preaaure
("H20)
1.3
1.4
(1.3)
1.3
1.4
(1.3)
1.05
1.2
(1.1)
(1.2)
0.85
1.2
(0.9)
(1.2)
•
AVERAGE (TOTAL)
Stack
Temp
(°F)
290
220
( 90)
90
200
(120)
90
190
(100)
(190)
90
160
(110)
(160)
Dry Gas Meter
Volume
(ft3)
582.05
582.4
582.81
582.81
583.1
583.579
583.579
583.9
584.27
584.27
584.5
584.91
•
( )
TempCF)
Inlet
96
96
(96)
98
98
(98)
100
100
(100)
104
104
(104]
Outlet
96
96
(96)
98
98
(98)
99
99
(99)
100
100
(100)
Orifice
Pressure
Differ-
ential
("H20)
1.8
1.9
(1.8)
1.8
1.9
(1.8)
1.5
1.6
(1.5)
1.2
1.3
(1.2)
filter
Box
Temp
CF)
250
250
(250)
250
250
(250)
250
250
(250)
250
250
(250)
Last
Imp.
Gas
Temp
CF>
70
70
(70)
70
70
[Sampling
Train
Static
Pressure
("Hg)
2.8
2.8
(70)|
70
70
2.6
(7oJ
70
70
(70)
2.4
Clayton Environmental Consultants, Inc.
-------
C-62
SAMPLING TRAIN DATA
Company; Ford Motor Company
(Page 3 of 4)
Source Designation; Coke Battery A Scrubber Inlet
7/16/75
Date: _
Test Number;EPA Method 5 Sample-9
Field Person: FIC/GMS
Filter Number: A-190-12
Barometric Pressure ("Hg); 29.60
Stack Static Pressure ("H20) :_-4J_5_
Stack Dimensions: 66" I.D.
Plume Appearance:
Filter Heater Setting:
Probe Heater Setting:
250'F
230°F
Ambient Temperature(8F) :
Record all Data Every 0.5
Minutes
Nozzle Number; — ,Dia.(in.); 0.187
Pitot Tube No. 18 ,Corr.Factor; 0.838
Meter Box No. RAC-liCorr.Factor; 0.974
Meter Isokinetic Factor; 1720
Assumed Moisture (1): 1
Condensate Volume (ml): -1
Silica Gel Weight Gain(g); 16
Leak Rate CFM at "Hg
Trav-
erse
Point
No.
S-8
S-7
S-6
S-5
Time
Samp-
ling
<8ec?
0
30
60
Max
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
10:50
11:09
11:23
11:37
Velocity
Pressure
("H20)
1.2
1.9
(1.3)
(1.9)
1.4
1.5
(1.5)
(1.5)
1.2
1.3
(1.2)
(1.2)
1.1
1.35
(1.1)
AVERAGE (TOTAL)
Stack
Temp
<°F>
90
>600
(130)
(>600)
100
210
(110)
(210)
100
210
(HO)
(220)
100
210
(110)
(210)
Dry Gas Meter
Volume
(ft3)
584.91
585.65
585.65
585.9
586.3
586.3
586.8
587.05
587.05
587.76
( )
Temp(°F)
Inlet
102
102
(102)
102
102
(102)
102
102
(102)
102
102
(102)
Outlet
100
100
(100)
100
100
(100)
100
100
(100)
100
100
(100)
Orifice
Pressure
Differ-
ential
("H20)
1.5
1.6
(1.5)
2.0
2.1
(2.0)
1.7
1.8
(1-7)
1.65
1.7
(1.65]
?iiter
Box
Temp
CF)
250
250
(250)
250
250
(250)
250
250
(250)
250
250
(250)
Last
Imp.
Gas
Temp
(•*)
76
76
(76)
76
76
(76)
76
76
(76)
76
76
(76)
Sampling
Train
Static
Pressure
("HR)
2.4
2.4
2.4
2.4
Clayton Environmental Consultants, Inc.
-------
Companyt
Source Designation^
Date: 7/16/75
C-63
SAMPLING TRAIN DATA
Ford Motor Company
(Page 4 of 4)
Coke Battery A Scrubber Inlet
Teat Humbert EPA Method 5 Sample-9.
Field Person: FIC/GMS
Filter Number:
Filter Heater Setting; 250'F
Probe Heater Setting; 250"F
A-190-12
Barometric Pressure ("Hg); 29.60
Stack Static Pressure ("HgO); -4.5
Stack Dimensions:_
Plume Appearance:
66" I.D.
Ambient Temperature (°F):
Record all Data Every
Nocsle Number; __ ,Dia.(in.); Q.187
Pitot Tube No. iSiCorr.Factor;p'.838
Meter Box No. RAG-1.Corr.Factor; 0.974
Meter Isokinetic Factor; 1720
Assumed Moisture (1): j
Condensate Volume (ml): -1
Silica Gel Weight Gain(g): 16
0.5 Minutes Leak Rate
-------
C-64
SAMPLING TRAIN DATA
Company; Ford Motor Company
(Page 1 of 5)
Source Designation! Coke Battery A Scrubber Outlet
6/24/75
Date:
Test Numbert EPA Method 5 Sample-1
Field Person: RJG
Filter Number; A-147-24
Barometric Pressure ("Hg); Ayg. 29.78
Stack Static Pressure ("H;0); -0.21
Stack Dimensions; 90" I.D.
Plume Appearance: --
Filter Heater Setting:
Probe Heater Setting:
250
75
Ambient Temperature(°F):
Record all Data Every 0.5
Minutes
NoBzle Number; -- ,Dia.(in.);Q.256
Pitot Tube No. 19.Corr.Factor; 0.854
Meter Box No. RAC-4.Corr.Factor; 0.991
Meter Isokinetic Factor; 1685
Assumed Moisture(Z):
Condensate Volume (ml): 2
Silica Gel Weight Gain(g):_
Leak Rate CFM at
16
"Hg
Trav-
erse
Point
No.
E-6
E-5
E-4
E-3
E-2
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
0
30
60
0
30
60
Clock
09:43
10:36
10:52
11:03
11:17
Velocity
Pressure
("H20)
0.35
0.35
0.33
0.33
0.27
0.27
0.23
0.23
0.18
0.18
•
AVERAGE (TOTAL)
Stack
Temp
(°F>
124
130
125
136
125
127
124
127
125
126
Dry Gas Meter
Volume
(ft3)
657.919
658.616
658.663
659.347
659.356
660.004
660.024
660.597
660.606
661.128
( )
Temp(°F)
Inlet
78
78
84
84
85
85
85
85
85
85
Outlet
78
78
84
84
85
85
85
85
85
85
Orifice
Pressure
Differ-
ential
("H20)
1.61
1.57
1.54
1.50
1.27
1.26
1.07
1.07
0.84
0.84
Filter
Box
Temp
CF)
245
245
260
260
245
245
230
230
275
275
Last
Imp.
Gas
Temp
(•F)
82
82
82
82
88
88
88
88
88
88
Sampling
Train
Static
Pressure
("Hg)
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
Clayton Environmental Consultants, Inc.
-------
C-65
SAMPLING TRAIN DATA
Company; Ford Motor Company
(Page 2 of 5)
Source Designation:.
Date: 6/24/75
Coke Battery A Scrubber Outlet
Teat Number;EPA Method 5 Sample-1
Field Person; RJG
Filter Heater Setting; 250
Probe Heater Setting; 75
Filter Number: A-147-24
Barometric Pressure ("Hg); Avg.29.78
Stack Static Pressure ("H;0); .0.21
Stack Dimensions! 90" I.D.
Plume Appearance:
Ambient Temperature(°F):
Record all Data Every 0.5 Minutes Leak Rate
Noccle Number; -- .Dia.(in.);0.256
Pitot Tube No. 19 • Corr.Factor;' 0.854
Meter Box No. RAC-4, Corr.Factor; 0.991
Meter Isokinetic Factor: 1685
Assumed Moisture(X):
Condensate Volume (ml): 2
Silica Gel Weight Gain(g):
16
CFM at
"Hg
Trav-
erse
Point
No.
B-l
N-6
N-5
N-4
N-3
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
0
30
60
0
30
60
Clock
11:32
11:46
11:58
13:30
13:40
*
Velocity
pressure
("H20)
0.16
0.16
0.68
0.68
0.77
0.77
0.76
0.76
0.65
0.65
•
AVERAGE (TOTAL)
Stack
Temp
(°F)
125
125
125
130
125
145
126
125
126
124
-
Dry Gas Meter
Volume
Temp(T)
Inlet
84
84
85
85
86
86
86
86
88
88
Outlet
84
84
85
85
86
86
86
86
88
88
Orifice
Pressure
Differ-
ential
("H20)
0.74
0.74
3.17
3.12
3.59
3.50
3.55
3.55
3.04
3.04
filter
Box
Temp
<°F)
275
275
265
265
265
265
275
275
260
260
Last
Imp.
Gas
Temp
(°P>
90
90
92
92
92
92
96
96
92
92
Sampling
Train
Static
Pressure
("Hg)
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
Clayton Environmental Consultants, Inc.
-------
C-66
SAMPLING TRAIN DATA
Company; Ford Motor Company
(Page 3 of 5)
Source Designation; Coke Battery A Scrubber Outlet
6/24/75 - 6/25/75
Date:
Test Number;EPA Method 5 Sample-1
Field Person: RJG/GMS
Filter Heater Setting:
Probe Heater Setting:
250
75
Filter Number; A-147-24
Barometric Pressure ("Hg); Ava. 29.78
Stack Static Pressure ("H?0); -0.21
Stack Dimensions: 90" I.D.
Plume Appearance: --
Ambient Temperature(°F); --
Record all Data Every 0.5
Minutes
Nozzle Number;-- .Dla.(In.); 0.256
Pltot Tube No.19 .Corr.Factort 0.854
Meter Box No. RAC-4iCorr.Factor 0.991
Meter Isoklnetlc Factor: 1685
Assumed Moisture(Z):
Condensate Volume (ml): 2
Silica Gel Weight Galn(g):
Leak Rate CFM at
16
"Hg
Trav-
erse
Point
No.
N-2
6/25
N-l
W-6
W-5
W-4
Time
Samp-
ling
(sec )
0
30
60
0
30
60
0
30
60
0
30
60
0
30
60
Clock
14:26
09:46
10:05
10:18
10:29
Velocity
Pressure
("H20)
0.60
0.60
0.41
0.41
0.61
0.61
0.70
0.70.
0.68
0.68
AVERAGE (TOTAL)
Stack
Temp
CF)
125
124
125
125
135
135
130
140
120
120
Dry Gas Meter
Volume
(ft3)
665.794
666.729
^
666.751
667.488
667.488
668.345
668.345
669.166
669.166
670.098
( )
Temp("F)
Inlet
84
84
80
80
70
70
70
70
70
70
Outlet
84
84
80
80
70
70
70
70
70
70
Orifice
Pressure
Differ-
ential
("H20)
2.79
2.79
1.89
1.89
2.6
2.6
2.7
3.1
3.1
3.1
filter
Box
Temp
CF)
270
270
250
250
270
270
274
274
275
275
Last
Imp.
Gas
Temp
(°F)
74
74
70
70
70
70
75
75
76
76
Sampling
Train
Static
Pressure
("Hg)
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
Clayton Environmental Consultants, Inc.
-------
C-67
SAMPLING TRAIN DATA
Companyt Ford Motor Company
(Page 4 of 5)
Source Deiignation; Coke Battery A Scrubber Outlet
6/25/75
Date:
Teat Number SPA Method 5 Sample-l
Field Person: RJG/GM8
Filter Heater Setting:
Probe Heater Setting:
250
75
Filter Number; A-147-24
Barometric Pressure ("Hg);Avg. 29.78
Stack Static Pressure ("H?0): -0.21
Stack Dimensions; 90" I.D.
Plume Appearance: --
Ambient Temperature (°F) : __.
Record all Data Every 0.5
Minutes
NocEle Number; -- .Dla.(in.);0.256
Pitot Tube No. 19 ,Corr.Factor;'p.854
Meter Box No. RAC-4»Corr.Factor; p.991
Meter Isokinetic Factor; 1685
Assumed Moisture(X):
Condensate Volume (ml): 2
Silica Gel Weight Gain(g):
Leak Rate CFM at
16
"Hg
Trav-
erse
Point
No.
tf-3
W-2
W-l
S-6
S-5
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
0
30
60
0
30
60
Clock
10:40
12:53
13:10
13:32
13:42
Velocity
Pressure
("H20)
0.68
0.68
0.55
0.55
0.40
0.40
0.32
0.32
0.30
0.30
•
AVERAGE (TOTAL)
Stack
Temp
(°F)
140
140
155
135
140
130
140
140
130
125
-
Dry Gas Meter
Volume
(ft3)
670.098
671.044
671.044
671.873
671.873
672.572
672.572
673.216
673.216
673.811
( )
Temp(°F)
Inlet
70
70
75
75
75
75
75
75
75
75
Outlet
70
70
75
75
75
75
75
75
75
75
Orifice
Pressure
Differ.
ential
<"H20)
3.0
3.0
2.3
2.0
1.6
1.6
1.4
1.4
1.1
1.3
filter
Box
Temp
CF)
250
250
270
270
250
250
250
250
250
250
Last
Imp.
Gas
Temp
<°FJ
77
77
78
78
81
81
81
81
82
82
Sampling
Train
Static
Pressure
("Hg)
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
Clayton Environmental Consultants, Inc.
-------
C-68
SAMPLING TRAIN DATA
Ford Motor Company
Company:
Source Designation; Coke Battery A Scrubber Outlet
(Page 5 of 5)
6/25/75
Date:
Test Number;EPA Method 5 Sample-1
Field Person; TRJ/GMS
Filter Heater Setting; 250
Probe Heater Setting; 75
Filter Number: A-I47-24
Barometric Pressure ("Hg); Avg. 29.78
Stack Static Pressure ("H20):
Stack Dimensions:_
Plume Appearance:
90" I.D.
Ambient Temperature (°F) : -_.
Record all Data Every 0.5
Minutes
Nozzle Number;-- ,Dia.(in.);0.256
Pitot Tube No. 19 .Corr.Factor; 0.854
Meter Box No. RAC-4,Corr.Factor; 0.991
Meter Isokinetic Factor; 1685
Assumed Moisture(X):
Condensate Volume(ml); 2
Silica Gel Weight Gain(g):
Leak Rate CFM at
16
"Hg
Trav-
erse
Point
No.
S-4
S-3
S-2
S-l
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
0
30
60
Clock
13:53
14:03
14:17
14:28
Velocity
Pressure
("H20)
0.25
0.25
0.20
0.20
0.15
0.15
0.15
0.15
.
AVERAGE (TOTAL)
Stack
Temp
(«F)
125
145
135
130
140
165
130
125
131
Dry Gas Meter
Volume
-------
C-69
SAMPLING TRAIN DATA
Company; Ford Motor Company
(Page 1 of 5)
Source Designation:
Coke Battery A Scrubber Outlet
6/26/75
Date: m
Teat Number; EPA Method 5 Sample-2
Field Person: RJG/GMS
Filter Number: A-147-32
Barometric Pressure ("Hg); Avg. 29.54
Stack Static Pressure ("HgO); -0.21
Stack Dimensions; 90" I.D.
Plume Appearance: --
Filter Heater Setting; 250
Probe Heater Setting: 75
Ambient Temperature(°F) : •
Record all Data Every 0.5
Minutes
Nocile Number; — ,Dia.(in.); 0.256
Pitot Tube No.19 ,Corr.Factor; 0.854
Meter Box No. RAC-4iCorr.Factor; 0.991
Meter Isoklnetic Factor; 1685
Assumed Moisture(1):
Condensate Volume (ml): 2
Silica Gel Weight Gain(g):
Leak Rate CFM at
1B.S
"Hg
Trav-
erse
Point
No.
E-6
B-5
E-4
E-3
"
E-2
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
0
30
60
0
30
60
Clock
09:25
10:16
10:39
10:49
11:02
'
Velocity
Pressure
("H20)
0.40
0.40
0.33
0.33
0.28
0.28
0.22
0.22
0.18
0.18
•
AVERAGE (TOTAL)
Stack
Temp
(°F)
123
•
125
126
130
120
125
125
120
123
124
•
Dry Gas Meter
Volume
(ft3)
676.022
676.738
676.780
677.458
677.474
678.135
678.149
678.726
678.733
679.292
•
. .
Temp(°F)
Inlet
70
70
72
72
74
74
76
76
78
78
Outlet
70
70
72
72
74
74
76
76
78
78
Orifice
Pressure
Differ-
ential
("H20)
1.75
1.75
1.50
1.48
1.28
1.28
1.01
1.00
0.83
0.83
(filter
Box
Temp
CF)
250
250
200
200
255
255
280
280
235
235
Last
Imp.
Gas
Temp
CF)
75
75
80
80
78
78
77
77
76
76
Sampling
Train
Static
Pressure
("Hg)
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
Clayton Environmental Consultants, Inc.
-------
C-70
SAMPLING TRAIN DATA
Ford Motor Company
Company:
Source Designation; Coke Battery A Scrubber Outlet
Date: 6/26/75 Filter Heater Setting:
Test Number; EPA Method 5 Sample-2 Probe Heater Settlng:_
Field Person: RJG/GMS
(Page 2 of 5)
250
75
Filter Number: A-147-32
Barometric Pressure ("Hg):Avg. 29.54
Stack Static Pressure C^O): -0.21
Stack Dimensions: 90" I.D.
Plume Appearance: --
Ambient Temperature(°F):
Noccle Number; — .Dia.(In.); 0.256
Pltot Tube No. 19.Corr.Factor; 0.854
Meter Box No. RAC-4,Corr.Factor; 0.991
Meter Isoklnetlc Factor; 1665
Assumed Moisture(I):
Condensate Volume (ml): 2
Silica Gel Weight Gain(g):
18.5
Record all Data Every 0.5 Minutes Leak Rate
CFM at
"Hg
Trav-
erse
Point
No.
E-l
N-6
N-5
N-4
N-3
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
0
30
60
0
30
60
Clock
11:25
11:39
12:55
13:10
13:32
Velocity
Pressure
("H20)
0.16
0.16
0.73
0.73
0.83
0.83
0.78
0.78
0.70
0.70
•
AVERAGE (TOTAL)
Stack
Temp
(°F)
120
120
122
122
126
145
130
130
130
125
Dry Gas Meter
Volume
(ft3)
679.305
679.800
679.800
680.804
680.831
681.869
681.885
682.912
682.920
683.916
( )
Temp(°F)
Inlet
80
80
78
78
78
78
78
78
79
79
Outlet
80
80
78
78
78
78
78
78
79
79
Orifice
Pressure
Differ-
ential
("H20)
0.75
0.75
3.36
3.36
3.82
3.75
3.56
3.56
3.17
3.22
filter
Box
Temp
(°F)
280
280
255
255
210
210
220
220
265
265
Last
Imp.
Gas
Temp
(°F)
82
82
82
82
82
82
84
84
88
88
Sampling
Train
Static
Pressure
("Hg)
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
Clayton Environmental Consultants, Inc.
-------
C-71
SAMPLING TRAIN DATA
(Page 3 of 5)
Company; Ford Motor Company
Source Designation:
Date: 6/26/75
Coke Battery A Scrubber Outlet
Teat Number;EPA Method 5 SampIe-2
Field Person: RJG/GMS
Filter Heater Setting: 250
Probe Heater Setting: 75
Filter Number: A-147-32
Noetic Number; -- ,Dia.(in.); 0.256
Pitot Tube No. 19 .Corr.Factor; '0.854
Barometric Pressure ("Hg); Avg. 29.54 Meter Box No. RAC-4* Corr.Factor; 0.991
Stack Static Pressure ("H?0); -0.21 Meter Isoklnetic Factor; 1685
Stack Dimensions; 90" I.D. Assumed Moisture (X):
Plume Appearance: -^
Ambient Temperature(°F):
Condensate Volume (ml): 2
Silica Gel Weight Cain(g); ia.5
Record all Data Every 0.5 Minutes Leak Rate
CFM at
HHg
Trav-
erse
Point
No.
N-2
N-l
W-6
W-5
W-4
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
0
30
60
0
30
60
Clock
13:37
13:45
14:08
14:38
14:58
'
(Telocity
Pressure
("H20)
0.58
0.58
0.42
0.42
0.62
0.62
0.70
0.70
0.76
0.76
AVERAGE (TOTAL)
Stack
Temp
(°F)
126
126
125
126
130
130
125
130
123
126
•
Dry Gas Meter
Volume
(ft3)
683.933
684.850
684.858
685.645
685.661
686.600
686.648
687.646
687.682
688.720
•
( )
Temp("F)
Inlet
80
80
80
80
80
80
80
80
80
80
Outlet
80
80
80
80
80
80
80
80
80
80
Orifice
Pressure
Differ-
ential
("H20)
2.68
2.68
1.94
1.94
2.83
2.83
•
3.23
3.20
3.50
3.50
filter
Box
Temp
(°F)
240
240
255
255
255
255
250
250
200
200
Last
Imp.
Gas
Temp
CP)
84
84
82
82
83
83
80
80
83
83
Sampling
Train
Static
pressure
("Hg)
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
Clayton Environmental Consultants, Inc.
-------
C-72
SAMPLING TRAIN DATA
Company; Ford Motor Company
(Page 4 of 5)
Source Designation; Coke Battery A Scrubber Outlet
Date: 6/26/75 - 6/27/75 Filter Heater Setting; 250
Probe Heater Setting:
75
Teet Number;EPA Method 5 Sample-2
Field Person: RJG/GMS
Filter Number; A-147-32
Barometric Pressure ("Hg); Avg. 29.54 Meter Box No. RAC-4.Corr.Factor; Q.991
Stack Static Pressure ("HgO); -0.21 Meter Isokinetic Factor; 1685
Stack Dimensions: 90" I.D.
Plume Appearance: --
Noccle Number; -- .Dia.(in.);Q.2S6
Pitot Tube No. 19 .Corr.Factor; 0,854
Assumed Moisture(Z):
Ambient Temperature(°F):
Record all Data Every Q.5
Condensate Volume (ml): 2
: Silica Gel Weight Gain(g); 18.5
Minutes Leak Rate CPM at "Hg
Trav-
erse
Point
No.
W-3
6/27
W-2
W-l
S-6
«
S-5
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
0
30
60
0
30
60
Clock
15:04
10:40
11:08
11:20
11:58
Velocity
Pressure
("H20)
0.70
0.70
0.62
0.62
0.45
0.45
0.36
0.36
0.27
0.27
AVERAGE (TOTAL)
Stack
Temp
(°F)
125
125
126
125
130
130
137
132
142
128
Dry Gas Meter
Volume
(ft3)
688.730
689.737
-
690.036
690.996
690.996
691.793
691.793
692.486
692.486
693.013
( )
Temp(°F)
Inlet
82
82
75
75
76
76
80
80
80
80
Outle t
82
82
75
75
76
76
80
80
80
80
Orifice
Pressure
Differ-
ential
("H20)
3.24
3.24
2.8
2.8
2.1
2.1
1.6
1.6
1.2
1.2
Filter
Box
Temp
(°F)
240
240
235
235
240
240
235
235
225
225
Last
Imp.
Gas
Temp
(°F)
84
84
80
80
80
80
82
82
85
85
Sampling
Train
Static
Pressure
("Hg)
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
Clayton Environmental Consultants, Inc.
-------
C-73
SAMPLING TRAIN DATA
Company; Ford Motor Company
(Page 5 of 5)
Source Designation: Coke Battery A Scrubber Outlet
6/27/75
Date:
Teat Number; EPA Method 5 Sample-2
Field Person: CMS
Filter Heater Setting:
Probe Heater Setting:
250
75
Filter Number: A-147-32
Barometric Pressure ("Hg); AVK. 29.54
Stack Static Pressure ("^0); -0.21
Stack Dimensions; 90" I.D.
Plume Appearance: --
Ambient Temperature(°F);
Record all Data Every
0.5
Minutes
Noicle Number; -- .Dia.(in.); 0.256
Pitot Tube No. 19 .Corr.Factor; 0.854
Meter Box No. RAC-4.Corr.Factor; 0.991
Meter Isokinetic Factor; 1685
Assumed Moisture(X) :
Condensate Volume (ml): 2
Silica Gel Weight Gain(g):_
Leak Rate CFM at
18.5
"Hg
Frav-
erse
Point
No.
S-4
S-3
S-2
S-l
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
0
30
60
Clock
13:25
13:40
14:05
14:24
'
Velocity
Pressure
("H20)
0.26
0.26
0.21
0.21
•
0.19
0.19
0.15
0.15
•
AVERAGE (TOTAL)
Stack
Temp
(°F)
125
124
130
128
130
125
125
142
127
Dry Gas Meter
Volume
(ft3)
693.013
693.615
693.615
694.168
694.168
694.677
694.677
695.158
( 18.392)
Temp(°F)
Inlet
80
80
80
80
82
82
82
82
78
Outlet
82
82
82
82
84
84
84
84
79
Orifice
Pressure
Differ-
ential
("H20>
1.2
1.2
0.96
0.96
0.86
0.87
0.69
0.67
2.08
filter
Box
Temp
(•F)
270
270
295
290
255
255
280
280
247
Cast
Imp.
Gas
Temp
CF)
82
82
86
86
88
88
86
86
82
Sampling
Train
Static
Pressure
("Hg)
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
Clayton Environmental Consultants, Inc,
-------
C-74
SAMPLING TRAIN DATA
Pord Motor Company
Company:
Source Designation; Coke Battery A Scrubber Outlet
(Page 1 of 5)
Date: 6/30/75
Teat Number; EPA Method 5 Sample-3
Field Person: RJG/GMS
Filter Heater Setting; 250
Probe Heater Setting; 75
Filter Number; A-147-36
Barometric Pressure ("Hg); Avg. 29.70
Stack Static Pressure ("^0); -0.21
Stack Dimensions; 90" I.D.
Plume Appearance: --
Ambient Temperature (°F) :
Record all Data Every 0.5
Minutes
Nozzle Number; -- ,Dla.(in.);Q.256
Pitot Tube No.19 ,Corr.Factor; 0.854
Meter Box No. RAC-4,Corr.Factor; 0,991
Meter Isokinetic Factor; 1685
Assumed Moisture(Z):
Condensate Volume (ml): 2
Silica Gel Weight Caln(g); 20
Leak Rate CFM at "Hg
Trav-
erse
Point
No.
E-6
E-5
E-4
E-3
E-2
Time
Samp-
ling
<8ec)
0
30
60
0
30
60
0
30
60
0
30
60
0
30
60
Clock
08:54
09:05
09:20
09:43
09:54
(Telocity
Pressure
("H20)
0.40
0.40
0.32
0.32
0.26
0.26
0.22
0.22
0.19
0.19
•
AVERAGE (TOTAL)
Stack
Temp
CF>
125
124
122
126
123
130
120
123
120
125
Dry Gas Meter
Volume
(ft3)
695.304
696.048
696.064
696.741
696.754
697.388
697.422
698.088
698.113
698.667
( )
TempCF)
Inlet
76
76
78
78
79
79
84
84
86
86
Outlet
76
76
78
78
79
79
84
84
86
86
Orifice
Pressure
Differ-
ential
("H20)
1.83
1.83
1.47
1.47
1.19
1.17
1.03
1.02
0.89
0.89
filter
Box
Temp
(°F)
250
250
240
240
275
275
240
240
275
275
Last
Imp.
Gas
Temp
(•F)
82
82
82
82
84
84
86
86
90
90
Sampling
Train
Static
Pressure
("Hg)
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
Clayton Environmental Consultants, Inc.
-------
C-75
SAMPLING TRAIN DATA
Company; Ford Motor Company
(Page 2 of 5)
Source Designation; Coke Battery A Scrubber Outlet
6/30/75
Date:
Teat Number; EPA Method S Sample-3 r
Field Person: RJG/GMS
Filter Number: A- 147-36
Barometric Pressure ("Hg); Ava. 29.70
Stack Static Pressure ("HgO); -0.21
Stack Dimensions: 90" I.D.
Plume Appearance: =_=
Filter Heater Setting; 250
Probe Heater Setting: 75
Ambient Temperature(°F):
Record all Data Every 0.5
Minutes
Nocsle Number;— .Dia. (in. ) ;0.256
Pitot Tube No. 19 .Corr.Factor;0.854
Meter Box No. RAC-4.Corr.Factor; 0.991
Meter Isokinetic Factor; 1685
Assumed Moisture (I):
Condensate Volume (ml): 2
Silica Gel Weight Catn(g); 20
Leak Rate CFM at "Hg
Trav-
erse
Point
No.
E-l
N-6
N-5
N-4
N-3
Time
Samp-
ling
(sec )
0
30
60
0
30
60
0
30
60
0
30
60
0
30
60
Clock
10:03
10:11
10:27
10:45
10:56
velocity
Pressure
("H20)
0.13
0.13
0.70
0.70
0.78
0.78
0.75
0.75
0.68
0.68
•
AVERAGE (TOTAL)
Stack
Temp
CF)
120
124
125
130
123
130
125
132
125
132
Dry Gas Meter
Volume
(ft3)
698.681
699.126
699.136
700.062
700.100
701.147
701.170
702.210
702.230
703.229
C )
TempCF)
Inlet
86
86
86
86
87
87
87
87
88
88
Outle t
86
86
86
86
87
87
87
87
88
88
Orifice
Pressure
Differ-
ential
("H20)
0.62
0.61
3.20
3.15
3.66
3.60
3.51
3.47
3.18
3.14
?ilter
Box
Temp
CF)
250
250
280
280
270
270
270
270
250
250
Last
Imp.
Gas
Temp
CF)
92
92
93
93
90
90
92
92
93
93
Sampling
Train
Static
Pressure
("Hg)
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
Clayton Environmental Consultants, Inc,
-------
C-76
SAMPLING TRAIN DATA
Company; Ford Motor Company
(Page 3 of 5)
Source Designation; Coke Battery A Scrubber Outlet
Date: 6/30/75
Teat Number;EPA Method 5 Sample-3
Field Peraon: RJG/GMS
Filter Heater Setting:
Probe Heater Setting:
250
75
Filter Number: A-147-36
Barometric Pressure ("Hg); Avg. 29.70
Stack Static Pressure ("H?0); -0.21
Stack Dimensions! 90" I.D.
Plume Appearance:
Ambient Temperature(°F):
Record all Data Every 0.5
Minutes
Nozzle Number; -- ,Dia.(in.); 0.256
Pitot Tube No.19 ,Corr.Factor; 0.854
Meter Box No. RAC-4tCorr.Factor; 0.991
Meter laokinetic Factor; 1685
Assumed Moisture(Z):
Condensate Volume (ml): 2
Silica Gel Height Gain(g); 20
Leak Rate CFM at
"Hg
Trav-
erse
Point
No.
N-2
N-l
W-6
W-5
W-4
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
0
30
60
0
30
60
Clock
12:20
12:47
13:30
13:50
14:02
Velocity
Pressure
("H20)
0.58
0.58
0.42
0.42
0.60
0.60
0.68
0.68
0.73
0.73
AVERAGE (TOTAL)
Stack
Temp
(°F)
128
130
120
124
128
130
120
125
126
126
Dry Gas Meter
Volume
(ft3)
703.288
704.227
704.257
705.042
705.127
706.068
706.084
707.088
707.102
708.132
( )
Temp(eF)
Inlet
89
89
87
87
89
89
89
89
88
88
Outle t
89
89
87
87
89
89
89
89
88
88
Orifice
Pressure
Differ-
ential
("H20)
2.71
2.71
1.97
1.96
2.81
2.79
3.22
3.19
3.42
3.42
filter
Box
Temp
(•F)
240
240
255
255
250
250
260
260
260
260
Last
Imp.
Gas
Temp
(°F)
92
92
92
92
90
90
90
90
93
93
Samplinj
Train
Static
Pressure
("Hg)
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
Clayton Environmental Consultants, Inc.
-------
C-77
SAMPLING TRAIN DATA
Ford Motor Company
(Page 4 of 5)
Company:__
Source Designation; Coke Battery A Scrubber Outlet
6/30/75 - 7/1/75
Date:
Test Number: EPA Method 5 Sample-3
Field Person; RJG/CMS
Filter Number:
Filter Heater Setting; 250
Probe Heater Setting: 75
A-147-36
Barometric Pressure ("Hg); Avg. 29.70
Stack Static Pressure ("H20): -0.21
Stack Dimensions;
Plume Appearance:
90" i.p.
Ambient Temperature (°F):
Record all Data Every 0.5
Minutes
Noetic Number; -- .Dia.(in.); 0.256
Pltot Tube No. 19 .Corr.Factor; 0.854
Meter Box No. RAC-4»Corr.Factor; 0.991
Meter Isokinetic Factor; 1685
Assumed Moisture(I):
Condensate Volume (ml): 2
Silica Gel Weight Gain(g):
Leak Rate CFM at
20
"Hg
Trav-
erse
Point
No.
W-3
W-2
W-l
S-6
7/1
S-5
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
0
30
60
0
30
60
Clock
14:15
14:23
14:58
15:13
08:51
(Telocity
Pressure
("H20)
0.70
0.70
0.58
0.58
0.42
0.42
0.37
0.37
0.35
0.35
AVERAGE (TOTAL)
Stack
Temp
(°F>
122
135
124
132
130
130
125
125
125
143
Dry Gas Meter
Volume
(ft3)
708.148
709.161
709.168
710.102
710.149
710.927
710.942
711.679
711.917
712.675
( )
Temp(°F)
Inlet
88
88
89
89
89
89
88
88
82
82
Outlet
88
88
89
89
89
89
88
88
82
82
Orifice
Pressure
Differ.
ential
("H20)
3.30
3.25
2.72
2.69
1.95
1.95
1.73
1.73
1.62
1.54
Filter
Box
Temp
(°F)
255
255
255
255
250
250
—
—
270
270
Last
Imp.
Gas
Temp
(°F)
96
96
96
96
92
92
89
89
Sampling
Train
Static
Pressure
("Hg)
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
Clayton Environmental Consultants, Inc,
-------
C-78
SAMPLING TRAIN DATA
Ford Motor Company
Company:__
Source Designation; coke Battery A Scrubber Outlet
(Page 5 of 5)
7/1/75 -7/2/75
Date:
Test Kumber;EPA Method 5 Sample-3
Field Person; RJG/GMS
Filter Humbert A-147-36
Barometric Pressure ("Kg); Avg. 29.70
Stack Static Pressure ("H?0); -0.21
Stack Dimensions; 90" I.D.
Flume Appearance:
Filter Heater Setting; 250
Probe Heater Setting; 75
Ambient Temperature(°F);
Record all Data Every 0.5
Minutes
Noccle Number; ,. ,Dia. (in. ); Q.256
Pitot Tube No.19 ,Corr.Factor; 0.654
Meter Box Ho. RAC-4,Corr.Factor; 0.991
Meter Isoklnetic Factor; 1685
Assumed Moisture(1):
Condensate Volume (ml): 2
Silica Gel Weight Cain(g); 20
Leak Rate CFM at
"Hg
Trav-
erse
Point
No.
S-4
7/2
S-3
S-2
S-l
Time
Samp-
ling
(8ec?
0
30
60
0
30
60
0
30
60
0
30
60
Clock
09:35
09:21
09:28
09:46
/elocity
Pressure
("H20)
0.23
0.23
0.18
0.18
0.16
0.16
0.14
0.14
AVERAGE (TOTAL)
Stack
Temp
(*F)
134
135
120
120
125
130
120
120
126
Dry Gas Meter
Volume
(ft*)
712.682
713.248
713.394
713.931
713.931
714.417
714.417
714.886
( 18.541)
Temp(°F)
Inlet]
82
82
95
95
93
93
93
93
87
Outlet
82
82
95
95
93
93
93
93
87
Orifice
Pressure
Differ-
ential
("H20)
1.05
1.05
0.86
0.86
0.76
0.75
0.67
0.67
2.05
filter
Box
Temp
CF>
250
250
250
250
265
265
250
250
257
Last
Imp.
Gas
lemp
CF)
88
88
92
92
93
93
90
90
90
Sampling
Train
Static
pressure
("HR)
1.0
1.0
1,0
1.0
1.0
1.0
1.0
1.0
1.0
Clayton Environmental Consultants, Inc.
-------
C-79
SAMPLING TRAIN DATA
Company; Ford Motor Company
(Page 1 of 4)
Source Designation; Coke Battery A Scrubber Outlet
7/2/75
Date:
Test Number; EPA Method 5 Sample-4
Field Person: RJG/GMS
Filter Number:
Filter Heater Setting:
Probe Heater Setting:
250
75
A-147-37
Barometric Pressure ("Hg); Avg. 29.46
Stack Static Pressure <"H?0); -0.21
Stack Dimensions:
Plume Appearance:
90" I.D.
Ambient Temperature(*F) : .
Record all Data Every 0.5
Minutes
Koczle Number;-- .Dia.(in.);Q.256
Pitot Tube No. 19 JCorr.Factor:0.854
Meter Box No. RAC-4.Corr.Factor; 0.991
Meter Isokinetic Factor; 1685
Assumed Moisture(I):
Condensate Volume(ml); -5
Silica Gel Weight Gain(g); 15
Leak Rate CFM at "Hg
Trav-
erse
Point
No.
E-4
E-3
E-2.
E-l
N-4
Time
Samp-
ling
(sec '
0
30
60
0
30
60
0
30
60
0
30
60
0
30
60
Clock
13:27
13:35
13:45
13:55
14:15
Velocity
Pressure
("H20)
0.35
0.35
0.27
0.27
0.23
0.23
0.17
0.17
0.70
0.70
•
AVERAGE (TOTAL)
Stack
Temp
(°F>
125
130
121
125
130
130
124
134
120
130
Dry Gas Meter
Volume
(ft3)
715.012
715.722
715.722
716.357
716.357
716.970
716.970
717.483
717.483
718.472
( )
Temp(°F)
Inle
90
90
90
90
90
90
90
90
90
90
Outlet
90
90
90
90
90
90
90
90
90
90
Orifice
Pressure
Differ-
ential
("H20>
1.65
1.63
1.28
1.27
1.07
1.07
0.80
0.77
3.30
3.25
Filter
Box
Temp
(°F)
250
250
250
250
250
250
250
250
250
250
Las
Imp
Gas
Temp
(°F
97
97
98
98
98
98
98
98
98
98
Sampling
Train
Static
Pressure
("Hg)
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
Clayton Environmental Consultants, Inc.
-------
C-80
SAMPLING TRAIN DATA
Company; Ford Motor Company
(Page 2 of 4)
Source Designation; Coke Battery A Scrubber Outlet
7/2/75
Date: _
Test Number;EPA Method 5 Sample-4
Field Person: RJG/GMS
Filter Number:
Filter Heater Setting:
Probe Heater Setting:
250
75
A-147-37
Barometric Pressure ("Hg); Avg. 29.46
Stack Static Pressure ("HgO): -0.21
Stack Dimensions:
Plume Appearance:
90" I.D.
Ambient Temperature(°F): .
Record all Data Every Q.5
Minutes
Nocele Number; -- ,Dia.(in.);0.256
Pitot Tube No. 19 ,Corr.Factor; 0.854
Meter Box No. RAC-4,Corr.Factor; 0.991
Meter Isokinetic Factor; 1685
Assumed Moisture(X):
Condensate Volume (ml): -5
Silica Gel Weight Gatn(g): 15
Leak Rate CFM at "Hg
Trav-
erse
Point
No.
N-3
N-2
N-l
W-4
W-3
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
0
30
60
0
30
60
Clock
14:42
14:55
15:05
15:35
15:45
Velocity
Pressure
("H20)
0.82
0.82
0.80
0.80
0.50
0.50
0.62
0.62
0.70
0.70
•
AVERAGE (TOTAL)
Stack
Temp
(°F)
123
126
121
124
123
123
121
125
125
126
Dry Gas Meter
Volume
(ft3)
718.472
719.545
719.545
720.602
720.602
721.448
721.448
722.410
722.410
723.416
( )
Temp(°F)
Inlet
90
90
90
90
90
90
90
90
90
90
Outle t
90
90
90
90
90
90
90
90
90
90
Orifice
Pressure
Differ-
ential
("H20)
3.87
3.86
3.79
3.78
2.36
2.36
2.93
2.92
.
3.29
3.29
filter
Box
Temp
<°F)
250
250
250
250
250
250
250
250
250
250
Last
Imp.
Gas
Temp
(°F)
98
98
98
98
98
98
96
96
96
96
Sampling
Train
Static
Pressure
("Hg)
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
Clayton Environmental Consultants, Inc.
-------
C-81
SAMPLING TRAIN DATA
Ford Motor Company
(Page 3 of 4)
Company:
Source Designation; Coke Battery A Scrubber Outlet
7/3/75
Date:
Test Number; EPA Method 5 Sample-4 .
Field Person;_ RJG/GMS
Filter Number:
Filter Heater Setting; 250
Probe Heater Setting; 75
A-147-37
Barometric Pressure ("Hg); Ava. 29.46
Stack Static Pressure ("H;0); -0.21
Stack Dimensions:_
Plume Appearance:
90" I.D.
Ambient Temperature(°F): .
Record all Data Every 0.5
Minutes
Nozzle Number; -- ,Dia.(in.); 0.256
Pitot Tube No. 19,Corr.Factor; p.854
Meter Box No. RAC-4.Corr,Factor; 0.991
Meter Isokinetic Factor; 1685
Assumed Moisture(Z):
Condensate Volume (ml): -5
Silica Gel Weight Gatn(g); 15
Leak Rate CFM at "Hg
Trav-
erse
Point
No.
W-2
W-l
S-4
S-3
S-2
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
0
30
60
0
30
60
Clock
08:38
09:03
09:39
09:54
10:06
Velocity
Pressure
("H20)
0.64
0.64
0.48
0.48
0.35
0.35
0.23
0.23
0.20
0.20
AVERAGE (TOTAL)
Stack
Temp
(°F>
120
120
120
120
120
120
120
120
123
125
Dry Gas Meter
Volume
(£t3)
723.463
724.417
724.417
725.240
725.240
726.039
726.057
726.637
726.665
727.224
( )
Temp(°F)
Inlet
76
76
78
78
79
79
80
80
82
82
Outlet
76
76
78
78
79
79
80
80
82
82
Orifice
Pressure
Differ-
ential
("H20)
2.95
2.95
2.23
2.23
1.63
1.63
1.07
1.07
0.93
0.92
Filter
Box
Temp
(°F)
250
250
250
250
250
250
250
250
250
250
Last
Imp.
Gas
Temp
CF>
80
80
80
80
82
82
84
84
84
84
Sampling
Train
Static
Pressure
("Hg)
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
Clayton Environmental Consultants, Inc.
-------
C-82
SAMPLING TRAIN DATA
Ford Motor Company
Compony:_
Source Deatgnatton; coke Battery A Scrubber Outlet
(Page 4 of 4)
7/3/75
Date: _
Test Number; EPA Method 5 Sample-4..
Field Person; RJG/GMS
Filter Number:
Filter Heater Setting; 250
Probe Heater Setting; 75
A-147-37
Barometric Pressure ("Hg);Avg. 29.46
Stack Static Pressure ("H?0); -0.21
Stack Dimensions:_
Plume Appearance:
90" I.D.
Ambient Temperature (T); —
Record all Data Every
0.5 Minutes
Nozzle Number; -- ,Dia.(in.); Q.256
Pitot Tube No.19 .Corr.Factor; 0.854
Meter Box No. RAC-4iCorr.Factor; p.991
Meter Isokinetic Factor; 1685
Assumed Moisture(I):
Condensate Volume (ml): -5
Silica Gel Weight Cain(g); 15
Leak Rate CFM at "Hg
Trav-
erse
Point
No.
S-l
Time
Samp-
ling
(sec)
0
30
60
Clock
10:27
Velocity
Pressure
("H20)
0.15
0.15
•
AVERAGE (TOTAL)
Stack
Temp
CF)
120
123
124
Dry Gas Meter
Volume
(£t3)
727.224
727.710
( 12.492)
Temp(°F)
Inlet
83
83
86
Outlet
83
83
86
Orifice
Pressure
Differ-
ential
("H20)
0.70
0.70
2.11
?iiter
Box
Temp
(°F)
250
250
250
Last
Imp.
Gas
Temp
<°F>
84
84
92
Sampling
Train
Static
Pressure
<"HR)
1.0
1.0
1.0
Clayton Environmental Consultants, Inc.
-------
C-83
SAMPLING TRAIN DATA
Ford Motor Company
Company}
Source Designation; Coke Battery A Scrubber Outlet
(Page 1 of 4)
7/8/75
Date:
Teat Number; EPA Method 5 Sample-5
Field Pereont RGK
Filter Number; A-147-14
Barometric Pressure ("Hg); 29.31
Filter Heater Setting; 200
Probe Heater Setting; 80
Stack Static Pressure ("H?0)t -0.21
Stack Dimensions; 90" I.D.
Plume Appearance: --
Nocsle Number; -- ,Dla. (in. ) ;j). 256
Pitot Tube No. 19 .Corr.FactortQ.854
Meter Box No. RAC-4«Corr.Factor; 0.991
Meter Isokinetlc Factor; 1685
Assumed Moisture(1):
Condensate Volume (ml): -3
Ambient Temperature(°F); —
Record all Data Every 0.5
Minutes
Silica Gel Weight Cain(g); 16
Leak Rate
CFM at
"Hg
Trav-
erse
Point
No.
E-4
B-3
E-2
E-l
N-4
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
0
30
60
0
30
60
Clock
09:28
10:17
10:33
10:43
10:56
Velocity
Pressure
r (»H2o)
0.37
0.37
•
0.32
0.20
.
0.7
•
AVERAGE (TOTAL)
Stack
Temp
(°F)
130
130
(130)
128
128
(130)
125
125
(128)
130
130
(130)
125
132
(132)
Dry Gas Meter
Volume
(ft3)
727.973
728.744
729.473
730.167
730.712
731.706
( )
Temp(°F)
Inlet
80
83
(83)
83
83
(83)
83
Outlet
80
83
(83)
83
83
(83)
83
Orifice
Pressure
Differ-
ential
("H20)
1.75
1.75
1.5
0.9
3.3
filter
Box
Temp
CF)
235
240
240
240
240
Last
Imp.
Gas
Temp
CF)
92
96
95
95
92
Sampling
Train
Static
Pressure
("Hg)
2.5
2.5
2.5
2.5
5.0
Clayton Environmental Consultants, Inc.
-------
C-84
SAMPLING TRAIN DATA
Conpany; Ford Motor Company
(Page 2 of 4)
Source Designation; Coke Battery A Scrubber Outlet
7/8/75
Date:
Teat Humbert EPA Method S Sample -5
Field Person;
Filter Number:
Barometric Pressure ("Hg); 29.31
Filter Heater Setting:
Probe Heater Setting:
200
80
A- 14 7 -14
Stack Static pressure ("HgO)t -0.21
Stack Dimensions! 90" I.D.
Plume Appearance: -.
Nocsle Number; -- ,Die.(in.)• p.256
Pitot Tube Ho. 19 jCorr.Factor; 0.854
Meter Box No. RAC-4tCorr.Factor; 0.991
Meter Isokinetic Factor; 1685
Assumed Moisture(I):
Ambient Temperature (°F) : __
Record all Data Every 0.5 Minutes
Condensate Volume(ml):
Silica Gel Weight Gain(g):
Leak Rate CFH at
-3
16
'Hg
Trav-
erse
Point
No.
N-3
N-2
K-l
W-4
W-3
Time
Samp-
ling
{sec)
0
30
60
0
30
60
0
30
60
0
30
60
0
30
60
Clock
11:41
12:13
12:45
13:05
13:20
Velocity
Pressure
("H20>
0.8
0.63
0.5
0.6
0.72
AVERAGE (TOTAL)
Stack
Temp
CF)
125
128
(128
145
137
(137
132
132
(132)
133
135
(135)
128
130
(130)
Dry Gas Meter
Volume
(ft3)
732.752
732.752
733.768
734.712
735.878
736.886
( )
Temp(°F)
Inle
83
85
(85)
65
85
86
Outlet
83
85
(85)
85
85
66
Orifice
Pressure
Differ-
ential
("H20)
3.8
2.9
2.35
2.8
3.4
Filter
Box
Temp
(•F)
240
240
240
240
240
Last
Imp
Gas
Temp
('*}
92
91
93
93
93
Sampling
Train
Static
Pressure
("Hg)
6.0
5.5
5.0
5.5
5.5
Clayton Environmental Consultants, Inc.
-------
Company:
Source Designation:
Date: 7/8/75
C-85
SAMPLING TRAIN DATA
Pord Motor Company
(Page 3 of 4)
Coke Battery A Scrubber Outlet
Teat Number;EPA Method 5 Sample-5
Field Person: RGK
Filter Heater Setting; 200
Probe Heater Setting; 80
Filter Number: A-147-14
Barometric Pressure ("Hg); 29.31
Stack Static Pressure ("H?0); -0.21
Stack Dimensions; 90" I.D.
Plume Appearance: --
Ambient Temperature(°P):
Record all Data Every
Nocsle Number;-- ,Die, (in. ); P., 256
Pitot Tube No. 19 .Corr.Factor; 0.854
Meter Box No. RAC-4.Corr.Factor; 0.991
Meter Isokinetic Factor; 1685
Assumed Moisture(Z):
Condensate Volume (ml): -3
Silica Gel Weight Gain(g) :_16__
0.5 Minutes Leak Rate
CFM at
MHg
Trav-
erse
Point
No.
V-2
W-l
S-4
S-3
S-2
Time
Samp-
ling
(sec}
0
30
60
0
30
60
0
30
60
0
30
60
0
30
60
Clock
13:35
/
13:45
14:03
i
14:21
14:40
.;
Velocity
Pressure
("H20)
0.7
0.48
0.35
0.26
0.21
AVERAGE (TOTAL)
Stack
Temp
(«F)
140
135
(137)
133
133
128
130
(130)
125
128
(130)
125
130
(130)
-
Dry Gas Meter
Volume
(ft3)
737.892
738.763
738.763
739. 48&
740.110
740.667
( )
Temp(°F)
Inlet
86
86
86
86
86
Outlet
86
86
86
86
86
Orifice
Pressure
Differ-
ential
("H20)
3.3
2.3
1.65
1.2
0.95
[Filter
Box
Temp
| (°F)
240
240
240
240
240
Last
Imp.
Gas
Temp
CF)
93
93
94
94
94
Sampling
Train
Static
Pressure
("Hg)
5.5
5.0
5.0
5.0
Clayton Environmental Consultants, Inc.
-------
C-86
SAMPLING TRAIN DATA
Companyt Ford Motor Company
(Page 4 of 4)
Source Designation; Coke Battery A Scrubber Outlet
7/8/75
Date: _
Test Number; EPA Method 5 Sample-5
Field Person:_
Filter Number:
Barometric Pressure ("Hg); 29.31
RGK
A-147-14
Stack Static Pressure ("H?0); -0.21
Stack Dimensions; 90" I.D.
Plume Appearance: --
Ambient Temperature (°F):
Record all Data Every
O.S Minutes
Filter Heater Setting:
Probe Heater Setting:
200
80
Noezle Number; -- ,Dia.(in.); 0.256
Pitot Tube No. i9,Corr.Factor; 0.854
Meter Box No. RAC-4,Corr.Factor; 0.991
Meter Isoklnetic Factor; 1685
Assumed Moisture(X):
Condensate Volume (ml): O
Silica Gel Weight Gain(g):
Leak Rate CFM at
16
"Hg
rrav-
eree
Point
No.
S-l
Time
Samp-
ling
(sec)
0
30
60
Clock
14:49
Velocity
Pressure
("H20)
0.16
AVERAGE (TOTAL)
Stack
Temp
(°F)
132
135
(135)
131
Dry Gas Meter
Volume
(ft3)
741.168
( 13.076)
Temp(°F)
Inlet
86
84
Outlet
86
84
OrificeL
PressurerV"
Differ- I'0*
ential *«J
("H20) | < FJ
0.76
2.2
240
240
Last
Imp.
Gas
Temp
CF>
94
93
Sampling
Train
Static
Pressure
("HR)
4.5
Clayton Environmental Consultants, Inc.
-------
C-87
SAHPLXNC TRAIN DATA
Company t Ford Motor Company
(Page 1 of 4)
Source Designation; Coke Battery A Scrubber Outlet
7/10/75
Date:
Teat Humbert EPA Method 5 Sample-6
Field Person: RGK
Filter Number: A-190-09
Barometric Pressure ("Hg); 29.33
Filter Heater Setting; 200
Probe Heater Setting: 80
Stack Static Pressure ("H;0); -0.21
Stack Dimensions; 90" I.D.
Plume Appearance: -_-
Ambient Temperature(°F) : .
Record all Data Every 0.5
Minutes
Noesle Number; — .Dla.(In.); 0.25
Pitot Tube No.19 »Corr.Factor ;• 0.854
Meter Box No. RAC-3«Corr.Factor; 0.993
Meter Isoklnetlc Factor; 1796
Assumed Moisture (X):
Condensate Volume (ml): 3
Silica Gel Weight Galn(g); 11
Leak Rate
CFM at
"Hg
Trav-
erse
Point
No.
B-4
E-3
B-2
E-l
N-4
Time
Samp-
ling
(»ec)
0
30
60
0
30
60
0
30
60
0
30
60
0
30
60
Clock
09:40
09:53
10:17
10:45
10:57
Velocity
Pressure
("H20)
0.35
0.33
•
0.22
0.18
0.7
•
AVERAGE (TOTAL)
Stack
Temp
(°F>
120
120
(130)
120
130
(130)
110
120
(120)
120
120
(120)
120
125
(125)
-
Dry Gas Meter
Vo lume
-------
C-88
SAMPLING TRAIN DATA
Companyt Ford Motor Company
(Page 2 of 4)
Source Deeignatlon; Coke Battery A Scrubber Outlet
7/10/75
Date:
Test Number;EPA Method 5 Sample-6
Field Person: RGK
Filter Number:
Filter Heater Setting! 200
Probe Heater Setting: 80
A-190-09
Barometric Pressure ("Hg); 29.33
Stack Static Pressure ("H?0); -0.21
Stack Dimensions:
Plume Appearance:
90" I.D.
Ambient Temperature(°F) : .
Record all Data Every 0.5
Minutes
NoKsle Number; -- .Dia.(in.); Q.25
Pitot Tube No. 19 ,Corr.Factor; 0.854
Meter Box No. RAC-3tCorr.Factor; 0.993
Meter Isokinetic Factor; 1796
Assumed Moisture(X) :
Condensate Volume(ml): 3
Silica Gel Weight Gatn(g); 11
Leak Rate CFM at "Hg
Trav-
erse
Point
No.
N-3
N-2
N-l
W-4
W-3
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
0
30
60
0
30
60
Clock
11:07
11:20
12:42
12:52
13:37
Velocity
Pressure
("H20)
0.77
0.65
0.45
0.55
0.66
•
AVERAGE (TOTAL)
Stack
Temp
(«F)
125
125
(125)
120
125
(125)
130
130
(130)
130
130
(130)
120
130
(130)
Dry Gas Meter
Volume
(ft3)
958.808
958.808
958.802
960.608
961.503
962.466
( )
Temp(°F)
Inlet
76
76
(78)
78
(80)
80
80
Outlet
76
76
(78)
78
(80)
80
80
Orifice
Pressure
Differ-
ential
(HH20)
3.85
3.25
(2.25)
2.25
2.75
3.3
filter
Box
Temp
CF)
230
230
(250)
250
(250)
250
250
Last
Imp.
Gas
Cemp
(°F)
82
84
(84)
84
(84)
84
84
Sampling
Train
Static
Pressure
("Hg)
2.0
(2.0)
2.0
2.0
Clayton Environmental Consultants, Inc,
-------
C-89
SAMPLING TRAIN DATA
Ford Motor Company
Company:_
Source Designation; Coke Battery A Scrubber Outlet
(Page 3 of 4)
7/10/75
Date:
Test Number;EPA Method 5 Sample-6
Pteld Person: RGK
Filter Heater Setting; 200
Probe Heater Setting: gp
Filter Number; A-190-09
Barometric Pressure ("Hg); 29.33
Stack Static Pressure ("HgO); -0.21
Stack Dimensions: 90" I.D.
Plume Appearance: --
Ambient Temperature(*F);
Record all Data Every 0.5
Minutes
Nocsle Number; -- ,Di«.(in.); 0.25
Pitot Tube No. 19 .Corr.Factor;' 0.854
Meter Box No. RAC-3,Corr.Factor; 0.993
Meter Isokinetic Factor; 1796
Assumed Moisture(1):
Condensate Volume(ml); 3
Silica Gel Height Gain(g):
Leak Rate CFM at
11
"Hg
trav-
erse
Point
No.
H-2
W-l
S-4
S-3
S-2
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
0
30
60
0
30
60
Clock
13:58
14:10
14:24
14:36
14:52
Velocity
Pressure
(nH20)
0.61
0.45
0.3
0.25
.
0.2
•
AVERAGE (TOTAL)
Stack
Temp
(°F)
125
130
(130)
120
125
(125)
125
125
(125)
120
125
(125)
125
120
(120)
Dry Gas Meter
Volume
-------
C-90
8AHPLING TRAIN DATA
Ford Motor Company
Company:_
Source Designation; Coke Battery A Scrubber Outlet
(Page 4 of 4)
7/10/75
Date:
Test Number; EPA Method 5 Sample.6
Field Person:__
Filter Number:
Barometric Pressure ("Hg); 29.33
Filter Heater Setting; 200
Probe Heater Setting; 80
RGK
A-190-09
Stack Static Pressure ("H?0); -0.21
Stack Dimensions; 90" I.D.
Plume Appearance: --
Ambient Temperature(°F): .
Record all Data Every 0.5
Minutes
Nozzle Number; — ,Dia. (in.); 0.25
Pitot Tube No. 19.Corr.Factor; 0.854
Meter Box No. RAC-3, Corr. Factor; 0.993
Meter Isokinetic Factor; 1796
Assumed Moisture(X) :
Condensate Volume (ml): 3 .
Silica Gel Weight Gain(g):
Leak Rate CFM at
11
"Hg
Trav-
erse
Point
No.
S-l
Time
Samp-
ling
(sec)
0
30
60
Clock
15:05
Velocity
Pressure
<"H20)
0.16
AVERAGE (TOTAL)
Stack
Temp
(°F)
120
125
(120)
124
Dry Gas Meter
Volume
(ft3)
966.589
( 12.231)
Temp(°F)
Inlet
77
75
Outlet
77
75
Orifice
Pressure
Differ-
ential
("H20)
0.8
2.1
filter
Box
Temp
(°F)
260
240
Last
Imp.
Gas
Temp
CFJ
81
79
Sampling
Train
Static
Pressure
("Hg)
2.0
Clayton Environmental Consultants, Inc.
-------
C-91
SAMPLING TRAIN DATA
Companys Ford Motor Company
(Page I of 4)
Source Designation; Coke Battery A Scrubber Outlet
Date: 7/14/75
Teat Number; EPA Method 5 Sample -7
Field Person:
Filter Kunber: _
Barometric Pressure (MHg); 29.63
Filter Heater Setting; 200
Probe Heater Setting; 80
A- 190- 13
Stack Static pressure ("H;0); -0.21
Stack Dimensions: 90" I.D.
Plume Appearance: --
Ambient Temperature(°F):
Moasle Number: -- .Dia. (in. ) ; 0.25
Pltot Tube Mo. 19. Cotr. Factor* 0.854
Meter Box No. RAC-3'.Corr. Factor; 0.993
Meter Xsoklnetlc Factor; 1796
Assumed MolsCure(Z): _
Condensate Volume (ml): _ ^5 _
Silica Gel Weight Cain(g); 15 _
Record all Data Every 0.5 Minutes Leak Rate
CFM at
"Hg
Trav-
erse
Point
Ho.
E-4
E-3
E-2
E-l
N-4
Time
Samp-
ling
(sec)
0
30
60
0.
30
60
0
30
60
0
30
60
0
30
60
Clock
08:40
09:23
09:32
09:50
10:22
Velocity
Pressure
(MH20)
0.34
0.3
•
0.2
0.2
0.7
•
AVERAGE (TOTAL)
Stack
Temp
(°F)
120
120
(120)
120
120
(120)
120
123
(125)
118
121
(121)
125
118
(118)
Dry Gas Meter
Volume
(ft3)
967.512
968.216
968.803
969.448
969.975
970.947
( )
Temp('F)
Inlet
63
67
70
68
68
Outlet
63
67
70
68
68
Orifice
Pressure
Differ-
ential
("H20>
1.7
1.5
1.0
1.0
3.5
Filter
Box
Temp
(•F)
220
225
230
230
235
Last
Imp.
Gas
Temp
CF)
74
74
76
76
76
Sampling
Train
Static
Pressure
("Hg)
2.0
2.0
1.5
1.5
2.5
Clayton Environmental Consultants, Inc.
-------
C-92
SAMPLING TRAIN DATA
Ford Motor Company
Company;
Source Designation:
Data: 7/14/75
Teat Number;EPA Method 5 Sample-7
Field Person: RGK
Filter Number; A-190-13
Barometric pressure ("Hg); 29.63
(Page 2 of 4)
Coke Battery A Scrubber Outlet
Filter Heater Setting; 200
Probe Heater Setting: 80
Stack Static Pressure ("^0); -0.21
Stack Dimensions; 9Q" i.p.
Plume Appearance:
Ambient Temperature('F):
Record all Data Every 0.5
Minutes
NocEle Number; -- .Dla.(in.); 0.25
Pitot Tube No. 19 ,Corr.Factor; Q.854
Meter Box No. RAG-3.Corr.Facton 0.993
Meter Isokinetic Factor; 1796
Assumed Moisture(I):
Condensate Volume(ml); -S
Silica Gel Weight Cain(g); 15
Leak Rate CFM at "Hg
Trav-
erse
Point
No.
N-3
N-2
N-l
W-4
W-3
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
0
30
60
0
30
60
Clock
10:33
10:58
11:10
12:45
12:55
Velocity
Pressure
("H20)
0.78
0.65
0.5
0.6
.
0.7
•
AVERAGE (TOTAL)
Stack
Temp
(°F)
120
122
(122)
125
125
(125)
123
125
(125)
120
120
(120)
123
123
(125)
Dry Gas Meter
Volume
(ft3)
971.973
971.973
972.932
973.782
974.843
975.837
C )
Temp(°F)
Inlet
68
70
70
70
72
Outlet
68
70
70
70
72
Orifice
Pressure
Differ-
ential
("H20)
3.9
3.25
2.5
3.0
3.5
Filter
Box
Temp
(°F)
250
250
240
250
260
Last
Imp.
Gas
Temp
(°F)
76
74
74
74
79
Sampling
Train
Static
Pressure
("HR>
2.5
2.5
2.0
2.0
2.5
Clayton Environmental Consultants, Inc.
-------
C-93
SAMPLING TRAIN DATA
Ford Motor Company
Company:
Source Designation; Coke Battery A Scrubber Outlet
(Page 3 of 4)
7/14/75
Date:
Teat Humbert EPA Method S Sample-7
Field Person: RGK
Filter Heater Setting; 200
probe Heater Setting; 80
Filter Number; A-190-13
-0.21
Barometric Pressure ("Hg); 29.63
Stack Static Pressure ("H20)
Stack Dimensions; 90" i.p.
Plume Appearance:
Ambient Temperature(*P);—
Record all Data Every
0.5 Minutes
Nocsle Number;-- .Dia.(in.);0.25
Pitot Tube No. 19 ,Corr.Factor;0.854
Meter Box Mo. RAC-3.Corr.Factor; 0.993
Meter Isokinetic Factor; 1796
Assumed Moisture(X) :
Condensate Volume(ml); -5
Silica Gel Weight Gain(g); 15
Leak Rate CPM at "Hg
Trav-
erse
Point
No.
W-2
W-l
S-4
S-3
S-2
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
0
30
60
0
30
60
Clock
13:18
13:38
13:47
13:58
14:10
Velocity
Pressure
("H20)
0.65
0.5
0.3
0.27
0.17
•
AVERAGE (TOTAL)
Stack
Temp
(°F>
118
120
(120)
124
124
(124)
122
125
(125)
115
118
(125)
123
125
(125)
Dry Gas Meter
Volume
(ft3)
976.793
977.656
977.656
978.347
978.985
979.500
( )
Temp(°F)
Inlet
72
72
75
75
75
Outlet
72
72
75
75
75
Orifice
Pressure
Differ-
ential
("H20)
3.25
2.5
1.5
1.35
0.85
Ifilter
Box
Temp
(•F)
200
200
200
220
250
Last
Imp.
Gas
Temp
CF)
78
78
74
74
74
Sampling
Train
Static
Pressure
("Hg)
2.5
2.0
2.0
1.5
1.5
Clayton Environmental Consultants, Inc.
-------
C-94
SAHPLXNC TRAIN DATA
Pord Mot«
Company:_ _
Source Designation; Coke Battery A Scrubber Outlet
(Pege 4 of 4)
7/14/75
Date: _
Teat Number;EPA Methqd 5 Sample-7
Field Person: RCK
Filter Number:
Filter Heater Setting; 200
Probe Heater Setting: 80
A-190-13
Barometric Pressure ("Hg); 29.63
Stack Static Pressure C^O): -0.21
90" I.D.
Stack Dimensions:
Plume Appearance: --
Ambient Temperature(°F);
Record all Data Every
Nocsle Number; -- ,Dia.(in.);g.25
Pitot Tube No.19 ,Corr.Factor; 0.854
Meter Box Ho. RAG-3iCorr.Factor; Q.993
Meter Zsokinetic Factor; 1796
Assumed Moisture(Z):
Condensate Volume(ml); -5
0.5 Minutes
Silica Gel Weight Gain(g); 15
Leak Rate ' CFM at "Hg
Trav-
erae
Point
No.
S-l
Time
Samp-
ling
<8ec?
0
30
60
Clock
14:24
Velocity
Pressure
("H20)
0.13
•
AVERAGE (TOTAL)
Stack
Temp
<°F)
122
120
(120)
121
Dry Gas Meter
Volume
(ft3)
979.947
( 12.348)
Temp('F)
Inlet
75
71
Outlet
75
71
Orifice
Pressure
Differ-
ential
("H20)
0.65
2.2
Filter
Box
Temp
<°F)
250
230
Last
Imp.
Gas
Temp
CF)
74
75
Sampling
Train
Static
Pressure
("Hg)
2.0
Clayton Environmental Consultants, Inc.
-------
C-95
SAMPLING TRAIN DATA
Ford Motor Company
Companyi_
Source Designation; Coke Battery A Scrubber Outlet
(Page 1 of 4)
7/15/75
Date:
Test Number; EPA Method 5 Samole-8
Field Personi RCK
Filter Number; A-190-02
Barometric Pressure ("Hg); 29.60
Filter Heater Setting: 200
Probe Heater Setting: 65
Stack Static Pressure ("H?0); -0.21
Stack Dimensions; 90" I.D.
• •••^^^^^^^MMM^^^V^^MMMMMMn^B^MM
Plume Appearance: --
Ambient Temperature(*F): -.
Record all Data Every 0.5
Minutes
Nossle Number: -- .Die.(in.); 0.254
Pitot Tube No.19 .Corr.Factor; 0.854
Meter Box No. RAC-5»Corr.Facton 0.993
Meter Isokinetic Factor; 1796
Assumed Moisture(X) :
Condensate Volume(ml); 0
Silica Gel Weight Galn(g):
Leak Rate CFM at
12
"Hg
trav-
erse
Point
No.
E-4
E-3
B-2
E-l
N-4
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
0
30
60
0
30
60
Clock
08:30
08:47
09:20
09:29
09:58
'
(Telocity
Pressure
("H20)
0.32
0.25
0.2
0.15
0.7
•
AVERAGE (TOTAL)
Stack
Temp
(«P)
120
123
(126)
120
120
(123)
123
126
(128)
130
128
(129)
126
127
(128)
Dry Gas Meter
Volume
(ft3)
980.240
980.927
981.541
982.089
982.558
983.557
( )
TempCF)
Inlet
73
75
77
78
78
Outlet
73
75
77
78
78
Orifice
Pressure
Differ-
ential
("H20)
1.6
1.25
1.0
0.75
3.5
niter
Box
Temp
CF)
260
245
225
250
225
Last
Imp.
Gas
Temp
CF)
84
87
84
84
84
Sampling
Train
Static
Pressure
("Hg)
1.5
1.5
1.0
1.0
2.5
Clayton Environmental Consultants, Inc,
-------
- 96 -
SAMPLING TRAIN DATA
(Page 2 of 4)
Ford Motor Company
Companyt
Source Designation; Coke Battery A Scrubber Outlet
D«t«: 7/15/75
Test Number;EPA Method 5 Sample-8
Field Person: RGK
Filter Number: A-190-02
Barometric Pressure ("Hg); 29.60
Filter Heater Setting; 200
Probe Heater Setting: 65
Stack Static Pressure ("H20) :__p_._21_
Stack Dimensions: 90" I.D.
Plume Appearance: --
Ambient Temperature(*F):
Record all Data Every
Noccle Number; -- ,Dia. (in.); 0.254
Pltot Tube No. 19 ,Corr.Factor; p.854
Meter Box No. RAC-3.Corr.Factor; 0.993
Meter Isoklnetlc Factor; 1796
Assumed Moisture(X) :
Condensate Volume(ml); 0
Silica Gel Weight Cain(g); 12
0.5 Minutes Leak Rate
CFM at
MHg
Trav-
erse
Point
No.
N-3
N-2
N-l
W-4
W-3
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
0
30
60
0
30
60
Clock
10:54
11:04
11:25
11:40
11:56
Velocity
Pressure
("H20)
0.8
0.65
0.45
0.6
.
0.7
•
AVERAGE (TOTAL)
Stack
Temp
CF>
123
125
(127)
121
126
(128)
121
125
(127)
122
122
(127)
120
123
(127)
Dry Gas Meter
Volume
(ft3)
984.618
984.618
985.666
986.488
987.405
988.392
( )
Temp('F)
Inlet
80
80
(80)
80
80
80
Outlet
80
80
(80)
80
80
80
Orifice
Pressure
Differ-
ential
("H20)
4.0
3.25
2.25
3.0
3.5
••liter
Box
Temp
(•F)
245
240
250
230
225
Last
Imp.
Gas
Temp
CF)
84
84
84
84
84
Sampling
Train
Static
Pressure
("Hg)
2.5
2.0
2.0
2.0
2.5
Clayton Environmental Consultants, inc.
-------
C-97
SAMPLING TRAIN DATA
Ford Motor Company
Company:_
Source Designation; Coke Battery A Scrubber Outlet
(Pag* 3 of 4)
7/15/75
Date:
Teat Number; EPA Method 5 Sample-B
Field Person:
Filter Heater Setting; 200
Probe Heater Setting: 65
Filter Humbert A-190-02
Bar000trie preiture ("Hg); 29.60
Stack Static Pressure (**H?0); -0.21
Stack Dimensions; 90" I.P.
Plume Appearance: ..
Ambient Temperature(*F):
Record all Data Every p.5
Minutes
NOBale Number; -- .Dia.(in.); 0.254
Pitot Tube Mo. 19 ,Corr.Factor; 0.854
Meter Box He. RAC-3,Corr.Factor; 0.993
Heter leoklnetic Factor; 1796
Assumed Moisture(I):
Condenaate Volume (ml): fl^
Silica Gel Weight Cain(g); 12
Leak Rate CFM at "Hg
trav-
erse
Point
Mo.
W-2
H.I
S-4
S-3
S-2
Time
Samp-
ling
<"c?
0
30
60
0
30
60
0
30
60
0
30
60
0
30
60
Clock
13:00
13:25
13:33
13:45
14:04
Velocity
pressure
("H20)
0.6
0.5
0.3
0.25
0.2
•
AVERAGE (TOTAL)
Stack
Temp
(e?>
127
128
(130)
125
127
(128)
127
128
(130)
125
128
(130)
122
124
(125)
Dry Gas Meter
Volume
(£t3)
989.337
990.190
990.190
990.668
991.468
992.023
i i
i ,
Temp('F)
Inlet
82
83
83
83
83
Outlet
82
83
83
83
83
Orifice
Pressure
Differ.
ential
("H20>
3.0
2.5
1.5
1.25
1.0
filter
Box
Temp
CF)
260
225
250
250
240
Last
Imp.
Gas
Temp
CF>
85
85
88
88
88
Samp I in)
Train
Static
Pressure
("Hg)
2.0
2.0
1.5
1.0
1.0
Clayton Environmental Consultants, Inc.
-------
C-98
SAMPLING TRAIN DATA
(Pag* 4 of 4)
Company: Ford Motor Company
Source Designation! Coke Battery A Scrubber Outlet
7/15/73
Date:
Teat Number; EPA Method 5. Sample-8
Field Person: RGK
Filter Number: A-190-02
Barometric Pressure ("Hg); 29.60
Filter Heater Setting; 200
Probe Heater Setting: 65
Stack Static Pressure ("H20); -0.21
Stack Dimensions; 90" I.D.
Plume Appearance: ^
Ambient Temperature (*F);
Record all Data Every 0,5
Minutes
Notzle Number; — ,Di«.(in.); Q.254
Pitot Tube No. 19 ,Corr.Factor;Q.854
Meter Box No. RAC-3.Corr.Faetor! 0.993
Meter Isokinetic Factor; 1796
Assumed Moisture(X) :
Condensate Volume (ml): 0
Silica Gel Height Gain(g):
Leak Rate CFM at
12
"Hg
Trav-
erse
Point
No.
S-l
Time
Samp-
ling
(secj
0
30
60
Clock
14:09
Velocity
Pressure
("H20)
0.15
•
AVERAGE (TOTAL)
Stack
Temp
(°F)
128
121
(123)
124
Dry Gas Meter
Volume
(ft3)
992.502
( 12.176 >
Temp(°F)
Inlet
83
80
Outlet
83
80
Orifice
Pressure
Differ-
ential
("H20)
0.75
2.1
'liter
Box
Temp
(°F)
230
240
Last
Imp.
Gas
re rap
CF)
88
85
Sampling
Train
Static
Pressure
("Hg)
1.0
1.7
Clayton Environmental Consultants, Inc.
-------
C-99
SAMPLING TRAIN DATA
Ford Motor Company
Companyi
Source Designation; Coke Battery A Scrubber Outlet
(Pege 1 of 4)
7/16/75
Date:
Teet Number; EPA Method 5 Sample-9
Field Person: VWH/CEH
Filter Number: A-190-1S
Barometric Preaaure ("Hg); 29.60
Filter Heater Setting; 250
Probe Heater Setting: 60
Stack Static Pressure ("HgO); -0.21
Steck Dimensions: 90" I.D«
Plume Appearance: --
Ambient Temperature(*F);
Record all Data Every 0.5
75
Minutes
Noscle Number; -- .Die.(in.); 0.254
Pitot Tube No. 19 .Corr.Factor;' 0.854
Meter Box No. RAC-3»Corr.Factor; p.993
Meter Isokinetie Factor; 1796
Assumed Moisture(I);
Condensate Volume (ml): -4
Silica Gel Weight Cain(g); is
Leak Rate 0.001 CFM at 15.0
"Hg
rrav-
erse
Point
No.
B-4
B-3
E-2
E-l
N-4
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
0
30
60
0
30
60
Clock
08:24
08:40
08:53
09:34
09:41
Velocity
Pressure
("H20)
0.37
0.37
(0.38)
0.25
0.18
0.18
0.18
(0.18)
0.15
0.15
(0.15)
0.65
0.65
(0.65)
•
AVERAGE (TOTAL)
Stack
Temp
CP)
120
120
(120)
120
120
(120)
120
120
(125)
120
120
(120)
120
125
(130)
-
Dry Gas Meter
Volume
(ft3)
992.770
993.487
994.087
994.60
995.075
995.923
•
( )
Temp('F)
Inlet
75
77
77
(77)
78
(78)
81
(83)
Outlet
75
75
78
(78)
78
(78)
82
(83)
Orifice
Pressure
Differ.
ential
("H20)
1.75
1.20
0.86
(0.86)
0.72
(0.72)
3.14
(3.14)
filter
Box
Temp
CF)
250
(240)
240
250
(250)
245
(245)
250
(250)
Last
Imp.
Gas
Temp
(•F)
85
(85)
88
84
(86)
85
88
Sampling
Train
Static
Pressure
("Hg)
1.5
1.0
0.80
0.80
3.0
Clayton Environmental Consultants, Inc.
-------
C-100
8AMPLINO TRAIN DATA
Ford Motor Company
Company:
Source Designation; coke Battery A Scrubber Outlet
(Page 2 of 4)
7/16/75
Date:
Teat Number;EPA Method 5 Sample-9.
Field Person: VWH/GEH
Filter Number: A-190-15
Barometric Pressure ("Hg); 29.60
Filter Heater Setting; 250
Probe Heater Setting: 60
Stack Static Pressure ("HgO); -0.21
Stack Dimensions: 90" I.D.
Plume Appearance: --
Ambient Temperature (°F):_
Record all Data Every
75
0.5 Minutea
Noccle Number; -- tDia.(in.); 0.254
Pitot Tube No.19 ,Corr.Factor; 0.854
Meter Box No. RAC-3«Corr.Factor; 0.993
Meter Zsokinetic Factor; 1796
Assumed Moisture(X):
Condensate Volume (ml): 4
Silica Cel Weight Cain(g); 15
Leak Rate CFM at "Hg
Trav-
erse
Point
No.
N-3
N-2
N-l
W-4
W-3
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
0
30
60
0
30
60
Clock
09:52
10:06
10:35
10:50
11:09
Velocity
Pressure
("H20)
0.73
0.73
(0.73)
0.60
0.60
(0.60)
0.45
0.45
(0.45)
0.58
0.58
(0.58)
0.68
0.68
(0.68)
•
AVERAGE (TOTAL)
Stack
Temp
(«F)
125
125
(130)
120
120
(125)
120
120
(125)
120
125
(130)
120
125
(125)
Dry Gas Meter
Volume
(ft3)
996.968
997.868
998.673
999.590
1000.572
( )
TempCF)
Inlet
84
(85)
85
85
(85)
86
87
(87)
87
87
(87)
87
87
(87)
Outlet
84
<85)
85
85
(85)
86
88
(88)
88
88
(88)
88
88
(88)
Orifice
Pressure
Differ-
ential
("H20)
3.51
3.51
(3.51)
2.90
2.9
(2.9)
2.17
2.17
(2.17)
2.81
2.81
(2.81)
3.30
3.3
(3.3)
filter
Box
Temp
CF)
245
(245)
250
255
(255)
255
(255)
250
(250)
Last
Imp.
Gas
Temp
CF)
90
(90)
90
88
(90)
90
(90)
90
(90)
Sampling
Train
Static
Pressure
("Hg)
3.0
(3.0)
2.5
(2.5)
2.0
2.5
(2.5)
3.0
(3.0)
Clayton Environmental Consultants, Inc.
-------
C-101
SAMPLING TRAIN DATA
Ford Motor Company
Company:
Source Designation: Cofca Battery A Scrubber Outlet
Date: 7/16/75
(Page 3 of 4)
Teat Number; EPA Method 5 Sample-9
Field Person: VWH/GKH
Filter Number:
Filter Heater Setting; 250
Probe Heater Setting; 60
A-190-15
Barometric Pressure ("Hg)t 29.60
Stack Static pressure ("HgO): -0.21
90" I.D.
Stack Dimensions:
Plume Appearance: .
Ambient Temperature(*F):
Record all Data Every 0.5 Minutes Leak Rate
Mosaic Number; — .Dia. (in.); 0.254
Pitot Tube No. 19.Corr.Factof;0.854
Meter Box No. RAC-3«Cerr. Factor; 0.993
Meter laokinetic Factor; 1796
Assumed Moisture (Z): _
-4
Condensate Volume (ml):
Silica Gel Weight Cain(g); 15
CPM at
"Hg
Trav-
erse
Point
No.
W-2
W-l
S-4
S-3
S-2
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
0
30
60
0
30
60
Clock
11:23
11:37
12:03
12:17
13:40
'
Velocity
pressure
("H20)
0.63
0.63
(0.63)
0.47
0.47
(0.47)
0.34
0.34
(0.34)
0.25
0.25
(0.25)
0.20
0.20
(0.20)
•
AVERAGE (TOTAL)
Stack
Temp
(°F)
120
125
(125)
125
125
(125)
120
125
(125)
125
125
(125)
125
125
(130)
-
Dry Gas Meter
Volume
(ft3)
1001.532
1002.340
1003.046
1003.671
1004.220
( )
Temp(°F)
Inlet
87
87
(88)
88
88
(89)
87
88
(88)
88
88
(88)
88
88
(88)
Outlet
88
88
(89)
89
89
(89)
88
89
(89)
89
89
(89)
90
90
(90)
Orifice
Pressure
Differ-
ential
("H20)
3.06
(3.06)
2.29
2.29
(2.29)
1.66
(1.66)
1.22
(1.22)
0.97
0.97
(0.97)
niter
Box
Temp
(°F)
250
(250)
245
(245)
250
250
(250)
250
250
(250)
245
245
(245)
Last
Imp.
Gas
Temp
CF)
90
(90)
90
(90)
91
91
(91)
91
90
(90)
93
93
(93)
Sampling
Train
Static
Pressure
("Hg)
2.5
2.5
2.0
(2.0)
1.5
1.6
1.0
Clayton Environmental Consultants, Inc.
-------
C-102
SAMPLING TRAIN DATA
Ford Motor Company
Company:___
Source Designation; Coke Battery A Scrubber Outlet
(Page 4 of 4)
7/16/75
Date:
Teat Number;EPA Method 5 Sample-9
Field Person:_
Filter Number:
Barometric Pressure ("Hg)t 29.60
250
60
VWH/GKH
A-190-15
Stack Static Pressure ("H;0); -0.21
Stack Dimensions; 90" I.D.
Plume Appearance: --
Filter Heater Setting^
Probe Heater Setting:^
NoBile Number;-- ,Dia. (in.);0.254
Pitot Tube No. 19,Corr.Factor;0.854
Meter Box No. RAC-3»Corr.Factor; 0.993
Meter Isokinetic Factor; 1786
Assumed Moisture(%):
Ambient Temperature(°F):
Record all Data Every 0.5
75
Minutes
Condensate Volume(ml):
Silica Gel Weight Gain(g):
Leak Rate CFM at
-4
15
•Hg
Trav-
erse
Point
No.
S-l
Time
Samp-
ling
(sec)
0
30
60
Clock
13:48
Velocity
Pressure
("H20)
0.14
0.14
(0.14)
.
•
AVERAGE (TOTAL)
Stack
Temp
CF)
130
130
(130)
123
Dry Gas Meter
Volume
(ft3)
1004.670
( 11.817)
Temp(°F)
Inlet
88
88
(88)
84
Outlet
90
89
(90)
85
Orifice
Pressure
Differ-
ential
("H20)
0.68
0.68
(0.68)
2.0
filter
Box
Temp
CF)
250
(250)
249
Last
Imp.
Gas
Temp
CF)
92
92
(92)
88
Sampling
Train
Static
Pressure
("Hg)
1.0
(1.0)
1.8
Clayton Environmental Consultants, Inc.
-------
C-103
SAMPLING TRAIN DATA
Companyt Ford Motor Company
Coke Battery A Scrubber Inlet
Source Designation:
Date: 2-12-75 ~Filter Heater Setting:
Teat Number; EPA Method 8 Preliminary-l Probe Heater Settlng:_
Field Person; RJG
Filter Number:
Barometric Pressure ("Hg): 29.52
Stack Static Pressure ("H20):
Stack Dimensions; 66" I.D.
Plume Appearance:
Ambient Temperature(°F):
Record all Data Every
Nocsle Number: ,Dia. (in. ) :_._
Pitot Tube No. ,Corr.Factor:
Meter Box No«MAC-5 \Corr.FactonO. 999
Meter Isokinetic Factor;
Assumed Moisture(Z):
Condensate Volume(ml):
Silica Gel Weight Gain(g):
Minutes Leak Rate CFM at
"Hg
Trav-
erse
Point
No.
CL
CL
CL
CL
CL
Time
Samp-
ling
(rain)
Clock
11:16
11:31
11:46
12:01
12:16
Velocity
Pressure
("H20)
.
•
AVERAGE (TOTAL)
Stack
Temp
<°F)
45
42
45
48
45
Dry Gas Meter
Vo lume
(ft3)
204.800
215.880
227.500
238.45
249.325
( 44.480)
Temp(°F)
Inlet
44
39
36
35
38
Outlet
40
39
37
35
38
Orifice
Pressure
Differ-
ential
("H20)
2.0
2.0
2.0
2.0
2.0
filter
Box
Temp
(°F)
Last
Imp.
Gas
rerap
(°F)
Sampling
Train
Static
pressure
("HR)
8.0
9.0
7.0
7.0
7.8
Clayton Environmental Consultants, Inc.
-------
C-104
SAMPLING TRAIN DATA
Company: Ford Motor Company
Coke Battery A Scrubber Inlet
Source Designation:
Date: 2-12-75 Filter Heater Setting:
Teat Numbar; EPA Method 8 Preliminary-2 Probe Heater Setting:_
Field Person! RJG
Filter Number:
,Dia.(in.)•
Barometric Pressure ("Hs)t 29.52
Stack Static Pressure ("H20):
Stack Dimensions: 66" I.D.
Plume Appearance:
Nozzle Number:
••
Pitot Tube No. ,Corr.Factor:
Meter Box No.MAC-5'iCorr.Factor; 0.999
Meter Isokinetic Factor:
Assumed Moisture(I):
Condensate Volume(ml):
Ambient Temperature (T):
Record all Data Every
Silica Gel Weight Gain(g):
Minutes Leak Rate CFM at
"Hg
Trav-
erse
Point
No.
CL
CL
CL
CL
CL
Time
Samp-
ling
(rain)
Clock
12:18
12:33
12:48
13:05
13:18
Velocity
pressure
("H20)
.
AVERAGE (TOTAL)
Stack
Temp
<°F)
40
40
45
42
42
Dry Gas Meter
Volume
(ft3)
249.325
259.82
270.81
283.82
293.163
( 43.794)
Temp(°F)
Inlet
36
34
35
36
35
Outlet
36
34
33
33
34
Orifice
Pressure
Diffe'r-
ential
("H20)
2.0
2.0
2.0
2.0
2.0
••liter
Box
Temp
(°F)
Last
Imp.
Gas
Temp
CF)
Sampling
Train
Static
Pressure
("Hg)
6.0
6.0
8.0
7.0
6.8
Clayton Environmental Consultants, Inc.
-------
C-105
SAMPLING TRAIN DATA
Ford Motor Comoanv
Coke Batterv A Scrubber Inlet
Company:
Source Designation:,
Date: 2-12-75Filter Heater Setting:
Test Number; EPA Method 8 Preliminarv-3 Probe Heater Setting:_
Field Person; RJG
Filter Number:
Barometric Pressure ("Hg); 29.52
Stack Static Pressure ("H20):
Stack Dimensions; 66" I.D.
Plume Appearance:
Nozsle Number: ,Dia.(in.):.
Pltot Tube No. ,Corr.Factor:
Meter Box No.MAC-5 »Corr.Factonp.999
Meter Isokinetic Factor;
Assumed Moisture(X) :
Condensate Volume(ml):
Ambient Temperature(QF):
Record all Data Every
Silica Gel Weight Gain(g):
Minutes Leak Rate CFM at
"Hg
Trav-
erse
Point
No.
CL
CL
CL
CL
CL
•
Time
Samp-
ling
(uin)
Clock
13:28
13:43
13:58
14:13
14:28
Velocity
Pressure
("H20)
•
AVERAGE (TOTAL)
Stack
Temp
(°F)
45
45
42
45
44
Dry Gas Meter
Volume
(ft3)
293.163
304.10
314.73
325.76
336.462
( 43.256)
Temp(°F)
Inlet
33
34
35
35
34
Outlet
33
32
32
32
32
Orifice
Pressure
Differ-
ential
<"H20)
2.0
2.0
2.0
2.0
2.0
Filter
Box
Temp
(°F)
Lest
Imp.
Gas
Temp
(°F)
•
Sampling
Train
Static
Pressure
("Hg)
6.0
6.0
7.0
7.0
6.5
Clayton Environmental Consultants, Inc.
-------
C-106
Company:
Source Designation:^
Date: 6/5/75
SAMPLING TRAIN DATA
Ford Motor Company
Coke Battery A Scrubber.Inlet
Teat Number; EPA Method 8 Sample-1
Field Person; ROM
Filter Number;
Barometric Pressure ("Hg): 28.85
Filter Heater Setting; 90
Probe Heater Setting; 90
Stack Static Pressure ("H?0); -5.0
Stack Dimensions; 66" I.D«
Plume Appearance;
Ambient Temperature("F): 73
Record all Data Every 0.25
Minutes
Nossle Number; -- ,Dia.(in.); 0.188
Pitot Tube No. 18,Corr.Factor; 0.838
Meter Box No.RAC-1.Corr.Factor;0.974
Meter Isokinetic Factor; 1720
Assumed Moisture(Z): 1
Condensate Volume(ml);
Silica Gel Weight Gain(g):_--
Leak Rate 0.01 CPM at 14 "Hi
Trav-
erse
Point
No.
S-7
S-7
S-7
Time
Samp-
ling
(sec)
0
15
30
45
60
0
15
30
45
60
0
15
30
45
60
Clock
15:02
15:03
15:22
15:23
16:13
16:14
Velocity
Pressure
("H20)
1.35
1.55
1.65
1.45
1.45
1.5
1.65
1.45
1.45
•
AVERAGE (TOTAL)
Stack
Temp
(°P)
86
135
210
180
125
89
105
295
210
140
87
200
Dry Gas Meter
Volume
(ft3)
276.637
277.636
277.643
278.652
278.6
279.79
( )
Temp(-F)
Inlet
80
86
84
Outlet
80
84
82
Orifice
Pressure
Differ-
ential
("H20)
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
••liter
Box
Temp
CF)
225
200
Last
Imp.
Gas
Temp
CP?
76
80
Sampling
Train
Static
Pressure
("Hg)
6.0
6.5
7.0
Clayton Environmental Consultants, Inc.
-------
C-107
SAMPLING TRAIN DATA
Company; Ford Motor Company
Source Designation:
Data: 6/5/75 "
Coke Battery A Scrubber Inlet
90
Test Humbert EPA Method
Field Peraon:
90
RCM
Filter Number: --
Barometric Preaaure (**Hg); 28.85
Stack Static Preaaure ("HgO); _s.o
Stack Dimensions; 66" I«D.
Plume Appearance;
Filter Heater Setting:,
8 Sample-Kcont.) Probe Heater Setting:
_________________ Noaale Number: — .Dia. (in. ) i .0.188
. Pitot Tube No. 18.Corr.Factor: 0.838
__ Meter Box No. RAC-li Corr. Factor; 0.974
_ Meter laokinetie Factor; 1720
Assumed Moisture(I); 1
Condenaate Volume(ml); —
73
Ambient Temperature(*F):
Record all Data Every 0.25
Minutes
Silica Gel Weight Cain(g); --
Leak Rate
CFM at
fHg
trav-
erae
Point
No.
S-7
Time
Samp-
ling
(sec)
0
15
30
45
60
Clock
16:25
16:26
(Telocity
Preaaure
<"H20>
1.45
1.50
1.50
1.50
•
AVERAGE (TOTAL)
Stack
Temp
CD
85
120
155
170
130
148
(Orifice
Dry Gaa Meter [pressure
Vo lume
(£t3)
279.79
280.700
„
( 3.957 )
Temp(-P)
Inlet
84
84
Outlet
84
82
Differ-
ential
("H20)
3.4
3.4
3.4
3.4
3.4
filter
Box
Temp
CF)
220
215
Last
Imp.
Gaa
Temp
rp?
80
79
Sampling
Train
Static
Preaaure
("Hg)
6.5
6.5
Clayton Environmental Consultants, Inc.
-------
C-108
SAMPLING TRAIN DATA
Ford Motor Company
Coapony:_
Source Designation; Coke Battery A Scrubber Inlet
6/6/75
Date: _
Teat Numbert EPA Method 8 Sample-2
Field Person; ROM
Filter Number: --
Barometric Pressure ("Hg)t 28.80
Filter Heater Setting; 90
Probe Heater Setting; 90
Stack Static Pressure ("H?0); -5.1
Stack Dimensions; 66" I.D.
Plume Appearance: --
65
Ambient Temperature('F):
Record all Data Every 0.25
Minutes
Nossle Number; — .Dia.(in.); 0.188
Pltot Tube No. 18 ,Cerr.Factor; 0.838
Meter Box No. RAC-liCorr. Factor. 0.974
Meter Isoklnetlc Factor; 1720
Assumed Moisture(X); 1
Condensate Volume(ml);
Silica Gel Weight Galn(g):__-_
Leak Rate 0.005 CFM at
17 "Kg
Trav-
erse
Point
No.
S-7
S-7
S-7
Time
Samp-
ling
(sec)
0
15
30
45
60
0
15
30
45
60
0
15
30
45
60
Clock
10:04
10:05
10:27
10:28
10:49
10:59
(Telocity
Pressure
("H20)
1.45
1.5
1.6
1.5
1.4
1.5
1.55
1.45
1.45
1.55.
1.6
1.65
•
AVERAGE (TOTAL)
Stack
Temp
(°F)
78
120
185
195
120
80
125
190
150
115
84
110
200
195
140
139
Dry Gas Meter
Volume
(ft3)
280.828
281.853
281.858
282.878
282.883
283.904
( 2.996 )
TempCF)
Inlet
76
78
82
79
Outlet
73
78
78
76
Orifice
Pressure
Differ-
ential
<"H20)
3.4
3.4
3.4
3.4
3.4 .
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
?ilterta8t
Box F-P-
(•?; F
( F) (.p)
280 | 68
200
225
235
70
70
69
Sampling
Train
Static
Pressure
("Hg)
7.0
7.0
7.0
7.0
Clayton Environmental Consultants, Inc.
-------
C-109
SAMPLING TRAIN DATA
Ford Motor Company
COBpanyi
Source Designation; Coke Battery A Scrubber Inlet
6/6/75
Date:
Test Number:_ EPA Method 8 Sample-3
Field Person:
Filter Humbert
Barometric Preaaure ("Hg)i 28.80
Filter Heater Setting; 90
Probe Heater Setting: 90
ROM
Stack Static Preasure ("HgO): ,5.0
Stack Dtmenaiona; 66" I.D.
Plume Appearance: ...
Anbient Temperature(*F):
Record all Data Every 0.25
68
Minutes
Moasle Mumber; -- .Die.(in.); 0.188
Pitot Tube Ho. 18.Cerr.Factor; 0.838
Meter Box Ho.RAC-l.Corr.Factor;0.974
Meter laokinetie Factor; 1720
Aeaumed Molature(Z): 1
Condenaate Volume (ml): -_-
Silica Gel Weight Gain(g);
Leak Rate 0.01 CFM at 18 "Hg
rrav-
erae
Point
Ho.
S-7
S-7
S-7
Tlme (Velocity
Samp-
ling
(aec)
0
15
30
45
60
0
15
30
45
60
0
15
30
45
60
Eeaaure
"H20)
1.4
11:28
11:41
11:42
11:50
11:51
1.55
1.55
1.45
1.35
1.4
1.5
1.4
1.35
1.4fr
1.55
1.45
AVERAGE (TOTAL)
Stack
Temp
(•F)
86
90
125
115
100
84
125
220
180
125
84
130
210
160
120
130
Dry Gaa Meter
Volume
(ft*)
298.783
299.789
299.793
-
300.805
300.808
301.820
( 2.958 )
Temp(»F)
Inlet
86
84
84
85
Outlet
82
80
82
81
Orifice
Preaaure
Differ-
ential
("H20)
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
filter
Box
Temp
CF)
220
220
220
220
Last
Imp.
Gaa
Temp
CP>
70
70
70
70
Sampling
Train
Static
Preaaure
("Hg)
5.0
5.0
5.5
5.2
Clayton Environmental Consultant*, Inc.
-------
C-110
8AHPLINC TRAIN DATA
Company; Ford Motor Company
Source Designation; Coke Battery A Scrubber lulet
6/6/75
Date:
Teat Number; EPA Method 8 Sample-4
Field Person; ROM
Filter Number;
Filter Heater Setting:
Probe Heater Setting:
90
90
Barometric Pressure ("Hg); 28.80
Stack Static Pressure ("HgO); -4.5
Stack Dimensions; 66" I.D.
Plume Appearance: --
Ambient Temperature(*F); 69
Record all Data Every 0.25 Minutes
Nozile Number; -- ,Dia.(in.); Q. 188
Pitot Tube No. 18.Corr.Factor; 0.838
Meter Box No.RAC-1.Corr.Factor;0.974
Meter Isoklnetic Factor; 1720
Assumed Moisture(I); 1
Condensate Volume(ml);
Silica Gel Weight Cain(g); --
Leak Rate 0.00 CFM at
16 "Hg
Trav-
erse
Point
No.
S-7
S-7
S-7
Time
Samp-
ling
(sec)
0
15
30
45
60
0
15
30
45
60
0
15
30
45
60
Clock
13:38
13:39
13:55
13:56
14:10
14:11
Velocity
Pressure
("H20)
1.30
1.5
1.55
1.45
1.40
1.45
1.60
1.45
1.40
1.45
1.65
1.45
AVERAGE (TOTAL)
Stack
Temp
(•P)
83
125
200
160
115
85
110
180
175
120
84
105
240
185
135
140
Dry Gas Meter
Volume
(ft3)
317.018
318.018
318.023
319.033
319.036
320.048
( 2.951 )
Temp('F)
Inlet
78
80
80
79
Outlet
76
78
79
78
Orifice
Pressure
Differ-
ential
("H20)
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
niter
Box
Temp
CF)
220
240
240
233
Last
Imp.
Gas
Temp
rp?
72
72
72
72
Sampling
Train
Static
Pressure
("Hg)
6.0
6.0
6.0
6.0
Clayton Environmental Consultants, Inc.
-------
C-lll
8AHFLXNG TRAIN DATA
Ford Motor Company
Company:
Source Designation; Coke Battery A Scrubber Inlet
6/6/75
Data:
Test Number; EPA Method 8 Sample-5
Filter Heater Setting; 90
probe Heater Setting; 90
Field Person; MM
•Filter Number:
Barometric Pressure ("Hg):
Stack Static Pressure (
Stack Dimensions; 66" I'D*
Plume Appearance:
28.80
Ambient Temperature(*F):
NoHle Number;--- .Dia. (in.); _0» 188
Pltot Tube No. 18 .Corr.Factor;0*838
Meter Box Mo. RAC-1,Corr.FactoRO.974
Meter Isoklnetic Factor; 1720
Assumed Moisture(X): 1
Condensate Volume(ml);
Silica Gel Weight Cain(g);
Record all Data Every 0.25 Minutes Leak Rate 0.00 CFM at 15 "Hg
Trav-
erse
Point
No.
S-7
S-7
S-7
Time
Samp-
ling
(sec)
0
15
30
45
60
0
15
30
45
60
0
15
30
45
60
Clock
14:58
14:59
15:10
15:11
15:22
15:23
Velocity
Pressure
("H20)
1.30
1.5
1.5
1.40
1.35
1.6
1.6
1.55
1.4
1.45
1.55
1.5
AVERAGE (TOTAL)
Stack
Temp
(°F)
85
130
205
170
135
84
175
325
225
150
83
135
180
190
125
160
Dry Gas Meter
Volume
(ft3)
335.313
336.312
336.315
-
337.329
337.332
338.365
( 2.973)
Temp('P)
Inlet
84
80
80
81
Outlet
81
78
78
79
Orifice
Pressure
Differ-
ential
<"H20)
3.4
3.4
3.4
3.4
3.4
3.4
3,4
3.4
3.4
3.4
3.4
3.4
3.4
filter
Box
Temp
(•F)
220
220
240
227
Last
Imp.
Gas
Cemp
CP}
74
72
74
73
Sampling
Train
Static
Pressure
("Hg)
5.0
5.0
5.2
5.1
Clayton Environmental Consultants) Inc.
-------
C-112
SAMPLING TRAIN DATA
Ford Motor Comoanv
Company:
Source Designation; Coke Battery A Scrubber Inlet
6/9/75
Date:
Teat Number; EPA Method 8 Sample-6
Field Person:_
Filter Number:
Filter Heater Setting; 95
Probe Heater Setting; 90
ROM
Berometrie Pressure ("Hg)t 29.42
Steek Static Pressure ("H?0); -4.6
Stack Dimensions:
Plume Appearance:
66" I.D.
Ambient Temperature("F); 70
Record all Data Every 0.25 Minutes
Nocsle Number; -- .Dia.(in.); 0.188
Pitot Tube No. 18,Corr.Factor; 0.838
Meter Box Ho.RAC-l'«Corr.Factor; 0.974
Meter Isokinetic Factor; 1720
Assumed Moisture (1): 1 fr
Condensate Volume(ml);
Silica Gel Height Gain(g); -- •
Leak Rate 0.00 CFM at
15 "Hg
Trav-
erse
Point
No.
S-7
S-7
S-7
Time
Samp-
ling
(sec)
0
15
30
45
60
0
15
30
45
60
0
15
30
45
60
Clock
10:58
10:59
11:15
11:16
11:28
11:29
(Telocity
Pressure
("H20)
1.30
1.5
1.6
1.4
1.30
1.5
1.65
1.5
1.35
1.4.
1.55
1.45
AVERAGE (TOTAL)
Stack
Temp
CF)
98
160
245
195
140
92
105
225
195
145
90
120
300
210
150
165
Dry Gas Meter
Volume
(£t3)
353.899
354.772
354.778
355.763
355.766
356.757
( 2.784 )
TempCF)
Inlet
72
75
75
74
Outlet
72
74
75
74
Orifice
Pressure
Differ-
ential
("H20)
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
••liter
Box
Temp
(•F)
235
250
240
242
Last
Imp.
Gas
Cemp
CF>
70
73
75
73
Sampling
Train
Static
Pressure
("Hg)
5.0
6.0
6.0
5.7
Clayton Environmental Consultants, Xne,
-------
C-113
SAMPLING TRAIN DATA
Company; Ford Motor Company
Source Designation; Coke Battery A Scrubber Inlet
Date: 6/9/75
Test Number; EPA Method 8 Sample-7
Field Persons RCM
Filter Number;
Barometric Pressure ("Hg)! 29.42
Filter Heater Setting:.
Probe Heater Setting:
90
90
Stack Static Pressure ("HgO); -4.6
Stack Dimensions; 66" I.D.
Plume Appearance;
Ambient Temperature(*F); 72
Record all Data Every 0.25
Minutes
Nocsle Number; -- .Dla. (In.)*. 0.188
Pltot Tube No. 18.Corr.Factor: 0.838
Meter Box No.RAC-l.Corr.Factor; 0. 974
Meter Isoklnetlc Factor; 1720
Assumed Moisture(X); 1
Condensate Volume(ml):
Silica Gel Weight Gain(g); --
Leak Rate 0.00 CFM at
18 "Hg
Trav-
erse
Point
No.
S-7
S-7
S-7
Time
Samp-
ling
(aec)
0
15
30
45
60
0
15
30
45
60
0
15
30
45
60
Clock
13:35
13:36
13:45
13:46
14:03
14:04
Velocity
Pressure
("H20)
1.35
1.35
1.65
1.5
1.35
1.5
1.6
1.4
1.40
1.40
1.55
1.5
•
AVERAGE (TOTAL)
Stack
Temp
(•F)
93
135
210
210
150
97
125
210
190
135
103
115
190
200
150
154
Dry Gas Meter
Volume
(ft3)
372.869
373.820
373.824
374.812
374.815
375.794
( 2.849 )
Temp(-F)
Inlet
70
74
76
73
Outlet
70
72
74
72
Orifice
Pressure
Differ-
ential
C'HzO)
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
filter
Box
Temp
CF)
245
250
240
245
Last
Imp.
Gas
Temp
CP?
75
75
77
76
Sampling
Train
Static
Pressure
("Hg)
5.0
5.5
5.5
5.3
Clayton Environmental Consultants, Inc.
-------
C-114
SAMPLING TRAIN DATA
Ford Motor Company
Company:_
Source Designation; Coke Battery A Scrubber Inlet
6/9/75
Data:
Test Number! EPA Method 8 Sample-8
Field Persont_
Filter Number: --
Barometric Pressure ("Hg); 29.42
Filter Heater Setting; 95
Probe Heater Setting! 95
ROM
Stack Static Pressure ("H;0); -5.2
Stack Dimensions; 66" I.D.
Plume Appearance:
Ambient Temperature(°F); 72
Record all Data Every 0.25
Minutes
Noxsle Number; -- .Dia.(in.); 0.188
Pltot Tube No. 18,Corr.Factor: 0.838
Meter Box No. RACJ.Corr.Factor;0.974
Meter Zsokinetic Factor; 1720
Assumed Moisture(I); 1
Condensate Volume(ml);
Silica Gel Height Cain(s);
Leak Rate 0.00 CPM at 18 "Hg
Trav-
erse
Point
No.
S-7
S-7
•
S-7
Time
Samp-
ling
(sec)
0
15
30
45
60
0
15
30
45
60
0
15
30
45
60
Clock
14:32
14:33
14:47
14:48
15:02
15:03
Velocity
Pressure
("H20)
1.40
1.40
1.55
1.45
1.35
1.55
1.65
1.45
1.40
1.40'
1.65
1.55
AVERAGE (TOTAL)
Stack
Temp
(°F)
102
120
190
180
150
99
160
285
240
175
108
175
295
225
175
179
Dry Gas Meter
Volume
(ft3)
390.383
391.356
391.358
392.330
392.333
393.305
( 2.846 )
Temp(°F)
Inlet
75
75
76
75
Outlet
75
75
76
75
Orifice
Pressure
Differ-
ential
("H20)
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
filter
Box
Temp
(-F)
240
245
240
242
Last
Imp.
Gas
Temp
CF>
76
76
77
76
Sampling
Train
Static
Pressure
("Hg)
5.5
6.0
6.0
5.8
Clayton Environmental Consultants, Inc.
-------
C-115
SAMPLING TRAIN DATA
Company: Pord Motor Company
Source Dasignatloa; Coke Battery A Scrubber inlet
6/10/75
Date:
Teat Number; EPA Method 8 Sample-9
Field Person:,
Filter Number: ^
Barometric Pressure ("Hg); 29.52
Filter Heater Setting:,
Probe Heater Setting:
90
90
JLCM_
Stack Static Pressure ("HgO); -5.2
Stack Dimensions: 66" I.D.
Plume Appearance;
Ambient Temperature(*F):
Record all Data Every 0.25
65
Minutes
NoBcle Number; -- .Dia.(in.); 0.188
Pitot Tube No. 18.Corr.Factor; 0.838
Meter Box No.RAC-1,Corr.Factor0.974
Meter Isokinetic Factor; 1720
Assumed Moisture(I); 1
Condensate Volume (ml): --
Silica Gel Height Gatn(g);
Leak Rate 0.00 CFM at 15 "Hg
Trav-
erse
Point
No.
S-7
S-7
S-7
Time
Samp-
ling
(sec)
0
15
30
45
60
0
15
30
45
60
0
15
30
45
60
Clock
09:33
09:34
09:50
09:51
10:14
10:15
Velocity
Pressure
("H20)
1.40
1.4
1.65
1.45
1.40
1.40
1.7
1.55
1.35
1.6'
1.8
0.9
•
AVERAGE (TOTAL)
Stack
Temp
CF)
94
115
175
190
135
104
110
170
275
190
98
140
250
250
175
165
Dry Gas Meter
Volume
(£t3)
410.298
411.271
411.273
-
412.274
412.281
413.259
( 2.884 )
TempCP)
Inlet
68
68
70
69
Outlet
68
68
70
69
Orifice
Pressure
Differ-
ential
("H20)
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
3.4
niter
Box
Temp
(•F)
200
240
240
227
Last
Imp.
Gas
Temp
fV)
70
72
74
72
Sampling
Train
Static
Pressure
("Hg)
6.0
6.5
6.5
6.3
Clayton Environmental Consultants, Inc.
-------
C-116
Company;
Source Designation:
Data: 6/5/75
SAMPLING TRAIN DATA
Ford Motor Company
Coke Battery A Scrubber Outlet
Tact Number; EPA Method 8 Sample-1
Field Person: VWH/GMS
Filter Number: --
Filter Heater Setting; 250
Probe Heater Setting; 95
Barometric Pressure ("Hg); 28.85
Stack Static Pressure ("H?0); -2.6
90" i.p.
Stack Dimensions:_
Plume Appearance: --
Ambient Temperature(°F); 75
Nossle Number; -- ,Dia.(in.); 0.256
Pitot Tube No. 19,Cerr.Factor; 0.854
Meter Box No. RAC-4»Corr.Factor; p. 991
Meter Isokinetic Factor; 1685
Assumed Moisture(I);
Condensate Volume(ml);
Silica Gel Weight Cain(g);
Record all Data Every 0.5
Minutes Leak Rate
0.001CFM at
15 "Hg
Trav-
erse
Point
No.
N-6
N-6
N-6
N-6
Time
Samp-
ling
fsecj
0
30
60
0
30
60
0
30
60
0
30
60
Clock
15:02
15:03
15:22
15:23
16:13
16:14
16:25
16:26
Velocity
Pressure
("H20)
0.69
0.65
0.67
0.70
0.60
0.68
0.68
0.68
0.68
0.68
0.68
0.68.
AVERAGE (TOTAL)
Stack
Temp
(°F)
123
125
128
120
122
124
125
126
128
125
130
133
126
Dry Gas Meter
Volume
(ft3)
478.843
479.3
479.723
480.3
480.731
481.1
481.725
482.3
482.732
(3.913 )
Temp(°F)
Inlet
80
78
80
80
80
79
79
79
79
79
79
Outlet
80
80
80
80
80
80
80
80
80
80
80
Orifice
Pressure
Differ-
ential
("H20>
3.3
3.3
3.3
3.3
3.3
3.3
3.3
3.3
3.3
3.3
3.3
3.3
3.3
filter
Box
Temp
CF)
280
280
280
280
290
290
290
260
260
279
Last
Imp.
Gas
Temp
CF)
82
82
82
79
80
80
84
82
81
Sampling
Train
Static
Pressure
("Hg)
14.0
14.0
14.0
14.0
14.0
14.0
14.0
14.0
Clayton Environmental Consultants, Inc.
-------
C-117
SAMPLING TRAIN DATA
Ford Motor Company
Company:_
Source Deaignation; Coke Battery A Scrubber Outlet
6/6/75
Data:
Teat Number; EPA Method 8 Samplc-2
Field Person! PIC/GMS
Filter Number: --
Barometric Preaaure ("Hg): 28.80
Stack Static Preaaure ("H?0>; -2.6
Stack Dimensions; 90" I.D.
Plume Appearance: ^
Filter Heater Setting; 250
Probe Heater Setting; 95
Ambient Temperature(*F):
Record all Data Every 0.5
75
Minutes
Hoc lie Number; -- .Dia. (in.);'0. 256
Pitot Tube No. 19.Corr.Factor; 0.854
Meter Box He. RAC-4»Corr.Factor; 0.991
Meter laokinetic Factor; 1685
Assumed Moisture (X): --
Condenaate Volume (ml): -_-
Silica Gel Weight Caln(g);
Leak Rate CFM at "Hg
Trav-
erae
Point
No.
65
65
65
65
65
65
72
72
72
67
Sampling
Train
Static
Preaaure
("Hg)
4.0
4.0
4.1
4.2
4.2
4.2
4.0
4.0
4.0
4.1
Clayton Environmental Consultants, Inc.
-------
C-118
SAMPLING TRAIN DATA
Company; Ford Motor Company
Source Designation; Coke Battery A Scrubber outlet
6/6/75
Date:
Tact Number; EPA Method 8 Sample-3
Field Person:__
Filter Number: --
Barometric Pressure ("Hg); 28.80
PIC/GMS
Stack Static Pressure ("^0): -2.6
Stack Dimensions; 90" I.D.
Plume Appearance: --
Filter Heater Setting; 250
Probe Heater Setting: 95
Ambient Temperature(°F): 75
Record all Data Every 0,5 Minutes
Nocsle Number; -- .Dia.(in.): 0.256
Pitot Tube No. 19«Corr.Factor; 0.854
Meter Box No.RAC-4«Corr. Factor; 0.991
Meter Isokinetic Factor; 1685
Assumed Moisture(I);
Condensate Volume(ml);
Silica Gel Weight Gain(g):_--
Leak Rate CPM at "Hg
Trav-
erse
Point
No.
72
72
72
72
72
72
72
72
72
72
Sampling
Train
Static
Pressure
("Hg)
4.0
4.0
4.0
4.0
4.0
4.0
4.0
4.0
4.0
4.0
Clayton Environmental Consultants, Inc.
-------
C-119
Company:
Source Designation:^
Data: 6/6/75
8AHPLXNC TRAIN DATA
Ford Motor Company
Coke Battery A Scrubber Outlet
Teat number; EPA Method 8 Sample-4
Field Peraon;
Filter Number:
Filter Neater Setting; 250
Probe Heater Setting: 95.
FIC/GMS
Barometric Pressure ("Hg); 28.80
Stack Static Pressure ("H;0); -2.6
Stack Dimensions!
Plume Appearance:
90" I.D.
Ambient Temperature(*P); 75
Record all Data Every 0.5
Minutes
Nocile Number; -- .Dia. (in.) ;J). 256
Pitot Tube No. 19.Corr.Factor; 0,854
Meter Box No.RAC-4tCorr,Factor;0.991
Meter laokinetic Factor; 1685
Assumed Moisture(I);
Condensate Volume(ml);
Silica Gel Weight Galn(g):_--
Leak Rate
CFM at
"Hg
Trav-
erse
Point
No.
1
-------
C-120
8AHPLXNC TRAIN DATA
Ford Motor Company
Company;
Source Designation; Coke Battery A Scrubber Outlet
6/6/75
Date:
Test Number; EPA Method 8 Sample-5
Field Person: Pic/CMS
Filter Number: --
Barometric Pressure ("Hg); 28.80
Stack Static Pressure ('M^O): -2.6
Stack Dimensions; 90" I.D.
Plume Appearance: _-
Filter Heater getting; 250
Probe Heater Setting: 95
Ambient Temperature(°F):
Record all Data Every 0.5
75
Minutes
Nocale Number; -- ,Dia.(in.); 0.256
Pitot Tube Mo. 19.Corr.Factor: 0.854
Meter Box No.RAC-4,Corr.Factor0.991
Meter Isokinetic Factor; 1685
Assumed Moisture(I);
Condensate Volume (ml): --
Silica Gel Weight Cain(g);
Leak Rate CFM at "Hg
Trav-
erse
Point
No.
-------
C-121
SAMPLING TRAIN DATA
Ford Motor Company
Company:_
Source Designation; Coke Battery A Scrubber Outlet
6/9/75
Date:
Test Number; EPA Method 8 Sample-6
Field Person: GMS/RJG
Filter Number;
Barometric Pressure ("Hg); 29.42
Filter Heater Setting; 250
probe Heater Setting; 80
Stack Static Pressure ("H?0); -2.6
Stack Dimensions: 90" I.D.
Plume Appearance: --
Ambient Temperature(*F); 75
Record all Data Every 0.5
Minutes
Nocsle Number; -- .Die, (in.) ; 0..256
Pltot Tube No. 19.Corr.Factor; 0.854
Meter Box No.RAC-4 .Corr.FactonQ. 991
Meter Isokinetic Factor; 1685
Assumed Moisture(I);
Condensate Volume (ml): --
Silica Gel Weight Galn(g);
Leak Rate CFM at "Hg
Trav-
erse
Point
No.
NW-6
NW-6
NW-6
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
Clock
10:58
10:59
11:15
11:16
11:28
11:29
Velocity
Pressure
<"H20)
0.65
0.64
0.64
0.67
0.67
0.67
0.70
0.67
0.64
•
•
AVERAGE (TOTAL)
Stack
Temp
(•F)
127
127
127
126
126
126
126
126
126
126
Dry Gas Meter
Volume
(£t3)
535.996
535.5
535.918
535.918
536.4
536.854
536.854
537.3
537.818
( 1.806 )
Temp('F)
Inlet
67
68
70
70
70
70
70
70
70
69
Outlet
68
68
70
71
71
71
71
7l'
71
70
Orifice
Pressure
Differ-
ential
("H20)
3.3
3.3
3.3
3.3
3.3
3.3
3.3
3.3
3.3
3.3
••liter
Box
Temp
CF)
250
260
270
270
280
290
280
260
250
268
Last
Imp.
Gas
Temp
CF)
70
70
70
74
76
78
77
77
77
74
Sempling
Train
Static
Pressure
("Hg)
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
Clayton Environmental Consultants, Inc.
-------
C-122
SAMPLING TRAIN DATA
Company; Ford Motor Company
Source Designation; Coke Battery A Scrubber Outlet
6/9/75
Data:
Test Number; EPA Method 8 Sample-7
Field Person:_
Filter Number:
Filter Heater Batting:
Probe Heater Setting:
250
80
GMS/RJG
Barometric Presaure ("Hg); 29.42
Stack Static Presaure ("H?0); -2.6
Stack Dimensions: 90" I.D.
Plume Appearance: -_-
Ambient Temperature (*F): 75
Record all Data Every p.5
NocEle Number; _. .Dia.(in.); p.256
Pitot Tube No. 19.Corr.Factor; 0.654
Meter Box No.RAC-4 ,Corr.FactonO.991
Meter Isokinetic Factor; 1685
Assumed Moisture(I);
Condenaate Volume(ml);
Silica Gel Weight Catn(g);
Minutes Leak Rate
CFM at
"Hg
Trav-
erse
Point
No.
NW-6
NW-6
NW-6
Time
Samp-
ling
(sec )
0
30
60
0
30
60
0
30
60
Clock
13:22
13:23
13:45
13:46
14:03
14:04
Velocity
Pressure
(MH20)
0.63
0.63
0.65
0.67
0.66
0.67
0.63
0.65
0.64
•
AVERAGE (TOTAL)
Stack
Temp
(°F)
125
126
126
125
125
125
125
126
126
125
Dry Gas Meter
Volume
(ft3)
550.659
551.1
551.646
551.646
552.1
552.617
552.617
553.1
553.600
(2.917 )
Temp('P)
Inlet
70
70
70
72
72
72
72
72
72
71
Outlet
72
72
72
73
73
73
73
73
73
73
Orifice
Pressure
Differ-
ential
("H20)
3.3
3.3
3.3
3.3
3.3
3.3
3.3
3.3
3.3
3.3
filter
Box
Temp
CF)
230
250
250
260
260
260
250
250
250
251
Last
Imp.
Gas
Temp
CF)
74
74
74
75
75
75
78
78
78
76
Sampling
Train
Static
Pressure
("Hg)
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
Clayton Environmental Consultants, Inc.
-------
C-123
SAMPLING TRAIN DATA
Companyt 7ord Motor Company
Source Designation; Coke Battery A Scrubber Outlet
6/9/75
Date:
Te«t Humbert EPA Method 8 Sample-8
Field Peraon; CMS/RJG
Filter Number: --
Barometric Pressure ("Hg)t 28.42
Filter Heater Setting:
Probe Heater Setting:
250
80
Stack Static Preaaure ("H?0); .2.6
Stack Dimensions; 90" I.D.
Plume Appearance: --
Ambient Temperature(°F); 75
Record all Data Every 0.5
Minutes
Nosile Number; -. .Dia.(in. ); p. 256
Pitot Tube No. 19.Corr.Factor; Q.854
Meter Box No. RAC-4,Corr.FaetenO.991
Meter Isokinetic Factor; 1685
Assumed Moisture (Z): --
Condenaate Volume(ml);
Silica Gel Weight Cain(g);
Leak Rate CFM at "Hg
Trav-
erse
Point
NO.
NW-6
NW-6
NW-6
Time
Samp-
ling
(sec y
0
30
60
0
30
60
0
30
60
Clock
14:32
14:33
14:47
14:48
15:02
15:03
Velocity
ressure
("H20)
0.64
0.64
0.64
0.66
0.64
0.63
0.64
0.62
0.62
•
AVERAGE (TOTAL)
Stack
Temp
(°F)
126
127
127
125
130
130
126
135
135
129
Dry Gas Meter
Volume
(ft3)
568.563
569.1
569.613
569.613
570.1
570.572
570.572
571.0
571.539
( 2.949 )
Temp(-F)
Inlet
72
72
72
72
72
72
73
73
73
72
Outlet
73
73
73
73
73
73
74
74
74
73
Orifice
Pressure
Differ-
ential
("H20)
3.3
3.3
3.3
3.3
3.3
3.3
3.3
3.3
3.3
3.3
Filter
Box
Temp
CF)
250
260
260
245
250
26 0~
230
235
235
247
Last
Imp.
Gas
Temp
rp?
82
82
82
80
80
80
80
80
80
81
{Sampling
Train
Static
Pressure
("Hg)
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
Clayton Environmental Consultants, Inc.
-------
C-124
SAMPLING TRAIN DATA
Company; Ford Motor Company
Source Designation; Coke Battery A Scrubber Outlet
6/10/75
EPA Method 8 Sample-9
GMS/RJG
Date:
Test Number:_
Field Person:
Filter Number: --
Barometric Pressure ("Hg); 29.52
Stack Static Pressure ("H?0); -2.6
Stack Dimensions; 90" I.D.
Plume Appearance: --
Filter Heater Setting:
Probe Heater Setting!
250
80
Ambient Temperature(*F); 75
Record all Data Every 0,5
Minutes
Notsle Number; -- .Dia. (in.); 0.256
Pitot Tube No. 19«Corr.Factor;Q.854
Meter Box No.RAC-4.Corr.FactonO.991
Meter Isokinetic Factor; 1685
Assumed Moisture(I);
Condensate Volume(ml);
Silica Gel Weight Gain(g):_--
Leak Rate
CFM at
"Hg
Trav-
erse
Point
No.
NW-6
NW-6
NW-6
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
Clock
09:33
09:34
09:50
09:51
10:14
10:15
Velocity
Pressure
("H20)
0.62
0.64
0.64
0.64
0.64
0.64
0.63
0.63
•
AVERAGE (TOTAL)
Stack
Temp
CF)
120
122
124
130
132
132
130
132
132
128
Dry Gas Meter
Volume
(ft3)
586.894
587.3
587.740
587.740
588.2
588.713
588.996
589.4
589.843
( 2.922 )
Temp(°F)
Inlet
66
66
66
66
66
66
67
68
68
-,
67
Outlet
67
67
67
68
68
68
68
70
70
68
Orifice
Pressure
Differ-
ential
("H20)
3.3
3.3
3.3
3.3
3.3
3.3
3.3
3.3
3.3
3.3
filter
Box
Temp
CF)
230
250
260
250
255
255
255
255
255
252
Lastlsampling
Imp. I Train
Gas (static
Tempjpressure
CF) ("Hg)
70
70
70
72
72
72
72
72
72
71
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
Clayton Environmental Consultants, Ine,
-------
C-125
SAMPLING TRAIN DATA
Ford Motor Company
Company j^
Source Designation; Coke Battery A Scrubber Inlet
2-6-75
Date:
Teat Number; Preliminary NaQH-1
Field Person; RCM
Filter Number:
Barometric Pressure ("Hg); 29.28
Stack Static Pressure ("H20): -3.0
Stack Dimensions:_
Plume Appearance:
66" I.P.
Ambient Temperature(°F):
Record all Data Every
Minutes
Filter Heater Setting:
Probe Heater Setting:
Nozzle Number: ,Dia.(in.):>
Pitot Tube No. ,Corr.Factor:
Meter Box No.MAC-5 iCorr.Factor; 0.999
Meter Isokinetic Factor:
Assumed Moisture(Z):
Condensate Volume (ml): ^6
Silica Gel Weight Gain(g):__6
Leak Rate CFM at "Hg
Trav-
erse
Point
No.
CL
CL
CL
6L
CL
Time
Samp-
ling
(rain)
Clock
11:30
11:45
12:00
12:15
12:30
(Telocity
pressure
("H20)
.
AVERAGE (TOTAL)
Stack
Temp
(«F)
38
34
34
32
34
Dry Gas Meter
Volume
(ft3)
961.605
973.8
986.0
998.3
L010.275
Temp(°F)
Inlet
42
39
39
40
( 48.62l)| 40
Outlet
39
38
37
36
38
Orifice
Pressure
Differ-
ential
("H20)
2.5
2.5
2.5
2.5
2.5
filter
Box
Temp
CF)
__
Last
Imp.
Gas
Temp
CF)
_
Sampling
Train
Static
Pressure
("Hg)
4.0
4.5
5.0
5.0
4.62
Clayton Environmental Consultants, Inc.
-------
C-126
SAMPLING TRAIN DATA
Company; Ford Motor Company
Source Designation^
Date: 2-6-75
Coke Battery A Scrubber Inlet
Teat Number; Preliminary NaOH-2
Field Person; RCM
Filter Number:
Barometric Pressure ("Hg); 29.28
Stack Static Pressure ("H20); -3.0
Stack Dimensions! 66" I.D.
Plume Appearance:
Ambient Temperature(CF):
Record all Data Every
Minutes
Filter Heater Setting:
Probe Heater Setting:
NoBBle Number: ,Dia.(in.):_
Pitot Tube No. ,Corr.Factor:
Meter Box No.MdC-5 ,Corr.Factory.999
Meter Isokinetic Factor:
Assumed Moisture(X) :
Condensate Volume (ml): -3
Silica Gel Weight Gain(g); 8
Leak Rate CFM at "Hg
Trav-
erse
Point
No.
CL
CL
CL
CL
CL
Time
Samp-
ling
(rain)
Clock
12:38
12:53
13:08
13:23
13:38
Velocity
Pressure
("H20)
AVERAGE (TOTAL)
Stack
Temp
(•F)
35
38
45
40
40
Dry Gas Meter
Volume
(ft3)
10.275
22.6
34.9
47.1
59.462
( 49.138)
Temp(eF)
Inlet
38
39
39
40
39
Outle t
35
35
35
35
35
Orifice
Pressure
Differ-
ential
<"H20)
2.5
2.5
2.5
2.5
2.5
Filter
Box
Temp
(°F)
__
Last
Imp.
Gas
Temp
<°F)
__
Sampling
Train
Static
Pressure
("Hg)
6.5
6.5
6.5
6.5
6.5
Clayton Environmental Consultants) Inc.
-------
C-127
SAMPLING TRAIN DATA
Ford Motor Company
Company:_
Source Designation; Coke Battery A Scrubber Inlet
2-6-75
Date:
Test Number preliminary NaOH-3
Field Person; RCM
Filter Number:
Barometric pressure ("Hg); 29.28
Stack Static Pressure ('^0); -3.0
Stack Dimensions: 66" I.p.
Plume Appearance:
Filter Heater Setting:
Probe Heater Setting:
Nocele Number: ,Dla.(ln.):.
Pitot Tube No. ,Corr.Factor:
Meter Box No .MAC-5 , Corr.Factonp.999
Meter Isokinetlc Factor:
Assumed Moisture(I):
Condcnsate Volume(ml); -4
Ambient Temperature("F):
Record all Data Every
Minutes
Silica Gel Weight Gatn(g); 9
Leak Rate CFM at
"Hg
Trav-
erse
Point
No.
CL
CL
CL
CL
CL
Time
Samp-
ling
(min)
Clock
14:03
14:18
14:33
14:48
15:03
'
Velocity
Pressure
("H20)
•
AVERAGE (TOTAL)
Stack
Temp
<°F)
33
38
33
35
35
Dry Gas Meter
Volume
(ft3)
59.462
72.6
86.1
99.5
112.463
< 52.948)
Temp(°F)
Inlet
38
37
39
40
38
Outlet
36
34
34
35
35
Orifice
Pressure
Differ-
ential
("H20)
3.0
3.0
3.0
3.0
3.0
Filter
Box
Temp
(°F)
^^^
Last
Imp.
Gas
Temp
(°F)
^^^
Sampling
Train
Static
Pressure
("Hg)
4.5
6.0
6.2
6.0
V
5.68
Clayton Environmental Consultants, Inc.
-------
C-128
SAMPLING TRAIN DATA
Ford Motor Company
Company:
Source Designation; Coke Battery A Scrubber Inlet
2-14-75
Date:
Test Number; preliminary NaOH-4
Field Person; RJG
Filter Number:
Barometric Pressure ("Hg); 29.76
Stack Static Pressure ("H,0):
Stack Dimensions: 66" I.D.
Plume Appearance:
Filter Heater Setting:
Probe Heater Setting:
Nozzle Number: ,Dia.(ln.):
Pltot Tube No. ,Corr.Factor:
Meter Box No«MAC-5'»Corr.Factor;
Meter Isoklnetlc Factor:
Assumed Moisture(X) :
Condensate Volume(ml); -4
Ambient Temperature(°F):
Record all Data Every
Minutes
Silica Gel Weight Galn(g):Ji^
Leak Rate
CFM at
"Hg
Trav-
erse
Point
No.
CL
CL
CL
CL
CL
Time
Samp-
ling
(rain)
Clock
11:18
11:33
11:48
12:03
12:18
Velocity
Pressure
<"H20)
AVERAGE (TOTAL)
Stack
Temp
<°F)
40
40
40
40
40
Dry Gas Meter
Volume
(ft3)
400.238
413.17
426.12
439.03
452.105
( 51.815)
Temp(°F)
Inlet
29
28.
29
30
29
Outle t
27
26
26
26
26
Orifice
Pressure
Differ-
ential
("H20)
3.0
3.0
3.0
3.0
3.0
Filter
Box
Temp
(°F)
Last
Imp.
Gas
Cemp
(°F)
Sampling
Train
Static
Pressure
("HR)
7.0
6.0
6.0
6.0
6.2
Clayton Environmental Consultants, Inc.
-------
C-129
SAMPLING TRAIN DATA
Company; Ford Motor Company
Source Designation; Coke Batterv A Scrubber Inlet
2-14-75
Date:
Test Number; preliminary NaQH-5
Field Person; RJG
Filter Number:
Barometric Pressure ("Hg); 29.76
Stack Static Pressure ("H20):
Stack Dimensions; 66" I.D.
Plume Appearance:
Ambient Temperature(°F):
Record all Data Every
Minutes
Filter Heater Setting: _ __
Probe Heater Setting: __ __
Nozzle Number: _ ,Dia.(in.): __
Pitot Tube No. _ ,Corr. Factor: _
Meter Box No.MAC-5 .Co rr. Factor; 0 .999
Meter Xsokinetic Factor; _
Assumed Moisture (X) : _
Condensate Volume (ml); -4 _
Silica Gel Weight Gain(g):__9 _
Leak Rate _ CFM at
"Hg
Trav-
erse
Point
No.
CL
CL
CL
CL
CL
Time
Samp-
ling
(rain)
Clock
12:20
12:35
12:50
13:05
13:20
Velocity
Pressure
<"H20)
AVERAGE (TOTAL)
Stack
Temp
<°F)
40
40
42
44
42
Dry Gas Meter
Volume
(ft3)
452.505
465.72
478.93
491.96
505.242
( 52.684)
Temp(°F)
Inlet
30
31
32
32
31
Outlet
26
27
28
28
27
Orifice
Pressure
Differ-
ential
("H20)
3.0
3.0
3.0
3.0
3.0
Filter
Box
Temp
(°F)
Last
Imp.
Gas
Temp
(°F)
Sampling
Train
Static
Pressure
("Hg)
8.0
7.0
7.0
7.0
7.2
Clayton Environmental Consultants, Inc.
-------
C-130
SAMPLING TRAIN DATA
Company: Ford Motor Company
Source Designation; Coke Battery A Scrubber Inlet
2-14-75
Date:
Test Number; preliminary NaOH-6
Field Person; RJG
Filter Number:
Barometric Pressure ("Hg): 29.76
Stack Static Pressure ("H20); -2.5
66" I.D.
Stack Dimensions ;
Plume Appearance:
Ambient Temperature(°F):
Record all Data Every
Filter Heater Setting:
Probe Heater Setting:
Nozzle Number: ,Dia.(in.):
Pitot Tube No. ,Corr.Factor:
Meter Box No .MAC-5 .Corr.Factono.999
Meter Isokinetic Factor:
Assumed Moisture(Z):
Condensate Volume(ml); -1
Minutes
Silica Gel Weight Gain(g); 8
Leak Rate
CFM at
"Hg
Trav-
erse
Point
No.
CL
CL
CL
CL
CL
Time
Samp-
ling
(min)
Clock
13:24
13:39
13:54
14:09
14:24
Velocity
Pressure
<"H20)
•
AVERAGE (TOTAL)
Stack
Temp
<°F>
46
46
45
48
46
Dry Gas Meter
Volume
(ft3)
505.242
518.48
531.66
544.73
557.866
( 52.571)
Temp(°F)
Inlet
32
33
35
34
34
Outle t
29
30
30
30
30
Orifice
Pressure
Differ-
ential
("H20)
3.0
3.0
3.0
3.0
•
3.0
filter
Box
Temp
<°F)
Last
Imp.
Gas
Temp
(°F)
Sampling
Train
Static
Pressure
("Hg)
7.0
7.0
7.0
7.0
7.0
Clayton Environmental Consultants, Inc,
-------
C-131
SAMPLING TRAIN DATA
Ford Motor Company
Company!
Source Designation: Coke Battery A Scrubber Inlet
Date: 6/3/75
Teat Number; HaOH-1
Field Peraon; RCM
Filter Number: A-147-48
Filter Heater Setting; 100
Frobe Heater Setting; 100
Barometric Pressure ("Hg); 29.15
Stack Static Pressure ("H20); -5.1
Stack Dimensions;
Plume Appearance:
66" I.D.
Ambient Temperature(°F): 67
Record all Data Every 0.5
Minutes
Nozzle Number; -- .Dla.(in.)• 0. 188
Pitot Tube No. 18.Corr.Factor; 0.838
Meter Box No.RAC-l,Corr.Factor; 0.974
Meter Isokinetic Factor; 1720
Assumed Moisture(I); 1
Condensate Volume(ml);
Silica Gel Weight Gain(g):__-
Leak Rate 0.02 CFM at
15 "Hg
Trav-
erse
Point
No.
S-7
S-7
S-7
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
16:40
16:53
17:10
Velocity
Pressure
("H20)
1.30
1.55
(1.65)
1.35
1.50
(1.55)
1.35
1.5
(1.7).
AVERAGE (TOTAL)
Stack
Temp
<"F)
80
160
150
(250)
80
220
160
(285)
84
280
250
(570)
163
Dry Gas Meter
Volume
(£t3)
250.666
251.302
251.302
252.072
252.072
252.839
( 2.117 )
Temp(°F)
Inlet
78
80
81
80
Outlet
78
80
81
80
Orifice
Pressure
Differ-
ential
("H20)
1.92
2.05
2.01
1.80
2.00
1.65
1.90
filter
Box
Temp
<°F)
200
255
240
232
[Last
Imp.
Gas
Temp
CF)
70
72
74
72
Sampling
Train
Static
Pressure
("Hg)
3.5
3.5
4.0
3.7
Clayton Environmental Consultants, Inc.
-------
C-132
SAMPLING TRAIN DATA
Company; Ford Motor Company
Source Designation; Coke Battery A Scrubber Inlet
6/4/75
NaOH-2
Date:
Test Number:
Field Person:_
Filter Number:
Barometric Pressure ("Hg); 29.18
ROM
A-147-50
Stack Static Pressure ("H?0): -4.4
Stack Dimensions; 66" I.D.
Plume Appearance: --
Ambient Temperature ("F): 65
Record all Data Every 0.5
Minutes
Filter Heater Setting:
Probe Heater Setting:
90
90
NOBile Number; — ,Dia.(in.); 0.188
Pitot Tube No. 18,Corr.Factor; 0.838
Meter Box No.RAC-1'tCorr.Factor;0.974
Meter Isokinetic Factor; 1720
Assumed Moisture(I); 1
Condensate Volume(ml);
Silica Gel Height Gain(§):_--
Leak Rate 0.015 CFM at
17 "Hg
Trav-
erse
Point
No.
S-7
S-7
S-7
Time
Samp-
ling
(sec }
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
09:04
09:14
09:26
Velocity
Pressure
("H20)
1.30
1.5
(1.55)
1.35
1.55
(1.60)
1.30
1.6
(1.65)
AVERAGE (TOTAL)
Stack
Temp
(»F)
75
150
165
(225)
80
180
150
(260)
84
180
150
(250)
135
Dry Gas Meter
Volume
(ft3)
253.168
253.838
253.838
254.616
254.616
255.410
( 2.184 )
Temp('F)
Inlet
75
80
82
79
Outlet
75
80
82
79
Orifice
Pressure
Differ-
ential
("H20)
1.94
2.0
2.01
2.03
1.93
2.03
1.99
Filter
Box
Temp
<°F)
230
250
260
247
Last
Imp.
Gas
Temp
CF}
72
72
74
73
Sampling
Train
Static
Pressure
("Hg)
3.0
3.0
3.0
3.0
3.5
3.5
3.2
Clayton Environmental Consultants, Inc.
-------
C-133
SAMPLING TRAIN DATA
Company; Ford Motor Company
Source Designation:
Coke Battery A Scrubber Inlet
6/4/75
Date:
Test Number; NaOH-3
Field Person:__
Filter Number:
Barometric Pressure ("Hg); 29,15
Filter Heater Setting; 90
Probe Heater Setting; 90
RCM
A-147-02
Stack Static Pressure ("H;0); -4.5
Stack Dimensions: 66" I.D.
Plume Appearance: --
Ambient Temperature(°F); 72
Record all Data Every 0.5
Minutes
NozBle Number; -- .Dia.(in.) ; 0.188
Pltot Tube No. 18,Corr.Factor; 0.838
Meter Box No.RAC-1 .Corr.FactonO. 974
Meter Isoklnetic Factor; 1720
Assumed Moisture (I): 1
Condensate Volume (ml): --
Silica Gel Weight Cain(g);
Leak Rate Q.Q2 CPM at 17 "Hg
Trav-
erse
Point
No.
S-7
S-7
S-7
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
10:49
11:04
11:16
Velocity
Pressure
("H20)
1.30
1.5
(1.6)
1.35
1.35
(1.7)
1.35
1.45
(1.6>
AVERAGE (TOTAL)
Stack
Temp
(°F)
82
170
270
(275)
84
90
280
(290)
85
100
238
(238)
155
Dry Gas Meter
Volume
(ft3)
256.229
257.014
257.014
257.801
257.801
258.680
( 2.387 )
Terap(°F)
Inlet
78
80
80
79
Outlet
78
80
80
79
Orifice
Pressure
Differ-
ential
("H20)
1.92
1.91
2.00
1.97
1.99
2.08
1.98
Filter
Box
Temp
CF)
210
225
240
225
Last
Imp.
Gas
remp
CF?
72
74
74
73
Sampling
Train
Static
Pressure
("Hg)
3.0
3.0
3.3
3.3
3.3
3.5
3.2
Clayton Environmental Consultants, Inc.
-------
C-134
SAMPLING TRAIN DATA
Company; Ford Motor Company
Source Designation: Coke Battery A Scrubber Inlet
6/4/75
ROM
A-147-03
Date:
Test Numbert NaOH-4
Field Pcrson:_
Filter Number:
Barometric Pressure ("Hg); 29,17
Stack Static Pressure ("HgO); -4.5
Stack Dimensions; 66" I.D.
Plume Appearance: --
Filter Heater Setting:
Probe Heater Setting:
90
90
Ambient Temperature(°F); 75
Record all Data Every 0.5
Minutes
Nozzle Number:_-_-_,Dia. (in.) :_0._188_
Pitot Tube No. 18.Corr.Factor; 0.838
Meter Box No.RAC-1 »Corr.Factor;0.974
Meter Isokinetic Factor; 1720
Assumed Moisture (I): 1
Condensate Volume(ml);
Silica Gel Weight Gain(g); --
Leak Rate
0.01 CFM at 15
"Hg
Trav-
erse
Point
No.
S-7
S-7
S-7
Time
Samp-
ling
(sec)
0
30
60
• Max
0
30
60
Max
0
30
60
Max
Clock
13:00
13:10
13:17
Velocity
Pressure
("H20)
1.30
1.45
(1.55)
1.30
1.4
(1.55)
1.25
1.40
(1.50)
AVERAGE (TOTAL)
Stack
Temp
CF)
75
150
130
(220)
82
220
130
(255)
82
205
135
(235)
134
Dry Gas Meter
Volume
(ft3)
258.802
259.570
259.582
260.326
260.327
261.054
C 2.193 )
Temp(°F)
Inlet
78
80
80
79
Outlet
78
80
80
79
Qrifice
Pressure
Differ-
ential
("H20)
1.95
1.92
1.92
1.65
1.86
1.69
1.83
Filter
Box
Temp
CF)
260
230
225
238
Last
Imp.
Gas
Temp
(°F)
75
82
80
79
Sampling
Train
Static
Pressure
("Hg)
3.0
3.0
3.0
3.2
3.2
3.4
3.1
Clayton Environmental Consultants, Inc.
-------
C-135
SAMPLING TRAIN DATA
Company; Ford Motor Company
Source Designation; Coke Battery A Scrubber Inlet
6/4/75
Date:
Test Humbert NaOH-5
Field Person:__
Filter Number:
Filter Heater Setting:
Probe Heater Setting:
90
90
ROM
A-147-06
Barometric Pressure ("Hg); 29.11
Stack Static Pressure ("^0): -5.0
Stack Dimensions:
Plume Appearance:
66" I.D.
Ambient Temperature(°F); 72
Record all Data Every 0.5
Minutes
Nossle Number; -- ,Dia.(in.); 0. 188
Fitot Tube No. 18fCorr.Factor; 0.838
Meter Box No.RAC-1 .Corr.FactonO. 974
Meter Xsokinetic Factor; 1720
Assumed Moisture(1): 1
Condensate Volume(ml);
Silica Gel Weight Gain(g):_--
Leak Rate 0.022 CFM at 14 "Hg
Trav-
erse
Point
No.
S-7
S-7
S-7
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
14:58
15:08
15:19
(Telocity
Pressure
("H20)
1.30
1.50
(1.55)
1.35
1.55
(1.7)
1.35
1.50
(1.60).
AVERAGE (TOTAL)
Stack
Temp
(°F)
82
220
125
(245)
85
240
125
(245)
85
165
115
(195)
138
Dry Gas Meter
Volume
(ft3)
261.319
262.064
262.065
262.820
262.841
263.607
( 2.229 )
Temp(°F)
Inlet
70
70
70
70
Outlet
70
70
70
70
Orifice
Pressure
Differ-
ential
("H20)
1.89
1.74
1.96
1.75
1.96
1.90
1.87
filter
Box
Temp
CF)
200
215
240
218
Last
Imp.
Gas
Temp
CF)
64
67
70
67
Sampling
Train
Static
Pressure
("Hg)
2.5
2.5
3.0
3.0
3.0
3.2
2.9
Clayton Environmental Consultants,
-------
C-136
Company:_
Source Designation:
SAMPLING TRAIN DATA
Ford Motor Company
Coke Battery A Scrubber Inlet
6/5/75
RCM
A-147-09
Date:
Test Number; NaOH-6
Field Person:^
Filter Number:
Barometric Pressure ("Hg); 28.85
Stack Static Pressure ("H20> :__-5±_5_
Stack Dimensions; 66" I.D.
Plume Appearance: --
Filter Heater Setting; 90
Probe Heater Setting; 90
Noccle Number; -- ,Dia.(in.) ; 0.188
Pitot Tube No. 18.Corr.Factor; 0.838
Meter Box No. RAG-l'»Corr.Factor; 0,974
Meter Isokinetic Factor; 1720
Assumed Moisture(I): 1
Condensate Volume(ml); —
Ambient Temperature(°F); 70
Record all Data Every 0.5
Silica Gel Weight Galn(g):--
Minutes Leak Rate 0.01 CFM at 17 "Hg
Trav-
erse
Point
No.
S-7
S-7
S-7
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
12:26
12:40
12:50
(Telocity
Pressure
<"H20)
1.40
1.50
(1.70)
1.40
1.5
(1.5)
1.4
1.45
(1.50)
AVERAGE (TOTAL)
Stack
Temp
(«F)
75
225
175
(275)
81
150
105
(150)
85
150
110
(155)
128
Dry Gas Meter
Volume
(ft3)
266.818
267.591
267.600
268.383
268.385
269.179
( 2.300 )
Temp(°F)
Inlet
72
75
80
76
Outlet
72
75
80
76
Orifice
Pressure
Differ-
ential
("H20)
2.07
1.73
2.06
1.96
2.07
1.91
1.97
filter
Box
Temp
<°F)
220
240
230
230
Last
Imp.
Gas
Temp
rp?
72
76
76
75
Sampling
Train
Static
Pressure
("Hg)
3.0
3.0
3.0
3.0
3.2
3.2
3.1
Clayton Environmental Consultants, Inc.
-------
C-137
SAMPLING TRAIN DATA
Company; Ford Motor Company
Source Designation; Coke Battery A Scrubber Outlet
6/3/75
Data:
Test Number; HaOH-l
Field Person:_
Filter Number:
Barometric Pressure <"Hg); 29.15
Filter Heater Setting:
Probe Heater Setting:
260
90
VWH/GMS
A-147-45
Stack Static Pressure ("H;0); -0.21
Stack Dimensions; 90" I.D.
Plume Appearance: ...
Ambient Temperature(°F); 77
Record all Data Every 0.5
Minutes
Noisle Humbert -- .Dia.(in.); 0.256
Pltot Tube Ho. 19 .Corr.Factor; 0.854
Meter Box No.RAC-4,Corr.Factor 0.991
Meter Isokinetic Factor; 1685
Assumed Moisture (Z): 2
Condenaate Volume (ml): --
Silica Gel Height Cain(g);
Leak Rate 0.002 CFM at 15 "Hg
Trav-
erse
Point
No.
N-6
N-6
N-6
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
Clock
16:40
16:53
17:10
Velocity
pressure
("H20>
_
0.65
0.70
0.70
0.70
0.70
0.73
0.73
0.70
•
AVERAGE (TOTAL)
Stack
Temp
(°F)
120
117
125
120
116
126
118
116
125
120
Dry Gas Meter
Volume
(ft3)
457.650
458.2
458.66
459.735
460.2
460.727
C 3.049 )
Temp('F)
Inlet
74
75
76
76
76
75
75
75
Outlet
76
75
76
78
77
75
75
76
Orifice
Pressure
Differ-
ential
("HzO)
3.03
3.2
3.2
3.2
3.2
3.35
3.35
3.2
3.22
••liter
Box
Temp
CF)
270
275
280
275
Last
Imp
Gas
Tern]
CF
74
75
76
75
Sampling
Train
Static
Pressure
("Hg)
2.0
2.0
2.0
1.5
1.5
1.8
Clayton Environmental Consultants, Inc.
-------
C-138
SAMPLING TRAIN DATA
Company; Ford Motor Company
Source Designation; Coke Battery A Scrubber Outlet
6/4/75
Date:
Test Number; NaOH-2
Field Person:
Filter Heater Setting:
Probe Heater Setting:
270
80
VWH
Filter Number:
A-147-49
Barometric Pressure ("Hg); 29.18
Stack Static Pressure ("HgO); -0.21
Stack Dimensions:
Plume Appearance:
90" I.D.
Ambient Temperature (°F) ; 71
Record all Data Every 0.5
Number; -- .Dia.(in.); 0.256
Fltot Tube No.19 .Corr.Factor; 0.854
Meter Box No. RAC-4i Corr. Factor; 0.991
Meter Isokinetic Factor: 1685
Assumed Moisture (I): 2.7
Condensate Volume(ml);
Silica Gel Weight Gain(g):_--
0.003CFM at
Minutes Leak Rate
15 »Hg
Trav-
erse
Point
No.
N-6
N-6
N-6
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
Clock
09:04
09:14
09:26
Velocity
Pressure
("H20)
0.65
0.65
0.65
0.60
0.60
0.60
0.63
0.63
0.63
•
AVERAGE (TOTAL)
Stack
Temp
(°F>
110
112
118
115
117
122
116
116
123
117
Dry Gas Meter
Volume
(ft3)
462.056
462.978
463.45
463.975
464.4
464.856
( 2.775 )
Temp(°F)
Inlet
74
74
74
74
74
74
75
75
75
74
Outlet
74
75
75
76
76
76
76
76
76
76
Orifice
Pressure
Differ-
ential
("H20)
3.03
3.03
3.03
2.78
2.78
2.78
2.93
2.93
2.93
2.91
'liter
Box
Temp
CF)
230
255
270
280
259
Last
Imp.
Gas
Temp
CF>
72
68
68
70
70
Sampling
Train
Static
Pressure
("Hg)
1.0
1.5
1.5
1.3
Clayton Environmental Consultants, Inc.
-------
C-139
SAMPLING TRAIN DATA
Ford Motor Company
Company:
Source Designation; Coke Battery A Scrubber Outlet
6/4/75
Date:
Test Number; NaOH-3
Field Person:_
Filter Number:
Barometric Pressure ("Hg); 29.15
Filter Heater Setting; 280
Probe Heater Setting: 85
VWH/GMS
A-147-01
Stack Static Pressure ("H?0); -0.21
Stack Dimensions; 90" I.D.
Plume Appearance: -.
Ambient Temperature(*F); 80
Record all Data Every 0.5
Norcle Number; —tDia.(in.); 0.256
Pitot Tube Me. 19 .Corr.Factor; 0.854
Meter Box No.RAC-4,Corr.Factor;0.991
Meter Isokinetic Factor; 1685
Assumed Moisture(I); 2.7
Condensate Volume(ml);
Silica Gel Weight Cain(g); --
Minutes Leak Rate 0.003 CFM at 15 "Hg
Trav-
erse
Point
No.
N-6
N-6
N-6
Time
Samp-
ling
/sec)
0
30
60
0
30
60
0
30
60
Clock
10:49
11:04
11:16
Velocity
Pressure
("H20)
0.65
0.65
0.65
0.65
0.65
0.65
0.65
0.65
0.65
AVERAGE (TOTAL)
Stack
Temp
CF)
115
115
122
115
115
120
116
119
121
118
Dry Gas Meter
Volume
(ft3)
465.248
465.85
466.225
466.7
467.247
467.7
468.276
( 3.001 )
Temp(°F)
Inlet
75
75
75
75
75
75
76
76
76
75
Outlet
75
76
76
76
77
77
78
78
78
77
Orifice
Pressure
Differ-
ential
("H20)
3.03
3.03
3.03
3.03
3.03
3.00
3.03
3.00
2.97
3.02
filter
Box
Temp
CF)
270
280
260
270
285
273
Last
Imp.
Gas
Temp
CP>
82
74
78
76
74
77
Sampling
Train
Static
Pressure
("Hg)
1.0
1.0
1.5
1.0
1.0
1.1
Clayton Environmental Consultants, Inc.
-------
C-140
SAMPLING TRAIN DATA
Company; Ford Motor Company
Source Designation; Coke Battery A Scrubber Outlet
6/4/75
Date:
Test Number; NaOH-4
Field Person:^
Filter Number:
Barometric Pressure ("Hs)t 29.17
Filter Heater Setting:
Probe Heater Setting:
280
85
VWH/GMS
A-147-04
Stack Static Pressure ("HgO); -0.21
Stack Dimensions; 90" I.D.
Plume Appearance: --
Ambient Temperature(*F); 75
Record all Data Every 0.5
Minutes
Nocsle Number; -- ,Dia.(in.); Q.256
Pitot Tube No. 19,Cerr.Factor; 0.854
Meter Box No.RAC-4.Corr.Factor; 0.991
Meter Isokinetic Factor; 1685
Assumed Moisture(I); 2.7
Condensate Volume(ml): --
Silica Gel Weight Cain(g);
Leak Rate CFM at
"Hg
Trav-
erse
Point
No.
N-6
N-6
N-6
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
Clock
13:00
13:10
13:17
Velocity
Pressure
("H20)
0.65
0.65
0.65
0.67
0.63
0.67
0.68
0.67
0.65
•
AVERAGE (TOTAL)
Stack
Temp
CF)
118
121
125
117
121
125
116
117
123
120
Dry Gas Meter
Volume
(ft3)
468.534
469.0
469.438
470.00
470.5
471.0
471.475
( 2.915 )
Temp(°F)
Inlet
74
74
74
74
74
74
74
74
Outlet
75
75
75
76
76
76
76
76
Orifice
Pressure
Differ-
ential
("H20)
3.03
3.00
3.00
3.03
2.97
3.00
3.1
3.1
30
3.03
filter
Box
Temp
(°F)
270
270
240
270
270
264
Last
Imp.
Gas
Temp
(°F>
75
72
70
75
75
73
Sampling
Train
Static
Pressure
("Hg)
1.5
1.5
1.5
1.5
1.5
Clayton Environmental Consultants, Inc.
-------
C-141
SAMPLING TRAIN DATA
Company; Ford Motor Company
Source Designation; Coke Battery A Scrubber outlet
6/4/75
Date:
Test Number; HaOH-5
Filter Heater Setting:
Probe Heater Setting:
270
85
Field Person; VWH/GMS
Filter Number;
Barometric Pressure ("Hg); 29.11
A-147-04
Stack Static Pressure ("H20); -0.21
Stack Dimensions; 90" I.D.
Plume Appearance: --
Ambient Temperature(*F); 69
Record all Data Every Q.5
Minutes
Noizle Number; -- .Die.(in.); 0.256
Pitot Tube No. 19 ,Corr.Factor; 0.854
Meter Box No.RAG-4.Corr.Factor;0.991
Meter Isokinetic Factor; 1685
Assumed Moisture(I); 2.7
Condensate Volume (ml): --
Silica Gel Weight Gain(g);
Leak Rate 0.001 CFM at IS "Hg
Trav-
erse
Point
No.
N-6
N-6
N-6
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
Clock
14:58
15:08
15:19
Velocity
Pressure
("H20)
0.70
0.70
0.73
0.73
0.70
0.71
0.73
0.73
0.73
•
AVERAGE (TOTAL)
Stack
Temp
(°F)
116
118
123
116
118
125
117
120
124
120
Dry Gas Meter
Volume
(ft3)
471.873
472.4
472.886
473.4
473.841
474.35
474.837
( 2.937 )
Temp('F)
Inlet
68
68
68
68
68
68
68
68
68
68
Outlet
69
69
69
69
69
69
69
69
69
69
Orifice
Pressure
Differ-
ential
<"H20)
3.26
3.26
3.35
3.36
3.20
3.25
3.36
3.36
3.36
3.31
Filter
Box
Temp
CF)
275
275
290
290
282
Last
Imp.
Gas
Femp
CV)
68
65
68
65
66
Sampling
Train
Static
Pressure
("Hg)
1.5
1.5
1.5
1.5
Clayton Environmental Consultants, Inc.
-------
C-142
SAHPLXNC TRAIN DATA
Ford Motor Company
Company:_
Source Designation; Coke Battery A Scrubber Outlet
6/5/75
VWH/GMS
A-147-08
Date: _
Teat Number; NaOH-6
Field Per son :_
Pilter Number:
Barometric Pressure ("Hg):
Stack Static Pressure
Stack Dimensions: _ 90" I.D.
Plume Appearance: _ ^
Filter Heater Setting; 270
Probe Heater Setting; 85
28^85
-0.21
Ambient Temperature(°F):
Record all Data Every 0.5
68
Minutes
NotBle Number; -- .Dia.(in.); 0.256
Pitot Tube No. 19.Corr.Factort 0.854
Meter Box No.RAC-4'.Corr.Factor;0.991
Meter Isokinetic Factor; 1685
Assumed Moisture(I); 2.7
Condensate Volume(ml):
Silica Gel Height Cain(g);
Leak Rate 0.001 CFM at 15 "Hg
Trav-
erse
Point
No.
N-6
N-6
N-6
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
Clock
12:26
12:40
12:50
(Telocity
Pressure
("H20)
0.65
0.60
0.60
0.67
0.67
0.65
0.65
0.65
0.65
AVERAGE (TOTAL)
Stack
Temp
(°F)
118
120
127
118
122
123
120
122
125
122
Dry Gas Meter
Volume
(ft3)
475.445
476.0
476.464
477.453
477.95
478.427
( 2.955 )
Temp(°F)
Inlet
73
73
74
76
75
75
75
75
75
75
Outlet
74
76
74
76
76
72
76
76
76
75
Orifice
Pressure
Differ-
ential
("H20)
3.02
2.80
2.80
3.15
3.15
3.15
3.00
3.00
2.0
2.90
filter
Box
Temp
(°F)
230
255
275
290
260
262
Last
Imp.
Gas
Cemp
(°P>
78
74
82
76
76
77
Sampling
Train
Static
Pressure
("Hg)
2.5
2.5
2.5
2.0
2.4
Clayton Environmental Consultants, Inc.
-------
NOX DATA SHEET
EPA METHOD 7
Project Ford Motor Company
Field Man:
GEH
Sampling
Station
Coke
Bat tery A
Scrubber
Inlet
Coke
Battery A
Scrubber
Inlet
Coke
Battery A
Scrubber
Inlet
Test
Number
Preliml-
nary-1
Prelimi-
nary -2
Prelimi-
nary -3
Flask
Number
&
Volume
14
2067
19
2044
20
2088
Initial
Final
^.Initial.
Final
_ Initial
Final
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Initial
Final
1975
Date
2-4
2-5
2-4
2-5
2-4
2-5
Time
13:00
17:00
13:22
17:00
13:30
17:00
Barometric
Pressure
29.84
29.18
29.84
29.18
29.84
29.18
Flask
Pressure
<±>
-26.5
- 0.20
-26.5
- 0.40
-26.5
- 2.0
Temperature
<°F>
30
70
30
70
30
70
Final
Volume
(liters)
1.72
1.69
1.87
o
t->
4>
Clayton Environmental Consultants, Inc.
-------
NOX DATA SHEET
EPA METHOD 7
Project: Ford Motor Company - Coke Battery A
Field Man: GMS/RJG
Sampling
Station
Scrubber
Outlet
Scrubber
Outlet
Scrubber
Outlet
Scrubber
Outlet
Scrubber
Outlet
Scrubber
Outlet
Scrubber
Outlet
Scrubber
Outlet
Test
Number
NOx-1
NOx-2
NOx-3
NOx-4
NOx-5
NOx-6
NOx-7
NOx-8
Flask
Number
&
Volume
19
2044
20
2088
10
70fi7
8
2065
4
Ofl7Q
14
2067
19
2044
4
2073
Initial
* Final
..Initial.
Final
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Initial
Final
1975
Date
6/10
6/11
6/10
6/11
6/10
6/11
6/10
6/11
6/10
6/11
6/11
6/12
6/11
6/12
6/11
6/12
Time
14:30
08:11
14:58
08:08
15:10
08:05
16:39
08:03
16:57
08:11
14:55
08:20
15:16
08:19
15:28
08:17
Barometric
Pressure
29.5
29.2
29.5
29.2
29.5
29.2
29.5
29.2
29.5
29.2
29.15
29.35
29.15
29.35
29.15
29.35
Flask
Pressure
<±>
-27.0
- 1.0
-27.2
- 1.0
-27.3
- 0.8
-27.4
- 0.8
-27.3
- 1.0
-26.7
- 0.6
-27.1
- 0.6
-26.7
- 0.4
Temperature
<°F)
74
62
74
62
73
62
73
62
- 71
62
68
62
68
62
68
62
Final
Volume
(liters)
1.76
1.81
1 81
11 a 9
.82
Inn
Ittt
• O£
100
. of.
IQ/.
. 84
Clayton Environmental Consultants, Inc.
-------
NOX DATA SHEET
EPA METHOD 7
Project: Ford Motor Company - Coke Battery A
Field Man:
GMS/RJG/GEH
Sampling
Station
Scrubber
Outlet
Scrubber
Outlet
Scrubber
n« t" i A i"
Scrubber
Outlet
Scrubber
Outlet
Test
Number
NOz-9
JOx-10
HOx-11
SOx-12
KOx-13
Flask
Number
&
Volume
8
2065
4
2073
19
7Clli.li.
20
2088
8
2065
Initial
Final
..Initial.
Final
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Initial
Final
1975
Date
6/11
6/12
7/18
7/22
7/18
7/22
7/18
7/22
7/18
7/22
Time
15:38
08:15
12:19
10:35
12:27
10:36
12:39
10:37
12:51
10:38
Barometric
Pressure
29.15
29.35
29.45
29.32
29.45
29.32
29.45
29.32
29.45
29.32
Flask
Pressure
(±)
-27.1
- 0.6
-27.4
- 0.8
-26.3
- 1.5
-27.3
- 0.7
-26.4
- 0.2
Temperature
<°F>
68
62
84
75
84
75
84
75
84
75
Final
Volume
(liters)
1o/.
• O4
• 79
1 65
1.80
1.76
in
Clayton Environmental Consultants, Inc,
-------
MOX DATA SHEET
EPA METHOD 7
Project: Ford Motor Company - Coke Battery A
Field Man: GMS/RJG/JBS/GEH
Sampling
Station
Scrubber
Inlet
Scrubber
Inlet
Scrubber
Inlet
Scrubber
Inlet
Scrubber
Inlet
Scrubber
Inlet
Scrubber
Inlet
Scrubber
Inlet
Test
Number
i
7
g
Flask
Number
&
Volume
2
2067
1
2064
4
2073
5
2078
6
2067
1
2064
2
2067
3
2060
Initial
Final
L.Initlal.
Final
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Initial
Final
1975
Date
6/10
6/11
6/10
6/11
6/10
6/11
6/10
6/11
6/10
6/11
6/11
6/12
6/11
6/12
6/11
6/12
Time
14:30
07:51
14:58
07:45
15:10
07:53
16:39
07:48
16:57
07:43
14:55
08:07
15:16
08:12
15:28
08:09
Barometric
Pressure
29.5
29.2
29.5
29.2
29.5
29.2
29.5
29.2
29.5
29.2
29.15
29.35
29.15
29.35
29.15
29.35
Flask
Pressure
(±)
-26.0
-1.0
-26.1
-1.5
-26.1
-1.0
-26.2
-1.0
-26.0
-5.0
-26.4
-4.4
-26.4
-3.4
-26.0
-3..0
Temperature
<°F)
66
62
66
62
66
62
66
62
66
62
62
62
62
62
62
62
Final
Volume
(liters)
1.71
1.68
. 72
. 73
1.43
1.53
.60
• 60
ei
i
Clayton Environmental Consultants, Inc.
-------
NOX DATA SHEET EPA METHOD 7
Project; Ford Motor Company - Coke Battery A
Field Man: JBS/GEH/GMS
Sampling
Station
Scrubber
Inlet
Scrubber
Inlet
Scrubber
Inlet
Scrubber
Inlet
Scrubber
Inlet
Test
Number
i n
1 2
13
Flask
Number
&
Volume
4
2073
1
2064
3
2060
4
2073
2
2067
Initial
Final
..Initial,
Final
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Initial
Final
1975
Date
6/11
6/12
7/18
7/22
7/18
7/22
7/18
7/22
7/18
7/22
Time
15:38
08:10
12:20
10t'30
12:27
10:31
12:39
10:32
12:50
10:33
Barometric
Pressure
29.15
29.35
29.63
29.32
29.63
29.32
29.63
29.32
29.63
29.32
Flask
Pressure
(±)
-26.1
-2.5
-26.7
-0.9
-26.6
-0.5
-26.6
-0.6
-26.6
-0.7
Temperature
<°F)
62
62
81
75
80
75
79
75
79
75
Final
Volume
(liters)
1.65
1.72
1.73
177.
• 74
17 4
• 73
o
t-1
•p-
Clayton Environmental Consultants, Inc.
-------
CRITICAL ORIFICE SAMPLING DATA
Company:
Source Designation^
Field Person; GEH
Ford Motor Company- Rouee Plant - Dearborn. Michisan
Coke Battery A Scrubber Inlet
Date
6-5
Material
Sampled and
Test Number
Activated
Charcoal-1
Activated
Charcoal-2
Activated
Charcoal-3
Activated
Charcoal-4
Activated
Charcoal-5
Activated
Charcoal-6
Activated
Charcoal-7
Orifice
Number
12
12
12
12
12
12
12
Sampling
Period
Start
12:26
12:40
12:50
14:52
15:22
16:14
16:25
Stop
12:27
12:41
12:51
14:53
15:23
16:15
16:26
At
(min)
1.0
1.0
1.0
1.0
1.0
1.0
1.0
Barometric
Pressure
("Hg)
29.51
29.51
29.51
29.51
29.51
29.51
29.51
Inlet
Vacuum
("H20)
17.5
14
22
15
15.5
14
15.5
Outlet
Vacuum
("Hg)
23
23
23
23
23
23
23
Inlet
Temp
CF)
68
68
68
76
77
78
78
Sampled
Vo lume
(liters)
1.22
1.23
1.21
1.22
1.22
1.22
1.22
• Qcal x
•P-
CO
Clayton Environmental Consultants, Inc.
-------
CRITICAL ORIFICE SAMPLING DATA
Company:
Source Designation:
Field Person: GEH "
Ford Motor Company- Rouge Plant - Dearborn. Michigan
Coke Battery A Scrubber Inlet
Date
1975
6-6
6-6
6-6
6-6
Material
Sampled and
Test Number
Activated
Charcoal-8
Activated
Charcoal-9
Activated
Charcoal-10
Activated
Charcoal- 11
Orifice
Number
12
'
12
12
12
Sampling
Period
Start
10:27
10:49
11:27
11:41
11:50
13:38
13:55
14:10
14:20
14:30
14:58
Stop
10:28
10:50
11:28
11:42
11:51
13:39
13:56
14:11
14:21
14:31
14:59
At
(min)
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
Barometric
Pressure
<"Hg)
28.82
28.82
28.82
28.82
28.82
28.82
28.82
28.82
28.82
28.82
28.82
Inlet
Vacuum
("H20)
17.5
17.5
14.5
16.5
15.5
17.5
17.5
18.5
15.5
15
15
Outlet
Vacuum
<"Hg)
23
23
23
23
23
23
23
23
23
23
23
Inlet
Temp
<°F)
68
68
66
66
66
68
68
70
70
70
70
Sampled
Volume
(liters)
1.19
1.19
1.20
1.20
1.20
1.19
1.19
1.19
1.20
1.20
1.20
Qstd - Qcal x
Clayton Environmental Consultants, Inc.
-------
CRITICAL ORIFICE SAMPLING DATA
Company; Ford Motor Company- Rouge Plant - Dearborn. Michigan
Source Designation: Coke Battery A Scrubber Inlet
Field Person; GEH
Date
1975
6-6
Material
Sampled and
Test Number
Activated
Charcoal- 12
Orifice
Number
12
Sampling
Period
Start
15:10
15:22
15:42
Stop
15:11
15:23
15:43
At
(min)
1.0
1.0
1.0
Barometric
Pressure
("Hg)
28.82
28.82
28.82
Inlet
Vacuum
<"H20)
15.5
15
15
Outlet
Vacuum
("Hg)
23
23
23
Inlet
Temp
<°F)
70
70
70
Sampled
Vo lume
(liters)
1.20
1.20
1.20
I
I-1
«J1
o
Qstd • Qcal x
Clayton Environmental Consultants, Inc,
-------
Company :
Source Designation:
Field Person: GMS~
CRITICAL ORIFICE SAMPLING DATA
Ford Motor Company - Rouge Plant - Dearborn. Michigan
Coke Battery A Scrubber Outlet
Date
1975
6-5
Material
Sampled and
Test Number
Activated
Charcoal-1
Activated
Charcoal-2
Activated
Charcoal-3
Activated
Charcoal-4
Activated
Charcoal-5
Activated
Charcoal-6
Activated
Charcoal-?
Orifice
Number
2
2
2
2
2
2
2
Sampling
Period
Start
12:26
12:40
12:50
14:52
15:22
16:14
16:25
Stop
12:27
12:41
12:51
14:53
15:23
16:15
16:26
At
(mln)
1.0
1.0
1.0
1.0
1.0
1.0
1.0
Barometric
Pressure
("Hg)
28.85
28.85
28.85
28.85
28.85
28.85
28.85
Inlet
Vacuum
<"H20)
8.9
9.8
11.6
10.4
8.8
5.8
5.9
Outlet
Vacuum
("Hg)
23
23
23
23
23
23
23
Inlet
Temp
<°F)
74
75
76
81
81
81
80
Sampled
Volume
(liters)
1.00
0.99
0.99
0.98
0.99
1.00
1.00
o
I
Qstd - Qcal *
Clayton Environmental Consultants, Inc.
-------
Company:
Source Designation:
Field Person: CMS '
CRITICAL ORIFICE SAMPLING DATA
Ford Motor Company - Rouge Plant - Dearborn. Michigan
Coke Battery A Scrubber Outlet
Date
1975
6-6
6-6
6-6
6-6
Material
Sampled and
Teat Number
Activated
Chare oal-8
Activated
Charcoal-9
Activated
Charcoal-10
Activated
Charcoal-11
Orifice
Number
2
2
2
2
Sampling
Period
Start
10:27
10:49
11:27
11:41
11:50
13:38
13:55
14:10
14:20
14:30
14:58
Stop
10:28
10r50
11:28
11:42
11:51
13:39
13:56
14:11
14:21
14:31
14:59
At
(min)
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
Barometric
Pressure
<"Hg)
28.82
28.82
28.82
28.82
28.82
28.82
28.82
28.82
28.82
28.82
28.82
Inlet
Vacuum
("H20)
11.3
10.1
10.1
10.1
10.1
6.8
6.8
6.8
6.8
6.8
6.8
Outlet
Vacuum
<"Hg>
27
27
27
14
14
14
14
14
14
14
17
Inlet
Temp
CF>
68
68
70
70
71
71
71
72
72
73
72
Sampled
Volume
(liters)
0.99
1.00
0.99
0.99
0.99
1.00
1.00
1.00
1.00
1.00
1.00
in
N>
Clayton Environmental Consultants, Inc.
-------
CRITICAL ORIFICE SAMPLING DATA
Ford Motor Company- Rouge Plant - Dearborn. Michigan
Corapany:
Source Designation; Coke Battery A Scrubber Outlet
Field Person:
CMS
Date
1975
6-6
Material
Sampled and
Test Number
Activated
*ilh flf9oa 'iniil?
Orifice
Number
2
"
Sampling
Period
Start
15:10
15:22
15:42
Stop
15:11
15:23
15:43
At
(min)
1.0
1.0
1.0
Barometric
Pressure
("Hg>
28.82
28.82
28.82
Inlet
Vacuum
("H20>
10.9
10.9
10.9
Outlet
Vacuum
<"Hg)
17
17
17
Inlet
Temp
<°F)
72
72
72
Sampled
Volume
(liters)
0.99
0.99
0.99
Qstd " Qcal
ui
OJ
•Clayton Environmental Consultants, Inc.
-------
CRITICAL ORIFICE SAMPLING DATA
EPA METHOD 11
Ford Motor Company
Company:
Source Designation! Coke Battery A Scrubber Inlet
Field Person: R.G. Keller
Date
1975
4-9
4-9
Material
Sampled and
Test Number
Preliminary
H2S-1
Preliminary
H2S-2
Orifice
Number
VOID
10
• Sampling
Period
Start
15:18:12
Stop
15:18:55
At
(min)
0.72
Barometric
Pressure
<"Hg>
29.59
•
•
Inlet
Vacuum
<"H20)
22.0
r
Outlet
Vacuum
("Eg)
23.0
Inlet
Temp
C°F>
42
.
Sampled
Vo lume
(liters)
0.74
rs
i-1
Ul
Qstd " Qcal *
rf
•std
T8td
Tcal
Clayton Environmental Consultants, Inc.
-------
CRITICAL ORIFICE SAMPLING DATA
EPA METHOD 11
Company: Ford Motor Company - Rouge Plant - Dearborn, Michigan
Source Designation; Coke Battery A Scrubber Inlet
Field Person: R.G. Keller
Date
1975
4-10
4-10
4-10
Material
Sampled and
Test Number
Preliminary
H2S- 1
prHe21sl-in2nary
Preliminary
H2S-3
Orifice
Number
10
•
2
10
Sampling
Period
Start
12:34:40
12:45:25
13:00:00
13:19:00
13:30:00
12:34:40
12:45:25
13:00:00
13:19:00
13:30:00
13:50:35
14:07:00
14:14:30
14:29:05
14:40:00
Stop
12:41:30
12:49:30
13:06:15
13:29:20
13:35:00
12:41:30
12:49:30
13:06:15
13:29:20
13:35:00
13:52:40
14:18:00
14:17:00
14:36:45
14:49:00
At
(min)
6.83
4.08
6.25
10.33
5.00
6.83
4.08
6.25
10.33
5.00
2.08
11.00
2.50
7.67
9.00
Barometric
Pressure
("Eg)
29.61
29.61
29.61
29.61
29.61
29.61
29,61
29.61
29.61
29.61
29.61
29.61
29.61
29.61
29.61
Inlet
Vacuum
C"H20)
18.8
18.8
19.1
18.3
18.5
19.1
19.3
19.8.
18.9
19.0
18.8
21.0
21.3
20.3
20.9
Outlet
Vacuum
<"Hg)
22.7
22.7
22.7
22.7
22.7
22.7
22.7
22.7
22.7
22.7
22.7
22.7
22.7
22.7
22.7
Inlet
Temp
CF)
46
46
46
49
49
46
46
46 •
49
49
48
48
49
46
46
Sampled
Volume
(liters)
7.02
4.19
6.42
10.59
5.13
7.08
4.23
6.46
10.68
5.17
2.13
11.21
2.54
7.85
9.20
Qstd • Qcal «
?std
Lcal
Ul
\Jt
Clayton Environmental Consultants, Inc.
-------
CRITICAL ORIFICE SAMPLING DATA
EPA METHOD 11
Ford Motor Company- Rouge Plant - Dearborn. Michigan
Company:,
Source Designation; Coke Battery A. Scrubber nut-let-
Field Person; VWH/GMS
Date
1975
6-3
6-3
6-3
6-3
Material
Sampled and
Test Number
H2S - 1
H2S - 2
NH3 - l
NH3 - 2
Orifice
Number
2
2
10
10
Sampling
Period
Start
10:40
10:47
11:04
11:14
11:24
12:04
10:40
10:47
11:04
11:14
11:24
12:04
Stop
10:41
10:48
11:05
11:15
11:25
12:05
10:41
10:48
11:05
11:15
11:25
12:05
At
(min)
1.0
1.0
1.06
1.03
1.0
1.0
1.0
1.0
1.06
1.03
1.0
1.0
Barometric
Pressure
<"Hg>
29.25
29.25
29.25
29.25
29.25
29.25
29.2
29.25
29.2
29.25
29.25
29.25
Inlet
Vacuum
<"H20)
12.9
13.2
13.3
11.0
10.3
10.3
5.4
5.4
5.5
5.9
6.6
6.6
Outlet
Vacuum
<"Hg>
22.0
22.5
22.5
22.5
22.5
22.5
22.5
22.5
22.5
22.5
22.5
22.5
Inlet
Temp
<°F)
66
66
66
66
68
67
66
66
66
66
67
67
Sampled
Volume
(liters)
1.006
1.006
1.066
1.042
1.011
1.012
1.009
1.010
1.069
1.040
1.006
1.006
o
I
t->
in
Qstd -
Clayton Environmental Consultants, Inc.
-------
C-157
SAMPLING TRAIN DATA
Ford Motor Company
Company:
Source Dealgnatton; Coke Battery A Scrubber Inlet
Date: 1-16-75
Test Number; Preliminary Ethanol-1
Field Person; RJP. MRP
Filter Number:
Barometric Pressure ("Hg); 29.96
Stack Static Pressure ("H20):_
Stack Dimensions: _ 66" I.D.
Plume Appearance: _
Ambient Temperature (°F) :
Record all Data Every
Minutes
Filter Heater Setting:
Probe Heater Setting:
Nozzle Number; ,Dia.(in.)«
Pitot Tube No. ,Corr.Factor:
Meter Box No .MAC-4 tCorr .Factonp.994
Meter Isokinetic Factor;
Assumed Moisture(I):
Condensate Volume(ml):
Silica Gel Weight Gain(g):
Leak Rate CFM at "Hg
Trav-
erse
Point
No.
CL
CL
CL
CL
Time
Samp-
ling
(rain)
Clock
13:53
14:03
14:13
14:23
Velocity
Pressure
<"H20)
AVERAGE (TOTAL)
Stack
Temp
CF)
Dry Gas Meter
Volume
(£t3)
592.374
601.1
608.8
617.556
( 25.031)
Temp('F)
Inlet
Oiitle t
26
26
26
26
26
Orifice
Pressure
Differ-
ential
("H20)
2.8
2.8
2.8
2.8
2.8
filter
Box
Temp
<°F)
Last
Imp.
Gas
Temp
(°P)
Sampling
Train
Static
Pressure
("Hg)
4.5
4.5
4.5
4.5
4.5
Clayton Environmental Consultants, Inc.
-------
C-158
SAMPLING TRAIN DATA
Company:
Source Designation:^
Date: 1-16-75
Ford Motor Company
Coke Battery A Scurbber Inlet
Test Number; Preliminary Ethanol-2
Field Person; RJP. MRP
Filter Number:
Barometric Pressure ("Hg); 29.96
Stack Static Pressure ("H20):
Stack Dimensions; 66" I.D.
Plume Appearance:
Ambient Temperature(°F):
Record all Data Every
Filter Heater Setting:
Probe Heater Setting:
Nozzle Number: ,Dla.(in.):
Pitot Tube No. ,Corr.Factor:
Meter Box No.MAC-4»Corr.Factor;Q.994
Meter Isokinetlc Factor:
Assumed Moisture(1):
Condensate Volume(ml):
Silica Gel Weight Gain(g):
Minutes Leak Rate
CFM at
"Hg
Trav-
erse
Point
No.
CL
CL
CL
CL
Time
Samp-
ling
(rain)
Clock
14:24
14:34
14:44
14:54
(Telocity
Pressure
("H20)
.
AVERAGE (TOTAL)
Stack
Temp
(°F)
Dry Gas Meter
Volume
(ft3)
617.556
625.9
634.1
624.410
( 24.705)
Temp('F)
Inlet
Outlet
26
26
26
26
26
Orifice
Pressure
Differ-
ential
("H20)
2.8
2.8
2.8
2.8
2.8
filter
Box
Temp
(•F)
Last
Imp.
Gas
Temp
<°F)
Sampling
Train
Static
Pressure
("Hg)
4.5
4.5
4.5
4.5
4.5
Clayton Environmental Consultants, Inc.
-------
C-159
SAMPLING TRAIN DATA
Ford Motor Company
Company:__
Source Designation; Coke Battery A Scrubber Outlet
7/17/75
Date:
Teat Number: Ethanol-1
Filter Heater Setting; 230
Probe Heater Setting; 50
A-190-10
Field Person! VWH/GEH
Filter Number:
Barometric Pressure ("Hg)t 29.59
Stack Static Pressure ("H20); --
Stack Dimensions; 90" I.D.
Plume Appearance: --
Ambient Temperature(°F): -.
Record all Data Every 0.5
Minutes
Nocile Number; -- .Die.(in. ) ; 0.254
Pltot Tube No. 19iCorr.Factor; Q.854
Meter Box Ne.RAC-3 ,Corr.Factor;0.993
Meter Isoklnetic Factor; 1796
Assumed Moisture(t): 2.5
Condensate Volume (ml):
Silica Gel Weight Cain(g);
Leak Rate 0.002 CFM at
15
Trav-
erse
Point
No.
N-4
N-4
N-4
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
Clock
08:24
08:25
08:40
08:41
08:50
08:51
Velocity
Pressure
("H20)
0.68
0.68
(0.68)
0.68
0.68
(0.68)
0.68
0.68
(0.68)
•
AVERAGE (TOTAL)
Stack
Temp
CF)
120
120
(126)
120
120
(125)
120
120
(125)
120
Dry Gas Meter
Volume
<*t3)
12.078
13.075
14.030
14.980
( 2.882 )
Temp(°F)
Inlet
79
(79)
79
(80)
80
(81)
80
Outlet
79
(79)
80
(80)
80
(81)
80
Orifice
Pressure
Differ-
ential
("H20)
3.23
3.23
3.23
3.23
3.23
3.23
3.23
3.23
3.23
'liter
Box
Temp
(•F)
220
(225)
255
(260)
265
(265)
247
Last
Imp.
Gas
Cemp
CFJ
80
00)
80
(80)
81
(82)
80
Sampling
Train
Static
Pressure
("Hg)
3.0
3.0
3.0
3.0
3.0
Clayton Environmental Consultants, Inc.
-------
C-160
SAMPLING TRAIN DATA
Ford Motor Company
Company:
Source Designation; Coke Battery A Scrubber Outlet
7/17/75
Date:
Teat Number; Ethanol-2
Field Person:
Filter Number:
Filter Heater Setting; 250
Probe Heater Setting; 50
VWH/GEH
A-128-71
Barometric Pressure ("Hg); 29.59
Stack Static Pressure <"H?0);
Stack Dimensions:_
Plume Appearance:
90" I.D.
Ambient Temperature("?):
Record all Data Every 0,5
Minutes
NoEEle Number; -- ,Dia.(in.); 0.254
Pitot Tube No. 19 .Cerr.FaetortO.854
Meter Box No. RAC-3iCorr.FactoRO.993
Meter Isokinetic Factor; 1796
Assumed Moisture(X); 2.5
Condensate Volume(ml);
Silica Gel Weight Gain(g):_j^
Leak Rate
0.00 CFM at
"Hg
Trav-
erse
Point
No.
N-4
N-4
N-4
Time
Samp-
ling
(sec )
0
30
60
0
30
60
0
30
60
Clock
14:41
14:42
14:54
14:55
15:14
15:15
Velocity
Pressure
("H20)
0.68
0.68
(0.68)
0.71
0.71
(0.71)
0.70
0.70
(0.70)
-
AVERAGE (TOTAL)
Stack
Temp
CF)
120
130
(130)
120
130
(130)
125
130
(130)
126
Dry Gas Meter
Volume
(ft3)
23.028
23.930
24.887
25.825
(2.777 )
Temp(°F)
Inlet
90
(88)
87
(88)
88
(88)
88
Outlet
90
(88)
88
(88)
88
(88)
89
Orifice
Pressure
Differ-
ential
("H20)
3.30
3.30
3.44
3.44
3.40
3.40
3.38
•liter
Box
Temp
CF)
255
255
270
275
250
261
Last
Imp.
Gas
Temp
CF)
92
92
90
90
91
Sampling
Train
Static
Pressure
("Hg)
3.0
3.55
3.5
3.4
Clayton Environmental Consultants, Inc.
-------
C-161
SAMPLING TRAIN DATA
Ford Motor Company
Company:_
Source Designation; Coke Battery A Scrubber Inlet
6/11/75
Date:
Teat Number; Cyclohexane-1
Field Person: ROM
Filter Number: A-147-29
Barometric Pressure ("Hg); 29.2
Filter Heater Setting; loo
Probe Heater Setting! 100
Stack Static Pressure ("H?0); -4.8
Stack Dimensions; 66" I.D.
Plume Appearance: _-
Ambient Temperature (*F) ; 68
Record all Data Every 0.5
Minutes
Nocale Number; -- .Dia.(In.); 0.189
Pitot Tube No. 18.Corr.Factor; 0.838
Meter Box No. RAG-1,Corr.Factor; 0.974
Meter laokinetic Factor; 1720
Assumed Moisture(I); 1
Condensate Volume(ml);
Silica Gel Weight Cain(g); --
Leak Rate 0.03 CFM at
16 "Hg
Trav-
erse
Point
No.
S-7
S-7
S-7
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
13:47
13:48
14:08
14:09
14:23
14:24
Velocity
Pressure
("H20)
1.35
1.6
(1.75)
1.35
1.50
(1.75)
1.35
1.5
(1.55)
AVERAGE (TOTAL)
Stack
Temp
<°F)
83
250
130
(285)
84
145
145
(155)
84
170
125
(175)
135
Dry Gas Meter
Volume
(ft3)
434.382
435.112
435.114
435.910
435.912
436.672
( 2.230 )
Temp(°F)
Inlet
70
73
78
74
Outlet
68
70
78
72
Orifice
pressure
Differ-
ential
("H20)
1.96
1.78
1.95
1.96
1.99
1.91
1.92
filter
Box
Temp
CF)
260
260
240
253
Last
Imp.
Gas
Temp
CP>
70
70
72
71
Sampling
Train
Static
pressure
("Hg)
3.0
3.3
3.5
3.3
Clayton Environmental Consultants, Inc.
-------
C-162
SAHPLING TRAIN DATA
Company; Ford Motor Company
Source Designation; Coke Battery A Scrubber Inlet
Data: 6/12/75
ROM
Teat Number; Cyclohexane-2
Field Person:
Filter Number:
Barometric Pressure ("Hg); 29.13
Filter Heater Setting; 95
Probe Heater Setting: 90
A-147-20
NoKzle Number; -- .Dia.(in.); 0.189
Pitot Tube No. IS.Corr.Factor: 0.838
' Meter Box No.RAC-l.Corr.Factor; 0.974
Meter Zaokinetic Factor; 1720
\ Assumed Moisture(I); 1
Condensate Volume(ml);
" Silica Gel Height Gatn(g);
Record all Data Every 0.5 Minutes Leak Rate 0.005CFM at 16 "Hg
Stack Static Pressure ("H?0); -4.2
Stack Dimensions; 66" I.D.
Plume Appearance:_ --
Ambient Temperature(*P); 66
Trav-
erse
Point
No.
S-7
S-7
S-7
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
10:37
10:38
11:01
11:02
11:14
11:15
Velocity
Pressure
("H20)
1.30
1.50
(1.55)
1.30
1.50
(1.55)
1.25
1.40
(1.50)
AVERAGE (TOTAL)
Stack
Temp
CP)
80
195
120
(205)
90
200
160
(275)
91
170
130
(175)
137
Dry Gas Meter
Volume
(ft3)
439.173
439.939
439.941
440.692
440.693
441.403
( 2.172 )
Temp(°F)
Inlet
80
82
82
81
Outlet
76
80
80
79
Orifice
Pressure
Differ-
ential
("H20)
1.93
1.82
1.91
1.88
1.83
1.79
1.86
filter
Box
Temp
(°F)
210
260
240
237
Last
Imp.
Gas
Temp
CP?
76
78
80
78
Sampling
Train
Static
Pressure
("Hg)
3.0
3.0
3.0
3.0
Clayton Environmental Consultants, Inc.
-------
C-163
SAMPLING TRAIN DATA
Company; Ford Motor Company
Source Designation; Coke Battery A Scrubber Inlet
6/12/75
Date:
Teat Number; Cyclohexane-3
Field Person: ROM
Filter Number: A-147-17
Barometric Pressure ("Hg); 29.15
Stack Static Pressure ("H?0); -4.0
Stack Dimensions: 66" I.D.
Plume Appearance: --
Filter Heater Setting:
Probe Heater Setting:
90
90
Ambient Temperature(*F):
Record all Data Every 0.5
72
Minutes
Notcle Humbert -- .Dia.(in.); o. 189
Pltot Tube No.18 «Corr.Factor; 0.838
Meter Box Mo. RAG-l.Corr. Factor 0.974
Meter laoklnetic Factor; 1720
Assumed Moisture(I); 1
Condensate Volume(ml);
Silica Gel Weight Cain(g):_--
Leak Rate 0.00 CFM at
16
•Hg
Trav-
erse
Point
No.
S-7
S-7
S-7
Time
Samp-
ling
(sec)
0
30
60
Max
0
30
60
Max
0
30
60
Max
Clock
15:10
15:11
15:21
15:22
16:23
16:24
Velocity
Pressure
("H20)
1.25
1.45
(1.5)
1.3
1.55
(1.60)
1.30
1.70
(1.75)-
•
AVERAGE (TOTAL)
Stack
Temp
(°F)
87
165
125
(200)
87
175
125
(195)
84
435
360
(485)
183
Dry Gas Meter
Volume
<^3-*»
442.249
442.959
442.960
443.672
443.697
444.390
( 2.085 )
Temp('F)
Inlet
80
82
80
81
Outlet
80
80
80
80
Orifice
Pressure
Differ-
ential
("H20)
1.84
1.82
1.92
1.96
1.92
1.53
1.83
filter
Box
Temp
CF)
240
260
260
253
Last
Imp.
Gaa
Temp
CF)
78
80
78
79
Sampling
Train
Static
Pressure
("Hg)
2.5
2.5
2.5
2.5
Clayton Environmental Consultants, Inc,
-------
C-164
SAMPLING TRAIN DATA
Company; Ford Motor Company
Source Designation; Coke Battery A Scrubber Outlet
6/11/75
Date:
Test Number; Cyclohexane-1
Field Person; RJG/GMS
Filter Number:
Filter Heater Setting:
Probe Heater Setting:
250
80
A-147-28
Barometric Pressure ("Hg); 29.2
Stack Static Pressure ("H?0); -Q.15
Stack Dimensions:
Plume Appearance:
90" I.D.
Ambient Temperature(*F): -
Record all Data Every 0.5
Minutes
Nocale Number; — .Die.(In.); 0.256
Pltot Tube No. 19«Corr,Factor: 0.854
Meter Box No.RAC-4'«Corr, Factor; 0.991
Meter Isoklnetlc Factor; 1685
Assumed Moisture(I): 2.7
Condenaate Volume(ml);
Silica Cel Weight Caln(g);
Leak Rate CFM at
"Hg
Trav-
erse
Point
No.
N-6
N-6
N-6
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
Clock
13:47
13:48
14:08
14:09
14:23
14:24
Velocity
Pressure
("H20)
0.60
0.60
0.63
0.63
0.63
0.63
•
AVERAGE (TOTAL)
'M.-U
Temp
(•F)
116
120
126
116
120
121
120
120
120
Dry Gas Meter
Volume
(ft3)
604.698
605.2
605.620
605.620
606.546
606.546
607.14
607.478
(2.755 )
Temp(-F)
Inlet
68
68
68
68
68
68
68
Outlet
69
69
68
68
68
68
68
OrUe
Prdl«Ure
Differ-
ential
("H20)
3.03
3.00
2.90
2.85
2.88
2.88
2.92
••liter
Box
Temp
CF)
275
275
260
260
280
280
272
Last
Imp.
Gas
Temp
(•F)
70
70
78
78
80
80
73
Sampling
Train
Static
Pressure
("Hg)
2.0
2.0
2.0
2.0
2.0
2.0
2.0
Clayton Environmental Consultants, Inc.
-------
C-165
SAMPLING TRAIN DATA
Company; Pord Motor Company
Source Designation:
Date: 6/12/75
Teat Number; Cyclohexane-2
Field Person: RJG/GMS
Filter Number;
Barometric Pressure <"Hg); 29.13
Coke Batterv A Scrubber outlet
Filter Heater Setting; 250
Probe Heater Setting: 80
A-I47-39
Stack Static Pressure ("H?0)t -0.15
Stack Dimensions: 90" I.D.
Plume Appearance: --
Ambient Temperature(°F): .
Record all Data Every 0.5
Minutes
NocBle Number; -- »Di«.(in. );0.256
Pltot Tube No* 19,Corr.Factor;0.854
Meter Box No.RAC-4 iCorr.FactoKQ.991
Meter Isokinetic Factor; 1685
Assumed Moisture(I); 2.7
Condensate Volume (ml): -_-
Silica Gel Weight Gain(g);
Leak Rate CFM at
"Hg
Trav-
erse
Point
No.
N-6
N-6
N-6
Time
Samp-
ling
(sec )
0
30
60
0
30
60
0
30
60
Clock
10:37
10:38
11:01
11:02
11:14
11:15
Velocity
Pressure
("H20)
0.60
0.60
0.60
0.60
0.60
0.60
•
AVERAGE (TOTAL)
Stack
Temp
(•*>
120
125
127
120
125
129
121
125
126
124
Dry Gas Meter
Volume
(ft3)
607.930
608.970
609.099
609.905
609.917
610.808
(2.712 )
Temp(°F)
Inlet
77
77
77
77
77
77
77
Outlet
78
78
78
78
78
78
78
Orifice
Pressure
Differ-
ential
("H20)
2.76
2.74
2.76
2.74
2.76
2.74
2.75
?ilter
BOX
Temp
(•F)
255
255
265
265
285
285
268
Last
Imp.
Gas
Temp
CF}
82
82
83
83
87
87
84
Sampling
Train
Static
Pressure
("Hg)
1.0
1.0
1.0
1.0
1.0
1.0
1.0
Clayton Environmental Consultants, Inc.
-------
C-166
SAMPLING TRAIN DATA
Company; Ford Motor Company
Source Destgnation; Coke Battery A Scrubber Outlet
6/12/75
Date:
Teat Number; Cvclohexane-3
Field Person; RJG/GMS
Filter Number: A-147-22
Filter Heater Setting; 250
Probe Heater Setting: 80
Barometric Pressure ("Hg); 29.15
Stack Static Pressure ("H?0); -0.15
Stack Dimensions:_
Plume Appearance:
90" I.D.
Ambient Temperature(*F):
Record all Data Every 0.5
Noccle Number; -- ,Dia.(in.); 0.256
Pitot Tube No. 19 .Corr.Factor; 0.854
Meter Box No.RAG-4.Corr.Facton0.991
Meter Isokinetic Factor; 1685
Assumed Moisture(I); 2.7
Condensate Volume (ml): --
Minutes
Silica Gel Height Gain(g):
Leak Rate CFM at
MHg
Trav-
erse
Point
No.
N-6
N-6
N-6
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
Clock
15:10
15:11
15:21
15:22
16:23
16:24
Velocity
Pressure
("H20)
0.60
0.60
0.60
0.60
0.60
0.60
•
AVERAGE (TOTAL)
Stack
Temp
CF)
120
125
120
125
120
125
122
Dry Gas Meter
Volume
(ft3)
612.189
613.067
613.079
613.932
614.020
614.848
( 2.536 )
Temp('F)
Inlet
81
81
82
82
82
82
82
Outlet
82
82
82
82
82
82
82
Orifice
Pressure
Differ-
ential
("H20)
2.76
2.74
2.76
2.74
2.76
2.74
2.75
i-iiter
Box
Temp
CF)
240
240
230
230
230
230
233
Last
Imp.
Gas
Cemp
CF)
80
80
80
80
82
82
81
Sampling
Train
Static
Pressure
("Hg)
1.0
1.0
1.0
1.0
1.0
1.0
1.0
Clayton Environmental Consultants, Inc.
-------
C-167
SAMPLING TRAIN DATA
Company; Ford Motor Company
Source Designation; Coke Battery A Scrubber Inlet
Date: 9/4/75 Filter Heater Setting:
Test Number; Andersen Impactor Sample-IA Probe Heater Setting:
RGK
Field Person:
Filter Number:
Barometric Pressure ("Hg); 29.5
Stsek Static Pressure ("H20); -4.5
Stack Dimensions; 66" I.D.
Plume Appearance;
Ambient Temperature("F):
Record all Data Every Push
Nozsle Number; — ,Dia.(in.); 3/16
Pitot Tube No.11 .Corr.Factor; 0.824
Meter Box No.RAC-3.Corr.Factor 0.993
Meter Isokinetic Factor; 1745
Assumed Moisture(1):
Condensate Volume(ml);
Silica Gel Height Gain(g):
Leak Rate 0.015 CFM at 15 "Hg
Trav-
erse
Point
No.
T-4
Time
Samp-
ling
(sec)
0
60
0
60
0
60
Clock
09:00
09:40
09:51
Velocity
Pressure
("H20)
1.05
1.05
1.05
1.05
1.05
1.05
AVERAGE (TOTAL)
Stack
Temp
(°P)
80
100
80
100
80
100
90
Dry Gas Meter
Volume
(ft3)
924.835
926.698
( 1.85 )
Temp(°F)
Inlet
67
68
68
70
71
71
69
Outlet
67
68
68
70
71
71
69
Orifice
Pressure
Differ-
ential
("H20)
1.32
1.32
1.3
1.3
1.3
1.3
1.3
••liter
Box
Temp
CF)
Last
Imp.
Gas
Temp
rp>
Sampling
Train
Static
Pressure
("Hg)
Clayton Environmental Consultants, Inc.
-------
C-168
SAMPLING TRAIN DATA
Ford Motor Company
Company: ______ __
Source Designation; Coke Battery A Scrubber inlet
Date: 9/4/75 Filter Heater Setting:_
Test Number; Andersen Impgetor Sample-lBProbe Heater Setting:
RGK
Field Person;
Filter Number:
Barometric Pressure ("Hg); 29.5
Stack Static Pressure ("H20):
Stack Dimensions; 66" I.D.
Plume Appearance:
Ambient Temperature(°F):
Record all Data Every Push
Noetic Number; -- .Dla.(in.); 3/16
Pitot Tube No. 11,Corr.Factor; 0.624
Meter Box No.RAC-2,Corr,Factor;0.996
Meter Isokinetic Factor; 1701
Assumed Moisture(1):
Condensate Volume(ml);
Silica Gel Weight Gain(g):
Leak Rate 0.01Q CFM at 15 "Hg
Trav-
etse
Point
No.
T-4
Time
Samp-
ling
(sec )
0
70
0
70
0
70
Clock
14:25
15:02
15:13
(Telocity
Pressure
<"H20)
1.05
1.05
1.05
1.05
1.05
1.05
.
AVERAGE (TOTAL)
Stack
Temp
(•F)
85
95
85
95
82
95
90
Dry Gas Meter
Volume
(ft3)
150.585
152.754
( 2.16 )
Temp('F)
Inle
73
73
73
73
73
73
73
Outlet
73
73
73
73
73
73
73
Orifice
Pressure
Differ-
ential
("H20)
1.2
1.2
1.2
1.2
1.2
1.2
1.2
filter
Box
Temp
CF)
Last
Imp.
Gas
Temp
(•F)
Sampling
Train
Static
Pressure
("Hg)
Clayton Environmental Consultants, Inc.
-------
C-169
SAMPLING TRAIN DATA
Ford Motor Comoanv
Coqipany;
Source Designation; Coke Battery A Scrubber Inlet
Date: 9/5/75 Filter Heater Setting:^
Teat Humbert Andersen Impactor Sample-lC Probe Heater Setting:
KDS
Field Person:
Filter Number:
Barometric Pressure ("Hg); 29.52
Stack Static Pressure ("HgO); -4.5
66" I.D.
Stack Dimensions:
Plume Appearance:
Ambient Temperature(°F):
Record all Data Every Push
Nocsle Number: .Dia. (in*); 3/16
Pitot Tube No.11 .Corr.Factor; 0.824
Meter Box No.RAC-2,Corr.Factor;0.996
Meter Isokinetic Factor; 1701
Assumed Moisture(X):
Condenaate Volume(ml);
Silica Gel Weight Gain(g):
Leak Rate CFM at "Hg
Trav-
erse
Point
No.
T-4
Time
Samp-
ling
(sec)
0
70
0
70
0
70-
Clock
09:04
09:16
09:30
Velocity
Pressure
("H20)
1.05
1.05
1.05
1.05
1.05
1.05
.
AVERAGE (TOTAL)
Stack
Temp
(«F)
80
95
80
105
82
99
90
Dry Gas Meter
Vo lume
(ft3)
153.118
153.813
153.813
154.503
154.503
155.206
(2.08 )
Temp(°F)
Inlet
70
70
70
71
71
72
71
Outlet
70
70
70
71
71
72
71
Orifice
Pressure
Differ-
ential
<"H20)
1.2
1.2
1.2
1.2
1.2
1.2
1.2
filter
Box
Temp
CF)
Last
Imp.
Gas
Temp
CF)
Sampling
Train
Static
Pressure
("Hg)
Clayton Environmental Consultants, Inc.
-------
Ford Motor Company
C-170
SAMPLING TRAIN DATA
anj
Company:
Source Designation; Coke Battery A Scrubber inlet
Date: 9/5/75 Filter Heater Setting:
Test Number; Andersen Impactor Sample-2A Probe Heater Setting:
KDS
Field Person;
Filter Number:
Barometric Pressure ("Hg); 29.32
Stack Static Pressure ("HgO); -4.5
66" I.D.
Stack Dimensions:
Plume Appearance;
Ambient Temperature(*F):
Record all Data Every Push
Nocsle Number: .Dla. (In.)• 3/16
Pltot Tube No. 11,Corr.Factor; 0.824
Meter Box No.RAC-2»Corr.Factor; 0.996
Meter Isoklnetlc Factor:
Assumed Moisture(I);
Condensate Volume(ml);
Silica Gel Weight Gain(g):
Leak Rate p.019 CFM at 15 "Hg
Trav-
erse
Point
No.
1
Time
Samp-
ling
(sec)
0
72
0
72
0
72
Clock
12:51
13:19
13:31
Velocity
Pressure
<"H20)
1.1
1.1
1.1
1.1
1.1
1.1
•
AVERAGE (TOTAL)
Stack
Temp
(°F)
82
105
78
94
75
94
88
Dry Gas Meter
Volume
(ft*)
155.792
156.554
156.554
157.266
157.266
158.150
( 2.35 )
Temp(-F)
Inlet
75
75
70
70
68
68
71
Outlet
75
75
70
71
70
70
72
Orifice
Pressure
Differ-
ential
("H20)
1.4
1.4
1.4
1.4
1.4
1.4
1.4
niter
Box
Temp
<°F)
Last
Imp.
Gas
Temp
(•pj
Sampling
Train
Static
Pressure
("Hg)
Clayton Environmental Consultants, Inc.
-------
C-171
SAMPLING TRAIN DATA
Ford Motor Company
Coke Battery A Scrubber Inlet
Company;
Source Designation:
Date: 9/8/75 Filter Heater Setting:
Test Number; Andersen Impactor Sample-2B Probe Heater Setting:
KDS
Field Person:
Filter Number:
Barometric Pressure ("Hg); 29.53
Stack Static Pressure ("H20):_
Stack Dimensions; 66" I»D.
Plume Appearance:
Ambient Temperature (°F):
Record all Data Every Push
Nozcle Number: ,Dia.(in.); 3/16
Pitot Tube No. 11.Corr.Factor: 0.824
Meter Box No. RAG-2.Corr.Factor; 0.996
Meter leokinetic Factor; 1701
Assumed Moisture(1):
Condensate Volume(ml):
Silica Gel Weight Gain(g):
Leak Rate CFM at
'Hg
Trav-
erse
Point
No.
-------
C-172
Company:
Source Designation:^
Date: 9/8/73
SAMPLING TRAIN DATA
Ford Motor Company
Coke Battery A Scrubber Inlet
Teat Number;Andersen Impactor Sample-2C
Field Person: KDS
Filter Number:
Barometric Pressure ("Hg); 29.53
Stack Static Pressure ("H?0); -4.5
Stack Dimensions: 66" I.D.
Plume Appearance:
Ambient Temperature(°F); 66
Record all Data Every push
Filter Heater Setting:
Probe Heater Setting:
Nozzle Number: ,Dia. (in.); 3/16
Pitot Tube No. 11 ,Corr.Factor; 0.824
Meter Box No. RAC-2»Corr.Factor; 0.996
Meter Isokinetic Factor; 1701
Assumed Moisture (X) : 1
Condensate Volume(ml):
Silica Gel Weight Gain(g):
Leak Rate CFM at "Hg
Trav-
erse
Point
No.
79
89
79
85
75
95
84
Dry Gas Meter
Volume
(ft3)
160.500
161.275
161.275
162.041
162.041
162.799
( 2.29 )
Tcmp(°F)
Inlet
65
65
66
66
66
66
66
Outle t
66
66
66
67
67
67
66
Orifice
Pressure
Differ-
ential
<"H20)
1.4
1.4
1.4
1.4
1.4
1.4
1.4
Filter
Box
Temp
<°F)
Last
Imp.
Gas
Temp
(°F)
-
Samplinf
Train
Static
Pressure
("Hg)
-
Clayton Environmental Consultants, Inc.
-------
C-173
SAMPLING TRAIN DATA
Ford Motor Company
Company:_
Source Designation; Coke Battery A Scrubber Inlet
Date: 9/9-10/75 ; Filter Heater Setting:
Test Number; Andersen Impactor Sample-3AProbe Heater Setting:
KDS
Field Person:
Filter Number:
Barometric Pressure ("Hg); 29.78
Stack Static Pressure ("H;0); -4.5
Stack Dimensions; 66" I.D.
Plume Appearance:
Ambient Temperature(*F):
Record all Data Every Push
Noxcle Number: ,Dia» (in.); 3/16
Pitot Tube No. 11.Corr.Factor; 0.824
Meter Box No.RAC-2.Corr.Pacton0.996
Meter Isokinetic Factor; 1701
Assumed Moisture(I); 1
Condensate Volume(ml):
Silica Gel Weight Gain(g):
Leak Rate CFM at
'Hg
Trav-
erse
Point
No.
1.4
1.4
1.4
1.4
1.4
1.4
1.4
••liter
Box
Temp
CF)
Last
Imp.
Gas
Temp
CP)
Sampling
Train
Static
Pressure
("Hg)
Clayton Environmental Consultants, Inc.
-------
C-174
SAMPLING TRAIN DATA
Company; Ford Motor Company
Source Designation; Coke Battery A Scrubber Inlet
Date: 9/10/75 Filter Heater Setting^
Teat Number; Andersen Impactor Sample-3B Probe Heater Setting:
EPS
Field Person:__
Filter Number:
Barometric Pressure ("Hg)t 29.61
Stack Static Pressure ("HjO):
Stack Dimensions; 66" I.P.
Plume Appearance:
Ambient Temperature(°F):
Record all Data Every Push
Noccle Number: .Dia. (in.); 3/16
Pitot Tube No.11 ,Corr.Factor; 0.824
Meter Box No. RAC-2',Corr. Factor; 0. 996
Meter Isokinetic Factor; 1701
Assumed Moisture(I);
Condensate Volume(ml):
Silica Gel Weight Gain(g):
Leak Rate CFM at "Hg
Trav-
erse
Point
No.
65
82
68
82
68
89
76
Dry Gas Meter
Volume
(ft3)
164.975
165.739
165.739
166.489
166.489
167.242
( 2.26 )
Temp(°F)
Inlet
65
65
66
67
66
66
66
Outlet
65
65
66
66
66
66
66
Orifice
Pressure
Differ-
ential
("H20)
1.4
1.4
1.4
1.4
1.4
1.4
1.4
filter
Box
Temp
CF)
Last
Imp.
Gas
Temp
(•FJ
Sampling
Train
Static
Pressure
("Hg)
Clayton Environmental Consultants, Inc.
-------
C-175
SAMPLING TRAIN DATA
Company; Ford Motor Company
Source Designation; Coke Battery A Scrubber Inlet
Date: 9/10/75 Filter Heater Setting^
Teat Number; Andersen Inpactor Sample-3C Probe Heater Setting:
KDS
Field Person;
Filter Number:
Barometric Pressure ("Hg):
Stack Static Pressure ("H20):_
Stack Dimensions! 66" I.D.
Plume Appearance:
29.61
Ambient Temperature(°F):
Record all Data Every Push
Nocile Number: .Dia. (In.); 3/16
Pltot Tube No. 11 ,Corr.Factor; 0.824
Meter Box No.RAC-2.Corr.Factor;0.996
Meter Isoklnetlc Factor; 1701
Assumed Moisture(1);
Condensate Volume(ml):
Silica Gel Weight Galn(g):
Leak Rate CFM at "Hg
Trav-
erse
Point
No.
-------
C-176
SAMPLING TRAIN DATA
Ford Motor Company
Company;
Source Designation; Coke Battery A Scrubber Inlet
Date: 9/10/75 Filter Heater Setting:
Test Number; Andersen Impactor Sample-AA Probe Heater Setting:
KDS
Field Person;
Filter Number:
Barometric Pressure ("Hg); 29.50
Stack Static Pressure ("H20):
Stack Dimensions; 66" I.D.
Plume Appearance:
Ambient Temperature(°F):
Record all Data Every Push
70
Notcle Number: .Dla. (In.); 3/16
Pltot Tube No. 11 ,Corr.Factor; 0.824
Meter Box No. RAC-2'.Corr.Factor; 0.996
Meter Isoklnetlc Factor; 1701
Assumed Moisture(I); 1
Condensate Volume(ml):
Silica Gel Weight Galn(g):
Leak Rate CFM at "Hg
Trav-
erse
Point
No.
<1
Time
Samp-
ling
(sec)
0
72
0
72
0
72
Clock
14:06
14:14
14:27
-
Velocity
Pressure
("H20)
1.1
1.1
1.1
1.1
1.1
1.1
•
AVERAGE (TOTAL)
Stack
Temp
(°F)
79
115
85
105
82
98
94
Dry Gas Meter
Volume
(ft3)
169.652
170.378
170.378
171.130
171.130
171.857
( 2.20 )
Temp(°F)
Inlet
70
70
70
70
71
72
70
Outlet
70
70
70
70
71
71
70
Orifice
Pressure
Differ-
ential
("H20)
1.4
1.4
1.4
1.4
1.4
1.4
1.4
filter
Box
Temp
CF)
LastlSampling
Imp.l Train
Gasl Static
Cemplpressure
CF)I ("Hg)
Clayton Environmental Consultants, Inc.
-------
C-177
SAMPLING TRAIN DATA
Ford Motor Company
Company:
Source Designation; Coke Battery A Scrubber Inlet
Date: 9/11/75 Filter Heater Setting:
Teat Number; Andersen Impactor Sample-4B Probe Heater Setting:
RCK
Field Person:
Filter Number:
Barometric Pressure ("Hg); 29.20
Stack Static Pressure ("I^O): -4.5
Stack Dimensions; 66" I.D.
Plume Appearance:
Ambient Temperature(°F):
Record all Data Every push
Nocile Number: .Dia. (in.); 3/16
Pitot Tube No. 11 .Corr.Factor; 0.824
Meter Box No.RAG-21Corr.Factor0.996
Meter Isokinetic Factor:
Assumed Moisture(Z):
Condensate Volume(ml):
Silica Gel Weight Gain(g):
Leak Rate 0.01 CFM at 15 "Hg
Trav-
erse
Point
No.
°L
Time
Samp-
ling
(sec)
0
36
72
0
36
72
0
36
72
Clock
08:41
08:51
09:09
Velocity
Pressure
("H20)
1.2
1.2
1.2
1.2
1.2
1.2
1.2
1.2
1.2
.
AVERAGE (TOTAL)
Stack
Temp
(°F)
70
190
88
75
195
85
70
180
95
116
Dry Gas Meter
Volume
(£t3)
171.866
172.677
172.677
173.468
173.468
174.269
( 2.39 )
Temp(°F)
Inlet
70
72
72
73
72
74
72
Outlet
70
71
71
72
72
73
72
Orifice
Pressure
Differ-
ential
("H20)
1.4
1.4
1.4
1.4
1.4
1.4
1.4
1.4
1.4
1.4
filter
Box
Temp
(•F)
Last
Imp.
Gas
Temp
rp?
Sampling
Train
Static
Pressure
("Hg)
Clayton Environmental Consultants, Inc.
-------
C-178
SAMPLING TRAIN DATA
Company; Ford Motor Company
Source Designation; Coke Battery A Scrubber Inlet
Date: 9/11/75 Filter Heater Setting:
Teat Number; Andersen Impactor Sample-4C Probe Heater Setting:_
Field Person: RGK
Filter Number:
Barometric Pressure ("Hg):
Stack Static Pressure <
Stack Dimensions; 66" I.D.
Plume Appearance:
29.10
-4.5
Ambient Temperature (°F) :
Record all Data Every Push
Nozzle Number: .Dia. (in. )8 3/16
Pitot Tube No.11 .Corr.Factor; 0.824
Meter Box No. RAC-2.Corr.Factor; 0.996
Meter Isokinetic Factor:
Assumed Moisture(X):
Condensate Volume(ml);
Silica Gel Weight Gain(g):
Leak Rate CFM at "Hg
Trav-
erse
Point
No.
-------
C-179
SAMPLING TRAIN DATA
Ford Motor Company
Conpany:
Source Designation; Coke Battery A Scrubber Inlet
Date: 9/11/75 ' Filter Heater Setting:
Teat Number; Andersen Impactor Sample-5A Probe Heater Setting:
RGK
Field Person:
Filter Number:
Barometric pressure ("Hg); 29.10
Stack Static Pressure ("H?0); -4.5
Stack Dimensions; 66" I.D.
Plume Appearance:
Ambient Temperature("F):
Record all Data Every Push
Noetic Number: .Dla.dn.l; 3/16
Pltot Tube No. 11.Corr.Factor; 0.824
Meter Box Ho. RAC-21 Corr. Factor. 0.996
Meter Isoklnetlc Factor;
Assumed Moisture(X):
Condensate Volume(ml):
Silica Gel Weight Galn(g):
Leak Rate 0.01 CFM at 15 "Hg
Trav-
erse
Point
No.
T-10
Time
Samp-
ling
(sec )
0
36
72
0
36
72
0
36
72
Clock
14:06
14:18
14:25
Velocity
Pressure
("H20)
1.2
1.4
1.2
1.2
1.4
1.2
1.2
1.4
1.2
•
AVERAGE (TOTAL)
Stack
Temp
(•F)
75
185
100
78
160
95
75
175
90
115
Dry Gas Meter
Volume
(«t3)
176.852
177.703
177.703
178.502
178.502
179.298
( 2.44 )
TempCF)
Inlet
74
74
74
74
74
Outlet
74
74
74
74
74
Orifice
Pressure
Differ-
ential
("H20)
1.4
1.4
1.4
1.4
1.4
1.4
1.4
1.4
1.4
1.4
rilter
Box
Temp
CF)
Last
Imp.
Gas
Temp
CF>
Sampling
Train
Static
Pressure
("Hg)
Clayton Environmental Consultants, Inc.
-------
C-180
SAMPLING TRAIN DATA
Ford Motor Company
Coke Battery A Scrubber Inlet
Company:
Source Designation:^
Date: 9/12/75 Filter Heater Setting:
Teet Number; Andersen Impacter Sample-6A Probe Heater Setting:
KDS
Field Person:
Filter Number:
Barometric Pressure ("Hg); 29.28
Stack Static pressure ("H?0); -4.5
Stack Dimensions; 66" I.D.
Plume Appearance:
Ambient Temperature(*F); 60
Record all Data Every Push
Noscle Number: .Die. (In.); 3/16
Pitot Tube No. 11 .Corr.Factor; 0.824
Meter Box No.RAG-21Corr.Factor; 0.996
Meter Isokinetic Factor;
Assumed Moisture(X):
Condensate Volume(ml);
Silica Gel Weight Gain(g):
Leak Rate CFM at "Hg
Trav-
erse
Point
No.
T-10
Time
Samp-
ling
(sec)
0
36
72
0
36
72
0
36
72
Clock
08:28
09:56
10:09
(Telocity
Pressure
("H20)
1.2
1.4
1.2
1.2
1.4
1.2
1.2
1.4
1.2
•
•
AVERAGE (TOTAL)
Stack
Temp
CF)
58
160
74
60
155
75
60
110
65
91
Dry Gas Meter
Volume
(£t3)
179.381
180.140
180.140
180.925
180.925
181.675
(2.28 )
Temp(°F)
Inlet
55
55
56
56
56
56
57
58
58
56
Outlet
55
55
56
56
56
56
57
58
58
56
Orifice
Pressure
Differ-
ential
("H20)
1.5
1.5
1.5
1.5
1.5
1.5
1.5
1.5
1.5
filter
Box
Temp
(•F)
1
1.5
LastlSampling
Imp. Train
Gas 1 Static
rempPressure
CF) C'Hg)
Clayton Environmental Consultants, Inc.
-------
C-181
SAMPLING TRAIN DATA
Ford Motor Company
Company:
Source Designation; Coke Battery A Scrubber Inlet
Date: 9/12/75 and 9/15/75 Filter Heater Setting:
Test Number; Andersen Impactor Sample-SB Probe Heater Setting:
KDS
Field Person:
Filter Number:
Barometric Pressure ("Hg)t Avg. 29.49
Stack Static Pressure ("HgO); -4.5
66" I.D.
Stack Dimensions:
Plume Appearance:
Ambient Temperature(°F); 65
Record all Data Every push
Noccle Number: .Die, (in.); 3/16
Pitot Tube No. 11 ,Cerr.Factor; 0.824
Meter Box No.RAC-2,Corr.Factor; 0.996
Meter Isoklnetic Factor; 1701
Assumed Moisture (X) : 1
Condensate Volume(ml);
Silica Gel Weight Gain(g):
Leak Rate CFM at "Hg
Trav-
erse
Point
No.
T-10
9/15
Time
Samp-
ling
(sec)
0
36
72
0
36
72
0
36
7 2
Clock
12:25
,
12:38
08:25
Velocity
Pressure
("H20)
1.2
1.4
1.2
1.2
1.4
1.2
1.2
1.4
1.2
AVERAGE (TOTAL)
Stack
Temp
(•F)
65
160
82
66
125
75
70
160
95
100
Dry Gas Meter
Volume
Sampling
Train
Static
pressure
("Hg)
Clayton Environmental Consultants, Inc.
-------
C-182
SAMPLING TRAIN DATA
Company; Ford Motor Company
Coke Battery A Scrubber inlet
Source Designation:^
Data: 9/15/75 Filter Heater Setting:
Teat Number! Andersen Impacter Sample-SC Probe Heater Setting:
KDS
Field Person:
Filter Number;
Barometric Pressure ("Hg); 29.70
Stack Static Pressure ("H;0); -ft.5
Stack Dimensions; 66" I.D.
Plume Appearance:
Ambient Temperature(*F) :
Record all Data Every Push
65
Nocsle Number; .Pia.(in.)•_ 3/16
Pitot Tube Ho. 11 .Corr.Factor; 0.824
Meter Box No.RAC-2,Corr.FactorI 0.996
Meter laokinetic Factor; 1701
Assumed Moisture(X):
Condensate Volume(ml):
Silica Gel Weight Gain(g):
Leak Rate CFM at "Hg
Trav-
erse
Point
No.
T-10
Time
Samp-
ling
(sec)
0
36
72
e
36
72
0
36
72
Clock
09:55
10:02
10:10
Velocity
Pressure
("H20)
1.2
1.4
1.2
1.2
1.4
1.2
1.2
1.4
1.2
•
AVERAGE (TOTAL)
Stack
Temp
CF)
60
305
107
74
220
95
76
165
89
L32
Dry Gas Meter
Volume
(ft3)
184.349
185.112
185.112
185.865
185.865
186.659
( 2.30 )
Temp('F)
Inlet
58
58
59
58
59
60
59
60
61
59
Outlet
58
58
59
58
58
59
59
59
59
59
Orifice
Pressure
Differ-
ential
("H20)
1.5
1.5
1.5
1.5
1.5
1.5
1.5
1.5
1.5
1.5
Filter
Box
Temp
CF)
Last
Imp.
Gas
temp
(°F>
Sampling
Train
Static
Pressure
("Hg)
Clayton Environmental Consultants, Inc.
-------
C-183
SAMPLING TRAIN DATA
Ford Motor Company
Coke Battery A Scrubber Inlet
Company:
Source Designation:
Date: 9/15/75 Filter Heater Setting:
Teat Number; Andersen Impactor Sample-7A Probe Heater Setting:
KDS
Field Person:
Filter Number:
Barometric Pressure ("Hg); 29.70
Stack Static Pressure ("HgO): -4.5
66" I.D.
Stack Dimensions:
Plume Appearance;
Ambient Temperature(*F):
Record all Data Every Push
68
Nettle Number: .Dia.(in.); 3/16
Pitot Tube No. 11.Corr.Factor; 0.824
Meter Box No. RAC-2.Corr.Factor; 0.996
Meter Isokinetic Factor; 1701
Assumed Moisture(I); 1
Condensate Volume(ml);
Silica Gel Weight Gain(g):
Leak Rate CFM at "Hg
Trav-
erse
Point
No.
T-10
Time
Samp-
ling
(eeo)
0
36
72
0
36
72
0
36
72
Clock
12:23
12:59
13:22
(Telocity
Pressure
("H20)
1.2
1.4
1.2
1.2
1.4
1.2
1.2
1.4
1.2
.
AVERAGE (TOTAL)
Stack
Temp
(°F)
68
250
84
68
335
105
72
72
90
127
Dry Gas Meter
Volume
(ft3)
186.743
187.539
187.539
188.322
188.322
188.988
(2.24 )
Temp(aF)
Inlet
64
65
65
65
66
66
66
66
66
65
Outlet
65
65
65
65
66
66
66
66
66
66
Orifice
Pressure
Differ-
ential
("H20)
1.5
1.5
1.5
1.5
1.5
1.5
1.5
1.5
1.5
1.5
••liter
Box
Temp
CF)
Last
Imp.
Gas
Temp
CV)
Sampling
Train
Static
pressure
("Hg)
Clayton Environmental Consultants, Inc.
-------
C-184
SAMPLING TRAIN DATA
Ford Motor Company
Coke Battery A Scrubber Inlet
Company:
Source Designation:
Date: 9/15/75 Filter Heater Setting:
Teat Number; Andersen Impactor Sample-7B Probe Heater Setting:_
Field Person:_
Filter Number:
KDS
Barometric Pressure ("Hg); 29.70
Stack Static Pressure ("I^O): -4.5
Stack Dimensions; 66" I.D.
Plume Appearance:
Ambient Temperature (*F):
Record all Data Every Push
70
Nocile Number: ,Dia. (In.); 3/16
Pitot Tube No. 11jCorr.Factor; 0.824
Meter Box No.RAC-2 ,Corr.Factor0.996
Meter Isokinetic Factor; 1701
Assumed Moisture(1): 1
Condensate Volume(ml);
Silica Gel Weight Gain(g):
Leak Rate CFM at "Hg
Trav-
erse
Point
No.
T-10
Time
Samp-
ling
(sec)
0
36
72
0
36
72
0
36
72
Clock
14:25
14:50
14:56
Velocity
Pressure
("H20)
1.2
1.4
1.2
1.2
1.4
1.2
1.2
1.4
1.2
•
AVERAGE (TOTAL)
Stack
Temp
(°F)
72
120
95
75
230
92
75
180
96
115
Dry Gas Meter
Volume
(ft3)
189.015
189.861
189.861
190.652
190.652
191.426
( 2.40 )
TempCP)
Inlet
68
68
68
67
67
67
67
68
68
68
Outlet
68
68
68
67
67
67
67
68
68
68
Orifice
Pressure
Differ-
ential
("H20)
1.5
1.5
1.5
1.5
1.5
1.5
1.5
1.5
1.5
1.5
••liter
Box
Temp
(°F)
Last
Imp.
Gas
Temp
CF>
Sampling
Train
Static
pressure
("Hg)
Clayton Environmental Consultants, Inc.
-------
C-185
SAMPLING TRAIN DATA
Company; Ford Motor Company
Source Designation; Coke Battery A Scrubber Inlet
Data: 9/16/75 Filter Heater Setting:,
Teat Number; Andersen Impaetoj Sample-7C Probe Heater Setting:
KDS
Field Pereon;
Filter Number:
Barometric Pressure ("Hg)t 29.51
Stack Static Pressure ("H?0); -4.5
Stack Dimensions: 66" I.D.
Plume Appearance;
Ambient Temperature("F) ; 60
Record all Data Every Push
NocKle Number: .Dia. (in.); 3/16
Pitot Tube No.11 .Corr.Factor; 0.824
Meter Box No. RAC-2,Corr.Factor; 0. 996
Meter Isokinetic Factor; 1701
Assumed Moisture(I); 1
Condensate Volume(ml):
Silica Gel Weight Gain(g):
Leak Rate CFM at "Hg
Trav-
erse
Point
No.
T-10
Time
Samp-
ling
(sec)
0
36
72
0
36
72
0
36
72
Clock
08:34
08:48
08:55
Velocity
Pressure
("H20)
1.2
1.4
1.2
1.2
1.4
1.2
1.2
1.4
1.2
.
AVERAGE (TOTAL)
Stack
Temp
(•F)
61
130
66
64
145
76
64
245
77
103
Dry Gas Meter
Volume
(*t3)
191.509
192.317
192.317
193.106
193.106
193.878
( 2.36 )
TempCP)
Inlet
57
57
57
57
58
58
58
58
59
58
Outlet
57
57
57
57
58
58
58
58
59
58
Orifice
Pressure
Differ-
ential
("H20)
1.5
1.5
1.5
1.5
1.5
1.5
1.5
1.5
1.5
1.5
filter
Box
Temp
CF)
Last
Imp.
Gas
Temp
(•pj
Sampling
Train
Static
Pressure
("Hg)
Clayton Environmental Consultants, Inc.
-------
C-186
SAMPLING TRAIN DATA
Company; Ford Motor Company
(Page 1 of 2)
Coke Battery A Scrubber Outlet
Source Designation:
Data: 9/4/75 Filter Heater Setting: --
Teat Number; Andersen Impactor Sample-1 Probe Heater Setting;
GMS/GEH
Field Person:__
Filter Number:
Barometric Pressure ("Kg); 29.5
A-245-04
Stack Static Pressure ("H20)t-0.31
Stack Dimensions! 90" I.D.
Plume Appearance: --
Ambient Temperature(*F):
Record all Data Every Push
Nocsle Number: --.Bta.(in.); 1/4
Pitot Tube No. 19»Corr.Factor; 0.854
Meter Box No.RAC-4»Corr.Factor! 1.009
Meter laokinetic Factor; 1683
Assumed Moisture(I); 1
Condensate Volume(ml);
Silica Gel Weight Gain(g):
Leak Rate CFM at "Hg
trav-
erse
Point
No.
S-l
S-l
S-l
S-l
S-l
Time
Samp-
ling
(sec)
0
30
60
0
30
60
0
30
60
0
35
70
0
35
70
Clock
09:00
09:40
09:51
14:25
15:02
Velocity
Pressure
("H20)
0.11
0.11
0.11
0.11
0.11
0.11
0.11
0.11
0.11
0.11
0.11
0.11.
0.11
0.11
0.11
AVERAGE (TOTAL)
Stack
Temp
CP)
120
125
130
120
125
125
120
125
125
120
120
125
120
125
125
Dry Gas Meter
Volume
(ft3)
91.106
91.5
91.927
91.927
92.1
92.315
92.315
92.5
92.685
92.685
92.8
93.146
93.146
93.4
93.599
( )
Temp('F)
Inlet
70
72
72
70
72
72
70
72
72
70
72
72
70
72
73
Outlet
70
72
72
70
72
72
70
72
72
70
72
72
70
74
75
Orifice
Pressure
Differ.
ential
<"H20)
0.46
0.46
0.46
0.46
0.46
0.46
0.46
0.46
0.46
0.46
0.46
0.46
0.46
0.46
0.46
'liter
Box
Temp
CF)
Last
Imp.
Gas
Temp
<*F>
Sampling
Train
Static
Pressure
("Hg)
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
Clayton Environmental Consultants, Inc.
-------
C-187
SAMPLING TRAIN DATA
Company; Ford Motor Company
(Page 2 of 2)
Source Designation; Coke Battery A Scrubber Outlet
9/4-5/75
Date:
Test Number; Andersen Impactor Sample-1
Field Person: GMS/GEH
Filter Number; A-245-04
Barometric Pressure ("Hg); 29.5
Filter Heater Setting:
Probe Heater Setting:
Stack Static Pressure ("HgO); -0.31
Stack Dimensions; 90" I.D.
Plume Appearance: --
Ambient Temperature(°F):
Record all Data Every Push
Nozzle Number; -- .Dia.(in.); 1/4
Pitot Tube No. 19.Corr.Factor; Q.854
Meter Box Ho.RAC-4.Corr.Facton11.009
Meter Isokinetic Factor; 1683
Assumed Moisture (X) : 1
Condensate Volume(ml);
Silica Gel Weight Gain(g):_--
Leak Rate
CFM at
"Hg
Trav-
erse
Point
No.
S-l
9/5
S-l
S-l
S-l
Time
Samp-
ling
(sec)
0
35
70
0
35
70
0
35
70
0
35
70
Clock
15:13
09:04
09:16
09:30
(Telocity
Pressure
("H20)
0.11
0.11
0.11
0.11
0.11
0.11
0.11
0.11
0.11
0.11
0.11
0.11
AVERAGE (TOTAL)
Stack
Temp
(°F)
120
125
125
125
125
125
125
125
125
120
120
120
123
Dry Gas Meter
Volume
(ft3)
93.599
93.8
94.043
94.124
94.3
94.559
94.559
94.8
95.027
95.027
95.3
95.478
( 4.33 )
Temp(°F)
Inlet
73
74
74
70
70
72
70
71
71
70
71
71
71
Outlet
75
76
76
70
70
72
70
71
71
70
71
71
72
Orifice
Pressure
Differ-
ential
("H20)
0.46
0.46
0.46
0.46
0.46
0.46
0.46
0.46
0.46
0.46
0.46
0.46
0.46
Filter
Box
Temp
(°F)
Last
Imp.
Gas
Temp
(°F)
Sampling
Train
Static
Pressure
("Hg)
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
Clayton Environmental Consultants, Inc.
-------
C-188
SAMPLING TRAIN DATA
Ford Motor Company
Company:
Source Designation; Coke Battery A Scrubber Outlet
Data: 9/5-6/75 Filter Heater Setting:
Teat Number; Andersen Impacfcor Sample-2 Probe Heater Setting:
(Page 1 of 2)
GMS/GEH
A-245-23
Field Person:_
Filter Number:
Barometric Pressure ("Hg); 29.52
Stack Static Pressure ("H20); -0.31
90" I.D.
Stack Dimensions:
Plume Appearance: --
Ambient Temperature(°F):
Record all Data Every Push
Nozzle Number; --,Dia.(in.); 1/4
Pltot Tube No. 19tCorr.Factor; 0.854
Meter Box No.RAC-4,Corr.Factor 1.009
Meter Isokinetic Factor; 1683
Assumed Moisture (I): 1
Condensate Volume(ml);
Silica Gel Weight Gain (g):__--
Leak Rate
CFH at
"Hg
Trav-
erse
Point
No.
W-l
W-l
W-l
9/6
W-l
W-l
Time
Samp-
ling
(sec)
0
36
72
0
36
72
0
36
72
0
36
72
0,
36
72
Clock
12:51
13:19
13:31
10:36
11:02
Velocity
Pressure
("H20)
0.39
0.39
0.39
0.39
0.39
0.39
0.39
0.39
0.39
0.39
0.39
0.39-
0.39
0.39
0.39
•
AVERAGE (TOTAL)
Stack
Temp
<°F)
120
125
125
120
120
120
120
125
125
125
135
130
120
125
130
Dry Gas Meter
Volume
(ft3)
95.745
96.1
96.514
96.514
96.8
97.312
96.312
97.7
98.139
98.225
99.047
99.048
99.976
( )
Temp(°F)
Inlet
70
71
71
70
70
71
70
71
71
65
65
65
65
65
Outlet
70
71
71
70
70
71
70
71
71
65
65
65
65
65
Orifice
Pressure
Differ-
ential
("H20)
1.6
1.6
1.6
1.6
1.6
1.6
1.6
1.6
1.6
1.6
1.6
1.6
1.6
1.6
rilter
Box
Temp
(°F)
Last
Imp.
Gas
Temp
CF)
Sampling
Train
Static
Pressure
("Hg)
3.0
3.0
3.0
3.0
3.0
3.0
3.1
3.1
3.1
4.0
4.0
3.5
3.5
Clayton Environmental Consultants, Inc.
-------
C-189
SAMPLING TRAIN DATA
Company; Ford Motor Company
(Page 2 of 2)
Coke Battery A Scrubber Outlet
Source Designation:
Date: 9/6/75 Filter Heater Setting:
Teat Number; Andersen Impactor Sample-2 Probe Heater Settlng:_
Field Person: RGK
Filter Number; A-245-23
Barometric Pressure ("Hg); 29.52
Stack Static Pressure <"H;0); -0.31
Stack Dimensions; 90" I,p.
Plume Appearance: --
Ambient Temperature(°F):
Record all Data Every Push
Nozzle Number; -- ,Dia. (in. ) ; J./4
Pitot Tube No. 19,Corr.Factor; 0.854
Meter Box No.RAC-4'tCorr.Factor; 1.009
Meter Isokinetic Factor; 1683
Assumed Moisture(I); 1
Condensate Volume(ml);
Silica Gel Weight Galn(g) :_J--
Leak Rate
CFM at
"Hg
Trav-
erse
Point
No.
W-l
W-l
W-l
W-l
Time
Samp-
ling
(8ec ?
0
30
72
0
36
72
0
36
72
0
36
72
Clock
11:51
13:37
14:03
14:31
Velocity
Pressure
("H20)
0.39
0.39
0.39
0.39
0.39
0.39
0.39
0.39
0.39
0.39
0.39
0.39
AVERAGE (TOTAL)
Stack
Temp
CF)
128
120
125
122
120
122
118
116
120
120
123
Dry Gas Meter
Volume
(ft3)
100.012
100.334
100.467
101.292
101.292
102.148
102.980
( 7.18 )
Temp(°F)
Inlet
65
66
66
66
67
67
66
66
66
68
Outlet
65
66
66
66
68
68
68
68
69
68
Orifice
Pressure
Differ-
ential
("H20)
1.6
1.6
1.6
1.6
1.6
1.6
1.6
1.6
1.6
1.6
1.6
1.6
1.6
••liter
Box
Temp
CF)
Last
Imp.
Gas
Temp
CF)
Sampling
Train
Static
Pressure
("HR)
3.2
Clayton Environmental Consultants, Inc.
-------
C-190
SAMPLING TRAIN DATA
Company; Ford Motor Company
(Page 1 of 2)
Source Designation; coke Battery A scrubber Outlet
Date: 9/9-10/75 Filter Heater Setting:
Test Number; Andersen Imoactor Sample-3Probe Heater Setting:_
RGK
A-245-17
Field Peraon:
Filter Number:
Barometric Pressure ("Hg); Avg. 29.70
Stack Static Pressure ("H20); -0.31
90" I.D.
Stack Dimensions:
Plume Appearance: --
Ambient Temperature(°F): -
Record all Data Every Push
Nozzle Number; — ,Dia.(in.); 1/4
Pitot Tube No. 19,Corr.Factor; 0.854
Meter Box No.RAC-4»Corr.Factor; 1.009
Meter Isokinetic Factor; 1683
Assumed Moisture(I);
Condensate Volume(ml);
Silica Gel Weight Gain(g); --
Leak Rate 0.004 CFM at 15
"Hg
Trav-
erse
Point
No.
W-3
9/10
W-3
W-3
W-3
W-3
Time
Samp-
ling
(sec)
0
36
72
0
36
72
0
36
72
0
36
72
0
36
72
Clock
09:59
08:22
08:35
10:05
10:17
Velocity
Pressure
("H20)
0.65
0.65
0.65
0.65
0.65
0.65
0.65
0.65
0.65
0.65
0.65
0.65
0.65
0.65
0.65
AVERAGE (TOTAL)
Stack
Temp
CF)
130
135
130
130
140
140
135
140
130
130
145
145
135
145
145
Dry Gas Meter
Volume
(ft3)
103.053
103.732
103.733
104.838
104.838
105.898
105.898
106.933
106.933
107.978
( )
Temp(°F)
Inlet
60
60
62
62
62
63
64
66
66
67
68
Outlet
69
69
69
69
70
69
69
69
69
68
68
Orifice
Pressure
Differ-
ential
("H20)
2.7
2.7
2.7
2.7
2.7
2.7
2.7
2.7
2.7
2.7
2.7
2.7
2.7
2.7
2.7
filter
Box
Temp
CF)
Last
Imp.
Gas
Temp
CPJ
Sampling
Train
Static
Pressure
("Hg)
Clayton Environmental Consultants, Inc.
-------
C-191
SAMPLING TRAIN DATA
(Page 2 of 2)
Company; Ford Motor Company
Source Designation! Coke Battery A Scrubber Outlet
Date: 9/10/75 Filter Heater Setting:
Test Number: Andersen Impactor Sample-3 Probe Heater Setting:
RGK
A-245-17
Field Person:
Filter Number:
Barometric Pressure ("Hg); Avg.29.70
Stack Static Pressure ("l^O); -0.31
Stack Dimensions; 90" I.D.
Plume Appearance: «
Ambient Temperature(°F):
Record all Data Every Push
Nocile Number; -- ,Dla. (in. ) ; J./4
Pitot Tube No. 19,Corr.Factor; 0.854
Meter Box No.RAC-4.Corr,Factor; 1.009
Meter Isokinetic Factor; 1683
Assumed Moisture (X) : _.
Condensate Volume(ml);
Silica Gel Height Galn(g):_-_-
Leak Rate
CFM at
"Hg
Trav-
erse
Point
No.
W-3
W-3
W-3
W-3
Time
Samp-
ling
(sec)
0
36
72
0
36
72
0
36
72
0
36
72
Clock
10:34
11:55
12:12
12:25
Velocity
Pressure
("H20)
0.65
0.65
0.65
0.65
0.65
0.65
0.65
0.65
0.65
0.65
0.65
0.65.
AVERAGE (TOTAL)
Stack
Temp
(°F)
120
130
130
125
140
130
125
125
130
125
130
140
134
Dry Gas Meter
Volume
(ft3)
107.978
109.059
109.062
110.131
110.131
111.213
111.213
112.285
( 9.31 )
Temp(°F)
Inle
68
69
70
70
70
70
71
71
71
71
67
Outlet
68
69
70
70
70
70
69
69
69
69
69
Orifice
Pressure
Differ-
ential
("H20)
2.7
2.7
2.7
2.7
2.7
2.7
2.7
2.7
2.7
2.7
2.7
2.7
2.7
••liter
Box
Temp
CF)
Last
Imp.
Gas
Temp
(°F)
Sampling
Train
Static
Pressure
("Hg)
Clayton Environmental Consultants, Inc.
-------
C-192
SAMPLING TRAIN DATA
Company; Ford Motor Company
(Page 1 of 2)
Source Designation; Coke Battery A Scrubber Outlet
Date: 9/10-11/75 Filter Heater Setting:
Teat Number; Andersen Impact tor Sample-4 Probe Heater Setting:
RGK/GMS
A-245-24
Field Person:_
Filter Number:
Barometric Pressure ("Hg);Ava. 29.40
Stack Static Pressure ("H?0): -0.31
Stack Dimensions; 90" I.D.
Plume Appearance: --
Ambient Temperature(°F):
Record all Data Every Push
Nozzle Number; ,Dia.(in.)• 1/4
Pitot Tube Ho. 19.Corr.Factor; 0.854
Meter Box No. RAC-4, Corr. Factor; 1.009
Meter Isoklnetlc Factor; 1683
Assumed Moisture(I); —
Condensate Volume(ml);
Silica Gel Weight Gain(g) i__-.
Leak Rate 0.01 CFM at
15 »Hg
Trav-
erse
Point
No.
W-4
W-4
W-4
9/11
W-4
W-4
Time
Samp-
ling
(sec)
0
36
72
0
36
72
0
36
72
0
36
72
0
36
72
Clock
14:06
14:14
14:27
08:41
08:51
Velocity
Pressure
("H20)
0.65
0.65
0.65
0.65
0.65
0.65
0.65
0.65
0.65
0.65
0.65
0.6-5
0.65
0.65
0.65
AVERAGE (TOTAL)
Stack
Temp
(°F)
135
145
140
130
140
135
130
135
125
125
135
135
125
125
130
Dry Gas Meter
Volume
(ft3)
112.342
113.427
113.427
114.495
114.495
115.567
115.567
116.0
116.561
116.561
117.0
117.621
( )
Temp(°F)
Inlet
73
74
74
74
74
74
70
71
72
70
71
71
Outlet
69
69
69
69
69
69
70
71
72
70
71
71
Orifice
Pressure
Differ-
ential
("H20)
2.7
2.7
2.7
2.7
2.7
2.7
2.7
2.7
2.7
2.7
2.7
2.7
2.7
2.7
2.7
•liter
Box
Temp
(°F)
Last
Imp.
Gas
Cemp
CFJ
Sampling
Train
Static
Pressure
("Hg)
5.0
5.0
Clayton Environmental Consultants, Inc.
-------
C-193
SAMPLIHC TRAIN DATA
Ford Motor Company
Coapany:_
Source Designation; Coke Battery A Scrubber Outlet
Date: 9/11/75 Filter Heater Setting:
Test Number; Andersen Impactor Sample-4 Probe Heater Setting:
(Page 2 of 2)
CMS
A-245-24
Field Person:
Filter Number:
Barometric Pressure ("Hg); Avg. 29.40
Stack Static Pressure ("HgO): -0.31
90" I.D.
Stack Dimensions:
Plume Appearance;
Ambient Temperature(°F);
Record all Data Every Push
Noeile Number; -- ,Dia.(in.); 1/4
Pitot Tube No.19 »Corr.Factor; 0.854
Meter Box No.RAC-4 ,Corr.Factor; 1.009
Meter Isokinetic Factor; 1683
Assumed Moisture(Z): ._.
Condensate Volume (ml): _-
Silica Gel Weight Cain(g);
Leak Rate CFM at "Hg
Trav-
erse
Point
No.
tf-4
W-4
W-4
W-4
Time
Samp-
ling
(sec)
0
36
72
0
36
72
0
36
72
0
36
72
Clock
09:09
10:41
10:52
11:18
Velocity
Pressure
("H20)
0.65
0.65
0.65
0.65
0.65
0.65
0.65
0.65
0.65
0.65
0.65
0.65
AVERAGE (TOTAL)
Stack
Temp
(eF)
125
125
125
125
125
125
125
127
127
125
130
130
130
Dry Gas Meter
Volume
(ft3)
117.621
118.2
118.738
118.738
119.3
119.892
119.802
120.3
120.855
120.855
121.3
121.907
( 9.65 )
Temp(eF)
Inlet
70
71
71
71
72
73
71
72
72
72
72
73
72
Outlet
70
71
71
71
72
73
71
72
72
72
72
73
71
Orifice
Pressure
Differ-
ential
("H20)
2.7
2.7
2.7
2.7
2.7
2.7
2.7
2.7
2.7
2.7
2.7
2.7
2.7
filter
Box
Temp
CF)
Last
Imp.
Gas
Temp
CF)
Sampling
Train
Static
Pressure
("Hg)
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
Clayton Environmental Consultants, Inc.
-------
C-194
SAMPLING TRAIN DATA
Company; Ford Motor Company
Source Designation; Coke Battery A Scrubber Outlet
Date: 9/11/75 Filter Heater Setting:
Teat Humbert Andersen Impactor Sample-5 Probe Heater Setting:
GMS_
A-245-30
29.10
Field Person:
Filter Number;
Barometric Pressure ("Hg):_
Stack Static Pressure ("H?0); -0.31
Stack Dimensions; 90" I.D.
Plume Appearance: --
Ambient Temperature(°F):
Record all Data Every Push
Nocsle Number; -- ,Dia.(in.); 1/4
Pitot Tube No. 19,Corr.Factor; 0.854
Meter Box No.RAq-4iCorr.Factor; 1.009
Meter Zsokinetic Factor; 1683
Assumed Moisture(X): 1
Condensate Volume(ml): --
Silica Gel Weight Gain(g):
Leak Rate CFM at
200
"Hg
Trav-
erse
Point
No.
N-4
N-4
N-4
Time
Samp-
ling
(sec)
0
36
72
0
36
72
0
36
72
Clock
14:06
14:18
14:25
Velocity
Pressure
("H20)
0.67
0.67
0.67
0.67
0.67
0.67
0.67
0.67
0.67
AVERAGE (TOTAL)
Stack
Temp
<°F)
125
125
125
120
125
125
125
125
125
124
Dry Gas Meter
Volume
(ft3)
121.978
122.5
123.098
123.098
123.6
124.227
124.227
124.8
125.310
( 3.36 )
Temp('F)
Inlet
71
71
72
71
72
72
71
72
72
72
Outlet
71
71
72
71
72
72
71
72
72
72
Orifice
Pressure
Differ-
ential
("H20)
2.8
2.8
2.8
2.8
2.8
2.8
2.8
2.8
2.8
2.8
filter
Box
Temp
<°F)
Last
Imp.
Gas
Temp
(°F>
Sampling
Train
Static
Pressure
("Hg)
5.0
5.0
5.0
5.0
5.0
5.0
5.0
Clayton Environmental Consultants, Inc.
-------
C-195
SAMPLING TRAIN DATA
Company; Ford Motor Company
(Page 1 of 2)
Source Designation; Coke Battery A Scrubber Outlet
Date: 9/12/75 Filter Heater Setting:
Test Number; Andersen Impactor Sample-6 Probe Heater Setting:
RGK
A-245-27
Field Person:
Filter Number:
Barometric Pressure ("Hg); Avg. 29.49
Stack Static Pressure ("HgO); -Q.31
90" I.D.
Stack Dimensions:
Plume Appearance: •
Ambient Temperature("F):
Record all Data Every Push
Nossle Number; -- ,Dla.(In.); 1/4
Pltot Tube No. 19,Corr.Factor; 0.854
Meter Box No.RAC-4»Corr.Factor 1.009
Meter Isoklnetlc Factor; 1683
Assumed Moisture(I); 1
Condenaate Volume(ml);
Silica Gel Weight Gain(g):_-_
Leak Rate 0.01 CFM at
15 "Hg
Trav-
erse
Point
No.
N-4
N-4
N-4
N-4
N-4
Time
Samp-
ling
(sec)
0
36
72
0
36
72
0
36
72
0
36
72
0
36
72
Clock
09:56
10:09
10:32
12:25
12:38
Velocity
Pressure
<"H20)
0.67
0.67
0.67
0.67
0.67
0.67
0.67
0.67
0.67
0.67
0.67
0.67
0.67
0.67
0.67
AVERAGE (TOTAL)
Stack
Temp
<°F)
110
115
125
115
125
110
115
115
115
117
125
110
115
117
Dry Gas Meter
Volume
(ft3)
125.570
126.614
126.614
127.685
127.685
128.757
128.757
129.835
129.840
130.934
( )
Temp(°F)
Inlet
56
57
57
57
57
57
59
59
59
60
60
Outlet
69
69
69
69
69
69
69
69
69
70
70
Orifice
Pressure
Differ-
ential
<"H20)
2.8
2.8
2.8
2.8
2.8
2.8
2.8
2.8
2.8
2.8
2.8
2.8
2.8
2.8
2.8
filter
Box
Temp
CF)
Last
Imp.
Gas
Temp
CF)
Sampling
Train
Static
Pressure
("Hg)
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
Clayton Environmental Consultants, Inc.
-------
C-195
SAMPLING TRAIN DATA
Company; Ford Motor Company
(Page 2 of 2)
Source Designation; Coke Battery A Scrubber Outlet
9/15/75
Date:
Test Number; Andersen Impactor Sampled
Field Person; QMS
Filter Number:
Filter Heater Setting:
Probe Heater Setting:
A-245-27
Barometric Pressure ("Hg); Avg. 29.49
Stack Static Pressure ("H;0); -0.31
90" I.D.
Stack Dimensions:
Plume Appearance: --
Ambient Temperature(°F):
Record all Data Every push
NocBle Number; -- ,Dla.(ln.); 1/4
Pitot Tube No. 19,Corr.Factor; 0.854
Meter Box No.RAC-4,Corr.Factor: 1.009
Meter Isokinetic Factor: 1683
Assumed Moisture(I); 1
Condensate Volume(ml);
Silica Gel Weight Caln(g):_^_
Leak Rate
CFM at
"Hg
Trav-
erse
Point
No.
N-4
N-4
N-4
N-4
Time
Samp-
ling
(secj
0
36
72
0
36
72
0
36
72
0
36
72
Clock
08:25
09:55
10:02
10:10
Velocity
Pressure
("H20)
0.67
0.67
0.67
0.67
0.67
0.67
0.67
0.67
0.67
0.67
0.67
0.67
AVERAGE (TOTAL)
Stack
Temp
(°F)
120
120
125
120
120
125
120
120
125
120
120
125
119
Dry Gas Meter
Volume
(ft3)
130.934
131.3
131.998
131.998
132.7
133.229
133.229
133.7
134.264
134.264
134.7
135.111
( 9.62 )
Temp(°F)
Inlet
67
68
68
68
68
68
68
68
68
68
68
68
63
Outlet
68
68
68
68
68
68
68
68
68
68
68
68
69
Orifice
Pressure
Differ-
ential
("H20)
2.8
2.8
2.8
2.8
2.8
2.8
2.8
2.8
2.8
2.8
2.8
2.8
tllter
Box
Temp
CF)
Last
Imp.
Gas
Cemp
CF)
Sampling
Train
Static
Pressure
("Hg)
5.0
Clayton Environmental Consultants, Inc.
-------
C-197
SAMPLING TRAIN DATA
Company; Ford Motor Company
(Page 1 of 2)
Source Designation; Coke Battery A Scrubber Outlet
Date: 9/15/75
Teat Number; Andersen Impactor Sample-7
Field Person; QMS
Filter Number; A-253-10
Barometric Pressure ("Hg); 29.60
Filter Heater Setting:
Probe Heater Setting:
Stack Static Pressure ("H20); -0.31
Stack Dimensions; 90" I.D.
Plume Appearance: --
Ambient Temperature(°F):
Record all Data Every Push
Nozsle Number; -- ,Dia.(in.): 1/4
Pitot Tube No. 19,Corr.Factor; 0.854
Meter Box No.RAC-4'iCorr.Factor; 1.009
Meter Isokinetic Factor; 1683
Assumed Moisture(I); 1
Condensate Volume(ml); __
Silica Gel Weight Cain(g); --
Leak Rate
CFM at
"Hg
Trav-
erse
Point
No.
N-4
N-4
N-4
N-4
N-4
Time
Samp-
ling
(sec)
0
36
72
0
36
72
0
36
72
0
36
72
0
36
72
Clock
12:23
12:59
13:22
14:25
14:50
Velocity
Pressure
("H20)
0.67
0.67
0.67
0.67
0.67
0.67
0.67
0.67
0.67
0.67
0.67
0.67 •
0.67
0.67
0.67
AVERAGE (TOTAL)
Stack
Temp
(°P)
120
125
125
120
125
125
120
125
120
120
120
120
120
120
Dry Gas Meter
Volume
(ft3)
135.402
135.9
136.408
136.408
137.0
137.577
137.577
138.746
138.746
139.2
139.812
139.812
140.2
140.854
( )
Temp(°F)
Inlet
68
68
68
68
69
69
69
69
69
69
69
69
69
69
Outlet
68
68
68
68
69
69
69
69
69
69
69
69
69
69
Orifice
Pressure
Differ-
ential
<"H20)
2.8
2.8
2.8
2.8
2.8
2.8
2.8
2.8
2.8
2.8
2.8
2.8
2.8
2.8
filter
Box
Temp
<°F)
Last
Imp.
Gas
Temp
CFJ
Sampling
Train
Static
Pressure
("Hg)
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
Clayton Environmental Consultants, Inc.
-------
C-198
SAMPLING TRAIN DATA
(Page 2 of 2)
Company; Ford Motor Company
Source Designation: Coke Battery A Scrubber Outlet
Date: 9/15-16/75 Filter Heater Setting:
Teat Number: Andersen Inpactor Sample-? probe Heater Setting:
CMS
Field Person:
Filter Number: A-253-10
Barometric Pressure ("Hg)t 29.60
Stack Static Pressure ("H?0); -Q.31
Stack Dimensions; 90" t.D.
Plume Appearance: --
Ambient Temperature (°F):
Record all Data Every Push
Nozzle Number; -- ,Dia.(in.); 1/4
Pitot Tube No. 19,Corr.Factor; 0.854
Meter Box No.RAC-4'.Corr.Factor; 1.009
Meter Isokinetic Factor; 1683
Assumed Moisture(I); 1
Condensate Volume(ml);
Silica Gel Weight Catn(g);
Leak Rate CFM at "Hg
Trav-
erse
Point
No.
N-4
N-4
N-4
N-4
Time
Samp-
ling
(sec)
0
36
72
0
36
72
0
36
72
0
36
72
Clock
14:56
08:34
08:48
08:55
(Telocity
Pressure
("H20)
0.67
0.67
0.67
0.67
0.67
0.67
0.67
0.67
0.67
0.67
0.67
0,67
•
AVERAGE (TOTAL)
Stack
Temp
(«F)
120
125
130
120
122
125
120
120
122
120
122
125
122
Dry Gas Meter
Volume
(£t3)
140.854
141.1
141.380
141.380
141.9
142.413
142.413
142.9
143.422
143.422
143.9
144.431
(9.11 )
Temp(°F)
Inlet
69
69
69
69
61
62
61
61
61
61
61
61
66
Outlet
69
69
69
70
70
70
70
70
70
70
70
70
69
Orifice
Pressure
Differ.
ential
("H20)
2.8
2.8
2.8
2.8
2.8
2.8
2.8
2.8
2.8
2.8
2.8
2.8
2.8
filter
Box
Temp
CF>
Last
Imp.
Gas
Temp
TF5
Sampling
Train
Static
Pressure
("Hg)
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
Clayton Environmental Consultants, Inc.
-------
TOTAL HYDROCARBON DATA SHEET
Project; Ford Motor Company
Field Person: RJP
Sampling
Station
Coke
Battery A
Scrubber
Inlet
Coke
Battery A
Scrubber
Inlet
Test
Number
Preliminary
1
Preliminary
2
Initial
Final
Initial
Final
1975
Date
1-10
1-10
Time
10:12
35 sec.
10:35
30 sec.
Sampling
Rate
(1pm)
4.5
4.5
Final
Vo lume
(liters)
2.62
20 c
m£j
Cl
I
VO
VO
Clayton Environmental Consultants, Inc.
-------
TOTAL HYDROCARBON DATA SHEET
Project; Ford Motor Company
Field Person:
GEH
Sampling
Station
Coke
Battery A
Scrubber
Inlet
Coke
Battery A
Scrubber
Inlet
Coke
Battery A
Scrubber
Inlet
Coke
Battery A
Scrubber
Inlet
Coke
Battery A
Scrubber
Inlet
Coke
Battery A
Scrubber
Inlet
Coke
Battery A
Scrubber
Inlet
Coke
Battery A
Scrubber
Inlet
Test
Number
Preliminary
4
Preliminary
5
Preliminary
6
Preliminary
7
Preliminary
8
Preliminary
9
Preliminary
10
Prel Indnary
11
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Initial
Final
.laititl.
Final
1975
Date
2-4
2-4
2-4
2-4
2-6
2-6
2-6
_l-4_..
Time
15:09
42 sec.
15:22
42 sec.
16:30
42 sec.
16:30
42 sec.
11:46
45 sec.
11:46
45 sec.
12:34
44 sec.
__JAi3A.
44 sec
Sampling
Rate
(1pm)
1.004
1.004
1.055
1.004
1.004
1.055
1.004
_1_._0_55____
Final
Vo lume
(liters)
0. 703
. 7O3
0-700
• 73o
07 no.
• 7 UJ
.753
. 791
0.736
0.774
10
o
o
Clayton Environmental Consultants, Inc.
-------
TOTAL HYDROCARBON DATA SHEET
Project; Ford Motor Company
Field Person:
GEH
Sampling
Station
Coke
Battery A
Scrubber
Tnle.t
Coke
Battery A
Scrubber
Inlet
Test
Number
Preliminary
12
Preliminary
13
Initial
Final
Initial
Final
1975
Date
2-6
2-6
Time
12:45
39 sec.
12:45
39 sec.
Sampling
Rate
(ipn)
1.004
1.055
Final
Vo lume
(liters)
0.653
.686
to
o
Clayton Environmental Consultants, Inc.
-------
C-202
SAMPLING '.T1AIN DATA
Company; Ford Motor Company
Source Designation! Coke Battery A Scrubber Inlet
Date: 2-6-75
Teat Number; Preliminary
Field Person; ROM
Filter Number:
Barometric Pressure ("Hg); 29.28
Stack Static Pressure ("H20): -3.0
Stack Dimensions; 66" I.D.
Plume Appearance:
Ambient Temperature(°F):
Record all Data Every
Filter Heater Setting:
Probe Heater Settlng:__
Nozzle Number: ,Dia,
Pitot Tube No. ,Corr.Factor:
Meter Box No .MAC-2 .Corr.FactoRQ .994
Meter Isokinetic Factor:
Assumed Moisture (X) :
Condensate Volume(ml): -3
Minutes
Silica Gel Weight Gatn(g); 8
Leak Rate
CFM at
"Hg
Trav-
erse
Point
No.
CL
CL
CL
CL
CL
Time
Samp-
ling
(rain)
Clock
11:25
11:40
11:55
12:10
12:25
Velocity
Pressure
("HzO)
i
AVERAGE (TOTAL)
Stack
Temp
CF)
35
34
35
31
34
Dry Gas Meter
Volume
(ft3)
664.345
677.5
690.6
703.6
716.710
( 52.051)
Temp(°F)
Inlet
49
46
46
46
47
Outle t
42
40
38
37
39
Orifice
Pressure
Differ-
ential
("H20)
2.5
2.5
2.5
2.5
2.5
'liter
Box
Temp
CF)
__
Last
Imp.
Gas
Temp
CF)
_
Sampling
Train
Static
Pressure
("HR)
5.5
5.5
5.5
5.5
5.5
Clayton Environmental Consultants, Inc.
-------
C-203
SAMPLING TRAIN DATA
Company; Ford Motor Company
Source Designation; Coke Battery A Scrubber Inlet
2-6-75
Date:
Test Number; Preliminary HjSO^-2
Field Person; ROM
Filter Number:
Barometric Pressure ("Hg); 29.28
Stack Static Pressure ("HgO); -3.0
Stack Dimensions: 66" I.D.
Plume Appearance:
Filter Heater Setting:
Probe Heater Setting:
Nozzle Number: ,Dia.(in.):
Pitot Tube No. ,Corr.Factor:
Meter Box No .MAC-2 t Corr.FactonQ.994
Meter Isokinetic Factor:
Assumed Moisture (X):
Condensate Volume(ml); -1
Ambient Temperature(°F):
Record all Data Every
Minutes
Silica Gel Weight Gatn(g); 8
Leak Rate CFM at
"Hg
Trav-
erse
Point
No.
CL
CL
CL
CL
CL
Time
Samp-
ling
(min)
Clock
12:35
12:50
13:05
13:20
13:35
Velocity
Pressure
<"H20)
AVERAGE (TOTAL)
Stack
Temp
<°F)
240
35
32
500
202
Dry Gas Meter
Volume
(ft3)
716.710
729.7
742.7
755.8
769.080
( 52.056)
Temp(»F)
Inlet
42
44
45
46
44
Outlet
35
35
35
35
35
Orifice
pressure
Differ-
ential
("H20)
2.5
2.5
2.5
2.5
2.5
Filter
Box
Temp
CF)
Last
Imp.
Gas
Femp
CF)
Sampling
Train
Static
Pressure
("Hg)
5.5
6.0
6.0
6.0
5.9
Clayton Environmental Consultants, Inc.
-------
C-204
SAMPLING TRAIN DATA
Company:_
Source Designation:^
Date: 2-6-75 "
Ford Motor Company
Coke Battery A Scrubber Inlet
Preliminary H.SO^-3
Teat Number:
Field Person': ROM
Filter Number:
Barometric Pressure ("Hg); 29.28
Stack Static Pressure ("HgO); -3.0
Stack Dimensions: 66" I.D.
Plume Appearance:
Filter Heater Setting:
probe Heater Setting:
Nozzle Number: ,Dia.(in.):_
Pitot Tube No. ,Corr.Factor:
Meter Box No .MAC-2 iCorr.FactonQ.994
Meter Isokinetic Factor:
Assumed Moisture(X) :
Condensate Volume(ml); -6
Ambient Temperature(*F):
Record all Data Every
Minutes
Silica Gel Weight Cain(g):_8_
Leak Rate
CFM at
"Hg
Trav-
erse
Point
No.
CL
CL
CL
CL
CL
Time
Samp-
ling
(min)
Clock
14:00
14:15
14:30
14:45
15:00
Velocity
Pressure
("H20)
AVERAGE (TOTAL)
Stack
Temp
(°F)
44
45
30
30
37
Dry Gas Meter
Volume
(ft3)
769.080
783.6
797.1
811.3
825.952
( 56.531)
Tcmp(°F)
Inlet
42
44
45
48
45
Outle t
35
34
35
36
35
Orifice
Pressure
Differ-
ential
("H20)
3.0
3.0
3.0
3.0
3.0
filter
Box
Temp
CF)
— .
Last
Imp.
Gas
Temp
(°F)
—
Sampling
Train
Static
pressure
<"H«)
6.5
7.5
7.5
10.0
i
7.9
Clayton Environmental Consultants, Inc.
-------
CRITICAL ORIFICE SAMPLING DATA
Ford Motor Company
Company:
Soured Designation; Coke Battery A Scrubber Inle-t
Field Person: E.G. Keller
Date
1975
4-9
4-9
4-10
Material
Sampled and
Test Number
Preliminary
CN-1
Preliminary
CN-2
Preliminary
CN-3
Orifice
Number
10
10
2
Sampling
Period
Start
13:21:30
13:32:45
13:45:50
13:53:45
14:13:00
14:20:15
14:29:45
14:50:00
15:08:18
13:50:35
14:07:00
14:14-30
14:29:05
14:40:00
Stop
13:23:00
13:34:15
13:47:35
13:54:45
14:17:45
14:23:00
14:34:35
15:00:53
15:10:52
13:52:4C
14:18}00
14:17:00
14:36:45
14:49:00
At
(min)
1.50
1.50
1.75
3.00
4.75
2.75
4.83
10.88
2.57
2.08
11.00
2.50
7.67
9.00
Barometric
Pressure
<"Hg>
29.59
29.59
29.59
29.59
29.59
29.59
29.. 59
29.59
• 29.59
29.61
29.61
29.61
29.61
29.61
Inlet
Vacuum
<"H20>
22.0
22.0
22.0
22.0
22.0
22.0
22.0
22.0.
.22.0
11.3
10.8
17.1
16.1
16.7
Outlet
Vacuum
("Hg>
23.0
23.0
23.0
23.0
23.0
23.0
23.0
23.0
23.0
22.7
22.7
22.7
22.7
22.7
Inlet
Temp
<-P>
42
42
42
42
42
42
42
42 •
42
48
48
49
46
46
Sampled
Volume
(liter*)
1.53
1.53
1.79
3.07
4.85
2.81
4.94
11.12
2.63
2.19
11.62
2.60
8.01
9.38
ro
o
Sample volume - Q8tdx («i*0
•Clayton Environmental Consultants, Inc.
-------
APPENDIX D
CALIBRATIONS
-------
D-l
_.
r/er
-------
-------
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ipipii ]••••
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8 llSSiii
-------
D-4
-------
D-5
-------
D-6
-------
D-7
z «
i I
5 e
- •
•"3""i""3
: ' '
' - ' . - I I. •:••... !• ••»•••»••• fpBII •••••
••*• •••••••••'••'•••••••••^•••••••^•••••••••
-------
D-?
-------
D-9
-------
D-?.0
-------
Date
SJS"
Client
TO
Btrometri Pressure Pb ("Hg) 2. 7.
Meter Box Number
Ca'"brator g. ^./f. Gas Meter Number
Orifice
Manometer
Setting, Am
(In. H20)
Pd
Gas Volume
Wet Test
Meter
v«
(ft*)
Gas Volume
Dry Gas
Meter
Temperature
wet
Test
Meter
Dry Gas Meter
Inlet
tdl
Outlet
Average
td
Vacuum
Wet Test
Meter
PW
(in. H20)
Time
e
(mln)
Stop
0.5
77
18
0%
Start
OQ
77
go
-0V
Average
(5)
r?
13
O./3/il
Stop
1.0
77'
Start
77'
74'
18
Average
(5)
11
0.977
o
I
Stop
2.0
0 f
*'
18
/o
Start
o o
74
IB
\verage
(10)
0./3030
Stop
3.0
74
Start
92
74'
/o
Average
£1.7-7
fi*.
CiEJ)
/0.4V
Stop
4.0
**'
80
.12.
Start
74
Average
(10)
so
-
15
!S t o
5.0
76'
30
Start
.00
77
R.Q.
Average
(10)
11
0.97-5
OM1I+
Pw Pj
T376- *d
„ (td + 460)
vw
"-5"V^
AVERAGE
Factor in isokinatle equation •
-------
Date rf/?SZ'£ 2.J. / ^ 7£" Client /-^5>C/9 /Tfar^n. £.c . N-CtLtA^ Meter Box Number ninths
Rarometr Pressure
Stop
Start
Average
Stop
Start
\verage
Stop
Start
\verage
Stop
Start
\vcrage
Stop
Start
\verage
"Stop"
Start
\verage
Pw - Pb
vw
y m W
Orifice
Manometer
Setting, Am
(in. H20)
0.5
- •-
^9 38
1.0
33 41
2.0
34.4^
3.0
z-q.'Sb
4.0
--•7.fc3
5.0
3-tf-~ll
Pb ("Hg) 2.V. 34
Gas Volume
Wet Test
Meter
0 6/ff. c,°
06/&. 00-
(5-) ,f.or.
0 £2.0.00
&
^ -Ol2
723.^70
7/
Outlet
/^"
7^'
7*'
72*
7*'
72"
Average
td
rl^b
14-
•
'/ 4-
7^
7u,
1(t>
V 1 9
13.6 B D T2
Pw (td + 460)
Factor in isoklnetic equati
,on- 27
Vacuum
Wet Test
Meter
(in. *H2°>
.Ot
^9.33
. /f
•=>
• ft
.^t 3i
./J.
3.*? 3i
./2.
0^.3^
Time
6
On In)
12. 70
12.71
/042.
V.'ff
X 21
AVERAGE
7
o.«i
o«*3
o.™
OW
Off*
^•977
0.3
.1^;
.«w
.«»3;
.0^
W2W*
"0
I-1
Is)
.40 . 27.40 . // i o
r ( ?
-------
Date
("»«-<
Client
Barometi-c pressure Pb ("Hg)
C Ibrator
Meter Box Number
Gas Meter Number
M(
Start
Stop
Average
Start
Stop
Average
Start
Stop
Average
Start
Stop
Average
Start
Stop
Average
Start
Stop
Average
Pw - Pb
Orifice
Manometer
Setting, Am
(in. H20)
o:s
1.0
2.0
3.0
•
4.0 •
5.0
' 13% l
Gas Volume
Wet Test
Meter
y
•.iit.cj
~* \l\ cL'
(5)
"1 • •* -\ • <*
1 I •» .-x w **
~* 1 "* ""* "*. N
(5) " .'. ;
•M-N<.CJ
- • '? 0- •
(10)
->jJ-< .. J
~i s"<1. ^.^
(10)
7 1 , C . .: v
T i 70 c..'
(10)
"7 \ ? i. 0 0
Ti °U... co
(10)
Gas Volume
Dry Gas
Meter
f£
^b^l ^^^
M "4 "7i> *
M. '«. <^
4-75- .7^
•Aid ~>~r<-\
^ fL . ~
^ M 1 '< ( 0
^. ^ '^^ j
• : ^ 1 -
•^c n -i i v.
r>" \ :» C - ,
10 ..i
T . 4 u •». <
^7^-| ,,..-
•• C • *•
sSc S5M
^•lu 74',
10 1*1
Temperature
wet
Test
Meter
ow
7^
7H
-14
T^
71>
7 >
7 "\
7^
T4
7 V>
-t \
"TX
Dry Gas Meter
Inlet
tdi
70
Tl
7 '-,
-..
nc-
>'4
^?
x^
:<-c
^^
ys"
V.-J I
Outlet
tV
"7^
7C
7 1
7^
7G
-•0
7^
T/
IV
Sf 1.
•^3.
Average
td
CF)
w I _
A. in v V I *W
*d - Pb + TJ
[77
~ -5
y TWA.
Vacuum
Wet Test
Meter
(in. WH2O)
. e
. 0*
. cy
. cv
. o '<
L? 1C
C 1 L,
O i :.
1- 1 1
C- i i
O » I
Time
6
(mln)
W7
>M,o
i,W
.*s-
«.H
AVBRAGB
7
o.m
O..SH
a.«^
o.'tu
0.=,^!
O-^0! 1
o.nJ
-
17*3
,171
183- »/
.m
.810
ii$«
•Wl.
V
o
, I
Vy Pv (td + 460)
Vd Pd
Taetor In l«okin«tic equation •
27.40 . 27.40
1 7
-------
Date
Client
Me tier Box Number
Barometric ^ressure Pb ("Hg)
CaJ'brator £.£".//. Gas Meter Number /£/&£
>>
Orifice
Manometer
Setting, An
(in. H20)
Gas Volume
Wet Test
Meter
Gas Volume
Dry Gas
. Meter
Temperature
Wet
Test
Meter
tw
Dry Gas Meter
Inlet
tdi
CP>
Outlet
Average
td
Vacuum
Wet Test
Meter
PW
(in. H20)
Time
e
(min)
Km
Stop
0.5
13.
101
Start
so.,
Average
(5)
10']
Stop
1.0
. 2
Start
0*74.00
3 /3 '
73*
78'
Average
. J?
-------
Client
Barometric 'rcssure Pb ("Hg)
CaJ •* brator
Mci:cr Box Number
Gas Meter Number
Stop
Start
Average
Stop
Start
Average
Stop
Start
Average
Stop
Start
Vvcrage
Stop
Start
Werage
'Stop
Start
Average
Pw - Pb
Orifice
Manometer
Setting, Am
(in. H20)
0.5
- / -^ v
1.0
^ •-.- :-
2.0
.•••'•
3.0
•X | )
4.0
•-
5.0
'
' TTT '
Gas Volume
Wet Test
Meter
' "
(5) /)" M
•
S * *
(5) A- o->
- •
,
(10) .'.
,
iio) •:•• ^
•
(10)y;,.0
(10) .' • •«."
>. • p. .4. /
Gas Volume
Dry Gas
, Meter
' ' / / • •
^ «»"
-.- 30 /
/ < /
.?
-; - -7 ^
. j • - -
~
/.; .C'/'',
• /• ' .
.
§ ,~ , • ' i
•
; •
' . ' '--
\
m R
(77
Temperature
~WeTf~~
Test
Meter
lv
•
f-'f
r
.-9
: '/
»". *
i /
_.- •
-
' • ^
Dry Gas Meter
Inlet
tdi
\
-'-
i /
•
-
10?
/ .;
.
• *i-
\^
' ^1
Outlet
V0
• j .
."
.
'
.,
1 7 -^
• •
•' ?
/
* •
r ./ PW
* 9 U Tw Am
Average
td
CF)
• ..
> c>
.-,.-
7 7
'fCr
:/..-
'.••)
' 7
: s
/" 3
/ -
.' ; . '.
/<•- 3
/O.-5
/,=:i
/. •
•. :,
v -
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D-22
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D-24
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D-25
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D-26
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JALIBRATED 1
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D-27
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0'.2 '"0.3 OU 0.5'
1.0
-------
D-28
PITOT TUBE CALIBRATION
PITOT TUBE TYPE S PITOT TUBE NO. /8
STANDARD PITOT TUBE NO, /6Q-/&
CALIBRATED BY:
DATE:
CLIENT:
M/H/75
po$t'
A- <
0
-pi> FO
B -S
P.td
Ptest
Ptest
Ap
.td
AP
test
Ptes
0.02
0.04
0.06
0.08
0,10
0.12
'w.16
0.20
0.30
0.50
0.70
0.80
o.£Lii
0.
Q-V3H
O.iZtt
o.lH
o.Jll
0.
0.
0.
0.
.Iil
llf
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jii
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0.221 ||o,
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0
o
0
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o
0
0 _
o.
0
0
00.90
0.01
-------
D-29
C -0
K
.99A/
,
>td
V^
PITOT TUBE CALIBRATION
PITOT TUBE TYPE S PITOT TUBE NO. l#
STANDARD PITOT TUBE NO. /6Q-/&.
CALIBRATED BY:
DATE:
CLIENT:
POS~fc~
A
0
P8td
Ptest
'Pteet
Ap
.td
Ptea
0.02
0.04
0.06
0.08
0,10
0.12
0.16
0.20
0.30
0.50
0.70
0.80
.02^
.OSL
QSSL.
ia
.»13
o.Q&k
o.M.
o.okl
*.o&
o.lli
>.J£Z
..2£L
.Ml
.143
.121
.318'
.21!
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
10.
V . .
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Jo..
jo.
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o._
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0 —
o._
o._
o._
o._
o.»_
0.—
0 —
o._
0.01
("H20>
-------
D-30
teat:
CALIBRATED BY: O -*• ^ Af
ft.J, C-1V.4-4O
DATE:
FITOT TUBE CALIBRATION
PITOT TUBE TYPE S PITOT TUBE NO. _ j\^ .
STANDARD PITOT TUBE N0» /60~/<$
CLIENT:
pott
C.fy
p.td
^
test
Ptest
APtest
Ptes
0.02
0.04
0.06
0.08
0.10
0.12
0.20
0.30
0.50
0.70
0.80
.033-
.Qli
0.
.4M
o.ii
n
. ill
.^iL
0.
0.
0.
0.
o.iiO.
o.i_Q
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o.lll.
0
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0
0
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o.lSi
>.!_____
em
o.
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0.01
-------
D-31
i.- -*.
Cc • u
PITOT TUBE CALIBRATION
PITOT TUBE TYPE S PITOT TUBE NO. l9
STANDARD PITOT TUBE NO. /60-/S
CALIBRATED BY: p -* r
IS . i J . 1-? r.»
DATE: ^ / J/->^
CLIENT:
fie- >*t -
A \t
PRC. f <-•,.;
B *,l« •*"
P.td
Pte«t
p.td
Pte«t
Ap
.td
APt
e.t
Ptei
0.02
0.04
0.06
0.08
0.10
0.12
0.16
0.20
0.30
0.50
0.70
0.80
o.
o.OV
O.SI51
o.
IL__3
0.
Sifif
o.
Cl'*
o.M
o.lli
0
o
0
0
0.
0.
0.
0.
0.
0.
0.
Jik
223
o.lfli
0.-121
0. J£_J
0.112
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o.l5_?
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0.
0.
0.
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0.
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0.
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o.lci:
0.
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0.89
! 0.88
> t
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=H!=fc
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0
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s
1
^
i
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> 1
1
1
— — _" • •
.0 1.
-------
D-32
PITOT TUBE CALIBRATION
PITOT TUBE TYPE S PITOT TUBE NO.
STANDARD PITOT TUBE NO. /6Q-/S
CALIBRATED BY: O -j-
DATB:
CLIENT:
poit- Cv-ft^.^e C.'-t^ Steel
EPA "ksk 14,
ft ©
P.td
Ap
te»t
Ptest
^p
.td
Pte«t
APte.t
'Ptesi.
0.02
0.04
0.06
0.08
0.10
0.12
'..16
0.20
0.30
0.50
0.70
0.80
o.itl
n
05^
.Hlli-
IO&
0.
0..
O.Jil
O.JM.
0
o.
0
0
0
0.,
0.
0.
0.
0.
0.
O.-Lil
0.121
o.
0. __
0
0
0
0.
0. .
0.
0.
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O.oi
.02 : .03 .04c« .06" "O'.l
0.2 0.3 0.4 0.5* ; * * 1.0
("H20)
-------
CRITICAL ORIFIC^'CALIBRATION
Client;
Dace:
Barometric Pressure;
Calibrator:
Orifice
Number
10
Z
Stop
Start
Average
Stop
Start
Average
Stop
Start
Average
Stop
Start
Average
Test Meter
Gas Volume
Tw
-7 4-
14-
H4-
^4.
14-
14-
Test Meter
Vacuum
("H20)
*v
o.l
o.|
c>-\ /
o.|
o.\
d.\
Orifice
Temp
(°F)
To
1Z.
ni
-TZ.
TZ.
•72^
-12.
Orifice
Vacuum
<"H20>
PO
o-S>
o.S
o -e>
»^
o.g
0-8
o.©
Orifice
Flowrate
(1pm)
Qcal
/. o(*&
i.o'H*
_ 28.32 Vtf(Pb - Ptf)(T0 + 460)
V
*'
o
i
Ul
- P0)(T
460)
Claytoa Environmental Consultants, Inc.
-------
Client: £
Date: . i C,?r/
O. •bS'il
Time
(min)
e
>o
0
10
0
Test Meter
Temp
<°F>
Tw
T?
7?
92.
7?
-71
72.
Test Meter
Vacuum
("H20)
?w
. oos-
.00 f
o.of>^
iOO$
^oos
o.o<5r
Orifice
Temp
(°P)
TO
~>2
-73
-73
7?.
T3,
-73
Orifice
Vacuum
("H20)
PO
0.-2.
0. -Z-
<9.^
-------
Client :m
Date:
CRITICAL ORIFI
~ t / P^>-ff
CALIBRATION
__ Barometric
Calibrator:
Pressure;
2 "Hg
Orifice
Number
Stop
Start
Average
Stop
Start
Average
Stop
Test Meter
Gas Volume
1*2*13
Time
(min)
0
Test Meter
Temp
C°F)
Test Meter
Vacuum
<"H20)
d. (
. /
0. 1
Orifice
Temp
CP>
m 28.32 Vw(Pb - PV)(T0 + 460)
Q"1 " 8
-------
CRITICAL ORIFIC
Client;
Date:
CALIBRATION
___ Barometric Pressure:
Calibrator: I? f^t
"Hg
Orifice
Number
J
Stop
Start
Average
Stop
Start
Average
Stop
Start
Average
Stop
Start
Average
Test Meter
Gas Volume
(ft3)
vw
75.4,177
T^z-r?
o.r7/^4'
.
Time
(min)
9
2.0
0
Test Meter
Temp
(°P)
Tw
&
-------
APPENDIX E
SAMPLE CALCULATIONS
-------
E-l
Nomenclature
2
A = Stack area, inches
Cf = Front half (probe & filter) particulate concentration,
gr/DSCF
C = Fitot tube correction factor, dimensionless
P
Ct = Total particulate concentration, gr/DSCF
Dn = Sampling nozzle diameter, inches
ERf = Emission rate of front half particulate, Ib/hr
ERt = Emission rate of total particulate, Ib/hr
FRC = Flowrate at calibration conditions, 1pm
GS = Specific gravity of stack gases relative to dry air,
dimensionless
Mj = Mole fraction of dry gas, g/g-mole
MW = Molecular weight of wet stack gas
MW
-------
E-2
SW = Total sample weight, mg
Tc = Average temperature at calibration conditions, °F
T = Average meter temperature, °F
T ° Stack temperature, °F
Tt = Net time of test, minutes
4
V = Volume of dry gas at meter conditions, ftj
V_ = Volume of dry gas at standard conditions, DSCF
std
V • Stack gas velocity at stack conditions, fpm
s
Vw = Total condensate collected in sampling train, ml
V = Volume of water vapor at standard conditions, SCF
gas
7 = Dry gas meter correction factor, dimensionless
£P = Velocity pressure, inches water
%M = Percent moisture, dimensionless
-------
E-3
Particulate Emissions
The dry volume of sampled gas corrected to standard condi-
tions of 20°C and 760 mm Hg (29.92 in. Hg) is calculated as
follows:
v = 17.65 * Vm * 7 * fpb + Pm }
mstd ^ 13.6/
Tm + 460
For the first particulate test taken at the Scrubber Inlet of
the Rouge Plant Coke Battery A,
17.65(17.348) (0.974) (29.78 + i^l)
86 + 460
= 16.34
The dry stack gas flowrate corrected to standard conditions is
calculated using the following set of equations sequentially.
Vw = 0.0471 * Vw
gas
100 * V
%M = Wgas
V_ + V
m w
std gas
-------
E-4
M _ 100 - %M
Md ' Too—
MWd
(%C02 * 44/100) + (%02 * 32/100) + K%CO + %N2) * 28/10oJ
MW = (MWd * Md) + 18(1 - M.)
P - P. + P fc
6 b st
Vg = 5120.8 * Cp * -APS * (Tg + 460) *l P * MW
*Al Ps *
0.1225 * Vg * Ag * Md * Pg
(Ts + 460)
The calculations for determining the flowrate for the first
particulate test at the Scrubber Inlet follow. Since this is
not a combustion source, the molecular weight of the wet stack
gas, MW, was assumed to be that of air, 28.95. The diameter of
the sampling station is 66 inches.
Wgas = 0.0471(12)
0.56
7M - 100(0.56)
' 16.3 + 0.56
= 3.3
-------
E-5
M. = 100 - 3.3
d Tffo
• 0.967
MW • 28.95
Pa - 29.78 + (-0.37)
D
- 29.41
V8 - 5120.8(0338) (29.18)
= 4291
/ 1
y29.41(28.
95)
0.1225 (4291) (3421) (0.967) (29. 41)
(158 + 460)
- 82,800
The equation employed to determine percent of isokinetic
variation is:
1032 * (T + 460) * V
std
V8 * Tt * P8 * Md * (Dn)2
For the first particulate test at the Scrubber Inlet,
1032(158 + 460)(16.3)
%I = 4291 (24) (29.41)(0.967)(0.189)2
= 99.4
-------
E-6
To determine the concentration of particulate matter in
grains per dry standard cubic foot (gr/DSCF), one of the following
equations is used:
C. = 0.01543 * SWf
std
and
SW.
0.01543 * t
vm
std
Front half particulate concentrations are obtained by summing
the weight of particulate matter collected on the filter and all
portions of the train preceding it. Total particulate concentra-
tion includes, in addition, any particulate matter collected in
the impingers.
The first particulate test at the Scrubber Inlet yielded the
following concentrations of filterable and total particulate:
Cf = 0.01543 * 18A3'7
•t ID . J
- 1.783
C,. = 0.01543 *
C
1.852
-------
E-7
The emission rate of particulate matter can be calculated
from the filterable or total particulate concentration using one
of the following equations:
ERf = 0.00857 * Cf * Qs
and
ERt - 0.00857 * Ct * Qs
To avoid rounding errors'It Is preferable to carry out the calcu-
lation of concentration and emission rate In one operation.
The emission rates of front half and total particulate
matter for the first particulate test at the Scrubber Inlet
are calculated as follows:
ER£ - 0.00857(1.783)(82,800)
= 1265
ERt - 0.00857(1.852)(82,800)
• 1314
Emission rates may also be calculated In pounds of particulate
matter per ton of feed, where the feed rate used is either on a
wet or a dry basis. The feed rate is determined by converting the
i
total pounds of feed charged during each test to tons and dividing
by the total number of minutes for which sampling occurred. Then
Ibs/ton of feed = (lbs/hr)/(tons/hr).
-------
E-8
For the first particulate test at the Scrubber inlet, 1051
tons of feed were charged per hour. Since the filterable particu
late emission rate was 1265 Ibs/hr,
Ibs/ton of feed - 1265/1051
= 1.20
For total particulate emissions,
Ibs/ton of feed - 1314/1051
= 1.25
Gaseous Emissions
volumes, concentrations, and emission rates for all
contaminants collected using a dry gas meter are calculated in a
manner similar to that used for particulate matter. If the
concentration is desired in parts per million (ppm), the following
equation is used:
ppm = 24040 * SWt _
28.32 * V *~MW
To correct this concentration to an emission rate, the following
equations are used:
-------
E-9
Ib/hr = (0.1559 * 10~6) * ppm * Qfi * MW
gas
and
Ib/ton of feed = (Ib/hr) (tons/hr)
Again, to avoid errors it is preferable to calculate the emission
rate before rounding off the concentration value.
For the first sulfur dioxide sample taken at the inlet
to the scrubber on the Rouge Plant Coke Battery A,
24040(3.11)
PPm = 28.32(3.74) (64.06)
- 11.02
Ib/hr = (0.1559 * 10~6)(11.02)(80,300)(64.06 )
= 8.84
Ib/ton
of feed
8.84/1053
0.0084
At the Rouge Plant Coke Battery A several samples were
also taken using a limiting orifice. In order to calculate
the sample volume, corrected to standard conditions, when a
limiting orifice is used and silica gel is used in the sampling
train, the following equation is applied:
-------
E-10
460
= °'6231 * T *
mstd * c Tc + 46° IT- + 460
For the first benzene samples taken at the Scrubber
Inlet,
= 0.0431
Concentrations and emission rates for samples taken with
a limiting orifice are calculated in the same manner as shown
previously.
Particle Size Distribution Calculations
All samples collected for particle size distribution at
the Rouge Plant Coke Battery A utilized the Andersen Stack
Sampler. These particulate samples were collected and sized
aerodynamically at isokinetic conditions. A sample volume was
calculated similar to that of a particulate test and expressed
in cubic feet at 70°F and 29.92 inches of mercury. The sample
volume was then divided by the total number of minutes the test
was run, yielding a flowrate through the Andersen sampler
expressed in cubic feet per minute (cfm) for each test.
Figure E-l is a plot of V versus flowrate (cubic feet per
P
minute) through the Andersen Sampler at 70°F. D' is the effective
P
aerodynamic diameter of a spherical, unit density particle.
-------
E-ll
Figure E-2 shows the correction factor for determining the
physical diameter of spherical particles having other than unit
density. (The assumption is made that the particles are spherical
in shape.) The effective aerodynamic diameter as determined
from Figure E-l is multiplied by the correction factor from Figure
E-2 to determine the physical diameter for that density.
Figure E-3 shows the correction factor for determining the
effective aerodynamic particle diameter for elevated temperatures.
The effective aerodynamic diameter as determined from Figure E-l
is multiplied by the correction factor from Figure E-3 to deter-
mine the diameter for that temperature.
The quantities collected on each stage and on the final
filter are each expressed as a percentage of the total amount
recovered. A cumulative percentage smaller than D (characteris-
P
tic particle diameter) is then calculated for each stage.
The particle size samples taken at the Rouge Plant Scrubber
Inlet were taken during three different time periods simultaneous
with one sample taken at the Scrubber Outlet. For the inlet
samples the characteristic particle diameters were averaged over
the three tests and the weights on each stage were summed.
For the first particle size sample taken at the Scrubber Out-
let, the flowrate at 70°F and 29.92 in. Hg was 0.446 cfm and the
stack temperature was 123°F. Particle density for these samples
was assumed to be 1.14 gm/cc.
-------
E-12
From Figure E-l, D ' was obtained for each stage. From
Figure E-2 the correction factor for a particle density of 1.14
gm/cc was found to be 0.95. From Figure E-3 the correction fac-
tor for a stack temperature of 123°F was found to be 1.040. The
characteristic diameter for each stage was determined by the
following equation:
D = D' (0.95)(1.040).
P p
The characteristic particle diameter for the various stages of
this test are shown below:
D
i
P
Stage 0
Stage 1
Stage 2
Stage 3
Stage 4
Stage 5
Stage 6
Stage 7
14.
9.
6.
4.
2.
1.
0.
0.
6
1
1
2
6
4
82
58
D
P
14.4
9.0
6.0
4.1
2.6
1.4
0.81
0.57
The results of these calculations were then combined with the
quantities determined in each of the fractions and distributed
as shown in Table 7.3.1-8.
-------
Fugitive Emissions Calculations
Fugitive emission samples were collected at the Rouge
Plant Coke Battery A with high-volume air samplers. Initial and
final rotometer readings were made for each test and the sample
duration was recorded. The rotometer readings were converted to
flowrates by reference to a calibration^ curve. The sample volume
was determined by multiplying the aveaage of these two flowrates
by the sample duration in minutes.
For the first fugitive emissions sample taken on June
10, 1975, the initial and final rotometer readings were 33
and 30, respectively. These two readings corresponded to
flowrates of 51 and 47 cfm. The sample duration was 25 seconds,
or 0.417 minutes. The sampled volume was thus calculated as
follows:
V -0.417|5l+47
m
= 20.4 ft3
In order to determine the concentration of particulate
matter in these emissions, the following equation was employed
mg _ SW..
^3 " t
Vm * O.OZ83Z
For the first sample on June 10th,
51 - 71.3
m3 20.4(0.02832)
= 123
-------
FIGURE E-l
AERODYNAMIC DIAMETER VERSUS FLOW RATE THROUGH ANDERSEN STACK SAMPLER
c
10
9
8
7
6
5
4
3
J>
U
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0.8
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0.6
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0<
03
0.2
0.1
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02
0.1 0.2 0.3 04 0.5 0.60708031.0 2.0 3.0 4.0 5.0 6.07.08.0,9010 20 30 40 SO 60 708090100
Op. Aerodynamic Diameter, microns
-------
E-15
FIGURE E-2
DENSITY CORRECTION FACTOR FOR PHYSICAL SIZE OF
PARTICLES CAPTURED IN ANDERSEN STACK SAMPLER
3
2.6 -
2 .
15 -
!
E t.O.
0,,
1
; 08 -
*0T
06 .
OS -
0.4 -
03 -
075.
0.2 -
015-
01 -
.. •
•
-^
^x,
\
X
X
^
"V,
\.
^<
^
V
^^s^
x^
^-
"" *^
*^^
,
0.15 0.2 02S 0.3 0.4 0.5 0.6 0.7 08 0.9 1.0 1.5
\O -j
. Particle Density. gm/cmj
2 2.5 3
5 G 7 8 9 10
-------
FIGURE E-3
TEMPERATURE CORRECTION FACTOR FOR AERODYNAMIC SIZE OF PARTICLES CAPTURED IN ANDERSEN STACK SAMPLER
1.60
1.50
1.40
1,
2
U.
1
8 1.20
1.10
1.00
0.90
•
• •
: •
• •
—
. — -
— -
x
,**
/
/
•
/
I/
/
/
/
/
(
/
/
t
I
/
-
••
"•••10 20 30 40 SO 60 70 8090100 200 300 400 5OO 600 800 1000 1500 20OO
Stack Temperature. °F >
-•
•
"
• • .
•
'.'I'.
**
••"
..
••
••
T
'••
• •
..
-,-
I.
-
*•
• •
'•'
— •
•-
...
"""
. .
: i
• *
,
•
.
•
...
"-
-
**
:••
. . u
'-
•:•
*
•;
-
M
1
I — »
0\
-------
APPENDIX F
PROJECT PARTICIPANTS
Project Manager
J. Mutchler, P.E.
Project Leaders
F. Cooper (Source Sampling)
I. Loch, Ph.D., P.E. (Data Evaluation and Reports)
D. Malzahn (Fugitive Emissions and Meteorology)
R. Powals, P.E. (Field Data and On-Site Observations)
Engineer-Observers
M. Dodyk, P.E.
T. Loch, Ph.D., P.E.
R. Powals, P.E.
G. Schlaf, P.E.
J. Schoch
Photographers
R. Cooper
C. Gruner
R. Keller
R. Marcus
Fugitive Emissions Samplers
T. Julien
W. Lee
D. Malzahn
-------
F-2
Appendix F (continued)
Source Samplers
F. Cooper (Group Leader)
R. Griffin
V. Hanson
G. Hawkins
R. Keller
R. Marcus
R. Powals, P.E.
G. Santorilla
J. Schoch
Data Analysts
J. Alore
R. Cooper
J. Vecchio (Group Leader)
Chemists
L. Beaubien
A. Hayes (Analytical Coordinator)
M. Kelly
J. McClain
Clerical
J. Alore
K. Hoskins
E. Peet
-------
APPENDIX G
DAILY LOG OF FUME HOOD PERFORMANCE
This appendix contains all field data pertaining to hood
performance recorded when the Clayton engineer-observer
was on-site and was not recording data on scrubber per-
formance .
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-16-74
Atmospheric Pressure 30.2 Initial:
RJP
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
44
X54
X64
6
16
26
36
46
X56
8
18
28
38
48
X58
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0906
1004
1016
1026
1038
1056
1103
1114
1128
1138
Cross-Draft
Velocity
(fpm)
Calm
264
Calm
440
Calm
Calm
1760
1320
880
880
Fume Hood
Capture
(%)
0
>90
>90
>90
>90
>90
>90
>90
>90
90
Stack
Opacity
(%)
0
0
0
0
0
0
0
0
0
20
Coke Side
Condition
Good
Good
Good
Good
Good
Good
Fire
Good
Good
Green
Net Coal
Charged
(Ibs)
35750
35550
35850
35900
36000
36300
35950
36000
35850
35550
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-16-74
Atmospheric Pressure 30.2 Initial: Rjp
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
•
Oven
No.
1
11
21
31
41
X51
X61
3
13
23
33
43
X53
X63
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1242
1252
1303
1314
1328
1340
1400
1407
1420
1432
1443
1453
Cross-Draft
Velocity
(fpm)
-
1760
2200
1760
1760
2200
2200
1760
880
264
440
440
440
Fume Hood
Capture
(7.)
80
80
>90
0
>90
80
>90
>90
>90
>90
0
>90
.Stack
Opacity
(%)
0
0
0
0
0
20
0
0
0
0
0
10
•
Coke Side
Condition
Fire & Smoke
Fire & Smoke
Good
Good
Good
Green
Good
Good
Good
Good
Good
Fire & Smoke
Net Coal
Charged
(Ibs)
35750
35850
35500
35250
34700
35950
35900
35800
35600
35400
35500
34600
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date: 8-19-74
Atmospheric Pressure 30.1 Initial:
MRD
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
-
Oven
No.
33
43
X53
X63
_ _
5
15
25
35
45
X55
7
17
27
37
Schedule
Time
0800
0815
0830
OS50
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0920
0935
0948
1000
1010
1025
1035
1045
1055
1110
1125
Cross-Draft
Velocity
(fpm)
880
440
440
264
264
264
264
440
880
1760
Fume Hood
Capture
(%)
<50
>90
>90
0
0
0
>90
>90
0
0
Stack
Opacity
(%)
0
0
0
0
0
0
0
0
0
0 -
Coke Side
Condition
Fire & Smoke
Good
Good
Fire & Smoke
Good
Good
Good
Good
Green
Fire & Smoke
Net Coal
Charged
(Ibs)
35500
35600
35300
35750
35650
35450
35700
35950
35450
35500
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-19-74
Atmospheric Pressure 30.1 Initial:
MRD
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
47
X57
9
19
29
39
49
X59
2
12
22
32
42
X52
X62
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1220
1230
1245
1300
1340
1350
1405
1420
1445
1500
1515
1533
1543
Cross-Draft
Velocity
(fpm)
264
44Q
1320
1320
440
1760
1760
440
264
Fume Hood
Capture
(7.)
0
0
0
0
>90
>90
>95
>90
>90
Stack
Opacity
(%)
0
0
0
0
0
0
10
0
10
.
Coke Side
Condition
Green
Smoke
Good
Good
Good
Good
Good
Good
Good
Good
Good
Net Coal
Charged
(Ibs)
35800
35850
35850
35850
36500
36250
36550
36650
36300
36200
36350
36450
36400
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-21-74
Atmospheric Pressure 30.3 Initial:
MRP
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
3
13
23
33
43
X53
X63
— —
5
15
25
35
45
X55
7
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0815
0826
0846
0906
0927
0937
0950
1000
1020
1033
1047
1057
1106
1115
Cross-Draft
Velocity
(fpm)
90
60
0
0
260
130
220
120
Fume Hood
Capture
(7.)
>95
>90
>90
~50
>90
>90
~50
Stack
Opacity
(7.)
0
0
0
20
0
0
0
0
0
0
0
0
0
0
Coke Side
Condition
Good
Good
Good
Fire & Smoke
Good
Good
Good
Good
Good
Good
Good
Good
Good
Good
Net Coal
Charged
(Ibs)
35900
34300
35750
34400
34600
34400
36500
34350
34550
34500
34550
34500
34850
34600
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-21-74
Atmospheric Pressure 30.3 Initial:
MRD
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
17
27
37
47
X57
9
19
29
39
49
X59
2
12
22
32
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1209
1215
1225
1245
1306
1317
1327
1342
1401
1412
1420
1434
1440
1458
1517
Cross-Draft
Velocity
(fpm)
320
410
500
480
540
240
220
Fume Hood
Capture
(%)
~50
-50
>90
>90
>90
>90
>90
>90
>90
Stack
Opacity
(%)
0
0
0
0
10
0
0
0
0
0
0
0
0
0
0
Coke Side
Condition
Good
Good
Good
Good
Good
Good
Good
Good
Good
Good
Good
Good
Good
Good
Good
1 Net Coal
Charged
(Ibs)
34850
34950
34800
34950
35300
35450
34950
35300
35150
35300
35200
35500
35700
35400
35400
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-22-74
Atmospheric Pressure 30.2 Initial:
MRP
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
.-
Oven
No.
32
42
X52
X62
4
—
14
24
34
44
X54
X64
6
16
26
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0813
0843
0903
0920
0931
0948
1003
1021
1043
1053
1108
1120
1131
1142
Cross-Draft
Velocity
(fpm)
150
200
380
230
660
360
60
510
260
Fume Hood
Capture
(7.)
>90
-50
-"50
~50
>90
>90
>90
~50
~50
Stack
Opacity
(1)
0
0
0
10
0
0
0
10
0
0
0
0
0
o •
Coke Side
Condition
Good
Fire & Smoke
Good
Good
Good
Good
Good
Fire & Smoke
Good
Good
Good
Good
Good
Good
Net Coal
Charged
dbs)
35050
36600
34950
35500
35100
35000
35100
35500
35200
35850
35250
35200
35000
34900
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-22-74
Atmospheric Pressure 30.2 Initial:
MRD
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
36
46
X56
8
18
28
38
48
X58
—
1
11
21
31
41
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1151
1242
1255
1305
1339
1355
1409
1422
1433
1450
1500
Cross-Draft
Velocity
(fpm)
Fume Hood
Capture
(%)
'-SO
Stack
Opacity
(%)
30
...
.
Coke Side
Condition
Green
Green
<
Net Coal
Charged
Clbs)
35050
35000
o
oo
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-23-74
Atmospheric Pressure 30.1 Initial:
MRP
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
41
X51
X61
3
13
23
33
43
X53
X63
—
5
15
25
35
Schedule
Time
0800
0815
0830
0650
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
1033
1043
1055
1112
1120
1135
Cross-Draft
Velocity
(fpm)
160
580
570
300
Fume Hood
Capture
(7.)
>90
>90
>90
>90
>90
>90
Stack
Opacity
(%)
0
0
0
0
0
0 •
Coke Side
Condition
Good
Good
Good
Good
Good
Good
Net Coal
Charged
abs>
35800
35850
36000
35800
35300
34550
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-23-74
Atmospheric Pressure 30.1 Initial:
MRP
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
45
X55
7
17
27
37
47
X57
9
19
29
39
49
X59
2
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1222
1230
1241
1249
1258
1322
1338
1356
1422
1430
1443
1454
1506
1528
1550
Cross-Draft
Velocity
(fpm)
110
300
750
600
1070
800
Fume Hood
Capture
(7.)
Stack
Opacity
(7.)
0
0
0
0
0
0
0
0
10
0
0
0
10
0
o •
Coke Side
Condition
Good
Good
Good
Good
Good
Good
Good
Fire & Smoke
Fire & Smoke
Good
Good
Good
Good
Good
Good
Net Coal
Charged
(Ibs)
36950
35700
35550
36600
35800
35500
35900
35750
35300
35750
35350 .
35650
35650
35600
35750
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-26-74
Atmospheric Pressure 30.1
Initial:
MRD
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
2
12
22
32
42
X52
rf2
—
4
14
24
34
44
X54
X64
Schedule
Time
0800
0815
0820
0550
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0825
0830
0855
0912
0930
0944
1002
1010
1031
1041
1055
1110
1120
1130
Cross-Draft
Velocity
(fpm)
860
550
190
920
440
260
110
Fume Hood
Capture
(%)
>90
>90
>90
>90
~50
~50
-50
Stack
Opacity
<*>
0
0
10
0
0
0
0
0
0
0
0
0
0
0
Coke Side
Condition
Good
Good
Good
Good
Good
Good
Good
Good
Good
Good
Good
Good
Good
Good
Net Coal
Charged
(Ibs)
36700
35700
35800
35550
35750
35600
36650
36100
35900
35700
35500
35400
35450
35350
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-26-74
Atmospheric Pressure 30.1
Initial:
MRD
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
6
16
26
36
46
X56
8
18
28
38
48
X58
—
1
11
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1210
1226
1259
1310
1323
1342
1350
1407
1417
1429
1444
1505
1515
1530
Cross-Draft
Velocity
(fpm)
550
240
590
560
230
310
Fume Hood
Capture
(7.)
>90
>90
>90
-50
-50
Stack
Opacity
(%)
0
0
..0
0
0
0
0
0
0
10
20
20
0
0
Coke Side
Condition
Good
Good
Good
Good
Good
Good
Good
Good
Good
Good
Fire & Smoke
Fire & Smoke
Good
Good
Net Coal
Charged
dbs)
35350
35700
35800
35600
35600
36200
35750
36200
35450
36750
35550
35400
37000
35950
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-27-74
Atmospheric Pressure 30 mp Initial:
RJP
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
11
21
31
41
X51
X61
3
13
23
33
43
X53
X63
—
5
Schedule
Time
0800
0815
0830
OS50
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0819
0827
0914
0923
0937
0948
1002
1017
1029
1040
1048
1058
1124
1134
Cross-Draft
Velocity
(fpm)
180
360
200
240
Ca 1m
180
Ca 1m
190
360
350
550
760
880
550
Fume Hood
Capture
(%)
10
10
10
10
>90
>90
>90
10
10
10
>90
Stack
Opacity
m
0
0
0
20
0
0
0
0
20
0
0
0
20
0
Coke Side
Condition
Good
Good
Good
Fire & Smoke
Good
Good
Good
Good
Fire & Smoke
Good
Good
Good
Fire & Smoke
Good
Net Coal
Charged
(Ibs)
36950
35650
36000
35350
35600
35800
35400
36050
35650
35600
35700
35400
35550
35450
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-27-74
Atmospheric Pressure 30.0 Initial: RJP
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
15
25
35
45
X55
7
17
27
37
47
X57
9
19
29
39
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1210
1223
1243
1252
1305
1318
1327
1346
1356
1405
1419
1431
1444
1455
1512
Cross-Draft
Velocity
(fptn)
570
980
990
850
800
670
830
970
790
1210
1070
440
420
560
350
Fume Hood
Capture
m
>90
>90
80
10
70
90
>90
>90
10
10
10
90
>90
>90
10
Stack
Opacity
(%)
0
0
20
0
20
0
0
0
20
20
40
0
10
0
10
Coke Side
Condition
Good
Good
Fire & Smoke
Good
Green
Good
Good
Good
Green
Green
Green
Good
Good
Good
Good
Net Coal
Charged
(Ibs)
35550
35300
35300
35550
35450
34600
35400
35000
35500
35400
36500
36500
35600
35050
33900
^
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-28-74
Atmospheric Pressure 30.0
Initial:
RJP
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
39
49
X59
2
12
22
32
42
X52
X62
—
4
14
24
34
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0820
0829
0838
0851
0904
0919
0939
0943
0952
1013
1020
1032
1051
1105
Cross-Draft
Velocity
(fpm)
430
410
Calm
170
150
530
560
150
180
420
200
80
170
360
Fume Hood
Capture
(%)
10
10
10
>90
>90
90
>90
10
10
10
>90
>90
>90
>90
Stack
Opacity
(7.)
0
10
40
0
0
20
0
10
40
50
0
0
0
0
Coke Side
Condition
Good
Fire & Smoke
Green
Good
Good
Fire & Smoke
Good
Fire & Smoke
Green
Green
Good
Good
Good
Good
Net Coal
Charged
fibs)
35550
35350
35000
35300
34150
34150
34100
34000
35550
35250
35650
35950
35600
36050
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-28-74
Atmospheric Pressure 30.0 Initial:
RJP
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
44
X54
X64
6
16
26
36
46
X56
8
18
28
38
48
X58
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1234
1245
1254
1306
1319
1326
1336
1345
1352
1411
1422
1442
1451
1502
1511
Cross-Draft
Velocity
(fpm)
160
290
400
370
240
450
330
360
340
310
350
360
130
280
350
Fume Hood
Capture
(%)
10
10
10
>90
>90
>90
>90
10
10
>90
>90
>90
10
10
10
Stack
Opacity
(%)
0
^ 0
40
0
0
0
0
20
80
0
0
0
0
20
40 .
Coke Side
Condition
Good
Good
Fire & Smoke
Good
Good
Good
Good
Fire & Smoke
Green
Good
Good
Good
Good
Fire & Smoke
Green
Net Coal
Charged
(Ibs)
36500
35700
35800
35950
36200
36150
35900
35850
35800
35300
34350
36650
35600
35600
36000
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-29-74
Atmospheric Pressure 30.0 Initial:
MRD
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
x58
1
11
21
31
41
X51
X61
3
13
23
33
43
X53
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0823
0833
0844
0915
0934
0944
1006
1029
1044
1053
1104
1116
1123
1135
Cross-Draft
Velocity
(fpm)
Fume Hood
Capture
(7.)
Stack
Opacity
(%)
•
Coke Side
Condition
Good
Good
Net Coal
Charged
(Ibs)
35800
35950
35950
36850
35750
36000
35500
35650
35900
36050
35800
35950
36000
35750
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-29-74
Atmospheric Pressure 30.0 Initial:
MRD
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
X63
—
5
15
25
35
45
X55
7
17
27
37
47
X57
9
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1211
1232
1242
1253
1303
1314
1325
1335
1351
1406
1419
1429
1453
1516
Cross-Draft
Velocity
(fpm)
Fume Hood
Capture
<%>
~50
>90
Stack
Opacity
(%)
20
0
Coke Side
Condition
Good
Good
Good
Good
Good
Good
Green
Good
Good
Good
Good
Good
Fire & Smoke
Good
Net Coal
Charged
(Ibs)
35850
35300
35600
35650
35700
35700
35450
35400
35700
36950
34250
35500
35500
35450
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-30-74
Atmospheric Pressure 3Q ,Q Initial:
MRD
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
-
Oven
No.
9
19
29
39
49
X59
2
12
22
32
42
X52
X62
—
4
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0817
0825
0844
0856
0909
0934
0951
1004
1015
1024
1027
1050
1107
1116
Cross-Draft
Velocity
(fpm)
220
190
130
Calm
210
340
460
220
Calm
Fume Hood
Capture
a>
>90
0
0
0
0
>90
>80
>90
Stack
Opacity
(*)
0
0
0
0
0
0
0
0
0
0
0
0
20
o •
Coke Side
Condition
Good
Good
Good
Good
Good
Good
Good
Good
Good
Good
Good
Good
Fire & Smoke
Good
Net Coal
Charged
(Ibs)
35000
35500
35200
35020
35200
35350
35150
35150
35300
35400
35750
35550
35550
35350
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-30-74
Atmospheric Pressure 30.0 Initial:
MRD
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
14
. £4 .
34
44
X54
X64
6
16
26
36
46
X56
8
18
28
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1204
1215
1242
1253
1301
1313
1323
1343
1353
1401
1421
1440
1457
1511
1524
Cross-Draft
Velocity
(fpm)
590
480
840
420
360
310
Calm
230
270
360
460
Calm
310
Calm
420
Fume Hood
Capture
(7.)
>90
>90
>90
>90
>90
80
Stack
Opacity
(%)
0
10
0
0
10
10
10
0
0
10
0
30
0
0
0
Coke Side
Condition
Good
Fire & Smoke
Good
Good
Fire & Smoke
Fire & Smoke
Good
Good
Good
Fire & Smoke
Good
Green
Good
Good
Good
Net Coal
Charged
(Ibs)
35400
35050
35350
35450
36750
35450
35350
35250
35300
36700
35600
35200
35050
35350
35250
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
9-3-74
Atmospheric Pressure 30 .p Initial:
MRP
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
7
17
27
37
47
X57
9
19
29
39
49
X59
2
12
22
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0831
0843
0857
0907
0914
0925
0943
0957
1007
1022
1033
1044
1100
1114
1128
Cross-Draft
Velocity
(fpm)
390
560
170
350
360
160
750
550
490
220
480
370
280
380
440
Fume Rood
Capture
(7.)
>90
>90
>90
>90
>90
>90
Stack
Opacity
(7.)
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Coke Side
Condition
Good
Good
Good
Good
Good
Good
Good
Good
Good
Good
Good
Good
Good
Good
Good
Net Coal
Charged
dbs)
36600
36600
36350
36450
36250
36400
36500
36300
36650
36700
36250
36350
36600
36350
36550
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
9-3-74
Atmospheric Pressure 30.1 Initial:
MRD
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
32
42
X52
X62
— —
4
14
24
34
44
X54
X64
6
16
26
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1216
1227
1240
1250
1303
1314
1324
1336
1349
1403
1429
1453
1459
1522
Cross-Draft
Velocity
(fpm)
400
430
450
390
790
280
620
610
760
230
680
310
400
350
.
Fume Hood
Capture
m
>90
>90
>90
>90
>90
>80
>90
Stack
Opacity
(%)
0
0
0
30
0
0
0
0
0
10
0
0
0
0
„
Coke Side
Condition
Good
Good
Good
Fire & Smoke
Good
Good
Good
Good
Good
Fire & Smoke
Good
Good
Good
Good
Net Coal
Charged
(Ibs)
35400
36750
36400
36100
36350
36400
36200
36450
36450
36400 .
36400
36200
36050
35950
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
9-4-74
Atmospheric Pressure 30.2
Initial:
MRD
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
26
36
46
X56
8
18
28
38
48
X58
—
1
11
21
31
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0810
0817
0837
0847
0922
0930
1003
1015
1032
1043
1107
1121
1142
1153
Cross-Draft
Velocity
(fpm)
Calm
190
160
170
520
340
480
410
140
620
340
230
170
120
Fume Hood
Capture
(7o)
>90
>90
>90
>90
>90
"50
Stack
Opacity
(%)
0
20
0
30
0
0
0
0
0
10
0
0
0
o •
Coke Side
Condition
Good
Good
Good
Green
Good
Good
Good
Good
Good
Green
Good
Good
Good
Good
Net Coal
Charged
(Ibs)
36850
36200
36050
35500
35950
34800
35400
35800
35600
35900
35500
35650
36800
35450
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
9-4-74
Atmospheric Pressure 30.2 Initial:'
MRP
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
41
361
X61
3
13
23
33
43
X53
X63
5
15
25
35
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1238
1248
1301
1312
1324
1336
1345
1356
1405
1416
1438
1453
1503
1513
Cross-Draft
Velocity
(fpm)
350
360
400
360
560
270
480
260
540
470
380
240
Z30
310
Fume Hood
Capture
(i)
>90
>90
>90
>90
>90
>90
~50
Stack
Opacity
(%)
0
0
0
0
0
0
0
0
0
20
0
0
0
0
Coke Side
Condition
Good
Good
Fire & Smoke
Good
Good
Good
Good
Good
Good
Fire & Smoke
Good
Good
Good
Good
Net Coal
Charged
(Ibs)
35250
35500
35150
35350
35550
35000
34350
35500
35550
35600
35200
34750
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
9-5-74
Atmospheric Pressure 30.4 Initial:
MRP
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
35
45
X55
7
17
27
37
47
X57
9
19
29
39
49
X59
Schedule
Time
0800
0815
0830
OS50
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0831
0841
0847
0857
0922
0932
0959
1018
1029
1040
1050
1103
1118
1128
1138
Cross-Draft
Velocity
(fpm)
220
180
220
250
220
290
390
590
360
490
390
550
380
Fume Hood
Capture
(7.)
>90
>90
>90
80
80
Stack
Opacity
(7.)
0
20
0
0
0
0
10
10
0
0
0
0
0
10 .
Coke Side
Condition
Good
Good
Green
Green
Good
Good
Good
Fire & Smoke
Green
Good
Good
Good
Good
Good
Fire & Smoke
Net Coal
Charged
(Ibs)
35900
36200
33850
33900
35650
37200
35850
35700
35350
35550
35250
35100
36300
35750
35900
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
9-5-74
Atmospheric Pressure 30.4 Initial:
MRP
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
2
12
22
32
42
X52
X62
4
14
24
34
44
X54
X64
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1228
1235
1250
1259
1310
1317
1328
1338
1351
1405
1429
1442
1505
1518
Cross-Draft
Velocity
(fpm)
840
1150
1080
960
1220
1160
970
420
340
310
260
140
340
280
.
Fume Hood
Capture
(%)
>90
>90
>90
>90
>90
>90
"50
Stack
Opacity
(7.)
0
0
0
0
0
0
30
0
0
0 '
0
0
0
0 .
Coke Side
Condition
Good
Good
Good
Good
Good
Good
Fire & Smoke
Good
Good
Good
Good
Good
Good
Good
Net Coal
Charged
(Ibs)
35700
35700
35800
35400
36400
37350
35850
36100
35650
36750
36100
36300
36300
37250
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
9-6-74
Atmospheric Pressure 30.3 Initial: RJP
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
X64
6
16
26
36
46
X56
8
18
28
38
48
X58
—
1
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0854
0921
0930
0940
0957
1011
1025
1040
1055
1106
1116
1128
1141
1152
Cross-Draft
Velocity
(fpm)
80
100
n
140
50
80
420
420
300
450
480
500
560
480
Fume Hood
Capture
(%)
0
>90
>90
>90
>90
>90
80
>90
>90
>90
>90
>90
>90
>90
Stack
Opacity
(%)
20
0
0
0
0
20
0
0
0
0
0
0
0 •
Coke Side
Condition
Good
Fire & Smoke
Good
Good
Good
Good
Fire & Smoke
Good
Good
Good
Good
Good
Good
Good
Net Coal
Charged
(Ibs)
36650
36050
36050
36200
35800
36200
36200
37150
36000
36300
35750
36050
36350
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
9-6-74
Atmospheric Pressure 30.3 Initial:'
RJP
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
11
21
31
41
X51
X61
3
13
23
33
43
X53
X63
5
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1203
1212
1253
1302
1320
1332
1345
1354
1405
1416
1425
1437
1449
1510
Cross-Draft
Velocity
(fpm)
700
380
160
190
80
110
200
240
80
340
240
330
100
140
Fume Hood
Capture
(%)
>90
>90
>90
>90
>90
>90
>90
>90
>90
>90
>90
80
80
>90
Stack
Opacity
(7.)
0
0
0
0
0
0
0
20
0
0
0
20
20
0 .
Coke Side
Condition
Good
Good
Good
Fire & Smoke
Good
Good
Good
Fire & Smoke
Good
Good
Good
Fire & Smoke
Fire & Smoke
Good
Net Coal
Charged
(Ibs)
36350
36000
35400
34800
35350 "
33550
35050
35150
37250
34350
33800
34200
34500
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
1-8-75
Atmospheric Pressure 29.56 Initial:
MRD
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
44
X54
X64
6
16
26
36
46
X56
8
18
28
38
Schedule
Time
0800
0820
0839
0859
0918
0938
0958
1017
1036
1056
1115
1134
1153
Push
Time
0825
0836
0847
0859
0913
0930
0950
1007
1030
1045
1107
1123
1140
Cross-Draft
Velocity
(fpm)
Calm
180
240
130
80
130
80
70
60
270
550
340
380
Fume Hood
Capture
(%)
90
90
90
90
90
90
70
70
90
90
90
90
70
Stack
Opacity
<*)
0
0
0
0
0
0
10
20
10
0
0
0
10
Coke Side
Condition
Good
Good
Good
Good
Good
Good
Fire & Smoke
Fire & Smoke
Good
Good
Good
Good
Fire & Smoke
Net Coal
Charged
(Ibs)
I
NJ
VO
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
1-8-75
Atmospheric Pressure 29.47 Initial:
MRD
Push
16
17_
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
48
X58 .
1
11
21
31
41
X51
X61
3
13
Schedule
Time
1212
1232
1252
1312
L332
1352
1412
1430
1450T
1510'
1530
Push
Time
1219
1233
1246
1312
1323
1340
1352
1414
1435
1507
1520
Cross-Draft
Velocity
(fpm)
320
240
360
Fume Hood
Capture
(%)
90
90
90
70
90
90
70
90
90
90
90
Stack
Opacity
(%)
0
0
0
20
0
0
20
10
0
0
0
.
Coke Side
Condition
Good
Good
Good
Fire & Smoke
Good
Good
Fire & Smoke
Good
Good
Good
Good
Net Coal
Charged
(Ibs)
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
1-9-75
Atmospheric Pressure 29.66 Initial:
MRP
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
X58
1
11
21
31
41
X51
X61
3
13
23
33
43
Schedule
Time
0800
0820
0839
0859
0918
0938
0958
1017.
1036
1056
1115
1134
1153
Push
Time
0820
0830
0900
0918
0931
0944
1001
1017
1024
1046
1057
1115
1127
Cross-Draft
Velocity
(fpm)
300
280
1280
580
650
540
1000
500
380
240
250
350
480
Fume Hood
Capture
(%)
90
90
90
90
90
90
90
90
90
90
90
90
0
Stack
Opacity
(%)
0
0
0
0
0
0
0
0
0
0
0
0
0
•
Coke Side
Condition
Good
Good
Good
Good
Good
Good
Good
Good
Good
Good
Good
Good
Green
Net Coal
Charged
(Ibs)
Ci
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
1-10-75
Atmospheric Pressure 29.51 Initial:
MRD
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
•
Oven
No.
X63
5
15
25
35
45
X55
7
17
27
37
47
X57
Schedule
Time
0800
0820.
0839
085§
0918
0938
0958
1017
1036
1056
1115
1134
1153
Push
Time
0820
0830
0900
0912
0923
0942
0957
1012
1025
1036
1051
1106
1120
Cross-Draft
Velocity
(fpm)
210
180
800
670
570
420
360
340
490
510
440
360
410
Fume Hood
Capture
(7.)
90
90
90
90
70
90
90
90
90
90
90
70
90
Stack
Opacity
CD
0
0
0
0
10
0
0
0
0
0
10
40
0
•
Coke Side
Condition
Godd
Good
Good
Good
Fire & Smoke
Good
Good
Good
Good
Good
Fire & Smoke
Green
Good
Net Coal
Charged
(Ibs)
o
Co
M
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
1-10-75
Atmospheric Pressure 29.37 Initial:
MRD
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
9
19
29
39
49
X59
2
12
22
32
42
Schedule
Time
1212
1232
1252
1312
1332
1352
1412
1430
1450
1510
1530
Push
Time
1215
1226
1310
1321
1335
1352
1403
1419
1446
1501
1516
Cross-Draft
Velocity
(fpm)
560"
410
440
360
700
550
560
470
610
Fume Hood
Capture
m
90
90
90
70
90
90
90
70
90
90
90
Stack
Opacity
(%)
0
0
0
30
0
0
0
20
0
0
10
•
Coke Side
Condition
Good
Good
Good
Green
Good
Good
Good
Fire & Smoke
Good
Good
Fire & Smoke
Net Coal
Charged
(Ibs)
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6-3-75
Atmospheric Pressure 29.50 Initial:
JBS
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
48
X58
^__
1
11
21
31
41
X51
X61
3
13
23
33
43
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0820
0830
0855
0958
1012
1022
1040
1047
1104
1114
1124
1204
1213
1224
Cross-Draft
Velocity
(fpm)
Fume Hood
Capture
(7.)
Stack
Opacity
(%)
.
Coke Side
Condition
Net Coal
Charged
(Ibs)
35700
35550
34700
34500
33500
34000
33800
33950
34850
—
^ ^
.^_
34750
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6-3-75
Atmospheric Pressure 29.5 Initial:
JBS
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
X53
X63
^^m
5
15
25
35
45
X55
7
17
27
37
47
X57
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1302
1308
1330
1340
1350
1407
1443
1437
1446
1458
1509
1519
1538
1552
Cross-Draft
Velocity
(fpm)
360
265
380
350
325
490
495
365
420
290
360
350
Fume Hood
Capture
(7,)
80-90
70
80
80
50
50
95
70
90
50
85
50
Stack
Opacity
(%)
25
10
10
10
40
10
0
30
0
25
15
30 •
Coke Side
Condition
Good
Good
Good
Good
Green
Green
Good
Fire & Smoke
Good
Green
Good
Green
Net Coal
Charged
(Ibs)
TSisn
35050
35000
34750
^^^
^^
_
35350
35500
29050
35600
34850
35750
36350
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6-3-75
Atmospheric Pressure 29.5
Initial:
JBS
Push
1
2 ...
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
9
. 19 ...
29
39
49
X59
Schedule
Time
1600
1615
1630
1645
1700
1715
Push
Time
1613
1626
1640
1653
1710
1729
Cross-Draft
Velocity
(fpm)
430
455
380
420
545
420
Fume Hood
Capture
m
90
85
75
35
25
70
Stack
Opacity
(7.)
5
25
15
20
55
25
•
Coke Side
Condition
Good
Good
Good
Green
Green
Fire & Smoke
Net Coal
Charged
(Ibs)
o
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6-4-75
Atmospheric Pressure
Initial:
JBS
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
X57
9
19
29
39
49
X59
2
12
22
32
42
X52
X62
Schedule
Time
0800
0815
0830
0550
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0830
0904
0914
0926
0940
0955
1018
1049
1104
1116
1125
Cross-Draft
Velocity
(fpm)
300
320
360
400
430
510
480
Fume Hood
Capture
(7.)
70
70
60
15
65
30
75
Stack
Opacity
(%)
20
15
30
45
25
25
10
•
Coke Side
Condition
Good
Good
Fire & Smoke
Green
Fire & Smoke
Green
Good
Net Coal
Charged
(Ibs)
_
_
—
—
—
—
36550
36650
35950
36250
—
36000
35700
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6-4-75
Atmospheric Pressure
Initial:
JBS
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
4
14
24
34
44
X54
X64
6
16
26
36
46
X56
8
18
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545 -
Push
Time
1300
1310
1317
1330
1346
1359
1411
1425
1434
1444
1458
1508
1519
1531
1537
Cross-Draft
Velocity
(fpm)
400
250
245
405
265
300
265
290
355
Fume Hood
Capture
(%)
90
95
75
65
10
60
60
10
10
Stack
Opacity
(%>
10
0
25
5
35
20
30
25
20
.
Coke Side
Condition
Good
Good
Good
Good
Green
Fire & Smoke
Green
Green
Green
Net Coal
Charged
(Ibs)
35800
36050
35100
33150
31950
35400
35500
35100
36700
35600
34700 .
36100
31750
35100
—
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6-5-75
Atmospheric Pressure 29.2 Initial:
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
23
33
43
X53
X63
^^_
5
15
25
35
45
X55
7
17
27
37
47
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1159
1213
1226
1240
1250
1315
1328
1350
1404
1422
1440
1452
1502
1522
1614
1625
Cross-Draft
Velocity
(fpm)
525
465
480
500
380
520
460
770
690
480
980
440
558
Fume Hood
Capture
(%)
80
60
50
>90
>90
>90
30
70
>90
80
70
80
75
Stack
Opacity
(%)
40
30
40
10
5
10
55
40
10
30
25 •
20
25
Coke Side
Condition
Green
Green
Green
Good
Good
Good
Green
Fire & Smoke
Good
Fire & Smoke
Fire & Smoke
Fire & Smoke
Met Coal
Charged
(Ibs)
35800
35500
35600
35350
35450
35550
34900
35400
35700
35250
35850
35350
35150
34700
—
—
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6-6-75
Atmospheric Pressure 29.1 Initial:
RJP
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
27
37
47
X57
9
19
29
39
49
X59
2
12
22
32
42
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0810
0820
0830
0950
1004
1027
1049
1100
1114
1127
1141
1150
1201
1215
1230
Cross-Draft
Velocity
(fpm)
540
690
515
530
575
560
660
450
830
480
Fume Hood
Capture
m
90
90
>90
60
>90
30
90
>90
80
90
Stack
Opacity
(%)
15
10
5
40
30
85
20
15
30
15
.
Coke Side
Condition
Good
Good
Good
Green
Good
Green
Fire & Smoke
Good
Fire & Smoke
Fire & Smoke
1 Net Coal
Charged
(Ibs)
36150
35600
35700
35350
35500
36050
34850
35650
35150
35050 •
34950
34950
34950
34750
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6-6-75
Atmospheric Pressure 29.1 Initial: Rjp
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
X52
X62
^^_
4
14
24
34
44
X54
X64
6
16
26
36
46
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1244
1300
1316
1338
1345
1355
1410
1420
1430
1458
1510
1522
1542
Cross-Draft
Velocity
(fpm)
1110
480
375
650
790
810
685
930
1105
660
645
Fume Hood
Capture
(7.)
90
>90
>90
>90
60
60
50
90
40
90
40
Stack
Opacity
(%)
0
10
0
5
45
50
60
0
80
5
85
-
Coke Side
Condition
Good
Good
Good
Good
Green
Green
Green
Good
Green
Good
Green
Net Coal
Charged
(Ibs)
34950
35500
34900
30800
34350
34600
34700
35250
35300
35500
35500
34700
34400
34450
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6-9-75
Atmospheric Pressure 29.67 Initial:
GJS
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
16
26
36
46
X56
8
18
28
38
48
X58
—
1
11
21
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0817
0830
0838
0853
0923
0942
0957
1013
1025
1038
1047
1058
1115
1128
Cross-Draft
Velocity
(fpm)
•
550
230
250
170
Fume Hood
Capture
(7.)
70
60
80
50
Stack
Opacity
(%)
30
20
5
10 •
Coke Side
Condition
•
Green
Green
Good
Green
Net Coal
Charged
(Ibs)
_
34550
34850
34750
34450
34450
34850
34750
34500
35000
34950
35000
35050
33200
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6-9-75
Atmospheric Pressure 29 .67 Initial:
GJS
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
31
41
X51
X61
3
13
23
33
43
X53
X63
—
5
15
25
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1139
1153
1206
1314
1322
1335
1345
1357
1403
1422
1432
1447
1502
1530
Cross-Draft
Velocity
(fpm)
460
750
520
450
540
480
Fume Hood
Capture
(%)
70
70
80
80
50
50
Stack
Opacity
(7.)
20
60
20
20
20
20
•
Coke Side
Condition
Good
Green
Good
Good
Good
Green
Net Coal
Charged
(Ibs)
31850
35300
35100
35050
34900
35050
35050
34950
34950
34700
34950
33650
35300
34950
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6-10-75
Atmospheric Pressure 29.85 Initial:
TAL
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
25
35
45
X55
7
17
27
37
47
X57
9
19
29
39
49
Schedule
Time
0800
0815
0830
OS50
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0823
0848
0855
0933
0940
0950
1000
1014
1024
1036
1051
1058
1110
1118
1126
Cross-Draft
Velocity
(fpm)
350
200
410
390
370
440
280
520
360
Fume Hood
Capture
(7.)
50
70
40
80
40
40
40
30
30
Stack
Opacity
(%)
20
10
20
0
30
20
20
30
40 .
Coke Side
Condition
Green
Green
Green
Good
Green
Green
Green
Green
Green
Net Coal
Charged
(Ibs)
358OO
34800
34900
^^^
35550
34850
35600
35550
35300
34800
—
34850
35200
35550
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6-10-75
Atmospheric Pressure 29.85 Initial:
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
Oven
No.
X59
2
12
22
32
42
X52
X62
—
4
14
24
34
44
X54
X6.4
6
16
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
1600
1615
1630
Push
Time
1210
1215
1236
1255
1305
1315
1330
1342
1350
1403
1419
1430
1458
1510
1612
1639
1657
Cross-Draft
Velocity
(fpm)
400
430
520
210
210
270
320
300
250
Fume Hood
Capture
(*)
30
80
50
60
80
20
80
80
20
Stack
Opacity
(%)
30
0
20
10
10
40
10 •
10
40
Coke Side
Condition
Fire & Smoke
Good
Fire & Smoke
Fire & Smoke
Good
Green
Good
Good
Green
Net Coal
Charged
Clbs)
35150
35100
34750
34850
35100
35000
34850
34950
34500
35150
35050
36700
^_
35100
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6-11-75
Atmospheric Pressure 29.15 Initial:
GJS
Push
1
.2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
X54
X64
6
16
26
36
46
X56
8
18
28
38
48
X58
—
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0816
0828
0843
0905
0938
1000
1004
1025
1050
1102
1111
1122
1135
1202
Cross-Draft
Velocity
(fpm)
340
890
500
Fume Hood
Capture
(7.)
60
40
60
Stack
Opacity
(7.)
40
40
20
•
Coke Side
Condition
Good
•
Green
Good
Net Coal
Charged
(Ibs)
36450
36250
35600
36500
36300
36000
36000
36350
36200
—
36200
36000
36750
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6-11-75
Atmospheric Pressure 29.55 Initial: QJS
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
1
11
21
31
41
X51
X61
3
13
23
33
43
X53
X63
—
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1250
1302
1310
1338
1347
1408
1423
1434
1445
1455
1508
1516
1528
1538
Cross-Draft
Velocity
(fpm)
340
650
450
650
630
600
650
630
610
Fume Hood
Capture
(7.)
50
80
50
50
80
90
30
90
90
Stack
Opacity
(%)
40
20
40
20
10
10
40
10
10
•
Coke Side
Condition
Green
Good
Green
Fire & Smoke
Good
Good
Fire & Smoke
Good
Good
Net Coal
Charged
(Ibs)
36150
36150
35600
34500
36650
36500
36550
37050
35750
35700
36250
36050
36150
35300
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6-12-75
Atmospheric Pressure
Initial:
GJS
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
5
15
25
35
45
X55
7
17
27
37
47
X57
9
19
Schedule
Time
0800
0815
0830
OS50
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0819
0841
0850
0932
0944
1000
1014
1037
1046
1101
1114
1126
1214
1226
Cross-Draft
Velocity
(fpm)
520
550
580
810
490
Fume Hood
Capture
(%)
50
70
50
70
90
Stack
Opacity
(%)
20
20
40
20
10
.
Coke Side
Condition
•
Green
Green
Green
Green
Good
Net Coal
Charged
(Ibs)
36200
34850
34450
^_
^_
37050
33900
33800
34350
37200
36900
36750
35200
35850
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6/12/75
Atmospheric Pressure
Initial: GJS
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
29
39
49
X59
2
12
22
32
42
X52
X62
—
4
14
24
34
44
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
1600
1615
Push
Time
1235
1245
1256
1315
1330
1342
1350
1410
1418
1434
1445
1452
1510
1521
1608
1623
Cross-Draft
Velocity
(fpm)
620
650
330
460
450
480
300
420
780
650
620
450
620
Fume Hood
Capture
(%)
60
90
40
60
50
90
90
80
70
80
80
90
10
Stack
Opacity
(7.)
20
<10
20
40
20
<10
<10
10
20
20
20 .
<10
60
Coke Side
Condition
Green
Good
Fire & Smoke
Green
Green
Good
Good
Good
Green
Good
Good
Good
Green
Net Coal
Charged
(Ibs)
34,750
33,100
35,850
32,700
34,450
34,600
35,000
34,850
35,200
34,700
34,950
34,500
35,200
35,050
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date: 6/12/75
Atmospheric Pressure 29.30 Initial:
GJS
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
,
Oven
No.
X54
X64
6
Schedule
Time
1630
1645
1700
Push
Time
1636
1651
1710
Cross-Draft
Velocity
(fpm)
650
620
Fume Hood
Capture
(%)
90
60
0
Stack
Opacity
<%)
<10
<10
•
Coke Side
Condition
Good
Good
•
Net Coal
Charged
(Ibs)
-
,
o
in
O
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6/18/75
Atmospheric Pressure
Initial: RJG
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
41
X51
X61
3
13
23
33
43
X53
X63
5
15
25
35
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0846
0853
0905
0916
0929
0942
0950
1006
1025
1037
1048
1100
1111
1124
Cross-Draft
Velocity
(fpm)
280
407
342
519
282
118
403
387
425
328
Fume Hood
Capture
(%)
Stack
Opacity
(7.)
Coke Side
Condition
Green
Fire & Smoke
Fire & Smoke
Fire & Smoke
Fire & Smoke
Fire & Smoke
Fire & Smoke
Green
Green
Fire & Smoke
Fire & Smoke
Net Coal
Charged
(Ibs)
36,750
35,750
36,050
35,750
34,750
35,500
36,250
34,800
36,750
35,650
33,200
35,250
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6/18/75
Atmospheric Pressure
Initial:
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
17
27
37
47
X57
9
19
29
39
49
X59
2
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1250
1300
1313
1333
1344
1350
1410
1422
1436
1447
1507
1518
Cross-Draft
Velocity
(fpm)
220
440
414
438
538
561
322
303
455
364
475
590
Fume Hood
Capture
(%)
Stack
Opacity
(%)
.
Coke Side
Condition
Green
Green
Fire & Smoke
Green
Fire & Smoke
Fire & Smoke
Green
Green
Fire & Smoke
Fire & Smoke
Green
Fire & Smoke
Net Coal
Charged
(Ibs)
34,800
34,800
35,000
35,050
34,650
35,200
...
_ _ _
34,300
34,950
35,300
35,900
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date: 6/20/75
Atmospheric Pressure
Initial: RJG
Push
1
2
3
A
5
6
7
8
9
10
11
12
13
14
15
-
Oven
No.
41
X51
X61
3
13
23
33
43
X53
X63
5
15
25
Schedule
Time
0800
0815
0830
f\ c C A
Uo_>U
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0900
0926
0935
0953
1005
1017
1032
1045
1107
1115
1125
1137
1148
Cross-Dra ft
Velocity
(fpm)
388
420
384
427
506
386
384
200
342
341
396
580
383
Fume Hood
Capture
(%)
Stack
Opacity
(%)
.
Coke Side
Condition
Good
T? -i *• A JC. CrnnlrP
Fire & Smoke
Green
Fire & Smoke
Fire & Smoke
Green
Good
Fire & Smoke
Fire & Smoke
Green
Green
Fire & Smoke
Net Coal
Charged
(Ibs)
34,300
34,350
34,600
33,300
34,700
34,500
34,000
34,900
32,850
34,350
33,650
33,750
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6/20/75
Atmospheric Pressure
Initial:
RJG
Push
16
17
18
19
20
21
2-2
23
24
25
26
27
28
29
30
Oven
No.
7
17
27
37
47
X57
19
19
29
39
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1332
1345
1358
1415
1434
1449
15QO
1510
1520
1530
Cross-Draft
Velocity
(fpm)
524
650
338
368
475
360
591
557
400
Fume Hood
Capture
(%)
.
Stack
Opacity
(%)
•
Coke Side
Condition
Fire & Smoke
Green
Green
Fire & Smoke
Green
Fire & Smoke
Fire & Smoke
Fire & Smoke
Green
Green
Net Coal
Charged
(Ibs)
33,100
34,300
34,550
34,300
35,150
34,950
35,250
33,850
34,450
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date: 6/24/75
Atmospheric Pressure
Initial:
RJP
Push
1
2
3
A
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
28
38
48
Y58
1
11
21
31
41
X51
Yfi 1
3
13
23
Schedule
Time
0800
0815
0830
r\ c c A
Uo5O
0905
0920
0935
0950
1005
1020
1035
1 f\ c c
1U.>.)
1110
1125
1145
Push
Time
0823
0846
0858
0921
0943
1013
1025
1036
1052
1103
1117
1132
1146
1158
Cross-Draft
Velocity
(fpm)
355
320
360
130
485
2^0
80
115
200
Fume Hood
Capture
(7.)
50
0
0
>90
>90
•S.QO
20
50
20
Stack
Opacity
(%)
40
0
0
0
0
75
60
60 .
Coke Side
Condition
Green
Fire & Smoke
Fire & Smoke
Good
Good
Green
Green
Green
Net Coal
Charged
fibs)
38,800
38,500
38,050
35,050
34,400
36,100
35,450
35,200
34,800
35,350
36,350
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date: 6/24/75
Atmospheric Pressure 30.0 Initial: RJP
Push
16
17
18
19
o r\
£. 0
21
22
23
24
25
26
27
28
29
30
Oven
No.
33
43
X53
X63
5
15
25
35
45
X55
7
17
27
37
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1211
1224
1330
1340
1348
1404
1412
1426
1438
1448
1501
1512
1523
1531
Cross-Draft
Velocity
(fpm)
310
280
340
420
360
400
Fume Hood
Capture
(%)
>90
70
30
30
50
80
Stack
Opacity
(%)
0
50
80
60
60
20
•
Coke Side
Condition
Good
Green
Green
Green
Green
Good
Net Coal
Charged
(Ibs)
34,900
_ _ _ —
35,550
35,750
35,500
35,000
35,750
35,000
34,350
35,250
35,100
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date: 6/25/75
Atmospheric Pressure
Initial: RJP
Push
1
2
3
5
6
7
8
9
10
11
12
13
14
15
-
Oven
No.
37
47
X57
19
29
39
49
X59
2
12
22
32
42
X52
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0820
0828
0840
O91 2
0946
0955
1005
1018
1029
1040
1053
1105
1120
1133
1146
Cross-Draft
Velocity
(fpm)
6 5
160
300
120
120
100
150
180
280
310
Fume Hood
Capture
(%)
20
20
20
70
40
90
20
60
10
10
Stack
Opacity
(%)
g 0
60
60
40
40
10
60
10
40
40
Coke Side
Condition
Green
Green
Fire & Smoke
Green
Good
Green
Fire & Smoke
Green
Green
Net Coal
Charged
(Ibs)
34,400
34,350
35,250
32,700
32,550
34,500
34,350
34,700
35,250
34,000
34,250
34,450
34,400
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date: 6/25/75
Atmospheric Pressure
Initial:
RJP
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
X62
4
14
24
34
44
X54
X64
6
16
26
36
46
X56
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1243
1253
1255
1310
1332
1342
1353
1403
1417
1428
1458
1454
1505
1516
Cross-Draft
Velocity
(fpm)
580
620
140
190
60
170
220
180
200
260
200
210
Fume Hood
Capture
(%)
5
20
90
50
50
>90
90
40
60
20
80
>90
Stack
Opacity
CD
100
60
10
60
40
5
10
40
30
60
20
10
•
Coke Side
Condition
Green
Green
Good
Green
Green
Fire & Smoke
Fire & Smoke
Green
Green
Green
Fire & Smoke
Good
Net Coal
Charged
(Ibs)
34.550
34,950
M v v H •»
34,700
34,450
34,200
34,400
34,450
34,350
34,050
34,200
34,500
32,800
34,400
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date: 6/26/75
Atmospheric Pressure 29.74 Initial: TAL
Push
1
2
3
5
6
7
8
9
10
11
12
13
14
15
r
Oven
No.
X56
8
18
9ft
£O
38
48
X58
_ _ _
1
11
21
31
41
X51
X61
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0815
0832
0846
no/\/\
0915
0925
0937
1016
1022
1039
1049
1102
1125
1139
Cross-Draft
Velocity
(fpm)
o cn
100
310
190
270
290
250
310
400
220
90
Fume Hood
Capture
(7.)
/.n
80
40
>90
50
60
90
30
>90
>90
Stack
Opacity
(%)
20
10
30
0
30
10
5
40
5
0
•
Coke Side
Condition
Good
Green
Good
Fire & Smoke
Green
Good
Green
Good
Good
Net Coal
Charged
(Ibs)
32,950
34,850
_____
31,050
33,850
34,550
35,000
34,900
34,750
32,050
32,800
33,000
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6/26/75
Atmospheric Pressure 29.74 Initial:
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
3
13
23
33
43
X53
X63
5
15
25
35
45
X55
7
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1232
1243
1255
1310
1332
1337
1345
1355
1408
1428
1438
1458
1504
1530
Cross-Draft
Velocity
(fpm)
480
330
220
270
280
280
360
250
170
350
400
Fume Hood
Capture
(%)
30
>90
90
90
20
60
90
50
20
80
<10
Stack
Opacity
(%)
40
0
0
0
40
20
0
10
60
10
60 .
Coke Side
Condition
Green
Good
Good
Good
Green
Green
Good
Green
Green
Good
Green
Net Coal
Charged
(Ibs)
32,550
35,500
35,750
35,450
35,600
35,700
33,850
35,100
31,650
35,800
34,650
34,850
33,850
34,450
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date: 6/27/75
Atmospheric Pressure 29.70 Initial: TAL
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
.
Oven
No.
7
17
27
37
47
X57
9
19
29
39
49
X59
2
12
22
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0825
0846
0910
0919
0930
0950
1016
1020
1040
1056
1108
1120
1135
1147
1158
Cross-Draft
Velocity
(fpm)
220
170
240
200
190
240
450
270
Fume Hood
Capture
(7.)
30
20
50
70
80
30
20
30
Stack
Opacity
U)
30
40
0
20
0
30
40
30 .
Coke Side
Condition
Green
Green
Good
Green
Good
Green
Good
Green
Net Coal
Charged
fibs)
36,000
35,700
35,900
34,400
34,600
34,200
33,500
34,800
34,650
34,250
34,750
34,800
33,700
33,500
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date: 6/27/75
Atmospheric Pressure 29.70 Initial:
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
32
42
X52
X62
—
4
14
24
34
44
X54
X64
6
16
26
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1205
1215
1225
1238
1325
1340
1405
1424
1435
1445
1455
1511
1528
1538
Cross-Draft
Velocity
(fpm)
260
350
170
320
Fume Hood
Capture
(%>
<10
90
70
30
Stack
Opacity
(%)
20
10
10
20
.
Coke Side
Condition
Green
Good
Fire & Smoke
Green
Net Coal
Charged
(Ibs)
33.300
32.450
34.700
34.600
33,800
34,350
34,900
33,300
34,250
35,400
33,000
35,100
34,000
34,700
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date: 6/30/75
Atmospheric Pressure 29.82 Initial:
TAL
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
34
44
X54
X64
6
16
26
36
46
X56
_ _ _
8
18
28
38
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0810
0826
0837
0854
0905
0920
0943
0954
1003
1011
1027
1045
1056
1141
Cross-Draft
Velocity
(fpm)
80
200
220
210
300
240
270
230
340
270
310
320
Fume Hood
Capture
(7.)
95
90
20
60
60
70
80
80
20
30
10
Stack
Opacity
(%)
0
5
20
10
10
5
10
10
40
20
50
•
Coke Side
Condition
Good
Fire & Smoke
Green
Fire & Smoke
Fire & Smoke
Fire & Smoke
Fire & Smoke
Good
Green
Green
Green
Net Coal
Charged
(Ibs)
39,100
35,550
29,750
35,350
34,250
32,900
32,850
33,000
_____
34,050
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6/30/75
Atmospheric Pressure 29.82 Initial: TAL
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
48
X58
__
1
11
21
31
41
X51
X61
3
13
23
33
43
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1155
1203
1213
1220
1247
1320
1330
1350
1402
1415
1423
1448
1458
1513
Cross-Draft
Velocity
(fpm)
370
280
390
120
150
230
280
230
80
540
360
Fume Hood
Capture
(%)
95
60
50
30
90
80
<10
60
50
10
60
Stack
Opacity
(7.)
0
30
40
50
0
0
60
30
30
60
20
Coke Side
Condition
Good
Green
Green
Green
Good
Good
Green
Fire & Smoke
Green
Green
Green
Net Coal
Charged
(Ibs)
35,200
33,100
32,000
31,150
33,300
33,400
34,850
34,400
35,800
33,800
33,800
33,450
-------
Date:
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
7/1/75 Atmoaoheric Pressure 29.8 Initial:
Atmospheric Pressure
TAL
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
43
X53
X63
5
15
25
35
45
X55
7
17
27
37
47
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0837
0851
0912
0925
0935
0958
1015
1018
1029
1042
1103
1119
1126
1140
Cross-Draft
Velocity
(fpm)
150
90
140
Fume Hood
Capture
(%)
90
80
10
20
0
Stack
Opacity
c*>
0
0
•
Coke Side
Condition
Good
Good
Green
Good
Green
Net Coal
Charged
(Ibs)
36,100
35,050
35,650
35,850
35,350
35,550
35,800
35,650
35,650
36,000
35,800
35,150
35,850
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7/2/75
Atmospheric Pressure 29.75 Initial: TAL
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
^^^^
4
14
24
34
44
X54
X64
6
16
26
36
46
X56
8
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950 •
1005
1020
1035
1055
1110
1125
1145
Push
Time
0822
0834
0921
0928
0946
0954
1005
1014
1030
1037
1100
1110
1123
1139
Cross-Draft
Velocity
(fpm)
70
125
60
100
150
Fume Hood
Capture
(7.)
95
0
30
30
30
Stack
Opacity
(%)
0
50
40
30
•
Coke Side
Condition
Good
Green
Green
Green
Green
Net Coal
Charged
(Ibs)
38,250
35,650
35,050
35,250
34,900
30,350
35,500
35,400
34,700
34,350
34,800
33,250
34,700
34,350
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7/2/75
Atmospheric Pressure 29.75
Initial:
TAL
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
18
28
38
48
X58
—
1
11
21
31
41
X51
X61
3
13
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1300
1306
1313
1327
1335
1345
1355
1415
1442
1455
1505
1516
1535
1545
Cross-Draft
Velocity
(fpm)
260
350
270
460
360
320
280
480
320
280
Fume Hood
Capture
(%)
80
90
90
20
50
50
90
80
70
60
Stack
Opacity
(%)
10
0
0
50
40
20
5
10
40
20 .
Coke Side
Condition
Good
Good
Good
Green
Green
Green
Good
Fire & Smoke
Green
Green
Net Coal
Charged
(Ibs)
34,750
34,500
34,500
33,300
_ _ _ _ _
34,800
35,000
34,850
34,950
35,100
35,600
35,200
35,150
34,950
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-3-75
Atmospheric Pressure 29.58 Initial:
TAL
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
13
23
33
43
X53
X63
—
5
15
25
35
45
X55
7
17
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0838
0844
0903
0924
0939
0954
1006
1027
1120
1127
1136
1153
1205
1216
Cross-Draft
Velocity
(fpm)
150
220
230
260
320
170
320
Fume Hood
Capture
(%)
95
60
60
50
90
90
30
Stack
Opacity
(%)
0
0
20
20
0
0
60
•
Coke Side
Condition
Good
Good
Fire & Smoke
Green
Good
Good
Green
Net Coal
Charged
(Ibs)
36100
36200
35300
35500
35550
34600
34700
35200
34900
35650
36000
35300
35700
00
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-8-75
Atmospheric Pressure
Initial:
TAL
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
49
X59
2
12
22
32
42
X52
X62
—
4
14
24
34
44
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0820
0832
0922
0928
0945
1006
1017
1033
1043
1056
1141
1200
1213
Cross-Draft
Velocity
(fpm)
0
180
140
170
240
170
260
240
Fume Hood
Capture
(7.)
80
95
80
80
90
80
60
(90)
(90)
(90)
Stack
Opacity
(%)
10
0
0
0
0
0
20
0
0
0
Coke Side
Condition
Good
Good
Good
Good
Good
Good
Green
(pood)
(Good)
(pood)
Net Coal
Charged
(Ibs)
33250
33850
34550
34850
32400
33850
34900
34350
32000
34250
34000
30900
33450
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-8-75
Atmospheric Pressure
Initial:
TAL
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
X54
X64
6
16
26
36
46
X56
8
18
28
38
48
X58
—
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1245
1252
1305
1320
1335
1345
1403
1421
1440
1449
1501
1510
1521
1530
Cross-Draft
Velocity
(fpm)
180
380
220
360
300
350
240
290
250
300
Fume Hood
Capture
(7.)
90
90
80
70
90
80
80
90
60
95
Stack
Opacity
(%)
0
0
10
10
0
5
5
0
30
0
Coke Side
Condition
Rood
Good
Fire & Smoke
Fire & Smoke
Good
Good
Good
Fire & Smoke
Green
Good
Net Coal
Charged
(Ibs)
^Tfinn
35050
34800
33200
33900
_
34350
28050
32850
35050
34200
33150
34400
33750
o
I
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-9-75
Atmospheric Pressure 29.40 Initial: TAL
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
__ij^
1
11
21
31
41
X51
X61
3
13
23
33
43
X53
X63
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0825
0834
0845
0910
0935
0950
1015
1028
1038
1046
1057
1105
1112
1125
Cross-Draft
Velocity
(fpm)
160
180
260
430
220
180
210
380
190
260
180
Fume Hood
Capture
m
80
60
20
90
95
80
10
50
40
20
80
Stack
Opacity
(%)
10
10
50
0
0
20
70
50
30
0
Coke Side
Condition
Fire & Smoke
Fire & Smoke
Green
Good
Good
Fire & Smoke
Green
Green
Green
Green
Good
Net Coal
Charged
(lbs>
37700
38400
38500
35650
ifinsn
35450
34900
34900
35200
34850
34450
35750
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-9-75
Atmospheric Pressure 29.40 Initial:
TAL
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
5
15
25
35
45
X55
7
17
27
37
47
X57
9
19
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1207
1220
1232
1250
1302
1344
1357
1408
1420
1428
1435
1500
1513
1518
Cross-Draft
Velocity
(fpm)
200
340
330
420
250
380
410
Fume Hood
Capture
(%)
70
10
60
5
95
60
80
Stack
Opacity
(%)
10
80
10
80
5
20
0
.
Coke Side
Condition
Good
Green
Fire & Smoke
Green
Good
Fire & Smoke
Good
Net Coal
Charged
(Ibs)
35100
35700
35150
35050
34950
34800
34900
34300
34600
34700
35300
—
34850
—
o
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-10-75
Atmospheric Pressure 29.34 Initial:
TAL
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
19
29
39
49
X 59
2
12
22
32
42
X 52
X 62
_
4
14
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0811
0841
0858
0910
0925
0940
0953
1017
1024
1045
1057
1107
1120
1130
Cross-Draft
Velocity
(fpm)
250
230
280
270
290
190
210
300
Fume Hood
Capture
(%)
95
90
50
90
95
95
80
Stack
Opacity
(%)
0
5
30
5
0
0
5
.
Coke Side
Condition
Good
Good
Green
Good
Fire & Smoke
Good
Good
Good
Green
Net Coal
Charged
(Ibs)
35300
34800
32700
33000
33500
35000
36650
33100
34150
34150
34500
33750
33900
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-10-75
Atmospheric Pressure 29.34 Initial:
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
24
34
44
X54
X64
6
16
26
36
46
X56
8
18
28
38
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1207
1221
1230
1242
1252
1300
1325
1337
1358
1410
1424
1436
1452
1505
1518
Cross-Draft
Velocity
(fpm)
240
360
820
670
570
520
730
850
910
580
Fume Hood
Capture
(%)
70
70
50
50
70
90
10
40
50
Stack
Opacity
(%)
10
20
30
20
10
0
60
40
30
.
Coke Side
Condition
Good
Fire & Smoke
Green
Fire & Smoke
Fire & Smoke
Fire & Smoke
Good
Green
Green
Green
Net Coal
Charged
(Ibs)
M*
^_
33850
34350
33950
34600
34650
33800
33550
35300
35700
35150
35550
34950
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-14-75
Atmospheric Pressure
Initial:
RJP
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
17
27
37
47
X57
9
19
29
39
49
X59
2
12
22
32
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0815
0825
0840
0907
0923
0932
0950
1022
1033
1049
1058
1110
1120
1132
1143
Cross-Draft
Velocity
(fpm)
250
210
160
350
300
510
490
270
450
210
460
350
610
890
700
Fume Hood
Capture
(%)
90
80
80
20
80
20
60
60
60
0
30
80
50
0
0
Stack
Opacity
(%)
5
5
10
0
10
60
20
0
30
0
60
5
15
0
0
Coke Side
Condition
Good
Good
Good
Green
Good
Green
Fire & Smoke
Good
Fire & Smoke
Green
Green
Good
Fire & Smoke
Fire & Smoke
Fire & Smoke
Net Coal
Charged
(Ibs)
33600
32500
32700
32850
34450
32350
31850
33000
33800
33400
31950
32100
33350
32950
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-14-75
Atmospheric Pressure
Initial: Rjp
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
42
X52
X62
—
4
14
24
34
44
X54
X64
6
16
26
36
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1230
1245
1255
1318
1338
1347
1358
1410
1424
1431
1445
1502
1514
1526
Cross-Draft
Velocity
(fpm)
620
550
900
350
390
540
1100
330
380
Fume Hood
Capture
(%)
50
30
50
80
80
80
80
50
50
Stack
Opacity
(%)
40
50
40
5
5
0
5
40
20
.
Coke Side
Condition
Fire & Smoke
Green
Fire & Smoke
Good
Good
Good
Good
Fire & Smoke
Fire & Smoke
Net Coal
Charged
(Ibs)
32900
33100
^^^
_
33150
32700
30400
33050
33700
33150
32550
32850
31450
o
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-15-75
Atmospheric Pressure
Initial:
TAL
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
-
Oven
No.
36
46
X56
8
18
28
38
48
X58
^^^^
1
11
21
31
41
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0817
0830
0847
0920
0929
0946
0958
1027
1036
1054
1104
1125
1140
1156
Cross-Draft
Velocity
(fpm)
100
250
120
150
160
210
190
220
190
190
220
610
Fume Hood
Capture
(7.)
90
80
60
90
90
95
95
95
20
80
75
30
Stack
Opacity
(%)
0
0
20
0
20
0
0
0
40
0
10
30 •
Coke Side
Condition
Good
Good
Fire & Smoke
Good
Fire & Smoke
Good
Good
Good
Green
Good
Good
Green
Net Coal
Charged
(Ibs)
33300
32950
33700
33500
34000
33750
33650
31950
34650
33300
32250
34250
32450
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-15-75
Atmospheric Pressure
Initial: TAL
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
X51
X61
3
13
23
33
43
X53
X63
5
15
25
35
45
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1300
1306
1325
1333
1345
1404
1409
1425
1440
1455
1507
1530
1535
1547
Cross-Draft
Velocity
(fpm)
250
270
510
240
270
580
Fume Hood
Capture
(7.)
90
60
80
90
90
95
Stack
Opacity
(%)
0
10
5
5
0
0
Coke Side
Condition
Good
Fire & Smoke
Good
Good
Good
Good
Net Coal
Charged
(Ibs)
33750
33550
33050
35050
34350
32150
34250
33050
33700
—
33450
33450
32600
33000
32750
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-16-75
Atmospheric Pressure 29.70 Initial:
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
45
X55
7
17
27
37
47
X57
9
19
29
39
49
X59
2
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0824
0840
0853
0934
0941
0952
1006
1035
1050
1109
1123
1137
1150
1203
1217
Cross-Draft
Velocity
(fpm)
150
170
140
270
160
120
170
420
260
150
320
370
420
490
360
Fume Hood
Capture
(%)
90
90
30
90
80
95
80
90
20
95
95
95
95
90
Stack
Opacity
(%)
0
10
40
0
10
0
10
5
40
0
0
0
0
5
Coke Side
Condition
Good
Good
Green
Good
Fire & Smoke
Good
Fire & Smoke
Good
Green
Good
Good
Good
Good
Good
Net Coal
Charged
(Ibs)
«•
35450
33400
35700
35650
33800
_
35850
34450
33500
34200
35250
35550
35400
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-16-75
Atmospheric Pressure 29.70 Initial:
TAL
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
12
22
32
42
X52
X62
_
4
14
24
34
44
X54
X64
6
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1225
1233
1317
1330
1340
1348
1403
1422
1432
1440
1449
1502
1511
1535
Cross-Draft
Velocity
(fpm)
710
450
430
540
350
410
Fume Hood
Capture
(7.)
95
95
95
95
95
95
Stack
Opacity
(%)
0
0
0
0
0
0
.
Coke Side
Condition
Good
Good
Good
Good
Good
Good
Net Coal
Charged
(Ibs)
35600
34650
34150
34000
32150
33200
33200
33900
34300
33400
33900
34550
32050
35000
I
oo
o
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-17-75
Atmospheric Pressure
Initial:
RJP
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
6
16
26
36
46
X56
8
18
28
38
48
X58
—
1
11
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0810
0824
0840
0850
0900
0910
0958
1010
1022
1034
1045
1056
1121
1132
Cross-Draft
Velocity
(fpm)
240
210
440
400
310
320
360
170
Fume Hood
Capture
(7.)
70
80
50
70
20
60
50
70
Stack
Opacity
(7.)
10
5
35
5
70
10
5
10
•
Coke Side
Condition
Good
Good
Fire & Smoke
Good
Green
Good
Good
Good
Net Coal
Charged
fibs)
35250
34100
34650
34300
34450
35000
34450
34350
35200
32950
34800
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-17-75
Atmospheric Pressure
Initial:
RJP
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
21
31' ~
41
X51
X61
3
13
23
33
43
X53
X63
—
5
15
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1230
1237
1245
1300
1315
1326
1342
1355
1410
1424
1441
1454
1514
1528
Cross-Draft
Velocity
(fpm)
720
630
420
240
260
700
420
Fume Hood
Capture
(%)
'
70
20
70
30
70
90
20
Stack
Opacity
(7.)
10
45
5
45
10
5
70 •
Coke Side
Condition
Good
Green
Good
Green
Good
Good
Green
Net Coal
Charged
(Ibs)
35850
34550
35150
33800
34450
34300
34450
34200
34850
34300
34400
33250
35700
35900
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-18-75
Atmospheric Pressure
Initial:
RJP
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
15
25
35
45
X55
7
17
27
37
47
X57
9
19
29
39
Schedule
Time
0800
0816
0832
0848
0904
0920
0936
0952
1008
1024
1040
1056
1112
1128
1144
Push
Time
0805
0830
0840
0852
0907
0922
1017
1024
1030
1039
1048
1142
1150
1205
1215
Cross-Draft
Velocity
(fpm)
410
450
500
750
320
410
940
650
430
660
440
Fume Hood
Capture
(7.)
50
30
90
80
80
90
80
90
20
80
80
Stack
Opacity
(%)
20
45
5
5
5
5
10
5
60
5
5 '
Coke Side
Condition
Fire & Smoke
Green
Good
Good
Good
Good
Good
Good
Green
Good
Good
Net Coal
Charged
(Ibs)
35450
...
— — —
36200
3&finn
35700
34800
35200
34750
35000
34350
33500
35300
34750
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-18-75
Atmospheric Pressure
Initial:
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
49
X59
2
12
22
32
42
X52
X62
-
4
14
24
34
44
Schedule
Time
1200
1216
1232
1248
1304
1320
1336
135-2
1408
1424
1440
1456
151 2
1528
1544
Push
Time
1220
1227
1239
1250
1304
1315
1326
1332
1353
1425
1435
1440
1454
1529
Cross-Draft
Velocity
(fpm)
950
510
430
520
Fume Hood
Capture
(7.)
90
80
50
10
Stack
Opacity
(7.)
0
5
15
80
.
Coke Side
Condition
Good
Good
Fire & Smoke
Green
Net Coal
Charged
fibs)
34500
34650
34400
34700
34700
34500
35600
34750
34600
34850
34650
34350
35200
34250
o
I
00
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-21-75
Atmospheric Pressure
Initial:
RJP
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
14
24
34
44
X54
X64
6
16
26
36
46
X56
8
18
28
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0804
0825
0845
0904
0912
0920
0934
0943
0950
0955
1013
1025
1047
1059
1110
Cross-Draft
Velocity
(fpm)
680
420
360
400
Fume Hood
Capture
(7.)
20
5
20
30
Stack
Opacity
(%)
20
90
60
60 •
Coke Side
Condition
Fire & Smoke
Green
Green
Fire & Smoke
Net Coal
Charged
(Ibs)
34750
35950
35450
33800
35100
34750
36700
35700
34400
37550
36600
36750
34350
34500
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-21-75
Atmospheric Pressure 29.48 Initial:
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
38
48
X58
__
1
11
21
31
41
X51
X61
3
13
23
33
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1210
1215
1225
1236
1243
1300
1356
1409
1415
1435
1440
1454
1507
1517
Cross-Draft
Velocity
(fpm)
480
420
450
420
480
450
470
Fume Hood
Capture
(7.)
40
10
70
50
5
5
90
Stack
Opacity
m
20
80
5
50
100
100
0 .
Coke Side
Condition
Fire & Smoke
Green
Good
Fire & Smoke
Green
Green
Good
Net Coal
Charged
(Ibs)
34950
34450
35100
35000
34750
34850
36150
30700
36100
35250
36200
34960
35850
34050
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-22-75
Atmospheric Pressure 29.5 Initial:
_RJP
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
33
43
X53
X63
__
5
15
25
35
45
X55
7
17
27
37
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0811
0823
0845
0855
0906
1020
1035
1051
1102
Cross-Draft
Velocity
(fpm)
270
330
370
580
170
490
320
200
130
Fume Hood
Capture
(7.)
0
10
10
80
80
10
40
40
70
Stack
Opacity
(7.)
5
65
25
5
5
70
40
40
5
•
Coke Side
Condition
Good
Green
Fire & Smoke
Good
Good
Green
Fire & Smoke
Fire & Smoke
Good
Net Coal
Charged
(Ibs)
36450
37750
35300
34350
34850
35250
35200
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-22-75
Atmospheric Pressure 29.5 Initial:
RJP
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
47
X57
9
19
29
39
49
X59
2
12
22
32
42
X52
X62
-
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1236
1247
1255
1306
1342
1359
1415
1445
1454
Cross-Draft
Velocity
(fpm)
510
570
360
390
740
370
780
520
460
Fume Hood
Capture
(7.)
80
80
20
20
10
90
10
10
40
Stack
Opacity
(%)
5
5
80
60
50
0
80
80
50
Coke Side
Condition
Good
Good
Green
Fire & Smoke
Green
Good
Green
Green
Fire & Smoke
Net Coal
Charged
(Ibs)
35300
36250
34,950
35350
35200
35350
35300
33850
35000
34800
34700
34800
34900
35050
35600
00
oo
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-23-75
Atmospheric Pressure
Initial:
GJS
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
X62
--
4
14
24
34
44
X54
X64
6
16
26
36
46
X56
Schedule
Time
0800
O815
0830
OS50
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0922
0936
0947
0957
Cross-Draft
Velocity
(fpm)
400
400
500
450
Fume Hood
Capture
(7.)
80
60
80
40
Stack
Opacity
(7.)
0
20
0
20
•
Coke Side
Condition
Good
Green
Good
Fire & Smoke
Net Coal
Charged
(Ibs)
34750
35200
35100
35900
35650
35450
36000
34150
35400
35600
34950
35000
34100
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7/23/75
Atmospheric Pressure
Initial: GJS
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
8
18
28
38
48
X58
—
1
11
21
31
41
X51
X61
3
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1303
1314
1326
1337
Cross-Draft
Velocity
(fpm)
425
600
500
380
Fume Hood
Capture
m
80
80
40
80
Stack
Opacity
(%)
0
0
20
0
Coke Side
Condition
Good
Good
Fire & Smoke
Good
Net Coal
Charged
(Ibs)
34950
35200
35450
35200
35050
34700
33750
34300
34950
33900
35250
35150
35150
—
VO
O
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
9-3-75
Atmospheric Pressure 29.4 Initial:' Rjp
Push
16
17
IS
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
36
46
X56
8
18
28
38
48
X58
—
1
11
21
31
41
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1324
1336
1343
Cross-Draft
Velocity
(fpm)
660
170
Fume Hood
Capture
(%)
80
45
Stack
Opacity
(%>
30
50
•
Coke Side
Condition
Good
Fire & Smoke
Net Coal
Charged
(Ibs)
o
VO
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
9-4-75
Atmospheric Pressure
Initial:
R.TP
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
41
X51
X61
3
13
23
33
43
X53
X63
—
5
15
25
35
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0812
0829
0851
0901
0939
0953
Cross-Draft
Velocity
(fpm)
Calm
Calm
210
Calm
430
Fume Hood
Capture
(7.)
0
40
90
5
50
85
Stack
Opacity
(%)
0
40
10
60
40
20
Coke Side
Condition
F i rp ft Smnkp
Fire & Smoke
Good
Green
Fire & Smoke
Good
Net Coal
Charged
(Ibs)
o
I
VO
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
9-4-75
Atmospheric Pressure
Initial: RJP
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
45
X55
7
17
27
37
47
X57
9
19
29
39
49
X59
2
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1300
1306
1314
1325
1354
1403
1410
1425
1434
1503
1515
1527
Cross-Draft
Velocity
(fpm)
410
720
180
220
310
Fume Hood
Capture
(%)
15
15
15
Stack
Opacity
(7.)
65
60
80 •
Coke Side
Condition
Fire & Smoke
Good
Fire & Smoke
Fire & Smoke
Green
Fire & Smoke
Good
Green
Green
Green
Green
Green
Good
Green
Net Coal
Charged
(Ibs)
n
\o
OJ
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date: 9-5-75
Atmospheric Pressure 29.52 Initial:
RGK
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
-
32
42
X52
X62
_
4
14
24
34
44
X54
X64
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0904
0916
0930
Cross-Draft
Velocity
(fpm)
222
121
150
Fume Hood
Capture
(%)
70
70
80
Stack
Opacity
(7.)
5
5
<5
•
Coke Side
Condition
Fire & Smoke
Fire & Smoke
Good
Net Coal
Charged
dbs)
to
.p-
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
9/5/75
Atmospheric Pressure 29.38 Initial:
RGK
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
6
16
26
36
46
X56
8
18
28
38
48
X58
—
1
11
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1250
1306
1319
1331
Cross-Draft
Velocity
(fpm)
502
750
1000
1100
Fume Hood
Capture
m
20
30
70
50
Stack
Opacity
a>
50
40
15
30
•
Coke Side
Condition
Green
Green
Fire & Smoke
Green
-
Net Coal
Charged
(Ibs)
o
vO
Ui
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
9-8-75
Atmospheric Pressure
Initial:
RJG
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
X58
^^^
1
11
21
31
41
X51
X61
3
13
23
33
43
X53
Schedule
Time
0800
0815
0830
0850
0905
0920
0933
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
1003
1036
1102
1110
1123
1135
1151
Cross-Draft
Velocity
(fpm)
440
973
728
678
900
693
642
Fume Hood
Capture
(%)
90
20
20
10
75
80
Stack
Opacity
<%)
5
60
40
70
<5
5 .
Coke Side
Condition
•
Good
Fire & Smoke
Fire & Smoke
Green
Good
Good
Good
Net Coal
Charged
(Ibs)
vo
Oi
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
9/8/75
Atmospheric Pressure
Initial:
RJG
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
X63
^^^
5
15
25
35
45
X55
7
17
27
37
47
X57
9
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
_
1326
1337
1344
1403
1411
1429
Cross-Draft
Velocity
(fpm)
1127
892
1034
892
920
1006
Fume Hood
Capture
(%)
80
20
80
20
75
Stack
Opacity
(%)
5
60
5
50
15
•
Coke Side
Condition
Good
Green
Good
Green
Fire & Smoke
Fire & Smoke
Net Coal
Charged
(Ibs)
\o
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
9/9/75
Atmospheric Pressure
Initial:
RJG
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
9
19
29
39
49
X59
2
12
22
32
42
X52
X62
—
4
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0823
0918
0931
0959
1022
1045
Cross-Draft
Velocity
(fpm)
300
577
360
568
Fume Hood
Capture
(7.)
80
—
—
70
—
Stack
Opacity
(7.)
5
_
—
20
—
•
Coke Side
Condition
Good
Fire & Smoke
Fire & Smoke
Fire & Smoke
Fire & Smoke
Net Coal
Charged
(Ibs)
o
I
VO
00
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date: 9-9-75
Atmospheric Pressure
Initial: RJG
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
14
24
34
44
X54
X64
6
16
26
36
46
X56
8
18
28
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1405
Cross-Draft
Velocity
(fpm)
450
450
450
450
450
Fume Hood
Capture
m
Stack
Opacity
(i)
"
•
Coke Side
Condition
Net Coal
Charged
fibs)
o
I
vo
to
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
9-10-75
Atmospheric Pressure
Initial:
RJG
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
28
38
48
X58
_
1
11
21
31
41
X51
X61
3
13
23
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0822
0835
1005
1017
1034
1155
Cross-Draft
Velocity
(fpm)
130
80
110
80
170
130
Fume Hood
Capture
(I)
90
25
40
80
40
10
Stack
Opacity
(I)
<5
50
10
50
75 .
Coke Side
Condition
Good
Fire & Smoke
Fire & Smoke
Good
Fire & Smoke
Green
Net Coal
Charged
(Ibs)
o
o
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
9-10-75
Atmospheric Pressure
Initial:
RJG
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
33
43
X53
X63
—
5
15
25
35
45
X55
7
17
27
37
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1212
1224
1406
1414
1427
Cross-Draft
Velocity
(fpm)
160
270
170
380
420
Fume Hood
Capture
(7.)
80
80
10
90
10
Stack
Opacity
(%)
5
5
70
5
65
-
Coke Side
Condition
Good
Good
Green
Good
Green
Net Coal
Charged
(Ibs)
o
I-"
o
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date: 9/11/75
Atmospheric Pressure 29. 2 Initial: RJG
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
.
Oven
No.
37
47
x57
9
19
29
39
49
x59
2
12
22
32
42
X52
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0840
0851
0908
1040
1051
1117
Cross-Draft
Velocity
(fpm)
200
120
50
130
125
200
Fume Hood
Capture
(%)
15
80
25
25
30
10
Stack
Opacity
(%)
70
5
50
65
50
70
.
Coke Side
Condition
green
good
green
•
fire Smoke
fire &
smoke
green
Net Coal
Charged
(Ibs)
o
NJ
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
9/11/75
Atmospheric Pressure 29.2 Initial:
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
x62
_ _ _
4
14
24
34
44
X54
x64
6
16
26
36
46
x56
Schedule
Time
1200
1215
1230
1250
1305
1320
1335
1350
1405
1425
1440
1450
1510
1530
1545
Push
Time
1405
1417
1424
Cross-Draft
Velocity
(fpm)
130
150
120
Fume Hood
Capture
(%)
50
90
50
Stack
Opacity
(%)
40
5
30
Coke Side
Condition
fire & smoke
good
fire & smoke
Net Coal
Charged
(Ibs)
o
I
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date: 9/12/75
Atmospheric Pressure
Initial: RJG
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
x56
8
18
28
38
48
x58
_ _ _ _
1
11
21
31
41
X51
x61
Schedule
Time
0800
0815
0830
0850
0905
0920
0935
0950
1005
1020
1035
1055
1110
1125
1145
Push
Time
0828
0956
1009
1225
1238
Cross-Draft
Velocity
(fpm)
490
420
490
890
1300
Fume Hood
Capture
(%)
75
50
70
50
75
Stack
Opacity
(%)
5
30
10
20
5
Coke Side
Condition
good
fire & smoke
fire & smoke
fire & smoke
good
Net Coal
Charged
(Ibs)
CD
t->
o
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
9/15/75
Atmospheric Pressure 29.70 Initial:
RGK
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
45
x55
7
17
27
37
47
x57
9
19
29
39
49
Schedule
Time
0800
0815
0825
0848
0904
0920
0936
0952
1008
1024
1040
1056
1112
1128
1200
Push
Time
0825
0955
1002
1010
Cross-Draft
Velocity
(fpm)
158
420
516
. 427
Fume Hood
Capture
m
70
15
30
90
Stack
Opacity
(I)
5
50
30
5
•
Coke Side
Condition
fire and
smoke
green
green
good
Net Coal
Charged
(Ibs)
o
U1
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
9/15/75
Atmospheric Pressure 29.7
Initial: RGK
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
x59
2
12
22
32
42
x52
x62
4
14
24
34
X61
44
Schedule
Time
1216
1232
1248
1250
1304
1336
1352
1408
1424
1440
1456
1512
1528
1544
Push
Time
1223
1226
1259
1324
1425
1450
1456
Cross-Draft
Velocity
(fpm)
828
542
797
0
240
388
350
Fume Hood
Capture
(%)
80
60
20
20
80
85
60
Stack
Opacity
(%)
25
15
40
30
10
5
30
•
Coke Side
Condition
lire and
smoke
;reen
green
green
good
good
fire and
smoke
Net Coal
Charged
(Ibs)
-------
DAILY LOG OF FUME HOOD PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
9/16/75
Atmospheric Pressure 29.51 Initial:
RGK
Push
1*
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
Oven
No.
X54
X64
6
16
26
36
46
X56
X66
8
18
28
38
48
X58
1
Schedule
Time
0745
0808
0824
0880
0856
0912
0928
1044
1000
1016
1032
1048
1004
1120
1136
1152
Push
Time
0834
0848
0855
Cross-Draft
Velocity
(fpm)
315
196
196
Fume Hood
Capture
(7.)
80
70
80
Stack
Opacity
(%)
20
30
5
Coke Side
Condition
good
fire and
smoke
good
Net Coal
Charged
(Ibs)
o
Last push of previous shift,
-------
APPENDIX H
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
This appendix contains all field data pertaining to the
scrubber operating characteristics recorded when the Clayton
engineer-observer was on-site and not recording fume hood
performance data. Because these data are somewhat redundant
with the scrubber inlet source sampling data, and because
scrubber operating parameters are quite constant from day to
day, these data are not recorded for each push.
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-16-74
Atmospheric Pressure: 30.2 Initial: RJP
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
IS
,
Oven
Mo.
44
X54
X64
6
16
26
36
46
X56
8
18
28
38
48
X58
Push
Time
0906
1004
1016
1026
1038
1056
1103
1114
1128
1138
• Inlet Conditions
Dry
Bulb
(°F)
178
158
158
198
192
Wet
Bulb
(°F)
108
106
106
114
109
Static
Pressure
<"HaO)
-4.5
-5.5
-5.5
-5.0
-5.0
Velocity
Pressure
<"H20)
1.40
1.50
1.50
1.35
1.40
•
Throat Conditions
Pressure
Drop
<"H20)
41
40
41
42
41
Water
Pressure
(psl)
41
41
41
41
41
Water
Temp.
(°F)
84
Outlet Conditions
Dry
Bulb
(°F)
74
82
82
80
82
Wet
Bulb
(°F)
72
80
80
78
80
Static
Pressure
C'H20)
-59.8
-63.9
-59.8
-59.8
-62.6
Reclrculated
Water
Flow
(gpm)
860
860
860
860
860
860
860
860
860 -
860
Fan
Motor
Current
(amp)
240
240
240
240
240
240
240
240
240
240
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-16-74
Atmospheric Pressure: 30.2 Initial: Rjp
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
— —
1
11
21
31
41
X51
X61
3
13
23
33
43
X53
X63
Push
Time
1242
1252
1303
1314
1328
1340
1400
1407
1420
1432
1443
1453
Inlet Conditions
Dry
Bulb
<°F>
210
200
184
.
210
210
210
Wet
Bulb
<°F>
110
109
106
112
89
106
Static
Pressure
C'H^O)
•
-4.5
-2.0
-4.5
-4.5
-2.0
-4.5
Velocity
Pressure
<"H20)
1.35
0.12
1.35
1.35
0.12
1.50
Throat Conditions
Pressure
Drop
<"H20>
41
41
41
41
41
41
Water
Pressure
(psi)
41
41
41
41
41
41
Water
Temp .
<°F)
84
Outlet Conditions
Dry
Bulb
<°F)
82
84
82
84
85
84
Wet
Bulb
(°F)
80
80
80
81
82
82
Static
Pressure
("HaO)
-61.2
-59.8
.59.8
-63.9
-63.9
-63.9
Recirculated
Water
Flow
(gpn)
860
860
860
860
860
860
860
860
860
860
860
860
Fan
Motor
Current
(amp)
240
240
240
120
240
240
240
240
240
240
120
240
P3
N>
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-19-74
Atmospheric Pressure: 30.1 Initial:
MRP
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
t*
Oven
Mo.
5
15
25
35
45
X55
7
17
27
37
Push
Time
0935
0948
1000
1010
1025
1035
1045
1055
11X0
1125
• Inlet Conditions
Dry
Bulb
CF>
220
190
200
180
140
140
190
.
Wet
Bulb
(°F)
160
160
160
100
85
85
106
Static
Pressure
<"HZ0)
•
-4.5
-5.0
-5.0
-1.8
-1.8
-1.8
-1.8
Velocity
Pressure
("HaO)
1.35
1.50
1.35
0.09
0.09'
0.09
0.10
Throat Conditions
Pressure
Drop
<"H20)
41
41
5
Water
Pressure
(psi)
41
41
41
41
41
41
41
41
Water
Temp .
<°F)
78
79
Outlet Conditions
Dry
Bulb
(°F)
80
86
76
Wet
Bulb
<"F)
77
79
72
Static
Pressure
<"H20)
-61.2
-59.8
-10.9
Recirculated
Water
Flow
(gpm)
860
860
860
860
860
860
860
860 •
860
860
Fan
Motor
Current
(amp)
240
240
240
120
120
120
240
240
120
120
35
i
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-19-74
Atmospheric Pressure: 30.i Initial:
NRD
Push
.16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
X59
2
12
22
32
42
X52
X62
Push
Time
1420
1445
1500
1515
1533
1543
Inlet Conditions
Dry
Bulb
(°F)
160
210
200
190
.
Wet
Bulb
<°F)
110
106
104
104
Static
Pressure
<"HaO)
•
-1.8
-4.5
-1.8
-1.8
Velocity
Pressure
("H20)
0.1
1.35
0.12
0.12
Throat Conditions
Pressure
Drop
<"H20)
5
41
41
Water
Pressure
(psl)
41
41
41
Water
Temp .
<°F)
.
80
Outlet Conditions
Dry
Bulb
<"F)
82
82
88
1
Wet
Bulb
<°F)
72
72
76
Static
Pressure
<"HZ0)
-12.2
-54.4
-54.4
Reclrculated
Water
Flow
(gpm)
860
860
860
860
860
860
Fan
Motor.
Current
(amp)
120
240
240
240
120
120
33
J>
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-21-74
Atmospheric Pressure: 30.3 Initial: MRP
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
.
Oven
Mo.
3
13
23
33
43
X53
X63
—
5
15
25
35
45
X55
7
Push
Time
0815
0826
0846
0906
0927
0937
0950
1000
1020
1033
1047
1057
1105
1115
• Inlet Conditions
Dry
Bulb
(°F)
210
200
180
180
206
186
Wet
Bulb
CF)
120
132
104
104
140
104
Static
Pressure
<"HaO)
4.5
•4.5
4.5
1.8
4.5
1.8
Velocity
Pressure
<"HaO)
1.35
1.35
1.35
0.10
1.35
0.08
Throat Conditions
Pressure
Drop
<"H20)
6
6
6
41
41
6
6
41
Water
Pressure
(psi)
41
41
41
41
41
41
41
41
41
41
41
41
41
41
Water
Temp.
<°F)
76
78
Outlet Conditions
Dry
Bulb
CF)
79
80
79
84
84
82
82
84
Wet
Bulb
(°F)
78
76
77
80
79
79
78
80
Static
Pressure
("H,0)
6.8
6.8
6.8
61.2
61.2
6.8
6.8
61.2
Recirculated
Water
Flow
(gpm)
860
860
860
860
860
860
860
•
860
860
860
860
860 •
860
860
Fan
Motor
Current
(amp)
240
240
240
120
120
120
120
240
240
240
120
120
120
240
PC
m
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-21-74
Atmospheric Pressure: 30.3 Initial:
MRP
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
17
27
37
47
X57
9
19
29
39
49
X59
2
12
22
32
Push
Time
1209
1215
1225
1245
1306
1317
1327
1342
1401
1412
1420
1434
1440
1458
1517
Inlet Conditions
Dry
Bulb
(°F)
204
160
180
168
225
218
Wet
Bulb
(°F)
106
104
104
102
104
103
Static
Pressure
(MHtO)
1.8
1.8
1.8
1.8
4.5
4.5
Velocity
Pressure
("H20)
0.1
0.1
0.1
0.1
1.35
1.35
Throat Conditions
Pressure
Drop
(MH20)
6
41
41
41
41
6.5
6.5
41
41
Water
Pressure
(psi)
41
41
41
41
41
41
41
41
41
41
41
41
41
41
41
Water
Temp.
<°F)
79
79
.
Outlet Conditions
Dry
Bulb
(°F)
82
84
86
84
86
82
84
86
81
Wet
Bulb
<°F)
79
60
79
79
82
78
78
82
74
Static
Pressure
("H*0)
6.8
61.2
61.2
61.2
58.5
10.9
10.9
61.2
61.2
Recirculated
Water
Flow
(gpm)
860
860
860
860
860
860
860
860
860
flfiO
860
ftftn
860
860
860
Fan
Motor
Current
(amp)
120
240
240
120
120
240
240
120
120
120
120
240
240
240
240
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Data:
8-22-74
Atmospheric Pressure: 30.2 Initial:
MRP
Push
1
2
3
4
S
6
7
8
9
10
11
12
13
14
15
.
Oven
No.
32
42
X52
X62
—
4
14
24
34
44
X54
X64
6
16
26
Push
Time
0813
0843
0903
0920
0931
0948
1003
1021
1043
1053
1108
1120
1131
1142
• Inlet Conditions
Dry
Bulb
CF)
170
160
144
124
210
205
184
187
164
Wet
Bulb
CF)
92
94
93
86
105
105
96
104
97
Static
Pressure
<"H40)
1.8
' 1.8
1.8
1.8
4.5
4.5
5.0
1.8
1.8
Velocity
Pressure
("H20)
0.1
0.1
0.1
0.1
1.35
1.35
1.35
0.1
0.1
Throat Conditions
Pressure
Drop
("H20)
6
6
41
41
41
Water
Pressure
(P8i)
41
41
41
41
41
41
41
41
41
Water
Temp.
<°F)
75
76
Outlet Conditions
Dry
Bulb
CF)
79
79
84
83
84
Wet
Bulb
CF)
78
75
78
78
79
Static
Pressure
C'HiO)
10.9
10.9
10.9
58.5
61.2
61.2
Recirculated
Water
Flow
(gpo)
860
860
860
860
860
860
860
860
860
860
860
860 '
860
860
Fan
Motor
Current
(amp)
120
120
120
120
240
240
240
120
120
120
120
240
240
240
33
-j
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-22-74
Atmospheric Pressure: 30.2 Initial:
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
36
46
X56
8
18
28
38
48
X58
—
1
11
21
31
41
Push
Time
1151
1242
Inlet Conditions
Dry
Bulb
<°F)
Wet
Bulb
(°F)
Static
Pressure
<"HaO)
•
•
Velocity
Pressure
C'H20)
Throat Conditions
Pressure
Drop
("H20)
6
Water
Pressure
(Psl)
41
Water
Temp.
<-F)
Outlet Conditions
Dry
Bulb
<°F)
90
Wet.
Bulb
<°F)
77
Static
Pressure
<"HtO)
10.8
Recirculated
Water
Flow
(gpn)
860
Fan
Motor
Current
(amp)
120
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
SB
i
oo
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-23-74
Atmospheric Pressure: 30.1 Initial:
MRP
Piish
1
2
3
4
5
6
7
8
9
10
11
12
13
14
IS
Oven
Mo.
41
X51
xfil
3
13
23
33
43
X53
X63
—
5
15
25
35
Push
Time
1033
1043
1055
1112
1120
1135
• Inlet Conditions
Dry
Bulb
<°F)
208
198
201
180
.
Wet
Bulb
<°F)
114
99
104
100
Static
Pressure
<"HaO)
4.5
5.0
4.5
1.8
Velocity
Pressure
<"H20)
•
1.35
1.35
1.35
0.1
Throat Conditions
Pressure
Drop
<"H20)
41
41
Water
Pressure
(psl)
41
41
Water
Temp .
<°F)
77
Outlet Conditions
Dry
Bulb
(°P>
88
84
Wet
Bulb
(°F>
79
79
•
Static
Pressure
<"H,0>
58.5
58.5
Reclrculated
Water
Flow
(gP«)
860
860
860
860'
860
860
Fan
Motor
Current
(amp)
240
240
240
240
240
120
re
\O
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-23-74
Atmospheric Pressure: 30.1 Initial: MRP
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
45
X55
7
17
27
37
47
X57
9
19
29
39
49
K59
2
Push
Time
1123
1130
1141
1249
1258
1322
1338
1356
1422
1430
1443
1454
1506
1528
1550
Inlet Conditions
Dry
Bulb
<°F)
300
191
202
160
160
125
.
Wet
Bulb
<°F)
125
140
130
104
98
85
Static
Pressure
("HiO)
•
4.5
4.5
4.5
1.8
1.8
1.8
Velocity
Pressure
<"1UO)
1.35
1.35
1.35
0.1
0.1
0.1
Throat Conditions
Pressure
Drop
<"H20)
6.5
6.5
41
41
41
6.5
6.5
6.5
41
Water
Pressure
(psi)
41
41
41
41
41
41
41
41
41
Water
Temp.
<°P>
.
77
77
77
Outlet Conditions
Dry
Bulb
<°F)
85
84
87
85
85
81
81
84
86
Wet
Bulb
<°F>
80
79
81
80
80
79
78
76
81
Static
Pressure
C'H.O)
9.5
10.9
61.2
58.5
58.5
9.5
9.5
9.5
58.5
Recirculated
Water
Flow
(gpm)
860
860
860
860
860
860
860
860
860
860
860
860
860
860
860
Fan
Motor
Current
(amp)
120
120
240
240
240
120
120
120
240
240
240
120
120
120
240
a
i-"
o
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-26-74
Atmospheric Pressure: 30.1 Initial:
MRP
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
- - . .
Oven
No.
2
12
22
32
42
X52
X62
—
4
14
24
34
44
X54
X64
Push
Time
0825
0830
0855
0912
0930
0944
1002
1010
1031
1041
1055
1110
1120
1130
• Inlet Conditions
Dry
Bulb
<°F)
190
188
196
186
178
142
140
Wet
Bulb
<°F)
95
88
90
88
87
88
88
Static
Pressure
<"HftO)
'
4.5
4.5
4.5
5.5
1.8
1.8
1.8
Velocity
Pressure
("lUO)
1.35
1.35
1.35
1.35
0.08
0.08
0.08
Throat Conditions
Pressure
Drop
<"H20)
41
41
41
41
6.5
6.5
6.5
Water
Pressure
(psi)
41
41
41
41
41
41
41
Water
Temp.
<°F)
75
75
Outlet Conditions
Dry
Bulb
(°F)
82
82
80
79
75
76
77
Wet
Bulb
(°F)
80
75
76
75
72
73
74
Static
Pressure
("H.O)
55.8
55.8
58.5
58.5
10.9
10.9
10.9
Recirculated
Water
Flow
(gpm)
860
860
860
860
86O
860
860
860
860
860
860
860'
860
860
Fan
Motor
Current
(amp)
240
240
240
240
120
120
120
240
240
240
240
120
120
120
-------
DAILY LOG OF SCRUBBER SYSTEH PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-26-74
Atmospheric Pressure: 30.l Initial:
MRD
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
6
16
26
36
46
X56
8
18
28
38
48
X58
-7-
1
11
Push
Time
1210
1226
1259
1310
1323
1342
1350
1407
1417
1429
1444
1505
1515
1530
Inlet Conditions
Dry
Bulb
<°F>
192
214
196
186
168
146
Wet
Bulb
<°F)
102
94
92
92
90
88
Static
Pressure
<"HA0)
•
4.5
4.5
4.5
1.8
1.8
1.8
Velocity
Pressure
("HjO)
1.35
1.35
1.35
0.06
0.08
0.08
Throat Conditions
Pressure
Drop
C'HzO)
41
41
41
6.5
6.5
6.5
41
41
Water
Pressure
41
41
41
41
41
41
41
41
Water
Temp.
<°F)
77
81
Outlet Conditions
Dry
Bulb
<°F)
83
85
83
80
81
84
91
90
Wet
Bulb
(°F)
80
80
79
77
78
77
82
82
Static
Pressure
("HaO)
58.5
58.5
61.2
9.5
9.5
9.5
57.1
57.1
Recirculatad
Water
Flow
(gpm)
860
860
860
860
860
860
860
860
860
860
860
860
860
860
Fan
Motor
Current
(amp)
240
240
240
120
120
120
240
240
240
120
120
120
240
240
*
I-"
NJ
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-27-74
Atmospheric Pressure: 30.0 Initial: RJP
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
.
Oven
No.
11
21
31
41
X51
X61
3
13
23
33
43
X53
X63
—
5
Push
Time
0819
0827
0914
0923
0937
0948
1002
1017
1029
1040
1048
1058
1124
1134
• Inlet Conditions
Dry
Bulb
<°F)
Wet
Bulb
<°F)
Static
Pressure
<"H40)
'
Velocity
Pressure
C'HzO)
Throat Conditions
Pressure
Drop
<"H20)
9.5
41
42
41
41
Water
Pressure
41
41
41
41
41
Water
Temp.
<°P>
77
77
78
77
77
Outlet Conditions
Dry
Bulb
<°F>
82
80
82
80
82
Wet
Bulb
<°F)
78
77
80
78
80
Static
Pressure
<"H*0)
6
58.5
59.8
57.1
58.5
Recirculated
Water
Flow
(gp»)
860
860
860
860
860
860
860
865
860
860
860
860
860*
860
Fan
Motor
Current
(amp)
120
120
120
120
120
120
120
240
240
240
120
120
120
240
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-27-74
Atmospheric Pressure: 30.0 Initial: RJP
Push
1-6
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
15
25
35
45
X55
7
17
27
37
47
X57
9
19
29
39
Push
Time
1210
1223
1243
1252
1305
1318
1327
1346
1356
1405
1419
1431
1444
1455
1512
Inlet Conditions
Dry
Bulb
(°F)
186
196
186
96
184
204
210
212
154
150
142
Wet
Bulb
(°F)
82
90
82
72
80
90
92
92
76
74
74
Static
Pressure
<"H£0)
-5.0
'-4.5
-4.5
-2.0
-4.5
-4.5
-4.5
-4.5
-2.0
-2.0
-2.0
Velocity
Pressure
("H20)
1.35
1.40
1.35
0.13
1.40
1.40
1.50
1.60
0.13
0.13
0.13
Throat Conditions
Pressure
Drop
<"H20)
41
41
41
41
Water
Pressure
(psi)
41
41
41
41
Water
Temp.
(*F)
78
78
77
77
Outlet Conditions
Dry
Bulb
<°F)
80
80
82
82
Wet
Bulb
<°F)
78
77
80
80
Static
Pressure
C'H.O)
-57.1
-58.5
-57.1
-57.1
Recircnlated
Water
Flow
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-28-74
Atmospheric Pressure: 30.0 Initial: RJP
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
39
49
X59
2
12
22
32
42
X52
X62
4
14
24
34
Push
Time
0820
0829
0838
0851
0904
0919
0931
0943
0952
1013
1020
1032
1051
1105
• Inlet Conditions
Dry
Bulb
<°F)
210
.
Wet
Bulb
(°F)
92
Static
Pressure
<"H£0)
•
-4.5
Velocity
Pressure
<"H20)
1.45
Throat Conditions
Pressure
Drop
<"H20)
6
6
6
41
41
41
41
6
6
6
41
41
41
Water
Pressure
(psi)
41
41
41
41
41
41
41
41
41
41
41
41
41
Water
Temp.
<°F)
72
72
72
72
72
72
72
72
72
72
73
72
72
Outlet Conditions
Dry
Bulb
<°F)
76
74
74
77
77
78
77
74
74
74
76
76
76
Wet
Bulb
CF)
74
72
72
74
74
75
74
72
72
72
74
73
74
Static
Pressure
("H.O)
-9.5
-10.9
-10.9
-59.8
-59.8
-59.8
-57.1
-9.5
-9.5
-9.5
-57.1
-57.1
-58.5
Recirculated
Water
Flow
(gpm)
865
865
865
865
865
865
865
865
865
865
865
865'
865
865
Fan
Motor
Current
(amp)
120
120
120
240
240
240
240
120
120
120
240
240
240
240
SB
!-•
in
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-28-74
Atmospheric Pressure: 30.0 Initial: Rjp
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
Mo.
44
X54
X64
6
16
26
36
46
X56
8
18
28
38
48
X58
Push
Time
1234
1245
1254
1306
1319
1326
1336
1345
1352
1411
1422
1442
1451
1502
1511
Inlet Conditions
Dry
Bulb
<°F)
179
145
140
235
250
200
160
166
170
230
250
180
165
160
156
.
Wet
Bulb
<°F>
85
76
78
98
98
86
90
82
88
95
99
84
82
80
80
Static
Pressure
<"HaO)
-2.0
-2.0
-2.0
-4.5
-5.0
-5.0
-5.5
-2.0
-2.0
-4.5
-4.5
-4.5
-2.0
-2.0
-2.0
Velocity
Pressure
<"HZ0)
0.13
0.13
0.13
1.60
1.60
1.55
1.55
0.13
0.13
1.50
1.50
1.45
0.13
0.13
0.13
Throat Conditions
Pressure
Drop
<"H20)
•
Water
Pressure
(pel)
Water
Temp.
<°F>
Outlet Conditions
Dry
Bulb
CF)
Wet
Bulb
(°F>
Static
Pressure
("HiO)
Recirculated
Water
Flow
(gpm)
860
860
860
865
860
860
860
860
860
860
860
860
860
860
860
Fan
Motor
Current
(amp)
120
120
120
240
240
240
240
120
120
240
240
240
120
120
120
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-29-74
Atmospheric Pressure: 30.0 Initial:
MRD
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
X63
_
5
15
25
35
45
X55
7
17
27
37
47
X57
9
Push
Time
1211
L453
1516
Inlet Conditions
Dry
Bulb
(°F)
Wet
Bulb
CF)
Static
Pressure
C'HfcO)
•
Velocity
Pressure
("HZ0)
Throat Conditions
Pressure
Drop
<"H20)
6
41
Water
Pressure
(psi)
41
41
Water
Temp.
<°F)
79
Outlet Conditions
Dry
Bulb
(°F>
74
86
Wet
Bulb
<°F)
72
81
Static
Pressure
C'HiO)
-9.5
-58.5
Recirculated
Water
Flow
(gpm)
865
865
Fan
Motor
Current
(amp)
120
240
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-30-74
Atmospheric Pressure: 30.0 Initial: MRP
Push
1
2
3
4
S
6
7
8
9
10
11
12
13
14
15
Oven
No.
9
19
29
39
49
X59
2
12
22
32
42
X52
X62
4
Push
Time
0817
0825
0844
0856
0909
0934
0951
1004
1015
1024
1027
1050
1107
1116
• Inlet Conditions
Dry
Bulb
<°F)
232
160
178
Wet
Bulb
<°F)
92
92
96
Static
Pressure
<"HaO)
•
4.5
5.0
6.0
Velocity
Pressure
<"HZ0)
1.4
1.4
1.4
Throat Conditions
Pressure
Drop
(ftHzO)
41
41
41
41
41
6.5
41
Water
Pressure
(psi)
49
49
49
49
49
49
49
Water
Temp .
<°F)
71
74
76
Outlet Conditions
Dry
Bulb
CF>
83
82
79
78
79
78
84
Wet
Bulb
CF)
80
80
76
73
74
72
81
Static
Pressure
C'H.O)
58.5
58.5
58.5
57.1
57.1
57.1
57.1
Recireulated
Water
Flow
(gpn)
940
940
940
940
940
940
940
940
940
940
940
940
940
940
Fan
Motor
Current
(amp)
240
240
240
240
240
240
240
•
240
240
240
a
t-'
oo
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
8-30-74
Atmospheric Pressure: 30.0 Initial:
MRP
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
14
24
34
44
X54
X64
6
16
26
36
46
X56
8
18
28
Push
Time
1204
1215
1242
1253
1301
1313
1323
1343
1353
1401
1421
1440
1457
1511
1524
Inlet Conditions
Dry
Bulb
<°F)
210
218
180
235
178
300
Wet
Bulb
<°F)
96
98
96
102
92
110
Static
Pressure
<"H40)
•
4.5
5.0
4.5
5.0
5.0
4.5
Velocity
Pressure
<"H20)
1.4
1.4
1.4
1.35
1.4
1.4
Throat Conditions
Pressure
Drop
<"H20)
41
41
41
41
41
41
41
41
41
Water
Pressure
(psi)
49
49
49
49
49
49
49
49
49
Water
Temp .
<°F)
.
75
74
74
74
Outlet Conditions
Dry
Bulb
<°F)
82
82
79
80
78
77
85
84
83
Wet
Bulb
CF)
78
78
75
74
74
73
81
80
78
Static
Pressure
("H.O)
57.1
57.1
57.1
58.5
58.5
58.5
57.1
57.1
57.1
Recirculated
Water
Flow
(gpn)
940
940
940
940
940
940
940
940
940
940
940
940
940
940
940
Fan
Motor
Current
(amp)
240
240
240
240
240
240
240
240
240
240
240
240
240
240
240
PC
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
9-3-74
Atmospheric Pressure: 30.0 Initial:
MRP
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
•*• /
Oven
No.
7
17
27
37
47
X57
9
19
29
39
49
X59
2
12
22
Push
Time
0831
0843
0857
0907
0914
0925
0943
0957
1007
1022
1033
1044
1100
1114
1128
• Inlet Conditions
Dry
Bulb
CF)
192
194
186
166
154
136
•
Wet
Bulb
(°F)
88
88
92
82
80
76
Static
Pressure
("HfcO)
•
5.0
5.0
5.0
5.0
5.0
5.0
Velocity
Pressure
("H20)
1.35
1.35
1.35
1.35
1.35
1.35
Throat Conditions
Pressure
Drop
("HzO)
41
41
41
41
41
41
41
41
41
Water
Pressure
(psi)
49
49
49
49
49
49
49
49
49
Water
Temp .
<°F)
62
62
62
62
62
Outlet Conditions
Dry
Bulb
<°F>
71
74
72
72
73
69
74
78
76
Wet
Bulb
<°F)
68
68
68
68
68
66
68
72
72
Static
Pressure
<"H,0)
58.5
58.5
58.5
58.5
58.5
58.5
57.1
57.1
58.5
Recirculated
Water
Flow
(gpm)
940
940
940
940
.940
940
940
940
940
940
940
940
940'
940
940
Fan
Motor
Current
(amp)
240
240
240
240
240
240
240
240
240
240
240
240
240
240
240
PC
i
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
9-3-74
Atmospheric Pressure: 30.1 Initial:
MRP
Push
' 16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
32
42
X52
X62
—
4
14
24
34
44
X54
X64
f>
16
26
Push
Time
1216
1227
1240
1250
1303
1314
1324
1336
1349
1403
1429
14s 3
1459
1522
Inlet Conditions
Dry
Bulb
(°F>
240
207
198
186
166
162
150
Wet
Bulb
(°F)
98
92
88
84
84
80
78
Static
Pressure
("11*0)
•
4.5
4.5
4.5
5.0
5.0
5.0
5.0
Velocity
Pressure
<"HZ0)
1.35
1.35
1.35
1.35
1.35
1.35
1.35
Throat Conditions
Pressure
Drop
("H20)
41
41
41
6
41
41
41
Water
Pressure
(psi)
49
49
49
49
49
49
49
Water
Temp.
<°F)
62.
62
62
62
62
62
62
Outlet Conditions
Dry
Bulb
<°F)
75
73
75
69
74
75
74
Wet
Bulb
(°F)
68
65
68
65
64
65
66
Static
Pressure
<"H*0)
58.5
58.5
58.5
9.5
58.5
58.5
58.5
Recirculated
Water
Flow
(gpm)
940
940
940
940
940
940
940
940
940
940
940
940
940
940
Fan
Motor
Current
(amp)
240
240
240
130
240
240
240
240
240
240
240
240
240
240
SB
l
ro
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
9-4-74
Atmospheric Pressure: 30.2 Initial:
MRP
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
26
36
46
X56
8
18
28
38
48
X58
1
11
21
31
Push
Time
0805
0812
0837
0847
0922
0930
1003
1015
1032
1043
1107
1121
1142
1153
• Inlet Conditions
Dry
Bulb
(°F)
184
206
184
164
164
168
Wet
Bulb
<°F)
84
92
92
86
82
82
Static
Pressure
("HaO)
•
5.0
5.0
5.0
5.0
5.0
5.0
Velocity
Pressure
("HZ0)
1.35
1.35
1.35
1.35
1.35
1.35
Throat Conditions
Pressure
Drop
<"HZ0)
41
41
41
41
41
41
41
41
41
Water
Pressure
(psi)
49
49
49
49
49
49
49
49
49
Water
Temp.
CF)
59
59
59
62
63
63
63
Outlet Conditions
Dry
Bulb
<°F)
76
74
72
90
70
7Z
74
72
Wet
Bulb
<°F)
64
62
60
75
64
66
66
64
Static
Pressure
<"H40)
58.5
58.5
58.5
58.5
58.5
58.5
58.5
58.5
58.5
Recirculated
Water
Flow
(gpm)
940
940
940
940
940
940
c
940
940
940
940
940
940
940
940
Fan
Motor
Current
(amp)
240
240
240
240
240
240
240
240
240
240
240
240
240
240
PC
Is)
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
9-4-74
Atmospheric Pressure: 30.2
Initial: MRP
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
41
*51
X61
3
13
23
33
43
X53
X63
—
5
15
25
35
Push
Time
1238
1248
1301
1312
1324
1336
1345
1356
1405
1416
1438
1453
1503
1513
Inlet Conditions
Dry
Bulb
(°F)
214
192
208
198
164
162
140
Wet
Bulb
CF)
95
88
91
89
80
80
72
Static
Pressure
C'HfcO)
•
4.5
4.5
4.5
4.5
4.5
5.0
1.8
Velocity
Pressure
<"HZ0)
1.35
1.35
1.35
1.35
1.35
1.35
0.1
Throat Conditions
Pressure
Drop
<"H20)
41
41
43
43
41
41
41
Water
Pressure
(P8i)
49
49
49
49
49
49
49
Water
Temp.
(°F)
64
64
64
66
66
67
Outlet Conditions
Dry
Bulb
CF)
71
69
71
80
77
74
76
Wet
Bulb
<°F)
65
65
64
70
70
67
66
Static
Pressure
C'HaO)
58.5
58.5
62.6
59.8
59.8
58.5
58.5
Recirculated
Water
Flow
(gpn)
940
940
940
940
940
940
940
940
940
940
940
940
940
940
Fan
Motor
Current
(amp)
240
240
240
240
240
240
240
240
240
120
240
240
2*0
240
SG
l
ro
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
9-5-74
Atmospheric Pressure: 30.4 Initial:
MRP
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
IS
Oven
Mo.
35
45
If55
7
17
27
37
47
X57
9
19
29
39
49
X59
Push
Time
0831
0841
0847
0857
0922
0932
0959
1018
1029
1040
1050
1103
1118
1128
1138
• Inlet Conditions
Dry
Bulb
<°F)
196
182
170
200
220
Wet
Bulb
CF)
94
86
89
96
95
Static
Pressure
("HaO)
•
5.0
5.0
5.5
5.5
5.5
Velocity
Pressure
("HfcO)
1.35
1.35
1.35
1.35
1.35
Throat Conditions
Pressure
Drop
<"H20)
41
41
41
41
43
43
43
43
43
Water
Pressure
(psi)
49
49
49
49
49
49
49
49
49
Water
Temp .
(°F)
62
64
65
67
Outlet Conditions
Dry
Bulb
(°F)
68
82
75
78
75
75
74
74
77
Wet
Bulb
<°F)
64
68
66
70
66
66
65
65
64
Static
Pressure
("H20)
58.5
58.5
57.1
61.2
59.8
58.5
61.2
59.8
58.5
Recirculated
Water
Flow
(gpn)
940
940
940
940
940
940
940
940
940
940
940
940
940'
940
940
Fan
Motor
Current
(amp)
iao
240
240
240
240
240
240
240
240
240
240
240
240
240
240
»
r-o
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
9-5-74
Atmospheric Pressure: 30.4 Initial:
_MBJ1_
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
.
Oven
Mo.
2
12
22
32
42
562
X62
4
14
24
34
44
X54
X64
Push
Time
1228
1235
1250
1259
1310
1317
1328
1338
1351
1405
1429
1442
1505
1518
Inlet Conditions
Dry
Bulb
<°F)
218
218
204
192
192
180
180
.
Wet
Bulb
(°F>
103
103
95
95
95
90
100
Static
Pressure
("HZ0)
4.5
'5.0
5.0
5.0
5.0
5.0
1.8
Velocity
Pressure
<"H20)
1.35
1.35
1.35
1.35
1.35
1.35
0.1
Throat Conditions
Pressure
Drop
<"H20>
43
43
43
43
43
43
7
.
Water
Pressure
(psi)
49
49
49
49
49
49
49
Water
Temp.
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
9-6-74
Atmospheric Pressure: 30.3 Initial: Rjp
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
X64
6
16
26
36
46
X56
8
18
28
38
48
X58
1
Push
Time
0854
0921
0930
0940
0957
1011
1025
1040
1055
1106
1116
1128
1141
1152
• Inlet Conditions
Dry
Bulb
<°F)
250
.
Wet
Bulb
(°F)
122
Static
Pressure
("H20)
'
-4.5
Velocity
Pressure
("HzO)
1.70
Throat Conditions
Pressure
Drop
<"H20)
7
42
45
45
45
45
45
45
45
45
45
45
45
Water
Pressure
(psi)
49
49
49
49
49
50
50
50
50
50
50
50
50
Water
Temp.
<°F)
63
63
63
63
63
63
63
63
63
63
63
63
63
Outlet Conditions
Dry
Bulb
<°F)
66
66
66
69
69
69
70
70
70
69
69
69
69
Wet
Bulb
<°F)
66
62
63
63
63
63
62
63
63
63
64
63
63
Static
Pressure
("H,0)
-10.9
-61.2
-61.2
-59.8
-59.8
-63.9
-61.2
-61.2
-61.2
-59.8
-61.2
-61.2
-61.2
Recirculated
Water
Flow
(gpm)
920
920
920
920
920
920
920
920
920
920
920
920
920
920
Fan
Motor
Current
(amp)
125
235
235
235
235
235
235
235
235
235
235
235
235
235
'
BB
to
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
9-6-74
Atmospheric Pressure: 30.3 Initial:
Push
16
17
. 18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
11
21
31
41
X51
X61
3
13
23
33
43
X53
X63
—
5
Push
Time
1203
1212
1253
1302
1320
1332
1345
1354
1405
1416
1425
1437
1449
1510
Inlet Conditions
Dry
Bulb
(°F)
220
204
202
196
180
152
235
220
204
186
182
Wet
Bulb
(°F)
132
112
108
106
96
86
120
117
114
110
98
Static
Pressure
<"HaO)
-4.5
-4.5
-5.0
-5.5
-6.0
-6.0
-4.5
-4.5
-4.5
-4.5
-5.0
Velocity
Pressure
("H20)
1.65
1.60
1.50
1.50
1.50
1.50
1.70
1.55
1.45
1.45
1.35
Throat Conditions
Pressure
Drop
<"H20)
45
45
45
Water
Pressure
(psl)
50
50
50
Water
Temp.
(°F)
64
64
64
Outlet Conditions
Dry
Bulb
<°F)
69
69
69
Wet
Bulb
CF)
63
63
64
Static
Pressure
("H*0)
-61.2
-59.8
-61.2
Reclrculated
Water
Flow
(gpn)
900
920
920
920
920
920
920
920
920
920
920
920
920
920
Fan
Motor
Current
(amp)
235
235
235
235
235
235
235
235
235
235
235
235
235
235
to
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
1-8-75
Atmospheric Pressure: 29.56 Initial:
MRP
Piish
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
.
Oven
No.
. 44
X54
X64
6
16
26
36
46
X56
8
18
28
38
Push
Time
0825
0836
0847
0859
0913
0930
0950
1007
1030
1045
1107
1123
1140
• Inlet Conditions
Dry
Bulb
(°F)
147
157
146
184
144
142
Wet
Bulb
<°F>
106
109
96
112
102
98
Static
Pressure
C'lUO)
•
Velocity
Pressure
<"H20)
Throat Conditions
Pressure
Drop
("H20)
40
40
40
40
40
40
40
41
Water
Pressure
(psi)
54
54
54
54
54
54
54
Water
Temp.
<°F>
47
47
47
47
47
47
47
Outlet Conditions
Dry
Bulb
<°F)
46
48
52
57
58
59
62
Wet
Bulb
<°F)
45
46
46
51
51
52
54
Static
Pressure
<"H,0)
57
57
57
57
60
57
57
60
Recirculated
Water
Flow
870
880
880
880
880
880
880
880
880
880
880
880
880 '
Fan
Motor
Current
(amp)
240
•
NJ
00
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
1-8-75
Atmospheric Pressure: 29.47 Initial:
MRP
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
48
X58
1
11
21
31
41
X51
X61
3
13
Push
Time
1219
1233
1246
1312
1323
1340
1352
1414
1435
1507
1520
Inlet Conditions
Dry
Bulb
(°F)
180
188
142
152
152
142
112
Wet
Bulb
<°F)
98
118
80
110
90
102
96
Static
Pressure
<"H40)
•
Velocity
Pressure
("H20)
Throat Conditions
Pressure
Drop
<"H20)
40
'40
40
40
40
40
•
Water
Pressure
(psi)
54
54
54
54
54
54
54
54
Water
Temp.
<°F)
47
Outlet Conditions
Dry
Bulb
<°F)
52
48
58
63
Wet
Bulb
<°F)
46
46
50
56
Static
Pressure
<"H»0)
57
57
57
57
57
57
Recirculated
Water
Flow
(gpm)
880
880
880
880
880
880
880
880
880
880
880
Fan
Motor
Current
(amp)
240
240
240
240
240
240
240
240
240
240
240
sc
I
is)
vO
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
1-9-75
Atmospheric Pressure: 29.66 Initial:
MRD
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
-
Oven
No.
X58
1
11
21
31
41
X51
X61
3
13
23
33
43
Push
Time
0820
0830
0900
0918
0931
0944
1001
1017
1024
1046
1057
1115
• Inlet Conditions
Dry
Bulb
<°F)
140
134
140
108
102
Wet
Bulb
(°F)
94
94
94
68
66
Static
Pressure
("HaO)
•
Velocity
Pressure
<"H*0)
Throat Conditions
Pressure
Drop
<"H20)
55
55 .
55
55
55
55
Water
Pressure
(psi)
54
54
54
54
54
Water
Temp.
(°F)
40
40
40
40
40
40
40
40
40
40
40
40
40
Outlet Conditions
Dry
Bulb
(°F)
48
54
52
52
54
58
56
Wet
Bulb
(°F)
44
44
44
46
48
48
48
Static
Pressure
("H,0)
60
63
63
63
63
63
63
Recirculated
Water
Flow
(gpn)
870
870
870
870
870
870
870
870
870
870
870
870
870 '
Fan
Motor
Current
(amp)
240
Sfl
o
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
1-10-75
Atmospheric Pressure: 29.51 Initial:
_MRD
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
"i"
Oven
No.
X63
5
• 15
25
35
45
X55
7
17
27
37
47
X57
Push
Time
0820
0830
09OO
0912
0923
0942
0957
1012
1025
1036
1051
1106
1120
• Inlet Conditions
Dry
Bulb
(°F)
152
156
152
•
Wet
Bulb
CF)
84
112
88
Static
Pressure
<"H£0)
•
Velocity
Pressure
("H20>
Throat Conditions
Pressure
Drop
<"H20)
61
61
61
61
55
55
55
55
55
55
55
Water
Pressure
(psl)
54
54
54
54
54
54
54
54
54
54
Water
Temp.
(°F)
40
Outlet Conditions
Dry
Bulb
(°F)
46
58
56
54
62
58
58
68
100
62
Wet
Bulb
(°F)
42
52
48
46
52
52
52
58
78
50
Static
Pressure
("H,0)
63
63
63
60
60
60
63
65
65
60
Reclrculated
Water
Flow
(gpm)
860
860
860
860
860
860
860
860
860
860
860
860
860 •
Fan
Motor
Current
(amp)
24O
240
240
240
240
240
240 !
240
240
240
240
240
240
I
|
i
BC
1
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Flant * Dearborn, Michigan
Date:
1-10-75
Atmospheric Pressure: 29.37 Initial:
MRD
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
9
19
29
39
49
X59
2
12
22
32
42
Push
Time
1215
1226
1310
1321
1335
1352
1403
1419
1446
1501
1516
Inlet Conditions
Dry
Bulb
(°F>
152
150
145
184
128
Wet
Bulb
<°F)
84
86
86
Static
Pressure
<"HaO)
'
Velocity
Pressure
<"H20)
Throat Conditions
Pressure
Drop
("HzO)
55
55
55
55
55
55
55
55
55
Water
Pressure
(psi)
54
54
54
54
54
54
54
54
54
Water
Temp .
(°F)
.
40
Outlet Conditions
Dry
Bulb
(°F)
52
62
78
58
58
68
Wet
Bulb
<°F)
48
50
56
52
52
56
Static
Pressure
<"H»0)
63
63
63
63
63
63
63
60
60
Recirculated
Water
Flow
(gpn)
860
860
860
860
860
860
860
860
860
860
860
Fan
Motor
Current
(amp)
240
240
240
240
240
240
240
240
240
240
240
I
U)
-------
DAILY LOG OP SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6-3-75
Atmospheric Pressure: 29.5 Initial:
JBS
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
_
Oven
Mo.
48
X58
1
11
21
31
41
X51
X61
3
13
23
33
43
Push
Time
0820
0830
0855
0958
1012
1022
1040
1047
1104
1114
1124
1204
1213
1224
• Inlet Conditions
Dry
Bulb
(°F)
190
190
350
150
210
280
400
300
180
225
•
Vet
Bulb
CF)
Static
Pressure
<"HaO)
•
-4.8
-4.8
-4.8
-4.8
5.2
4.3
5.5
4.2
4.2
5.5
Velocity
Pressure
("HZ0)
1.3
1.2
1.3
1.3
1.2
1.3
1.2
1.2
1.2
1.2
Throat Conditions
Pressure
Drop
("H20)
41
40
39
40
40
42
42
42
40
40
Water
Pressure
(psi)
39
40
39
39
39
38
38
38
38
38
Water
Temp .
CF)
Outlet Conditions
Dry
Bulb
CF)
72
62
72
74
72
78
82
78
74
78
Wet
Bulb
CF)
62
56
70
72
70
76
76
72
72
72
Static
Pressure
("H.O)
-46.2
-51.7
-50.3
51.7
53.0
50.3
51.7
50.3
53.0
46.2
Raclrculated
Water
Flow
(gpn)
750
•
Fan
Motor
Current
(amp)
125-215
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plane * Dearborn, Michigan
Date:
6-4-75
Atmospheric Pressure:
Initial: JBS
Push
.1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
X57
9
19
29
39
49
X59
2
12
22
32
42
X52
XS2
Push
Time
0830
0904
0914
0926
0940
0955
1018
1049
1104
1116
1125
1140
1152
1207
• Inlet Conditions
Dry
Bulb
<°F)
160
180
320
Wet
Bulb
CF)
Static
Pressure
<"H£0)
4.5
4.8
4.8
Velocity
Pressure
<"H20)
1.2
1.3
1.3
Throat Conditions
Pressure
Drop
("H2CO
41
43
42
Water
Pressure
(psi)
39
39
39
Water
Temp .
<°F)
Outlet Conditions
Dry
Bulb
<°F)
70
92
88
Wet
Bulb
<°F>
64
82
81
Static
Pressure
("HaO>
50.3
55.8
54.4
Recirculated
Water
Flow
(gpm)
750
750
750
•
Fan
Motor
Current
(amp)
125 -
215
•
a
I
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6-4-75
Atmospheric Pressure:
Initial: JBS
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
4
14
24
34
44
X54
X64
6
16
26
36
46
X56
8
18
•
Push
Time
1300
1310
1317
1330
1346
1359
1411
1425
1434
1444
1458
1508
1519
1531
1537
Inlet Conditions
Dry
Bulb
<°F)
260
.
Vet
Bulb
<°F)
Static
Pressure
<"H40)
•
-4.3
Velocity
Pressure
<"H20)
1.3
Throat Conditions
Pressure
Drop
<"H20)
-
44
Water
Pressure
(pal)
38
Water
Temp .
<°F)
Outlet Conditions
Dry
Bulb
(°F)
80
Wet
Bulb
(°F)
78
Static
Pressure
<"H.O)
51.7
Reclrculated
Water
Flow
(gpm)
Fan
Motor
Current
(amp)
UI
1/1
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6-5-75
Atmospheric Pressure: 29.1 Initial: RJP
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
IS
y
Oven
No.
18
28
38
48
X58
1
11
21
31
41
X51
X51
3
13
Push
Time
0828
0844
0857
0914
0930
0944
0950
1005
1025
1035
1045
1100
1111
1122
• Inlet Conditions
Dry
Bulb
<"F)
210
195
225
220
•
Wet
Bulb
Static
Pressure
C'H^O)
-4.3
" -4.1
-4.3
-4.3
Velocity
Pressure
<"H20)
1.50
1.45
1.50
1.50
Throat Conditions
Pressure
Drop
<"H20)
44
45
45
45
Water
Pressure
Outlet Conditions
Dry
Bulb
<°F>
84
82
82
78
Wet
Bulb
<°F)
82
80
80
78
Static
Pressure
<"HaO)
53
50.3
50.3
50.3
Recirculated
Water
Flow
(gpm)
760
760
760
760
•
Fan
Motor
Current
(amp)
125-
215
•
S
u>
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6-6-75
Atmospheric Pressure: 29tl Initial: RJP
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
.
Oven
No.
27
37
47
X57
9
19
29
39
49
X59
2
12
22
32
42
Push
Time
0810
0820
0830
0950
1004
1027
1049
1100
1114
1127
1141
1150
1201
1215
1230
• Inlet Conditions
Dry
Bulb
<°F)
220
215
285
Wet
Bulb
(°F>
Static
Pressure
<"H40)
-5.4
'-4.9
-5.5
Velocity
Pressure
("HaO)
1.45
1.50
1.45
Throat Conditions
Pressure
Drop
<"H20)
42
43
43
Water
Pressure
(psi)
38
38
38
Water
Temp.
<°F)
Outlet Conditions
Dry
Bulb
(°F)
80
70
80
Wet
Bulb
<°F)
76
68
76
Static
Pressure
<"H,0)
53.0
50.3
49.0
Recirculated
Water
Flow
(gpn)
800
800
780
t
Fan
Motor
Current
(amp)
215
215
215
•
SB
w
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6-9-75
Atmospheric Pressure: 29.67 Initial: GJS
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
16
26
36
46
X56
8
18
28
38
48
Push
Time
9817
3830
1838
)853
1923
)942
>957
L013
L025
L038
X58 JL047
I
1 JL058
11 h.115
21
L128
• Inlet Conditions
Dry
Bulb
<°F)
100
100
•
Wet
Bulb
(°P)
Static
Pressure
<"HaO)
4.5
5.5
5.4
Velocity
Pressure
("H20)
1.2
1.3
1.2
Throat Conditions
Pressure
Drop
<"H20)
40-44
42
45
Water
Pressure
(psi)
38-40
40
40
-
Water
Temp.
<°F>
Outlet Conditions
Dry
Bulb
<°F)
160
• 80
84
75
Wet
Bulb
<8F)
80
72
Static
Pressure
<"H,0)
54.4
52
Recirculated
Water
Flow
(gpm)
750
750
750
i
Fan
Motor
Current
(«mp)
115-
215
•
u>
00
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6-9-75
Atmospheric Pressure: 29.67 Initial:
GJS
Push
:
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
31
41
X51
X61
3
13
23
33
43
X53
X«3
--
5
15
25
Push
Time
1139
1153
1206
1314
1322
1335
1345
1357
1403
1422
1432
1447
1502
1530
Inlet Conditions
Dry
Bulb
(°F)
110
220
210
Wet
Bulb
(°F)
Static
Pressure
<"H40)
•
4.6
5.0
•
4.8
Velocity
Pressure
<"H*0)
1.3
1.3
1.2
Throat Conditions
Pressure
Drop
("H20)
46
46
40
Water
Pressure
(pel)
40
40
40
Water
Temp.
<°F>
Outlet Conditions
Dry
Bulb
(°F>
74
80
68
Wet
Bulb
<°F)
74
80
70
Static
Pressure
("H*0)
53
53
46
Recirculated
Water
Flow
(gpm)
760
760
760
Fan
Motor
Current
(amp)
215
PS
vo
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6-10-75
Atmospheric Pressure: 29.85 Initial: TAL
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
45
47
9
Push
Time
0855
1024
1051
• Inlet Conditions
Dry
Bulb
(T)
260
300
420
Wet
Bulb
CF)
Static
Pressure
("H40)
5.5
• 5.8
5.5
Velocity
Pressure
<"H20)
1.3
1.5
1.6
•
Throat Conditions
Pressure
Drop
C'HZ0)
43
45
45
Water
Pressure
(psi)
38
38
38
-
Water
Temp.
<-F)
Outlet Conditions
Dry
Bulb
<°F)
72
78
84
Wet
Bulb
CF)
70
75
82
Static
Pressure
<"H,0>
53
53
51.7
Recirculated
Water
Flow
(gP»)
770
770
770
•
Fan
Motor
Current
(amp)
220
220
220
•
a
i
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6-10-75
Atmospheric Pressure: 29.85 Initial: TAL
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
32
42
X52
Push
Time
130!
131!
133(
Inlet Conditions
Dry
Bulb
<°F)
340
850
390
Wet
Bulb
<°F)
Static
Pressure
<"H£0)
5.8
'6.0
5.5
•
Velocity
Pressure
<"HZ0)
1.4
1.7
1.4
Throat Conditions
Pressure
Drop
<"H20)
45
45
45
Water
Pressure
(psl)
38
38
Water
Temp.
CF)
Outlet Conditions
Dry
Bulb
<°F)
82
94
90
Wet
Bulb
CF)
80
92
88
Static
Pressure
("HZ0)
53
53
45
Reclrculated
Water
Flov
(gpn)
770
770
770
Fan
Motor
Current
(amp)
220
220
220
PC
I
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6-11-75
Atmospheric Pressure: 29t ** Initial:
GJS
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15 .
Oven
No.
X54
1C 6 4
6
16
26
36
46
K56
8
18
28
38
48
X58
Push
Time
0816
0828
0843
0905
0938
1000
1014
1025
1050
1102
1111
1122
1135
1202
• Inlet Conditions
Dry
Bulb
(°F)
- -
400
Wet
Bulb
(°F)
Static
Pressure
<"HaO)
•
5.0
Velocity
Pressure
<"H20)
1.3
Throat Conditions
Pressure
Drop
<"H20)
40
Water
Pressure
(pal)
40
Water
Temp.
<°F)
Outlet Conditions
Dry
Bulb
CF)
84
Wet
Bulb
<°F)
84
Static
Pressure
("HaO)
47.6
Reeirculated
Water
Flow
(gpm)
•
Fan
Motor
Current
(amp)
•
PC
N3
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6-11-75
Atmospheric Pressure: 29.15 Initial: GJS
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
1
11
21
31
41
X51
X61
3
13
23
33
43
X53
X63
—
Push
Time
1250
1302
1310
1338
1347
1408
1423
1434
1445
1455
1508
1516
1528
1538
Inlet Conditions
Dry
Bulb
(°F)
160
210
.
Wet
Bulb
(°F)
Static
Pressure
C'lUO)
•
5.1
4.7
Velocity
Pressure
<"H20)
1.3
1.3
Throat Conditions
Pressure
Drop
("H20)
•
36
40
Water
Pressure
(psi)
40
40
Water
Temp.
<°F)
Outlet Conditions
Dry
Bulb
(°F>
76
82
Wet
Bulb
CF)
76
82
Static
Pressure
("H,0)
42.2
45
Recirculated
Water
Flow
(gpa)
Fan
Motor
Current
(amp)
,
sa
I
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6-12-75
Atmospheric Pressure:
Initial: GJS
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
•
Oven
No.
• • _
5
. 15
25
35
45
X55
7
17
27
37
47
X57
9
19
Push
Time
0819
0841
0850
0932
0944
1000
1014
1037
1046
1101
1114
1126
1214
1226
• Inlet Conditions
Dry
Bulb
<°F)
Wet
Bulb
(°F)
Static
Pressure
<"H*0)
•
5.0
Velocity
Pressure
("H20)
1.3
Throat Conditions
Pressure
Drop
<"H20)
40
Water
Pressure
(psi)
Water
Temp.
<°F>
Outlet Conditions
Dry
Bulb
<°F)
*
80
Wet
Bulb
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6-12-75
Atmospheric Pressure: 29.35 Initial: GJS
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
Mo.
29
39
49
X59
2
12
22
32
42
X52
X62
--
4
14
24
Push
Time
1235
1245
1256
1315
1330
1342
1350
1410
1418
1434
1445
1452
1510
1521
Inlet Conditions
Dry
Bulb
CF)
Wet
Bulb
(°F)
Static
Pressure
("H40)
•
5.3
5.1
•
Velocity
Pressure
<"HaO)
1.3
1.3
Throat Conditions
Pressure
Drop
("H20)
•
40
40
Vater
Pressure
(psl)
40
40
Water
Temp .
(°F)
Outlet Conditions
Dry
Bulb
(°F)
79
74
Wet
Bulb
(°F)
79
74
Static
Pressure
<"H*0)
44.9
44.9
•
Recirculated
Water
Flow
(gpm)
Fan
Motor
Current
(amp)
rs
i
4>
Ui
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6-24-75
Atmospheric Pressure:
Initial: RJF
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
33
43
X53
X*3
5
15
25
35
45
X55
7
17
27
37
Push
Time
1211
1224
1230
1248
1320
1336
1352
1408
1424
1440
1456
1512
1528
1544
Inlet Conditions
Dry
Bulb
CF)
220
Wet
Bulb
<°F)
Static
Pressure
<"HaO)
•
-4.9
Velocity
Pressure
("H20)
1.45
-
Throat Conditions
Pressure
Drop
<"H20)
43
Hater
Pressure
(psl)
40
Hater
Temp.
(°F)
Outlet Conditions
Dry
Bulb
(°F)
84
Het
Bulb
(°F)
82
Static
Pressure
("H*0)
49.0
Recirculated
Hater
Flow
(BPn)
800
Fan
Motor
Current
(amp)
210
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
Atmospheric Pressure:
Initial: Rjp
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
.
Oven
No.
37
47
X57
9
19
29
39
49
X59
2
12
22
32
42
X52
Push
Time
0820
0828
0840
0912
0946
0955
1005
1018
1029
1040
1053
1105
1120
1133
1146
• Inlet Conditions
Dry
Bulb
(°F>
210
Wet
Bulb
<°F)
Static
Pressure
<"H40)
•
-4.0
Velocity
Pressure
<"HZ0)
•
1.4
Throat Conditions
Pressure
Drop
<"H20)
.
42
Water
Pressure
(pal)
40
Water
Temp.
<°F>
Outlet Conditions
Dry
Bulb
<°F)
86
Wet
Bulb
<°F)
84
Static
Pressure
<"H,0)
-49.0
Recirculated
Water
Flov
(gpm)
800
•
800
Fan
Motor
Current
(aap)
215
•
215
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6.-26-7S
Atmospheric Pressure: 29.74 Initial: TAL
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
-
Oven
No.
X56
8
18
28
38
48
X58
1
11
21
31
41
SCSI
K61
Push
Time
0815
0832
0846
0900
0915
0925
0937
1016
1022
1039
1049
1102
1125
1139
• Inlet Conditions
Dry
Bulb
<°F)
700
950
Wet
Bulb
(°F)
Static
Pressure
("H40)
4.8
4.8
Velocity
Pressure
("HZ0)
1.4
1.2
Throat Conditions
Pressure
Drop
C'HzO)
40
40
Water
Pressure
(psl)
42
42
Water
Temp.
<°F)
Outlet Conditions
Dry
Bulb
<°F)
80
LOO
Wet
Bulb
CF)
78
98
Static
Pressure
("H^)
-54
-54
Recirculated
Water
Flow
(gpn)
780
780
780
-
•
Fan
Motor
Current
(amp)
210
•
•
•p-
00
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6-27-75
Atmospheric Pressure: 29.70 Initial: TAL
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
.-.
Oven
No.
7
17
27
37
47
367
9
19
29
39
49
X59
2
12
22
Push
Time
0825
0846
0910
0919
0930
0950
1010
1020
1040
1056
1108
1120
1135
1147
1158
• Inlet Conditions
Dry
Bulb
(°F)
900
260
260
300
.050
•
Wet
Bulb
(°F)
Static
Pressure
("HaO)
4.05
4.0
5.0
5.0
5.0
Velocity
Pressure
<"HZ0)
1.1
0.7
1.1
1.2
1.5
Throat Conditions
Pressure
Drop
<"HZ0)
40
40
41
41
42
Water
Pressure
(pst)
40
40
40
40
40
Water
Temp.
CF)
Outlet Conditions
Dry
Bulb
<°F)
100
90
88
90
110
Wet
Bulb
CF)
98
88
86
88
108
Static
Pressure
<"H*0)
29.9
32.6
49
40.8
54.4
Recirculated
Water
Flow
(gpm)
790
790
790
790
790
790
•
Fan
Motor
Current
(amp)
215
•
•
PC
vo
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6-27-75
Atmospheric Pressure: 29.70 Initial:
TAL
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
32
42
X52
X62
4
14
24
34
44
X54
X64
6
16
26
Push
Time
1205
1215
1225
1238
1325
1340
1405
1424
1435
1445
1455
1511
1528
1538
Inlet Conditions
Dry
Bulb
<°F)
250
.
Wet
Bulb
<°F)
Static
Pressure
("HaO)
•
5.0
Velocity
Pressure
<"H20)
1.2
Throat Conditions
Pressure
Drop
("HzO)
•
40
Water
Pressure
(psi)
40
Water
Temp.
<-F)
Outlet Conditions
Dry
Bulb
(°F)
87
Wet
Bulb
(°F)
86
Static
Pressure
<"HaO)
54.8
Recirculated
Water
Flow
(gpm)
Fan
Motor
Current
(amp)
Sfi
o
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
6-30-7S
Atmospheric Pressure:
Initial: TAL
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
34
44
X54
#4
6
16
26
36
46
266
8
ia
28
38
Push
Time
0810
0826
0837
0854
0905
0920
0943
0954
1003
1011
1027
1045
1056
1141
• Inlet Conditions
Dry
Bulb
CF)
690
270
Wet
Bulb
<°F)
Static
Pressure
<"H20)
5.5
5.0
Velocity
Pressure
<"HZ0)
1.4
1.4
Throat Conditions
Pressure
Drop
("H20)
38
38
Uater
Pressure
(psi)
40
40
Water
Temp.
(°F)
Outlet Condition*
Dry
Bulb
CF)
96
83
Wet
Bulb
<°F)
94
81
Static
Pressure
("H,0)
49.0
54.4
Recirculated
Water
Flow
(gpm)
780
780
f
Fan
Motor
Current
(amp)
220
•
PC
in
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-2-75
Atmospheric Pressure: 29.75 Initial: TAL
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Oven
No.
_ _ _
4
14
24
34
44
X54
X64
6
16
26
36
46
X56
8
Push
Time
0822
0834
0921
0928
0946
0954
1005
1014
1030
1037
1100
1110
1123
1139
• Inlet Conditions
Dry
Bulb
<°F)
180
Wet
Bulb
(°F)
Static
Pressure
<"HaO)
•
5.0
Velocity
Pressure
("HZ0)
1.3
Throat Conditions
Pressure
Drop
<"H20)
38
Water
Pressure
(psi)
40
Water
Temp.
<°F)
Outlet Conditions
Dry
Bulb
(°F)
82
Wet
Bulb
<°F)
81
Static
Pressure
("H.O)
49.0
Recirculated
Water
Flow
(gpm)
780
780
•
Fan
Motor
Current
(amp)
220
PC
I
01
to
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-2-75
Atmospheric Pressure: 29.75 Initial: TAL
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
NO.
18
28
38
48
X58
1
11
21
31
41
X51
X61
3
13
Push
Time
1301
1306
1313
1327
1335
1345
1355
1415
1442
1455
1505
1516
1535
1545
Inlet Conditions
Dry
Bulb
(°F)
330
650
240
Wet
Bulb
(°F)
Static
Pressure
("H^O)
5.3
'5.3
5.3
•
•
Velocity
Pressure
<"HZ0)
1.2
1.5
1.2
Throat Conditions
Pressure
Drop
<"HzO)
38
38
38
Water
Pressure
(psi)
40
40
40
Water
Temp.
(°F)
Outlet Conditions
Dry
Bulb
(°F)
90
98
89
Wet
Bulb
(°F)
89
97
88
Static
Pressure
<"H»0)
54.4
54.4
54.4
Recirculated
Water
Flov
(gpm)
Fan
Motor
Current
(amp)
Sfl
i
V/l
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-8-75
Atmospheric Pressure:
Initial: TAL
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
X54
X64
6
16
26
36
46
X56
8
18
28
38
48
X58
_
Push
Time
1245
1252
1305
1320
1335
1345
1403
1421
1440
1449
1501
1510
1521
1530
Inlet Conditions
Dry
Bulb
(°F)
210
230
260
.
Wet
Bulb
<°F)
Static
Pressure
<"H20)
•
•
-5.3
-5.3
-5.3
Velocity
Pressure
<"H20)
1.2
1.3
1.3
Throat Conditions
Pressure
Drop
<"H20)
•
40
40
40
Water
Pressure
(psi)
55
55
55
Water
Temp .
<°F)
.
Outlet Conditions
Dry
Bulb
<°F)
85
84
84
Wet
Bulb
<°F)
83
82
82
Static
Pressure
C'HiO)
-54.4
-54.4
-54.4
Recirculated
Water
Flow
(gpn)
840
840
840
Fan
Motor
Current
(amp)
215
215
215
PC
I
in
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-9-75
Atmospheric Pressure: 29.40 Initial: TAL
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
IS
Oven
No.
1
11
21
31
41
X51
X61
3
13
23
33
43
X53
X63
Puah
lime
0825
0834
0845
0910
0935
0950
1015
1028
1038
1046
1057
1105
1112
1125
• Inlet Conditions
Dry
Bulb
(CF)
260
770
Wet
Bulb
<°F)
Static
Pressure
<"H£0)
-4.8
-4.9
Velocity
Pressure
<"H20)
1.1
1.3
Throat Conditions
Pressure
Drop
C'HzO)
40
40
Water
Pressure
(psi)
55
55
Water
Temp .
<°F)
Outlet Conditions
Dry
Bulb
<°F)
82
99
*
Wet
Bulb
<°F)
80
97
Static
Pressure
<"H,0)
-54.4
-54.4
Reclrculatad
Water
Flow
(gpm)
820
820
•
Fan
Motor
Current
(amp)
210
210
Ui
Ol
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-Q-7S
Atmospheric Pressure: 29.40
Initial:
TAL
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
_
5
15
25
35
45
X55
7
17
27
37
47
X57
9
19
Push
Time
1207
1220
1232
1250
1302
1344
1357
1408
1420
1428
1435
1500
1513
1518
Inlet Conditions
Dry
Bulb
<°F)
320
260
Wet
Bulb
(°F)
Static
Pressure
<"HaO>
•
-5.5
-5.5
Velocity
Pressure
<"H20)
1.5
1.2
Throat Conditions
Pressure
Drop
("H20>
40
40
Water
Pressure
(P8i)
55
55
Water
Temp.
CF)
Outlet Conditions
Dry
Bulb
<°F)
88
84
Wet
Bulb
(°F)
86
82
Static
Pressure
C'HiO)
-54.4
-54.4
Recirculated
Water
Flow
(gpm)
820
820
Fan
Motor
Current
(amp)
210
210
sc
in
O\
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-10-75
Atmospheric Pressure: 29.34 Initial: TAl
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
-
Oven
No.
19
29
39
49
X59
2
12
22
32
42
X52
X62
— •
4
14
Push
Time
0611
0841
0858
0910
0925
0940
0953
1017
1024
1045
1057
1107
1120
1130
• Inlet Conditions
Dry
Bulb
<°F)
230
Wet
Bulb
(°F)
Static
Pressure
("H^O)
-5.5
•
Velocity
Pressure
<"H*0)
1.2
Throat Conditions
Pressure
Drop
<"H20)
40
•
Water
Pressure
(P8i)
55
Water
Temp.
<°P)
Outlet Conditions
Dry
Bulb
<°F)
78
Wet
Bulb
<°F>
76
Static
Pressure
<"H,0)
54.4
Recirculated
Water
Flov
(gP«)
880
•
Fan
Motor
Current
(amp)
210
•
a
i
in
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-10-75
Atmospheric Pressure: 29.34 Initial:
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
Mo.
24
34
44
X54
X64
6
16
26
36
46
X56
8
18
28
38
Push
Time
1207
1221
1230
1242
1252
1300
1325
1337
1358
1410
1424
1436
1452
1505
1518
Inlet Conditions
Dry
Bulb
<°F)
220
Wet
Bulb
<°F)
Static
Pressure
("lUO)
•
-5.0
Velocity
Pressure
<"HZ0)
1.2
Throat Conditions
Pressure
Drop
("H20)
38
Water
Pressure
(psi)
55
Water
Temp.
<°F)
Outlet Conditions
Dry
Bulb
<°F)
85
Wet
Bulb
<°F)
83
Static
Pressure
("HX0)
.54.4
Recirculated
Water
Flow
(gpm)
880
Fan
Motor
Current
(amp)
210
in
00
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-14-75
Atmospheric Pressure:
Initial: RJP
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
X64
6
16
26
36
Push
Time
1431
1445
1502
1514
1526
Inlet Conditions
Dry
Bulb
<°F)
170
260
.
Wet
Bulb
(°F)
Static
Pressure
("H^O)
•
•
-3.5
-3.8
Velocity
Pressure
<"HZ0)
1.25
1.25
Throat Conditions
Pressure
Drop
("HzO)
38
38
Water
Pressure
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-15-75
Atmospheric Pressure:
Initial: TAL
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
X51
X61
3
13
23
33
43
S3
X63
^^
5
15
25
35
45
Push
Time
1300
1306
1325
1333
1345
1404
1409
1425
1440
1455
1507
1530
1535
1547
Inlet Conditions
Dry
Bulb
<°F)
190
Wet
Bulb
(QF)
Static
Pressure
<"HaO)
•
-5.0
Velocity
Pressure
(WH20)
1.2
Throat Conditions
Pressure
Drop
("H20)
40
Water
Pressure
(psl)
55
Water
Temp.
CF)
Outlet Conditions
Dry
Bulb
<°F>
82
Wet
Bulb
(°F)
80
Static
Pressure
("HZ0)
-54.4
Recirculated
Water
Flow
(gpm)
890
Fan
Motor
Current
(amp)
215
re
i
&<
o
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-16-75
Atmospheric Pressure:
Initial: TAL
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
12
22
32
42
X52
X62
^^^
4
14
24
34
44
X54
X64
6
Push
Time
1225
1233
1317
1330
1340
1348
1403
1422
1432
1440
1449
1502
1511
1535
Inlet Conditions
Dry
Bulb
CF)
250
290
260
Wet
Bulb
(°F)
Static
Pressure
C'HfcO)
•
-5.2
-5.0
-5.0
Velocity
Pressure
("HZ0)
1.4
1.5
1.4
Throat Conditions
Pressure
Drop
("HzO)
40
40
40
Water
Pressure
(psi)
55
55
55
Water
Temp .
(°F)
Outlet Conditions
Dry
Bulb
<°F)
86
84
82
Wet
Bulb
(°F)
84
82
80
Static
Pressure
C'HiO)
-54.4
-54.4
-54.4
Recirculated
Water
Flov
(gpm)
•
890
890
890
Fan
Motor
Current
(amp)
•
215
215
215
PC
I
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-17-75
Atmospheric Pressure:
Initial: RJP
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
Mo.
21
31
41
X51
X61
3
13
23
33
43
X53
X63
_
5
15
Push
Time
1200
1216
1232
1248
1304
1320
1336
1352
1408
1424
1441
1454
1514
1528
Inlet Conditions
Dry
Bulb
<°F>
220
230
.
Wet
Bulb
CF)
Static
Pressure
("HaO)
•
•
-5.0
-4.5
Velocity
Pressure
("H20)
1.4
1.35
Throat Conditions
Pressure
Drop
("H20)
38
38
Water
Pressure
(psi)
56
58
Water
Temp.
<°P)
76
76
Outlet Conditions
Dry
Bulb
<°F)
78
78
Wet
Bulb
(°F)
76
76
Static
Pressure
("H*0)
-54
-56
Recirculated
Water
Flow
(gpn)
880
880
Fan
Motor
Current
(amp)
215
215
BB
ro
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-18-75
Atmospheric Pressure:
Initial:
RJP
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
22
32
Push
Time
1304
1315
Inlet Conditions
Dry
Bulb
<°F)
230
220
Wet
Bulb
<°F)
Static
Pressure
("H£0)
•
-5.0
-5.0
•
Velocity
Pressure
("H*0)
1.3
1.3
Throat Conditions
Pressure
Drop
("H20)
38
37
Water
Pressure
(pal)
56
56
Water
Temp.
(°F)
68.0
68.0
Outlet Conditions
Dry
Bulb
(°F)
78
78
Wet
Bulb
<°F)
76
77
Static
Pressure
<"IUO)
-65
-65
Recirculated
Water
Flow
(gpm)
880
880
Fan
Motor
Current
(amp)
215
215
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-21-75
Atmospheric Pressure:
Initial: RJP
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
'
X58
__
1
Push
Time
1225
1236
Inlet Conditions
Dry
Bulb
CF)
180
280
.
Wet
Bulb
CF)
Static
Pressure
("H^O)
•
-4.3
-5.0
Velocity
Pressure
<"H20)
1.25
1.45
Throat Conditions
Pressure
Drop
<"H20)
38
38
Water
Pressure
(psi)
55
56
Water
Temp.
CF)
68
68
Outlet Conditions
Dry
Bulb
CF)
79
79
Wet
Bulb
CF)
76
76
Static
Pressure
("HiO)
-65
-67
Recirculaeed
Water
Flow
(gp«)
880
880
Fan
Motor
Current
(amp)
215
215
i
CT»
•P-
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date:
7-22-75
Atmospheric Pressure:
Initial: RJP
Push
1
2
3
4
5
6
7
8
9
10
11
12
13
14
IS
.
Oven
No.
.
IS
25
Push
Time
0932
0940
• Inlet Conditions
Dry
Bulb
(°F)
460
280
.
Wet
Bulb
(°F)
Static
Pressure
<"HaO)
•
-4.6
-4.8
Velocity
Pressure
(HH*0)
1.3
1.4
Throat Conditions
Pressure
Drop
("H20)
38
38
Water
Pressure
(psi)
48
48
Water
Temp.
(°F)
69
69
Outlet Conditions
Dry
Bulb
(°F)
77
77
Wet
Bulb
<°F)
76
76
Static
Pressure
<"H,0)
-30
-30
Recirculated
Water
Flow
(gpn)
880
880
•
Fan
Motor
Current
(amp)
215
215
•
•
S
Ul
-------
DAILY LOG OF SCRUBBER SYSTEM PERFORMANCE
Ford Motor Company * Rouge Plant * Dearborn, Michigan
Date: 9-3-75
Atmospheric Pressure: 29.4 Initial: RJP
Push
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
Oven
No.
36
I
Push
Time
1208
Inlet Conditions
Dry
Bulb
(°F)
Wet
Bulb
(°F>
Static
Pressure
<"HaO)
-3.5
•
Velocity
Pressure
("HaO)
1.1
Throat Conditions
Pressure
Drop
<"H20)
41
Water
Pressure
(psi)
60
Water
Temp.
<°F)
60
Outlet Conditions
Dry
Bulb
(°F)
Wet
Bulb
(°F)
Static
Pressure
<"H»0)
57.1
Recirculated
Water
Flow
(gpm)
890
Fan
Motor
Current
(•up)
215
a
i
-------
APPENDIX I
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
-------
1-1
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No.: 1
Sampling Location:
EPA Method 5
Sampling Date:
Scrubber Inlet
6-24-75 - 6-25-75
Push
Time
0943
1036
1052
1103
1117
1132
1146
1158
1330
1340
1426
1438
Oven
Number
1
31
41
X51
X61
3
13
23
X53
X63
35
45
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
3
1
1
1
3
3
3
1
3
3
1
Coke
Oven
Flue
Temp.
(°F)
2510
2420
2500
2550
2440
2440
2420
2410
2430
2390
2460
2470
Cross
Draft
Velocity
(fpm)
355
130
485
230
80
115
200
310
280
360
400
Stack
Gas
Opacity
(Percent)
40
0
0
0
75
60
60
0
50
60
20
Net
Coal
Charged
(Ibs)
38,050
36, 100
35,450
35,200
(35,700)
34,800
35,350
36, 350
(35,700)
35,550
35,750
35, 000
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psl)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.)
Clayton Environmental Consultants, Inc,
-------
1-2
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: EPA Method 5
Test No.: 1 Sampling Date:
Sampling Location: Scrubber Inlet
6-24-75 - 6-25-75
Push
Time
6-25
1005
1018
1029
1040
1253
1310
1332
1342
1353
1403
1417
1428
Oven
Number
39
49
X59
2
4
24
34
44
X54
X64
6
16
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
2
3
1
3
3
3
3
2
2
3
3
3
2.3
Coke
Oven
Flue
Temp.
(°F)
2460
2420
2420
2440
2360
2300
2400
2490
2440
2380
2510
2400
Cross
Draft
Velocity
(fpm)
120
120
100
150
620
190
60
170
220
180
200
260
230
Stack
Gas
Opacity
(Percent)
40
40
10
60
60
60
40
5
10
40
30
60
35
Net
Coal
Charged
(Ibs)
32,550
34,500
34.350
34,700
34,950
34,700
34,450
34,200
34,400
34,450
34,350
34,050
35,050
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (pal)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM) 800
Fan Motor Current (AMP) 210
Gross Coking Time (mln.) 985
Clayton Environmental Consultants, Inc.
-------
1-3
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: EPA Method 5
Test No. : 1
Sampling Location:
Sampling Date:
Scrubber Outlet
6-24-75 - 6-25-75
Push
Time
0943
1036
1052
1103
1117
1132
1146
1158
1330
1340
1426
6-25
0946
Oven
Number
1
31
41
X51
X61
3
13
23
X53
X63
35
19
TEST
AVERAGE
Greenness
(Engineering
Observer ' s
Estimate)
3
1
1
1
3
3
3
1
3
3
3
Coke
Oven
Flue
Temp.
(°F)
2420
Cross
Draft
Velocity
(fpm)
355
130
485
230
80
115
200
310
280
360
160
Stack
Gas
Opacity
(Percent)
40
0
0
0
75
60
60
0
50
60
60
Net
Coal
Charged
(Ibs)
38,050
36, 100
35,450
35,200
(35,700)
34,800
35, 350
36, 350
(35,700)
35,550
35, 750
35, 250
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psl)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.)
Clayton Environmental Consultants, Inc.
-------
1-4
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No. : 1
EPA Method 5
Sampling Location:
Sampling Date:
Scrubber Outlet
6-24-75 - 6-25-75
Push
Time
1005
1018
1029
1040
1253
1310
1332
1342
1353
1403
1417
1428
Oven
Number
39
49
X59
2
4
24
34
44
^X54
X64
6
16
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
2
3
1
3
3
3
3
2
2
3
3
3
2.4
Coke
Oven
Flue
Temp.
(°F)
Cross
Draft
Velocity
(fpm)
120
120
100
150
620
190
60
170
220
180
200
260
220
Stack
Gas
Opacity
(Percent)
40
40
10
60
60
60
40
5
10
40
30
60
35
Net
Coal
Charged
(Ibs)
32,550
34,500
34,350
34,700
34,950
34,700
34,450
34,200
34,400
34,450
34,350
34,050
34,050
Averages
Inlet Dry Bulb (°F) 215
Inlet Stat. Pres. ("H20) .4.5
Throat Pres. Drop ("H20) 42
Water Pres. (psl) 4p
Outlet Dry Bulb (°F) ag
Outlet Wet Bulb (°F) 83
Outlet Stat. Pres. ("H20) ,49
Water Flow (GPM) BOO
Fan Motor Current (AMP) 210
Gross Coking Time (mln.) gas
Clayton Environmental Consultants, Inc.
-------
1-5
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: EPA Mpthpd 5
Test No.: 2 Sampling Date:
Sampling Location: Scrubber Inlet
6-26-75 - 6-27-75
Push
Time
0925
1016
1039
1049
1102
1125
1139
1255
1310
1332
1337
1345
Oven
Number
48
1
21
31
41
X51
X61
23
33
43
X53
X63
TEST
AVERAGE
Greenness
(Engineering
Observer ' s
Estimate)
3
2
1
3
1
1
—
—
3
1
1
1
Coke
Oven
Flue
Temp.
<°F>
2260
2300
2430
2480
2350
2490
2420
2330
2400
2320
2450
2390
Cross
Draft
Velocity
(fpm)
310
270
250
310
400
220
90
480
330
220
270
Stack
Gas
Opacity
(Percent)
30
30
5
40
5
0
—
..
40
0
0
0
Net
Coal
Charged
(Ibs)
31,050
34, 550
34,900
34,750
32,050
32, 800
33, 000
35,750
35,450
35, 600
35, 700
33,850
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Fres. (psi)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (mln.)
Clayton Environmental Consultants, Inc,
-------
1-6
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: EPA Method 5
2
Test No.:
Sampling Location:
Sampling Date:
Scrubber Inlet
6-26-75 - 6-27-75
Push
Time
1408
1438
1458
1504
6-27
1056
1108
1135
1158
1325
1340
1405
1424
Oven
Number
15
35
45
X55
39
49
2
22
4
14
24
34
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
3
3
3
1
1
3
3
3
3
1
2
3
2.1
Coke
Oven
Flue
Temp.
(°F)
2360
2380
2440
2420
No
data
No
data
No
data
No
data
No
data
No
data
No
data
No
data
Cross
Draft
Velocity
(fpm)
280
250
170
350
240
200
240
270
260
350
170
320
270
Stack
Gas
Opacity
(Percent)
20
10
60
10
0
20
30
30
20
10
10
20
20
Net
Coal
Charged
(Ibs)
31,650
34,650
34,850
33,850
34,650
34,250
34,800
33,500
33,800
34,350
34,900
33,300
34,100
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop
Water Pres. (psl)
Outlet Dry Bulb (°F)
583
-4.7
Outlet Wet Bulb (°F)
Outlet Stat. Pres.
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.)
1005
Clayton Environmental Consultants, Inc,
-------
1-7
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No. : 2
Sampling Location:
EPA Method 5
Sampling Date:
Scrubber Outlet
6-26-75 - 6-27-75
Push
Time
0925
1016
1039
1049
1102
1125
1139
1255
1310
1332
1337
1345
Oven
Number
48
1
21
31
41
X51
X61
23
33
43
X53
X63
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
3
2
1
3
1
1
_
-
3
1
1
1
Coke
Oven
Flue
Temp.
(°F)
Cross
Draft
Velocity
(fpm)
310
270
250
310
400
220
90
_
480
330
220
270
Stack
Gas
Opacity
(Percent)
30
30
5
40
5
0
-
-
40
0
0
0
Net
Coal
Charged
(Ibs)
31,050
34,550
34, 900
34,750
32,050
32,800
33,000
35,750
35,450
35,600
35, 700
33,850
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psi)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.)
Clayton Environmental Consultants, Inc.
-------
1-8
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: EPA Method 5
Teat No.: 2 Sampling Date:
Sampling Location: Scrubber Outlet
6-26-75 - 6-27-75
Push
Time
1408
1438
1458
1504
6-27
1040
1108
1120
1158
1325
1340
1405
1424
Oven
Number
15
35
45
X55
29
49
X59
22
4
14
24
34
TEST
AVERAGE
Greenness
(Engineering
Observer* a
Estimate)
3
3
3
1
•?
3
1
3
3
1
2
3
2.1
Coke
Oven
Flue
Temp.
(QF)
Cross
Draft
Velocity
(fpm)
280
250
170
350
170
200
190
270
260
350
170
320
270
Stack
Gas
Opacity
(Percent)
20
10
60
10
40
20
0
30
20
10
10
20
20
Net
Coal
Charged
(Ibs)
31,650
34,650
34,850
33,850
34,800
34,250
34,750
33,500
33,800
34,350
34,900
33,300
34, 100
583
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20) -4.7
Throat Pres. Drop ("H20) 40
Water Pres. (psi)
Outlet Dry Bulb (°F)
40
93
Outlet Wet Bulb (°F) 91
Outlet Stat. Pres. ("H20) -46
Water Flow (GPM) 785
Fan Motor Current (AMP) 210
Gross Coking Time (mln.) 1QQ5
Clayton Environmental Consultants, Inc,
-------
1-9
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No.: 3
Sampling Location:
EPA Method 5
Sampling Date: 6-30-75, 7-1-75 and 7-2-75
Scrubber Inlet
Push
Time
0854
0905
0920
0943
0954
1003
1011
1027
1045
1056
1220
1247
Oven
Number
X64
6
16
26
36
46
X56
8
18
28
11
21
TEST
AVERAGE
Greenness
(Engineering
Observer ' s
Estimate)
2
3
2
2
2
2
1
3
3
3
1
3
Coke
Oven
Flue
Temp.
(°F)
2340
2480
2460
2400
2480
2440
2260
2270
2240
2300
2360
Cross
Draft
Velocity
(fpm)
200
220
210
300
240
270
230
340
270
310
370
280
Stack
Gas
Opacity
(Percent)
5
20
10
10
5
10
10
40
20
50
0
30
Net
Coal
Charged
(Ibs)
39, 100
35,550
29,750
35,350
(33,850)
34,250
32, 900
32,850
33,000
(33,850)
31,150
33,300
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres.. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psi)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.)
Clayton Environmental Consultants, Inc.
-------
1-10
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No.: 3
EPA Method 5
Sampling Date: 6-30-75, 7-1-75 and 7-2-75
Sampling Location: Scrubber Inlet
Push
Time
1330
1350
1402
1415
1423
1448
1458
7-1
0851
0935
7-2
0921
0928
0946
Oven
Number
41
X51
X61
3
13
23
33
X53
15
24
34
44
TEST
AVERAGE
Greenness
(Engineering
Observer' a
Estimate)
3
1
1
3
2
3
3
1
fm
3
3
3
2.3
Coke
Oven
Flue
Temp.
(°F)
2230
2420
2380
2340
2380
2340
2380
2260
2360
2400
2360
Cross
Draft
Velocity
(fpm)
120
150
230
280
230
80
540
150
^
60
100
150
230
Stack
Gas
Opacity
(Percent)
50
0
0
60
30
30
60
0
—
50
40
30
25
Net
Coal
Charged
(Ibs)
34,850
34,400
34,800
33,800
33,800
33,450
(33,850)
36,100
35, 850
35,050
34,250
34,900
34,250
Averages
Inlet Dry Bulb (°F) 393
Inlet Stat. Pres. ("H20) -5.2
Throat Pres. Drop ("H20) 38
Water Pres. (psi) 40
Outlet Dry Bulb (°F) 90
Outlet Wet Bulb (°F) 88
Outlet Stat. Pres. ("H20) -52.6
Water Flow (GPM) 770
Fan Motor Current (AMP) 220
Gross Coking Time (min.) 982
Clayton Environmental Consultants, Inc,
-------
1-11
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: EPA Method 5
3
Teat No.:
Sampling Location:
Sampling Date: 6-30-75, 7-1-75 and 7-2-75
Scrubber Outlet
Push
Time
0854
0905
0920
0943
0954
1003
1011
1027
1045
1056
1220
1247
Oven
Number
X64
6
16
26
36
46
X56
8
18
28
11
21
TEST
AVERAGE
Greenness
(Engineering
Observer1 s
Estimate)
2
3
2
2
2
2
1
3
3
3
1
3
Coke
Oven
Flue
Temp.
<°F)
Cross
Draft
Velocity
(fpm)
200
220
210
300
240
270
230
340
270
310
370
280
Stack
Gas
Opacity
(Percent)
5
20
10
10
5
10
10
40
20
50
0
30
Net
Coal
Charged
(Ibs)
39, 100
35,550
29, 750
34, 350
(33,850)
34, 250
32, 900
32,850
33,000
(33,850)
31, 150
33,300
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psi)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.)
Clayton Environmental Consultants, Inc.
-------
1-12
SUMMARY 0? PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: EPA Method 5
Test No.: 3
Sampling Location:
Sampling Date: 6-30-75. 7-1-75 and 7-2-75
Scrubber Outlet
Push
Time
1330
1350
1402
1415
1423
1458
1513
7-1
0851
0935
7-2
0921
0928
0946
Oven
Number
41
X51
X61
3
13
33
43
X53
15
24
34
44
TEST
AVERAGE
Greenness
(Engineering
Observer1 s
Estimate)
3
1
1
3
2
3
3
1
3
3
3
2.3
Coke
Oven
Flue
Temp.
(8F)
2340
Cross
Draft
Velocity
(fpm)
120
150
230
280
230
540
360
150
60
100
150
240
Stack
Gas
Opacity
(Percent)
50
0
0
60
30
60
20
0
50
40
30
25
Net
Coal
Charged
(Ibs)
34,850
34,400
35,800
33,800
33,800
(33,850)
(33,850)
36,100
35,850
35,050
35,250
34,900
34,250
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psl)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F) 88
Outlet Stat. Pres. ("H20) -52.6
Water Flow (GPM) 770
Fan Motor Current (AMP) 220
Gross Coking Time (min.) 982
Clayton Environmental Consultants, Inc,
-------
1-13
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: EPA Method 5
Teat No.: 4 Sampling Date: 7-2-75 - 7-3-75
Sampling Location: Scrubber Inlet & Outlet
Push
Time
1327
1335
1345
1355
1415
1442
1455
1505
1535
1545
7-3
0838
0903
Oven
Number
48
X58
1
11
21
31
41
X51
3
13
13
33
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
1
1
1
3
3
3
1
3
3
J.
2
Coke
Oven
Flue
Temp.
(°F)
2260
2400
2360
2390
2300
2260
2410
2430
2360
2410
2350
Cross
Draft
Velocity
(fpm)
260
350
270
460
360
320
280
320
280
150
230
Stack
Gas
Opacity
(Percent)
10
0
0
50
40
20
5
40
20
0
20
Net
Coal
Charged
(Ibs)
33, 300
(34,800)
34,800
35,000
34,850
34,950
35, 100
35,600
35, 150
34, 950
(26. 0501
36, 200
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psl)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (mip.)
Clayton Environmental Consultants, Inc.
-------
1-14
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No.: 4
EPA Method 5
Sampling Date: 7-2-75 - 7-3-75
Sampling Location: Scrubber Inlet & Outlet
Push
Time
0939
0954
1006
1027
Oven
Number
X53
X63
5
15
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
3
1
1
3
2.0
Coke
Oven
Flue
Temp.
(°F)
2480
2420
2460
2340
Cross
Draft
Velocity
(fpm)
260
320
170
320
290
Stack
Gas
Opacity
(Percent)
20
0
0
60
20
Net
Coal
Charged
(Ibs)
35,500
35,550
34,600
34,700
35,050
Averages
350
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20) -5.2
Throat Pres. Drop ("H20) 38
Water Prea. (pal) 40
Outlet Dry Bulb (°F) 90
Outlet Wet Bulb (°F) 89
Outlet Stat. Pres. ("H20) -53.U
Water Flow (GPM) 780
Fan Motor Current (AMP) 220
Gross Coking Time (mln.) 997
Clayton Environmental Consultants, Inc.
-------
1-15
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: EPA Method 5
5
Test No. :
Sampling Date: 7-8-75
Sampling Location: Scrubber Inlet & Outlet
Push
Time
0928
1017
1033
1043
1056
1141
1213
1245
1305
1320
1335
1345
Oven
Number
12
X52
X62
4
14
24
44
X54
6
16
26
36
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate )
_
1
1
1
3
1
1
1
2
2
1
1
Coke
Oven
Flue
Temp.
(°F)
2300
2420
2380
2340
2160
2400
2360
2420
2400
2340
2400
2400
Cross
Draft
Velocity
(fpm)
—
170
240
170
260
240
_
180
220
360
300
350
Stack
Gas
Opacity
(Percent)
_
0
0
0
20
0
0
0
10
10
0
5
Net
Coal
Charged
(Ibs)
34,550
34, 900
34,350
32,000
34,250
34,000
33,450
33,600
34,800
33,200
33, 900
(33,600)
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psi)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (mj.n.)
Clayton Environmental Consultants, Inc.
-------
1-16
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: EPA Method 5
5
Test No. :
Sampling Date:
7-8-75
Sampling Location: Scrubber Inlet & Outlet
Push
Time
1403
1421
1440
1449
Oven
Number
46
X56
8
18
TEST
AVERAGE
Greenness
(Engineering
Observer ' s
Estimate)
1
2
3
1
1.5
Coke
Oven
Flue
Temp.
(°F)
2420
2410
2190
2400
Cross
Draft
Velocity
(fpm)
240
290
250
300
260
Stack
Gas
Opacity
(Percent)
5
0
30
0
5
Net
Coal
Charged
(Ibs)
34,350
28,050
32,850
35,050
33,550
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psi)
Outlet Dry Bulb (°F)
233
Outlet Wet Bulb (°F) 82
Outlet Stat. Pres. ("H20) -54.4
Water Flow (GPM) 840
Fan Motor Current (AMP) 215
Gross Coking Time (min.) 1019
Clayton Environmental Consultants, Inc,
-------
1-17
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No. : 6
EPA Method 5
Sampling Date:
7-10-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
0940
0953
1017
1045
1057
1107
1120
1242
1252
1337
1358
1410
Oven
Number
2
12
22
42
X52
X62
4
X54
X64
26
36
46
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
1
3
1
.
1
1
1
1
2
2
2
2
Coke
Oven
Flue
Temp.
(°F)
2360
2280
2320
2350
2380
2380
2400
2400
2380
2380
2360
2470
Cross
Draft
Velocity
(fpm)
230
280
270
—
190
210
300
240
360
670
570
520
Stack
Gas
Opacity
(Percent)
5
30
5
—
0
0
5
10
20
30
20
10
Net
Coal
Charged
(Ibs)
33,500
35,000
36,650
34,150
34, 150
34,500
33, 750
33,850
34, 350
34,650
33,800
33,500
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psi)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.)
Clayton Environmental Consultants, Inc.
-------
1-18
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: EPA Method 5
6
Test No. :
Sampling Location:
Sampling Date: 7-10-75
Scrubber Inlet & Outlet
Push
Time
1424
1436
1452
1505
Oven
Number
X56
8
18
28
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
1
3
3
3
1.8
Coke
Oven
Flue
Temp.
(°F)
2380
2250
2340
2340
Cross
Draft
Velocity
(fpm)
730
850
910
580
460
Stack
Gas
Opacity
(Percent)
0
60
40
30
20
Net
Coal
Charged
(Ibs)
35,300
35,700
35,150
35,550
34,600
Averages
Inlet Dry Bulb (°F) 225
Inlet Stat. Pres. ("HaO) -5.2
Throat Pres. Drop ("H20) 39
Water Pres. (psi) 55
Outlet Dry Bulb (°F) 82
Outlet Wet Bulb (°F) 80
Outlet Stat. Pres. ("H20) -54.4
Water Flow (GPM) 880
Fan Motor Current (AMP) 210
Gross Coking Time (mln.) 987
Clayton Environmental Consultants, Inc,
-------
1-19
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: EPA Method 5
Test No.: 7 Sampling Date:
7-14-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
0840
0923
0932
0950
1022
1033
1058
1110
1245
1255
1318
1338
Oven
Number
37
X57
9
19
29
39
X59
2
X52
X62
4
14
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
1
1
3
2
1
2
3
1
3
2
1
1
Coke
Oven
Flue
Temp.
(°F)
2460
2300
2440
2510
2420
2420
2440
2400
2440
2330
2410
Cross
Draft
Velocity
(fpm)
160
300
510
490
270
450
460
350
550
900
350
390
Stack
Gas
Opacity
(Percent)
10
10
60
20
0
30
60
5
50
40
5
5
Net
Coal
Charged
(Ibs)
32,500
32,850
34,450
32, 350
31,850
33,000
33,400
31,950
33, 100
(32,800)
(32,800)
(32, 800)
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psi)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.)
Clayton Environmental Consultants, Inc.
-------
1-20
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No. : 7
EPA Method 5
Sampling Date:
7-14-75
Sampling Location: Scrubber Inlet & Outlet
Push
Time
1347
1358
1410
1424
Oven
Number
24
34
44
X54
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
1
1
2
2
1.7
Coke
Oven
Flue
Temp.
(QF)
2400
2390
2390
2440
Cross
Draft
Velocity
(fpm)
540
1100
330
380
470
Stack
Gas
Opacity
(Percent)
0
5
40
20
20
Net
Coal
Charged
(Ibs)
33, 150
32, 700
30,400
33,050
32,700
Averages
Inlet Dry Bulb (°F) 215
Inlet Stat. Pres. ("H20) -3.6
Throat Pres. Drop ("H20) 38
Water Pres. (psi) 47
Outlet Dry Bulb (°F) 75
Outlet Wet Bulb (°F) 72
Outlet Stat. Pres. (MH20) -54.4
Water Flow (GPM) 880
Fan Motor Current (AMP) 215
Gross Coking Time (mln.) 990
Clayton Environmental Consultants, Inc.
-------
1-21
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: EPA Method 5
8
Test No.:
Sampling Date: 7-15-75
Sampling Location: Scrubber Inlet & Outlet
Push
Time
0830
0847
0920
0929
0958
1054
1104
1125
1140
1156
1300
1325
Oven
Number
46
X56
8
18
38
1
11
21
31
41
X51
3
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
1
1
2
1
1
1
3
1
1
3
_
2
Coke
Oven
Flue
Temp.
<°F)
2430
2420
2440
2360
2200
2500
2440
2320
2410
2300
Cross
Draft
Velocity
(fpm)
100
250
120
150
210
220
190
190
220
610
_
270
Stack
Gas
Opacity
(Percent)
0
0
20
0
0
0
40
0
10
30
_
10
Net
Coal
Charged
(Ibs)
33, 300
32,950
33,700
33, 500
33,750
34,650
33,300
32, 250
34,250
32,450
33,750
33,050
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psi)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.)
Clayton Environmental Consultants, Inc,
-------
1-22
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: EPA Method 5
Test No.:
8
Sampling Date:
7-15-75
Sampling Location: Scrubber Inlet & Outlet
Push
Time
1333
1345
1404
1409
Oven
Number
13
23
33
43
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
1
1
1
1
1.4
Coke
Oven
Flue
Temp.
(°F>
2360
2440
2450
2410
Cross
Draft
Velocity
(fpm)
510
240
270
580
280
Stack
Gas
Opacity
(Percent)
5
5
0
0
10
Net
Coal
Charged
(Ibs)
35,050
34,350
32, 150
34,250
33,550
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (pal)
Outlet Dry Bulb (°F)
40
55
82
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.)
215
998
Clayton Environmental Consultants, Inc,
-------
1-23
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: EPA Method 5
Teat No.: 9
Sampling Date:
7-16-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
0824
0840
0853
0934
0941
0952
1006
1035
1050
1109
1123
1137
Oven
Number
45
X55
7
17
27
37
47
X57
9
19
29
39
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
1
1
3
1
2
1
2
1
3
1
1
1
Coke
Oven
Flue
Temp.
(°F)
2420
2390
2380
2490
2430
2240
2420
2460
2360
Cross
Draft
Velocity
(fpm)
150
170
140
270
160
120
170
420
260
150
320
370
Stack
Gas
Opacity
(Percent )
0
10
40
0
10
0
10
5
40
0
0
0
Net
Coal
Charged
(Ibs)
(35, 200)
(34, 300)
35,450
33,400
35,700
35,650
33, 800
(34, 300)
35,850
34,450
33,500
34,200
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop< ("H20)
Water Pres. (psl)
Outlet Dry Bulb (,°F)
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (mtn.)
Clayton Environmental Consultants, Inc,
-------
1-24
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Teat No.: 9
EPA Method 5
Sampling Date:
Sampling Location: Scrubber Inlet & Outlet
7-16-75
Push
Time
1203
1217
1340
1348
Oven
Number
X59
2
X52
X62
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
1
1
1
1
1.4
Coke
Oven
Flue
Temp.
(°F)
2380
2400
2370
2380
Cross
Draft
Velocity
(fpm)
490
360
450
430
280
Stack
Gas
Opacity
(Percent)
0
5
0
0
5
Net
Coal
Charged
(Ibs)
35,550
35,400
32,150
33,200
•
34,500
Averages
Inlet Dry Bulb (°F) 267
Inlet Stat. Pres. ("H20) -5. 1
Throat Pres. Drop ("H20)
Water Pres. (psi)
Outlet Dry Bulb (°F) 84
Outlet Wet Bulb (°F) 82
Outlet Stat. Pres. ("H20) -54.4
Water Flow (GPM) 890
Fan Motor Current (AMP) 215
Gross Coking Time (min.) 999
Clayton Environmental Consultants, Inc,
-------
1-25
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: EPA Method 8
Test No.: 1 Sampling Date:
6-5-75
Sampling Location: Scrubber Inlet & Outlet
Push
Time
1502
1522
1616
1625
Oven
Number
17
27
37
47
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
2
2
_
2
2
Coke
Oven
Flue
Temp.
(°F)
2370
2500
2410
2460
Cross
Draft
Velocity
(fpm)
480
980
_
440
630
Stack
Gas
Opacity
(Percent)
30
25
—
20
25
Net
Coal
Charged
(Ibs)
35, 150
34,700
(35,350)
(35,250)
35,100
Averages
Inlet Dry Bulb (°F) 212
Inlet Stat. Pres. ("H20) -4.2
Throat Pres. Drop ("H20) 45
Water Pres. (psi), 39
Outlet Dry Bulb (°F) 82
Outlet Wet Bulb (°F) 80
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP) 170
Gross Coking Time (min.) 989
Clayton Environmental Consultants, Inc.
-------
1-26
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No.: 2
EPA Method 8
Sampling Date: 6-6-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1004
1027
1049
Oven
Number
9
19
29
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
1
1
3
1.7
Coke
Oven
Flue
Temp.
(°F)
2510
2460
2510
Cross
Draft
Velocity
(fpm)
690
515
530
580
Stack
Gas
Opacity
(Percent)
10
5
40
20
Net
Coal
Charged
(Ibs)
35,350
35,500
36,050
34,650
Averages
Inlet Dry Bulb (°F) 240
Inlet Stat. Pres. ("H20) -5.3
Throat Pres. Drop ("H20) 43
Water Pres. (psi) 38
Outlet Dry Bulb (°F) 77
Outlet Wet Bulb (°F) 73
Outlet Stat. Pres. ("H20) -50.8
Water Flow (GPM) 793
Fan Motor Current (AMP) 215
Gross Coking Time (min.) 1033
Clayton Environmental Consultants, Inc,
-------
1-27
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No. : 3
EPA Method 8
Sampling Date:
6-6-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1127
1141
1150
Oven
Number
X59
2
12
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
2
1
2
1.7
Coke
Oven
Flue
Temp.
<°F)
2440
2460
2320
Cross
Draft
Velocity
(fpm)
660
450
830
650
Stack
Gas
Opacity
(Percent)
20
15
30
20
Net
Coal
Charged
(Ibs)
35, 150
35,050
34, 950
35,050
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Free. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psi)
Outlet Dry Bulb (°F)
240
-5.3
Outlet Wet Bulb (°F) 73
Outlet Stat. Pres. ("H20) -50.8
Water Flow (GPM) 793
Fan Motor Current (AMP) 215
Gross Coking Time (min.) 1024
Clayton Environmental Consultants, Inc.
-------
1-28
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: EPA Method 8
Test No.: 4 Sampling Date: 6-6-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1338
1355
1410
Oven
Number
14
34
44
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
1
1
3
1.7
Coke
Oven
Flue
Temp.
(°F)
2480
2500
2420
Cross
Draft
Velocity
(fpm)
480
650
790
640
Stack
Gas
Opacity
(Percent)
10
5
45
20
Net
Coal
Charged
(Ibs)
30,800
34,600
34,700
33,350
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. (
Throat Pres. Drop ("H20)
Water Pres. (psl) 38
Outlet Dry Bulb (°F) 77
Outlet Wet Bulb (°F) 73
Outlet Stat. Pres. ("H20) .50.8
Water Flow (GPM) 793
Fan Motor Current (AMP) 215
Gross Coking Time (mln.) 999
Clayton Environmental Consultants, Inc.
-------
1-31
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No.: ^
EPA Method 8
Sampling Location:
Sampling Date:
Scrubber Inlet
6-9-75
Push
Time
1335
1345
1403
Oven
Number
13
23
43
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
_
_
_
-
Coke
Oven
Flue
Temp.
<°F)
Cross
Draft
Velocity
(fpm)
,
_
_
-
Stack
Gas
Opacity
(Percent)
_
_
_
-
Net
Coal
Charged
(Ibs)
35,050
35,050
34,950
35,000
Averages
Inlet Dry Bulb (°F) 148
Inlet Stat. Pres. ("H20) -5.0
Throat Pres. Drop ("H20) 44
Water Pres. (psl) 40
Outlet Dry Bulb (°F) 75
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.)
Clayton Environmental Consultants, Inc,
-------
1-32
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No.: 7
EPA Method 8
Sampling Location:
Sampling Date:
Scrubber Outlet
6-9-75
Push
Time
1322
1345
1403
Oven
Number
3
23
43
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
_
-
-
-
Coke
Oven
Flue
Temp.
(°F)
Cross
Draft
Velocity
(fpm)
_
-
-
-
Stack
Gas
Opacity
(Percent)
_
-
-
-
Net
Coal
Charged
(Ibs)
34,900
35,050
34,950
34,950
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psi)
Outlet Dry Bulb (°F)
44
40
76
Outlet Wet Bulb (°F) 75
Outlet Stat. Pres. ("H20) -52
Water Flow (GPM) 760
Fan Motor Current (AMP) 165
Gross Coking Time (min.) 998
Clayton Environmental Consultants, Inc.
-------
1-31
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No. : 7
EPA Method 8
Sampling Location:
Sampling Date:
Scrubber Inlet
6-9-75
Push
Time
1335
1345
1403
Oven
Number
13
23
43
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
_
_
-
-
Coke
Oven
Flue
Temp.
(°F)
Cross
Draft
Velocity
(fpm)
«•
_
_
-
Stack
Gas
Opacity
(Percent)
_
_
-
-
Net
Coal
Charged
(Ibs)
35,050
35,050
34,950
35,000
Averages
Inlet Dry Bulb (°F) 148
Inlet Stat. Pres. ("H20) -5.0
Throat Pres. Drop ("H20) 44
Water Pres. (psi) 40
Outlet Dry Bulb (°F) 76
Outlet Wet Bulb (°F) 75
Outlet Stat. Pres. ("H20) -52
Water Flow (GPM) 760
Fan Motor Current (AMP) 165
Gross Coking Time (min.) 999
Clayton Environmental Consultants, Inc.
-------
1-32
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No.: 7
EPA Method 8
Sampling Location:
Sampling Date:
Scrubber Outlet
6-9-75
Push
Time
1322
1345
1403
Oven
Number
3
23
43
TEST
AVERAGE
Greenness
(Engineering
Observer ' s
Estimate)
_
_
-
-
Coke
Oven
Flue
Temp.
(°F)
Cross
Draft
Velocity
(fpm)
_
_
-
-
Stack
Gas
Opacity
(Percent)
_
_
-
-
Net
Coal
Charged
(Ibs)
34,900
35,050
34,950
34,950
Averages
Inlet Dry Bulb (°F) 148
Inlet Stat. Pres. ("H20) -5.0
Throat Pres. Drop ("H20)
Water Pres. (psi)
Outlet Dry Bulb (°F) 76
Outlet Wet Bulb (°F) 75
Outlet Stat. Pres. ("H20) -52
Water Flow (GPM) 760
Fan Motor Current (AMP) 165
Gross Coking Time (min.) 998
Clayton Environmental Consultants, Inc,
-------
1-33
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No.: 8
EPA Method 8
Sampling Date:
6-9-75
Sampling Location: Scrubber Inlet & Outlet
Push
Time
1432
1447
1502
Oven
Number
X63
5
15
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
1
3
2.0
Coke
Oven
Flue
Temp.
(°F)
2400
2400
Cross
Draft
Velocity
(fpm)
540
480
510
Stack
Gas
Opacity
(Percent)
20
20
20
Net
Coal
Charged
(Ibs)
34.950
33,650
35,300
34,650
Averages
Inlet Dry Bulb (°F) 148
Inlet Stat. Pres. ("H20) -5.0
Throat Pres. Drop ("t^O) 44
Water Pres. (psi) 40
Outlet Dry Bulb (°F) 76
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.)
Clayton Environmental Consultants, Inc.
-------
1-34
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method;
Test No.: 9
EPA Method 8
Sampling Date:
6-10-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
0933
0950
1014
Oven
Number
X55
17
37
TEST
AVERAGE
Greenness
(Engineering
Observer1 s
Estimate)
3
3
3
3
Coke
Oven
Flue
Temp.
(°F)
2480
2390
2420
Cross
Draft
Velocity
(fpm)
350
410
370
380
Stack
Gas
Opacity
(Percent)
20
20
30
25
Net
Coal
Charged
(Ibs)
34.900
35,550
35,600
35,350
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psi)
Outlet Dry Bulb (°F)
427
83
Outlet Wet Bulb (°F) 81
Outlet Stat. Pres. ("H20) -51
Water Flow (GPM) 770
Fan Motor Current (AMP) 220
Gross Coking Time (min.) 1003
Clayton Environmental Consultants, Inc,
-------
1-35
SUMMARY 0? PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No. : 1
Sodium Hydroxide
Sampling Date:
6-3-75
Sampling Location: Scrubber Inlet & Outlet
Push
Time
1640
1653
1710
Oven
Number
29
39
49
TEST
AVERAGE
Greenness
(Engineering
Observer1 s
Estimate)
1
3
3
2.3
Coke
Oven
Flue
Temp.
(°F)
2510
2440
2460
Cross
Draft
Velocity
(fpm)
380
420
545
450
Stack
Gas
Opacity
(Percent)
15
20
55
30
Net
Coal
Charged
(Ibs)
f34r650}
(34.650^
(34.650)
34,650
Averages
Inlet Dry Bulb (°F) 248
Inlet Stat. Pres. ("H20) -4.8
Throat Pres. Drop ("H20) 41
Water Pres. (psl) 39
Outlet Dry Bulb (°F) 74
Outlet Wet Bulb (°F) 70
Outlet Stat. Pres. ("H20) -50.4
Water Flow (GPM) 750
Fan Motor Current (AMP) 170
Gross Coking Time (min.)
Clayton Environmental Consultants, Inc,
-------
1-36
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No.: 2
Sodium Hydroxide
Sampling Date:
6-4-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
0904
0914
0926
Oven
Number
9
19
29
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
1
1
2
1.3
Coke
Oven
Flue
Temp.
(°F)
2500
2520
2510
Cross
Draft
Velocity
(fpm)
300
320
360
330
Stack
Gas
Opacity
(Percent)
20
15
30
22
Net
Coal
Charged
(Ibs)
(35,250)
(35,250)
(35,250)
35,250
Averages
Inlet Dry Bulb (°F) 230
Inlet Stat. Pres. ("H20) -4.6
Throat Pres. Drop ("H20) 42
Water Pres. (psi) 39
Outlet Dry Bulb (°F) 82
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.) 1008
Clayton Environmental Consultants, Inc.
-------
1-37
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No. : 3
Sodium Hydroxide
Sampling Date:
6-4-75
Sampling Location: Scrubber Inlet & Outlet
Push
Time
1049
1104
1116
Oven
Number
2
12
22
TEST
AVERAGE
Greenness
(Engineering
Observer1 s
Estimate)
2
3
1
2.0
Coke
Oven
Flue
Temp.
(°F)
2470
2420
2470
Cross
Draft
Velocity
(fpm)
430
510
480
470
Stack
Gas
Opacity
(Percent)
25
25
10
20
Net
Coal
Charged
(Ibs)
36,550
36,650
35,950
36,400
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres.'("H20)
Throat Pres. Drop ("H20)
Water Pres. (psi)
Outlet Dry Bulb (°F)
230
-4.6
Outlet Wet Bulb (°F) 77
Outlet Stat. Pres. ("H20) -53.0
Water Flow (GPM) 750
Fan Motor Current (AMP) 170
Gross Coking Time (min.) 1021
Clayton Environmental Consultants, Inc,
-------
1-38
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No.: 4
Sodium Hydroxide
Sampling Date:
6-4-75
Sampling Location: Scrubber Inlet & Outlet
Push
Time
1300
1310
1317
Oven
Number
4
14
24
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
I
1
1
1
Coke
Oven
Flue
Temp.
(°F)
2470
2470
2490
Cross
Draft
Velocity
(fpm)
400
250
245
300
Stack
Ga>
Opacity
(Percent)
10
0
25
10
Net
Coal
Charged
(lb«)
35,800
36,050
35,100
35,650
Averages
230
Inlet Dry Bulb (°F)
Inlet Stat. Pres. (
Throat Pres. Drop ("H20)
Water Pres. (pal) 39
Outlet Dry Bulb (°F)
-4.6
42
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM) 750
Fan Motor Current (AMP) 170
Gross Coking Time (min.) 1011
Clayton Environmental Consultants, Inc,
-------
1-39
SUMMARY 07 PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No. : 5
Sodium Hydroxide
Sampling Date:
6-4-75
Sampling Location: Scrubber Inlet & Outlet
Push
Time
1458
1508
1519
Oven
Number
36
46
X56
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
3
3
3
3
Coke
Oven
Flue
Temp.
(°F)
2440
2370
2420
Cross
Draft
Velocity
(fpm)
265
290
355
300
Stack
Gas
Opacity
(Percent)
30
25
20
25
Net
Coal
Charged
(Ibs)
34,700
36, 100
31,750
34,200
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psi)
Outlet Dry Bulb (°F)
230
77
-53.0
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM) 750
Fan Motor Current (AMP) 170
Gross Coking Time (min.) 982
Clayton Environmental Consultants, Inc.
-------
1-40
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method;
Test No.: 6
Sodium Hydroxide
Sampling Date: 6-5-75
Sampling Location: Scrubber Inlet & Outlet
Push
Time
1226
1240
1250
Oven
Number
43
X53
X63
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
3
3
3
3
Coke
Oven
Flue
Temp.
(°F)
2420
2400
2360
Cross
Draft
Velocity
(fpm)
525
465
480
490
Stack
Gas
Opacity
(Percent)
40
30
40
35
Net
Coal
Charged
(Ibs)
35,600
35,350
35,450
35r450
Averages
Inlet Dry Bulb (°F) 212
Inlet Stat. Pres. ("H20) -4.2
Throat Pree. Drop ("H20) 45
Water Pres. (psl) 39
Outlet Dry Bulb (°F) 82
Outlet Wet Bulb (°F) 80
Outlet Stat. Pres. ("H20) -51.0
Water Flow (GPM) 760
Fan Motor Current (AMP) 170
Gross Coking Time (mln.) 968
Clayton Environmental Consultants, Inc,
-------
1-41
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: EPA Method 7
1
Test No. :
Sampling Location:
Sampling Date:
6-10-75
Scrubber Inlet & Outlet
Push
Time
1430
Oven
Number
34
TEST
AVERAGE
Greenness
(Engineering
Observer ' s
Estimate)
1
1
Coke
Oven
Flue
Temp.
<°F)
2470
Cross
Draft
Velocity
(fpm)
210
210
Stack
Gas
Opacity
(Percent)
10
10
Net
Coal
Charged
(Ibs)
36,700
36,700
Averages
Inlet Dry Bulb (°F) 427
Inlet Stat. Pres. ("H20) -5.7
Throat Pres. Drop ("H20) 45
Water Pres. (psi) 38
Outlet Dry Bulb (°F) 83
Outlet Wet Bulb (°F) 81
Outlet Stat. Pres. ("H20) -51
Water Flow (GPM) 770
Fan Motor Current (AMP) 220
Gross Coking Time (min.) 940
Clayton Environmental Consultants, Inc.
-------
1-42
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method;
Test No.: 2
EPA Method 7
Sampling Date: 6-10-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1458
Oven
Number
44
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
3
3
Coke
Oven
Flue
Temp.
<°F>
2340
Cross
Draft
Velocity
(fpm)
270
270
Stack
Gas
Opacity
(Percent)
40
40
Net
Coal
Charged
(Ibs)
(35,150)
35,150
Averages
Inlet Dry Bulb (°F) 427
Inlet Stat. Pres. ("H20) -5.7
Throat Pres. Drop ("HaO) 45
Water Pres. (psi) 38
Outlet Dry Bulb (°F) 83
Outlet Wet Bulb (°F) 81
Outlet Stat. Pres. ("H20) -51
Water Flow (GPM) 770
Fan Motor Current (AMP) 220
Gross Coking Time (min.) 963
Clayton Environmental Consultants, Inc,
-------
1-43
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No.: 3
EPA Method 7
Sampling Date:
6-10-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1510
Oven
Number
X54
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
1
1
Coke
Oven
Flue
Temp.
(°F)
2420
Cross
Draft
Velocity
(fpm)
320
320
Stack
Gas
Opacity
•(Percent)
10
10
Net
Coal
Charged
(Ibs)
35,100
35, 100
Averages
Inlet Dry Bulb (°F) 427
Inlet Stat. Pres. ("H20) -5.7
Throat Pres. Drop ("H20) 45
Water Pres. (psi) 38
Outlet Dry Bulb (°F) 83
Outlet Wet Bulb (°F) 81
Outlet Stat. Pres. ("H20) 51
Water Flow (GPM) 770
Fan Motor Current (AMP) 220
Gross Coking Time (min.) 965
Clayton Environmental Consultants, Inc,
-------
1-44
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No.: 4
EPA Method 7
Sampling Date:
6-10-75
Sampling Location: Scrubber Inlet & Outlet
Push
Time
1639
Oven
Number
6
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
1
1
Coke
Oven
Flue
Temp.
<°F)
2320
Cross
Draft
Velocity
(fpm)
300
300
Stack
Gas
Opacity
(Percent)
10
10
Net
Coal
Charged
(Ibs)
(35.150)
35,150
Averages
427
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20) -5.7
Throat Pres. Drop ("H20) 45
Water Pres. (psl) 38
Outlet Dry Bulb (°F) 83
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (mln.)
220
Clayton Environmental Consultants, Inc,
-------
1-45
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No. : 5
EPA Method 7
Sampling Date:
6-10-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1657
Oven
Number
16
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
3
3
Coke
Oven
Flue
Temp.
(°F)
2390
Cross
Draft
Velocity
(fpm)
250
250
Stack
Gas
Opacity
(Percent)
40
40
Net
Coal
Charged
(Ibs)
(35,150)
35,150
Averages
Inlet Dry Bulb (°F) 427
Inlet Stat. Pres. ("H20) -5.7
Throat Pres. Drop ("H20) 45
Water Pres. (psi) 38
Outlet Dry Bulb (°F) 83
Outlet Wet Bulb (°F) 81
Outlet Stat. Pres. ("H20) 51
Water Flow (GPM) 770
Fan Motor Current (AMP) 220
Gross Coking Time (min.) -
Clayton Environmental Consultants, Inc,
-------
1-46
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method;
Test No. : 6
EPA Method 7
Sampling Date:
6 11-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1455
Oven
Number
23
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
1
1
Coke
Oven
Flue
Temp.
<°F)
2380
Cross
Draft
Velocity
(fpm)
630
630
Stack
Gas
Opacity
(Percent)
10
10
Net
Coal
Charged
(Ibs)
35,700
35,700
Averages
Inlet Dry Bulb (°F) 257
Inlet Stat. Pres. ("H20) -4.9
Throat Pres. Drop ("H20) 39
Water Pres. (psl) 40
Outlet Dry Bulb (°F) 81
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (mln. )
988
Clayton Environmental Consultants, Inc,
-------
1-47
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No. : 7
EPA Method 7
Sampling Date:
6- 11-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1516
Oven
Number
43
TEST
AVERAGE
Greenness
(Engineering
Observer ' s
Estimate)
2
2
Coke
Oven
Flue
Temp.
<°F)
2340
Cross
Draft
Velocity
(fpm)
650
650
Stack
Gas
Opacity
(Percent)
40
40
Net
Coal
Charged
(Ibs)
36.050
36,050
Averages
Inlet Dry Bulb (°F) 257
Inlet Stat. Pres. ("H20) -4.9
Throat Pres. Drop ("H20) 39
Water Pres. (psi) 40
Outlet Dry Bulb (°F) 81
Outlet Wet Bulb (°F) 81
Outlet Stat. Pres. ("H20) -45
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (mln.) 979
Clayton Environmental Consultants, Inc,
-------
1-48
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No. : 8
EPA Method 7
Sampling Date:
6-11-75
Sampling Location: Scrubber Inlet & Outlet
Push
Time
1528
Oven
Number
X53
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
1
1
Coke
Oven
Flue
Temp.
(°F)
2450
Cross
Draft
Velocity
(fpm)
630
630
Stack
Gas
Opacity
(Percent)
10
10
Net
Coal
Charged
(Ibs)
36, 150
36, 150
Averages
257
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20) -4.9
Throat Pres. Drop ("H20)
Water Pres. (psi)
Outlet Dry Bulb (°F)
39
40
81
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM) -
Fan Motor Current (AMP) -
Gross Coking Time (min.) 985
Clayton Environmental Consultants, Inc.
-------
1-49
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: EPA Method 7
Test No.: 9 Sampling Date:
6-11-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1538
Oven
Number
X63
TEST
AVERAGE
Greenness
(Engineering
Observer1 s
Estimate)
1
1
Coke
Oven
Flue
Temp.
(°F)
2380
Cross
Draft
Velocity
(fpm)
610
610
Stack
Gas
Opacity
(Percent)
10
10
Net
Coal
Charged
(Ibs)
35,300
35,300
Averages
Inlet Dry Bulb (°F) 257
Inlet Stat. Pres. ("H20) -4.9
Throat Pres. Drop (MH20) 39
Water Pres. (psi)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM) -
Fan Motor Current (AMP) -
Gross Coking Time (mini) 983
Clayton Environmental Consultants, Inc,
-------
1-50
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No.: 10
EPA Method 7
Sampling Date:
7-18-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1220
Oven
Number
49
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
1
1
Coke
Oven
Flue
Temp.
(°F)
2420
Cross
Draft
Velocity
(fpm)
950
950
Stack
Gas
Opacity
(Percent)
0
0
Net
Coal
Charged
(Ibs)
34,500
34,500
Averages
Inlet Dry Bulb (°F) 225
Inlet Stat. Pres. ("H20) -5.0
Throat Pres. Drop ("H20) 38
Water Pres. (psl) 56
Outlet Dry Bulb (°F) 78
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20) -65
Water Flow (GPM) 880
Fan Motor Current (AMP) 215
Gross Coking Time (mln.) 1013
Clayton Environmental Consultants, Inc,
-------
1-51
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: EPA Method 7
11
Test No.:
Sampling Location:
Sampling Date: 7-18-75
Scrubber Inlet & Outlet
Push
Time
1227
Oven
Number
X59
TEST
AVERAGE
Greenness
(Engineering
Observer ' a
Estimate)
1
1
Coke
Oven
Flue
Temp.
(°F)
2380
Cross
Draft
Velocity
(fpm)
510
510
Stack
Gas
Opacity
(Percent)
5
5
Net
Coal
Charged
(Ibs)
34,650
34,650
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psi)
Outlet Dry Bulb (°F)
225
-5.0
76
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP) 215
Gross Coking Time (min.) 973
880
Clayton Environmental Consultants, Inc,
-------
1-52
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No. : 12
EPA Method 7
Sampling Date: 7-18-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1239
Oven
Number
2
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
2
2
Coke
Oven
Flue
Temp.
<°F)
2310
Cross
Draft
Velocity
(fpm)
430
430
Stack
Gas
Opacity
(Percent)
15
15
Net
Coal
Charged
(Ibs)
34.400
34,400
Averages
Inlet Dry Bulb (°F) 225
Inlet Stat. Pres. ("H20) -5.0
Throat Pres. Drop ("H20) 38
Water Pres. (psi) 56
Outlet Dry Bulb (°F) 78
Outlet Wet Bulb (°F) 76
Outlet Stat. Pres. ("H20) -65
Water Flow (GPM) 880
Fan Motor Current (AMP) 215
Gross Coking Time (min.) 972
Clayton Environmental Consultants, Inc,
-------
1-53
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No. : 13
EPA Method 7
Sampling Date:
7-18-75
Sampling Location: Scrubber Inlet & Outlet
Push
Time
1250
Oven
Number
12
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
3
3
Coke
Oven
Flue
Temp.
(°F)
2400
Cross
Draft
Velocity
(fpm)
520
520
Stack
Gas
Opacity
(Percent)
80
80
Net
Coal
Charged
(Ibs)
34,700
34,700
Averages
Inlet Dry Bulb (°F) 225
Inlet Stat. Pres. ("HzO) .5.0
Throat Pres. Drop ("H20) 33
Water Pres. (psi)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F) 76
Outlet Stat. Pres. ("H20) _65
Water Flow (GPM) 880
Fan Motor Current (AMP) 215
Gross Coking Time (min.) 973
Clayton Environmental Consultants, Inc,
-------
1-54
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No. : l
Grab Sample
Sampling Date:
6-4-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1049
Oven
Number
2
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
2
2
Coke
Oven
Flue
Temp.
(°F)
2470
Cross
Draft
Velocity
(fpm)
430
430
Stack
Gas
Opacity
(Percent)
25
25
Net
Coal
Charged
(Ibs)
36,550
36,550
Averages
Inlet Dry Bulb (°F) 230
Inlet Stat. Pres. ("H20) -4.6
Throat Pres. Drop ("H20) 42
Water Pres. (psi)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F) 77
Outlet Stat. Pres. ("H20) -53.0
Water Flow (GPM) 750
Fan Motor Current (AMP) 170
Gross Coking Time (min.) 1024
Clayton Environmental Consultants, Inc.
-------
1-55
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No.: 2
Grab Sample
Sampling Date: 6-4-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1104
Oven
Number
12
TEST
AVERAGE
Greenness
(Engineering
Observer ' s
Estimate)
3
3
Coke
Oven
Flue
Temp.
(°F)
2420
Cross
Draft
Velocity
(fpm)
510
510
Stack
Gas
Opacity
(Percent)
25
25
Net
Coal
Charged
(ibs)
36.650
36,650
Averages
Inlet Dry Bulb (°F) 230
Inlet Stat. Pres. ("H20) .4.6
Throat Pres. Drop ("H20)
Water Pres. (psi)
Outlet Dry Bulb (°F) 82
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20) .53.0
Water Flow (GPM) 750
Fan Motor Current (AMP) 170
Gross Coking Time (min.) 1023
Clayton Environmental Consultants, Inc,
-------
1-56
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No. : 4
Grab Sample
Sampling Date:
6-4-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1300
Oven
Number
4
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
1
1
Coke
Oven
Flue
Temp.
<°F)
2470
Cross
Draft
Velocity
(fpm)
400
400
Stack
Gas
Opacity
(Percent)
10
10
Net
Coal
Charged
(Ibs)
35,800
35,800
Averages
Inlet Dry Bulb (°F) 230
Inlet Stat. Pres. ("H20) -4.6
Throat Pres. Drop ("H20) 42
Water Pres. (psi) 39
Outlet Dry Bulb (°F) 82
Outlet Wet Bulb (°F) 77
Outlet Stat. Pres. ("H20) -53..0
Water Flow (GPM) 750
Fan Motor Current (AMP) 170
Gross Coking Time (min.) 1043
Clayton Environmental Consultants, Inc.
-------
1-57
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No. : 5
Grab Sample
Sampling Date:
6-4-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1310
Oven
Number
14
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
1
1
Coke
Oven
Flue
Temp.
(°F)
2470
Cross
Draft
Velocity
(fpm)
250
250
Stack
Gas
Opacity
(Percent)
0
0
Net
Coal
Charged
(Ibs)
36,050
36,050
Averages
Inlet Dry Bulb (°F) 230
Inlet Stat. Pres. ("H20) .4.6
Throat Pres. Drop ("H20) 42
Water Pres. (psl) 39
Outlet Dry Bulb (°F) 82
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM) 750
Fan Motor Current (AMP) 170
Gross Coking Time (min.) 993
Clayton Environmental Consultants, Inc,
-------
1-58
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No. : 7
Grab Sample
Sampling Date:
6-4-75
Sampling Location: Scrubber Inlet & Outlet
Push
Time
1519
Oven
Number
X56
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
3
3
Coke
Oven
Flue
Temp.
(°F)
2420
Cross
Draft
Velocity
(fpm)
355
355
Stack
Gas
Opacity
(Percent)
20
20
Net
Coal
Charged
(Ibs)
31r750
31,750
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop (
Water Pres. (psi)
Outlet Dry Bulb (°F)
230
-4.6
Outlet Wet Bulb (°F) 77
Outlet Stat. Pres. ("H20) -53.0
Water Flow (GPM) 750
Fan Motor Current (AMP) 170
Gross Coking Time (min.) 981
Clayton Environmental Consultants, Inc,
-------
1-59
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No.: 8
Grab Sample
Sampling Date:
6-4-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1531
Oven
Number
8
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
-
Coke
Oven
Flue
Temp.
(°F)
Cross
Draft
Velocity
(fpm)
-
Stack
Gas
Opacity
(Percent)
-
Net
Coal
Charged
(Ibs)
35.100
35,100
Averages
Inlet Dry Bulb (°F) 230
Inlet Stat. Pres. ("H20) -4.6
Throat Pres. Drop ("H20) 42
Water Pres. (psi) 39
Outlet Dry Bulb (°F) 82
77
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20) -53.0
Water Flow (GPM) 750
Fan Motor Current (AMP) 170
Gross Coking Time (min.)
981
Clayton Environmental Consultants, Inc.
-------
1-60
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No. : 10
Grab Sample
Sampling Date: 6-12-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1636
Oven
Number
X54
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
1
1
Coke
Oven
Flue
Temp.
<°F>
2400
Cross
Draft
Velocity
(fpm)
650
650
Stack
Gas
Opacity
(Percent)
0
0
Net
Coal
Charged
(Ibs)
(35,050)
35,050
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. (
Throat Pres. Drop ("H20)
Water Pres. (psi)
Outlet Dry Bulb (°F)
-5.1
40
Outlet Wet Bulb (°F) 78
Outlet Stat. Pres. ("H20) -44.9
Water Flow (GPM) 770
Fan Motor Current (AMP) 215
Gross Coking Time (min.) -
Clayton Environmental Consultants, Inc,
-------
1-61
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: Grab Sample
Test No.: 11 Sampling Date:
6-12-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1651
Oven
Number
X64
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
1
1
Coke
Oven
Flue
Temp.
(°F)
2390
Cross
Draft
Velocity
(fpm)
620
620
Stack
Gas
Opacity
(Percent)
0
0
Net
Coal
Charged
(Ibs)
(35,050)
35,050
Averages
Inlet Dry Bulb (°F) .
Inlet Stat. Pres. ("H20) .5.1
Throat Pres. Drop ("H20) 40
Water Pres. (psi) 40
Outlet Dry Bulb (°F) 73
Outlet Wet Bulb (°F) 73
Outlet Stat. Pres. ("H20) .44.9
Water Flow (GPM) 770
Fan Motor Current (AMP) 215
Gross Coking Time (min.)
Clayton Environmental Consultants, Inc,
-------
1-62
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No. : 12
Grab Sample
Sampling Date: 7-16-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
0952
Oven
Number
37
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
1
1
Coke
Oven
Flue
Temp.
(°F)
2380
Cross
Draft
Velocity
(fpm)
120
120
Stack
Gas
Opacity
(Percent)
0
0
Net
Coal
Charged
(Ibs)
35,650
35,650
Averages
Inlet Dry Bulb (°F) 267
Inlet Stat. Pres. ("H20) -5.1
Throat Pres. Drop ("H20) 40
Water Pres. (psl)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F) 82
Outlet Stat. Pres. ("H20) .54.4
Water Flow (GPM) 890
Fan Motor Current (AMP) 215
Gross Coking Time (mln.) 1QQ2
Clayton Environmental Consultants, Inc,
-------
1-63
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No. : 13
Grab Sample
Sampling Date:
7-16-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1006
Oven
Number
47
TEST
AVERAGE
Greenness
(Engineering
Observer1 s
Estimate)
2
2
Coke
Oven
Flue
Temp.
(°F)
2490
Cross
Draft
Velocity
(fpm)
170
170
Stack
Gas
Opacity
(Percent)
10
10
Net
Coal
Charged
(Ibs)
33,800
33,800
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psi)
Outlet Dry Bulb (°F)
267
-5.1
Outlet Wet Bulb (°F) 82
Outlet Stat. Pres. ("H20) -54.4
Water Flow (GPM) 890
Fan Motor Current (AMP) 215
Gross Coking Time (min.) 994
Clayton Environmental Consultants, Inc,
-------
1-64
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No. : 14
Grab Sample
Sampling Date:
7-16-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1035
Oven
Number
X57
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
1
1
Coke
Oven
Flue
Temp.
(°F)
2430
Cross
Draft
Velocity
(fpm)
420
420
Stack
Gas
Opacity
(Percent)
5
5
Net
Coal
Charged
(Ibs)
(34,300)
34,300
Averages
Inlet Dry Bulb (°F) 267
Inlet Stat. Pres. ("H20) .5.1
Throat Pres. Drop ("H20) 40
Water Pres. (psl) 55
Outlet Dry Bulb (°F) 84
Outlet Wet Bulb (°F) 82
Outlet Stat. Pres. ("H20) -54.4
Water Flow (GPM) 890
Fan Motor Current (AMP) 215
Gross Coking Time (min.) 1015
Clayton Environmental Consultants, Inc,
-------
1-65
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No. : 15
Grab Sample
Sampling Date: 7-16-75
Sampling Location: Scrubber Inlet & Outlet
Push
Time
1123
Oven
Number
29
TEST
AVERAGE
Greenness
(Engineering
Observer1 s
Estimate)
1
1
Coke
Oven
Flue
Temp.
(°F)
2460
Cross
Draft
Velocity
(fpm)
320
320
Stack
Gas
Opacity
(Percent)
0
0
Net
Coal
Charged
(Ibs)
33,500
33,500
Averages
Inlet Dry Bulb (°F) 267
Inlet Stat. Pres. ("H20) -5.1
Throat Pres. Drop ("H20) 40
Water Pres. (psi) 55
Outlet Dry Bulb (°F) 84
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.)
215
983
Clayton Environmental Consultants, Inc,
-------
1-66
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No. : 16
Grab Sample
Sampling Date: 7-16-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1137
Oven
Number
39
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
1
1
Coke
Oven
Flue
Temp.
(»F)
2360
Cross
Draft
Velocity
(fpm)
370
370
Stack
Gas
Opacity
(Percent)
0
0
Net
Coal
Charged
(Ibs)
34,200
34,200
Averages
Inlet Dry Bulb (°F) 267
Inlet Stat. Pres. ("H20) -5.1
Throat Pres. Drop ("H20) 40
Water Pres. (psi) 55
Outlet Dry Bulb (°F) 84
Outlet Wet Bulb (°F) 82
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.) 989
Clayton Environmental Consultants, Inc,
-------
1-67
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No. : 17
Grab Sample
Sampling Date: 7-16-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1203
Oven
Number
X59
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
1
1
Coke
Oven
Flue
Temp.
(°F>
2380
Cross
Draft
Velocity
(fpm)
490
490
Stack
Gas
Opacity
(Percent)
0
0
Net
Coal
Charged
(Ibs)
35,550
35,550
Averages
Inlet Dry Bulb (°F) 267
Inlet Stat. Pres. ("H20) -5.1
Throat Pres. Drop ("H20) 40
Water Pres. (psi) 55
Outlet Dry Bulb (°F) 84
82
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20) ^54.4
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.)
890
215
987
Clayton Environmental Consultants, Inc.
-------
1-68
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No.: 18
Grab Sample
Sampling Date:
7-16-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1217
Oven
Number
2
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
1
1
Coke
Oven
Flue
Temp.
<°F)
2400
Cross
Draft
Velocity
(fpm)
360
360
Stack
Gas
Opacity
(Percent)
5
5
Net
Coal
Charged
(Ibs)
35,400
35,400
Averages
Inlet Dry Bulb (°F) 267
Inlet Stat. Pres. ("H20) -5.1
Throat Pres. Drop ("H20) 40
Water Pres. (psi) 55
Outlet Dry Bulb (°F) 84
Outlet Wet Bulb (8F) 82
Outlet Stat. Pres. ("H20) -54.4
Water Flow (GPM) 890
Fan Motor Current (AMP)
Gross Coking Time (min.)
Clayton Environmental Consultants, Inc.
-------
1-69
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: Activated Charcoal
Test No. : 1
Sampling Date: 6-5-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1226
Oven
Number
43
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
3
3
Coke
Oven
Flue
Temp.
(°F)
Cross
Draft
Velocity
(fpm)
525
525
Stack
Gas
Opacity
(Percent)
40
40
Net
Coal
Charged
(Ibs)
35,600
35,600
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psi)
Outlet Dry Bulb (°F)
212
-4.2
Outlet Wet Bulb (
Outlet Stat. Pres,
Water Flow (GPM)
Fan Motor Current
Gross Coking Time
F) 80
("H20) -51.0
(AMP)
(min. )
760
170
967
Clayton Environmental Consultants, Inc.
-------
1-70
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No. : 2
Activated Charcoal
Sampling Date:
6-5-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1240
Oven
Number
X53
TEST
AVERAGE
Greenness
(Engineering
Observer1 a
Estimate)
3
3
Coke
Oven
Flue
Temp.
(°F)
Cross
Draft
Velocity
(fpm)
465
465
Stack
Gas
Opacity
(Percent)
30
30
Net
Coal
Charged
dbs)
35,350
35,350
Averages
Inlet Dry Bulb (°F) 212
Inlet Stat. Pres. ("H20) .4.2
Throat Pres. Drop ("H20) 45
Water Pres. (psl) 39
Outlet Dry Bulb (°F) 82
Outlet Wet Bulb (°F) 80
Outlet Stat. Pres. ("H20) -51.0
Water Flow (GPM) 760
Fan Motor Current (AMP) 170
Gross Coking Time (min.) 968
Clayton Environmental Consultants, Inc,
-------
1-71
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: Activated Charcoal
Test No.: 3 Sampling Date: 6-5-75
Sampling Location: Scrubber Inlet & Outlet
Push
Time
1250
Oven
Number
X63
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
3
3
Coke
Oven
Flue
Temp.
<°F)
Cross
Draft
Velocity
(fpm)
480
480
Stack
Gas
Opacity
(Percent)
40
40
Net
Coal
Charged
(Ibs)
35,450
35,450
Averages
Inlet Dry Bulb (°F) 212
Inlet Stat. Pres. ("H20) .4. 2
Throat Pres. Drop ("H20) 45
Water Pres. (psl) 39
Outlet Dry Bulb (°F) 82
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.)
80
Clayton Environmental Consultants, Inc.
-------
1-72
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battezy
Dearborn, Michigan
Sampling Method:
Test No. : 4
Activated Charcoal
Sampling Date: 6-5-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1452
Oven
Number
7
TEST
AVERAGE
Greenness
(Engineering
Observer1 a
Estimate)
1
1
Coke
Oven
Flue
Temp.
(°F)
2430
Cross
Draft
Velocity
(fpm)
690
690
Stack
Gas
Opacity
(Percent)
10
10
Net
Coal
Charged
(Ibs)
35,350
35,350
Averages
Inlet Dry Bulb (°F) 212
Inlet Stat. Pres. ("HzO) -4.2
Throat Pres. Drop ("H20) 45
Water Pres. (psi) 39
Outlet Dry Bulb (°F) 82
Outlet Wet Bulb (°F) 80
Outlet Stat. Pres. ("H20) .51.0
Water Flow (GPM) 750
Fan Motor Current (AMP) 170
Gross Coking Time (min.) 979
Clayton Environmental Consultants, Inc,
-------
1-73
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No. : 5
Activated Charcoal
Sampling Date:
6-5-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1522
Oven
Number
27
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
2
2
Coke
Oven
Flue
Temp.
(°F)
Cross
Draft
Velocity
(fpm)
980
980
Stack
Gas
Opacity
(Percent)
25
25
Net
Coal
Charged
(Ibs)
34,700
34,700
Averages
Inlet Dry Bulb (°F) 212
Inlet Stat. Pres. ("H20) -4.2
Throat Pres. Drop ("H20) 45
Water Pres. (psi) 39
Outlet Dry Bulb (°F) 82
80
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20) -51.0
Water Flow (GPM) 760
Fan Motor Current (AMP)
Gross Coking Time (min.)
170
979
Clayton Environmental Consultants, Inc.
-------
1-74
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No. : 6
Sampling Location:
Activated Charcoal
Sampling Date: 6-5-75
Scrubber Inlet & Outlet
Push
Time
1615
Oven
Number
37
TEST
AVERAGE
Greenness
(Engineering
Observer1 s
Estimate)
-
Coke
Oven
Flue
Temp.
(°F)
Cross
Draft
Velocity
(fpm)
_
-
Stack
Gas
Opacity
(Percent)
—
-
Net
Coal
Charged
(Ibs)
(35,250)
35,250
Averages
Inlet Dry Bulb (°F) 212
Inlet Stat. Pres. ("HzO) -4.2
Throat Pres. Drop ("H20)
Water Pres. (psl)
Outlet Dry Bulb (°F) 82
Outlet Wet Bulb (°F)
Outlet Stat. Pres. C"H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.)
80
-51.0
760
Clayton Environmental Consultants, Inc,
-------
1-75
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: Activated Charcoal
Test No.: 7 Sampling Date:
6-5-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1625
Oven
Number
47
TEST
AVERAGE
Greenness
(Engineering
Observer' s
Estimate)
2
2
Coke
Oven
Flue
Temp.
<°F>
Cross
Draft
Velocity
(fpm)
440
440
Stack
Gas
Opacity
(Percent)
20
20
Net
Coal
Charged
(Ibs)
(35,250)
35,250
Averages
Inlet Dry Bulb (°F) 212
Inlet Stat. Pres. ("H20) -4.2
Throat Pres. Drop ("H20) 45
Water Pres. (psl) 39
Outlet Dry Bulb (°F) 82
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM) 760
Fan Motor Current (AMP) 170
Gross Coking Time (mln.) -
Clayton Environmental Consultants, Inc,
-------
1-76
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No.: 8
Activated Charcoal
Sampling Date: 6-6-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1027
1049
Oven
Number
19
29
TEST
AVERAGE
Greenness
(Engineering
Observer ' s
Estimate)
1
3
2.0
Coke
Oven
Flue
Temp.
(°F)
Cross
Draft
Velocity
(fpm)
515
530
520
Stack
Gas
Opacity
(Percent)
5
40
20
Net
Coal
Charged
(Ibs)
35,500
36,050
35,800
Averages
Inlet Dry Bulb (°F) 240
Inlet Stat. Pres. ("H20) .5.3
Throat Pres. Drop ("H20) 43
Water Pres. (psl) 38
Outlet Dry Bulb (°F) 77
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.)
1033
Clayton Environmental Consultants, Inc,
-------
1-77
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: Activated Charcoal
Test No.: 9 Sampling Date:
6-6-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1127
1141
1150
Oven
Number
X59
2
12
TEST
AVERAGE
Greenness
(Engineering
Observer1 a
Estimate)
2
1
2
1.7
Coke
Oven
Flue
Temp.
(°F)
Cross
Draft
Velocity
(fpm)
660
450
830
650
Stack
Gas
Opacity
(Percent)
20
15
30
20
Net
Coal
Charged
(Ibs)
35,150
35,050
34,950
35,050
Averages
Inlet Dry Bulb (°F) 240
Inlet Stat. Pres. ("H20) -5.3
Throat Pres. Drop ("H20) 43
Water Pres. (psi) 38
Outlet Dry Bulb (°F) 77
Outlet Wet Bulb (°F) 73
Outlet Stat. Pres. ("H20) -50.8
Water Flow (GPM) 793
Fan Motor Current (AMP) 215
Gross Coking Time (min.) 1024
Clayton Environmental Consultants, Inc,
-------
1-78
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: Activated Charcoal
Test No.: 10
Sampling Date: 6-6-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1338
1355
1410
Oven
Number
14
34
44
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
1
1
3
1.7
Coke
Oven
Flue
Temp.
(°F)
Cross
Draft
Velocity
(fpm)
480
650
790
650
Stack
Gas
Opacity
(Percent)
10
5
45
20
Net
Coal
Charged
(Ibs)
30,800
34,600
34,700
33,350
Averages
Inlet Dry Bulb (°F) 240
Inlet Stat. Pres. ("H20) .5.3
Throat Pres. Drop ("H20) 43
Water Pres. (psi)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F) 73
Outlet Stat. Pres. ("H20) -5Q.8
Water Flow (GPM) 793
Fan Motor Current (AMP) 215
Gross Coking Time (min.) 999
Clayton Environmental Consultants, Inc,
-------
1-79
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No. : 11
Activated Charcoal
Sampling Date: 6-6-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1420
1430
1458
Oven
Number
X54
X64
6
TEST
AVERAGE
Greenness
(Engineering
Observer1 s
Estimate)
3
3
1
2.3
Coke
Oven
Flue
Temp.
(°F)
2420
2400
Cross
Draft
Velocity
(fpm)
810
685
930
810
Stack
Gas
Opacity
(Percent)
50
60
0
35
Net
Coal
Charged
(Ibs)
35.250
35.350
35,500
35,350
Averages
Inlet Dry Bulb (°F) 240
Inlet Stat. Pres. ("H20) .5.3
Throat Pres. Drop ("H20) 43
Water Pres. (psi) 38
Outlet Dry Bulb (°F) 77
73
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20) _sn
Water Flow (GPM) 793
Fan Motor Current (AMP)
Gross Coking Time (min. )
215
995
Clayton Environmental Consultants, Inc.
-------
1-80
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No. : 12
Activated Charcoal
Sampling Date: 6-6-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1510
1522
1542
Oven
Number
16
26
36
TEST
AVERAGE
Greenness
(Engineering
Observer ' s
Estimate)
3
1
3
2.3
Coke
Oven
Flue
Temp.
<°F)
2420
Cross
Draft
Velocity
(fpm)
1105
660
645
800
Stack
Gas
Opacity
(Percent )
80
5
85
55
Net
Coal
Charged
(Ibs)
35.500
34,700
34,400
34,850
Averages
Inlet Dry Bulb (°F) 240
Inlet Stat. Pres. ("H20) -5.3
Throat Pres. Drop ("H20) 43
Water Pres. (psi) 38
Outlet Dry Bulb (°F) 77
Outlet Wet Bulb (°F) 73
Outlet Stat. Pres. ("H20) -50.8
Water Flow (GPM) 793
Fan Motor Current (AMP) 215
Gross Coking Time (mln.) 1012
Clayton Environmental Consultants, Inc.
-------
1-81
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: EPA Method 11
Test No.: 1
Sampling Location:
Sampling Date:
Scrubber Outlet
6-3-75
Push
Time
1040
1047
1104
Oven
Number
41
X51
X61
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
„
.
-
Coke
Oven
Flue
Temp.
(°F)
Cross
Draft
Velocity
(fpm)
_
.
-
Stack
Gas
Opacity
(Percent)
.
—
-
Net
Coal
Charged
(Ibs)
34,000
33,800
33,950
33,900
Averages
Inlet Dry Bulb (°F) 248
Inlet Stat. Pres. ("H20) -4.8
Throat Pres. Drop ("H20) 41
Water Pres. (psi) 39
Outlet Dry Bulb (°F) 74
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.)
70
Clayton Environmental Consultants, Inc,
-------
1-82
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: EPA Method 11
Test No.: 2
Sampling Location:
Sampling Date:
Scrubber Outlet
6-3-75
Push
Time
1114
1124
1204
Oven
Number
3
13
23
TEST
AVERAGE
Greenness
(Engineering
Observer1 a
Estimate)
-
Coke
Oven
Flue
Temp.
(°F)
Cross
Draft
Velocity
(fpm)
_
Stack
Gas
Opacity
(Percent)
_
Net
Coal
Charged
(Ibs)
34.850
(34.650)
(34.650)
34,700
Averages
Inlet Dry Bulb (°F) 248
Inlet Stat. Pres. ("H20) -4.8
Throat Pres. Drop ("H20) 41
Water Pres. (psi) 39
Outlet Dry Bulb (°F) 74
Outlet Wet Bulb (°F) 70
Outlet Stat. Pres. ("H20) -50.4
Water Flow (GPM) 750
Fan Motor Current (AMP) 17Q
Gross Coking Time (min.) 989
Clayton Environmental Consultants, Inc,
-------
1-83
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: Ethanol
Test No. : 1
Sampling Location:
Sampling Date:
Scrubber Outlet
7-17-75
Push
Time
0824
0840
0850
Oven
Number
16
26
36
TEST
AVERAGE
Greenness
(Engineering
Observer ' s
Estimate)
1
2
1
1.3
Coke
Oven
Flue
Temp.
<°F)
Cross
Draft
Velocity
(fpm)
210
440
400
350
Stack
Gas
Opacity
(Percent)
5
35
5
15
Net
Coal
Charged
(Ibs)
(34,600)
(34,600)
35,250
34,800
Averages
Inlet Dry Bulb (°F) 225
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psi)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F) 75
Outlet Stat. Pres. ("H20) -55
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.) 969
Clayton Environmental Consultants, Inc.
-------
1-84
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No.: 2
Ethanol
Sampling Location:
Sampling Date:
Scrubber Outlet
7-17-75
Push
Time
1441
1454
1514
Oven
Number
X53
X63
5
TEST
AVERAGE
Greenness
(Engineering
Observer 's
Estimate)
_
1
1
1
Coke
Oven
Flue
Temp.
(°F)
2360
2340
Cross
Draft
Velocity
(fpm)
_
260
700
480
Stack
Gas
Opacity
(Percent)
10
5
10
Net
Coal
Charged
(Ibs)
34,400
33,250
35,700
34,450
Averages
Inlet Dry Bulb (°F) 225
Inlet Stat. Pres. ("H20) .4.8
Throat Pres. Drop ("H20) 33
Water Pres. (psi) 57
Outlet Dry Bulb (°F) 78
Outlet Wet Bulb (°F) 76
Outlet Stat. Pres. ("H20) -55
Water Flow (GPM) 880
Fan Motor Current (AMP) 215
Gross Coking Time (mln.) 978
Clayton Environmental Consultants, Inc,
-------
1-85
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: Cyclohexane
Test No. : 1
Sampling Date: 6-11-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1347
1408
1423
Oven
Number
41
X51
X61
TEST
AVERAGE
Greenness
(Engineering
Observer ' s
Estimate )
3
1
3
2.3
Coke
Oven
Flue
Temp.
(°F)
2360
2420
. 2380
Cross
Draft
Velocity
(fpm)
340
650
450
480
Stack
Gas
Opacity
(Percent )
40
20
40
35
Net
Coal
Charged
(Ibs)
36,650
36,500
36,550
36,550
Averages
Inlet Dry Bulb (°F) 247
Inlet Stat. Pres. ("HzO) -4.9
Throat Pres. Drop ("H20) 39
Water Pres. (psi) 40
Outlet Dry Bulb (°F) 81
Outlet Wet Bulb (°F) 81
Outlet Stat. Pres. ("H20) -45
Water Flow (GPM) -
Fan Motor Current (AMP) -
Gross Coking Time (min.) 999
Clayton Environmental Consultants, Inc,
-------
1-86
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: Cyclohexane
Test No. : 2
Sampling Date: 6-12-75
Sampling Location:
Scrubber Inlet & Outlet
Push
Time
1037
1101
1114
Oven
Number
17
37
47
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
3
3
3
3
Coke
Oven
Flue
Temp.
(»F)
2300
2360
2380
Cross
Draft
Velocity
(fpm)
520
580
810
640
Stack
Gas
Opacity
(Percent)
20
40
20
25
Net
Coal
Charged
(Ibs)
33,800
37,200
36,900
35,950
Averages
Inlet Dry Bulb (°F) -
Inlet Stat. Pres. ("H20) -5.1
Throat Pres. Drop ("H20) 40
Water Pres. (psl) 40
Outlet Dry Bulb (°F) 78
78
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20) -44.9
Water Flow (GPM) 770
Fan Motor Current (AMP) 215
Gross Coking Time (mln.) 1QQ6
Clayton Environmental Consultants, Inc.
-------
1-87
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No.: 3
Sampling Location:
Cyclohexane
Sampling Date: 6-12-75
Scrubber Inlet & Outlet
Push
Time
1510
1521
1623
Oven
Number
14
24
44
TEST
AVERAGE
Greenness
(Engineering
Observer ' s
Estimate)
1
1
3
1.7
Coke
Oven
Flue
Temp.
<°F)
2400
2360
2300
Cross
Draft
Velocity
(fpm)
650
620
620
630
Stack
Gas
Opacity
(Percent)
20
20
60
35
Net
Coal
Charged
(Ibs)
35,200
35,050
(35,050)
35,100
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psi)
Outlet Dry Bulb (°F)
- Outlet Wet Bulb (°F) 78
-5.1 Outlet Stat. Pres. ("H20) -44.9
40 Water Flow (GPM) 770
Fan Motor Current (AMP) 215
Gross Coking Time (rain.) 983
Clayton Environmental Consultants, Inc.
-------
1-88
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: Andersen Impactor
Test No.: 1-A,1-B,1-C Sampling Date: 9-4-75 and 9-5-75
Sampling Location: Scrubber Inlet
Push
Time
1-A
0900
0940
0951
1-B
1425
1502
1513
1-C
0904
0916
0930
Oven
Number
3
13
23
29
49
X59
32
42
X52
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
3
2
1
3
3
1
2
2
1
2.0
Coke
Oven
Flue
Temp.
(°F)
Cross
Draft
Velocity
(fpm)
210
Calm
430
410
180
220
220
120
150
220
Stack
Gas
Opacity
(Percent)
60
40
20
65
60
—
5
5
0
30
Net
Coal
Charged
(Ibs)
_
—
—
_
_
_
-
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psl)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.)
Clayton Environmental Consultants, Inc,
-------
1-89
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No.: 1
Sampling Location:
Andersen Impactor
Sampling Date:
Scrubber Outlet
9-4-75 and 9-5-75
Push
Time
0900
0940
0951
1425
1502
1513
9-5
0904
0916
0930
Oven
Number
3
13
23
29
49
X59
32
42
X52
TEST
AVERAGE
Greenness
(Engineering
Observer ' s
Estimate)
3
2
1
3
3
1
2
2
1
2.0
Coke
Oven
Flue
Temp.
(°F)
Cross
Draft
Velocity
(fpm)
210
Calm
430
410
180
220
220
120
150
220
Stack
Gas
Opacity
(Percent)
60
40
20
65
60
_
5
5
0
30
Net
Coal
Charged
(Ibs)
„
.
_
.
„
_
_
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psi)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.)
Clayton Environmental Consultants, Inc.
-------
1-90
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: Andersen Impactor
Test No.: 2-A,2-B,2-C Sampling Date: 9-5-75 and 9-8-75
Sampling Location: Scrubber Inlet
Push
Time
2-A
1251
1319
1331
2-B
1036
1102
1151
2-C
1337
1403
1431
Oven
Number
46
8
18
3
13
X53
25
45
7
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
3
2
3
2
2
1
3
3
2
2.3
Coke
Oven
Flue
Temp.
(°F)
Cross
Draft
Velocity
(fpm)
500
1000
1100
975
730
640
890
890
1005
860
Stack
Gas
Opacity
(Percent)
50
15
30
60
40
5
60
50
15
35
Net
Coal
Charged
(Ibs)
—
—
—
—
—
_
«.
-
-
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psi)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.)
Clayton Environmental Consultants, Inc,
-------
1-91
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: Andersen Impactor
2
Test No. :
Sampling Location:
Sampling Date:
Scrubber Outlet
9-5-75 and 9-6-75
Push
Time
1251
1319
1331
9-6
1036
1102
1151
1337
1403
1431
Oven
Number
46
8
18
3
13
X53
25
45
7
TEST
AVERAGE
Greenness
(Engineering
Observer ' s
Estimate)
3
2
3
2
2
1
3
3
2
2.3
Coke
Oven
Flue
Temp.
(°F)
Cross
Draft
Velocity
(fpm)
500
1000
1100
975
730
640
890
890
1005
860
Stack
Gas
Opacity
(Percent)
50
15
30
60
40
5
60
50
15
35
Net
Coal
Charged
(Ibs)
—
_
-
-
-
-
-
_
_
-
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psi)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.)
Clayton Environmental Consultants, Inc.
-------
1-92
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: Andersen Impactor
Test No.: 3-A,3-B,3-C Sampling Date: 9-9-75 and 9-10-75
Sampling Location: Scrubber Inlet
Push
Time
3-A
0959
0822
0835
3-B
1005
1017
1034
3-C
1155
1212
1225
Oven
Number
49
28
38
1
11
21
23
33
43
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
2
1
2
2
1
2
3
1
1
1.7
Coke
Oven
Flue
Temp.
(°F)
Cross
Draft
Velocity
(fpm)
360
130
80
110
80
170
130
160
270
170
Stack
Gas
Opacity
(Percent)
20
0
—
50
10
50
75
5
5
25
Net
Coal
Charged
(Ibs)
—
—
—
_
_
_
-
_
-
-
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psi)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.)
Clayton Environmental Consultants, Inc.
-------
1-93
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No. : 3
Andersen Impactor
Sampling Location:
Sampling Date:
Scrubber Outlet
9-9-75 and 9-10-75
Push
Time
0959
9-10
0822
0835
1005
1017
1034
1155
1212
1225
Oven
Number
49
28
38
1
11
21
23
33
43
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
2
1
2
2
1
2
3
1
1
1.7
Coke
Oven
Flue
Temp.
(°F)
Cross
Draft
Velocity
(fpm)
360
130
80
110
80
170
130
160
270
170
Stack
Gas
Opacity
(Percent)
20
0
_
50
10
50
75
5
5
25
Net
Coal
Charged
(Ibs)
_
-
_
.
_
-
-
_
_
-
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psi)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.)
Clayton Environmental Consultants, Inc,
-------
1-94
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: Andersen Impactor
Teat No.: 4-A,4-B,4-C Sampling Date: 9-10-75 and 9-11-75
Sampling Location: Scrubber Inlet
Push
Time
4-A
1406
1414
1427
4-B
0841
0851
0909
4-C
1041
1052
1117
Oven
Number
25
35
45
37
47
X57
2
12
22
TEST
AVERAGE
Greenness
(Engineering
Observer ' a
Estimate)
3
1
3
3
1
3
2
2
3
2.3
Coke
Oven
Flue
Temp.
(°F)
Cross
Draft
Velocity
(fpm)
170
380
420
200
120
50
130
125
200
200
Stack
Gas
Opacity
(Percent)
70
5
65
70
5
50
65
50
70
50
Net
Coal
Charged
(Ibs)
_
_
_
-
_
-
-
-
-
-
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop (
Water Pres. (psi)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.)
Clayton Environmental Consultants, Inc.
-------
1-95
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: Andersen Impactor
Teat No.: 4 Sampling Date:
9-10-75 and 9-11-75
Sampling Location:
Scrubber Outlet
Push
Time
1406
1414
1427
9-11
0841
0851
0909
1041
1052
1117
Oven
Number
25
35
45
37
47
X57
2
12
22
TEST
AVERAGE
Greenness
(Engineering
Observer ' s
Estimate)
3
1
3
3
1
3
2
2
3
2.3
Coke
Oven
Flue
Temp.
(°F)
Cross
Draft
Velocity
(fpm)
170
380
420
200
120
50
130
125
200
200
Stack
Gas
Opacity
(Percent)
70
5
65
70
5
50
65
50
70
50
Net
Coal
Charged
(Ibs)
—
—
—
—
—
_
-
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psi)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.)
Clayton Environmental Consultants, Inc.
-------
1-96
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No.: 5
Andersen Impactor
Sampling Location:
Sampling Date:
Scrubber Inlet
9-11-75
Push
Time
1406
1418
1425
Oven
Number
34
44
X54
TEST
AVERAGE
Greenness
(Engineering
Observer ' s
Estimate)
2
1
2
1.7
Coke
Oven
Flue
Temp.
(°F)
Cross
Draft
Velocity
(fpm)
130
150
120
130
Stack
Gas
Opacity
(Percent)
40
5
30
25
Net
Coal
Charged
(Ibs)
_
_
_
-
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (pal)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.)
Clayton Environmental Consultants, Inc.
-------
1-97
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method:
Test No.: 5
Andersen Impactor
Sampling Location:
Sampling Date: 9-11-75
Scrubber Outlet
Push
Time
1406
1418
1425
Oven
Number
34
44
X54
TEST
AVERAGE
Greenness
(Engineering
Observer ' s
Estimate )
2
1
2
1.7
Coke
Oven
Flue
Temp.
(°F)
Cross
Draft
Velocity
(fpm)
130
150
120
130
Stack
Gas
Opacity
(Percent)
40
5
30
25
Net
Coal
Charged
(Ibs)
_
—
_
-
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psi)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.)
Clayton Environmental Consultants, Inc.
-------
1-98
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: Andersen Impactor
Test No.: 6-A,6-B,6-C Sampling Date: 9-12-75 and 9-15-75
Sampling Location: Scrubber Inlet
Push
Time
6-A
0828
0956
1009
6-B
1225
1238
0825
6-C
0955
1002
1010
Oven
Number
8
48
X58
X51
X61
45
27
37
47
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
1
2
2
2
1
2
3
3
1
1.9
Coke
Oven
Flue
Temp.
<°F)
Cross
Draft
Velocity
(fpm)
490
420
490
890
1300
160
420
515
425
570
Stack
Gas
Opacity
(Percent)
5
30
10
20
5
5
50
30
5
20
Net
Coal
Charged
(Ibs)
—
_
_
_
_
..
-
-
-
-
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psl)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.)
Clayton Environmental Consultants, Inc.
-------
1-99
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: Andersen Impactor
Test No. : 6
Sampling Location:
Sampling Date:
Scrubber Outlet
9-12-75 and 9-15-75
Push
Time
0956
1009
1032
1225
1238
9-15
0825
0955
1002
1010
Oven
Number
48
X58
mm
X51
X61
45
27
37
47
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate )
2
2
_
2
1
2
3
3
1
2.0
Coke
Oven
Flue
Temp.
(°F)
Cross
Draft
Velocity
(fpm)
420
490
—
890
1300
160
420
515
425
580
Stack
Gas
Opacity
(Pircent)
30
10
fm
20
5
5
50
30
5
20
Net
Coal
Charged
(Ibs)
„
.
—
—
—
—
—
_
-
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psl)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (mtn.)
Clayton Environmental Consultants, Inc,
-------
1-100
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: Andersen Impactor
Test No.: 7-A.7-B.7-C
Sampling Location:
Sampling Date:
Scrubber Inlet
9-15-75 and 9-16-75
Push
Time
7-A
1223
1259
1322
7-B
1425
1450
1456
7-C
0834
0848
0855
Oven
Number
2
22
32
X62
4
14
X54
X64
6
TEST
AVERAGE
Greenness
(Engineering
Observer's
Estimate)
2
3
3
1
1
2
1
2
1
1.8
Coke
Oven
Flue
Temp.
<°F)
Cross
Draft
Velocity
(fpm)
830
795
0
240
390
350
315
195
195
370
Stack
Gas
Opacity
(Percent)
25
40
30
10
5
30
20
30
5
20
Net
Coal
Charged
(Ibs)
.
—
_
_
..
_
-
-
-
-
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. ("H20)
Throat Pres. Drop ("H20)
Water Pres. (psl)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GFM)
Fan Motor Current (AMP)
Gross Coking Time (min.)
Clayton Environmental Consultants, Inc.
-------
1-101
SUMMARY OF PROCESS AND CONTROL SYSTEM DATA
Ford Motor Company
Rouge Plant - Coke Battery
Dearborn, Michigan
Sampling Method: Andersen Impactor
Test No.: 7 Sampling Date: 9-15-75 and 9-16-75
Sampling Location:
Scrubber Outlet
Push
Time
1223
1259
1322
1425
1450
1456
9-16
0834
0848
0855
Oven
Number
2
22
32
X62
4
14
X54
X64
6
TEST
AVERAGE
Greenness
(Engineering
Observer ' s
Estimate)
2
3
3
1
1
2
1
2
1
1.8
Coke
Oven
Flue
Temp.
(°F>
Cross
Draft
Velocity
(fpm)
830
795
0
240
390
350
315
195
195
370
Stack
Gas
Opacity
(Percent)
25
40
30
10
5
30
20
30
5
20
Net
Coal
Charged
(Ibs)
_
_
Averages
Inlet Dry Bulb (°F)
Inlet Stat. Pres. (
Throat Pres. Drop ("H20)
Water Pres. (psl)
Outlet Dry Bulb (°F)
Outlet Wet Bulb (°F)
Outlet Stat. Pres. ("H20)
Water Flow (GPM)
Fan Motor Current (AMP)
Gross Coking Time (min.)
Clayton Environmental Consultants, Inc,
-------
TECHNICAL REPORT DA^A
(Please read Instructions on the reverse before completing)
\. REPORT NO.
EPA-600/2-77-187b
3. RECIPIENT'S ACCESSION NO.
4. TITLE AND SUBTITLE
Emission Testing and Evaluation of Ford/Koppers
Coke Pushing Control System; Volume II. Appendices
5. REPORT DATE
September 1977
6. PERFORMING ORGANIZATION CODE
7.AUTHORIS)Fred Cooper> Thomas Loch, John Mutchler,
and Jan Vecchio (Clayton Environmental Consultants,
8. PERFORMING ORGANIZATION REPORT NO.
9. PERFORMING ORGANIZATION NAME AND ADDRESS
Ford Motor Company
The American Road
Dearborn, Michigan 48121
10. PROGRAM ELEMENT NO.
1AB604
11. CONTRACT/GRANT NO.
68-02-0630
12. SPONSORING AGENCY NAME AND ADDRESS
EPA, Office of Research and Development
Industrial Environmental Research Laboratory
Research Triangle Park, NC 27711
13. TYPE OF REPORT AND PERIOD COVERED
Final: 12/73-8/77
14. SPONSORING AGENCY CODE
EPA/600/13
is. SUPPLEMENTARY NOTES J.ERL-RTP project officer for this report is Norman Plaks, Mail
Drop 62, 919/541-2733.
16. ABSTRACT
The report documents a field testing and engineering evaluation of the per-
formance of a retrofitted, mobile-hood, high-energy-scrubber control system, abating
coke-side pushing emissions from a 58-oven coke battery. It documents the venturi-
scrubber inlet and outlet emission rates, as well as emission factors for filterable and
condensible particulate, sulfur dioxide, sulfur trioxide, total sulfur oxides, carbon
monoxide, nitrogen oxides, benzene, benzene and homologues, total light hydrocarbons
methane and homologues, and ethylene and homologues. Results indicate that the
mobile hood collects particulate emissions resulting from green and clean pushes afo
22% to 54% efficiencies, respectively, or from 30% to 92%, respectively, using two
different estimating techniques. Scrubber performance averaged 99.3% for particulate
emissions captured in the hood.
17.
KEY WORDS AND DOCUMENT ANALYSIS
DESCRIPTORS
b.lDENTIFIERS/OPEN ENDED TERMS
c. COSATI Field/Group
Air Pollution
Scrubbers
Coke
Coking
Emission
Dust
Jron and Steel Industry
Air Pollution Control
Stationary Sources
Coke Pushing
Particulate
13B
07A
21D
13H
11G
11F
13. DISTRIBUTION STATEMEN1
Unlimited
19. SECURITY CLASS (ThisReport)
Unclassified
21. NO. OF PAGES
600
20. SECURITY CLASS (This page)
Unclassified
22. PRICE
EPA Form 2220-1 (9-73)
------- |