ENVIRONMENTAL PROTECTION AGENCY
OFFICE OF ENFORCEMENT
EPA-330/2-77-012
Emission Testing
at
Marathon Steel Company
Tempe, Arizona
(APRIL 12-16, 1977)
NATIONAL ENFORCEMENT INVESTIGATIONS CENTER
DENVER, COLORADO
AND .
$ £*
REGION IX
SAN FRANCISCO. CALIFORNIA
JUNE 1977
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Environmental Protection Agency
Office of Enforcement
EPA - 220/2-77-012
EMISSION TESTING
AT
MARATHON STEEL
TEMPE, ARIZONA
April 12-16, 1977
June 1976
National Enforcement Investigations Center - Denver, Colorado
and
Region IX - San Francisco, California
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CONTENTS
I INTRODUCTION 1
II SUMMARY AND CONCLUSIONS 2
III PROCESS DESCRIPTION 3
IV TEST PROCEDURES 6
V TEST RESULTS 12
FIGURES
1 Old Baghouse Station 1 (0401) 9
2 New Baghouse - Stations 2 and 3
(0402 - 0403) 11
TABLES
1 Process Weight Summary 5
2 Data Summary - Station 1 13
•
3 Data Summary - Station 2 14
4 Data Summary - Station 3 15
5 Visible Emission Summary (Opacity) 16
APPENDICES
A Presurvey Inspection of Marathon Steel Company
B Production Data and Process Weight Calculations
C Stack Sampling Equipment
D Calibration Data
E Source Tests
F Chain of Custody Record
G Particulate Field Data
ii
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I. INTRODUCTION
Marathon Steel Company, Tempe, Arizona manufactures steel reinforc-
ing rods from scrap steel melted in three electric-arc furnaces. After
melting, the scrap steel is refined and then cast into ingots. The
ingots are heated and rolled into reinforcing rods of various diameters
and lengths. Two baghouses (old and new) control the emissions from
the furnaces, casting and other sources [Appendix A].
On November 15, 1976, National Enforcement Investigations Center
(NEIC) performed a presurvey inspection requested by Environmental
Protection Agency (EPA), Region IX, to determine if the baghouse emis-
sions could be sampled. It was concluded that sampling was feasible
provided that minor modifications be made on the old baghouse stack
testing platform. No changes were needed at the new baghouse sampling
location.
During the period April 12 to 16, -1977 the baghouse emissions of
Marathon Steel were tested by NEIC to determine the compliance status of
the plant with the Arizona particulate regulation (R9-3-306). The
allowable baghouse particulate emission rates were calculated with the
equation in the Arizona regulation and the furnace process weight
rates. There are no limitations on particulate concentrations. Visible
emission observations were also made and compared to the Arizona opacity
regulation (R9-3-301), which limits the emission opacities to 20%,
except for excursions to 40% for five minutes.
* Designation used by Marathon Steel.
** The plant is located in the Phoenix-Tucson Air Quality Control Region.
= O.62
.
*** E = 3.59 pO.62^ uhere E ±s the allowable particulate emissions (Ib/hr)
and P is the furnace process weight (tons/hr).
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II. SUMMARY AND CONCLUSIONS
1. The participate sampling results are summarized below.
Particulate Emissions
Baghouse
Old
New
Process
Weight
m. tons/hr
7.2
17.0
Al 1 owed
kg/hr
5.9
10.0
Ib/hr
12.9
22.1
Actual
kg/hr
6.0
2.9
Ib/hr
13.3
6.4
%
of allowable
emissions
102%
29%
The plant met the requirements of the Arizona process weight regu-
lation. On an individual basis, the old baghouse emissions (furnace
No. 1) exceeded the allowed emissions by 2%. The new baghouse emissions
(furnaces 2 and 3), however, were only 29% of the allowable.
2. The baghouse visible emissions are in compliance with the
Arizona opacity regulation of 40%. Visible emissions from the old and
new baghouses averaged 7 and 5%, respectively.
3. The average particulate concentration from the old baghouse is
more than eight times that of the new baghouse. The possible causes of
the high particulate concentration include bleaking bags, the bag
cleaning cycle, suitability of bag material, etc.
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III. PROCESS DESCRIPTION
Marathon Steel manufactures steel reinforcing rod from reprocessed
scrap steel. The Company operates three electric arc melting furnaces
(capacities-22.7, 22.7 and 27.2 m. tons) which are the major emission
sources. Other emission sources include ladle cleaning (skulling),
casting, and fugitive. The furnaces and skulling emissions are col-
lected by hoods and ducted to two baghouses. The fugitive emissions
from the hoods and casting area collect under the building roof and are
also vented to the baghouses.
The furnace No. 1 emissions are controlled by the old baghouse
(Station 1). The baghouse uses Nomex bags to clean 1,700 m /min
(60,000 acfm) of gas (air to cloth ratio of 2.3:1).
Furnaces No. 2 and 3 and the skulling emissions are ducted together
and then split to the two sides (north, Station 3 and south, Station 2)
of the new baghouse. Both sides have Dacron bags and each clean 2,820
act. m3/min (100,000 acfm) of gas (air to cloth ratio of 2.7:1).
The ducting to the baghouses is interconnected so that the gas
streams can be rerouted to one baghouse if necessary. The fugitive
emissions can be vented to either baghouse.
Plant log sheets lists the exact amounts of material charged to a
furnace during a heat (melt) along with any changes in operating pro-
cedure, e.g., changes of furnace electrodes, downtime, oxygen blow
* Trade name.
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duration. These log sheets were used to calculate the process weight
of each furnace during the sampling period [Appendix B]. The process
weight for furnaces Nos. 2 and 3 were combined when calculating the new
baghouse allowable particulate emission rate. The furnace process
weights and the allowable emissions are summarized in Table 1.
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Table 1
PROCESS WEIGHT SUMMARY
Marathon Steel
Tempe, Arizona
April 12-16, 1977
Date
(April)
12
13
14
15
16
Average
Furnace
No.
1
2 and 3
1
2 and 3
1
2 and 3
2 and 3
1
2 and 3
1
2 and 3
Process
m.tons/
hr
8.0
16.2
6.4
14.2
7.4
18.1
0
19.7
6.9
16.5
7.2
17.0
Weight
tons/
hr
8.8
17.9
7.1
15.6
8.2
20.0
0
21.7
7.6
18.2
7.9
18.7
Allowable
Emissions
kg/
hr
6.3
9.8
5.5
9.0
6.0
10.5
0
11.0
5.7
9.9
5.9
10.0
hr
13.8
21.5
12.1
19.7
13.2
23.0
0
24.2
12.6
21.7
12.9
22.1
t Furnace No. 1 down for reline.
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IV. TEST PROCEDURES
Testing was conducted at Marathon Steel from April 12 to 16, 1977
at the following locations: Station 1, old baghouse; Station 2, new
baghouse (south side); Station 3, new baghouse (north side). A pre-
liminary velocity, temperature and moisture traverse was made on Station
3, April 12. Except for the number of points sampled in the old bag-
house stack (see section on sample locations), the tests were conducted
in accordance with the procedures specified in Method 5.
The sampling train used was the Model AP 5000 manufactured by
Scientific Glass, Inc. [Appendix C] which was configured as follows:
1. Stainless steel (316) nozzle
2. Glass-lined probe
3. Glass fiber filter (11.4 cm diameter)
4. First impinger -- modified Greenburg-Smith with 100 ml
distilled water
5. Second impinger -- Greenburg-Smith with 100 ml distilled water
6. Third impinger — modified Greenburg-Smith, empty
7. Fourth impinger -- modified Greenburg-Smith with approximately
200 g of silica gel
Moisture content of the gas stream was determined from the increase in
volume in the first three impingers and the weight gain of the silica
gel (Method 4*).
Stack gas molecular weight was based on the average analyses of
two to three gas samples collected during each run. Gas samples were
* 40 CFR 603 Standards of Performance for New Stationary Sources^
Appendix Test Methods, June 83 1976.
-------
obtained by the grab sample technique of Method 3 (40 CFR 60). Analy-
ses were performed with Fyrite type combustion gas analyzers.
A minimum of three sampling runs, within the isokinetic range of 90
to 110%, were performed on each stack. Prior to each run, the sampling
train was leak-checked at 38 cm (15 in) Hg. At the completion of the
run, a second leak check was conducted at the highest vacuum recorded
during the test. These checks are acceptable if the leakage rate did
not exceed 0.00057 m /min (0.02 cfm). All sampling runs were structured
to provide a minimum sampling time of 60 minutes* and a minimum sample
volume of 849 dry std. liters (30 dscf).* Probe and oven temperatures
were held within 14°C (25°F) of 120°C (248°F) during testing.
All pitobe assemblies, dry gas and orifice meters used in this test
had been calibrated prior to leaving Denver and were recalibrated upon
return [Appendix D]. The pitobe assemblies used during the compliance
test were those identified as 5-5 (old baghouse stack) and 8-1 (new
baghouse ducts).
An NEIC mobile laboratory, located at the plant, was used for all
sampling train preparation and sample recovery. Sample recovery pro-
ceeded as follows:
1. All filters were returned to their storage container (Petri-
dish) and sealed with aluminum foil.
2. The nozzles, probes, cyclones and front portion of the glass
filter holder were washed with acetone and the washings from
each train were collected in a glass jar with a Teflon -lined
cap.
* The Arizona SIP stack sampling requirements specify that 1) an
integrated gas sample be taken, 2) the sampling period be at least
2 hours, and 3) at least 60 dscf be sampled. These requirements,
which are more stringent than Method 5 requirements, were not
strictly followed. It was determined during the pre-survey inspec-
tion that the Method 5 procedures would obtain representative
results.
** Brand name.
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8
3. The volume of the contents of impingers 1-3 was measured as
part of the moisture determination. The contents were then
discarded.
4. Impinger 4, which contained silica gel, was weighed to determine
the moisture gain and the silica gel was discarded.
All samples were returned to the NEIC laboratories for particulate
analyses [Appendix E]. Chain of custody was maintained at all times
[Appendix F].
Sample Locations
The old baghouse stack (Station 1) is 1.5 m (5 ft) in diameter and
12 m (40 ft) tall [Figure 1]. The ports are located 3.0 stack diameters
(4.5 m or 15 ft) downstream of the inlet and 3.0 stack diameters upstream
of the stack exit. Based on Method 1 criteria a total of 42 sampling
points were required.
Two parallel bars (5 cm angle irons) cross the stack immediately (5
cm) upstream of the test ports and could cause flow disturbance. Based
on a preliminary velocity traverse, a flow disturbance was found only
within 2.5 cm (1 in) of these bars. The preliminary traverse also
determined that the gas velocity profile in the stack was flat, indi-
cating uniform flow. Thus, the number of sample points could be reduced
to avoid sampling within 2.5 cm of the bars without affecting the sample
representativeness. The number of sample points was therefore reduced
to 28 (from 42), which increased the distance from the bars to the
nearest sampling point to 7.6 cm (3 in). Each point was sampled for 3
minutes (84 minutes per test).
* Brand name.
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STACK
E
0
EC
to o
Fan
EXISTING BAGHOUSE
I I I 111
SIDE VIEW
GROUND
1.6m (5.Oft)
STACK
EXISTING BAGHOUSE
;PORTS
CATWALK
TOP VIEW
Figure I. Marathon Stool, Tempo, Arizona
Old Baghouse — Sfafion 040I
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10
The new baghouse emissions were sampled in the ducts between the
baghouse and the fans (Stations 3, north side, and 2, south side). Six
equally spaced 10 cm (4 in) sampling ports are located 2.1 equivalent
diameters (4.3 m or 14 ft) downstream of a flow disturbance and 0.5
equivalent diameters (1 m or 3.4 ft) upstream of a flow disturbance
i **
[Figure 2], therefore, Method 1 requires 48 sample points. Each point
was sampled for 2 minutes (total test time of 96 minutes).
* The new baghouse has two identical ducts (north and south), each
of which handles approximately half of the waste gases.
** The length to width ratio is 1.3.
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11
FROM
BAQHOUSE
FLOW
FRONT VIEW
1 8m (6 Oft)
,PORTS
2.3m (7 5ft)
FAN
FAN EXHAUST
TOP VIEW
SIDE VIEW
"B"
FAN EXHAUST
FAN EXHAUST
*^W//////S
STATION O4O3,
(NORTH)
i
1
PORTS
J 2.1m (7ft)
PLATFORM
PORTS
/
>
S
1
STATION O402 |
(SOUTH)
T—W/M
1
1
*
-.— 0
-I
IL
>
o
-*-_!
IL
BAGHOUSE
BAGHOUSE
i
Figure 2. Afarafhon Steel Tempo, Arizona
New Baghouse - Stations 0402, 0403
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V. TEST RESULTS
The old baghouse (Station 1) and the new baghouse, north side
(Station 3), were sampled three times, while the new baghouse, south
side (Station 2), was sampled five times. The second run of the new
baghouse, south side, was unacceptable because the filter was not in
proper position after the final leak check. Isokinetic sampling rates
for the eleven sample runs ranged from 94.6 to 108.9%, within the
specified range of 90 to 110%. The test data [Appendix G] is summarized
in Tables 2, 3 and 4.
/'
The old baghouse (Station 1), particulate emissions [Table 2],
averaged 6.0 kg (13.3 lb)/hr, 2% over the allowed 5.9 kg (12.9 lb)/hr.
Since 2% is within the accuracy of the test method, a violation did not
occur.
The new baghouse particulate emissions are in compliance with state
regulations. The emissions [Tables 3 and 4] averaged 2.9 kg (6.4 lb)/hr,
29% of the allowable emission (i.e. 10 kg/hr. Combining the emission of
the two sides (north and south) was necessary because there are no
dampers to evenly control the gas flow rate to each side and the fur-
naces 2 and 3 process weights cannot be separated. The design gas flow
rate of both sides (north and south) of the new baghouse is 2,830 act.
o
m /min (100,000 acfm). The flow rates observed during the survey were
3,020 act. m3/min (106,800 acfm) for the north side (Station 3), 35%
more volume than treated in the south side (Station 2) 2,230 act.
2
m /min (78,700 acfm). The emission particulate concentrations, however,
3
differed by less than 1.5 mg/m .
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13
Table 2
DATA
Run Number
Sample Date (April)
Volume Sampled (STP)t
ft3
liters
Moisture %
Barometric Pressure
cm of Hg
in of Hg
Stack Gas Temperature
°F
°C
Molecular Weight (dry)
% Isokinetic
Stack Gas Velocity
ft/ sec
m/sec
Volumetric Flow Rate (STP)t
ft3/min
m3/min
Particulate Collected (mg)
Acetone Wash
Filter
Total
Particulate Concentration
gr/SCF
mg/m3
Particulate Emissions
Ib/hr
kg/h
SUMMARY - STATION .
Marathon Steel
Tempe, Arizona
April 197?
1
16
41.10
1,163
0.3
73.18
28.81
206
97
28.82
99.2
42.9
13.1
38,500
1,080
95.4
20.9
116.3
0.044
100
14.3
6.47
2
16
37.04
1,048
0.1
73.18
28.81
220
105
28.84
99.9
39.1
11.9
34,400
960
93.2
24.8
118.0
0.049
113
14.4
6.53
1
3
16
35.29
998
0.2
73.18
28.81
212
100
28.83
94.6
38.9
11.9
34,600
970
46.3
42.0
88.3
0.039
88.4
11.3
5.14
Average
101
35,800
1,000
0.044
13.3
6.05
t STP - Standard Temperature (68°F) and Pressure (29.92 in of Hg)-Dry
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14
Table 3
DATA SUMMARY - STATION 2
Marathon Steel
Tempe, Arizona
April 1977
Run Number
Sample Date (April)
Volume Sampled (STP)t
ft3
liter
Moisture %
Barometric Pressure
cm of Hg
In of Hg
Stack Gas Temperature
°F
°C
Molecular Weight (dry)
% Isokinetic
Stack Gas Velocity
ft/sec
m/sec
Volumetric Flow Rate (STP)t
ftVmin
m3/min
Particulate Collected (mg)
Acetone Wash
Filter
Total
Particulate Concentration
gr/SCF
mg/m3
Particulate Emissions
Ib/hr
kg/hr
14
41.97
118
1.9
72.52
28.55
142
61
28.64
106.7
34.2
10.4
60.800
1,700
14.1
2.6
16.7
0.0061
14.1
3.17
1.44
T
14
40.80
1,134
0.0
72.52
28.55
154 .
68
28.84
108.9
32.6
9.94
58,500
1 ,640'
4.7
0.7
5.4
0.0021
4.76
1.04
0.47
3
14
44.40
1,256
0.4
72.52
28.55
180
82
28.84
107.4
29.2
8.91
50,300
1,400
15.1
0.9
16.0
0.0055
12.7
2.36
1.07
15
55.12
119
0.8
73.00
28.74
184
85
28.84
99.8
39.1
11.9
67,100
1,880
25.3
0.6
25.9
0.0072
16.6
4.12
1.87
5 " A'
15
52.40
148
0.2
73.00
28.74
197
92
28.84
98.2
38.3
11.7
64,800
1,800
6.9
2*
.1
9.0
0.0026-
6.07
1.46
0.66
78
60.300
1,690
0.0054
12.4
2.78
1.26
ft Run No. 2, station 0402 results not included in emission averages because
filter was not in proper position after final leak check.
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15
Table 4
DATA
Run Number
Sample Date (April)
Volume Sampled (STP)t
ft3
liters
Moisture %
Barometric Pressure
cm of Hg
in of Hg
Stack Gas Temperature
°F
°C
Molecular Weight (dry)
% Isokinetic
Stack Gas Velocity
ft/sec
m/sec
Volumetric Flow Rate (STP)t
ft3/min
m3/min
Particulate Collected (mg)
Acetone Wash
Filter
Total
Particulate Concentration
gr/SCF 0.
mg/m3 8.
Particulate Emissions
Ib/hr 2.
kg/hr 1 .
SUMMARY - STATION
Marathon Steel
Tempe, Arizona
April 1977
1
13
57.39
1,624
0.9
72.90
28.70
127
53
28.84
100.0
47.9
14.6
90,000
2,520
12.5
0.5
13.0
0035
00
67
21
2
13
54.28
1,536
1.3
72.90
28.70
157
70
28.84
102.1
46.8
14.3
83,300
2,330
13.2
4.7
17.9
0.0051
11.7
3.62
1.64
3
3
13
53.93
1,526
0.4
72.64
28.60
149
65
28.84
100.1
46.6
14.2
84,500
2,370
17.5
3.7
21.2
0.0061
13.9
4.34
1.97
Average
9
63
\
85,900
2,410
0.0049
11.2
3.55
1.61
tSTP - Standard Temperature (68°F) and Pressure (29.92 in of Hg)-Dry.
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16
o
The particulate concentration from the old baghouse is 100 mg/m ,
more than eight times the new baghouse particulate concentrations of
12.4 and 11.2 mg/m , south and north side, respectively. The old bag-
o
house gas flow rate was 1,340 act. m/min (47,500 acfm), only 80% of
the design flow rate of 1,700 act. (60,000 acfm). No problems were
caused by the gas temperature (101°C)or moisture (<1%). Possible
reasons for this difference include leaking bags, the bag cleaning
cycle or suitability of bag material.
The visible emissions from all three emission points are in com-
pliance with the Arizona limitation of 40% opacity [Table 5]. Rarely
(2 of 14 observations) did the average opacities exceed 10% and these
observations occurred during one sample run (run 3 of the new baghouse,
north side). As can be seen in the observation data sheets [Appendix G]
the emissions increased in opacity at regular intervals. These inter-
vals occurred immediately after a baghouse section was cleaned.
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17
Table 5
VISIBLE EMISSION SUMMARY (Opacity)
Marathon Steel
Tempe3 Arizona
April 12-16, 1977
Station
No.
0401
0402
0403
Run
No.
1
2
3
1
2
2
3
4
5
1
]T
2
3t
3
Avg. of 24
Readings
(%)
5.6
9.4
6.5
1.9
1.0
2.7
0.6
1.5
0.6
1.3
0.9
4.8
13.8
22,3
Readings
High Low
30
20
10
15
10
15
10
15
10
10
10
15
30
35
0
5
5
0
0
0
0
0
0
0
0
0
5
10
More than one set of 24 readings performed
during a single run.
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APPENDIX A
Presurvey Inspection of Marathon Steel Company
Tempe, Arizona
-------
APPENDIX A
ENVIRONMENTAL PROTECTION AGENCY
OFFICE OF ENFORCEMENT
NATIONAL ENFORCEMENT INVESTIGATIONS CENTER
BUILDING 53, BOX 25227. DENVER FEDERAL CENTER
DENVER, COLORADO 80225
Chief, Field Operations Branch DATE. December 20, 1976
:OM : Paul R. dePercin
IBJECT. Presurvey Inspection of Marathon Steel Company, Tempe, Arizona
On November 15, 1976, Messrs. Daniel Yee, EPA, Region IX, and Gregory
Witherspoon, Maricopa County Health Department, accompanied the writer on
the subject inspection to determine the feasibility of performing source
testing. The inspection also included a review of the process operations,
the pollution control equipment and an evaluation of the control equipment
operations.
The plant manufactures structural reinforcement rods from scrap steel.
Approximately 205 m. tons (226 tons) of reinforcement rods are produced
each day. The reinforcement rods vary in diameter and length according
to customer orders [Figure 1].
The plant representatives contacted were Messrs. Charles Brooks,
Manager-Engineering, and George Collins, Plant Engineer.
Process Description
The scrap steel that enters the plant is used without any prior
conditioning (shredding or drying). The scrap steel and alloying materials
(silica, ferro manganese, feldspar, and carbon) are charged into one of
three electric arc furnaces from a bottom drop charge bucket with only
tv/o furnaces operating at a time. The furnaces have rated capacities as
follows:
Process Rate
Per Heat Per Hour
Furnace No. m. tons (tons) m. tons (tons)
1 22.7 (25) 9.1 (10)
2 22.7 (25) 9.1 (10)
3 27.2 (30) 11.3 (12.5)
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-2-
furnace and the beginning and end times of each heat.
A hood is placed over the furnace after charging and contains three
arc electrodes The scrap acts as a conductor between the electrodes.
The hood and eiectrodes a're removed from the furnace after m
-------
-3-
When furnaces No. 2 and 3 are melting scrap the dampers are open causing
60% of the gase flow to be drawn from the furnace hoods and 40% from the
roof monitor and skulling hood. At all other times (i.e., pouring, slagging
and charging) the No. 2 and 3 furnace dampers are closed resulting in 1007,
of the gas flow to be drawn from the roof monitor and the skulling hood.
While furnace No. 1 is melting (damper open) all the emissions controlled
by baghouse No. 1 are from the furnace hood. At present, the No. 1 furnace
is inoperable, the damper is closed and thus baghouse No. 1 controls just
the emissions collected in the roof monitor.
All three baghouses have a control system to prevent the baghouse gas
temperature from exceeding the bag material limitations. During the furnace
melting cycle, if the baghouse temperature reaches a predetermined value
(i.e., 250°F) the damper closes further to allow greater dilution with
roof monitor gases.
At the base of each baghouse are the damper controls, gas temperature
indicators and the cleaning cycle controls. The Company reported that the
bags in each compartment are cleaned by shaking 30 seconds out of every
two minutes. The baghouss operate under a vacuum because the fans are
downstream.
Baghouse No. 1 emissions vent from a steel stack. Baghouses No. 2
and 3 emissions are exhausted directly to the atmosphere from the fans.
The exhaust gas velocity from the three baghouses are expected to ranga
from 12-18 m (40-60 ftj/sec with temperatures ranging from ambient to 300°F.
The moisture of the gases will be near ambient (0-5%). The bulk of the
particulate present in the emissions gases will be less than ten microns
in size. No visible emissions were observed from the No. 1 baghouse, but
visible emissions of 5-10% occurred periodically from baghouses No. 2 and 3.
Source Sampling Feasibility
The baghouse emissions can be sampled following the EPA, Method 5
procedures. Modifications at baghouse No. 1 are required.
Baghouse No. 1 stack is 1.5 m (5 ft) in diameter and 12 m (40 ft) tall
[Figure 2] and has two sets of sample ports. The first set of ports are
10 cm (4 inches) in diameter and are located 3.5 stack diameters (5.2 m or
17.6 ft) downstream of the fan inlet and 2.5 stack diameters (3.8 m or 12.4
ft) upstream of the stack exit. The ports are located 1.1 m (3.6 ft) above
a dualrail sampling platform and 2 m (6.5 ft) about the catwalk. The second
set of ports are 9 cm ( 3.5 inches) in diameter and are located 3.0 stack
diameters (4.5 m or 15 ft) downstream of the fan inlet and 3.0 stack diameters
(4.5 m or 15 ft) upstream of the stack exit. The second set of ports are
directly underneath the first set and about .3 m (1 ft) above the dualrail
sampling platform mentioned previously. The catwalk guardrail supports
the dualrail sampling platform .9 m (3 ft) above the catwalk. The dualrail
sampling platform is 32 cm (12.5 inches) wide and 2.7 m (8.8 ft) long and
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-------
-4-
is made of 5 cm (2 inches) angle iron. Guide wire brackets for supporting
• a portable monorail are located approximately 1.8 m (6 ft) above the lower
ports. Access to the sampling platform is by ladder.
Either sampling location on the No. 1 baghouse stack meet the EPA,
Method 1 and 2 requirements. The top set of ports are 2 m (6.5 ft) above
the catwalk. Sampling at this location would require a platform to be
built. The ports are 1.2 m (4 ft) above the catwalk, but only .3 m (1 ft)
•above the dualrail sampling platform. A clearance of .4 m (13 ft) below
the ports is needed by the sample box, therefore, the dualrail samplinn
platform and supporting section of guardrail would have to be removed.
Baghouse No. 2 and 3 have identical geometries. Neither baghouse
fan exhausts to a stack, however, the baghouse emissions can be sampled
in the duft* between the baghouse and the exhaust fan [Figure 3J. The
duct is straight for half its length and then tapers the other half.
The sample ports are located approximately halfway in this run of duct
or 2 2 equivalent diameters downstream of the 90° bend. Downstream of
the ports the duct geometry converges in one place and diverges in another
[Figure 3] At 0.5 equivalent diameters downstream of the ports the etrect
of the diverging and converging section should have little impact because
the cross sectional area decreases only slightly. Forty-eight sampling
points will be used at the baghouse 2 and 3 location.
There are six 10 cm (4 inch) ports equally spaced across the 1.8 m
(6 ft) wide duct. The ports are 1.2 m (4 ft) above the sampling platform
which is 2.1 m (7 ft) wide and 4.6 m (15 ft) long. The same platform
would be used to sample both baghouse ducts. No modifications are needed
to perform the source sampling.
Summary and Conclusions
The emissions from the Marathon Steel Company plant can be determined
using EPA, Method 5 procedures. To sample baghouse No. 1 several modifi-
cations at existing locations will be necessary;
a. If the lower ports are used the dualrail system presently
in place will need to be moved. In addition, a 51 cm (20
inch) wide section of the guardrail where the dual rails
are attached must be removed in order that sufficient
horizontal and vertical clearances are provided.
b. If the upper ports are used, a work platform with proper
guardrails would need to be provided. This would require
raising the present platform about .75 cm (2.5 ft) and
* The gases at the sample point have a negative static pressure (vacuum)
of approximately 13 cm (5 inches) of mercury.
-------
a09^<
9 B •
/
t t *
-------
6 a
O O
7~c>-A
.©
Figure 1: Plant Plot Plan
-------
-5-
providing the horizontal and vertical clearances described
under (a).
No modifications are necessary to sample baghouses 2 and 3 emissions,
Source tests at the three locations described will provide an adequate
determination of the total emission load.
The process and control equipment operations can be monitored from
the heat logs and the baghouse control panels.
-------
APPENDIX B
Production Data and Process Weight Calculations
-------
APPENDIX B
Marathon Steel
Daily Production Rates
Furnace
1
2
3
m. tons
HR
8.0
6.5
9.7
Production
tons/hr
8.8
7.2
10.7
Hour
0837-1155
1222-1625
0833-1923
4/13
1
2
3
6.5
4.7
9.4
7.14
5.16
10.4
0832-1727
1118-1721
0731-1830
4/14
1
2
3
7.4
8.9
9.3
8.2
9.8
10.2
0957-1321
0820-1936
0550-1714
4/15
1
2
3
— Down*
10.2
9.5
11.2
10.5
0725-1755
0618-1741
4/16
1
2
3
6.9
9.3
7.3
7.6
10.2
8.0
0722-1806
0727-2000
0954-1752
*Furnace Daun for reline
-------
Marathon Steel
Furnace #1 Weight of
Date Material Melted Time Period
4/12 58,989 Lbs 8:37 to 11:55
4 mi n 02
57,331 Lbs 12:00 to 14:37
12 min 02
59,994 Lbs 14:55 to 18:29
29 min 02
4/13 58,536 Lbs 8:32 to 11:49
No Go
57,866 Lbs 12:35 to 5:27
No 02
4/14 54,339 Lbs 9:57 to 13:21
No 02
4/15 Furnace Down
4/16 51,333 Lbs 7:22 to 10:06
No 02
54,486 Lbs 10:26 to 13:33
No 0
no uo
,830 Lbs
54,830 Lbs 14:14 to 18:06
No 02
-------
Marathon Steel
Furnace #2 Weight of
Date Material Melted Time Period
4/12 57,401 Lbs 12:22 to 4:25
No 02
4/13 56,049 Lbs 11:30 to 2:14
6 nrin 0?
57,666 Lbs 2:35 to 5:13
3 min 0?
61,911 Lbs 11:18 to 15:30
No Op (down time)
59,026 Lbs 15:30 to 17:21
No 02 (down time)
4/14 55,301 Lbs 8:20 to 10:45
5 min Oo
61,666 Lbs 12:25 to 15:30
12 min 02 (maintanence)
58,771 Lbs 15:55 to 19:36
No 02 (maintanence)
4/15 59,676 Lbs 7:25 to 10:01
7 min 02
59,186 Lbs 10:11 to 12:37
3% min 0?
58,921 Lbs 12:45 to 15:00
3 min 02
58,159 Lbs 15:22 to 17:55
No 02
4/16 54,006 Lbs 7:27 to 10:15
No 02
51,761 Lbs 11:24 to 14:35
3 min 02
56,659 Lbs 17:40 to 20:00
22 min 02
-------
Marathon Steel
Furnace #3 Weight of
Date Material Melted Time Period
4/12 59,216 Lbs 8:33 to 11:03
1 min 02
59,444 Lbs 11:12 to 13:44
15 min On
59,474 Lbs 13:51 to 16:58
lh min 02
57,561 Lbs 17:09 to 19:23
10 min 02
4/13 58,286 Lbs 7:31 to 10:08
3 min Op
60,586 Lbs 10:16 to 12:49
No 02
55,036 Lbs 12:59 to 15:46
Mo Oo
54,665 Cbs 15:55 to 18:30
No 02
4/14 59,306 Lbs 5:50 to 8:46
No 02
51,586 Lbs 8:53 to 11:35
No 02
53,436 Lbs 11:53 to 14:11
No 02
60,504 Lbs 14:34 to 17:14
5 min 02
4/15 57,236 Lbs 6:18 to 8:28
No Oo
58,624 Lbs 8:34 to 11:08
No 02
53,424 Lbs 11:25 to 13:59
No 02
60,589 Lbs 14:34 to 17:41
No 02
4/16 53,274 Lbs 9:54 to 13:40
No Op (problems)
59,374 Lbs 15:03 to 17:52
3 min 02
-------
APPENDIX C
STACK SAMPLING EQUIPMENT
-------
APPENDIX C
STACK SAMPLING EQUIPMENT
The Scientific Glass Model AP-5000 modular STAC-O-LATUR1'" sampling
train consists of a control unit, a sampling unit and a vacuum unit. The
units are connected together with quick disconnect electrical and air lines
and umbilical cords. A ground fault interrupter provided personnel safety
from electrical shorts.
The AP-5000 control unit contains the following:
1. Dual-inclined monometer (range 0-5" H20) for indicating the
pitot tube velocity pressure and the orifice pressure drop.
2. Temperature control for the oven and probe.
3. A flow valve and a bypass valve for adjusting sampling rates.
4. Digital Temperature Indicator (DTI) which give an instant
readout from six (6) points; stack, probe, oven, impinger
outlet, meter inlet, meter outlet by the use of a selector
switch.
5. Umbilical cords of (50 and 100 ft lengths) which interconnect
the control and sampling units.
6. Communications sets are wired through control unit, umbilical
cord to the sampling unit*.
The sampling unit is made up of three distinct sections; impinger
case, oven and probe. All three sections can be converted to form one
sampling unit or can be separated for unusual sampling conditions. Below
are the individual component descriptions:
1. Probe Sheath - Made of 316 stainless steel. The nozzle end
is packed with asbestos string. The ball joint (sampling
unit) end has a woven teflon 0 Ring as packing material.
2. Probe liner - 5/8" O.D. medium wall glass (pyrex) or stainless
steel (316) tubing logarithmically wrapped with nicrome heating
element, having a resistance of 2 ohms/ft. The liner is in-
sulated with fiberglass and asbestos with a type K thermocouple
imbedded for sensing the probe temperature.
3. Filter Frit - Porous glass frit (coarse) banded to silicone
rubber.
4. Oven - Fiberglass insulated capable of maintaining 120°C
(248°F) in cold weather (0°C).
*Separate communication system used during this test program.
-------
-2-
Thc vacuum unit (pump) is capable of drawing a high vacuum (50 cm Hg)
and a moderate volume (11 1pm) of air. The pump is rotary fiber vane type
which does not require lubrication, but oil bath filters are used for pump
protection.
-------
APPENDIX D
Calibration Data
-------
APPENDIX D
CALIBRATION DATA
Dry Gas Meter Calibration by outside source
Control Module #_zb _ Make fip $<:<.<:
DGM Serial i
Calibrated by (\>HLK WV/ce. On 7 eft ?
DGM adjusted (yes/no) ycz _
Calibration: IN. OUT
Capacity
Check (40%) Runyff/ ??.?
Personnel v/ho obtained calibration
<.
Date fen 7,
Comments:
Dry Gas Meter Calibration by outside source
Control Module # Make
DGM Serial 9
Calibrated by On_
i
DGM adjusted (yes/no)
Calibration: JN OUT
Capacity Run
Check (40%) Run
Personnel who obtained calibration
Date ~
Comments:
-------
Orifice Meter Calibration
Date
Box No.
Barometric pressure, Pb= in. Hg Dry gas meter No. 7& 6
Ori f i ce
Manometer
setting,
AH
in. H,0
t.
0.5
1.0
2.0
3.0
4.0
Gas volume
wet test
meter
V
ft3
_5_
-*-
-40-
*h
Wr
Calculations
AH
0.5
1.0
2.0
3.0
4.0
AH
13.6
0.0368
0.0737
0.147
0.219
Gas volume
dry gas
meter
V
ft3
^/07
f /re
A* Wf
/e>>34/
Tern
Wet Test
Meter
V
°F
erature
Dry g^as meter
Inlet
°F
£3
£y
6 2
63
Outlet Average
W td'
op op
£f &
£1 63
(,*> £*>
6
-------
Orifice Meter Calibration
Date
7
Box No.
--
Barometric pressure, Pb= in. Hg Dry gas meter Ho.
Ori f i ce
Manometer
setting,
AH
in. H90
0.5
1.0
2.0
3.0
1 4.0
Gas volume
wet test
meter
VM,
ft3
5
5
10
10
10
Gas volume
dry gas
meter
vd«
ft3
57 /
/O o~3>
/c,r^3
/o 2 )
Tern
Wet Test
Meter
V
°F
(*zT
(*g~
CZ.&
GCr,
66 rj-
erature
Dry qas meter
Inlet
V
°F
7V
S^
^
cfi
/.c
/c
/c
/£
/AH0
/
/
/
.c=
/. 4.
,'
. /
I.L
AH(3
0.0317AH
Ph (tri+ 460)
f
(tv, + 460)5
' vw _..
.ooo«3/t.^ /373//<^-/.^
. Of V -.€"••£? tf^x. 7.7^42^ 5 ^ • ^"' '•* / d;
. o< ->c^r>r> M 7 < "3 -S t;3 7c.7'7 - LL,/
. Of ~>c>f~>f ">"?-£ *) VoSy?) u. \ ~ I l
~ f
, £>O("'<'5o<7?,rXSv/ snt'/'^ "'!S'/-7t
Where: V = Volume, v;et test meter Calibration
Vd = Volume Dry gas meter
Tw = Temperature, Uet Test Meter ' Checkec
Tj = Temperature, Dry Gas Meter
?5 = Atmospheric Pressure, Inches Hg
0 = Time, minutes
i by: 5^(-r^j-^U-/^-
J by: ^'-'' -' - -r
-— — •
j
y
*-
7
o
c?
>7'
,>"
— - —
Remarks:
4/24/77
-------
U> I nvironrnsruai rOi.cci.ion if
NaL'onal Enforcement Investigations Center-Denver
Calibration Pitot Tube: ID Number
Typc-S Pitot Tube ID Number:
/
Ap
Standard
Pitot
2.f
i r\
&* -Ls
i..f
10 .
.So
• fe/
.41
•
.
•3-1
•
AP S-Type Pitot
A leg
•tf.c
V.o
4.0^
3.&\
3o^
2 V
;?3*r
5.35"
/, (o
/.<*
LL>
"/. 2S"
1,^-5^
/ *75K
, 'J7X
*&Z
,74*
,735
•'7V*
,7V*
•/J"?
, Tti-\
>7Xl
<7?3
.777
, 7M
,7*£
. ?Q *>
,'77
-------
Ur Fnvironnnntal Protection Ayoncy
Nai:onal enforcement Investigations Center-Denver
Calibration Pilot Tube: ID Number
Type-S Pi tot Tube ID Number:
AP
Standard
Pi tot
.11 •
.o?.
i3V^'
Xtf^
•
•
3
B
// ^ /
.^-f ^
/V^^
*V33
• sr 3 7
.^•^7
- ^-^>
-;7//fr
Co^ioients
•
•
•
•
•
-
-
•
•
•
.
Leg Average Cp
During Pitot Calibration:
probe sheath attached
nozzle attached
sampling iso!flJ( I
7-7
-------
US rnvironnrnlfli iTCKecuon
oiuil Diforccn!«rit
Ccntcr-Dc:nvc:r
Calibration Pitot TubcrlH Number /{/
^).SD
O.SD
6. (So)
*> !&<•
,
.
•
>Ap S-Type Pitot
A leg
1. IS
I-/0
>\0
n-~\i •
/Ml
0 .-71
n •'*?>
/) -^^
(0 ^^
B loq
\.-\o
1-1"
1 - 10
o.~j£s-
/J-T6S
n 1<^^
/? . "Ji'S
O - a ?3
^ .a V3>
-
c
A
.''.^r/.'
£) Vjb
.0- :.>b
6 -7^
c--?^
,---. ~,*r
/» •*/ ^-:
o-9«
. 7':>'
.
6-^95
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o.'(M
6'ftf
f) "'d
D-tM
/>•?(«*
,1 ?^
i ""' '
>7^
^, "C?.V
6 'S-61
Comments
LtixJ /5^,/Z-^r- <^K
Vvv^,. *- ?>
_
•
^vvu.lt 'kiAtuM^wtfcL. "^ 6
l,,t,l f ^v,-. rj/r '
•
•
»
•
.
Leg Average Cp
During Pitot Calibration:
probe sheath attached
nozzle attached
sampling'isokinetically j
PerFonr.ad By:
Calibration Date:.^/ ^ 77
-------
US Environmental Protection i\gcncy
National Enforcement Investigations Center-Denver
Lcll IUi CILIUII r
Typs-S Pi tot
Standard
Pi tot
^0
1,5"
77
.9?
,5-?
.3?
.£/
1 W ^ 1 W W W * * *
Tube ID Numt
AP S-Tvpe
A leg
y 2^
*/2-
3.2-
3.2-.
Ziff
2,15
2.M5
l'l
\,(*5
]MS
A3
1.3
1,3 '
£7^7"
ffi
£7
.£7
,37
/?#
i3&
During Pitot Calibration
proba sheath attach
nozzle attached )
sampl i ng " i sojprf^t ip
Performed By^f^/^-^/o
>er: ^-/
Pitot
B leg
l/2_
t/2^
4'L^
3?>
3.*>
13
2,5-
^.«/5'
2£
\,n
1,1
/.35
A3
1,3
.9^
i9fr
i^7
,67
.57
iJ9
:
ed V^3"
^-5^\
C
A
,??/
»77/
i77/
,913
/9^3
^75"
,975'
,76"5
,7^7
,9^7
.77Z
,7^7
.7^7
.762-
,762L
,753
,95?
,93^
/7J^
/ 7^^*
B
, 777
-77/
.97'
/?^7 -•
t&&1>'
/9£9
,775"
,7^,7
9t$5"
\^].^S'
,9^-7
,75*7
,7^7
.7^7
>1U
.n&L
,n&-
,H53
,953
/75"3
,74^
.9^
,7^
Comments
'
11
!''
•
B
•
.
Leg Average Cp
R-l 0 (o^" M«v
^ ^n J
nr
'ally)/z/(?
^^
Ax y y X^7 ^^^ X
'J*ri£*L/ Calibration Date-.J^V^X^^X7
-------
.ivironmpntal Protection Agency
.uional Enforcement Investigations Center-Denver
Calibration Pi tot Tube: ID Number
Type-S Pitot Tube ID Number: fr
Ap
Standard
Pitot
.// '
.OZZ
•
m
•
xAp S-Type Pitot
A leg
.21
i7l
i2\
ill
- - t-^-t — - -—
,//
./I
B leq
,2i
,2)
M
,!/
t'l
,/i
c
A
.nil
-7/7
-•7/7
.900
,900
r9oo
B
..9/7
.9/7
/9/7
,9oo
,700
i7oo
Comments
•
•
.
•
•
Leg Average Cp
During Pitot Calibration:
probe sheath attached y
-------
US r.nviromnenlal Protection Agency
.io'L Enforcement Investigations CenLer-Denvo*'
Calibration Pi tot Tube: ID Numh2r_
Type-S Pi tot Tube ID Number:
Standard
Pi tot
S-Type Pi tot
A leq
B leg
A
D
.
6 • 1 '
•^ • i -.
-> •-'
0
(9
"I
•\.y\i
1 .
-v'7
, ' /
0 *:.
i_io
P 6 6
During Pitot Calibration:
probe sheath attached
nozzle attached
samp!ing'isokinet;
">rfor;nsd By:
Leg Average Cp
Calibration Date:
-------
APPENDIX E
Source Tests
-------
V-/3-97
O4t>3
APPENDIX E
SOURCE TESTS AT MARATHON STEEL
01
00003
"
o.
0*1311
- 77
0^03
02
0. 73
0.
-£- 77
03
0.
0.7317
0.0039
-/?- 77
-<-
01
OOOO&
0. 73S8
0.
0.73*8
0.00 £(&
-------
BS/fK^K.
7/JJL Of
H/T?
7/1XS.
Of
96.
01
98.
o.ooov
03
£2°-
. 0/38
?'/.
O.OOO'/
7?
Of
V/.J&08
ovo/
'/-
£33
9A/P/89
0. 073/2
03
9Z39/0
97.370?
of
98.326V
0.0/+/I
&L
o.
03
30
O*/
/to
73.
O-
96. 3 8/'/
O. O06?
-#- 7?
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O. Oft?
-------
($
- 79
O'/O/
01
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COOS'?
it/?:
o.
a
0.
F/JL
a
a 73 7?
IV7T
-------
APPENDIX F
Chain of Custody Record
-------
APPENDIX F
ENVIRONMENTAL PROTECTION AGENCY
Office Of Enforcement
NATIONAL ENFORCEMENT INVESTIGATIONS CENTER
Building 53, Box 25227, Denver Federal Center
Denver, Colorado 80225
CHAIN OF CUSTODY RECORD
^URVEY
.' /' ft >*— — -. ^
,-•:- • ....... TV'. .>.&«./ f
STATION
NUMBER
•i '/ -» "
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f ' •;• - 1
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Wo'
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STATION LOCATION
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elinquished by: /Signoiure;
.elinquished by: (Signoiurej
Relinquished by: /Signa»u-e;
Relinquished by: (Signature)
Uispatched by: (Signature)
.Method of Shipment:
Date/
TIME
/«//<
, v/
/.:/::,
7-r-T
v' <- '.-
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SAMPLERS: /Signer,;
SAMPLE TYPE
Water
Camp
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Air
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Received by: /Signa/urej |V
Received by: ffrgnorure;
Received by: /Signature;
Received by Mobile Laboratory for field
analysis: /Signature;
'Time
Received for Laboratory by:
Date/Time
Date/Time
Date/Time
Date/Time
Date/Time ,
c;i5/7/
Distribution: Orig.—Accompany Shipment
1 Copy—Survey Coordinator Field Files
CPO B3I-48*
-------
ENVIRONMENTAL PROTECTION AGENCY
Office Of Enforcement
NATIONAL ENFORCEMENT INVESTIGATIONS CENTER
Building 53, Box 25227, Denver Federal Center
Denver, Colorado 80225
CHAIN OF CUSTODY RECORD
JRVEY
STATION
NUMBER
'/".•"
f
• '/ * v
...
.
- It
'-.II- *
/ -'•• ->
STATION LOCATION
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elinqujshed by: (Signature;
lelinquished by: (Signature;
Relinquished by: (Signotu.-ej
Relinquished by: (Signature;
Dispatched by: (Signoiurej
Method of Shipment:
Dote;
TIME
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SAMPLERS: (s.gnoture;.
•"" SAMPLE TYPE
Water
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.* • • r
' ' • *"
.-<,. /
^i.r'.
.-^>7r>
Received by: (Signature;
Received by: (Signature;
Received by: (Signature;
Received by Mobile Laboratory for field
analysis: (Signature;
^Time
Received for Laboratory by:
Date/Time
Date/Time
Date/Time
Date/Time
Date/Time
Distribution; Orig. — Accompany Shipment
1 Copy—Survey Coordinator Field Files
6PO 831 -464
-------
ENVIRONMENTAL PROTECTION AGENCY
Office Of Enforcement
NATIONAL ENFORCEMENT INVESTIGATIONS CENTER
Building 53, Box 25227, Denver Federal Center
Denver. Colorado 80225
CHAIN OF CUSTODY RECORD
SURVEY
STATION
NUMBER
^,,.7>.
1
STATION LOCATION
0.0 ^ <-tJ> *?
A.T. * i. J^
DATE
<•)/' ^.V
uf. r-V
'
Relinquished by: {s,gnoiurc)
Relinquished by: (Signoiure;
Relinquished by: (Signotu.-e)
Relinquished by: (Signoturej
Dispatched by: (Signature;
Method of Shipment:
Datey
TIME
' /-^ uCV
,-?r.
SAMPLERS: (Signature)
SAMPLE TYPE
Watei
Camp
Crab
;.-'
, .-'
Air
SEO
NO
<•-
I
NO OF
CONTAINERS
3
i
ANALYSIS
REQUIRED
. ''./'., '.<.- ( -t1'-'^"
../^. /v.;..^
Received by: (s,gnoiuie)
Received by: (
-------
APPENDIX G
Participate Field Data
-------
Plant,.
Run No.
Location
Date
Operator
?ri£. iK>
ICU _ IE1 A
VERY IMPORTANT - FILL IH ALL BLA.VKS
Read and record at the start of
each test point.
Time: Start Time
End Time
Ambient Temp "F C* <~
Bar. Press. "Hg ^^ .<
Assumed Moisture 7._
Probe Tip Dia. In._
Pitot Tube No.
-------
!. f „,
Point
R-/V
II
JG
Clock
'/£"
bo
(-1
Dry Gas
Meter, CF
.7
C*
L
VL
7<
Pitot
in. H-O
AP
m.
AZ
Orifice AH
in H20
Desired
,76=
Actual
'• i r
,17.
±£L
/.O
Dry Gas Temp.
•F
Outlet
yv:
Inlet
f?
sv;
.96
Pump
Vacuum
In. Hg
Ir.pinger
Temp.
°F
U-
131
9--'.
/— '
Oven
Ten? .
Probe
Temp .
°F
Pvy
Stack
Tec?.
°F
St
Te
n
7?
Cocunents:
3/16/77
iZ
.47
1,0
?/ w
-7
/--si?
-------
SAMPLE CLEANUP SHEET
Plant: >^<..s*£. ^fc^
Address: /^.^r? , ^2— •
Station No'.: O^QJ
Run No.: ?^/
Barometric Pressure: -3,^7
Date: bs% ml Of ^-rd'-^l
> ml
ml
ml of fas &•(*->
ml
ml
ml of -^ — \^£.
ml ' ?
ml
ml of
ml
ml
r~gmof 4.£:'*^. &J&'
s" gm ^
gm
ml
Weight .
Tare Weight Collected
gm gm
gm qm
^C -v- on f/2'4/'??
-------
KECOJfl OF VISUAL DETOMIWTION OF OPACITY
a
C7
COMPANY /v-d/2/^no/J *Q:&&-L
LOCAT ION "^fCn^p^ t £\(L '] 2o.o*V-
TEST NUMBER ' O -7_
nnSFIIVER ArFILIATIOII L^"> ^/^ .
POIHT OF missions ^C^evC
HEIGHT OF DISCIWRGE POINT LrO r£T _
o
P
v>
•o
0
1
CLOCK TIME
OBSERVER LOCATION '
Distance to Discharge
Direction from Discharge
Height of Observation Point
BACKGROUND DESCRIPTION
LEATHER CONDITIONS
Hind Direction
VMnd Speed
Ambient Temperature
SKY CONDITIONS (clear,
overcast, % clouds, etc.)
PLUKE DESCRIPTION
Color
Distance Visible
OTHER IHFOK'ATIOIl
Initial
&
^
-T
r"1//^"'! y^
<&>y
z£i?
of
???£
CM*.
vh.bz
\s *^ " **
Final
So'
fat
£w^
^
tottf
o-£
?£- %£
CLSK
Uh:te
tip'
i
i
1
SUWftRY OF AVERAGE OPACITY
• Set
Number
leadings i
'he sourc1
:he tiir.c
Tl-n
Start-End
Csaclty
S-jn
•anqcd from to X opac
i was/was not in ccnpliance wit
ivdlualion v;as race,
I^SS5«
ii-y
h .at
-------
03SERYATIOH RECORD
CO^AVY I'kr&Jfo^SjTZiZL, Q9SERVCR ^
LOCATIC'r"^-. -n,1-^ qp-.Tror-irt- TYPE FAClUT
TEST .v,"';U 'si/r,/ POINT OF ""
PATE cy///./'-, 7
D x-~-£AGE , OF x ,
L'lt
HI
i
^L
Y-J --j-r'-.r;/1 r^ )._/_t_
5S IC'li b ^ '4 ~'\ c UL
CC'-lHEtlTS
» ^ ' ' tr*
(Con
COMPANY
LOCATION
TCST
DATE
Mr.
,
MMSER
K
3'j
3"UJ
37
3!t
'.0
•TV"
15
47
/•.ij
50
fil
5,,
ij
" l^j;
15
"Of,
57
59
Seconds
6
Ib
3'J
<".'j
(c^
A(
[FO Doi.T
CESERVATIOX RECORD
PACE _ Or ^ .
02SEJWM
TYPE FACIllTV
POINT OF CMISSTftiT
[FO Ooc.?4-20ISO FUMl 11-11-71:8:45 am]
WCJ^CZ, VOL 39, NO. 219-.TUZSDAY, NOV£;rtB:S 19, 1974
-------
Jy-ut>Vv-. ^
ART DAT
VERY IMPORTANT - FILL IN ALL BLANTCS
Asblent Temp *F /T7T
Run No.
Location
• *
Date
/
= /~
f
Operator_
Read and record at the start of
each test point.
Time: Start Time_
End Time
Bar. Press. "Hg ."<,~
Assumed Moisture Z jQ
Probe Tip Dia. In."
Pi tot Tube No. £.> a_-
Filter No. /.2 ,
/,
z >
Point
Clock
Dry Cas
Meter, CF
Pitot
in. H-0
AP
Orifice AH
In H20
Desired Actual
Dry Cas Temp.
"F •
Outlet Inlet
Pu-"?
Vacuun
In. Hg
Inpingcr
Temp.
•F
Oven
Temp.
"•F
I'robe
Tenp.
•F
Stack
Tcp>p.
•F
Stack-
Ten-p.
•F
CF+460)
F—/9
.S
/ ^
V v/ •--•
'c
/•r,
v
v/
c/
c .
VI
c
f) -'
"l.'/'J
'77
X -'-
/o/
•\
to*
12_
/<$
< a
Coraccnts:
-------
5riv.t-i_ ~
Point
10
7
Clock
9
Dry Gas
Meter, CF
Pitot
In. H-0
AP
to
Orifice AH
in H20
Desired
Actual
67
Dry Gas Temp.
°F
Outlet
/oo
Inlet
97
• -
/&>
/GO
/cf
/oo
Puaip
Vacuum
In. Hg
i.v
Icpinger
Temp.
/*?•-.
Oven
Ter.o .
°F
372-
Probe
Ten?.
6F
Stack
Teno.
°F
23$
Sta'
Ter
CR
CF
1.1
, 0 y
57
1.
jut*
/o-O
/• 7
2,0
*2-
Comments:
3/16/77
/ 7
,56 •
fCrO ,
/(rf
/&
-------
SAMPLE CLEANUP SHEET
Plant: // iv« "*.» ,W,v-/
Address: v'J^ ,,- ,.#v,t,. — .
^' Date: /^'.-'•/Xr.//r7
Operators: -^.i'/^^-'
Station No. : .;' -//. ,- : '
Run No. : £1
Barometric Pressure: '^Lf.
Ambient Temperature: /to
Sample Box Number: /
Impinqer 1
Final Volume /be?
Initial Volume ,'&!_,
Volume collected c*
Impinqer 2
Final Volume 9^
Initial Volume 7 oo
Volume collected —(,
Impinqer 3
Final Volume &
Initial Volume <-',.... L,
Volume collected ' xr>
Impinqer
Final Volume \^
Initial Volume \^
ml of Oi^ 1. ^-"' /'\j 0
ml
ml
ml of Pi < 1 • 'l^ U 5 C
ml
ml
ml of
ml
ml
ml of
ml
Volume collected ^^^^ ml
Impinqer
Final weight 7 '.^^ °
Initial weight 1-5 J . t
Weight collected -7. ^
Total Volume Collected /
Fi 1 ters
No. Final Weight
1 <*• . qm
qm
gm of '^. '..-_.-.. G< I
gm
gm
ml
Weight
Tare Weight Collected
qm gm
qm qm
Cleanup performed
on
-------
RECOW OF YISVAt, DETEPfllMTMK OF OPACITY
PAGS_
O
C.
COMPANY
LOCATION rtffl&ti * I-
TEST NUMBER
DATE
/77
TYPE FACILITY v-^u/^
/~-^
raOC
"ft-^r
-Tar5"
HOURS OF OBSERVATION //. VsT- /V..57
03SEHVER ^ X/
OBSERVER CERTIFICATION DATE.
OBSERVER AFFIUATICII/Al/S
POIfiT Or EMISSIONS ST/J
HEIGHT OF DISCHARGE POINT
o
p
O
J5
o
et->
Final
F
1
1
SUMMARY OF AVERAGE OPACITY
Set
Number
leadings i
'he source
the tir.c <
TVo
Start-End
OoacUy
S'JT
•anqed fro.Ti to % cpcc
; was/was not in ccnpliance, wit
: valuation was rade.
/'vcrcgc
-.,
iiy
h it
-------
COV?A
LC:AT
TEST
PATE ,
OBSERVATION RECORD PAGE t OF 1
VY (Yi, \idfVi i^.-u :-rc,
n-/
IV.
1 —
^^mm^
:jj=
rt— 1
-ij—
— -i —
0
1
2
3
tT~
•7
c
1'J
11
\2
13
I-1-
t»-tT
I""""1" "
— lic-j
.1
V?
li'l
^J
;o
Ml
i 1
?H
23
Seconds
0
—
s
tjl
_
la , 3H | £3
1 1
-V
rj;
~c:
TT"
—
r— — r~f
r^q
..'
ir
Vr?"
•*»•'
1
j •
r-
!tC
AC
/C
_.-
STEAM
(ch?C'' If
7i-:tocT?T
TYPE FPCIL1T
POINT CF EX1
•LU.1 iE
iT^l Iciblc^
ilCUChoS
Y sr.-^d- ,^i/i i
5510|ib -.r/i •- '--
CCMHEHTS
COUPA
L OCA i
TCST
DATE
HP.
II
_U_
_Li_
|i
I 1
-
c
(Con
IOM ^it,, .- r> J_
NUKaE*
'/
1. " -?-
'//,-/-/'/
/ /
Kin.
30
31
3?
.(1
3'j
37
33
• '.0
•11
1<>
a.r
45
— jy
'•H
50
51
' b3
iX
SS
5G
57
OB
50
IT
•^r-
-=5-
"ll^'
;.;•
II :
S-cond
T5~
-3=-
cT
—^~
/-,"
3'J
4^
Tr^
,f.
•.,'1
,^-
IP
s
-r
~7"T\
;«,-
(•**'
'c1
At
n oos.7
OBSERVATION RECORD
PAGE OF_
OBSERVER
7T?c rAClLlTV s -i^-.
POINT OF EMlSS10;i7"Tr>I2L
D05.7i-201}0 FUcd 11-11-74.U:«5 us]
KDt-lAl KCCtJTE^ VOL 39, NO. 219_7U:St»AY, NOVWfltR 12, 1974
-------
Run
Location
Date
Operator >
RTIi 1 ATA
VERY IHPORTANT - FILL IN ALL BLANKS
Read and record at the start of
each test point.
Time: Start Tiire_
End Time
Ambient Temp *F
Bar. Press. "Hg C? f~. /"/'
Assured Moisture Z (. "*
Probe Tip Dia. In. <• -2
/£,
Picot Tube No. ."5~~J
Sample Box No._
Meter Box No._
Meter A H
C Factor /. /5
/
Probe Length/type
...
Filter No. /- ^
/. 6 S
-•* / •
/ / V J '
Point
Clock
Dry Cas
Meter, CF
Pitot
in. H,0
AP
Orifice fiH
in H20
Desired Actual
Dry Gas temp.
°F
Outlet Inlet
Punp ,
Vacuum
In. Hg
TCP?.
"F
Oven
Te~p.
°F
Ten1?.
•F
Stack
Tcro.
"F
tack
Ter-p.
°F
/-
?;"' X "
'//
/'/*
//&
r - A-
f,/)
v'i'V
x'
Jl
J//
/V
(,
670
6,76
7
/'f
3 a*
Coments:.
-------
aheec
-' -r
Point
10
Clock
(,-.&
Dry Gas
Meter, CF
"03 .
-9
L±
Pitot
in. H-0
AP
, So
Orifice AH
in H20
Desired
9o
,9o
Actual
.1*?
Dry Gas Teirp .
°F
Outlet
137
Inlet
/3
13$
310. II
•3/3,11
Pump
Vacuum
In. Hg
lopinger
Tenp.
/if
A3—/I
I.I | /H9
Oven
Ten? .
J&9
Probe
111-
P-7/
tack
Stac!
Terp,
Lcr
2-10
6,-?
7?
,70
3/?..»./
.vi
Ch
131
Comcients!
in
ffl*
/O"
iff
3/16/77
-------
SAMPLE CLEANUP SHEET
Plant:
Date:
Address: " X^.-,i_e ^V
Operators:
Station No.: rv-- / :
Run No. : -^ V
Barometric Pressure: Z*.F. 7Y
Ambient Temperature: sr^'"
Sample Box Number: /
Impinger 1
Final Volume
/(
Initial Volume
Volume collected_
Impinqer 2
Final Volume
_ml of
jnl
ml
Initial Volume
Volume collected_
Impinqer 3
Final Volume
ml of_
>1
ml
c?
Initial Volume
Volume collected
Impinger
Final Volu>
Initial Volu
Volume coll
Impinqer
Final weight
Initial v/eight
Weight collected_
_ml of
_ml
ml
ml of
of
-7/7
gm
Total Volume Collected_
Fi1ters
/
No.
Final V'eight
gm
Tare Height
gm
gm
Weight
Collected
_gm
Cleanup performed by
on
*//*/?> -
-------
RECORD Or YISU/V. DETCRHIWWK Of OPACITY
PASS
o
c;
COMPANY..
LOCATION
TEST NUMBER
DATE •
TYPE FACIL1TY_
CONTROL DEVICE
//£><->--.£
HOURS 0? 03SERVATJOJK
OBSERVER )A/ ~7~r'
OBSERVER CERTIFICATION GATE
OBSERVER AFFILIATION
POINT OF EMISSIONS '
"HEIGHT OF DISCHARGE FOMT r* ^p '
o
u
i>
5
v«
O
>
r
o
CLOCK TIME
OBSERVER LOCATION
Distance to Discharge
Direction from Discharge
Height of Observation Point
BACKGROUND DESCRIPTION
HEATHER COMITIOw'S
Wind Direction
Wind Speed
A.m.b1cnt Temperature
SKY CONDITIONS (clear,
overcast, X clouds, etc.)
PLUKS DESCRIPTIOft
Color
Distance Visible
OTIIC^ 1KFOOT10II
Intal
LlfafL
Final
SlWIttRY OF AVERAGE OPACITY
Sot
Number
Start— End
Osjcity
S-j-n
Readings ranged from
to
opacity
The source was/was not In ccnpllancc with ,
the time evdluaLion v;as rracie.
-------
OBSERVATION RECORD -PAGE OF
LC-ATJC'i _—i •- 'f-,, >i
TTCT I'H'oTS—r~t—r
I t J 1 | lv • t. A f "I / I • /
BATE •/ A,. / -7 7
OBSERVER
7Y?E FACILITY'' x^,-,.- / ,'Q
POINT OF EMISSIONS -->.>K v
,,„
^M^VB*.
Mln.
0
s—
3
t.
1 0
0
7
r
<•
Vj
n
U'
13
K
1 5
16
17
•-1-
15
*;j
0
~S'J~
^n
?>
"i
i9
1 STL AM
Seccirfs !(ch?c''. 1f
0 l 1 > ; 3(T
•>F t
->
-,
7^
«7 '/ (s
• f\ /,
->
'~
•/^
"^i
1 1
1
1
—
I
1 '
•-b
•s
^
-y
VT'.lcC/ VJ
I
|
I'LU.'.t
"n^cfea
'CCWt.'lTS
'» **
^
.
CESEWATIOK RECO!ID
(Continued) '
PAGE OF^.
COKPA'JV
lOCAfioM
TEST liW,SER
DATE '
TYPE FA:I
POIIlT OF
llr.
Kin.
20
31
??
Jj
J-!
3'j
3u,
37
3)1
>1
'.U
•11
«<;
«i
•M
15
.-.r,"
17
'••1
ao
5"o
r.i
5?
bJ
M
OS
'"or,1
i/
50
"59
Srconds
0
IJ>
3U
'.'j
-
STtAM I'LO.'ili
/c'lock If as-iHcnble)
Attacicd
Ootecnoo
COIWcKTS
1
us]
FEOIMl RIGIJTCZ, YOU 39, NO, 219—7U;SDAY, NOVEMBER 12, 1974
-------
Plant x
CULj ELE
VERY IMPORTANT - FILL IN ALL 3LAMCS
Ambient Temp "?_
Run No.
Location
Date /i".
Read and record at the start of
each test point.
Time: Start Time
Bar. Press. "Hg >.? fr • ^
Assumed Moisture 7. C*
Probe Tip Dia. In. C • 3-]$
Operator/*^,
End Time /Old)
Sarple Box No._
Meter Box Ho._
Meter A 11
Pltot Tube Ho. o " i
Probe Lengtli/type c /(?/<-*<*
Filter No. 6; .
C Factor /•
7£'
"/A O •<* a 5 C
Point
Li£
Li_i
A'-/,
-
Clock
If?
- 1
£i_Z
/" -'/
*•!
Dry Gas
Meter, CF
>7
<•)*.}! .0$
Pitot
In. H,0
AP
0 7>
r . rt
Orifice AH
In It20
Desired Actual
//*
X/o
/-
0
0
Z1A
/
Dry Gas Temp.
°F
Outlet Inlet
2/
73
-73.
7/
7/
V/
-7V
7-5
^ /
Coiracnta:
Punp
Vacuum
In. HE
? -o
? 6
Inplngcr
Ten?.
8F
7'
I/
7*
71
7V
Oven
Tcrp
°F
Probe
Temp.
°F
-
tf-S-
Stack
Tcr-p.
°F
Stack
Teirp.
•F
US
//f
"7
s/t
,.
-------
X7*"- /
Sheet g2. of
Point
Clock
Dry Gas
Pitot
in. H20
AP
Orifice AH
in H20
Desired
Actual
Dry Gas Temp.
Outlet
Inlet
Pump
Vacuum
In. Hg
Impinger
Temp.
oF
Oven
Temp.
Probe
Teap.
Stack
Ten?.
op-
Stack
Tenp.
°F
D-'s
C? '
a-5
16
o-So
O
14
16
D-6
6
o-s
11
O - q S
n
It,
/o
11
0-3
0-
.<:<•/
<6\
M
;G
2 (30
6-S
0-7
L,
0 s^ 0 GG
- Vb
O
-sd
/T9
0-
t
0
o.
9?
S-5
l»
'V
c-i n
Comments:
a-"*
a
65
f 7
A /
(*lf
L'LO
3/16/77
-------
Sheet "S of
Point
Clock
Dry Gas
Meter, CF
PItot
in. H~0
AP
Orifice AH
in H20
Desired
Actual
Dry Gas Temp.
°F
Outlet
Inlet
Pump
Vacuum
In. Hg
} y
Impinger
Temp.
Oven
Ten?
°F
Probe
Temp.
op
Stack
Temo.
°F
Stack
Ten?.
°F
0
0
0
0
•56
/c
257
f
0-
O. 'i
o
0
3.
JO
0-MS
0
o
.0
2-0
/to
O lo
o-n | O.n
n-f
o-
0 '£"0
o
Jo
Jv?
Cil
n-
So
0
o
1o
(o 6
o
fl
0 Cv I
P'C/
<-/<•(
/M
6
a IS
*?<-/$
/?*
6 -
C J
Comments:
3/16/77
-------
SAMPLE CLEANUP SHEET
Plant:
Date:
Address:
Station No
Run No.:
Barometric
7 -r-
m *
s?t
*£'£• ^
Operators:
•
•
/ ' •
>f / Ambient Temperature:
Pressure:
Impinger 1
Final Volume
Initial Volume
/ S"
Total Volume Collected
Filters
No.
Final Weight
gm
_gm
Cleanup performed by
_ml of
jnl
ml
ml of
"ml
ml of
ml
ml
ml of
~ml
"ml
*/. S~ qm of
ml
Tare Weight
gm
gm
•
on
Weight
Collected
gm
gm
-------
RECORD OF VISUAL DETCRHHttTIOK OF 0?AC!TV
PAG" / C?X'
LOCATION,/Sv.^ -
TEST MJKBER_2±/_
DATE
TYPE FACILITY
COIJ1P.OL DEVICE
HOURS or ossERVATiofr.
OBSERVER
X:- --S-v -•-
OBSERVER CERTIFICATION DATE,
OBSERVER AFFILIATION' &/. /"
POINT OF EMISSIONS /;^/
-------
OBSERVATION RECORD
PAGE
OF£_
LC1ATIC
TEST I;1."'.'I7T
PATE
7v?t fY-cinT7
POIHT CF EM!
/4fc,
IV.
'• *•:
'Hn.
0
1
2
3
'.
_ t-
0
7
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[Pit oo5.74-aeiio
Il-ll-74i8:4) wa]
TEDI2AI UC1STE2, VOL 39, NO. 219~TU£tt>AY, N
!2, 1974
-------
Plant
Run No.
Location
Date /f,3~. I / /,
Operator £r /( fJ<^~>
ICU" IEI A
VERY IMPORTANT - FILL IN ALL BLANKS
Read and record at the start of
each test point.
Time: Start Time I O l) Q
End Time ( £.%
Ambient Temp *F
Bar. Press. "Hg
Assumed Moisture 7.
Probe Tip Dia. In.
Pitot Tube No.
V " '
Sample Box No._
Meter Box No.
Meter A H /
C Factor /
Probe Length/type
Filter No. ~7 .
/S" l-k -
Point
Clock
Dry Gas
Meter, CF
Pitot
in. H,0
AP
Orifice AH
in H20
Desired Actual
Dry Gas
°F
Temp.
Outlet
Inlet
Pu
Vacuum
In. Hg
Inplngcr
Temp.
°F
Oven
Tenp
"F
Probe
Teirp
°F
Stack
Temp.
"F
Stack
Tcr?.
°F
CF+460)
0 41
a
fl'
LOP
/- 7
0
/I -
o-M-G
0
Gl
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97^7?
61
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70
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-------
of ->
Point
Clock
Dry Gas
Meter, CF
Pitot
in. H00
AP fc
Orifice AH
in H00
Desired
Actual
Dry Gas Tetnp.
°F
Outlet
Inlet
Pump
Vacuum
In. Hg
Impinger
Ternp.
°F
Oven
Tenp .
°F
Probe
Teir.p.
°F
Stack
Tenp.
°F
Stack
Ten?.
0
Sg
0
76
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0 /
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0
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3/16/77
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7
V<"
(# 1 5
-------
Sheet 3 of 3
Point
Clock
Dry Gas
Meter, CF
Pitot
in. H-0
Orifice AH
in H20
Desired
Actual
Dry Gas Temp.
Outlet
Inlet
Pump
Vacuum
In. Kg
Impingcr
Temp.
°r
Oven
Tetnp .
°F
Probe
Tercp.
°
Stack
Tenp.
°
Stack
Tecp.
°
c? '
0
11
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Comments:
3/16/77
0/5.7$
P3C-
35
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4/7
-------
SAMPLE CLEANUP SHEET
Plant: A... ^~z€ -. -X^-,-
Address:' ^^-.x , ^
Station No'. : ' ^: -^ :?
Run No.: .«-~»
Barometric Pressure: ^r. j"1"'
Dote: £y^fx£';-
Opera to rs : ,^XX_ /^v
: "/^V/ /'i ^L^
Ambient Temperature: /*->«>-
Sample Box Number: /
Implnger 1
Final Volume
nl of
Initial Volume //? =. ml
Volume collected - *-/ ml
Impinger 2
Final Volume
Initial Volume
Volume collected
Impinqer 3
Final Volume
Initial Volume
Volume collected
Impinqer
Final VW-mpe
Initial VoluTna^
Volume collected^
Impinger
Final weight %
Initial weight ^
<.-^> ml
Z ml
0
(-> nil
ml
ml of
ml
ml
r T / c*1^ £ s s
'/£• o gm ''
Weight collected £ c qm
Total Volume Collected i
6- S ml
Filters
No.
Final Weight
/
gm
Tare l.reight
Weight
Collected
_gm
gm
_gm
Cleanup performed
on
-------
TEST K'JKEER
DATE 9
TYPE FACILITY^.
CONTROL DEVICE
WCQRO OF yiSUAU DETCPJIIHATIOK OF OPACITY
PASc / of
. ,/
HOURS OF OBSERVATION ^/
OBSERVER X '' .rC- /^-c _'~
OBSERVER CERTIFICATION LV,TE_
OBSERVER AFFILIATION' L>- •>''4
POIliT OF
HEIGHT OF DISCI'ARGS POINT
o
Z
O
o
If
i
u>
•o
M
CLOCK TIME
OBSERVER LOCATIOH
Distance to Discharge
Direction from Discharge
Height of Observation Point
BACKGROUND DESCRIPTION
WEATHER CONDITIONS
Kind Direction
VHnd Speed
Ambient Temperature
SKY CONDITIONS (clear,
overcast, % clouds, ctc.y
PLUKE DESCRIPTlOft
Color
Distance Visile
IHFOWIUIOH
Initial
ifo^r
ff
^zsSfr-
H..T-
f&u
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XT,*"
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I
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SUGARY OF AVERAGE OPACITY
Set
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leadings i
"he sourc1
the tiir.c
T<^ '
Start—End
Cocdty
S'JT
•anqcd fro.i to * cpac
: v/,is/wjs not -In compliance wit
2valuaUon was irade.
/vcrcge
fly
h at
-------
OBSERVATION RECORD
PAGE
_ ' --•• Q. . -". -"_^-L..
-«A • .C*i ^* - -/Jf' s fsi
PATE
essrRVCR X-"9-: -^* ,.
TYPE FACILITY " s'-.^--?,,,/:
POL'IT CF EMISSIONS -''.v^T
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CC'IMENTS
/V'Vi /•ir-.lf, {* .*>
OBSERVATION' RECORD
(Continued)
PAGE OF
C(W?A','Y
TEST UMBER
DATE _
02SEWE3
7Y?c FACILITY
POINT or i
.70 §5
'llr'.
fJ'C1
.
MMW
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'check
-------
Plant
Run No. ^ .7
Location_
Date (->
•s /^
>/-=» -V
/ '
Operator_
UL/' ELD
VERY IMPORTANT - FILL IN ALL BLANKS
Read and record at the start of
each test point.
Tine: Start Tire /v/\S
End Time
Ambient Tern? *F
Bar. Press. "Kg
Assumed Moisture 7,
Prebe Tip PJa. In._
Pitot Tube No. >
Sample Box No._
Meter Box No.
Probe Length/type
^
Filter No. 7* .
Meter A H / f'. ?T
C Factor
~ Q,Q p
Point
sv
Clock
Dry Gas
Meter, CF
Pitot
in. H,0
AP
Orifice AH
in H20
Desired
Actual
Dry Gas Temp.
°F
Outlet Inlet
Pump
Vacuum
In. H8
Impinger
Temp.
°F
Oven
Temp.
"F
Probe
Temp.
"F
Stack
Tc--?.
Stack
Tei??.
•F
("F+460)
0.1./0
LOT
/O D
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Coamiciitii:
-------
Sh ee t X o f
Point
Clock
Dry Gas
Pitot
in. H20
AP
Orifice AH
in H.,0
Desired
Actual
Dry Gas Temp.
°F
Outlet
Inlet
Pump
Vacuum
In. Hg
Impinger
Temp.
Oven
Temp.
°F
Probe
Temp.
Stack
Temp.
°F
Stack
Terp.
°F
c,/r
sn
J/C
c-w
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C-7C
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Comments
£./(*
7
.?'•'**
3/16/77
-------
Sheet
of
Point
Clock
Dry Gas
Meter, CF
Pitot
in. H«0
AP *
Orifice AH
in H20
Desired
Actual
Dry Gas Temp.
Outlet
Inlet
Pump
Vacuum
In. Hg
Impinger
Temu.
°F
Oven
Ter.o .
°F
Probe
Teno.
"
Stack
Ter.n .
°F
Stack
Ten?.
A *
/? 7
3. '
0
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in
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040.5^
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0-93
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3.0
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53
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3
£_£
VI
0
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3
// JL
/A
063
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g*?
0
5*
P S"
Comments:
3/16/77
-------
SAMPLE CLEANUP SHEET
Plant:
Address:
Station No.:
Run f!o.:
jDperators:
Pate:.__fc/£^£z
nr<; • .s/ '/. /{.'
Barometric Pressure:
__Ambicnt Temperature:
_Samplc Box Number:
Impinqer 1
Final Volume
ml Of
Initial Volume /o_-
Volume collected - ~7
Impinqer 2
Final Volume
Initial Volume /„&
Volume collected /of
Impinqer 3
Final Volume
Initial Volume 0
Volume collected
Impinqer
Final vVlume
Initial VtsLyme
Volume collected
\
Impinqer
Final weight "J.Z*? -J
Initial weight -^.-3. r. /."
ml
ml
ml of £^TC£
ml
ml
ml of u'/^r-f-.^
ml
ml
ml of
ml
ml
gm of f'LSr,* A_. f
gm
Weight collected 9- -C gm
Total Volume Collected 5, . 5
Filters
No. Final Weight
P . qm
qm
ml
Weight
Tare Weight Collected
gm qm
qm qm
Cleanup performed by
on
(/
j
-------
rccoao OF yis'JAu DETERMHWXON or OPACITY pAss_Lpf_i
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n
C>
COMPANY /ft?*'1 <*«-•" &&*(• Co
LOCATION C> M o "J, ...
TEST KUKDER 1>
DATE //p" ) 1 LL /°l1'l
TYPE FACILITY ,S-io I \M • I/
i\ i
CONTROL DEVICE 1?* • UJw A
o ^j
o-
M
n
% ^^HTIJWTO c
HOURS 0? 03SERVATIOH r
~l i- / ^ C'
OBSERVE!* CEPJlFICi\T10.ir>D.\TE
03SEKVER AFFILIATICH T I3 /I
POIliT OF EMISSIONS £•/«.;'
riEIGIil Or DI5CI!/\Kui r'JI.u / O
o
O
V)
I
1
CLOCK TIH£
OBSERVER LOCATIOK
Distance to Discharge
"Direction from Discharge
Height of Observation Point
BACKGROUND DESCRIPTION
WATHER CONDITIONS
Wind Direction
VJind Speed
Anblcnt Temperature
SKV CO«OITIONS
overcast, % clouds, etc.)
PLL'Kt DESCRIPTION
Color
Distance Visible
OTHER UIFOKuUIOll
Initial
•ifl1
-------
OBSERVATION' RECORD
,.wi. A \.
•
PAGE 1 OF J
C?
.
f— I
L--lT:c' '"' ;' J
TEST i.-j1'::,'. p.-.
PATE »-i / .'i 1 i i 'i
TYPE FACILITY
POI.'iT CF EH
.(0150
1!-.
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1
'
".In. T^
0 . c>
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2 TV
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(choc1'. If
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I'LU'.E
Pciiieho«I
CC'IHiHTS
OBSERVATION RECOilO
(Continued)"
iccArioM""""
TEST II'JKSCK
DATE
TYPE: FACILITY
POINT OF EK
PASS OF , _
tlr.
.
IMn.
30
31
-?
J3
.1-1
3'j
36
37
3H
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fi5
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50
',1
5?
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L4
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Sfi
57
sn
59
Seconds
0
li>
JO
•'.'j
STEAM PLU-'.£
'e'iccV K iipillcnblc)
Aiucico
ilrucncd
CO'iV.ENTS
1
[rn Dos.74-:eiso
i:-u-7-i.8:<} MS]
BIOSTE8, VOL 39, NO. 319—TUZS&AY, NOVLM3I2 12, 1974
-------
Plant //fart 7K£ '' o) 6vVx VERY IMPORTA'JT - FILL IN ALL BLANKS
Run No. •// ^/
Location {} '-/ & •'
/1 . I if- /<&-/•-?
Date y/^'/ • / / ^ . / / / , '
-///'/,}.<£
Operator — •/ /C. / A.' • -'s
Sample Bo
Meter Bos
Meter A 1
C Factor
x No. %""/
No. ,^
6^l«5y
^-ir'( 51
Pitot
in. H.O
AP
fl-Vi
C?.V
0- ^X
^7 «*
^-V~o
O.^c
<9.M
o -^-^
C'P '. -
<9 m
O Ml
o » L M
^,7.)
O '^-c
Read and record at the start of
each test point.
Time: SLafC Time C> ^ £ I
End Tiire O* 1 S VJ
Anbicnt Temp °F ft (.'
Bar. Press.
-Hg -?^ /'/
Assumed Moisture
2 &
Prcbc Tip Dia. In. /"^ /•/'/
Pitot Tube !!o.
.-• '
> •'
Probe Lengtli/cype •*" /
Filter No. 7 , ,
U,uc.U,l.
Orifice AH
in H20
1
Desired ' Actual
rf ?,? 0 r;"'
,"i ") '"• O."'/:-
<:r °l 1. 1 r> Id,
j.o?. Mo
tf oS o ^
0./,| 0.(. |
O Tr c? "/V
O • 6 ( ^5 6(
o • ^ •.' i ii^;«j
Ml M^
l-l^l l-IS
/ /O 1 1 10
I 1 o \ 1 1 '-'
o-'r? | £>--n
0 2b C-^4
c" jr11 n ^ or
Dry Gas Temp.
"F
Outlet
Is
1^
11
11
1L
14,
Tl
11
So
Si
^\
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^3
>j'-X
Inlet
"/'•/
"7/0
1^
l°l
1^>
li
1C7
T> .1
O -^
u 1
v^
^(-,
f/G
0 v^
Puirp
Vacuum
In. !Ig
^ !>"
n b"
3 o
2.-c;
S-O
3 • o
:- o
"5 c'>
•? o
i o
3'0
"5 , J
'•v . ;.
?,-o
.i 0
)1 C Cv
Temp.
"F
in ,
}r, 1
13 S
17'U
P)
1SC^
Ji £ 1
MS
ir
1/6
) 1 o
i i ^
I2l
;3 1
I«?G
v>
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.^'/.
.?n
^"/ ^
3 ")S
?14
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;jt:v
lV 'j
^5 !
;PU 4
(5 <4 ^
.7s:<
5^'L
y^'i
'T ^" ^
Probe
Tenp.
°F
y^T
:^'-l
:^r-.
u.1 i " 1
31,*
;.cc
.^ '^ci
u\
y/- ••>
^C4
^i-4
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"h:c
^^
>5^.
Stack
Terrp.
°F
171
ni
1^4
I'.l
rn
ns
Hi
ns
ns
n\
n^
115
i -\_~:
113
Jl*i
Stack
Ten-?.
°F
("F+460)
L> '••> f
C3?
(^i/ i/
6-^*7
i-y i
b^y _
l*&5
^•%c/
Lf$<
L3f
6,5-3
L-&5
G'W .
^.••^ .^ ^-^
I /* ^«^ i/
/ li at* ,5' SOI 0-6^ tf-t-'ft 6i o « 30 13 <. c?SH c^, /<>o GVL,
Consients:
-------
Sheet ^ of •>
0 H ° •>-
Point
1
Clock
Dry Gas
Meter, <
Pitot
in. H90
AP ~
Orifice /
in H90
Desired
(j '• ''o
1-00
Actual
c"; -
Dry Gas Temp.
Outle
Inlet
Pump
Vacuum
In. Hg
Inpinger
Temp.
Oven
Temp.
OF
Probe
Temp.
°F
Stack
Temp .
Stack
L
f'>
c
(a
0 -'
(5 Y,1
//*
I'aS
Ui i
OS?". 61
1-0?:
5 o
. 1 3
o '1*5
"i o
(* Co
o.
fj
oo
OP
3 0
IJLt
) - 00
J CO
I o
(6
M
0-
V\
• & C
0
6 1t
SI
i-c
60
6
I 10
Si
5-u
!?»
0 • SM.
S
0 '
(0
Comments:
3/16/77
)QQ. l*|
0-ft
16 1. M
O . '-1
vi
136
IT]
/AC
It
0
1 - 10
-------
OC./09
Sheet
of S
Point
Clock
Dry Gas
Meter, CF
Pitot
in. H00
AP '
Orifice AH
in H00
Desired
Actual
Dry Gas Temp.
°F
Outlet
Inlet
Pxinp
Vacuum
In. Hg
Impinger
Tenp .
Oven
Temp.
Probe
Tenp
°F
Stack
Tenp .
°F
Stack
Tero.
°F
1
0- t
. lo
c>
;? s
00
c
o
I?
0
O
1 iX
c
/o
77
s
P "/
M
/o
qo
/ 60
/ 6,?
S-o
/il
ir/q
\ Go
u
N
o
3 -o
.3
;
s
!?>.'!
O
Sc,
2-0
r
.-0
J
667
6
0 60
o
1- So
1 60
1)
R.
6 • -°
3-
6
.; -5
6 ^-'
i-- ^
\ ^6, 1)
":> 'O
-
/ <;
6
5
0
-13
; • o
H
0
f \
?, 0
Comments :
5
-------
SAMPLE CLLAHUP SHEET
Plant:
7<,*+ J/..-,
Address: X-->, //..v, //^
Operators: '
Stati on No . : o y c ^ :
Run No.: *-f
Barometric Pressure: 3$'*?fi
Impinger 1
Final Volume /c <^
Initial Volume /&<:>
Volume collected «
Impinqer 2
Final Volume f*5~
Initial Volume y o o
Ambient Temperature: f'Z"
Sample Box Number: /
ml of /)/$/• /I? J ^c
ml
ml
ml of £•£?•'&<* /6 O
ml
Volume collected — S' ml
Impinger 3
Final Volume c
Initial Volume
Volume collected_
Impinger
Final Volume
c-
Initial Volume
Volume collected_
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Initial weight
Weight collected ji/ .
Total Volume Collected 9:
Fi1ters
No.
Final Weight
gm
gm
ml of
'4-
_
ml
of
_
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.ml
m of
_gm
_gm
ml
Tare Weight
Weight
Collected
_gm
gm
gm
Cleanup performed by
on
-------
n
n
0
RECORD OF VISUAL DETOMIKATIOK OF OPACITY
PAG" / of/
•''•"' / LLL^-^
COMPANY ^-t*x=*?=, ^-^
LOCATION .-'^'<-C^ ; 6'\ .
TEST KuflBcRV^"/ ' C'/C'>
DATE '• i-//;^/? '~7
TYPE FACILITY' 17^1 '*-*.*!(
CO.'llROL DEVICE tf/\c.hrrt-S
HOURS OF OBSERVATION 1A/
OBSERVER ^r^'^< *••*' .
OBSERVER CERTIFICATION DATE
OBSERVER AFFILIAT1CII L'. S~ (=". rt <" •
POIIJT OF EMISSIONS
•O
V
CLOCK TIME
OBSERVER LOCATION
Distance to Discharge
Direction from Discharge
Height of Observation Po^nt
BACKGWUNO DESCRIPTIOf!
' 7,-ER CONDITION'S
Kind Direction
Wind Speed
Ar.bicnt Tenpcrature
SKY CONDITIONS (clear,
overcast, % clouds, etc.)
PLUM? DESCRIPTION
Color
Distance Visible
OTIICK IHFOK1AT10II
Initial
Final
OF AVERAGE OPACITY
Set
Number
Start-End
OozcUy
Readings ranged fron
to
2 cpaciiy
The source VMS/was not in ccnpli:ncc with t-
the tiir.c evaluation was race.
-------
CCiV?A\f "/•'
LCl^TIC1.1"^:
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PAfE -/', - /->-,
OBSERVATION1 RECORD PAGE I OF/
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TEST NUMBER
DATE '
OBSERVATION RECORD
(Continued)
OBSERVE*
TYPE
P011IT OF
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Mr.
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30
31
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CO-J'.ENTS
DOJ.7-V-261JO
11-11-74,8:4: US]
VOl. 37, KO. 219—.TUSSDAY, NOVmBtR 13, 1974
-------
2LD
Plant I I iC^g \
VERY IJIPORTAMT - FILL IN ALL BLANKS Ambient Temp "F ££"
Run No
•ii C
. " •=>
Location CM
Date
Operator_
Read and record at the start of
each test point.
Time: Start Time_
End Time
Bar. Press. "Hg 3 5
Assuncd Moisture 7._
Probe Tip Dia. In._
Pitot Tube No. •!
-?«/. |.50
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/£,
0--3>6
o-H
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«£
w. b
Point
Clock
Dry Gas
Meter, CF
Pitot
in. H20
AP
Orifice AH
in H20
Desired
Actual
Dry Gas Temp.
Outlet
Inlet
Pump
Vacuum
In . Kg
Impinger
Tenp.
Oven
Tenp.
°F
Probe
Temp .
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Stack
Tenp.
°F
Stack
Te:rp.
0 1-1
1
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3/16/77
o
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of
Comments:
3/16/77
-------
SAMPLE CLEANUP SHEET
Plant: //"'"•'• -/,£/,< J^.- /
Address: >V-_,^. .. <^-
' c:- Hate: -/'^/' '
Operators: ?)^'_.,(i
Station No'.: X^--? ' ''
Run Mo. : >*• S"~"
Barometric Pressure: '2 f y"/
Ambient Temperature:
Sample Box. Number: /
Impinqor I
Final Volume *y 3
Initial Volume /^o
Volume collected - V
Impinqer 2
Final Volume 9?
Initial Volume /co
Volume collected ~~ /
Impinoer 3
Final Volume
Initial Volume ^Vt/'/'i c
Volume collected '
Impinqer .
Final VolumeX^
Initial Volume ^-v^
Volume collected "\.
Impincer
Final weight ~^'-^~^' *J
Initial v;eight ^^'^ 0
Weight collected , /
Total Volume Collected -S 3-
Filters
No. Final Weight
/£' gm
gm
Cleanup performed by // /c2^
/ * ' / '
ml of ^>-*/' 'fa"' /'; -'
ml
ml
ml of /?, '-/' '-^J /-£ -'
ml
ml
ml of
ml
ml
ml of
ml
ml
gm of S •' '' c-^ Co'< /
gm
gm
ml
Weight
Tare Weight Collected
gm gm
qm gm
// *
'-' J^r^ on ///'''•'/ A^ /9~S
-------
RECORD OF VISUAL DETOM1M7IOK OF OPACITY
PAGZ
o
COMPANY1
LOCATION
TEST NUXCER.
DATE
TYPE FACIL1TY_
CONTROL DEVICE
HOURS Or OBSERVATION.
03SERYER
ii LVJE
OBSERVER AFFILIATION
POINT OF EMISSIONS
HEIGHT OF DISCHARGE FOI.TT
o
M
o
o
m
01
TIME
OBSERVER LOCATION
Distance to Discharge '
Direction from Discharge
Height of Observation Point
BACKGROUND DESCRIPTION
VEATHER CONOITIOHS
Kind Direction
Vlind Speed
Arsbicnt Temperature
•SKY CONDITIONS (dear,
overcast, 2 clouds, etc.)
PLL'Kc DESCRIPTIOK
Color
Distance Visible
1NFOOTIOII
Initial
•
'
•
•
•
Fir.al
!.
I
1
1
SUWttRY OF AVERAGE OPACITY
Set
Number
leadings r
'he source
the tir.c <
T'.r*
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•anged from to £ o?:c
» was/was not in ccnplicncs wit
:vd1uat1or. was rrac'c.
/•/erase
iiy
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-------
OBSERVATION RECORD
PAGE
L*J.
PATE
TYPE FACILITY
POL'iT CF
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•
OBSERVATION RECORD
(Continued)
PAGE OF
COMPAVY
7CST W.W3ER
DATE _
OBSERVES __
TYPE rACILlTY
POINT OF
llr.
IMn.
10
Jl
i?
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ALIlcMCil
id- 1 .cited
CO-WTS
005.74-201:
n-ii-7*;u:'.j
KOESAt RSOISTC?, VOL 39, NO. 219-.TUESSAY, NOVH?A3EB 12, 1974
-------
:LD
Plant
VERY IMPORTANT - FILL IN ALL BLANKS
Ambient Tc-np "F
o
^ 1 ,
Run No. **•/ -i si' ." i&Z
*
(,ut\. <-/ r;
/Tc' Ij C, (i H
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Operator
Sample Bo
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C Factor
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x No. (
NO. :z
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7,
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73 -f
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in. H20
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each test point.
Time: Stare Tine
End Time
Bar. Press.
"»g *j. y ^ri
Assumed Moisture
7. ¥
Probe Tip Dia. In. , .? / ^
Pitot Tube No.
7- /
Probe Lencth/cype . '•' j
Orifice AH
in H20
Desired
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——^
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Actual
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.
Comncnto:
-------
SAMPLE CLEANUP SHEET
Plant: /V //. „ ,< /» /
Address: 7 '•..-./..> // , , L..
Station No.: o LLx^ -*<^ty
Run No.: xz^j1' ^HX"1'"
Barometric Pressure: 3.*. ~ih
Impinger 1
Final Volume \f>o
Initial Volume 1 1?,.
Volusne collected 6
Impinger 2
Final Volume c/ 1 • 5
Initial Volume 1 t> o
Volume collected —
-------
0
U
0 C
0
A
Plant
Run No.
• :UL/< ELD
VERY IMPORTANT - FILL IN ALL BLANKS
Read and record at the start of
each test point.
Ambient Temp "F
Bar. Press. "Hg_
A' '7/0
Location
a
Date St.**. S /J /I* ' '/*
Tire: Start Time
Operator_
End Time O> \
Assu-ned Moisture Z_
Probe Tip DJa. In.
Pitot Tube No. d ~~ /
I
Sanple Box No
Meter Box No. ^L.
Meter o H / & ^
C Factor
Probe Lcngth/type_
Filter No.
L
C
C t.
O*
L^\C'
Point
/I
Clock
^L
in
U
Dry Gas
Meter, CF
U
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Pitot
in. H-
AP
0
0 •'Co
6
Q.^lg
^ . fto
0
o
Orifice AH
in H0
Desired Actual
1-15
Lol
a?*l
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C- o
6
1.35
/•go
Jo
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Lcl
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5-0
3-o
S'O
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"F
l-o
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5 -o
li
16
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All
TIC
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135
7)!
Stack
Te--?.
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("F+460)
-* ' A
4-7?
Consents:
-------
Sheet JL of
Point
-
Clock
Dry Gas
Me
Pitot
in. H-0
AT* ^
Ui.
Orifice
in H.,C
Desired
Actual
Dry Gas Temp.
°F
Outlet
Inlet
Punp
Vacuum
Kg
i.o
Iinpinger
Temp.
op-
Oven
Tcnp
Of
10
Probe
Te^.p .
OTT
Stack
Temp .
OT?
Stack
Tec?.
°F
(°F+460)
0- 1
M.
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1
C'- C,
c- s
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67
II
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bneet
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C-7
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C
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0-6^
0
0 "IS
CD
Orifice AH
in H00
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1-
). lo
Actual
1-1,0
I lo
Dry Gas Temp.
Outlet
70
"It
11
1!
Inlet
"U
11
16
Pump
Vacuum
In. Hg
2-0
a o
-o
a-
a . o
Impinger
Temp.
CF
lo
Oven
Tes?
Probe
Temp.
°F
341
Stack
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°F
S tack
Teir.p.
n «
(°F+450)
574
6*-
57
1 10
MO
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r- 1
F-t
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6 -
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I -
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13
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f- i
Connients:
3/16/77
0-10
. 10
-35
c'-V
l.lfl
15
2-0
346
-51
iM :
2-c
3 MM
• J?
*T
3 -o
17,6
/|C-
-------
SAMPLE CLEANUP SHEET
Plant:
Address:__ 'TT-'-^o/ ••
Station No.: 'G'Sc.
Run No.: -^ /
,.,^^fe*
Barometric Pressure:
Operators:
_Ambient Temperature: --_.
on
-------
1
n
O
TEST KUKEER
DAT E
/ X
TYPE FAcllTY
CO-'HROL DEVICE <
RECORD OF VISUAL DETOfllKATIOK Or OPACITY
PAGc / o? /
HOURS OF OBSERVATION ^
OBSERVER S^s? Xvc ^-
lRVtP. CERTIFICATION LVJE
OBSERVER AFF IL IAT1C" ^
POIIJT OF 'EMISSIONS ^ xl
HEIGHT OF DISCHARGE FOI.NT
"u
.-°
O
r
O
.5
O
'^ TIMS
OBSERVER LOCATION
Distance to Discharge
Direction from Discharge
Height of Observation Point
BACKGROUND DESCRIPTION
KATHER CONDITIONS
Wind Direction
Wind Speed
Anbicnt Temperature
SKY CONDITION'S (dear,
overcast, % clouds, etc.)
PLL'KE DESCRIPTION
Color
Distance Visible
OTIIta IIJFOKIUIOII
Initial
Final
SUWWRY OF AVERAGE CPACIT/
Sot
Number
Start-End
OsscUy
S-JT
Readings ranged from
to
opacity
The source VMS/was not in compliance, with mm
the time evaluation was race.
-------
OBSERVATION RECORD
PAGE 7^ OF/^
LCI'- ''ill r:
TEST KVElTr
C/Jt ^xf Jx
OBSERVES
TYPE F/'ClLitY xT7>
POl.'lT CF £.'-!lSSTi^r
IV.
",'.n.
^erpnri
C
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CC:i".EHTS
OBSERVATION RECORD
(Continued) '
PASS OF
COWA'JY
LOCATION
TEST Uir.S
DATE .
03SCRVE3
TYPE FACILITY
POltlT OF CKISSIG.'S"
Mr.
,
Kin.
30
31
•J?
,1
.U
3'j
V,
.17
J(l
'H
1U
•i 1
1Z
0
-------
Plant
Run No.
Location
Date ^
Operator
p; LA :D i
VERY IMPORTANT - FILL IN ALL BLANKS
Read and record at the start of
each test point.
Time: Start Time_
End Tiu-e
Aaibient Temp *F_
Bar. Press. "HB 3 ^ . ~1 0
Assuned Moisture 7. O
Probe Tip Dla. In. 0 • 3 I
Pltot Tube No.
Sample Box No.
Meter Box No._
Meter A H
C Factor
Probe Lenp.ch/type
Filter No. *-[
Point
L
Clock
Dry Gas
Meter, CF
^0*4.0 1
Pitot
in. H.O
AP
Orifice AH
in H20
Desired Actual
1.15
1
Dry Gas Temp.
"F
Outlet Inlet
Punp
Vacuun
In. Hg
3
Inpingcr
Ten?.
"F
Tero
"F
Probe
Tcrp.
°F
Stack.
Terp.
°F
H6
Stack
Te-1?.
•F
("F-^60)
r-s
lo
3L
751
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153
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157
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Conr.cn ts :
-------
bneet
of
Point
Clock
Dry Gas
Meter, CF
Pitot
in. H-O
Orifice AH
in H20
Desired
Actual
Dry Gas Temp.
°F
Outlet
Inlet
Pump
Vacuum
In. HE
Icpinger
Tenp.
°F
Oven
Te.ro ,
"
Probe
Stack
Tercp .
'
Stack
Teirp.
°F
l-lo
l-lo
I7S
b-i
0 -10
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1 -00
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top
C-
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C-2
li.
Comments:
3/16/77
MS
M5
3.V-
1 6
O O
si
11
\U
\. \ 0
Mo
65
-( e- ^ 6 ') i s1 /
6,26,
-------
Sheet ?x of
Point
Clock
Dry Gas
Meter, CF
5
Pitot
in. H00
AP fc
Orifice AH
in H00
Desired
Actual
1 Do
Dry Gas Temp.
°F
Outlet
Inlet
Pump
Vacuum
In. Hg
Iipinger
Temp.
°F
Oven
Tenp
s
34H
Probe
Tenp .
SF
Stack
Tena.
Stack
Terp.
fW.
I
S'MI
) .
30
1 Jo
<**
IS
0
o-lo
l-lo
IS
IV
fo
U
-o
A- \
Consents:
3/16/77
-------
SAMPLE CLCAf.'UP SI I LET
Plant: ^^^-^^ . -ifc>
Address: xr— ^^ "•»"'•<-.., *•
Station NoT: CYC? ''
Run No.: ^-^
BaroneLric Pressure: 3. F,'*>r>
Date: '//s>J->'?
Operators: ^ '
*
Ambient Temperature: s' ','"
Sample Box Number: /
Impinger 1
Final Volume ^,
Initial Volume xo
Impinqer 2
Final Volume /a?
Initial Volume /oo
Volume collected _ /'
Impinger 3 \
Final Volume\
Initial VolumX
Volume collected
Impinqer
Final Volume - ^
Initial Volume d'^
Volume collected o
Impiniier
Final weight *?&? &
Initial v/eight ^/L-^CJ
Height collected ;~> <^>
Total Volume Collected / ->j "r?*"/r
of
/" «-^"
of r^--.- -r^^-
Weight
Tare Weight Collected
gm gm
gm gm
Cleanup performed by
on
-------
Cl
^
COMPAKY^^y-^-Z*-.
LOCATION
TEST NUMBER
DATE
RECORD Or VISUAL DETOSUMTIOK OF OPACITY FAG" / cf /
HOURS OF OBSERVATION x£
o .-
TYPE FACILITY x^/
COHTROL DEVICE .,/-
OBSERVER
OBSERVER CERTIFICATION DATE
OBSERVER AFFILIATIC.'I L',~/*'r9.~1
POINT OF EHISS
HEIGHT OF DISCl'ARGi FOII1T
o
Z
O
r
>
s
CLOCK TIME
OBSERVER LOCATION
Distance to Discharga
Direction from Discharge
Height of Observation Point
BACKGROUND DESCRIPTION
LEATHER CONDITIONS
Kind Direction
Vlind Speed
Ambient Temperature
SKY CONDITIONS (clear,
overcast, % clouds, etc.)
PLL'Ks DESCRIPTION
Color
Distance Visible
OTliCH
Initial
Y*.S>
^
t^fl
'•£.•.?"/
2
y-f /}
7?.-'
r£^
'V*'- y
S I
Av /T
Final
I
1
1
SlTCttRY OF AVERAGE OPACITY
Set
Mur.be r
leadings r
'he sourc!
the time (
Tlr-n
Start—End
Cssclty
_....^, . , .
' 1
I
•anged fro.n to % cp;c
j VMS/was not in ccr.pl io^cc wit
jvdlu'alion VMS race,
iiy
h ..&t
-------
Plant
:uu ELD
VERY IMPORTANT - FILL IN ALL BLANKS
Run No.
Read and record at the start of
each test point.
Anbient Temp °
Bar. Press. "H
Location ?lr~^/> F . /T?
Bate V/V ~/~ ~'' //'
C»-i~t- T-f mn
End Time
)6
Assumed Moisture 7. O
"i ~7 ' <~
Prnhe Tip Dia. In.«- * - " / -*
Pitot Tube No. f~ /
Sample Box No.
Keter Box No._
Keter A H
C Factor
{_
Probe Lenp.th/type
Filter No.
/./?
*/. ^
Point
// f
Clock
12
Dry Gas
ieter, CF
.<»V 7 ^
Pitot
in. H,0
A?
o -
o. SS
Orifice fill
in H20
Desired Actual
I-3S
106'
1 .
6 Ij
-06.
r.
Dry Gas Te:rp.
°F
Outlet Inlet
Pum|/
Vacuun
In. Hg
•«>
i -o
Impinge r
Tenp.
"F
"*>
•
Oven
Teirp.
"F
/; (,
Tcnp .
°F
=?-;/.,
P
Terp.
"F
15S
K-i
U
Stack
, L-^C-
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IS ;. K
c
u
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3-6
135 -3S
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6 •
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GtT-
-/
(fonncnco ;
-------
Sheet
of
Point
Clock
Dry Gas
Meter, <
Pitot
in. H.,0
AP -
Orifice AH
in H20
Desired
Actual
Dry Gas Temp.
Outlet
Inlet
Pump
Vacuum
In. Hg
Inpinger
Ten?.
Oven
Tenp
Probe
Temp.
°F
Stack
Tenn =
°F
e- 1
6-7
1-0
S
lo
l-\o
t I
l.c
2 SI
c-d
"S-6
;.*
? 0
.76 r
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c
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3
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3.0
-?.£•:?
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60 |
M
0
0
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% 1.
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J
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Comments:
3/16/77
0
J
-------
Sheet S of
Point
Clock
Dry Gas
Meter, CF
Pitot
in. H?0
AP "
Orifice AH
in H90
Desired
Actual
Dry Gas Temp.
Outlet
Inlet
Pump
Vacuum
In. Hg
Impinger
Tenn .
"
. r«
£••' '5
Oven
leap.
°F
Probe
Tesp.
°F
Stack
Terp.
°F
I- 10
Hi
r- 7
Mo
lie
L
1 o ,
O • 1 0
o .
13
S -r-
<-!('.
1
). to
lo
o
1.1?
). 16
3 o
o
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Mo
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C
\\
a Go
2 .5
H
4
c/-x
MJ-
3 6
/o
-/ o
s
3
••/
/'-''/
Co events:
3/16/77
o
16
I Jto
3
\-.lo
76
/r/
/\?£<6S
' & 0
-------
SAMPLE CLEANUP SHEET
Plant:
Da Le :
Address: 7?...; ..> ^'L^-.^.-
Station No. : ' c'-^c • '
Run No. : *?3
Baromc-tric Pressure: jj-.'^c
Operators: '
i
Ambient Temperature: _j> *<•/--
Sample Box Number: /
i
Impinqer 1
Fi nal Volume
Initial Volume
Volume collected
Impincjer 2
Final Volume
Initial Volume
Volume collected
Impinqer 3
Final Volume
Initial Volume
Volume collected
Impincier
/so
r
_ml of
jnl
ml
_ml of
_ml
ml
jnl of_
jnl
ml
Final Vtnume
Initial VoSoime
Volume col levied
Impinqer
Final weight_
Weight collected
Total Volume Collected_
Filters
No.
Final I/eight
jnl of_
jnl
ml
Of
Initial weight /: £ :. o qm
c._gm
ml
Tare Height
Weight
Collected
gm
gm
gm
gm
gm
gm
Cleanup performed by
/LtL^z
/
-------
n
o
RECOR3 OF yiStW, DETERMINATION Of OPACITY
HOURS 0? OBSERVATION
LOCATION
TEST NUMBER
DATE
TYPE FAC1LITY__
CO.'HROL DEVICE
OBSERVER
03SERVEP. CEB.TIFICATIO.X LVJE
OBSERVER AFF ILIATIC!.' £S ^
POINT OF EMISSIONS X^-X'f
HEIGHT OF DISCIWRG; FO'l.'iT
O
I
\
CLOCK TIME
OBSERVER LOCATION
Distance to Discharge
Direction from Dfscfiarge
Hclfjht of Observation Point
BACKGROUND DESCRIPTION
LEATHER CONDITIONS
Wind Direction
VMnd Speed
Anblcnt Temperature
SKY COIJOITIONS (clear,
overcast, % clouds, ctc.y
PLUME DESCRIPTION
Color
Distance Visible
OTHER IKFOOTIOII
Initial
Final
OF AVERAGE OPACITY
Set
Number
T',^
Start— End
Co;c1
Sun
ty
/vorcgs
^
_
Readings ranged from
to
The source VMS/was rot In ccnpUs.ncs with
the time evaluation VMS race.
-------
AST V'".:
OBSERVATION RECCttD PAGE / .OF/
LciATitrT
TEST .'..•'.;'.* _-j-_?—
CAT: >" y. -•
OOSERVrR X - «-'*'-' ""•" " "
TV;'! FACitTfy ;_'••(. — *•"'
FOI'iT Cr E-'ilSSTliiTT/-. •>. r~
r
= >'-
".In.
0 1/3
f } \'°
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^
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7
r
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IS
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5-1 •!-
ar~
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—
•*
i
•LU.'.E
t
COMMENTS
•*^~ ,. ^_ * ^
OBSERVATION RECORD
(Continued)
COM?A','y
Loc/ifioM"^
TCST liUXSEK
DATE
a
TYPE r/.ciLi'TY
ponir o
£?.A9/6,
PACE Or_
fc-
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•
Kl
5?
SJ
fi
55
56
57
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59
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