74-GAS -I
(REPORT NUMBER)
AIR POLLUTION EMISSION TEST
GASOLINE TRANSFER
(PLANT NAME)
VAPOR RECOVERY SYSTEMS
SAN DIEGO COUNTY
(PLANT ADDRESS)
CALIFORNIA
U. S. ENVIRONMENTAL PROTECTION AGENCY
Office of Air and Water Programs
Office of Air Quality Planning and Standards
Emission Standards and Engineering Division
Emission Measurement Branch
Research Triangle Park, N. C. 27711
-------
TEST EVALUATION
OF
GASOLINE TRANSFER
VAPOR RECOVERY SYSTEMS
D.E. Hasselmann
TRW, Inc.
Transportation and Environmental Operations
One Space Park, Redondo Beach, California 90278
Contract 68-02-0235
November 1974
Prepared for:
Emission Measurements Branch
Office of Air Quality Planning and Standards
Environmental Protection Agency
Research Triangle Park, North Carolina 27711
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DISCLAIMER PAGES
ACKNOWLEDGEMENT
1.0 INTRODUCTION 1-1
2.0 SUMMARY & DISCUSSION OF RESULTS 2-1
2.1 TEST SEQUENCE 2-1
2.2 STATION DATA 2-2
2.3 BULK DROP DATA 2-2
2.3.1 Environics System 2-3
2.3.2 Intermark System 2-3
2.3.3 Process Products System 2-3
2.3.4 Gulf Balanced System 2-4
2.3.5 Standard Balanced System 2-6
2.3.6 Performance Efficiencies 2-6
2.4 VEHICLE REFUELING DATA 2-8
2.4.1 Baseline Vehicles 2-8
2.4.2 Environics System 2-10
2.4.3 Intermark System 2-14
2.4.4 Process Products System 2-14
2.4.5 Gulf Balanced System 2-15
2.4.6 Standard Balanced System 2-15
2.4.7 Explosimeter Readings 2-23
2.4.8 Fill Rates 2-23
2.4.9 Test Time 2-23
2.4.10 Spitback 2-25
2.5 PROCESSING UNIT PERFORMANCE 2-25
2.5.1 Environics System 2-25
2.5.2 Intermark System 2-25
2.5.3 Process Products System 2-29
2.6 OVERALL SYSTEM EFFICIENCIES 2-29
2.7 RVP ANALYSIS 2-34
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PAGES
2.8 MOLECULAR WEIGHT ANALYSIS 2-38
2.9 PROBLEMS ENCOUNTERED 2-38
2.9.1 Environics 2-38
2.9.2 Intermark 2-38
2.9.3 Process Products 2-39
2.9.4 Gulf Balanced 2-40
2.9.5 Standard Balanced 2-40
3.0 PROCESS DESCRIPTION . 3-1
3.1 ENVIRONICS 3-1
3.2 INTERMARK 3-3
3.3 PROCESS PRODUCTS 3-5
3.4 GULF OIL BALANCED 3-7
3.5 STANDARD OIL BALANCED 3-7
3.6 VEHICLE SAMPLING LOCATIONS 3-7
4.0 SAMPLING METHODS 4-1
4.1 EQUIPMENT 4-1
4.1.1 Hydrocarbon Concentrations 4-1
4.1.2 Pressure 4-4
4.1.3 Temperature 4-4
4.1.4 Volume 4-4
APPENDIX
APPENDIX A - Daily Station Data
APPENDIX B - Bulk Drop Data
APPENDIX C - Vehicle Refueling Data
APPENDIX D - Laboratory RVP Analysis
APPENDIX E - Sample Data Sheets
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TABLE LISTING PAGES
1-1 System Locations 1-1
2-1 Test Sequence 2-1
2-2 Bulk Drop Data 2-7
2-3 Vapor Return Ratio 2-9
2-4 Baseline Vehicles 2-11
2-5 High Return Volume Reading of Cars 2-19
2-6 Explosimeter Reading During Dispensing 2-24
2-7 Fill Rates 2-24
2-8 Fill Rate Data 2-26
2-9 Environics Processing Unit 2-27
2-10 Overall System Efficiency Calculation Method 2-31
2-11 Overall System Efficiencies 2-33
2-12 Product RVP Analysis 2-35
2-13 Vehicle RVP Analysis 2-36
4-1 Major Equipment List 4-2
FIGURE LISTING
2.1 Directional Flow Valve 2-5
2.2 Baseline Vehicle Data 2-12
2.3 Baseline Vehicle Data 2-13
2.4 Returned Vapor Ratios - Gulf 6/12 2-16
2.5 Returned Vapor Ratios - Gulf 6/13 2-17
2.6 Returned Vapor Ratios - Gulf 6/14 2-18
2.7 Returned Vapor Ratios - Standard 6/17 2"20
2.8 Returned Vapor Ratios - Standard 6/18 2-21
2.9 Returned Vapor Ratios - Standard 6/19 2-22
2.10 Intermark Flow Balance 2-28
2.11 Process Products Flow Balance 2-30
2.12 Distribution of Vehicle RVP ' 2-37
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FIGURE LISTING (Continued) PAGES
3.1 Environics System 3-2
3.2 Intermark System 3-4
3.3 Process Products System 3-6
3.4 Gulf Oil Co. Balanced System 3-8
3.5 Standard Oil Balanced System 3-9
3.6 Vehicle Sampling Locations 3-10
4.1 Hydrocarbon Analyzer Calibration 4-3
4.2 Polyethylene Bag Volume 4-5
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ACKNOWLEDGEMENT
The support and help provided by Mr. D. Nielsen and other personnel
from the San Diego County Health Care Agency is greatly appreciated. In
addition, Mr. P. Rosenbloom, TRW, developed and ran the computerized data
reduction program for analyzing the results of this program.
This program was funded by the Environmental Protection Agency under
Contract No. 68-02-0235, Task Order #19.
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1.0 INTRODUCTION
This report describes the results from tests of systems for collecting
hydrocarbon vapors at automobile filling stations. These tests were con-
ducted by TRW Environmental Services under sponsorship from EPA with support
from San Diego County. The purpose of these tests was to develop test pro-
cedures for determining gasoline vapor emissions during transfer operations at
service stations and to use these methods to evaluate five different vapor re-
covery systems.
Two balanced and three secondary vapor recovery systems were tested. The
balanced systems were designed to return the vapors via simple piping to the
underground tank. Pressure differentials created by liquid displacement from
the underground tank into the vehicle tank provided the driving forces. The
two balance systems differed in that one configuration had separate manifolds
for each grade of product while the other system had all three product grades
manifolded together.
The secondary systems had vacuum blowers for collecting the vapors from
the vehicle tank with subsequent processing of the excess vapors. Processing
by the secondary units tested was done by incineration or refrigeration/con-
densation.
The location of these systems in San Diego, California is shown in Table
SYSTEM
LOCATION
Erwironics, Inc.
Vapox 3000 (Incineration)
Intermark Industries, Inc.
Mark I
(Compressions-Refrigeration)
Process Products, Inc.
Vapor Savor 200
(Refrigeration-Carbon Adsorption)
Gulf Oil Balanced
(Multi-Product Manifold)
Standard Oil Balanced
(Single-Product Manifold)
Texaco Station
Baltimore & Fletcher Parkway
Chevron Station
Interstate "5" & Carmel Valley Rd
Tibbs Union
Waring and Zion Road
Gulf Station
University & Boundary
Chevron Station
Baltimore & Lake Murray Blvd.
Table 1-1 System Locations
1-1
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The measurements which were taken at these stations consisted primarily
of hydrocarbon concentration and volumes. The concentrations were measured as
total hydrocarbons by a flame ionization detector. The volumes were measured
by dry gas meters along with temperature and pressure measurements for standard-
ization purposes. These measurements were made in the return vapor line from
the fill nozzle, at the inlet and outlet of the secondary system processing
units, and at the underground tank vents of the balanced systems.
Over 400 cars were tested during a three-week period from 6 to 26 June,
1974. The team performing the tests consisted of the following members:
P. Westlin, EPA Project Officer
D. Hasselmann, TRW Project Manager
T. Eggleston, TRW Project Engineer
T. Hurst, TRW
J. McReynolds, TRW
W. Davis, TRW
R. Redmond, TRW
D. Savia, TRW
1-2
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2.0 SUMMARY AND DISCUSSION OF RESULTS
2.1 TEST SEQUENCE
The sequence of tests and the number of vehicles tested each day are shown
in Table 2-1.
DATE
6/6
6/7
6/10
6/11
6/12
6/13
6/14
6/17
6/18
6/19
6/20
6/21
6/24
6/25
6/26
SYSTEM
Inter-mark
Intermark
(STATION DELAY)
Process Products
Gulf Balanced
Gulf Balanced
Gulf Balanced
Standard Balanced
Standard Balanced
Standard Balanced
Environics
Environics
Process Products
Process Products
Intermark
TEST
Vehicle Refueling
Bulk Drop & Process Unit
-
Vehicle Refueling
Bulk Drop & Vehicle Refueling
Vehicle Refueling
Vehicle Refueling
Vehicle Refueling
Bulk Drop & Vehicle Refueling
Vehicle Refueling
Vehicle Refueling
Bulk Drop & Processing Unit
Vehicle Refueling
Processing Unit
Processing Unit
# OF VEHICLES
51
•-
_
25
30
62
75
29
18
35
54
-
21
-
-
Table 2-1. Test Sequence
2-1
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2.2 STATION DATA
The daily station data is shown in Appendix A. The parameters which
were recorded for each station were the morning, noon, and evening weather
conditions; the underground tank volumes and temperatures at the beginning
and end of each day; and the amount of fuel dispensed at each of the islands.
It should be noted that the volume of liquid dispensed at the island
may be different from the reading for the liquid taken out of the underground
tank. In all cases, the accurate measurement is that noted for the dispensers.
The underground tank volume was measured by a dip stick inserted through the
fill tube. If there was any pressure in the underground tank, as was the case
for some of the secondary recovery systems, the underground tank reading was
in error. This was due to the fact that the liquid level in the fill tube was
displaced proportional to the underground tank pressure.
The general weather conditions for the test period were fair and sunny
with daytime temperatures in the mid-80's. Evening temperatures dropped to
the low 70's.
2.3 BULK DROP DATA
The bulk terminal for the Standard Station was located on Harbor Drive
near the Coronado Bridge in downtown San Diego. The bulk facilities for
Union 76, Texaco, and Gulf were all located at Mission Valley near the Sports
Coliseum. The truck loading was generally performed in the morning, and
travel times from the bulk terminal to the station under test were approxi-
mately one-half to three-quarters of an hour. This resulted in bulk drops at
the station before noontime.
Data for each of the bulk drops is provided in the data sheets of
Appendix B. The filling of the tank trucks was observed at the bulk terminals.
The volume loaded into the tank truck was obtained from the certified meter
at the bulk station. Temperature readings were obtained from the dial ther-
mometers located in each of the product lines. Temperatures of the product
being loaded into the truck generally were around 72°F., and nominal loading
rates were 600 gpm. RVP samples, for the product being tested at the stations,
were obtained by taking a sample through a tap on the product lines at the
bulk terminal.
2-2
-------
The dome hatches on the tank trucks were monitored during bulk loading
by an explosimeter. The domes were generally tight; although, there was an
occasional leak as indicated on the data sheets. These leaks were generally
minor and consisted of occasional puffs on the sniffer.
2.3.1 Environics System
During the drop at the Texaco Station, a slight leak was observed at the
liquid fill to underground tank connection. This leak was not sufficient to
cause a flow of liquid but it did cause a reading on the explosimeter. A
slight leak was also observed at the vapor return line from the underground
tank causing an explosimeter reading around 0.6 L.E.L.
Both regular as well as premium gasoline were dropped at the same time.
2.3.2 Intermark System
The bulk drop at the Standard Station was made by dropping both premium
and regular gasoline at the same time. This station is temporarily restricted
by the APCD to single product drops because of the processing unit; however,
it was decided to drop both grades simultaneously for this test in order to
simulate normal operating conditions.
During loading of the truck at the bulk terminal it was noted that there
was a slight leak at the number 2 tank of the truck and number 1 and number 3
tanks of the trailer.
The pressure at the tank truck during bulk drop rose to 14.5 inches of
water at the start and then decreased to 11.5 inches of water at the end of
drop. The hookup lines were retained in place for approximately five minutes
at which time the tank pressure had dropped to 2.5 inches of water. This was
the same pressure as at the processing unit inlet line.
A few drops of fuel spilled during disconnecting of the liquid line. This
was difficult to avoid since the truck driver was required to lift the product
hoses above his head in order to drain out liquid remaining in the lines.
2.3.3 Process Products System
The OPW vent was noted to be leaking on the day prior to the bulk drop
A new valve was installed; however, it too had a small leak despite cleaning
of the diaphragm faces. A quantitative measurement could not be made; how-
ever, a plastic bag fitted over the vent indicated a leak rate between
2-3
-------
one-half to one cubic foot per hour.
The tank truck drop was made by simultaneous drop of the regular and the
premium gasoline. A leak was observed on the hose fitting at the underground
tank adaptor on the regular grade dispensing line. This leak caused air bub-
bles in the liquid which could be observed through the sight glass.
The premium product was loaded on the tank truck in San Diego. The regular
grade, however, was loaded in Los Angeles and had come down the previous morning.
The Union storage facilities were out of regular grade gasoline and Union in-
dicated they had been given approval to ship regular grade gasoline from Los
Angeles to fulfill the needs of the test program. As a result it was not pos-
sible to take an RVP sample during loading, and a sample was taken from the
submerged fill tube after the product was delivered.
The pressure in the test tank truck averaged around 3-4 inches of water
during the drop. At the end of the drop, the pressure remained at 1.5 inches
of water in the underground lines and in the tank truck.
During removal of the liquid dispensing line from the underground fitting
to the tank a significant spill of liquid occurred. The quantity of liquid
spilled was sufficient to fill up the manhole at the underground fitting.
2.3.4 Gulf Balanced System
Vents on the underground tank were manifolded together to a common outlet.
A Christmas tree arrangement, as shown in Figure 2.1, was placed on this common
outlet to allow inbreathing through one port and outbreathing through another
port. These ports were opened and closed by 3/4" diameter solenoid valves.
These solinoid valves were in turn activated by pressure/vacuum switches. The
switches are actuated at a pressure (or vacuum) of approximately 0.25 in. H20
and close when the pressure (or vacuum) has dropped to approximately 0.15 in.
HLO. Thus there is a dead band between the closing of one switch and the
opening of the other switch. The outbreathing vent was connected to a long
collapsed polyethyline bag during bulk drip and a carbon canister during over-
night periods.
The bag was used instead of a dry gas meter during bulk drop in order to
reduce back pressure on the vent lines. The inlet to the bag was monitored by
a flame-ionization detector for total hydrocarbon concentrations.
2-4
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SOLENOID
VALVES
IN-FLOW
METER
OUT-FLOW
METER
NEGATIVE PRESSURE
SWITCH
POSITIVE PRESSURE
SWITCH
ADAPTOR TO
VENT PIPE
Figure 2.1 DIRECTIONAL FLOW VALVE
CHRISTMAS TREE
2-5
-------
A slight leak was noted in the bag just prior to the bulk drop. This was
caused by chafing upon the rock roof of the station. The leak was patched prior
to the bulk drop and verified to have been sealed at the end of the bulk drop.
During the bulk drop a slight leak was noted on the explosimeter at the
two dome covers of the truck. No leaks were noted on the domes of the trailer.
Vehicle refueling was discontinued during the bulk drop and the islands
remained shut down for an hour and one-half after the bulk drop. The nozzles
at the islands were not bagged with polyethyline bags; however, all nozzles
were checked with an explosimeter during bulk drop, and while the underground
tanks were venting into the collection bag. No movement of the explosimeter
was noted during this check of each nozzle.
The underground tanks vented during the drop. As soon as the drop was
completed, the underground tanks started to breathe in. This inbreathing
occurred during the hour and one-half station shutdown and continued through-
out the afternoon. No outbreaking was noted during the afternoon following
the drop period. This suggested that vapor absorption was occurring in the
underground tank since the temperature differential was small between the
gasoline dropped and the gasoline already in the underground tank.
At the end of the next day a carbon canister was placed on the outlet
and monitored for the next two and one-half days. No change in carbon canister
weight was noted so that no hydrocarbon vapors appeared to have escaped.
2.3.5 Standard Balanced System
The bulk drop at the Standard Station was monitored by the same Christmas
tree arrangement mentioned above. A polyethylene bag was used to capture out-
flow during bulk drop. Dry gas meters were then connected to the inbreathing
and outbreathing solenoid valves to continue flow measurement after the drop.
The addition of the dry gas meter to the inbreathing line was done to measure
the effects noted at the Gulf Station.
The activated carbon canister was placed on the outbreathing solenoid
valve line during the overnight periods. No change in canister weight was
noted, and no hydrocarbon vapors appear to have been emitted.
2.3.6 Performance Efficiencies
The summary of all the bulk drops is shown in Table 2-2. The secondary
systems all had volume capture efficiencies greater than 99%. Two of the
systems' had a positive pressure in the underground lines which was transferred
to the tank truck.
2-6
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BULK DROP DATA
Secondary
Environi cs
Intermark
Process Products
Balanced
Gulf
Standard
Drop
(gal)
7800
8685
8800
8250
4665**
Volume
(ft3)
1043
1161
1180
1103
632.7
Vented
(ft3)
10.14
6
0*
26.3
23.8
Volume
Efficiency
(%)
99+
99+
100
97.6
96.2
Mass
Emission
(gm)
14.45
28.5
0
260
183
Unit
Mass
(gm/gal)
.002
.003
0
.03
.04
Final
Pressure
(in.H20)
0
2.5
1.5
0
0
ro
t
* The underground piping at this station had a leak which was discovered during
subsequent tests. Venting may occur after the leak is repaired.
** Standard Balanced represents a normal drop of approximately 4000 gallons into
each underground tank. Only the tested tank is indicated because the Standard
Station uses separate vapor lines for each grade of product. Other stations use
a manifold connecting the underground tanks.
Table 2-2. Bulk Drop Data
-------
The balanced systems vented slightly during the bulk drop, but maintained
a capture efficiency greater than 96%.
The dry gas meters recorded a 23.8 cu.ft. outflow of vapors for a 4665
gallon drop, and a subsequent inflow of 2.53 cu. ft. of air over 6 hours after
the drop.
2.4 VEHICLE REFUELING DATA
The data collected for each car during vehicle refueling is provided in
Appendix C. This data lists all of the reported and measured parameters for
each vehicle during the test program. The data for each car is shown on four
separate pages. The first two pages, Appendix Cl, Appendix C2, show the data
recorded and measured during the test program. The third page, Appendix C3,
shows the performance calculations from the collected data. The fourth page,
Appendix C4, shows the vapor collection ratios for each car compared to the
"baseline" curve.
The amount of vapor volume returned per volume of liquid dispensed (grams
per gallon) and the volume of vapor returned per volume of liquid dispensed
(cubic feet per cubic feet) is shown in Table 2-3. In order to relate these
values to .the vapors escaping when there is no vapor recovery, it was necessary
to develop a "baseline" vehicle curve. A "baseline" vehicle was to represent
the vapors emitted during vehicle refueling if no control devices were applied.
2.4.1 Baseline Vehicles
Previous tests have shown that a relationship can be established between
the liquid temperature differential and the returned vapor volume ratio. The
liquid temperature differential is the vehicle tank temperature minus the
dispensed liquid temperature. This temperature difference affects the
amount of the vapor in the empty vehicle tank which expands or contracts prior
to its emission from the tank.
To establish the "baseline" values for the test program, cars were tested
at both of the balanced stations. A "baseline" car was measured by requiring
the following three conditions:
. Blocking tank vent line with a pressure gauge
. Zero explosimeter reading during fill
. No leaks in vehicle tank during check after fill
2-8
-------
System
Environics
Intermark
Process Products
Gulf
Standard
Vapor Mass To
Liquid Volume
(Gm/Gal)
4.97
9.89
3.31
4.52
Avg. 3.91
2.43
2.48
2.02
Avg. 2.31
2.92
3.05
2.39
Avg. 2.78
Vapor Volume To
Liquid Volume
(Ft3/Ft3)
4.61
2.40
1.20
1.40
1.30
.57
.56
.43
.52
.63
.74
.59
.65
Table 2-3 Vapor Return Ratio
2-9
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The vehicle tank vent could be blocked satisfactorily only on post-1970
cars. This was done by disconnecting the carbon canister from the tank vent
line under the hood of the car and attaching a manometer. A force fit was then
established at the nozzle/gas tank interface, and a zero explosimeter had to
be maintained throughout the filling at this interface. Upon completion of
the fill, the vehicle tank was checked by pressurizing it with dry nitrogen to
three inches of water. This pressure had to be maintained with a dry nitrogen
flow of less than 10 ml/minute.
These baseline data were obtained only at the balanced stations where they
could not be influenced by any vacuum assisted devices. The vehicles which met
all three criteria were then used to determine a baseline curve. Six cars at
the Gulf Station and eight cars at the Standard Station met all of these criteria
and are listed in Table 2-4. Additional cars were tested, but were rejected
during data analysis because they had slight explosimeter readings, did not
have the canister line blocked, or failed to have some other data measured.
The results of these fourteen cars and the best fit curves are shown in
Figures 2.2 and 2.3. The coefficient of regression for these curves is good.
For the volume ratio, the regression coefficient was 87%, while for the mass
ratio it was 63%. The curve fit for the mass return was slightly poorer be-
cause it depended upon measurement of volume as well as concentration, while
the volume ratio only depended upon a single measurement. The baseline curves
shown in Figure 2.2 and 2.3 were then used to calculate the relative perfor-
mance of each vehicle in Appendix C4. The temperature differential for each
car was used to obtain its baseline value, and then the performance of the car
was compared to this baseline value.
2.4.2 Environics System
The Environics system used a modified OPW-7 nozzle with a sleeve extending
partially into the automobile tank. As a result of this modification, it did
not hang firmly onto the vehicle fillneck. On one occasion the nozzle was seen
to have been pushed out of the vehicle tank by spitback. The nozzle did not
shut off and several pints of gasoline were sprayed on to the station floor
before the nozzle could be shut off.
2-10
-------
License No.
205 JRT
236 KLM
105 HOT
603 GBY
312 HPO
680 GOC
918 KKL
932 HWN
XXX
574 KMK
545 HTC
405 JVC
603 GBY
438 JUA
Date
6/12
6/12
6/13
6/14
6/14
6/14
6/17
6/17
6/17
6/17
6/19
6/19
6/19
6/19
Station
Gulf
Gulf
Gulf
Gulf
Gulf
Gulf
Standard
Standard
Standard
Standard
Standard
Standard
Standard
Standard
Table 2-4 Baseline Vehicles
-------
Line Equation:' Ft3/Ft3 = 0.860 - 0.014AT
1.4-
X = Gulf
= Standard
-TO 0 TO 2'0 30 40
Vehicle Tank. Disp. Liquid Temperature (°F)
Figure 2.2 Baseline Vehicle Data
2-12
-------
Line Equation: Gm/Gal =3.601 - 0.043AT
X = Gulf
= Standard
-10 o 10 20 30
Vehicle Tank - Disp. Liquid Temperature (°F)
40
Figure 2.3 Baseline Vehicle Data
2-13
-------
The vacuum at the nozzle ranged from 20 to 25 inches of water, and was
the highest vacuum noted of all the vacuum assisted systems. The nozzle did
not provide a tight fit with the fillneck so that excess air quantities
probably were ingested through the gap.
The vacuum was started whenever one of the pumps at an island was turned
on. Thus, air was drawn throught the vapor return line after the dispensing
of liquid had stopped. The data for the returned vapor in the calculations of
Appendix C3 have been modified to account for this condition. The return vapor
shown in Appendix C3 were the vapors returned only during dispensing of liquid.
i
The readings on the hydrocarbon analyzer indicated that high vapor concentra-
tions only occurred while liquid was being dispensed. As soon as dispensing was
stopped, the hydrocarbon concentration dropped nearly to zero.
Due to the high vacuum, the unit returned a significant amount of volume.
Since excess air could be ingested around the nozzle to vehicle tank interface,
the actual concentration of hydrocarbons was not as high as would have been
for a tight fft.
2.4.3 Intermark System
The Intermark nozzle was a modified OPW nozzle with a rubber boot and a
magnetic seal at the vehicle tank interface. The return vapor line was actuated
by a mechanical valve attached to the nozzle. The vacuum measured at the nozzle
ranged from 10 to 15 inches of water. This value was found to be quite repre-
sentative of the remaining nozzles at the station. The vapor mass drawn back
by this system was quite high due to the tight fit between the rubber boot and
the vehicle tank. Only slight amounts of air could be ingested from the outside.
2.4.4 Process Products System
The Process Products nozzle was a modified OPW nozzle with a sleeve ex-
tending into the vehicle tank. In addition, a rubber boot was provided to
enclose the gap between the nozzle handle and the vehicle tank. This boot was
not connected to the vapor return line, but acted simply to catch any spitback.
The spitback was supposed to drain back into the vehicle tank; however, a
slight amount of liquid remained entrapped in the rubber boot. This was
indicated with the explosimeter after the nozzle was removed from the tank.
2-14
-------
2.4.5 Gulf Balanced System
The data for each vehicle during the testing are shown in Figures 2.4
through 2.6. The data show some scatter below the baseline curve. A large
number of vehicles show a zero return vapor volume on 6/14. These appear to
have been caused by liquid entrainment in the vapor return line. Early in the
afternoon it was noted that liquid was starting to collect in the glass traps
ahead of the dry gas meter. Upon raising the hoses to drain the liquid into
the glass traps, it was determined that 40 to 50 cc. of liquid had collected
at the dispenser on both islands being tested. The liquid traps were drained
before the tests were continued. Prior to this o.ccurrance no liquid was
observed to be entrained at the Gulf Station vapor return line.
The vehicles with the zero return vapor volume are included in the efficiency
data presented for the Gulf Station. The glass traps were capable of collecting
several quarts of liquid prior to being filled. A contributory cause to
liquid in the lines may have been the slight rise in the return hose prior
to entering the glass trap. Every effort was made to prevent the formation
of a loop which could trap liquid; however, it was not possible to eliminate
it always.
Several cars indicated high volume return ratios. These cars are shown in
Table 2-5. As noted in the table, it appears likely that some of these values
are the result of incorrect meter readings.
2.4.6 Standard Balanced System
The volume return ratio for each day of testing at the Standard Station is
shown in Figures 2.7 through 2.9. The data for 6/18 are of interest. During
this day testing was set up for bulk drop measurement and measurement at only
one dispenser. The same test personnel operated the instrumentation at the
dispenser^ and the same filling station operator was used during most of the
day .It should be noted that the station attendants were inexperienced with
the new OPW-7VN nozzle. Standard, therefore, brought in an operator experienced
in using the nozzle. While both the experienced and inexperienced operators
filled on all days, the experienced operator appears to have filled most of the
cars on 6/1.8. He used as many or more hands-off fillings on 6/18 as for the
other two days. It appears that he may have been more careful in inserting
the nozzle. Excluding three cars, the data closely match the baseline curve.
The remainder of the data show the same general pattern as for the Gulf
Balance System,
-------
1.4-
1.2-
co
X = Baseline Car
-20 -10
40
Vehicle Tank - Disp. Liq.Temp.
Figure 2.4 Returned Vapor Ratios/Gulf 6/12
2-16
-------
1.4--
o
•
O"
o.
5
Q.
«o
X = Baseline Car
-10 0 10 20
Veh. Tank Temp. - Disp. L1q. Temp. (°F)
Figure 2.5 Returned Vapor Ratios - Gulf 6/13
2-17
-------
1.4-
1.2--
X= Baseline Car
I
8--
Q_
•r~
o
.2-
0.9|—I \
-20 -10 T) "TO 20 30 40
Veh. Tank Temp. - Disp. Liq. Temp (°F)
Figure 2.6 Returned Vapor Ratios - Gulf 6/14
2-18
-------
License #
V29741
KUL605
FQA058
582782
222647D
111KLP
R55989
P29192
EHY401
449JEL
15874V
730 HNF
399 CQQ
103AFM
PHP979
Date
6/12
6/13
6/13
6/13
6/13
6/13
6/14
6/14
6/14
6/17
6/1.7
6/17
6/19
6/19
6/19
Apparent Cause
Misread volume, previous car low
Misread volume
Low volume before & after car
Low volume before & after car
Low volume before & after car
Hot empty tank, large fill
Appears OK
Appears OK
Misread volume
1st car in morning (Pump 1)
1st car in morning (Pump 5)
Appears OK
Misread volume
Hot empty tank, large fill
Misread tank temperature
Table 2-5 High Return Volume Reading of Cars
2-19
-------
X = Baseline Car
o.a
-10 0 10 20 30
Veh. Tank Temp. - Disp. Liq. Temp. (°F)
Figure 2.7 Returned Vapor Ratios - Standard 6/17
2-20
-------
1.4--
1.2-
2 .8
o
a. .6
i.
o
o.
.4
.2--
0.0
-20
'10 0 10 20 30
Veh. Tank Temp. - Disp. Liq. Temp. (°F)
H h
40
Figure 2.8 Returned Vapor Ratios - Standard 6/18
2-21
-------
X = Baseline Car
-20 -10 0 10 20 3'0
Veh. Tank Temp. - Disp. Liq. Temp. (°F)
40
Figure 2.9 Returned Vapor Ratios - Standard 6/19
2-22
-------
2.4.7 Explosimeter Readings
The explosimeter was used to determine whether any leaks occurred at the
dispensing nozzle/vehicle tank interface. This was accomplished by moving the
explosimeter probe around the interface. The interface was monitored continuous-
ly for all the balance system tests. For the secondary systems, however, the
interface was monitored generally for only the first twenty to thirty seconds.
If no reading was observed, the explosimeter was withdrawn. Based upon
these procedures, the data recorded in Appendix Bl and B2 were obtained.
A summary of the number of vehicles with explosimeter readings is shown
in Table 2-6. It should be noted, however, that a slight explosimeter reading
could be obtained on many more cars at the secondary recovery systems during
the end of fill. When the nozzle was shut off at the end of the fill, a puff
of vapor was sometimes noted. This was not included in the indicated explosi-
meter readings because the amount of vapor leak was considered to be very
small.
2.4.8 Fill Rates
The operators at the stations were allowed to fill vehicles at the normal
rates; however, they were also requested to occasionally fill at higher rates.
The normal position for filling was the middle notch of the three notches a-
vailable in the nozzle. The average dispensing rate at the stations is shown
in Table 2-7 . The results indicate that the flow rates at the balanced system
stations were slightly lower than the values at the secondary system stations.
The normal dispensing rate for gasoline is 2 to 4 gpm on the first notch, 6 to 8
gpm on the second notch, and 10 to 12 gpm on the third notch. Most vehicles
were filled at the second notch because it permitted time for the operator to
service the car. Some cars caused premature shutoff or spitback when the highest
dispensing rate was used.
2.4.9 Test Time
The time required to measure each car was approximately 7 to 8 minutes.
This included noting the driving history, measuring the tank temperature, and
monitoring the fill. This time compared to about 5 minutes for a conventional
fill of a vehicle.
A complete test of the car, Including measurement of tank pressure at the
carbon canister vent line and leak checking of the tank after filling, required
15 to 20 minutes. This precluded a large number of cars from being tested be-
cause drivers were in a hurry and not Inclined to wait for the test. Incentives
such as free gasoline might have induced more customers to wait for a complete
check. 2-23
-------
Vehicle Readings
System Total Explo. Reading Percent
Envi rentes
Intermark*
Process Products
Gulf Balanced
Standard Balanced
52
49 .
43
175
80
17
17
9
121
60
33%
35%
21%.
69%
75%
Table 2-6 Explosimeter Reading During Dispensing
Sys tern
Environics
Intermark
Process Products
Gulf Balanced
Standard Balanced
Gal /Mi n
6.99
8.42
6.51
5.34
5.48
Table 2-7 Fill Rates
2-24
-------
2.4.10 Spitback
Spitback was noted whenever liquid was seen to emerge from the vehicle
tank. The gasoline would run down the car side or spill on the station floor.
The estimates for spitback shown in Appendix B2 are judgement values and should
not be used for an accurate determination. The number of vehicles with spit-
back are shown in Table 2-8.
The amount of spitback was higher at the secondary systems because of
location of the nozzle shutoff vent. This vent is located near the tip of the
dispensing nozzle. On the nozzle modified by the secondary manufacturers, this
vent does not protrude as far into the vehicle tank as for the new OPW-7VN
nozzle. The new OPW-7VN nozzle was used only at the balanced system stations.
As a result of using a modified nozzle, liquid in the vehicle tank was able to
rise closer to the exit plane before the nozzle was shut off. This increased
the possibility of liquid spraying out of the vehicle tank, or, in two cases,
caused the nozzle to eject from the vehicle tank.
2.5 PROCESSING UNIT PERFORMANCE
The performance of the processing unit was determined only for the secondary
systems.
2.5.1 Environics System
The Environics processing unit efficiency was determined by measuring the
inlet and outlet concentrations at the reactor. Mass flow through the reactor
was considered to be constant. The concentration and resulting processing unit
efficiency are shown in Table 2-9. The efficiency value agrees well with the
San Diego APCD stated processing efficiency of 94%.
2.5.2 Intermark System
The processing efficiency for the Intermark unit was not determined be-
cause a complete flow balance could not be obtained. Subsequent inspection by
the manufacturer indicated that the bladder in the surge chamber had a tear in
it.
Figure 2.10 shows the attempted flow balance. 1,603 gallons of liquid were
dispensed during the processing unit test. This represents 214 cu.ft. of liquid.
2-25
-------
ro
r\>
FILL RATE
GPM
0-1
1-2
2-3
3-4
4-5
5-6
6-7
7-8
8-9
9-10
10-11
11-12
12-13
13-14
14-14.55
TOTAL
ENVIRONICS
# OF
FILLS
-
-
1
0
4
6
16
12
8
4
2
53
# OF
SPITBACKS
-
-
0
0
0
1
7
1
1
1
0
11
INTERMARK
# OF
FILLS
-
-
-
2
2
1
22
2
1
1
8
9
1
1
1
51
# OF
SPITBACKS
-
_
-
2
0
0
5
0
0
0
3
1
0
0
0
11
PROCESS PRODUCTS
# OF
FILLS
-
-
-
2
6
2
19
9
5
1
44
# OF
SPITBACKS
-
_
--
0
0
1
2
1
0
1
5
GULF
# OF
FILLS
_
_
8
17
29
76
19
6
6
4
165
# OF
SPITBACKS
_
_
0
0
1
7
1
0
0
0
9
STANDARD
# OF
FILLS
_
_
1
6
8
48
12
5.
80
# OF
SPITBACKS
_
—
0
0
0
1
0
0
1
Table 2-8 Fill Rate Data
-------
A line inlet 1.9% CH4
B line inlet 1.8% CH4
Reactor Exhaust 0.125% CH4
Processing Efficiency 1- T^KF- x 100 = 93.3%
li- -125~
L '-85.
Table 2-9 Environics Processing Unit
2-27
-------
ro
i
r\a
CO
/v
1
*•—
VENT
4
••
1603 GAl .
214 FT;
H
t±
t
-.512 FT3
64'F
r*~
h
•
-s^,s^^^«
1
x»—
•M^
5 FT3
70% C3
4FT3 «=i
82% C-,
80°F^
•^^^ •"
SURGE
CHAMBER
^ r
\J
v«/
VENT 86.4 FT3
80° F
8%C,
IKT 3
4
„ ?
VOLUME COLLECTION RATIO
^ ^
7 dn FT /FT
MASS COLLECTION RATIO
9.89 GM/GAL
Figure 2.10 Intermark
Flow Balance
-------
Based on a volume collection ratio of 2.40, 512 cu.ft. of vapor were returned.
214 cu.ft. was used to displace the liquid dispensed. 86.4 cu.ft. of air was
vented representing 140 cu.ft. of saturated vapor. This results in approximately
158 cu.ft. of unaccounted vapor. The subsequent investigation by the manufacturer
indicated that this volume could have escaped through the torn bladder.
2.5.3 Process Products System
The processing efficiency of the Process Products unit was not determined
because a complete flow balance could not be attained. 'Figure 2.11 is a
schematic showing the attempted flow balance.
The amount of liquid dispensed during the processing unit tests was 863
gallons which equals 115 cu,ft. Based on a volume collection ratio of 1.30
( cu.ft. vapor/cu.ft. liquid) determined previously at the island dispenser,
the return vapor was calculated to be 150 cu.ft. Of this 150 cu.ft., 115 cu.ft.
was returned to the underground tank to displace the liquid dispensed. The
hydrocarbon analyzer used during the; tests withdrew 5 cu.ft. Approximately
7 cu.ft. were estimated to be lost through the leaking P/V vent from a plastic
bag attached to the P/V vent. This bag inflated to approximately 1 cu.ft. in
1 hour.
During the testing 2.68 cu.ft. were vented through the carbon canister.
This represents approximately 5 cu.ft. of saturated vapors. Subtracting the
amount removed by the hydrocarbon analyzer and the amount vented through the
carbon canister, approximately 26 cu.ft. of vapors were lost. Approximately
7 cu.ft. went through the P/V vent valve, while 19 cu.ft. were unaccounted
for. A reliability test program, run following this program, showed that the
underground piping had a leak in the lines going to the processing unit. It
appears that this accounted for the significant leak. Since no mass balance
could be obtained, no processing efficiency was determined.
2.6 OVERALL SYSTEM EFFICIENCIES
The efficiencies for the vapor recovery systems were calculated from the
amount of vapors vented to the atmosphere compared to the amount vented for a
vehicle without a recovery system as shown in Table 2-10. For the balanced
system, the amount vented to the atmosphere was considered to be the amount
2-29
-------
VENT
2.68 FT3
.09 GM
94° F
ro
REFRIG.
UNIT
P/V VENT
3,507 FT
71% C3
81°F
1 FT°/HR
269 GM
7 MRS
DISPENSER
150 FT
3380 GM
863 GAL
115 FT"3
UNDERGROUND
TANK
VOLUME COLLECTION RATIO =1.30
MASS COLLECTION RATIO = 3.91
FT3
FT
Figure 2.11 Process Products
Flow Balance
-------
Table 2-10 Overall System Efficiency Calculation Method
Overall Efficiency:
Balanced Systems:
Secondary Systems:
(gm/gal) emitted
•]
, 1nn
"(gm/gal) baseline x IUU
(gm/gal) emitted = (gm/gal) baseline -(gm/gal) vehicle
(gm/gal) emitted = (gm/gal) vehicle x
_ Processing Unit
Efficiency
-------
lost at the vehicle tank/nozzle interface. For the secondary systems, it
was considered to be the amount exhausted from the processing unit vent.
Based on this analysis the efficiencies in Table 2-11 were obtained.
The efficiencies could not be calculated for two of the systems due to the
leaks described previously.
Due to the wide day to day variations at the balanced stations, the data
and test procedures were reviewed in an effort to identify possible causes
for these variations. The higher efficiency on the first day at the Standard
Station was affected by higher hydrocarbon vapor concentrations at one of the
pumps. A review of the vapor concentration shown in the computer printout of
Appendix C, indicates that there was a pronounced shift in vapor concentrations
starting with car license No. 545 HTC on 6/17/74. A review of the strip charts
as well as pre and post test calibration data does not indicate any abnormalities;
nevertheless, the data for this single pump and day are approximately 10% higher
than the remaining data.
The higher efficiency on the second day appears to have been influenced by
the experienced station operator mentioned previously. Figures 2.4 through 2.9
show the data for the returned vapor ratios. The data 'Show a scatter on the:
three days at the Gulf Station, and the first and third day at the Standard
Station. The data for the second day at the Standard Station (Figure 2.8) show
good correlation to the baseline curve. Only three readings out of eighteen do
not follow the curve, one of them being for the first car on that day. Only
one pump was used for filling and tests on that day, since a bulk drop was
scheduled and the second set of measuring equipment was used to monitor the
underground tank vents. The single pump dispensing the regular grade product
was operated, for the most part, by an operator on loan from the Standard Oil
Gas Station at Davis, California.
The data on Table 2-11 indicates a lower range of efficiencies for the
Gulf Station than for the Standard Station. This may be due to a different
piping layout and a slight pressure drop across the dry gas meter. The multi-
product vapor return lines at the Gulf Station permit vapors to return from
any open nozzle. If the restriction from one nozzle is less, more return vapors
will be drawn through it. Thus, operation of a premium grade dispenser without
a dry gas meter to restrict this flow could decrease the amount of vapor returned
from a regular grade dispenser with a dry gas meter.
2-32
-------
Table 2-11 Overall System Efficiencies
System
Processing
Unit
Efficiency
Overall
Efficiency
Environics
Intermark
Process Products
Gulf Balanced 6/12
6/13
6/14
Standard Balanced 6/17
6/18
6/19
93.3
89.4
Not determined due to leak
Not determined due to leak
N/A
N/A
69
76
62
88
87
76
2-33
-------
The pressure drop measured across the dry gas meters ranged from 0.17
irtiFLO to 0.25 in. f^O depending upon flow. The effect of the meter in the
return vapor line would have been to increase the pressure at the nozzle-finer-
neck interface. This increased the possibility of vapors leaking into the
atmosphere from the interface. Offsetting the pressure restriction of the dry
gas meters was the directional flow valve arrangement at the underground^tank
vent.
The directional flow valves opened and closed in the range from 0.15 to
0.25 in. H20 as discussed previously. At the Gulf Station these valves probably
had little effect due to the interconnected tanks. At the Standard Station,
the valves appear to have had an effect. The pressure measurements shown in
Appendix C show that the underground tank pressure at the Standard Station was
usually negative and averaged around 0.2 in. HpO. This was borne out by the
fact that the inbreathing valve was observed to be the one that opened during
most of the test days. Thus the oressure drop across the dry gas meters at
the Standard Station may have been offset by the reduced underground
tank pressure.
2.7 RVP ANALYSIS
Reid Vapor Pressure (RVP) samples were drawn from the bulk delivered gaso-
line, from the gasoline in the underground tank, and from a selected number of
vehicles. The RVP samples were drawn and stored in ice chests prior to the
analysis. All RVP samples were analyzed by E.W. Saybolt & Co., Wilmington,
California. Copies of their lab reports are included in Appendix D.
The results of the product RVP's at the stations is shown in Table 2-12.
The average value of the product RVP was 8.5.
Table 2-13 shows the RVP analysis performed on the samples drawn from
vehicles. The distribution of the RVP's is further shown in Figure 2.12. The
average RVP for all the vehicles was 8.3 Thus, the product and vehicle RVP's
were nearly equal and suggest that the volatility of the gasoline was not ap-
preciably different.
2-34
-------
Standard Station
Intermark System
Union 76 Station
Process Products System
Gulf Station
Manifolded Balance
Standard Station
Single Product Balance
Texaco Station
. Environics System
Union 76 Station
Process Products System
Standard Station
Intermark System
Date
Underground
Tank
—
8.6
8.1
8.9
—
8.6
—
Bulk Drop
8.9
—
8.1
9.1
8.3
7.9*
—
*Sample taken from fill tube after drop. Product delivered from Los Angeles.
Table 2-12 Product RVP Analysis
2-35
-------
License #
Gil 57827
079 EQU
059 GJX
1043376
312 HPO
909 JSZ
452 SOL
603 GBY
312 HPO
TUS 029
KTR 796
918 KKL
932 HWN
574 KMK
572 FFR
ZND 264
603 GBY
438 JUA
907 KES
662 FZG
Time
0830
1055
1745
0930
1105
1310
1335
0910
0940
1525
1445
1150
1400
1610
1345
1425
0750
0835
0930
1100
Driving History
Freeway 12
Freeway 100
Freeway 8
Freeway 9.7
Local 0
Freeway 8
Local 0.2
Freeway 15
Freeway 6
Freeway 8
Standing
Freeway 15
Local 3
Freeway 118
Freeway 20
Parked
Freeway 8
Local 3
Freeway 8
Freeway 100
Date
6/7
6/11
6/11
6/12
6/12
6/13
6/13
6/14
6/14
6/14
6/14
6/17
6/17
6/17
6/18
6/18
6/19
6/19
6/19
6/20
RVP
8.1
8.6
7.4
8.8
7.6
8.6
8.1
8.8
6.6
8.4
8.7
8.5
8.8
8.2
8.6
8.6
8.0
8.7
8.6
8.2
Table 2-13 Vehicle RVP Analysis
2-36
-------
4,
ro
on
LU
CQ
8
RVP
Figure 2.12 Distribution of Vehicle RVP
-------
2.8 MOLECULAR WEIGHT ANALYSIS
A gas chromatograph/flame ionization detector was used in the field to
obtain molecular weights of the gasoline vapors. Insufficient separation of
\
the C,, Cg, and Cg hydrocarbon peaks, however, made reduction of this data
difficult. Individual span gases for the C., Cg, and Cg hydrocarbon fractions
were not obtainable in the field. Several peaks were noted during field mea-
surements and were thought to be the C., Cg, and Cg peaks. Subsequent calibra-
tion in the laboratory showed that the peaks were Cg peaks and higher. Only
one chromatogram could be obtained which could be successfully analyzed. This
chromatogram was obtained from a sample taken 2 inches down the fillneck of an
automobile. The fractions of hydrocarbons were as follows:
AID ~
C5H12-54 %
C6H1Q- 9.8%
The molecular weight of the hydrocarbons in this vapor sample was calculated
to be 68.1
2.9 PROBLEMS ENCOUNTERED
2.9.1 Environies
The testing of the Environics system proceeded without significant problems.
The vehicle collection was performed on one day and the bulk drop and processing
unit efficiencies were determined on the second day. On the evening of the first
day one of the test technicians inadvertently opened a line from the carbon
canister to the processing unit. The processing unit was immediately shut down
and the lines reconnected. Subsequent checks showed that this did not affect -
the system.
2.9.2 Intermark
The Intermark system tests were performed over a three-day period. The
initial test program consisted of vehicle collection tests on one day and proces-
sing unit tests on the second day. On the second day, an exhaust valve froze
up around noontime causing raw liquid to be discharged at the exhaust vent.
The test was immediately discontinued to determine the cause of this failure.
The cause could not be readily determined so that the tests were discontinued
for the day.
2-38
-------
It was decided to retest this unit at the end of the test program in
order to obtain processing unit data. During this third day of testing it
was noted that high explosimeter readings were obtained at the breathing vent
for the surge tank bladder. It was subsequently determined that the bladder
had torn and was causing vapors to leak out to the atmosphere.
2.9.3 Process Products .
The Process Products system tests were performed over a four-day period.
Initially only two days of testing were planned, with the first day for vehicle
collection tests and the second day for processing efficiency tests. The first
day at the station did not see any tests performed because Union 76 withheld
permission to conduct the tests. On the second day, permission was obtained
and vehicle collection tests were performed. It was then decided to return
to the station at the end of the test program to obtain an additional day of
vehicle refueling data and one day of processing unit performance data.
Several problems were noted with this system. One of the ITT valves regulating
vapor return flow was noted to be leaking at the liquid line inlet. This leak
did not effect ,the vapor return line so that it was decided to proceed with-
out replacing the valve.
It became evident during the test that significant quantities of excess
air were ingested into the system without any of it venting. During the two
days at the beginning of the program as well as during the two days at the
end of the program, the system never vented. The refrigeration unit occa-
sionally came on for a short while in the morning, but no exhaust was noted.
San Diego APCD personnel indicated that this lack of venting indicated high
processing efficiency. However, it appeared more likely that a leak was
occurring somewhere in the system.
The system does not start until the underground system pressure rises
to three inches of water. It was noted on several occasions that there was
a slight pressure buildup during refueling but that this pressure decayed
without the unit starting. Since excess air is ingested during vehicle re-
fueling this air must be discharged somewhere. During reliability tests sub-
sequent to these tests, an underground leak in the vapor return piping was
discovered. It appears that this leak was caused during initial construction,
and was never located in previous testing.
2-39
-------
It should also be noted that the flow through the processing unit was
approximately 3,000 cu.ft. per hour, and that on the day of bulk drop the
unit remained on for approximately 1 hour. During this time, the inlet con-
centration remained at approximately 71% by volume of propane and 80°F for
the entire hour.
The flow of 3000 cfh was measured on ;a dry gas meter rated at 1000 cfh.
This caused the pressure drop across the meter to be higher than normal. Cali-
bration of the meter before and after testing, however, showed that this high
flow did not damage the meter.
Another problem observed at this station was the leaking P/V vent valve.
The valve was changed, but the new valve also leaked.
2.9.4 Gulf Balanced
The problems encountered at the Gulf Balanced station were minimal. The
OPW-7VN nozzle had only been installed recently so that the personnel were in-
experienced in using them. Some problem was encountered in hooking the nozzle
to the lip of the vehicle fill tank. The only malfunction occurred when an
attendant left the nozzle in the gas tank and the vehicle was driven off. The
nozzle was sheared at Its designed breakaway notch. The nozzle was not dispensing
at the time and no liquid was spilled.
2.9.5 Standard Balanced
No major problems were encountered at the Standard Balanced station. This
station was a new station so that the operators were inexperienced in using the
OPW-7VN nozzle. An experienced attendant was brought down from the Standard
Station at Davis, California, to assist in education of the attendants. Filling
of the vehicles was done by the experienced attendant as well as regular station
personnel, except for the second day of operation. While no specific records
were kept it appears that the experienced attendant did service a majority of
the 18 cars during that day. Traffic through the station was quite low due to
it opening up just the week previously.
2-40
-------
3.0 PROCESS DESCRIPTION
3.1 ENVIRONICS
The system manufactured by Environics is shown in Figure 3.1. This system
has two modes of operation depending upon whether there is a bulk drop or
vehicle refueling. For a bulk drop, the excess vapors are passed through a
carbon bed and vented to the atmosphere. As the pressure in the underground
tank builds up during a bulk drop, the solenoid valve connecting the carbon
bed to the remainder of the system is closed. Thus all the excess vapors are
passed through carbon bed #2. Approximately six hours after a bulk drop, the
solenoid valve is opened and carbon bed #2 is connected directly to the remainder
of the processing unit. Carbon bed #2 is stripped by inbreathing of the under-
ground tank for six hours after the bulk drop as well as during normal unit opera-
tion after the six hour time period.
The processing unit for automobile refueling operates on a vacuum suction
principle. The hydrocarbon vapors are drawn from the vehicle tank and through
parallel connected carbon beds. These carbon beds adsorb the hydrocarbon from
the vapor stream. Upon completion of gasoline dispensing at the island, sole-
noids are activated to close the vapor intake line to each carbon bed and open
an air intake line at the opposite end of the carbon beds. The vacuum pump
is then used to desorb the hydrocarbon from the carbon beds by reverse flow.
The hydrocarbons are pumped into a catalytic reactor wheVe they are incinerated.
The exhaust from the reactor is vented to the atmosphere.
The unit which was tested was installed a week before the test and had a flow
system which was different from schematics provided by San Diego APCD, The new
processing unit replaced an older unit which had been operating on site for several
months. Flow diagrams for the new system were not available from the manufacturer.
The previously installed unit operated on a cycle whereby one carbon bed was
adsorbing hydrocarbons from the island dispenser line while the other carbon bed
was being desorbed by the vacuum pump. In that mode the system operated on a
reversing cycle lasting approximately three minutes for each cycle.
The performance of the system was determined by measuring at the sampling
points shown on Figure 3.1. Flow, volume, concentration, pressure, and temper-
ature were measured at the inlet and outlet of carbon bed #2 during bulk drop.
3-1
-------
I
ro
VENT AND
INTAKE
PA
VALVE
CN
Og
co •£.
GAS TANK
INTAKE
VENT
#; = SAMPLING LOCATIONS.
Figure 3.1 Environics System
Bncineratioiif
-------
These points were monitored to measure the efficiency of the carbon bed and
ensure that no breakthrough of vapors occurred. Subsequent to the bulk
drop, the test equipment at the outlet of the carbon bed was removed and used
on the other portion of the processing unit. Volume, concentration, pressure
and temperature measurements were continued on the desorption side of the
carbon canister to show when this process had been completed.
The efficiency of the processing unit was determined by measuring the
concentration of vapors into and out of the reactor. Dry gas meters were
installed at the inlet to the individual carbon beds of the processing unit;
however, these were only used to provide data on flow balance between carbon
beds. It was assumed that the volume of flow into and out of the reactor
was the same for efficiency calculations.
A plastic bag was placed over the P/V valve in order to capture any leak-
ing vapors.
3.2 INTERMARK
The Intermark system is diagrammatically shown in Figure 3.2. This system
utilizes a high pressure refrigeration-condensation process to remove hydro-
carbons from the returned vapors. The vacuum pump (blower) is located at the
processing unit. It pumps the collected vapors through a bed of saturated
liquid located within a surge tank. The surge tank and its moveable bladder
are used primarily for evening out large volumes which may occur during bulk
drop. The saturated vapors from the lower half of the surge tank are com-
pressed in a two-stage high pressure refrigeration unit. The condensed liquid
is returned to the surge tank liquid basin while the dry vapors are vented
directly to the atmosphere. The overflow liquid from the bottom of the surge
tank is returned to the underground gas storage tank.
The processing efficiency of the Intermark unit was determined by measur-
ing the volume, concentration, pressure and temperature of the vapors entering
the surge tank as well as those leaving the processing unit to the atmosphere
(Figure 3.2). The tests during bulk drop as well as during vehicle refueling
were started and ended with the surge tank bladder at the bottom position.
A plastic bag was also placed over the P/V vent in order to capture any
leaking vapors.
3-3
-------
PA VALVE
CJ
GAS TANK
TWO
STAGE
H.P.
REFRIG.
#) = SAMPLING
LOCATIONS
Figure 3.2 Intermark System
[Ref ri gerati on-Condensati on]
VENT
I
5
-------
3.3 PROCESS PRODUCTS
The Process Products flow system is shown in Figure 3.3. The system
operates in the same manner for a bulk drop as for vehicle refueling. A
vacuum blower at the island dispenser draws the vapor from the vehicle
tank and pumps it to the underground tank. The system uses a special flow
control valve to regulate the amount of vapor return depending upon the liquid
dispensing rate.
The refrigeration-carbon adsorption unit operates on a separate flow loop.
The unit is started whenever the pressure of the underground tank reaches three
inches of water. The refrigeration system and blower are started at that pres-
sure and the vapors are passed across the low temperature cooling coils. During
this time the valves to the carbon canister are closed.
When the underground tank pressure reaches five inches of water, the inlet
valve to the carbon canister is opened to permit the carbon canister to reach
atmospheric pressure. At the same time, the blower next to the refrigeration
unit is turned off and vapors allowed to flow by convection.
When the underground tank pressure reaches seven inches of water, valve
B is opened and excess vapors are allowed to vent through the carbon canister
to the atmosphere. When the sytem pressure has dropped to one and one-half
inches of water the refrigeration unit is turned off and the solenoid .valves
are closed. The vacuum pump is then started and continues to operate for
seventy minutes to desorb the carbon canister. The unit is then ready to re-
peat the cycle.
In case seven inches of water are not reached within sixty minutes, valve
B is opened to permit excess air to pass through the carbon canister.
This unit was installed a few days prior to the test, and replaced a
previously installed unit.
The efficiency of the processing unit was determined for bulk delivery
as well as vehicle refueling by measuring the volume, concentration, pres-
sure and temperature at the inlet to the refrigeration unit as well as the exit
from the activated carbon canister.
A small activated carbon canister was attached to the Process Product
carbon canister during vehicle refueling tests as well as for overnight venting.
3-5
-------
VENT
P/V VALVE
U)
REFRIGERATION
UNIT
VACUUM
PUMP
Figure 3.3 Process Products, Inc.
fkefrige rat ion -Carbon]
[Absorption J
UNDERGROUND TANK
= SAMPLING
LOCATIONS
-------
A plastic bag was placed over the P/V vent to determine any leaks. As noted
in Section2. 9, this valve was leaking during the tests since the bag inflated.
3.4 GULF OIL BALANCED
The configuration of the balance system at the Gulf Oil station is shown
in Figure 3.4. This configuration consisted of a single manifold return line
from each island. The vapor lines from each product dispenser were manifolded
to this single return line which was connected to the premium tank. Additional
lines were installed in the station to provide for future changes to the system.
These lines ran to a manifold connecting all three grades of underground tank
storage. Each underground tank had a separate vent at the back of the station.
These vents were manifolded together during the tests to form a common outlet.
3.5 STANDARD OIL BALANCED
The Standard Oil balance system diagram is shown in Figure 3.5. This system
utilizes separate return lines for each product grade. The vapor return lines
for each grade at the island dispenser are manifolded back through a common
grade return line to the underground tank. The underground piping includes
lines for subsequent installation of additional recovery equipment.
3.6 VEHICLE SAMPLING LOCATIONS
The sampling location for measuring vehicle collection efficiencies was
the same for all systems as shown in Figure 3.6. The temperature of the
dispensed liquid and the returned vapor was measured at the back end of the
fill nozzle. Volume, pressure and concentration of the returned vapors was
measured where the flexible hose attaches to the island dispenser.
Prior to vehicle filling, the vehicle tank temperature was measured by
inserting a probe into the gas tank. Vehicle data such as make, model, and
immediate driving history were also obtained at that time. On selected post-
1970 cars, the vent line to the carbon canister was disconnected and a ma-
nometer attached to measure tank pressure during filling. Samples for RVP
analysis were also obtained prior to filling on selected post-1970 vehicles.
As the vehicle was being filled a Teak check was performed around the
gas tank nozzle interface with an explosimeter reading on the 0-1 LEL scale.
3-7
-------
PROVISION FOR
FUTURE CHANGES
CO
I
00
VENT
NO LEAD
Figure 3.4 Gulf Oil Company Multi-Product Balanced System
-------
DISPENSER
DISPENSER
VENT
CO
IX)
DUAL PURPOSE
FILL
#) = SAMPLING
POINTS
Figure 3.5 Standard Oil Company
(Single Product Balanced System]
-------
CO
_<
o
VEHICLE
CARBON
CANISTER
ISLAND
DISPENSER
I DISPENSED
LIQUID
VAPOR
RETURN
LEGEND
Figure 3.6 Vehicle Sampling Locations
P) = PRESSURE
£) = CONCENTRATION
? = TEMPERATURE
= VOLUME
-------
This sniffer check was used to indicate if any vapors were escaping. It
should be noted that this sniff test in no way indicates the volume of leak
when the meter shows an indication.
The amount of fuel dispensed was taken directly from the island gallonage
dispenser. In addition, the time required for filling was noted as well as
the total time that the dispensing nozzle remained in the vehicle tank.
3-11
-------
4.0 SAMPLING METHODS
4.1 EQUIPMENT
The major equipment used for the test program is shown in Table 4-1.
4.1.1 Hydrocarbon Concentrations
Hydrocarbon concentrations were measured by two different instruments
providing continuous output of hydrocarbon concentrations. One instrument
was a Beckman 109 flame ionization detector which was used as is for hydro-
carbon concentrations less than 10% by volume. For hydrocarbon concentra-
tions in excess of 10% by volume, a dilution board was used to provide a
100% by volume propane output reading. The dilution board consisted of
flow meters to measure the sample stream as well as the zero air dilution
stream. The dilution air was delivered from a zero air gas cylinder through
a constant pressure regulator. The flow rates through the dilution board were
maintained at the flow rates set during the calibration runs.
The second analyzer was a Beckman 400 flame ionization detector which had
been modified by TRW to provide direct reading of 100% by volume propane. This
modification was made by installing suitable capillaries to reduce sample flow
size. The modified analyzer was calibrated in the laboratory with diluted
standards and provided the data shown in Figure 4.1.
Both analyzers were calibrated at the beginning and end of each day by
spanning with 100% propane gas. In addition, a 2.06% methane calibration gas
was used whenever concentrations below 10% were measured.
In addition to the continuous analyzers, a portable AID gas chromatograph-
flame ionization detector was used for obtaining molecular weights of the gases.
The calibration gases available for this unit in the field were the same two
indicated above.
Hydrocarbon vapors were also detected by the use of a Bachrach SSP Explo-
simeter. This unit measured hydrocarbon vapors in the 0-1000 ppm and 0-1.0
LEL (Lower Explosive Limit, approx. 2% CH ) ranges. This unit only measures
/\
relative concentration AND NOT VOLUME
4-1
-------
Parameter
Equipment
Hydrocarbon Concentration
Beckman 109 F.I.D.
Beckman 400 (Mod) F.I.D.
AID GC/F.I.D.
Bacharach'SSP Explosimeter
Pressure
0-6" HpO Dwyer Manometer
0-4" H20 Dwyer Manometer
0-2" H20 Dwyer Manometer
0-1" H,,0 Dwyer Manometer
0-6" H20 Magnehelix Gauge
0-140" H20 Magnehelix Gauge
30 " U-Tube Manometer
Temperature
-100 to 300°F Strip Chart Recorder
-100 to 300°F Strip Chart Recorder
-100 to 300°F Thermo Electric Bridge
-32 to 140°F YSI Temp. Probe
Misc. Glass Thermometers
Vol ume
1000 cfh Sprague Dry Gas Meter
1000 cfh Sprague Dry Gas Meter
175 cfh Sprague Dry Gas Meter
175 cfh Sprague Dry Gas Meter
150 cfh Rockwell Dry Gas Meter
Calibrated Polyethylene Bag
Table 4-1 Major Equipment List
4-2
-------
100
80
60
o
40
20
BECKMAN 400 (MOD)
CALIBRATION FOR
PROPANE
20
40 60
ACTUAL VALUE
80 100
Figure 4.1 Hydrocarbon Analyzer Calibration
4-3
-------
4.1.2 Pressure
Pressures at the various test points were measured using Dwyer liquid
level gauges as well as U-tube manometers. In addition, a vacuum dial gauge
and Magnehelix gauges were used as required.
4.1.3 Temperature
Temperatures of the dispensed liquid and the returned vapor were measured
by thermocouples. The dispensed liquid temperature was continuously recorded
on a strip chart recorder. The vapor temperature was measured by portable
Thermo Electric reference cells and read manually.
The underground tank temperatures were measured by thermocouples attached
to the pole used to measure liquid level. The temperatures were manually read
from the reference cells.
Vehicle tank temperature was initially measured using thermocouples and
Thermo Electric reference cells. Early in the program, however, a Yellow Springs
Instrument direct readout thermister unit was obtained for measuring vehicle
tank temperatures.
4.1.4 Volume
Volume of vapors were measured in all cases by dry gas meters. The vapor
return line vapors were measured using 175 cfh dry gas meters with liquid traps
ahead of the meters. These traps were used to prevent liquid gasoline due to
spitback from entering the meters. Flow at several of the processing units
which exceeded a few hundred cubic feet per hour was measured using 1000 cfh
dry gas meters.
Volumes during bulk drop at the balanced stations were measured by a
long polyethylene bag. The bag length was calibrated by filling through a
dry gas meter. The calibration data is shown in Figure 4.2
4-4
-------
45
40
35
30
S
u.
U
3
3
15
10
T
10
20 30 40
BAG LENGTH, FEET
50 60
Figure 4.2 Polyethylene Bag Volume
4-5
-------
APPENDIX A
DAILY STATION DATA
-------
o
I/O
LU
U
u
INTERMARKUNIT
oo
STANDARD
STATION
Uj3| [2.
Ill
1 1" 1 1 1
jlili.
|io
9
CARMEL VALLEY ROAD
A-l
INTEKM.ARK SYSTFM
STAMOA!:0 STATION LAYOUT
-------
Station Standard, Carmel Valley Rd. & 15
Date
6-6-74
Vapor Recovery System
Dry Bulb Temp.
Wet Bulb Temp.
Relative Humidity
Ambient Pressure
Wind Velocity
Overcast
Intermark
'AM
7:50
68
60
63
29.87
calm
100
Noon
Hrs Hrs
oF op
op op
* I
" Hg " Hg
ft/sec ft/sec
%of
%
Start of Day
No-Lead ( 5,000 gal)
Low-Lead (10. 000 gal)
Premium (10,000 gal)
Pump 1
2
3
4
5
6
7
8
9
10
11
12*
1275
925
3600
Initial
7:50 hrs
75299
21021
74273
31749 (note)
44311
48744
59185
13715
38782
12697
94816
29444
gal 72 °F
gal 67 °F
gal 72 °F
Final
6:30 nrs
75927
21138
68064
90766
45273
48846
59709
13862
38782
12697
94816
30029
PM
6:30 Hrs
63 °F
59 ,°F
79 i
" Hg
5-7 ft/sec
100 X
End of Day
1125 gal 73 °F
5000 gal 72 °F
5100 gal 73 °F
Gallons Dispensed
628
117
379
N/A
962
102
524
147
0
0
0
585
*Tested pump
Note: Pump 4 initial reading in error A-2
-------
Station Standard, carmel Valley Rd. & 15
Date
6-7-74
Vapor Recovery System
Dry Bulb Temp.
Wet Bulb Temp.
Relative Humidity
Ambient .Pressure
Wind Velocity
Overcast
Intermark
AM
8:30 Hrs
62 °F
60 «F
89 -
29.78 " Hg
10-15 ft/sec
100 %
Noon '
12:45 Hrs
64 op
62 °F
90 x
" Hq
3-5 ft/sec
100 %
Start of Day
No-Lead (5,000 gal)
Low-Lead(lO,000 gal)
Premium (10,000 gal)
Pump 1
2
3
4
5
6
7
8
9
10
11
12
1125 gal
. 5100 gal
5050 qal
Initial
8:30a hrs
75991
21138
68077
90848
45326
48846
59794
13907
38782
12697
94816
30029
72 °F
72 °F
74 °F
Final
10:00a hrs
76118
21138
68105
90972
45463
48860
59955
13946
38782
12697
94816
30053
PM_
5:00 Hrs
64 • op
62 °F
90 %
" Hg
5-7 ft/sec
100 %
End of Day
925 gal 73 °F
8000 gal 71 °F
7675 gal 71 °F
Gallons Disoensed
127
0
28
124
137
14
161
39
0
0
0
24
A-3
-------
VAPOR ._,
SAVOR| |
UNIT
TIBBS
STATION
[i
WARING ROAD
PROCESS PRODUCTS SYSTEM
UNION 76 STATION LAYOUT
Q
<
O
0£
z
O
N
A-4
-------
Station
Union 76, Zion & Waring Road
Date 6-10-74
Vapor Recovery System
Process Products
Dry Bulb Temp.
Wet Bulb Temp.
Relative Humidity
Ambient Pressure
Wind Velocity
Overcast
No-Lead (10,000 gal)
Low-Lead( -- gal)
Premium (10,000 gal)
Pump
1
2
3
4
5
6
7
8
9
10
11
12
AM
7:30 _Hrs
_ °F
op
63
61
Noon
1:00 _ Hrs
_ °F
°F
PM
76
68
89
66
29.86 " Hg
4-5NW ft/sec
4-5 NW
Hrs
°F
." Hg
ft/sec
100
5-10 %
Start of Day
2289 gal 74
3448
Initial
8:35 hrs
gal
gal
70910
01680
18353
92699
40088
64947
72158
57693
°F
°F
76
Final
hrs
_ft/sec
%
End of Day
gal _
gal _
gal
°F
°F
Gallons Disoensed
NOTE: No testing this day
A-5
-------
Station
Union 76, Zion & Waring Road
Date
6-11-74
Vapor Recovery System
Dry Bulb Temp.
Wet Bulb Temp.
Relative Humidity
Ambient Pressure
Wind Velocity
Overcast
No-Lead (10,000 gal)
Low-Lead ( .-=- gal)
Premium (10,000 gal)
Pump 1
2
3
4
5*
6
7
8
9
10
11
12
Process Products
AM Noon FW
9:00 Hrs 12:00 Hrs 5:30 Hfs
62 op 72 oF 70 op
60 °p 66 op 64 op
89 t 73 x 72 x
29,90 " Hg " Hq " Hq
2-3 SW ft/sec 4-5 SW ft/sec 3-4 SWft/sec
100 % 75 % 0-5 %
Start of Day End of Day
1468 gal 77 °p 1045 gai 75 °p
gal °F qal °F
2665 gal 76 °p 2167 gal 74 °p
Initial Final Gallons Dispensed
9:00 hr-s 12:00 hrs
71032* 71298 266
02037 02087 50
18580 18713 133
92931 93113 182
40116 40184 68
65075 65159 89
72251 72319 68
57748 57828 80
*Tested pump
A-6
-------
UJ
<
I
O
D
o
co
VENTS
ooo
GULF
STATION
2 3
5 6
UNIVERSITY AVE
BALANCED SYSTEM
GULF STATION LAYOUT
A-7
-------
Station
Date
6-12-74
Vapor Recovery System
Dry Bulb Temp.
Wet Bulb Temp.
Relative Humidity
Ambient Pressure
Wind Velocity
Overcast
No-Lead (10,000 gal)
Low-Lead(10,000 gal)
Premium (10,000 gal)
Pump 1
2
3
4
5*
6
7
8
9
10
11
12
Balanced
AM Noon PM
8:15 Mrs 1:15 Mrs 6:15 Hrs
61 <>f 70 °F 67 op
58 °F 65 °F 62 °F
84 s 77 t 75 t
29.86 " Hg " Hg 29.78 " Hg
4-5 NW ft/sec 5+ W ft/sec 5+ W ft/sec
100 % 0 % 0 %
Start of Day End of Day
9613 gal 78 °F 9680 gal 85 °F
6810 gal 76 °F 9302 gal 83 °F
4306 gal 75 °F 8837 gal 81 °F
Initial Final Gallons Disoensed
9:00 hrs 6:30 hrs
73647 73670 23
92069 92448 ^
49284 49662 378
58751 58751 0
21426 21792 366
15243 15279 36
*Tested pump
A-8
-------
Station
Gulf., University & Boundary
Date
6-13-74
Vapor Recovery System
Dry Bulb Temp.
Wet Bulb Temp.
Relative Humidity
Ambient Pressure
Wind Velocity
Overcast
No-Lead (10,000 gal)
Low-Lead(10,000 gal)
Premium (10,000 gal)
Pump 1
2*
3
4
5*
6
Balanced
AM Noon PM
7:30 Hrs 12:30 Hrs 5:30 Hrs
62 op 69 oF 68 op
60 °p 65 op 64 op
89 c, 81 « 80 o,
la Tk %
30.08 " Hg " Hq " Hq
2-3 NW ft/Sec 5+ NW ft/sec 5+ W ft/sec
100 % o % • o %
Start of Day End of Day
9680 gai 75 op 9680 qai 82 op
9125 gal 72 °F 7000 qal 81 °F
8527 gal 75 °F 8085 qai 79 °p
Initial Final Gallons Dispensed
7:30 hrs 5:30 hrs
73689 73691 2
92720 93193 473
49934 50175 241
58754 58777 23
21931 22390 459
15330 15553 223
7
8
9
10
n
12
*Tested pump
A-9
-------
Station
Gu1f» University & Boundary
Date 6-14-74
Vapor Recovery System
Dry Bulb Temp.
Wet Bulb Temp.
Relative Humidity
Ambient Pressure
Hind Velocity
Overcast
No-Lead do, 000 gal)
Low-Lead(10,000 gal)
Premium (10,000 gal)
Pump 1
2*
3
4
5*
6
Balanced
AM Noon PM
7:00 Hrs 2:00 Hrs 5:00 Hrs
63 °F 78 °F '77 °F
61 °F 70 °F 70 OF
89 % 67 « 71 %
29 -88 " Hg " Hq " Hq
3-4 NE f
-------
i
LU
V
VENTS
ooo
BALTIMORE AVE
BALANCED STATION
STANDARD STATION LAYOUT
A-ll
-------
Station
Standard, Baltimore & Lake Murray
Date
6-17-74
Vapor Recovery System
Dry Bulb Temp.
Wet Bulb Temp.
Relative Humidity
Ambient Pressure
Wind Velocity
Overcast
No-Lead ( 8,000 gal)
Low-Lead ( 8,000 gal)
Premium ( 8,000 gal)
Pump 1 *
2
3
4*
5
6
7
8
9
Balanced
AM Noon PM
7:30 Hrs 1:15 Hrs 5:30 Hrs
64 °F 75 °F 74 °F
59 °F 65 °F 64 °F
74 % 58 x 58 x
29.49 " Hg " Hq " Hq
1-1.5 Nflt/sec 5+ NW ft/sec 5+ W ft/sec
% % %
Start of Day End of Day
2600 gal 70 °F 2200 qai 75 °p
850 gal 73 °F 825 ga] 73 °p
2950 gal 72 °F 2675 qal 73 °F
Initial Final Gallons Dispensed
8:00 hrs 5:45 hrs
09557 00693 136
99790 ~ 99790 0
00785 00863 78
00283 00497 214
99710 99710' 0
00037 00177 140
00316 00351 35
99740 99759 19
Closed Closed 0.
10
11
12
*Tested pump
A-12
-------
Station
Standard, Baltimore & Lake Murrary
Date 6-18-74
Vapor Recovery System
Dry Bulb Temp.
Wet Bulb Temp.
Relative Humidity
Ambient Pressure
Wind Velocity
Overcast
No-Lead ( 8,000 gal)
Low-Lead( 8,000 gal)
Premium ( 8,000 gal)
Pump 1 *
2
3
4*
5
6
7
8
9
Balanced
AM
7:15 Mrs
fil °F
58 °F
84 «
.29. 49 " Hg
Noon PM_
11:45 Hrs 3:30 Hrs
7fi °F 7ft °F
fi5 °F 57 °F
55 . % 53 £
11 Hg " Hq
3_R NF ft/sec 5+ w ft/sec q+ ft/sec
in %
Start of
2050 gal
900 gai
2575 gal
Initial
7:30 hrs
00830
99790
00946
00560
99710
00217
00378
99761
Closed
n % n %
Day^ End of Day
71 °F 6275 gal 76 . °F
73 °F 825 gal 72 °F
72 °F 5900 gal 74 °F '
Final Gallons Dispensed
3:30 hrs
00884 54
99792 2
01030 84
00764 204
99710 0
00217 0
00400 22
99761 0
Closed
10
11
12
*Tested pump
A-13
-------
Station
Standard, Baltimore & Lake Murray
Date 6-19-74
Vapor Recovery System
Dry Bulb Temp.
Wet Bulb Temp.
Relative Humidity
Ambient Pressure
Wind Velocity
Overcast
No-Lead ( 8,000 gal)
Low-Lead( 8,000 gal)
Premium ( 8,000 gal)
Pump 1 *
2
3
4*
5
6
7
8
9
10
11
12
Balanced
AH Noon PM
5:30 Hrs 12:00 Mrs 3:00 Hrs
55 °F 74 °F 81 °p
54 °F 64 °F 67 °F
94 2 58 % 47 %
29.57 " Hg " Hg " Hg
0-1 NW ft/sec 5+ W ft/sec 5+ ft/sec
0 % 0 % 0 %
Start of Day End of Day
6150 gal 67 °F 5800 gai 73 op
825 gai 67 °F 825 gal 71 °F
5600 gal 66 °p 5300 ga] 72 op
Initial Final Gallons Dispensed
5:30 hrs 3:30 hrs
00949 01086 137
99792 99792 0
01201 01296 95
00787 01108 321
99710 99710 0
00228 00360 132
00489 00641 152
99761 99787 26
Closed Closed 0
*Tested pump
A-14
-------
VAPOX 3000
UNIT
SHAMBRAZIL
STATION
nm CD
BALTIMORE AVE
'ENV1RONICS SYSTEM
TEXACO STATION LAYOUT
Oi
Q
C£
LU
X
u
i—
LU
—I
U_
A-15
-------
Station
Texaco, Baltimore & Fletcher
Date 6-20-74
Vapor Recovery System
Dry Bulb Temp.
Wet Bulb Temp.
Relative Humidity
Ambient Pressure
Wind Velocity
Overcast
No-Lead ( 8,000 gal)
Low-Lead( 8,000 gal )
Premium ( 8,000 gal)
Pump 1*
2
3
4
5
6*
7
8
Environics
AM
7:30 Hrs
66 OF
60 °F
66 %
29.58 " Hg
1-2 E ft/sec
0 %
Start of Day
4430 gal 72
4646 gal 72
2501 gal 73
Initial
7:45 hrs
36734
44893
04070
99167
39526
42961
03963
44748
Noon PM.
12:45 Hrs 6:00 Hrs
82 °F 78 °F
69 °F 68 °F
51 i 60 %
" Hq " Hg
5+ W ft/sec 5+ W ft/sec
0 % 0 %
End of Day
°F 3779 gal 75 °F
°F 4646 gal 72 °f
°F 1798 gal 74 °F
Final Gallons Dispensed
6:00 hrs
36888 159
44972 79
04070 0
99244 77
39727 201
43422 461
03970 7
45158 410
9
10
11
12
*Tested pump
A-16
-------
Station
Texaco, Baltimore & Fletcher
Date
6-21-74
Vapor Recovery System
Dry Bulb Temp.
Wet Bulb Temp.
Relative Humidity
Ambient Pressure
Wind Velocity
Overcast
No-Lead ( 8,000 gal)
Low-Lead( 8,000 gal)
Premium ( 8,000 gal)
Pump 1
2
3
4
5
6
7
8
9
10
11
12
Environics
AM
7:20 Mrs
60 °F
59 °F
94 «
la
29.59 " Hg
Noon PM_
12:00 Hrs 3:00 Hrs
83 °F 81 °F
70 °F 69 °F
51 t 54 *
" Hq " Hq
0-1 NE ft/sec 5+ SW ft/sec 5+ SW ft/sec
100 %
Start of
4646 gal
3455 gal
1607 gal
Initial
7:30 hrs
36947
45007
04071
99302
39803
43491
03975
05212
0 % 0 %
Day End of Day
68 °F 4646 gal 72 °F
71 °F 6947 gal 74 °F
70 °F 5075 gal 75 °F
Final Gallons Dispensed
3:00 hrs
37046 99
45119 H2
04070 l
99520 218
39929 126
43723 232
03977 2
45482 270
A-17
-------
Station Union 76» Zton & Wartng
Date 6-24-74
Vapor Recovery System
Dry Bulb Temp.
Wet Bulb Temp.
Relative Humidity
Ambient Pressure
Wind Velocity
Overcast
No-Lead (10,000 gal)
Low-Lead( —^ gal)
Premium (10,000 gal)
Pump 1
2
3
4
5*
6
7
8
9
10
11
12
*Tested pump
Process Products
AM Noon
7:30 Hrs 12:00 Hrs
66 °F 79 °F
65 °F 72 °F
95 % 71 £
29.91 " Hg " Hq
3-5 SE ft/sec 3-5+ W ft/sec
10 % 0 %
Start of Day
2793 gal 75 °F
gal . °F
4397 gal 72 °F
Initial Final
7:30 hrs 5:15 hrs
73552 73669
04819 04940
21111 21452
95342 95574
40869 41111
66661 66691
73343 73370
58853 58897
PM '
5:00 Hrs
79 °F
69 °F
60 %
" Hq
5+ W ft/sec
0 %
End of Day
2665 gal 75 °F
gal °F
3987 gal 76 °F
Gallons Dispensed
117
121
341
232
242
30
27
44
A-18
-------
Station
Union 76, Zion & Waring
Date 6-25-74
Vapor Recovery System
Dry Bulb Temp.
Wet Bulb Temp.
Relative Humidity
Ambient Pressure
Wind Velocity
Overcast
Process
'AM
7:30
65
62
85
29.94
0-1 NW
90
Products
Noon fW
Hrs 12:00 Hrs 3:00 Hrs
°F 78 op 83 °F
op 69 °F 71 °F
j, 63 2 55 %
" Hg " Hq " Hq
ft/sec 2-3 W ft/sec 5+ W ft/sec
% 0 % 0 %
Start of Day End of Day
No-Lead (10,000 gal)
Low-Lead ( — gal)
Premium (10,000 gal)
Pump 1
2
3
4
5
6
7
8
1867
3448
Initial
7:30 hrs
73669
04940
21452
95574
41111
66691
73370
58897
gal 74 °F 5707 qal 75 °F
gal °F gal °F
gal 74 °F 8325 gal 74 °F
Final Gallons Dispensed
3:00 hrs
73827 158
05175 . 235
21615 163
95625 51
41164 53
66773 82
73458 88
58930 33
9
10
11
12
A-19
-------
Station
Standard, Carmel Valley Rd. & 15
Date 6-26-74
Vapor Recovery System
Dry Bulb Te;~p.
K'et Bulb Terp.
Relative Humidity
Ambient Pressure
Wind Velocity
Overcast
No-Lead ( 5,000 gal)
Lov:-Lead(l 0,000 gal)
Premium. (10,000 gal)
Pump 1
2
3
4
5 „
6
7
8
9
10
11
12
Intermark
AM
9:30 Hrs
72 °F
67 °F
77 *
29.86 " Kg
5+ W ft/sec
c/
/o
Start of Da
3700 gal
4650 gal
8600 gal
Initial
9:30 hrs
91502
22124
78304
01657
65246
50495
74359
26433
Closed
12751
95139
30484
Noon
12:45 Hrs
77 °F
68 °F
63
" Hg
5+ W ft/ sec
e/
to •
V
72 °r
72 °F
70 °F
Final
3:30 hrs
91775
22166
78532
01880
65504
50495
74638
26783
Closed
12751
951 39-
304S4
FW
3:15 Hrs
75 °F
69 °F
74 %
" Hq
5+ W ft/sec
V
a
End of Da-/
3500 gal 72 °F
3650 gal 72 °F
7975 gal 72 °F
Gallons Dispensed
273
42
228
223
258
0
279
300
0
0
0
0
A-20
-------
Station
Standard, Carmel Valley Rd. & .15
Date 6-26-74
Vapor Recovery System
Dry Bulb Te;-p.
l-.'et Bulb Terp. •
Relative Hunidity
Ambient Pressure
Wind Velocity
Overcast
No-Lead ( 5,000 gal)
Low-Lead(10,000 gal)
Premium (10,000 gal)
Pump 1
2
3
4
5
6
7
8
9
10
11
12
Intermark
AM
9:30 Mrs
72 °F
67 °F
77 *
29.86 " Hg
5+ W ft/sec
a
la
Start of Da
3700 gal
4650 gal
8600 gal
Initial
9:30 hrs
91502
22124
78304
01657
65246
50495
74359
264S3
Closed
12751
95139
30484
Noon
12:45 Hrs
77 "F
68 °F
63
" Kq
5+ W ft/sec
V
to •
V
72 °F
72- °F
70 °F
Final
3:30 hrs
91775
22166
78532
01880
65504
50495
74638
26783
Closed
12751
951 39"
304S4
PM_
3:15 Hrs
75 °F
69 °F
74 *
" Hq
5+ W ft/sec
V
/o
End of Da-/
3500 gal 72 °F
3650 gal 72 °F
7975 gal 72 °F
Gallons Disoensed
273
42
228
223
258
0
279
300
0
0
0
0
A-20
-------
Station
Standard, Carmel Valley Rd. & IS
Date 6-26-74
Vapor Recovery System
Dry Bulb Te~p.
Wet Bulb Terp. •
Relative Humidity
Ambient Pressure
Wind Velocity
Overcast
No-Lead ( 5,000 gel)
Lov:-Lead(10,000 gal)
Premium (10,000 gal)
Pump 1
2
3
4
5
6
7
8
9
10
11
12
Intermark
AM
9:30 Hrs
72 CF
67 °F
77 g
29.86 " Kg
5+ I! ft/sec
o/
/'O
Start of Da
3700 gal
4650 gal
8600 gal
Initial
9:30 hrs
91502
22124
78304
01657
65246
50495
74359
264S3
Closed
12751
95139
30484
N'bon
12:45 Hrs
77 °F
68 °F
63 e.
11 Kg
5+ W ft/sec
el
to •
V
72 °F
72 °F
70 °F
Final
3:30 hrs
91775
22166
78532
01880
65504
50495
74638
26783
Closed
12751
95139
304S4
PM
3:15 Hrs
75 °F
69 °F
74 «
11 Hq
5+ W ft/ sec
V
/o
End of Day
3500 gal 72 °F
3650 gal 72 °F
7975 gal 72 °F
Gallons Disoensed
273
42
228
223
258
0
279
300
0
0
0
0
Ar20
-------
APPENDIX B
BULK DROP DATA
-------
BULK DROP DATA
Station Standard (Intermark Unit)
Date
6/7
Truck Configuration
Trailer)
3 21
Loading
Grade: L.L. L.L. L.L.
(Truck)
.2 1 C
; A
/ B
Sup. Sup.
Gallons Fill: 2100 890 1690 1865 2140
Explosimeter: ^W"* 0 <.2
0 0
, %
Loading Time: * (Auurox. COOypin) •
Temperature: 70 70 70
RVP: , 8.9
Drop
Seouence: 1 3 2
Explosimeter: 0 00
Drop Time:
70 70
2 1
0 0
-
Avg. Iruck Press: 12. 5 Lo 14.5 inches H00 •
i r • i n n
Final Truck Press: * " ^.0 inches I^U
Tank
Initial
Grade Capacity Volume Temp
(gal) (gal) (°F)
Premium 10,000 4,700 74
Reaular 10,000 4,675 72
No-Lead 5,000 1,125 72
*•
Final
Volume Temp RVP
(gal) (°F)
8,500 72
9,000 72
1,125
Start Truck Loading: 0940
Complete Truck Loading: 1000
Depart from Terminal: 1005
Arrive at Station: 1035
Start Bulk Drop: 1100
Complete Bulk Drop: 1120
B-l
-------
BULK DROP DATA
Station Gulf (Balanced System)
Truck
Configuration
^_ , Tn rk Trailer
C
A
B
1
2*
^x
•
3 4
Date 6/12
Loading
Grade: Prem.
Gallons Fill: 2500
Explosimeter: 0
Loading Time: 4:00
Temperature: 72
RV:
Drop
Sequence: 1
Explosimeter: 0
Drop Time: 8:15
Avg. Truck Press: *"
Final Truck Press: 0
Tank
Grade Capacity
(gal)
Premium 9,940
Reaular 9.940
No-Lead
Start Truck Loading:
Complete Truck Loading:
Depart from Terminal:
Arrive at Station:
Start Bulk Drop:
Complete Bulk Drop:
Prem. Regular Regular
1000 1650 3100
Slight leak 0 0
1:30 3:00 5:20
72 7.1 71
8.1
1 1 1
000
3:05
— — — — MpprOX. I.U muitJb HOU
000 0
Initial Final
Volume Temp Volume Temp RVP
(gal) (°F) (gal) (°F)
6,746 77 9,302 77
4,042 75 9;925 76 8.1
— - — — _
0950
1015
1020
1200
1220
1240
* Note: Premium grade dropped into regular grade underground tank since premium
tank was filled. B-2
-------
BULK DROP DATA
Station Standard (Balanced System)
Date
6/18
Truck Configuration
c
A
B
1
2
3
4
5
Loading
Grade:
Gallons Fill:
Explosimeter:
Loading Time:
Temperature:
RVP:
Drop
Sequence:
Explosimeter:
Drop Time:
Avg. Truck Press:
Final Truck Press:
Supreme
2515
4:40
72
Tank
Grade
Premium
Regular
No-Lead
Capacity
(gal)
8.000
8.000
8,000
Start Truck Loading:
Complete Truck Loading:
Depart from Terminal:
Arrive at Station:
Start Bulk Drop:
Complete Bulk Drop:
Supreme
990
1:45
72
Lo-Lead
835
1:30
73_
9.1
Lo-Lead Lo-Lead
1715
2115
3:30
4:00
73
0
Start: -2 to -3" H00
0
End; -1/2 to ~1" H£0
0 0
Initial
Final
Volume Tem
2.500
1.900
900
0915
72
71
Volume Temp
"Tg^iT m
5,975 78
6.425 81
73
0930
0945
1010
1030
1040
73
RVP
8.9
B-3
-------
BULK DROP DATA
Station Texaco (Envimonies System)
Date
6/21
Truck Configuration
c
A
B
1
2
3
4
Loading
Grade:
Gallons Fill:
Exp1osimeter:
Loading Time:
Temperature:
Premi urn
2400
3:50
71
Premi urn
1500
Lo-Lead
1500
2:30
71
2:30
72
8.3
Lo-Lead
2400
.6 to 1.0 .2 puffs .5 to 1.0 1.0+
3:50
73
Sequence:
Explosimeter:
Drop Time:
Avg. Truck Press:
Final Truck Press:
Tank
5:15
0
3:45
4:08
Varying from -3; to -5" HgO
000
Grade
Premium
Regular
No-Lead
Capacity
(gal) .
a.oon
8tQQQ
8.OOP
Start Truck Loading:
Complete Truck Loading:
Depart from Terminal:
Arrive at Station:
Start Bulk Drop:
Complete Bulk Drop:
6:50
+0.1
Initial
Volume
"TgiiT
1 ,600
3.455
0815
0830
0835
0845
0930
1005
Temp
m
Final
Volume
TgaTT
5r08Q
6.960
Temp
m
22—
22—
RVP
B-4
-------
BULK DROP DATA
Station Union 76 (Process' Products System) Date
Truck Configuration
6/25
Loading
Grade:
Gallons Fill:
Explosimeter:
Loading Time:
Temperature:
Premium
2400
3:30
74
Unleaded Unleaded Premium
2000
2000
2400
.9
3:30
74
Sequence:
Explosimeter:
Drop Time:
Avg. Truck Press:
Final Truck Press:
Tank
5:15
1.5"
Grade
Premium
Regular
No-Lead
Capacity
(gal)
10.000
10,000
.7
4:05
1.0
4:15
2 to 4 " H20
1.5"
1.5"
Initial
Volume
"TglTT
3.250
1.580
0900
Temp
m
75 _
74
5:30
1.5"
0910
0915
1000
1015
1025
Final
Volume Tem
8.384 . 78
6,054 78
RVP
8.6
Start Truck Loading: _
Complete Truck Loading: _
Depart from Terminal: _
Arrive at Station: _
Start Bulk Drop:
Complete Bulk Drop: _
* Note: Unleaded product delivered from Los Angeles.
RVP Sample from fill tube after drop was 7.9
B-5
-------
APPENDIX C
VEHICLE REFUELING DATA
Appendix C-l
Appendix C-2
Appendix C-3
Appendix C-4
Appendix C-5
Index
Field Data, Page 1
Field Data, Page 2
Performance Calculations
Vapor Collection Ratios
Calculation Methods
-------
APPENDIX C-l
FIELD DATA, PAGE 1 OF 2
C-l
-------
.MATIJ1N* .1IA!1QARP_JPRJ£^
LICENSE TIME STATE MAKE MOOEL
NUMBER
LOCATIONS CARMEL VALLEY * 15
DATES 6/ 6/74
YEAR DRIVING VEH.
HISTORY TANK
TEMP
VEH. LEAK RVP GALL FILL TOT
TANK CHECK FILL TIME NOZL
932HWN
080 EAT
[2V2CTX
0(8k 0 CAL I f___Fp_RD_
0925 CAL V/OLKS
T955~~~CAirCHEVT
S/W
sw
~¥EGT
..?.?.: __FREL i.-...-..
69 LOCAL 3
._._ __.__.____.___..
PRES
65 1.6 1.5
TIME
NO 16.5 2830 3*00
NO 7 .k
NO 7.2
1358<»R 1030 FORD COURIER. 7k FREE 130 60 .9 .d NO 10.
0«59 1*30
£830974
55865F
;874FLS
C9809
059KFQ
:VCL446
Y YG 563
GQP810
60969
924Q2X
1038
1055
1115
1125
1135
1150
1205
1215
1225
1230
CAL.
CAL.
CAL
NLVAO
CAL
CAL.
CAL
CAL
CAL
SAL
DODGE
FORD
CHEV.
MERCURY
AMC
V.W.
FORD
VOLKS
FORD
MERCURY
POLARA
PICKUP
S.W.
S.W
JAVLIN
BUS
MUSTANG
BUS
MAVERICK
S.W.
73
70
69
72
7k
67
69
62
73
72
FREE
BOTH
FREE
FREE
FREE
FREE
FREE
LOCAL
FREE
FREE
5
1*»0
100
85
100
10
<•
1
12
2d
tt& 0 N/A
72 N/A
7k N/A
9U N/A
90 -5
6k
74
70
39
ai
13.9
17. k
18.7
6.7
12.5
8.5
17.3
8.3
13.5
13.
1*02
1*40
1*41
0*50
1*4•':,;:.. V
1*48
0*51
•HS8::-.-':;;|:;r
1*13- :';',f;
2*37
2*01
1*55
-------
STATION! STANDARD PROCESS: INTERMARK
LOCATION: CARMEL VALLEY
is
DATEt 6/ 6/7<»
LICENSE TIME
NUMBER
96695E
XYV086
IR27816
TUCKIE
950DVE
VWA636
,026BHA
2A8ACV
:588YHU
C 29ESQ
2LX232
838GOA
830HPA
651FV*
12*»5
1305
1320
1335
1350
1*»00
1«*10
1M5
1V30
15<»0
i<»50
1<»55
1505
1510
STATE
CAL
CAL.
CAL
CAL.
CAL
CAL
CAL
CAL
B.C.
CAL
GAL
CAL.
CAL
MAKE
FORD
CHRYSLER
CHEV
FORD
MERCURY
V.W.
FORD
V.W.
CHEV.
V.W.
FORD
FORD
FORO
MODEL
PICK-UP
NEWYORKE
PICKUP
PINTO
MARQUIS
BUS
FALCON
BUG
2 TON TR
SEDAN
MUSTANG
FAIRLANE
PINTO WA
YEAR DRIVING
HISTORY
69
68
67
7<»
71
68
69
70
56
70
72
69
72
FREE
LOCAL
FREE
LOCAL
LOCAL
LOCAL
FREE
LOCAL
FREE
LOCAL
FREE
FREE
LOCAL
20
6
15
7
10
10
^0
12
*»0
1
30
3
2
VEH. VEH. LEAK RVP
TANK TANK CHECK
TEMP PRES
0 78
67
72
80
0 88
78
86
73
7<»
75
__ 71
~~ I «?
87
73
1/2 76 -3
GALL
FILL
1^.7
16.1
12. *
3.5
9.«r
3.5
12.3
6.2
13. A
8.3
8.8
!<*.!
8.9
8.0
FILL
TIME
1J17
1S25
1MO
OJ20
It22
Ot36
1:50
0:55
1*16
0**t7
1:23
1:09
H18
mo
TOT
NOZL
TIME
1120
1:27
i"» ii' :.••/>''
0:20
1:22
0:36
1150
0:55
1»20
Oti»7
1123
1:20
i:i9
1110
I
ro
-------
STATION! STANDARD PROCESS* INTERMARK
LICENSE TIHE STATE MAKE MODEL
NUMBER
LOCATION: CARMEL VALLEY
is
DATE! 6/ 6/74
YEAR DRIVING VEH.
HISTORY TANK
1 8_29 360
9C2DBT
1520 CAL
1530 CAL
BUICK
_SA J_A LITE _ 73
LASAORE 71
HMX668
'XDU752
S KE 220
'4l5~2
4152
TEMP
JFREE_ 13 0 _87
75 81
73
VEH.
TANJ<
PRES"
LEAK RVP GALL FILL TOT
_CHEC_K FILL TIME NQZL
15.1 1120 U23
13.9 H15 1122
1550 CAL
TeooCAL"
1605 CA.
v.w.
PLYMOUTH"
FORO
FREE 15
71
8.7
1500 CAL CMC PICK-UP 73 LOCAL 1 73 11.4 ItOl 1:07
1545 CAL PAT SUN...?_ICK-UP 72 _f.REE 30 82 ___ _ N_0 8.1 H10 It 11
BUG 65
TJuTlANf68 FREE 50 84 14.51U8i:20
TORINO 74 30TH 50 90 2.8 2.3 19.2 2i43 2»5lj
76
1620 CAL
MERCURY
COMET
66
LOCAL 1
8.6
1120
1630 OKLAH WINNE8AGO
1630 OKLAH HINNEBAGC
70
70
FREE 20
FREE 20
91
100
17.5 <»J«»S ASV8
12.4 3»19 3J20
186 LEG
329HQA
CUD 923
TG528697
1645 CAL
1645 CAL
1700 GEORG
1705 CAL.
CHEV. .
FORO
MERCURY
TOYOTA
CAMERO
S.W
CAPRI
OELUX
74
73
74
74
FREE
FREE
BOTH
FREE
25
?5
20
20
96
a?
82
80
-.6 -.
-3.2-2
-.1 -.
1
.4
1
9.
18
9.
7.
7
.8
6
H23 1825
1:07 1:0
CO
-------
STATION* STANDARD PROCESS* INTERMARK
LOCATION: CARMEL VALLEY *• is
DATE: e/ 6/7<»
LICENSE
NU MBE R
TIME
STATE
MAKE
MOOEL
VEAR DRIVING VEH. tfEH.
HISTORY TANK TANK
LEAK RVP GALL
CHECK FILL
FILL
TIME
j TEMP PRES
(.06 OKA
228BQ1
T093
-------
STATION: UNION 75
SS: PROCESS PRODUCTS
LOCATIONS WARING
ZION
DATE: 6/11/7**
LICENSE TIME
NUMBER
i
iZMR<*01 1022HpS
738JLA
123Q CALIF CHEVROLET CHEVELLE 73
12<»5 CALIF AMERICAN M GREMLJ[NI 72
SEDAN 66
TAIRLAM~f~68~
SATELLIT 73
1305 CALIF Virf
1310 CALIF FORD
1315 CALIF PLYMOUTH
k 72 -k
. PARKIP..l.jy*s._..78
LOCAL 1 77
1 79~
LOCAL 2
l
-------
STATION: UNION 76
PROCESS: PROCESS PRODUCTS
LOCATION: WARING * ZION
DATE: e»/u/7**
LICENSE
NUMBER
<*50ETV
Q59GJX
TIME STATE
MAKE
MODEL
YEAR DRIVING VEH.
TANK
TEMP
VEH.
TANK
P~RES
LFAK RVP GALL FILL TOT
CHECK FILL TIME NOZL
«r 3 20 1300
137GXA
AMERICAN 65
GRANOPRI 71
ELECTRA 7ir
______ .__
65
81
"aT
9.8
1S18 1:20
FREE 5 .
PREE 8-10 33 5.6 5.6
FREE 8 8<* 7.5 6.5
12.0 2:18 2S3Q
.?.! j?J ._.311JL_I.1.30_
20.*» 3:ca 3J17
1755 CALIF BUICK
DUSTER
S/M _____ _
CUSTOM 5 68
"MUSTANG &T
LOC,AL_1.5
LOCAL 6
RIVIERA
73
LOCAL 12
FREE_ 20
LOCAL 10
77
.__
86
9.6 1:30 1130
NO 15.1 2:25 3:10
NO 10.6 U20 1:2?
NO 8.2
NO 3.5
OJ50 0:50
NO 8.9
1U9 1J19
o
i
-------
STATION: GULC
PROCESSt GULF BALANCED
LOCATION'! UNIVERSITY •+ BOUNDARY OATEt 6/12/7
-------
LOCATION: UNIVERSITY + BOUNDARY
DATE: 6/12/7<+
LICENSE
NU MBE R
i
60421F
446JEC
i526GGC
236KLM
101ASI
;653F6X
iZQ.0792
V 29741
RGD594
86394E
6890LX
550KPG
611GGS
mSHDT
TIME
STATE
NAKE
MODEL
YEAR DRIVING VEH. VEH. LEAK RVP
HISTORY TANK TANK CHECK
GALL
FILL
FILL
TIME
TEMP PRES
l
-------
j - . .. ,- . . ... -.„.,...
j STATION! GULF PROCESS* GULF BALANCED LOCATION: UNIVERSITY * BOUNDARY DATE: 6/12/7**
LICENSE TIME STATE MAKE MODEL *EAR DRIVING
NUMBER HISTOR*
;37*»98W 17«»5 CALIF CHEVROLET VAN-20 7<» LOCAL
159KZQ 1755 GAL ^ORO RANCH W. 66 FREE
1
15
VEH.
TANK
TEMP
7k
30
VEH. LEAK RVD GALL
TANK CHECK FILL
PRES
NO 14.8
NO 11.6
FILL TOT
TIME NOZL
2*30 2*
-------
STATION* GULF
PROCESS: GULP BALANCED
LOCATION: UNIVERSITY + BOUNDARY
DATE* 6/13/74
LICENSE TIME
NUMBER
STATE
MAKE
MOOEL
YEAR DRIVING VEH. VEH. LEAK RVP
HISTORY TANK TANK CHECK
GALL FILL
FILL TIME
: TEMP PRES
Q 72 787
78784L
! 105 HOT
93229G
QMV785
754KLS
TET248
999DUH
KUL605
9C9JSZ
45280L
3 76 OF J
668KHW
TXG714
1117
1125
1133
1145
1155
1225
1230
1257
1300
1310
1335
1345
1350
1415
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
GALIF
FORO
FORO
OLDSHOBILE
CHEVORLET
CHEVROLET
PLYMOUTH
V.W.
V.W.
DODGE
CHEVROLET
CHEVROLET
CHEVROLET
MERCURY
FONT! AC
RANGER P
PICKUP
CUTLASS
C-30 TRU
DELUXE
VALIANT
BUG
BUG
LANCER 7
VEGA GT
CUSTOM 2
NOVA
COMET
LEMANS
67
7?
73
7G
52
67
66
71
61
73
72
71
66
67
LOCAL
LOCAL
FREE
LOCAL
LOCAL
FREE
LOCAL
FREE
LOCAL
FREE
LOCAL
FREE
LOCAL
LOCAL
7
.5
3
.25
3
7
1
11
10
8
.2
10
2
.5
7H
-
86 1
70
75
75
7k
88
ao
89 0
63
S3
85
81
NO
NO
.5 3 NO
3 NO
NO
NO
NO
NO
NO
0 8.6
6.6
NO
NO
NO
16.
5.7
8.5
1C.
7.6
9.1
8.6
n.
8.4
9.9
10.
6.5
12.
5.7
0 2:35
' U10
2:00
0 2:50
2SGQ
2:30
1:00
1 2:30
1*26
2:
-------
STATIONS GULF
PROCESS* GULF BALANCED
LOCATION: UNIVERSITY + BOUNDARY
DATE:
LICENSE
NUMBER
i
I
'OUM753
0238796
:735GOW
2 88 BEX
VtU721
;U<»0716
8776*»N
122DFK
!2*7AOR
TTF-876
585G8T
XTL389
89
-------
STATION* GULP
PROCESS: GULP BALANCED
LOCATION: UNIVERSITY + BOUNDARY
DATE: 6/13/7**
LICENSE
NUMBER
86<*67P
728FEA
ITST28V
H 5i»0.55
7«*10ZE
53VBXV
735DQK
1C3AFO
567KAC
TAAifSO
C 1*9 OZN
378GNZ
5G8KHV
TIME
17<»0
1750
1000
1015
1025
1030
1050
1055
1120
m.
1150
1330
1355
STATE
CALIP
CALIF
CAL
CAL
CAL
"CAL.
CAL
CALIF
CALIF
CAL
CALIF
CALIF
CALIF
CALIF
MAKE
CHEVROLET
TOYOTA
VW
CHEV
CHEV
VW
CHEV
FORD
VW
PLYMOUTH
PLYMOUTH
VW
PLYMOUTH
CHEV
MODEL
CUSTOM/2
LAND CRU
STATION
1/2 PICK
VEGA2300
BUG
CAPRICE
MAVERICK
8UG
OUSTER
3ARRACUD
DUSTER
IMP ALA
YEAR DRIVING VEH. VtH. LEAK RVP
HISTORY TANK TANK CHECK
73
71
67
72
70
71
72
70
72
66
71
73
7,
LOCAL
FREE
LOCAL
LOCAL
FREE
LOCAL
LOCAL
LOCAL
FREE
LOCAL
LOCAL
FR
LOCAL
LOCAL
TEMP PRES
<» 77
100 S5
2 6**
5 81
-------
STATIONS GULC
PROCESS* GULF BALANCED
LOCATION: UNIVERSITY * BOUNDARY
DATE: &/i3/7<*
LICENSE
NU MBE R
j
3 89CEC
58278S
ZRDLR2733
VNM013
FQA058
J962GAP
226*70
OZN598
111KLP
2 86 KPH
RBA63*
«»69HOR
LZA573
1<*OEAV
TT '
i
co
TIME
STATE
MAKE
MODEL
YEAR ORIV
ING
HISTORY
1400
11*00
1*15
1*25
1*30
1*55
1505
1520
1555
1500
1610
1630
161*5
CAL
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CAL
CAL
CALIF
CALIF
CALIF
GAL
PORO
OATSUN
FORO
CLDS
CHRYSLER
PONTIAC
FORO
FORO
CHEtf
HONOA
BUICK
HONOA
MERCEDES
vw
PINTO
PICKUP
MUSTANG
CUTLASS
NEWPORT
LEMANS
250-3/*
GALAXIE
MONTECAR
CIVIC
<*<*OSPEC
COUPE
220SE
aus
71 LOCAL
7k FREE
7k LOCAL
67 FREE
63 LOCAL
68 FREE
69 FREE
6* LOCAL
7* FREE
7k FREE
66 FREE
72 LOCAL
60 LOCAL
71 LOCAL
3
15
2
18
1
6
17
2
6
12
50
3
1
1
VEH. VEH. LEAK
TANK TANK CHECK
TEMP PRES
90
91
92
81
8* 3
93
32
72
103
79
87
79
85
77 3
RVF
NO
NO
NO
NO
NO
NO
NO
NO
NO.,
NO
NO
NO
GALL
FILL
9.
3.8
3.3
8.7
3.8
1.9
23.*
5.8
18.2
3.8
9.5
k.
1.9
9.5
PILL
TIME
1:00
0:56
IS 00
is 00
1,15
Q**Q
3J30
ma
3315
0**5
1:00
Q:<4Q
1*15
TOT
NOZL
TIME
1*15
0*56
1*00
U05
1*30
Cl*0
3*35 '
1.3, .
3»25
n»*5
1*10
ISO
1*15
-------
STATION:
PROCESS* GULP BALANCED
LOCATION: UNIVERSITY + BOUNDARY DATE: 6/13/74
LICENSE TIME
NU MBE R
48457W
WRY 045
iXCR052
228KZC
2C6ANU
46729P
VSL427
1655
1700
0955
1020
1040
1050
1103
STATE
CAL
CAL
CALIF
CALIF
CALIF
CALIF
CALIF
MAKE
DODGE
VH
OATSUN
CHEVY
CLDSM03ILE
CHEVROLET
CLDSMOBILE
MOOEL
1/2TON P
3UG
510SM
CHEVY II
F-85
C-20 PIC
TORONAOO
YEAR DRIVING VEH. tfEH.
HISTORY TANK TANK
65
69
7k
67
64
69
69
LOCAL
LOCAL
LOCAL
fREE...
LOCAL
LOCAL
LOCAL
TEMP PRES
2 75
5 86
2 64
7? N.D
16 77
3 68
.25 76
LEAK RVP
CHECK
NO
NO
NO
ND NO
NO
NO
NO
GALL
FILL
16.2
8.
8. a
7.8
3. a
9.5
3.8
FILL
TIME
3:00
1:40
1131
1151
1:45
2:32
1:01
TOT
NOZL
• ;-TIJJ-E^>;
3:10
1:45
1 1 31
.1151
1:45
2t33
It 0.1
o
-------
STATIONI GULF PROCESSi GULF BALANCED
LOCATION* UNIVERSITY + BOUNDARY
DATE! 6/14/74
LICENSE
NUMBER
76625H
603GBY "
; X WE 767
E 82 646
130HQE
312HPO
045CHF
12831R
32391E
049FNU
811HSD
44053F
700KFC
724CTU
TIME
0845
0910
0915
2520
0925
0940
Q950
10C5
1020
1030
1045
1050
112n
1120
STATE
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CAL
MAKE
FORD
FORD
VW
FORD
DODGE
MERCURY
CHEVY
FORD
CHEVY
FORD
DATSUN
MERCURY
CHEVY
CHEV.
MODEL
VAN
TORINO
SEDAN
CAMPER
DART
MARQUIS
VEGA
ELCAMINO
CAMPER
TORINO
51QSEOAN
MAG ON
VEGA
VEGA
YEAR DRIVING VEH. VEH.
HISTORY TANK TANK
71
72
69
57
73
73
71
73
69
7?
73
70
74
71
TEMP PRES
PARKEOO
FREE
LOCAL
FREE
LOCAL
FREE
LOCAL
15
1
9
l.C
6
1
PARKEDO
LOCAL
LOCAL
LOCAL
FREE
FREE
LOCAL
3
1/2
H
8
154
3 BLK
75 1.0 .3
69
65
76
BO 1.0 .3
73
69
69
63 3.0 .75
76
76
101
87
LEAK RVP
CHECK
NO
3 8.8
NO
NO
NO
3 6.6
NO
NO
NO
3 NO
NO
NO
NO
NO
GALL
^ILL
3.8
5.0
8.5
8.2
12.0
12.0
3.8
V.3
16.3
3.5
4.7
14.3
5.4
9.4
FILL
TIME:
Qt45
0:55
It 15
1520
2:iQ
2J19
Ot50
1:10
2 SCO
PJ4Q
U5
2«30
1:00
1*45
TOT
NOZL
TIME
1:45
1 t45
1J40
U22
2150
3t55
0150
3?20
2S35
2t06
1J13
2S45
1:54
t:55
'O
I
-------
S.T ATI QN«_GULf _...PR.QCE.SS* .GULf_ BALANCED
LICENSE TIME STATE MAKE MODEL
NUMBER
LOCATION: UNIVERSITY * BOUNDARY DATES
P29192
680GOC
iDZNeiOO
379HMW
GREATE
1 05JSX
OOJ977
UZA117
0~45 GXH"
BTJ-788
RQX803
WTK414
060HZL
5 54 CO A
YEAR DRIVING VEH. VEH.
_ HISTORY _ TANK TANK
- TEMP" "" p^£s
LEAK RVF GALL FILL TOT
CHECK FILL TIME NOZL
.1.130 CALIf CHEVY
1145 CALIF CHEVY
120Q" CALIF ""CHEVY"
12C5 CALIF DODGE
1215 CALIF VW
CAMPER
NOVA
WAGON" "
CHARGER
SEDAN
73
f REE ..2.6.0. 32
PARKEDG
„_.. _„__.___
73 LOCAL H
69 LOCAL 40
1215 CALl'F~"OLOSM03'frE OMEGT ~ "73~"~LO"CAT""5~
1220 .CALIF ..CHEVY SEDAN 56 LOCAL__l/_2
1225 CALIF CHRYSLER 300SEDAN 67 LOCAL 1 8«,
i23:o "CALIF""MAZOA " RXS-'WAGO 73 LOCAL" 1/2" ~oF
1235 MICH I CHEVY CHEVELLE 70 FREE 12 8_7
1245 CALIF DODGE OART 65 LOCAL 1/2 93
1250 CALIF DODGE "DART 68 LOCAL l""" SO
1250 CALIF DODGE CHARGER 73 LOCAL 1/2 93
1255 CALIF FORC PINTO 71 LOCAL 1 83
NO 15.
TIME
2:51
82 H .5 0.25 3
..„_
87
75
„_
82
NO 13.3 2:30 3:10
"NO T5T8" 3~:05 3:07
NP.......lf*-».q 2|5'3 3*J30_
NO 8.1 1:35 1:45
NO 16.3 2:55 3110
N-°__J>iZ _ _?_: 55 0:55
NO 5.7 l:CO 1:05
NO 13.1 1S45 1:47
NO 5.7 1117 U20
NO 10.5 2M5 2:20
NO 11.5 2:31 2S35
N.P..... 1 • g_ __0 s_55 0 ^5_5
NO 5.7 2:00 2JOO
o
-------
STATION! GULP
PROCESS! GULP BALANCED
LOCATION* UNIVERSITY
OOUNDARY
DATE: 6/i<»/7<»
LICENSE
NUMBER
{
TWAM+i
36-0699
1M12136
f
ZZW270
373COR
235JEG
OZV830
916CFV
6 32 AW.
V IX 957
KPP3**6
WJX321
RSS989
W8F<*2<»
TIME
1300
1305
1315
1330
1332
1335
13«»0
1<*00
1M5
1«*25
1<»3Q
1<»35
lk**Q
1<»50
STATE
CALIP
NE3RA
GAL
CAt
GAL
CAL
CAt
CAL
CALIF
CAL
CAL
CALIF
CAL
CAL
MAKE
PORO
FORD
CHEtf
CHEtf
VW
PLYM
CHEV
FORD
VW
CHEV
CHEV
FORO
CHEV
MERCURY
MOQFL
MUSTANG
GALAXIZ
PICKUP
IMP ALA
S/WAG
IMP ALA
TORINO
3US
COR
DELUX
MUSTANG
3ELAIR W
COUGAR
YEAR
70
70
56
66
66
72
6<*
71
61
65
ki
68
66
63
DRIVING
HISTORY
LOCAL 1
LOCAL 1
LOCAL 7
LOCAL 1/2
PREE 1/4
LOCAL 5
FREE 2k
FREE 35
PARKEOO
FREE 30
LOCAL 15
LOCAL 7
LOCAL 6
LOCAL 5
VEH.
TANK
TEMP
98
79
79
85
8>
8<»
95
93
78
79
79
90
85
88
VEH. LEAK RVF
TANK CHECK
PRES
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
GALL
FILL
10.0
16.1
3.8
9.5
8.«*
15.9
3.3
13.6
8.9
1.9
0.0
li,.2
6.
1.9
PILL
TIME
2t05
3:00
:50
i:<»5
1515
2J50
0:53
2J25
i:*»7
J35
1S55'
2:*,5
:tf5
:
-------
LOCATION: UNIVERSITY + BOUNDARY
DATE! 6/14/74
LICENSE TIME
NUMBER
77111R
756CYO
X NO 019
0233401
TV5029
VEP825
WIW853
XV0904
8C4GJD
624EOY
VES152
432GJH
RDJ199
XOR989
rr "
i
i
. so
1502
1500
1510
1520
1525
1540
1545
1555
1600
1640
1645
1310
1345
1350
STATE
CAL
CAL
CALIF
CALIF
CALIF
CAL
CAL
CAL
CAL
CAL
CAL
CAL
CALIF
CAL
HAKE
FORD
AMC
CHEV
FORO
DODGE
TOYOTA
VH
TOYOTA
CHEV
FORO
OOCGE
FORD
FONTIAC
PLYMOUTH
MOOEL
WALK-IN
JAVELIN
CHEVELLE
PINTO
270
BUG
CRONA
VEGA230Q
GALAXIE
QART
PINTO ST
LEMANS
VALIENT
YEAR DRIVING
HISTORY
65
7n
68
74
66
67
68
65
72
72
67
72
65
69
LOCAL .5
FREE 8
LOCAL 2
FREE 98
FREE 8
LOCAL 1
LOCAL 1
LOCAL .5
FREE 120
LOCAL 3
LOCAL .5
LOCAL 1/4
LOCAL 0.1
FREE 1Q
VEH. VEH. LFAK RVP
TANK TANK CHECK
TEMP PRES
37 NO
86
35
96
88
89
86
83
108
35
84
77
79
91
NO
NO
NO
8.4
NO
NO
NO
NO
NO
NO
NO
NO
NO
GALL PILL TOT
FILL TIME NOZL
• • , -'nti-MIE 'f:
8.9 l:4<» 1:55
8.8 U4Q 2125
10.7 It 55 3105
10.9 2J10 2:15
11.5 2:20 2:45
9.5 1J55 210
0.0 :45 145
3.8 1X15 1115
9. U45 2X20
16.0 3 t C 3 1 1 3
15.4 2!45 2:55
9.1 2SO 2:0
1.9 S23 0X20
3.8 «55 155
-------
STATION?
PROCESS* GULP 3ALANCEO
LOCATION: UNIVERSITY + BOUNDARY
DATE* 6/14/74
LICENSE
NUMBER
i
XVC286
093GFK
117KPH
OV9512
232GSN
KTR796
216KXG
EHY401
265KXL
870BML
225HQB
77263V
78059V
SMI 602
TIME
STATE
MAKE
MODEL
YEAR DRIVING VEH. VEH. LFAK RVP
HISTORY TANK TANK CHECK
GALL
FILL
PILL
TIME
TEMP PRES
1405
1410
1428
1425
1430
1445
1458
1515
1530
1533
1337
1542
1546
1555
CAL
CALIF
CALIF
PENNA
CALIF
CAL
CAL
VIRGI
CAL
CAL
CAL
CAL
CAL
PENN
MERCEDES
AMD
HONDA
CHEV
V*
PLY
FORD
CHEVY
DODGE
VH
BUICK
FORD
DODGE
CHEV
220SE
S/W
CIVIC
NOVA
KAMBACK
VALIANT
PINTO
VEGA WAG
DART
BUS
RIVIERA
FALCCN
VAN
NOVA
63
73
7<4
73
69
63
72
73
7i4
65
67
6Q
73
73
PREE
LOCAL
LOCAL
BOTH
LOCAL
STANOI
FREE
FREE
BOTH
FREE
FREE
LOCAL
LOCAL
FREE
85
1/t*
-------
.__-__ ?RPCESJJ__(^JL^_3ALANCEP LOCATION: UNIVERSITY + BOUNOARY DATEt 6
LICENSE TIME STATE MAKE MODEL YEAR DRIVING VEH. VEH. "LEAK RVP GALL PILL TOT
NUMBER _ __ HJ.STORY J_ANK TANK CHECK FILL TIME NOZL
I ' ----- - ----- - - - -- - -TEM-p >R-£s " " " ~ . TIME
IVH 7<* 16_P 5 C ALI P CHE tf IMPAL A 67 L 0 C A L ^ . _ _ 00 1<9 .J5 _ 3^30 3135
2818IJ 1625 CAL PLYMOUTH OUSTER 71 BOTH 6 88 -NO 9.6 1150 2J15
JKSUIQ28 ~~~1632 CAL MERCURY COMET 6«* LO'CAT'S 86 ~~ T/TTl 2*00 2HO
962GAP . __1650 CAL PpNTIAC LEMANS 68 LOCAL 2 90 NO 15. f» 2t3H 2SW5
TXG511 16<»5 CAL CHEtf IMP ALA 67 FREE ? Ill NO 5.7 HO HO
o ——.- - - ... -. - ._ ..-. ... ._ ____
i
ro
o •
-------
STATION! STANDARD PROCESS: STANDARD BALANCED
LOCATION: BALTIMORE * LAKE MURRAY DATE* &/17/7V
LICENSE TIME
NUMBER
449JEL 1003
44763S 1006
J359KZC 1100
918KKL 1150
730HNF 1220
89046N 1230
HSU778 1350
932HWN 1400
:XXX 1450
574KMK 1610
2D5JRT 1615
694HDP 1648
15874V G905
STATE
CAL
CAL
CAL
GALIF
CALIF
CALIF
CALIF
CALIF
GALIF
CAL
GALIF
CALIF
MAKE
CHEtf
VM
OLDS
PLYMOUTH
FORD
VW
FORD
FORD
OLDSM03ILE
CHEV
FORD
OAT3UN
MODEL
VEGA SW
BUS
CUTLASS
FURY II
CAPRI
SEDAN
WAGON
KARMANNG
CAPRI
DELTA 88
HONTE CA
CAPRI
1600PICK
YEAR DRIVING VEH. VEH. LEAK RVP
HISTORY TANK TANK CHECK
73
60
7k
73
72
68
73
73
7k
7k
7k
73
73
LOCAL
LOCAL
FREE
FREE
LOCAL
LOCAL
LOCAL
LOCAL
FREE
FREE
FREE
LOCAL
LOCAL
TEMP PRES
10 82
i/t
25
15
1/4
6
1/2
3
11
10
118
k
k
68
88
78 .6 .3
90
30
88 2.5 1.5
77
90 .75 .30
100 .70 .30
96
9B
72
NO
NO
NO
.3 8.5
NO
NO
3 8.*
NO
3 NO
3 8.2
NO
NO
NO
GALL
FILL
5.1
19.8
ZC.k
10.3
22.5
8.5
10.0
3.5
3.5
7.5
9.5
8.2
FILL
TIME
noa
*55
2**»5
1*45
3 :«i'5'
1*30
833
*30
1*15
1:50
2*05
1*32
TOT
NOZL
1*25
1*0
3*00 -
V*15
1*55
VM5
H50
»45
1*45
2*30
U3?
o
i
ro
-------
STATIONS STANOARO PROCESS* STANDARD BALANCED
LOCATION: BALTIMORE
LAKE MURRAY OATEI
LICENSE
NU MBE R
292GOZ
5,5HTC
,570CYH
V 28 979
786KXO
012JOH
VNX<»30
315KZ8
519KZE
DUL602
ZQM799
5 90 BAG
675EAU
223LKY
o
i
ro
fNJ .
TIME
STATE
MAKE
MODEL
YEAR DRIVING VEH. VEH. LFAK RVF
HISTORY TANK TANK CHECK
GALL
FILL
FILL
TIMT
TEMP PRES
0930
1000
1005
1125
1155
1210
1315
13*5
1^20
1<*35
1510
15<»5
1550
1555
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CHEV
CALIF
CALIF
CALIF
CALIF
CAIF
FORD
PLYMOUTH
CHEVY
CHEVROLET
CHEVROLET
FORO
VH
FORD
CHEVROLET
FORD
FORD
CAPRI
CHEVROLET
CHEVROLET
PINTO
SATELLIT
IMP ALA
PICKUP
IMP ALA
PINTO
SEDAN
CUSTOM
3EAUVILL
FAIRLANE
FAIRLANE
CAPRI
CAPRICE
CHEVtLLE
72
73
62
67
7k
73
67
68
7U
65
69
71
71
71
LOCAL .5
FREE IOC
LOCAL 10
LOCAL 2
FREE 6
FREE 25
LOCAL 3
LOCAL 5
LOCAL 2 *~
FREE 30
FREE 10
FREE 20
LOCAL 1.5
LOCAL .5
77
93
75
76
»»
91
80
82
00
95
33
35
33
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
5.2
17.1*
17.8
5.2
16.7
5.2
7.7
19.it
17.2
1.7
10.0
9.9
19.5
5.2
it 03
3:CQ
3:10
JL«*5_
2:52
0555
1J25
3:25
3:10
OS15
1115
1:55
3:10
G :57
TOT
NOZL
TIME
1:00
3t55
UtOO
!Ur5
2:52
OJ55
1:25
3S33
3:15
0515
1115
?:<*5
3:15
1*00
—
-------
STATION? STANDARD PROCESS: STANDARD BALANCED .... LOCATION: BALTIMORE * LAKE MURRAY DATES 6/17/7?*
LICENSE TIME STATE MAKE MODEL YEAR DRIVING VEH. \/EH. LEAK RVF GALL FILL TOT
NUMBER HISTORY TANK TANK CHECK FILL TIME NOZL
i
TEMP PRES TIME
295KQQ . 16^5_J?_ALI.P._CHO.!?PMI...-SFQ.RTyANI 7J» FREE !_.._ Q.0.__._._ NO 12.9 2t23 2:30
o
i
ro
-------
STATION! STANDARD ' PROCESS* STANOARO BALANCED LOCATION: BALTIMORE * LAKE MURRAY DATE! 6/18/7**
LICENSE
NUMBER
TIME
STATE
MAKE
MODEL
YEAR DRIVING VEH. VFH.
HISTORY TANK TANK
LEAK RVP
CHECK
GALL
PILL
FILL
TIME
I TEMP PRES
597DWY
915HWP
751GGX
427KQR
172FVP
031H01
074KQ5
679GTH
903KLW
6 78 GUP
5 72 FFR
082 JDK
311JLE
723HFP
o '
ro
•P-
0745
0810
0845
0845
0855
C905
0915
0920
1235
1230
1345
IdOO
1410
1415
CALIF
CALIF
GALTF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
I
CALIF
CALIF
CALIF
TOYOTA
DODGE
PONTIAC
CHEVROLET
FORD
FORD
FORD
CHEVROLET
CHEVROLET
FORD
FORD
CHEVROLET
FORD
FORD
CORONA
CORONET
CATALINA
IMPALA
PINTO
GALAXIE
PINTO
CAPRICE
MALI3U
PINTO
CUSTOM
MONTE CA
TORINO
LTD
72
7k
73
73
72
73
73
73
74
71
72
73
73
73
LOCAL
LOCAL
LOCAL
LOCAL
LOCAL
LOCAL
LOCAL
LOCAL
FREE
LOCAL
FREE
LOCAL
LOCAL
FREE
ft
.5
1.
1.
1
10
2
.25
10
2
20
10
20
10
72
63
66
69
63
79
76
70
37
85
33
88
99
89
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
8.6
NO
NO
3 NO
10.0
18.5
17.6
2C.8
6.1
18.5
9.7
20.2
4.3
7.2
9.8
8.6
15.2
8.6
2145
3!1!3
3:05
3:45
i:05
3:15
2140
3:20
CS45
1«10
1:55
1J42
3t20
1:37
TOT
NOZL
TIME
4100
3t2T
413
4:39
2:01
3J25
3:00
3:45
2:10
3:35
2 130
4*42
1:40
3:15
-------
STATION? STANQARO PROCESS* STANDARD BALANCED
TIME STATE MAKE MODEL
LOCATION: BALTIMORE * LAKE MURRAY DATES 6/is/7<»
LICENSE
NU MBE R
ZN3_26
-------
. ST ATIO N : _SJMPA?P_
LICENSE TIME STATE
NUMBER
PROCESS: STANDARD BALANCED
MAKE MODEL
LOCATION! BALTIMORE + LAKE MURRAY DATE* 6/19/7*,
YEAR DRIVING VEH.
HISTORY TANK
0388293
170FTO
f842GOZ" ~
645 KZR
603ESM
T99CQQ
NpZ707
545HTC
T03AFM'""
239CTy
Gil 57827
260KZE"
«* 05 JYC
3C2JQU
A*!»5__.Q*Jr.?f_.'l?.?D__
0715 CALIF MAZDA
VAN
C730 CALIF MAZDA
0800 CALIF MERCURY
0855 CALIF VW
RX2
MONTEGO
BUG
73
"72"
1*
70
TEMP
LOi C AJL J. 0 pj_
LOCAL 1 62
VEH.
JTANK_
PRES
LEAK RVP GALL FILL TOT
CHECK FILL TIME NOZL
LOCAL 1/8
LOCAL 1.5
LOCAL 1
00
67
70
0925 CALIF CHEVROLET CAPRICE
1030 CALIF DODGE DART
69
65
LOCAL .5
LOCAL .5
SATELLIT 73
BUG " 70""
FURY I 71
LOCAL 1
FREE 10
1335 CALIF PLYMOUTH SATELLIT 73 FREE 125
"i4oir~ cTriT~vw
_i^50. c_*LLF_!M 1PJJJH
0630 GOVT A M C MATADOR 71 LOCAL 10
"0655 CALIF"Ob"DGE " "VATN 71 "TOCAT 75""
0657 CALIF CHEVROLET IMP ALA _74_ __ FREE: 15
0745 CALIF DODGE VAN 73 LOCAL .25
71
J?JL
96
95
A8___-.rl_i?_5_
66
Tl~
74 .8.5
60
NO 16.8 2t50 3J
NO 9.5
2S
2:15
NO 14.5 3:30 3»30
JiP.__ 13 • 5 3:10 3:23
NO 9.5 1:35 2tl5
NO 5.2 1:30 1:33
NO 11.3 1:55 2:05
NO 15.0 2t35 3:15
9.2 1:30 1
NO 12.3 2:15 2:25
NO
2:30 2:55
NO 8.6 2:30 2:35
YES 17.5 3:20 4t20
NO 16.7 3tQO 3:05
O"
',-j
i
ro
-------
STATIONI STANDARD PROCESS* STANDARD BALANCED
LOCATION: BALTIMORE + LAKE MURRAY DATE: 6/19/7%
LICENSE
NUMBER
TIME STATE
MAKE
MODEL YEAR DRIVING V£H.
HIS_TORY_ _TANK
- "~ " " "TEHP"
VEH.
TANK
LEAK RVP GALL FILL TOT
CHECK fJLkk_ TIME NIOZ'L
T.IME
NO 12.1 2:10 2:15
P-RES
'fA2_55& 073 0 .C.A_L_IF___CHE.VR 0_L E..T.. PJjCKUJ3 ..61 L OCA L .___. _1_C _______ 58 _______ __________ _____________ NO 15.9 2*55 3tQO
5^5JSK 0735 CALI^ FONTIAC ^IREBIRO 73 LOCAL .25 69
i6~03GB? 0750 CALIF FORD fORINO 72 FREE 3 77 T.l~~9 2~
0.38KQR ________ 0815. ..CAL.IF pATSUN_ 2602 7^ LOCAL. 1 00
UUP088 0830 CALIF MERCURY NONTERY 67 LOCAL .75 66
'V38JUA 08'35""~CATlF~DOO'GE CORONET 73 LOCAIL~3 6T .~f>~~~'.l* 2 T7? 7.5 H30 1:35
:9 99 HGP _________ fl 9 1_5 _____ C IjftJL LFJFORQ _________________ TORI N_Q _________ 7J ________ fJR EE ____ 13_0_ .^A..._^_? __ _•.!_ _________ N0 7«0 i:3° 3t0n
338JQN 0935 CALIF CADILLAC OE VILLE 73 LOCAL .5 70
:9T7~KES~~ ~"093"0 cTLlTToRO" ....... HU'STANG 7^ FRET~~8 7A 3 0 2™
122JQV
1 05HOT
RKP800
8.0 5.2 0»42 Ot55
NO 10.1 2J_55_2_I_55_
NO 1C.5
NO 12.6 2:00 2H»5
8.6 7.3 1«35 2*00
NO 12.0 2:00 2«3Q
1035 CALIF CADILLAC SEDAN 73 FREE 115 90 +.7 +.2 2
iO'55~" CALIF ^^ blOSWMill^CUf LASS" "T3~" "FRlEE 10 ..... " "97~*75~0"" ...... 2~
1125 ARIZ CHEVROLET VEGA 71 _LOCAL 3 30
1155 CALIF DODGE CHARGER 73 LOCAL .5 77
NO 1C.O 2tt,5 3SOO
NO 16.0 2:45 3:00
...HP.. A».5. ._._i J.o^...l!H.
NO 8.6 1:35 U^O
o
ro
-------
STATION! STANDARD
PROCESS* STANDARD BALANCED
LOCATION: BALTIMORE * LAKE MURRAY DATEI 6/19/7^
LICENSE
NU MBE R
PHP 979
uNPea,
033KZ3
9fc
-------
STATION! TEXACO
PROCESS: ENVIRONICS
LOCATION: BALTIMORE + FLETCHER
DATES 6/20 ATI*
LICENSE
NUMBER
f
651BEB
12<»ELL
[623HTS
PWA68<*
THE7K
*»6825L
WYM088
WJU<*56
:770KLB
305HOS
WSC130
STEAM2
MW1510
93353G
••• o •
i
ro
VC
TIME
STATE
MAKE
MODEL
YEAR DRIVING VEH. VEH. LEAK RVF GALL FILL
HISTORY TANK TANK CHECK FILL TIME
TOT
NOZL
TEMP PRES TIHE ; v
1COO
m,
11<»0
1200
1208
1226
1510
1520
0(f08
GM5
C520
0537
1000
1015
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CONN
CALIF
VW
CLDS
CHEV
VW
BUICK
DATSUN
VW
CHEVROLET
MERCEDES
CLDSMOBILE
FORD
CHEV
AMC
DODGE
BUG
CUTLASS
H CARLO
BUG
S WAGON
PICK-UP
S WAGON
C WAGON
U50SE
CUTLASS
LTD
LUV
HORNET
CARRYALL
68
72
73
66
73
7k
68
68
7k
73
68
7k
70
FREE
LOCAL
LOCAL
LOCAL
LOCAL
LOCAL
FREE
LOCAL
FREE
LOCAL
LOCAL
FREE
FREE
LOCAL
k
i
i
2
1/16
1/16
100
5
12 C
1/2
1/2
10
k
.25
80
78
81
73
79
30
82
90
86
92
83
37
79
78
NO 3.6 :30
NO 15.0 2:00
NO 3.6 :30
6.3 ItOO
12. k 1:53
1.8 OU5
NO 1.8 :i*
NO 15.0 3:25
NO 17.9 2*20
19.7 2!«*5
3.6 1 :4»
-------
STATION* TEXACO
PROCESS* ENVIRONICS
LOCATION! BALTIMORE + FLETCHER
DATE! 6/20/74
LICENSE
NUMBER
!
314GXE
PH8110
;662FZG
3 84 KLQ
77458U
DYN439
5 30 13L
5 71 HOT
496JQS
14382R
37778W
UKW764
ZXM782
9 63 GOY
TIME
1050
1055
1100
1105
1115
1125
1130
1135
1135
1145
1200
1215
1307
1310
STATE
CALIF
C.LI,
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
GALIF
MAKE
MERCURY
CHEVROLET
FORO
BUICK
CHEVROLET
VW
CHEVROLET
DODGE
MERCURY
CHEVROLET
CHEVROLET
VH
FORO
FORO
MODEL
MONTEGO
CUSTOM
APOLLO
LUV
BUG
EL CAMIN
OART
MONTEGO
CAMPER
LUV
WAGON
FALCON
PINTO
YEAR DRIVING VEH. VEH. LEAK RVP
HISTORY TANK TANK CHECK
73
61
72
73
72
72
73
70
74
67
69
72
LOCAL
LOCAL
FREE
FREE
FREE
LOCAL
LOCAL
LOCAL
FREE
LOCAL
LOCAL
LOCAL
LOCAL
FREE
TEMP -PRES
7 79
1
10G
8
12
10
4
1
5
1.0
1.5
15
.25
4
73
90
107
92
32
95
79
39
76
96
86
32
9U
NO
NO
8.2
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
GALL
FILL
18.4
3.6
12.3
3.6
5.4
8.8
8.9
11.7
3.6
17.3
3.6
8.4
1Q.2
11.6
FILL
TIME
2*52
.2,
2*04
0*25
0*35
S55
2*15
0*40
2*45
0*30
1:25
1*35
2:40
TOT
NOZL
3*10
135
0135
0*45
2*00
1*43
3*05
0*5(1
3*20
0*40
1*37
2*08
3tOO
o
-------
STATION: TEXACO
PROCESS* ENVIRONICS
LOCATION: BALTIMORE * FLETCHER
DATE: 6/2c/7if
LICENSE
NUMBER
TIME
STATE
MAKE
MODEL
YEAR
DRIVING VEH. VtH. LEAK RVP
HISTORY TANK TANK CHECK
GALL
FILL
FILL
TIME
j TEMP PRES
:973JQP
FPN866
j23«.HKK
716KPH
74«»GOX
760BSB
«*<»<» JLC
SNP596
<»75KLX
*6287P
726FVX
785JLA
TAM267
AZV
-------
ST AT I_0_NI_I P.** C 0 PR pC ES.S»_EN VI; R ON IC S
LOCATION? BALTIMORE + FLETCHER
DATE: 6/20/7**
LICENSE
NU MBE R
KOW8Q8
17662T
20263T
<»OOJSJ
W AC 301
TC8765
.710KLT
7 31 ELS
3980LD
Q81070
VNVO*»9
KGS913
TIME
625
1630
1635
1655
1705
1707
1713
1720
1725
1730
1753
STATE
p
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
CALIF
?1ICH
MAKE
LET
CHEVROLET
CHEVROLET
FORO
CLOS
FORO
CHEVROLET
FORO
FORO
DART
OLOS
MODEL
3ELAIR
LOVE
LUV
LTD
*«
PINTO
CHEVELLE
PINTO
PICKUP
GT
DELTA 38
VEAR
DRIVING VEH. VEH. LEAK RVP
HISTORV TANK TANK CHECK
TEMP PRES
5k LOCAL .5 86
72
73
68
6«.
62
71
56
69
7G
FREE 15
FREE ••:.:;;
»15 *25
:*»0 S55
J50 IS 05
»25 135
:32 i:00
» C 0 1 s Q 0
S35 J<*5
1:30 2»QO
:25 t30
:*t5 S55
2:22 2:50
:50 1!25
o
i
CO
-------
STATION* UNION 76 PROCESS* PROCESS PRODUCTS
LOCATION: WARING + ZION
OATEt 6/2A/7
-------
STATION! UNION 76
PROCESS* PROCESS PRODUCTS
LOCATION: WARING * ZION
DATE:
LICENSE
NUMBER
W55CTV
731«*6W
H YL
-------
APPENDIX C-2
FIELD DATA, PAGE 2 OF 2
C-2
-------
QNJ._.ST_ AN_D_AR0___£ROCJESSl_J NTERMARK .1= OCAlIOJNt_CAR MEL...VALLEY » 15
DATES 6/ 6/7t>
LICENSE
NU MBE R
NOZZ EXPL.
FIT VALUE
SPIT AMOUNT
BACK
VAP.
TEMP
LIQ.
VAPOR VAPOR VAP. VAP.
VOLUM VOLUM CONC RET.
; AFTER BEFORE
9 32 HWN
080EAT
I242CTX
E63097<»
:55865F
874FLS
C9809
'OSgKFQ
VCL4<»6
YYG563
GQP810
60969
o
ro
GOOO 0
G003 0
G003 .1
GOOO >1.0
GOOD .05
BAD 1
GOOO .1
GOOD 0
GOO a o
SOME SLIPPAGE 0
GOOO 0
BAD >1
BAD >1
GOOO C
NO
NO
NO
/YES IC.C.
NO
YES 3IG.AMT.
NO
NO
NO
YES
NO
NO
YES
NO
61
62
63
.6.3
70
68
70
69
66
68
68
65
67
6
-------
STATION? STANDARD
PROCESS* INTERMARK
LOCATION! CARMEL VALLEY
15
DATES 6/ 6/74
LICENSE
NUMBER
96695E
XYV086
IR27816
TUCKIE
950DVE
VWA636
026BHA
248ACV
588YHU
029ESQ
2LX232
838GOA
830HPA
651CVR
o
ro
i
ro
NOZZ
FIT
FAIR
GOOD
POOR
GOOD
GOOD
POOR
GOOD
GOOO
GOOD
GOOO
POOR
GOOO
GOOD
G003
EXPL. SPIT AMOUNT
VALUE BACK
>i YES SLIGHT
0
>1 YES 100CC
0 NO
0
.2 NO
a YES 2cc
C NO
0 NO
0 NO
.2
0 NO
0 NO
C NO
VAP.
TEMP
64
68
63
63
64
61
63
64
65
65
64
67
68
65
LIQ.
TEMP
75
75
75
7.5..
75
7*t
75
75
75
75
75
75
75
75
VAPOR
VOLUM
.AFTER
312.7
317.2
321.9
._.3.?_2.*r
326.3
327.6
332.5
333.1
339.2
3«»1,6
3<»5.C
3**8.8
351.9
35<».7
VAPOR
VOLUM
BEFORE
308.
313.2
317.7
321.
322.9
326.3
328.2
332.
335.6
339.3
3<*1.7
3<«5.3
1<»8.9
351.9
VAP.
CONC
7 63
64
64
6C
60
57
58
58
64
64
58
64
70
62
VAP.
RET.
PRES .- .-•_••. ;.,••:.;•• ::
-11.0
-11.0
-10.5
__^_1 1.0
-13.0
-15.0
-13.0
-14.0
-11.0
-1G.5
-10.0
-1C. 5
-16. H
-15. G
-------
STATION: STANOARO
PROCESS* INTERMARK
LOCATION: CARMEL VALLEY «• is
DATE: &/ 6/71*
LICENSE NOZZ
NU MBE R FIT
829360 GOO 3
90208T GO 0:1
I73438M GOOD
18354V GOO J
H MX 668 POOR
XDU752 GOO'i
296K6I . GOO a
SKE220 POO^
'4152 Fftl*
.4152 6003
186LEC GOOD
CUO 923 GO 01
TC528697 POO ;
EXPL. SPIT AMOUNT VAP. LIQ. VAPOR VAPOR
VALUE BACK TEMP TEMP VOLUM VOLUH
0 NO 65
0 NO 64
0 NO 63
NO 64
1.0 NO 62
0 NO 65
0 1TES 2CC 64
>1 VES 50CC 63
0 YES 25CC 64
0 VES 25CC 63
0 NO 62
0 NO 63
.1 64
AFTER BEFORE
75 358.6 354.
75 362.6 358.8
75 366.0 362.8
75 369.0 366.2
75 371.6 369.2
75 375.2 371.8
75 382.1 375.3
75 385. 382.2
75 391.8 385.6
75 399.7 391.9
75 402.6 399.8
75 410 4 407 0
75 413.3 410.6
VAP.
CONG
.»
60
63
60
62
66
58
60
59
62
6C
67
59
57
VAP.
RET.
PRES . -.,;-,:;;;:;V^;:;
-9.5
-10.5
-11. fl . '-. ^'•'•,.:^.
-13.0
-11.0
-10.5
-15.0
-14.5
-15.0 . :.•'.,,;: :;:-'
-10. 0
-11.0
-15. n
-14.0
o
rss
co . .
-------
STATION! STANDARD PROCESS* INTERMARK
LOCATIONS CARMEL VALLEY «• 15
DATEt 5/ 6/74
LICENSE
NUMBER
406DKA
228BQ1
i *» A A ^/.Q Q £.
3 72 KLS
D2T709
'447DKC
XUV484
016JRX
!Z~NQ264
0
ro
I
NOZZ
FIT
GOOD
GOOD
C A T D
7 AJL K
GOOD
FAIR
GOOD
GOOD
GOOD
GOOD
EXPL. SPIT AMOUNT VAP. LIQ. VAPOR
VALUE BACK TEMP TEMP VOLUM
AFTER
0 NO 64 75 416.4
0 NO 62 75 420.8
flC _ ___ _________ f,7 ~? d liOl K.
Q NO 64 75 426.1
.4-. 6 NO 64 75 431.6
0 NO 62 75 434.7
0 NO 62 75 438.3
.1 NO 6^ 75 443.4
0 NO 62 75 447.4
VAPOR VAP. VAP.
VOLUM CONC RFT.
BEFORE PRES ^ -'/..•/> "\?r;n :ff:
413.5 61 -15.0
416.4 62 -11.0
HcU«U oU ^S^y^yjj . • . • .:
423.8 59 -18.5
426.2 60 -15.7
431.8 57 -15.7
434.8 60 -12.0
438.4 58 -15.0
443.6 60 99999
-------
STATION* UNION 76 PROCESS* PROCESS PRODUCTS
LOCATION: WARING + ZION
DATEI 6/11/74
LICENSE NOZZ
NUMBER FIT
EXPL.
VALUE
SPIT AMOUNT
SACK
VAP. LIQ.
TEMP TEMP
VAPOR VAPOR VAP. VAP.
VOLUM VOLUM CONG RET.
; . AFTER BEFORE
ZMR401
079EQU
!18116R
937JFS
672GXG
774JEL
0 41 GOA
T GT 771
862JQT
;422HOS
738JLA
072FKX
689ESK
613KAC
GOOD
GOOO
GOOO
FAIR
GOOD
GOOD
GOOD
GOOD
GOOO
POOR
GOOO
N. A.
GOOD
0
0
0
.1
0
0
0
0
0
.2
0
N.A.
C
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
74
76
80
79
82
82
82
84
85
85
80
32
82
84
75
77
77
77
79
79
73
73
78
78
77
77
77
78
719.
722.
724.
728.
730.
733.
734.
I
736.
738.
740.
741.
742.
745.
2
2
%
08
85
18
30
40
63
46
70
92
23
717.6
719.2
722.2
726.20
728.08
733.85
733.2
734.30
736.40
738.88
740.46
741.70
742.92
37
41
43
45
47
53
41
32
43
41
40
43
34
37
PRES
-1
-1
-4
-4
-6
-4
-4
-3
-1
-7
-3
-3
-1
-8
.5.
.4
.3 ..-•V\V'-^:T.--V
.0
.5
.'8 . • •/ ,
.3
.1
.6
.0
• 8 .
.5
0.0
.0
r»
-------
, STATION* UNION 76 PROCESS* PROCESS PRODUCTS
LOCATION: WARING > ZION
DATE! 6/ll/7i»
LICENSE NOZZ EXPL.
NUMBER FIT VALUE
i
! •
«r'3 20t» U POOR H/H .2
799JEH BAD H/H 1.0*
:RJP777 GOOD H/H .1
(»50ETV GOOO 0
059GJX GOOO 0
299HWV GOOD 0
211FYZ GOOO .6
WLN696 GOOD H/H 0
W8F900 GOOO H/H .1
1DDLR1221 GOOO 0
137GXA GOOO 0
o
ro
i
Ol
SPIT AMOUNT VAP. LIQ. VAPOR VAPOR VAP. VAP.
BACK TEMP TEMP VOLUM VOLUM CONC RET.
AFTER 3ECOR£ PRES . ;^
NO 93 78 7^6.8^ 7^5.28 3
-------
STATIONS GULF
PROCESSI GULF BALANCED
LO CAIIQNt UNIVERSITY * BOUNDARY DATE: 6/12/7*
i
i
il
7
1
7
6
JT
3
0
,9
K
1
2
2
LICENSE
NUMBER
NOZZ
FIT
EXPL. SPIT AMOUNT
VALUE BACK
VAP.
TEMP
LIQ.
TEMF
VAPOR VAPOR '
VOLUM VOLUM
AFTER BEFORE
0
-------
STATIONS GULF
PROCESS? GULF BALANCED
LOCATION: UNIVERSITY + BOUNDARY DATE: 6/12/74
LICENSE
NU MBE R
NOZZ
FIT
EXPL.
VALUE
SPIT AMOUNT
BACK
VAP.
TEMP
LIQ.
TEMP
VAPOR VAPOR
VOLUM VOLUM
VAP. VAP.
CONC RF.T.
j AFTER BEFORE
; .
60421F
446JEC
J526GGC
236KLM
1C1ASI
:653F8X
;ZQ0792
V 297M.
R GO 594
86394E
689DLX
550KPG
611GGS
148HDT
POOR
BAD
GOOD
GOOD H/H
BAD
GOOD
BAD
GOOD
GOOD
GOOD
BAD
BAD H/H
GOOD
BAD
1.0 +
.1
1.0
0
1.0 +
OT0.2
1.0
0
0
0
1.0>
1.9 +
0
1.0 +
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
0
0
0
0
Q
0
0
0
0
0
0
0
0
G
72
72
72
76
7k
80
72
72
76
7 . ..•:*••/:$
60 + .3
63 .2
62 .4
72 .3
49 +.2
69 +.30
70 + .3
63 + . 3
63 +.4
63 + . 2
63 + . 5
67 C
65 +.3
65 +.15
o
ro
00 . .
-------
STATION! GULP
PROCESS! GULF BALANCED LOCATION: UNIVERSITY * BOUNDARY DATES 6/12/7^
LICENSE NOZZ EXPL. SPIT AMOUNT VAP. LIQ. VAPOR VAPOR VAP. VAF.
NUMBER FJJ __yAk.U§ 3ACK TEMP JEMP_ VOLUM VOLUM CONC RET.
I "~ ~ " ~ ~" " " "~ ~ AFTER "BEFORE" PRES
;37t»98M ..__BA.PJH/H 1.0 * NOI 3 70 75 .751.66 760^^0 67 ±*2_,
159KZQ BAD H/H 1.0* NO C 70 75 761.60 761.66 67 +.18
o
ro
i
vo
-------
STATIONS GULF
PROCESS* GULF BALANCED
LOCATION: UNIVERSITY * BOUNDARY DATE? 6/13/71*
Q
7
LICENSE
NU MBE R
72787
6784L
S105HOT
93229G
Q.MV785
7
T
5«,KLS
ET243
9 99 OUH
KUL605
909JSZ
k
3
6
T
5230L
76DFJ
63KHH
XG71<»
o
ro
NOZZ
FIT
FAIR
GOOD HANDHELD
GOOD HANDHELD
GOOD HANDHELD
FAIR
POOR HANDHELD
FAIR HANDHELD
FAIR HANDHELD
FAIR HANDHELD
POOR HANDHELD
N.D.
POOR
POOR HANDHELD
-• •- -- ••
EXPL. SPIT
VALUE BACK
1.0 NO
0 NO
0 NO
0 NO
N.D. NO
1.0 NO
1.0 NO
.5 NO
1.0 YES
1.0+ NO
l.Ofr NO
YES
1.0 NO
1.0* NO
AMOUNT VAP.
TEMP
72
72
72
72
72
72
72
72
50 ML. 72
72
72
SCC 72
72
72
LIQ.
TEHP
78
7k
7t*
7k
7k
7k
7k
7k
7k
7k
7k
7k
7k
76
VAPOR VAPOR VAP.
VOLUM VOLUM CONC
AFTER BEFORE
771.13 770.92
771
772
773
77k
775
776
777
778
778
779
750
731
781
.78
.52
. 6k
kk
32
12
i»9
37
96
89
2Q
40
62
62
67
67
62
63
62
63
66
67
6?
63
66
65
VAP.
RET.
PRES •-.- •;•;.:
+ .20
+ .25
+ .23
+ .17
+ .17
+ .!<»
+ .25
+ .28
+ .2V
+ .18
+ .UO
+ .1
+ .2<*
+ .18
-------
PRPCESSa_GULf_BAj.ANCEQ; LOCATION* UNIVERSITY + "BOUNDARY DATE* 6/13/7<+
LICENSE
NU M8E R
i
OUM753
0238796
J735GOW
2 88 BEX
VEU721
;U««0716
8776<»N
122DFK
2**7ADR
TTF-876
585GBT
XTL389
89461L
OZT057
NOZZ
FIT
EXPL.
VALUE
SPIT AHOUNT
3ACK
VAP.
TEMP
LIQ.
TEMP
VAPOR VAPOR
VOL'JM VOLUH
AFTER
PAIR HANDHELD
FAIR
POOR
GOOD
FAIR
GOOD
FAIR
GOOD
GOOD
FAIR
GOOD HANDHELD
CORCED HANDHELD
POOR HANDHELD
POOR
1.0*
1.0*
•1
1.0
c
1.0*
0
.3
1.0
.1
.95
1.0
1.0 +
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO F£W DROPS
NO
NO
NO
NO
75
72
68
73
73
73
73
73
75
75
75
75
75
75
76
"•
7k
7k
75
7k
7k
75
7k
7k
7k
7k
7k
7k
782
782
784
785
786
786
788
788
790
792
792
793
793
793
.00
.96
.22
.11
.55
.37
.12
.3*
.<*3
.20
.50
.95
.80
.85
VAP. VAP.
CONG RET.
BEFORE
781.
782.
7dk.
7Sk.
785.
786.
736.
788.
789.
790.
792.
792.
793.
793.
90
00
12
22
11
55
37
12
9*»
<*6
20
k?
80
80
63
63
63
67
63
65
65
62
65
65
65
~63~
63
63
PRES ; ..;.•••
+ .18
+ .20
0 •'•/' ':•':••••'".;.•
+ .23
+ .18
-.2
+ .30
+ .1
+ .!*»
+ .11
..»
+ .3
+ .1
C
ro
i
-------
STATION* GULF
PROCESS! GULF BALANCED
LOCATION: UNIVERSITY + BOUNDARY
DATEl 6/13/74
LICENSE NOZZ
NUMBER FIT
86467P
728PEA
;TST284
H 54 055
7 41 OZE
534BXV
743CTT
7350QK
1C3AFO
587KAC
T AA480
0 49 DZN
378GNZ
508KHV
o
ro
GOOD
FORCED FIT
NONE
BAD
BAD
BAD
FAIR
GOOD
GOOD
BAD H/H
BAD H/H
BAD H/H
GOOD
BAD
EXPL.
VALUE
0
0
1.0 +
1.0 +
1.0 +
1.0 +
1.0
1.0 +
0.3
1.0
0
1.3 +
0
1.0
SPIT
BACK
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
AMOUNT
0
o_
Q
0
Q
0
0
Q
0
0
0
VAP. LIQ.
TEMP TEMP
75
75
78
77
76
76
75
75
75
75
75
73
76
73
• - - -
7«t
74
76
76
76
75
7k
7k
75
7k
75
75
7k
7k
VAPOR
VOLUM
VAPOR VAP. VAP.
VOLUM CONC RET.
AFTER BEFORE
795. 7k 793. Bk
798.
320.
321.
321.
322.
322.
323.
32k.
325.
326.
327.
332.
332.
01
1
90
90
18
bk
28
52
00
3k
22
2
6
797.03
320.0
320.15
321.90
321.90
322.18
322. 6
-------
.S.LATIONJ....G.ULF PR.Q.CE.SS..:.._GU.LF,_BA;JLANCEO__.._ .._ .LOCATION.!! UNIVERSITY + BOUNDARY DATE* 6/13/74
3
5
LICENSE
NUMBER
89CF.C
8278S
ZROLR2733
VNM013
P
UA053
962GAP
,226470
0
1
2
ZN598
11 KLP
86KPH
RBA634
4
L
1
69HDR
ZA573
40EA\/
O •"
ro
NOZZ 6XPL.
FIT VALUE
GOOD 7
GOOD 0
GOOD H/H 0
3AO 1.0
PAIR .9
GOOD C
GOOD 1.0+
POOR 1.0
GOOD 0
BAD 1.0
BAD 1.0+
BAD 1.0+
POOR 1.0+
GOOD H/H 0
SPIT AMOUNT
BACK
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
C
a
0
0
0
a
0
0
0
0
Q
0
VAP.
TEMP
73
73
77
76
78
74
75
81
75
76
73
75
76
LIQ. VAPOR VAPOR VAP.
TEMP VOLUM VOLUM CONC
AFTER BEFORE
74 333.45 332.60
74 334.
74 334.
74 335.
74 335.
74 338.
74 339.
74 341.
74 341.
75 342.
74 342.
. 7V.. 3.f»2.
75 343.
OP
36
10
14
18
90
72
80
74
75
75
92
333.
334.
334.
335.
335.
339.
340.
341.
342.
342.
342.
342.
45
00
?o.
36
in
14
32
00
72
34
74
75
75
60
61
60
62
70
63
J68_
77
72
76
76
77
75
77
VAP.
RET.
PRES ' .; -: :•:•• - a-
+ . 4
+ .3
+ .2
+ .1
+ .5
-.1
+ .5
+ .1
+ .2
+ .1
-0.0
-.1
P
+ .5
-------
STATION: GULF
PROCESS! GULP BALANCED
LOCATION* UNIVERSITY * BOUNDARY
DATE* 6/13/7t»
LICENSE
NUMBER
l
48457M
WRY 045
228KZC
206ANU
46729P
;VSL427
NOZZ
FIT
GOOD H/H
POOR
POOR
POOR
HAND HELD.
PAIR
FAIR
EXPL. SPIT AMOUNT
VALUE 3ACK
0
1
1
1
1
1
1
.0
.0 +
.0
.0
.0
NO 0
NO 0
YES 10CC
NO
NO
NO
NO
VAP.
TEMP
76
73
00
66
72
72
72
LIQ.
TEMP
75
7k
70
71
7k
76
76
VAPOR VAPOR
VOLUM VOLUM
VAP. VAP.
CONC RET.
AFTER BEFORE
346.10 343.92
346.14
768.58
763.28
768.40
769.06
769. <«C
346.
768.
768.
768.
768.
769.
10
60
24
30
40
06
76 +.3
74 +.1
46 0 •;- ;
48 +.18
56 0
59 +.1
58 *.2
ro
i
-------
STATION* GULF
?JRQC_ESSJ.._ GJJL F ...BALANCE 0 ____________________ LOCATION? UNIVERSITY + BOUNDARY
DATE* 6/lW7<»
LICENSi
NUMBER
76625H
603GBY
E 8261*6
130HQE
312HPO
12831R
J32391E
Q<+9FNU
811HSD
700KFC
7Z«W
o
ro
E NOZZ EXPL. SPIT AMOUNT
FIT VALUE BACK
BAD 1.0+ NO
GOOO FORCE FIT 0 NO
BAD 1.0* NO
SAD 1.0+ NO
GOOO FORCE FIT 0 NO
GOOO FORCE FIT 0 NO
FAIR HANDHELD 0.2 NO
GOOO FORCE FIT 0 NO
GOOO 0 N
GOOD 1.0+ NO
GOOD 0 NO
GOOO 0.2 NO
VAF.
62
66
66
68
68
68
70
70
70
70
72
72
72
72
LIQ.
TFMF
73
75
78
79
75
78
78
78
80
80
79
79
75
73
VAPOR VAPOR VAP. VAP.
' VOLUM VOLUM CONC RET.
AFTER BEFORE PRES : .;- .vfr
799.00 799.00 27 0
799.56 799.00 6<* +.25
80 Q.6<+ 799.56 6<* 0.30 ; t; ; , ;,
801.08 800. &<+ 6
-------
STATION! GULP
PROCESS* GULP BALANCED
LOCATION: UNIVERSITY + BOUNDARY DATE: t>/ik/7k
LICENSE
NUMBER
t
P 29 192
680GOC
D2N300
379HMH
CREATE
105JSX
OOJ977
UZA117
BTJ-788
RQX808
WTK414
0 60 HZL
554COA
NOZZ
FIT
EXPL.
VALUE
SPIT AMOUNT
BACK
VAP. LIQ.
TEMP TEMP
VAPOR VAPOR VAP.
VOLUM VOLUM CONG
AFTER BEFORE
GOOD HANDHELD
GOOD FORCE FIT
3AD
GOOD
FAIR
PAIR
POOR HANDHELD
GOOD
BAD HANDHELD
BAD
BAD HANDHELD
GOOD
POOR
BAD HANDHELD
0
0
1
0
0
0
0
•
1
0
0
0
G
1
.0 +
.8
.55
.25
11
.0 +
.3
.55
.3
.a +
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
72
7k
72
7k
7k
7k
7k
7k
7k
7k
7k
7k
7k
76
76
76
76
76
76
76
76
76
76
76
76
76
76
809.20
810.56
810. 64
812.28
813.08
814.84
815.44
315.4'*
815.44
315.44
815.70
317.10
317.10
317.4"
3G7.
309.
313.
310.
•U2.
313.
814.
315.
315.
315.
31 5 .
316.
317.
317.
24
20
56
23
08
84
44
44
44
44
72
4G
70
70
63
72
72
72
72
72
71
70
72
71
71
69
VAP.
RET.
PRES <
+ 0 .4H
0
+0.18
0
D
+ 0.20
+ 0.20
+ .02
0
+ 0.03
+ 0.10
+ 0.20
C
0
ro
-------
STATION! GULF
PROCESS* GULF BALANCED LOCATION* UNIVERSITY * BOUNDARY DATE: 6/14/74
LICENSE
NUMBER
NOZZ
FIT
EXPL.
VALUE
SPIT
BACK
AMOUNT VAP.
TEMP
LIQ. VAPOR VAPOR VAP. VAP.
TEMP VOLUM VOLUM CONC RET.
: APTER BEFORE
!
TWA4M.
36-0699
.M12136
ZZW270
3 73 COR
235JEG
OZV830
916CFV
632AVL
,tf 1X957
KPP346
WJX321
RSS989
WBF424
BAD
BAD
GOOD
BAD
FORCE
BAD
GOOD
GOOD
BAD
FORCE FIT HAND
BAD
SAD
GOOD FORCE FIT
FAIR
1.0*
1.0*
0
1.0*
.1
1.0
0
0
1.0*
0
1.0*
1.0*
0
.1
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
YES
NO
NO
74
74
74
74
74
74
74
74
74
76
0 74
TABLESPOON 76
0 76
P 74
76
76
76
76
76
76
80
80
30
80
80
80
80
76.
31
7.
318.
81
31
81
81
3.
a.
9.
9.
819.
82
1.
821.
82
3
82
82
82
1.
21
3.
3.
3.
42
52
96
96
73
78
73
06
06
18
.9
DC
73
66
817
317
318
318
318
819
319
320
321
321
082
321
323
323
.40
.42
.52
.96
.96
.73
.78
.04
.06
.06
1.1
.90
.00
. 73
PRES
69 0
70 C
70 *.2
70 -.02
70 * . 3
72 *.05
72 -.3
73 + .15
73 +.04
73 +0
73 +.10
70 n
70 +. 30
67 +.10
o
ts>
i
-------
STATIONS GULF
PROCESS: GULF BALANCED
LOCATION: UNIVERSITY
BOUNDARY
DATE* 6/l«»/7i,
LICENSE
NUMBER
NOZZ
FIT
EXPL.
VALUE
SPIT
BACK
AMOUNT
VAP.
TEMP
LIQ.
TEMP
VAPOR VAPOR
VOLUM VOLUM
VAP. VAP.
CONC RET.
! AFTER BEFORE
77111R
756CYO
;XN0019
•0233M51
TV5029
VEP825
WIH853
XV091K
80<»GJO
6 2«» EOY
VES152
U32GJH
RDJ199
XOR989
o
ro
BAD
BAD
GOOD
GOOD
POOR
POOR
BAD
POOR
POOR
GOOD
BAD
GOOD
POOR
HAND HELD
1
1
1
f
1
1
1
1
1
1
1
•
0
1
.0 +
.0* •
.0 +
2
.0 +
.0
.0*
.0 +
.0 +
.0 +
.0 +
8
.1
.0 +
YES
NO
NO
NO
YES
NO
NO
NO
NO
NO
NO
NO
NO
NO
TABLESPOON
0
0
0
SLIGHT
0
0
0
0
G
0
SPILLED OR
76
76
76
78
78
78
78
80
80
80
fit*
7<»
75
73
79
79
79
79
79
79
79
79
79
79
79
79
78
78
823.86
823.88
82<».6<*
325.62
825.66
826.60
326. 6U
826.66
S26.66
829.70
829.76
361.15
361.80
362.0?
823.
823.
823.
82«».
325.
825.
326.
326.
326.
328.
829.
360.
361.
361.
86
36
88
6
-------
STATION* GULF
PROCESS: GULF BALANCED
LOCATION* UNIVERSITY * BOUNDARY
OATEJ 6/1W74
LICENSE
NU M8E R
XVC286
0
fi"
0
2
'K
„?_
E
fjT
8
2
7
7
S
93GFK
17 KPH
V9512
32GSN
TR796
16KXG
HY401
65 KXL
70BML
25HQB
7263V
8059V
HI 602
o
ro
i
NOZZ
FIT
BAD
GOOD
BAD
GOOD
BAD
POOR HANDHELD
GOOD
GOOD
GOOD
POOR
GOOD
GOOD
GOOD
GOOD
EXPL. SPIT
VALUE BACK
1.0* NO
.4 NO
1* NO
0 NO
1.0* NO
1.0* NO
1.0 NO
1.0* NO
1.3* NO
1.0* NO
.1 NO
1.0* NO
.1 NO
.2 NO
AMOUNT VAP.
TEMP
76
74
76
75
76
77
77
76
75
77
OC
00
OC
LIQ. VAPOR VAPOR
TEMP VOLUM VOLUM
78
78
79
79
79
77
79
80
80
80
80
30
80
80
VAP. VAP.
CONC RET.
AFTER BEFORE
362. C2 362.02
362.
362.
363.
363.
363.
364.
365.
366.
* 366.
366.
366.
368.
370.
88
88
0
02
89
56
08
10
25
67
7C
60
t»
362.
362.
362.
363.
363.
363.
364.
365.
366.
366.
366.
366.
368.
02
88
00
02
89
06
76
1
25
67
70
60
•PRES • - v^™?^,
63 +.2
68 .15
64 *.2 : '••• <;;.';"
66 +.4
72 0
73 +.4
72 -.1
76 +.40
78 +.1
81 0
75 -.1
7 8 + . 1
73 +.4
71 +.3
Jfi.
-------
STATIONI GULF
PROCESS! GULF BALANCED
LICENSE
NUMBER
NOZZ
FIT
LOCATION: UNIVERSITY
BOUNDARY
DATE: 6/i<»/7<*
EXPL.
VALUE
SPIT AMOUNT
BACK
VAP. LIQ. VAPOR VAPOR VAP. VAP.
TEMP TEMP VOLUM VOLUM CONC RET.
TVW7M,
281BIJ
JKSU028
962GAP
TXG511
NONE
GOOD
POOR HANDHELD
GOOO
POOR
1.0 +
0
.1
.2
1.0*
NO
NO
NO
NO
NO
AFTER 3EFORE PRES "• • •^'.^•^^••^
77
76
79
78
81
80
80
80
80
80
370.
372.
37*..
375.
375.
lit
67
00
56
58
370.
371.
372.
375.
i<*
62
60
00
56
71 0 • '.
72 -.<+
65 -.<» ;;
66 -,
-------
STATION1 STANDARD PROCE
LICENSE
NU MBE R
j
s
449JEL
44763S
I359KZC
918KKL
730HNP
:89046N
WSU778
932HWN
|549JLB
XXX
574KMK
205JRT
6 94 HDP
15874V
0
ro
i
ro
NOZZ
FIT
GOOO
G003 H/H
BAD H/H
GOOO H/H
BAD H/H
POOR H/H
POOR
GOOO FORCE FIT
POOR H/H
GOOO FORCE FIT
GOOO FORCE FIT
GOOD
POOR
BAD
SSI STANDARD BALANCED LOCATIONS BALTIMORE
EXPL.
VALUE
.1
0
1.0 +
0
1.04
1.0*
1.0 +
00
1.0 +
0.0
0.0
0
1.0 +
1.0 +
SPIT AMOUNT VAP.
BACK TEMP
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
70
70
75
78
78
76
79
75
74
74
78
77
83
76
LIQ.
TEMP
76
76
76
7t*
77
76
77
77
77
78
79
78
78
78
* LAKE
MURRAY DATE: 6/17/74
VAPOR VAPOR VAP.
VOLUM VOLUM CONC
AFTER BEFORE
376.88 376.12
376.
378.
380.
381.
334.
384.
385.
336.
386.
387.
388.
388.
834.
12
22
78
94
28
70
70
06
44
00
Cl
90
99
375
376
378
380
382
384
384
385
386
386
387
38S
833
.58
.88
.22
.78
.00
.33
.70
.70
•1JL
.45
.00
.01
.04
00
QC
54
63
66
62
61
62
61
55
68
68
54
62
VAP.
RET.
PRES • •:':••'::: l
-.1
-.?
-.1 - .. •".
-.1
-.1
-.14
-.25
-.2
-.15
-.1
-.18
-.2
-.2
.01
-------
STATIONl STANDARD PROCESS* STANDARD BALANCED
LOCATION: BALTIMORE + LAKE MURRAY DATEJ 6/17/7**
LICENSE
NUMBER
NOZZ
FIT
EXPL.
VALUE
SPIT AMOUNT VAF. LIQ.
BACK TEMP TEMP
VAPOR VAFOR VAP.
VOLUM VOLUM CONC
1 AFTER BEFORE
l
292GOZ
545HTC
;570CVM
V 28 979
786KXO
0 12 JOH
V NX 430
315KZB
519KZE
OUL602
ZQM799
5 90 BAG
675EAU
228LKY
BAD
GOOD
POOR
FAIR HANDHELD
POOR
GOOD HANDHELD
FAIR HANDHELD
POOR
GOOD
GOOD H/H
POOR H/H
FAIR
POOR H/H
POOR
1.0*
0
1.0 +
.6
1.0*
0
.3
1.0*
0
0
.3
.40
1.0*
1.0*
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
NO
78
78
78
76
78
77
77
77
77
77
73
75
75
75
80
82
78
82
81
80
80
a*
83
83
a.
79
30
76
834.65
836.94
839.11
839.82
841.11
341.50
842.50
844.51
846.50
846.50
847.70
847.87
349.14
849.43
334.99
835. ?6
836.94
839.12
339.82
341.12
841.50
842.50
344.51
846.50
346.50
847.70
347.37
349.14
65
75
73
63
78
76
70
75
75
72
78
78
76
75
VAF.
RET.
PRES / ,. :,:;H
0.2
-.13
-.05. • . .- ;.;; .. .:-:
0
*.2
-0.22
-.2
-.18
-.16
-.2
.0
-.3
-.?
.-2
ro
ro
-------
STATION* STANDARD _____ PROjCElSjl._STAJiO.ARD_8M..AjMC£jD __________ LOCATION* BALTIMORE + LAKE HURRAY DATE! 6/17/7**
LICENSE NOZZ EXPL. SPIT AMOUNT WAP. LIQ. VAPOR VAPOR VAP. VAP.
NU MEIER ______ FIT _________ VALUE _MCK. ___ __ _ _ TEMP T_ErtP__ VOLUM _VOLU_M _JCON_C__REJ_._
" ~ "" """""" ........ "' " " ......
_ _ _ _ __ ______
"""" ........ ' " AFTER" BEFORE ...... PRES
POOR 1.0 NO 78 7« 851.59 851.52 81 -.21
ro
ro
-------
STATIONS STANDARD PROCESS! STANDARD BALANCED
LOCATION? BALTIMORE + LAKE MURRAY DATE* 6/ie/7*»
LICENSE
NUMBER
NOZZ
FIT
EXPL.
VALUE
SPIT AMOUNT VAP. LIQ.
BACK TEMP TEMP
VAPOR VAPOR VAP. VAF.
VOLUM VOLUW CONC RET.
I AFTER BEFORE
i
5970HV
915HHP
J751GGX
«»27KQR
172FVP
; 031 HOI
07<»KQ5
679GTH
9G3KLW
6 78 GUP
572FFR
082 JDK
311JLE
723HFP
POOR
FAIR
FAIR
FAIR
GOOD
POOR
FAIR
GOOD
POOR HAND HELD
BAD
POOR HAND HELD
POOR HAND HELD
GOOD
GOOD FORCE FIT
1.0 +
1.0 +
0.•
-.28
+ .05
0 . " • -'';::"--. •/ '-V-'Y'
-.18
-.18
-.20
-.15
-.15
-.2 •-• ;:- /•;•'*
-.in
0
-P. 27
-.22 .
-.2
C~J
ro
ro
-------
STATION* STANDARD PROCESS! STANDARD BALANCED
LOCATION! BALTIMORE * LAKE MURRAY DATE! 6/18/7i»
LICENSE
NUMBER
!
•ZND264
7C1BLK
JSPOOK J
!<»38CTV
NOZZ EXPL. SPIT AMOUN1
FIT VALUE 3ACK
POOR FORCE FIT 1.0* NO
POOR FORCED FIT 1.0 NO
FAIR 1.0 NO
POOR 1.0+ NO
r VAP.
TEMP
78
77
77
77
LIQ. VAPOR VAPOR VAP. VAP.
TEMP VOLUM VOLUM CONC RET.
AFTER BEFORE PRES. • ;. ..> . . .;-: ;H*M'
78 873.78 972.43 65 -.17
78 374.92 873.78 69 -.20
78 876.75 87^.92 6% -.17. '•:.«,'•;: .-.••"^'••.:! ;;.;^.:
78 877.42 876.75 67 -.15
._._
ro
ro
-------
STATIONl STANDARD PROCESS* STANDARD 3ALANCED
LOCATION! BALTIMORE * LAKE MURRAY DATE* 6/19/71*
i
i
0
1
8
LICENSE NOZZ EXPL.
NUMBER FIT VALUE
SPIT AMOUNT
BACK
VAP. LIQ.
TEMP TEMP
VAPOR VAPOR VAF.
VOLUM VOLUM CONC
AFTER BEFORE
388293 POOR HAND HELD 1.0 +
70FTD POOR HAND HELD 1.0+
42GOZ POOR HAND HELD 1.0+
645KZR GOOD 1.0 +
6
;3
03ESM POOR OPEN ON TP 1.0 +
99CQQ POOR HAND HELD 1.0 +
NOZ707 HAND HELD
5
1
2
G
2
4
3
45HTC GOOD HAND HELD 0
03AFM POOR 1.0+
39GTV POOR HAND HELD 1.0+
1157827 POOR 1.0
60KZE NOT TAKEN
05JYC GOOD FORCE FIT 0
02JQU FAIR 1.0
o
i
ro
i
ro
ju
VES TABLE-SPOO 62 75 395.36 394.28
NO
NO
NO
NO 0
NO 0
NO 3
NO 0
NO 0
NO 0
NO
NO
NO
NO
63
61
65
68
72
72
68
69
62
72
72
73
75
74
74
75
75
77
78
79
79
80
79
78
78
395
395
398
399
400
402
404
405
406
377
878
881
883
.88
.92
.36
.20
.04
.54
.06
.00
.32
.67
.92
.24
.25
395.
395.
395.
398.
399.
401.
402.
404.
405.
577.
877.
373.
881.
36
91
92
48
20
26
80
06
00
42
75
94
24
47
27
36
56
55
57
54
63
62
68
47
49
56
53
VAF.
RET.
PRES .. - ... ^;:;..:^;|v,s;;%
'-"••- • '••-. " "•"."::'".•.-.--•. '. !-• :."
-.15
-.12
-.04 . . . :':•••:••''•
-.02
-.15
-.15
-.03
-.1
+ .03
-.1
-.45
-.40
-.22
-.03
-------
STATION! STANDARD PROCESS* STANDARD BALANCED
LOCATION: BALTIMORE * LAKE MURPA* DATE: 6/i9/7<»
LICENSE
NU HBE R
F*2556
NOZZ
FIT
tXPL. SPIT AMOUNT
VALUE BACK
VAP. LIQ. VAPOR VAPOR VAP. VAP.
T.EMP _TFMP_ VOLUM _VQLU_M __CONC RE.T.
" PRES"
A..O*
1.0 +
"GOOD FORCE Fif~T
PPQR_
POOR
NO
NO
"NO"
105 HOT
RKP800
6C3G8Y
0 38 KQR FOOR_ H_ANO_..HE.LO _.1..0_ NO
UUPC88 POOR 1.0* NO
VslfJuAGOOID~?O"RCE FTT o "NO"
999HGP !lPM_fP_RG.E_flI l.t
-------
STATI ONI STANDARD PROCESSt STANDARD BALANCED
LOCATION! BALTIMORE * LAKE MURRAY DATES 6/19/7**
LICENSE
NUMBER
NOZZ
FIT
tXPL.
VALUE
SPIT AMOUNT
SACK
VAP. LIQ. VAPOR VAPOR VAP. VAP.
TEMP TEMP VOLUM VOLUM CONC RET.
i
PHP 979
UNP6*
I033KZB
:RSK*»21
90<.87L
:KKG377
J2M1FFS
GOOD HAND HELD
POOR
POOR
POOR HAND HALO
GOOD
FAIR
FAIR
0
1
1
1
1
1
1
.0*
.0 +
.0 +
.0*
.0*
.0*
NO
NO
NO
NO
NO
NO
NO
7k
76
78
78
78
78
76
78
78
78
78
77.5
78
78.5
AFTER £
898.50
898.81*
899. 5
-------
STATION* TEXACO
PROCESS* ENVIRONICS LOCATION! BALTIMORE + FLETCHER
DATFJ 6/20/74
LICENSE NOZZ
NUMBER FIT
1
651BEB HAND HELD
1
2 4 ELL
i623HTS
PWA684
T
;4
W
W
HE7K
8825L
YM088 GOOD H/H
JU456
770KLB
,305HOS
WSC130 H/H
S
M
9
TEAM2 H/H
W1510 _ ;
3353G HANO HELD
o
ro
EXPL.
VALUE
.4
0
0
0
0
0
0
0
1.0
G.O
0.4
0
0
.1-.4
SPIT AMOUNT
BACK
NO
NO
NO
NO
NO
NO
NO
NO
NO
YES 20CC
NO
NO
YES 2-5CC
YES 20CC
VAF. LIQ.
TEMP TEMP
76
77
75
79
77
00
81
82
,*
83
76
80
76
76
77
77
77
78
80
78
79
78
78
78
76
76
VAPOR VAPOR
VOLUM VOLUM
AFTER BEFORE
000.00 003.00
953
959
975
981
995
50.
68.
105
120
t«
155
488
500
.92
.30
.30
.6u
.8
89
98
.53
.10
.90
.60
.99
.82
942. 20
954.9
963.80
976.00
994.5
48.1
51.50
081.28
107.00
142.90
151.10
464. 7P
491.66
'
VAP. VAP.
CONC PET.
PRES . , - ;.-: /.. oyvj-
-18
31 -18
12 -21 "•• •'..-,-;.;
15 -24
28 -24
9 -24 .. '.:;
17 -24
31 -24.5
24 -21.5
19 -24.0
8 -25
15 -?5
17 -20.0
16 -24.5
ro
-JkO-
-------
STATION! TEXACO
PROCESS? ENVIRONICS
LOCATION: BALTIMORE * FLETCHER
OATEt 6/20/74
LICENSE NOZZ EXPL.
NUMBER FIT VALUE
SPIT AMOUNT VAP.
BACK TEHP
LIQ. VAPOR VAPOR VAP.
TEMP VOLUM VOLUM CONC
; AFTER BEFORE
314GXE
PHB110
!662FZG
384KLQ
77458U
DYN439
53013L
5 71 HOT
496JQS
14382R
37778W
UKW764
ZXM782
963 GOY
<*>
ro
i
CO
o... .....
C
1.0
1.0*
HAND HELD 0
HAND HELD -1.0
0
0
0
HAND HELO 1.0*
0
HAND HELD 1.0*
0
0
HAND HELD 1 .0
NO DRIPS
NO
NO
NO
NO
NO
NO
NO
NO
NO 1 CC
NO
NO
NO
NO
80
80
8Q
80
80
80
82
82
82
82
82
82
82
80
77
77
77
78
78
78
78
78
79
78
78
78
78
7tt
530.
532.
545.
.5>7.
550.
559.
566.
579.
582.
597.
599.
606.
b38.
638.
04
28
87
35
40
36
70
45
18
07
86
47
82
82
514.
530.
532.
545.
5i»7.
550.
559.
566.
579.
582.
597.
603.
628.
o32.
99
0
-------
STATION* TEXACO
PROCESS: ENVIRONICS
LOCATIONS BALTIMORE + ^LETCHER
DATE* 6/20/74
LICENSE NOZZ
NUMBER FIT
'973JQP HANO HELD
FPN866 HAND HELD
234HKK HAND HELD
;716KPH HANO HELD
744GOX HAND HELD
I7608SB
i444JLC HANO HELD
SNP596
!«.75KLX
.46287P
726FVX
785JLA
TAM267
AZV456 HAND HELD
EXPL.
VALUE
1.0 +
0
0
0
0
.5
0
0
1.0
c
1.0
0
0
SPIT AMOUNT
BACK
NO
YES
NO
NO
NO
YES
NO
NO
NO
NO
NO
NO
NO
NO
SPOONFULL
10CC
0
0
50CC
0
0
0
0
0
0
Q
0
VAP.
TEMP
82
80
82
82
82
82
82
82
60
80
80
76
78
8G
LIQ.
TEMP
78
78
78
78
78
78
78
78
78
78
73
78
78
.»
VAPOR VAPOR VAP. VAP.
VOLUM VOLUM CONC PET.
AFTER BEFORE
637.52 633.38
650
651
656
663
673
683
693
723
746
758
765
768
771
.70
.20
.32
.18
.56
.60
.08
.00
.20
.12
.52
. 6G
637.52
650.70
653.02
657.14
664.90
678.94
583. 70
696.00
723.08
746.00
758.24
765.14
768.62
'DO C" ^ -•.'•-"•".• '-. •• -'.-•-• '
i r\ t_ J . - . ._ • .•.--••-'.
23 -24.0
13 -23
16 -19 v
13 -24.0
16 -19.0
18 -24.0
10 -24.0
17 -24.0
14 -24.0
27 -24.5
15 -20.5
14 -24.0
4 -17.5
15 -24. H
o
ro
CO
-------
STATION* TEXACO
PROCESSt ENVIRONICS
LOCATION: BALTIMORE »• FLETCHER
DATES 6/20/74
LICENSE
NUMBER
KOW808
17662T
20263T
40QJSJ
WAC301
TCB765
710KLT
7 31 ELS
3 98 OLD
061070
V NY 049
KGS913
NOZZ
FIT
HAND
HANO
HAND
HAND
HAND
HAND
HAND
HANO
HANO
HANO
HELO
HELO
HELO
HELO
HELO
HELO
HELO
HELO
HELO
HELO
EXPL.
VALUE
1.0 +
1.0*
0
0
0
0
0
0
1.0*
0
0
SPIT
BACK
NO
NO
fES
NO
NO
NO
NO
YES
NO
NO
VES
. o
NO
AMOUNT
0
0
CUPFULL
0
0
g
Q
1 TSP
Q
0
1 TSP
^
:.i
VAP. LIQ.
TEMP TEMP
80
78
80
84
82
78
8G
80
80
82
82
82
78
78
78
78
78
78
78
78
78
78
78
78
VAPOR VAPOR VAP.
VOLUM VOLUM CONG
AFTER BEFORE
773.40 771.62
777.02
781.76
788.60
794.20
797.56
800.30
807.70
810.14
813.76
8?7.1G
335.62
7/3.42
777.02
783.72
790.40
794.24
797.56
300.30
307.72
310.26
913.80
327.32
4
13
15
5
19
15
19
19
19
12
14
16
VAP.
RET.
PRES
-24. Q
-24.5
-24.5
-21.5
-24.0
-21.0
-24.0
-24.0
-24.0
-17.5
-24.0
-24.0
o
I
ro
i
OJ
ro
-------
: STATION: UNION 76 PROCESS: PROCESS PRODUCTS
LOCATIGNt WARING + ZION
DATE:
LICENSE
NUMBER
i
960KZD
L36087
|6 09677
72Q85W
9 55 KLP
OE REEN
iTAC138
RUUA88
!866DND
2 33 HMS
680GOC
1MJ 22V
833FVQ
3 50 GOB
o
ro
NOZZ
FIT
EXPL.
VALUE
SPIT AMOUNT
BACK
VAP.
TEMP
LIQ.
TEMP
VAPOR VAPOR VAP.
VOLUM VOLUM CONC
AFTER BEFORE
HANO HELD POOR
GPPO
GOOD
HANO HELD
GOOO
GOOD
GOOO
HANO HELD POOR
GOOO
GOOD
GOOO
GOOO
GOOO
1.0
0
0
0
c
c.
0
0
1.0*
0
0
c
0
c
NO 0
YES 1TBSP
NO 0
NO 0
NO
NO
NO
YES 5CC
NO a
NO
NO 0
NO
YE3 10CC
NO
68
69
71
68
71
73
71
71
71
71
78
73
80
77
83
79
77
78
79
79
73
79
79
79
79
61}
BG
817
820
823
823
825
327
830
a«
835
837
8Ut5
8^3
•--•
. _.
.92
.73
.«»2
• 9«*
.03
.77
.85
.«
.30
.70
.83
.67
.29
..3
817.
817.
820.
323.
323.
925.
327.
330.
833.
835.
837.
3<»0.
8i»3.
*7.
38 38
92 <*5
78 kl
<»<» i»i
9%«
03 <*5
77 5G
88
-------
STATION! UNION 76
PROCESS* PROCESS PRODUCTS
LOCATION: WARING * ZION
DATE I 6/2<*/7<»
LI CEN SE
NU MBE R
NOZZ
FIT
EXPL.
VALUE
SPIT AMOUNT VAP.
BACK TEMP
LIQ.
TEMP
VAPOR VAPOR VAP. VAP.
VOLUM VOLUM CONC RET.
i AFTER BEFORE PRES .*-.
\55CTV
731*6,,
WYL<»23
OVC759
023»9,7
WCMSLM
GOOD
GOOD
BAD
HAND HELD GOOD
HAND HELO GOOD
GOOD HAND HELD
GOOD
0
0
1.0*
G
0
0
0
NO
NO
YES
NO
NO
NO
NO
80
80
80
88
88
83
GO
76
76
76
7b
76
76
GO
851.88
85«».oa
857. i»2
858. 1**
859.32
860.90
862.39
3V9.83 1*5 -<*.0
851.88 bk -9.Q
85^.12 ^ 3 -3.9
357. <+6 65 -?.8
858.1<+ 30 -3.6
859.32 50 -8.0
860.91 53 00
•
ro
i
CO
..J&L.
-------
APPENDIX C-;3
PERFORMANCE CALCULATIONS
C-3
-------
STATION* STANDARD PROCESS* INTERHARK . LOCATION: CARMEL VALLEY + 15
DATE: 6/6/74
LICENSE
NUMBER
i
932HWN
i C8QEAT
24 2CT X
13584R
£830974
i 55 865 F
874FLS
C9809
G59KFQ
VCL446
YYG563
GQP810
60969
92 402 X
RETURNED STANDARD
VAPOR RETURNED
VAPOR
(CU FT) (CU FT)
6.10
1.90
3.20
2.70
3.40
4.40
4.60
1.20
6.20
2.80
5.70
2. CO
5.10
4.8C
6.05
1.88
3.17
2.67
3.31
4.31
4.48
1.17
6.09
2.73
5.55
1.97
5.00
4.73
RET VAP
TO
DISPL LIQ
RATIO
(CF/CFI
2
1
3
2
1
1
1
1
3
*
1
2
2
.74
.90
•29
.00
.78
.85
.79
.30
.64
.,1
.78
.77
.72
FILL
RATE
(GPM)
b.60
10.83
.10.29
IP. 17
13.45
11.11
8.04
7.50
6.54
6.70
11.0 7
6.69
6.90
VEH TANK- VAPOR
UNO TANK MASS
TEMP
(OEG F)
-8. 00
*99.99
. -7.00 .
-13.00
13.00
-1.00
1.00
21.00
17.00
-9. GO
1.30
-3.00
16.00
8. GO
165
55
75
95
124
132
3u
169
73
160
57
139
141
(GM)
.36
.53
.34
.30
• 31
.76
.10
.17
.94
.54
.31
.10
.71
.54
VAP MASS VEH TANK-
TO OISP LIQ
OISP LIQ TF.MP : ^
RATIO V
(GM/GAL) (OEG P)
10. C5
7.50
12.96
7.59
6. 89
7.17
7. 06
4.50
13. 60
8.65
9.3C
6.88
If .35
10.91
-11.
*99.
-9.
-15.
10.
-4.
-2.
19.
15.
-11.
-1.
-5.
14.
6.
00
99
OJ5
00
00
00
00
00
OC
OQ
00
00
00
on
o
i
co
-------
STATION! STANDARD PROCESS: INTERMARK
LOCATIONt CARMEL VALLEY * 15
DATE: &/ e//<.
LICENSE
NU MBE R
i
96 695 E
! XYV086
R27816
TUCKIE
950DVE
VHA636
026BHA
21* 8 AC V
, 588YHU
C29ESQ
2LX232
833C-OA
83CHPA
651R/R
RETURNED
VAPOR
(CU FT)
,.00
<».20
l.UQ
1.30
<».3Q
1.10
3.60
2.30
3.30
3.50
3.0U
2.80
STANDARD
RETURNED
VAPOR
(CU FT)
. 3.9%
3.91
1.38
3.33
1.27
u
72
28
VAP
MASS
TO
DISP LIQ
RATIO
CGM/GAL)
3.
8.
11.
13.
10.
10.
1C.
5.
8.
9.
11.
8.
11.
10.
72
03
07
05
99
72
28
20
73
02
10
05
77
91
VEH TANK-
DISP LIQ
. TEMP -• •'••.- ;
(OEG F)
3.
-8.
-3.
5.
13.
*f .
11.
-2.
-1.
a.
-i.
12.
-2.
1.
00
00
30
0(1
00
00
GO
00
00
00
00
00
on
00
o
W
ro
-------
STATION! STANDARD PROCESS! INTERMARK „ LOCATION: CA*MEL VALLEY
15
DATE* 6/ 6/74
LICENSE
NU MBE R
RETURNED STANDARD RE
VAPOR RETURNED
| VAPOR
fCU FT) (CU FT)
82 936 0
; 902DBT
73 438 H
18354V
HHX668
XDU752
29 6KB I
! SKE220
4152
4152
136LEC
329HQA
CUD923
T0528697
4.60
3.89
3.20
2.80
2.40
3.40
6.80
2.80
6.20
7.80
2.80
4.10
3. 40
2.70
4.53
3.74
3.15.
2.74
2.37
3.34
6.62
2.74
6.04
7.61
2.77
4.03
3.32
2.64
T VAP
TO
FILL
RATE
OISPL LIQ
RATIO
(CF/CF) (GPM)
2
2
2
2
2
1
2
2
2
4
2
1
2
2
.25
.01
.53
.04
.72
.58
.38
.58
.59
.14
.60
.76
.59
11.33
11.12
6.94
4.79
11.15
6.86
6.97
3.65
3.74
14.55
11.28
6.51
6.81
VEH TANK- VAPOR VAP
UNO TANK MASS
TEMP
(DEG F)
14.00
8.00
C.CG
9.00
-2.00
11.00
17.00
3.00
18.00
27.00
23. OC
9.00
9.uu
7.00
(GMI
150.09
116.16
102.78
85.05
76.00
114.12
198.66
84.39
184.26
244.05
91.76
139.52
101.23
77.72
MASS
TO
OISP LIQ
RATIO
(GM/GAL*
9.
9.
10.
8.
7.
1C.
9.
10.
19.
9.
7.
11.
IP .
94
36
02
50
74
87
35
87
53
68
46
42
25
23
VEH
OISP
TANK-
LTQ
TEMP
(OEG P)
12
6
-2
7
-4
9
15
1
16
25
21
7
7
5
.00
.00
.on
.00
.00
.00
.00
.00
.30
.00
.00
.00
.00
.00
0
W
(A)
-------
STATION* STANDARD PROCESS* I.NTERMA.RK LjOCAJ I 0 N t C A RMIE L ._V_A_L LE T
DATES 6/ 6/74
LICENSE
NUMBER
4060KA
2288Q1
TO 934 996
372KLS
D2T709
447DKC
XU V48 4
C16JRX
ZND264
RETURNED
VAPOR
(CU FTI
2.90
4.40
3.50
2.3Q
5.40
2.90
3.50
5.00
3.80
STANDARD
RETURNED
VAPOR
(CU FT)
2.82
4.35
3.61
2.22
5.25
2.83
5.«
4.89
3.95
RET VAP
TO
DISPL LIQ
RATIO
(CF/CF)
2.25
3.28
.2.78
2.M,
2.83
2.86
2.93
2.73
2.19
^ILL
RATE
(GPMI
6.96
7.42
4.85
6.3C
6.67
6.83
6.86
6.81
9.53
VEH TANK-
UNO TANK
TEMP
(DEG F)
6.00
-5.00
3.30
1.00
1 .CO
7.00
-3.00
9.00
l.OG
VAPOR
MASS
(GM)
89.11
139.34
111.90
67.74
162.91
83.43
106.99
146.62
122.63
VAP MASS
TO
DISP LIQ
RATIO
(GM/GALI
9.48
14.07
11.54
9.96
11.72
11.27
12.16
1C. 94
9.08
VEH TANK-
01 SP LIQ
TEMP ••• -
'•.
(OEG F)
4.00
-7.00
1.90
-1.00
-1.30
5.00
-5. DC
7.ao
-1.00
-------
STATION: UNION 76 PROCESS: PROCESS PRODUCTS :LQLCAIIJ^JLJLRRING._*_ZION DATE; 6/11/74
LICENSE
NUMBER
ZMR401
j 079EQU
18116R
937JFS
672GXG
774JEL
Q41GOA
TGT771
862JQ.T
422HOS
73QJLA
07 2CK X
689ESK
613KAC
o
CO
01
RETURNED
VAPOR
CCU FT)
*99.99
1.60
3.00
2.20
1.88
2.77
2.33
1.10
2.10
2.48
1.58
1.24
1.22
2.36
STANDARD
RETURNED
VAPOR
(CU FT)
*99.99
1.58
2.91
2.14
1.81
2.68
2.26
1.06
2.04
2.37
1.54
1.20
1.16
2.26
RET VAP
TO
DISPL L3
RATIO
(CF/CF)
*99.99
1.25
1.19
1.03
1.00
1.09
1.12
1.50
1.29
.95
1.47
1.01
.98
1.12
^ILL
RATE
-------
STATIONS UNION 76 PROCESS* PROCESS PRODUCTS
LOCATION: WARING
ZION
DATE: 6/11/74
LICENSE RETURNED
NUMBER VAPOR
! CCU FTI
43 204 U
i 799JEH
t - '
RJP777
450ETV
059GJX
299HWV
211RTZ
WLN696
; W8F900
1DDLR1221
137GXA
1.56
1.98
1.83
2.84
2.40
1.40
3.30
2.10
1.70
.60
1.80
STANDARD
RETURNED
VAPOR
-------
STATION* GULF
PROCESS! GULF BALANCED
LOCATION: UNIVERSITY + BOUNDARY
DATE: 6/12/74
LICENSE
NUMBER
RETURNED STANDARD
VAPOR RETURNED
| VAPOR
CCU FT)
-------
STATION* GULF
PROCESS* GULF BALANCED
LOCATION: UNIVERSIT*
BOUNDARY
DATE: 6/12/7V
LICENSE
NUMBER
i
60 421 F
; 446JEC
526GGC
236KLM
101ASI
653FBX
ZQ0792
V2 974 1
RGD594
66 394 E
689DLX
550KFG
611GGS
148HDT
o
i
U)
CO
RETURNED
VAPOR
ICU FT)
.22
. 88
1.82
.80
O.C2
.94
-.10
2.16
1.02
.25
1.38
.36
.74
.06
STANDARD
RETURNED
VAPOR
CCU FT)
.22
.83
1.82
.79
o.ao
.92
-.10
2.15
1.01
.26
1.37
.36
.74
.06
RET VAP
TO
DISPL LIQ
RATIO
CCF/CF)
.,3
.82
.94
.59
0.00
.52
-.09
1.06
.91
.51
.36
.28
.30
.03
PILL
RATE
(GPM)
5.70
5.65
6. CO
5.52
5.87
5.52
5.88
9.05
7.6C
8.40
5.70
5.91
9.13
VE
H TANK-
UNO TANK
(
3
7
-3
16
13
25
4
6
5
8
-3
13
6
5
TEMP
DEG F)
.00
.CO
.CO
.00
.00
.00
.CG
.00
.oc
.00
.CO
.00
.00
.00
V
M
c
b.
28.
53.
29.
0.
32.
-3.
70.
32.
3.
44.
12.
24.
2.
APOR
ASS
GM)
«
58
20
48
on
96
61
17
90
41
69
43
71
02
VAP MASS
TO
OISP LIQ
RATIO
CGM/GAL)
1. 79
3.57
4.01
2.95
n.oo
2.50
-.45
4.62
3.96
e.n
3.76
1.31
3.58
.15
VEH
OISP
T
TANK-
LI3
EHP--v^:/;--r
- ; , '• • • • ' - ft:
COEG F)
2
5
-5
14
12
24
2
4
2
5
-6
11
4
3
.00
.00 . •.. ;v-
.on
.00
.00 - : (
.00
.00
.00
.00
.TO
.00
.00
.30
.O'Q ... -.•••••, •:.;+
-------
STATIONS GULF
PROCESS* GULF BALANCED
LOCATION: UNIVERSITY * BOUNDARY
DATE* 6/12/7**
LICENSE
NUMBER
'•
37498W
I 159KZQ
RETURNED
VAPOR
(CU FT)
1.66
-.06
STANDARD
RETURNED
VAPOR
-------
STATION* GULF
PROCESS* GULF BALANCED
LOCATION* UNIVERSITY * BOUNDARY
OATEt 6/13/74
LICENSE
NUMBER
RETURNED STANDARD RET VAP
VAPOR RETURNED TO
FILL
RATE
VEH TANK- VAPOR
UNO TANK MASS
i VAPOR OISPL LIQ TEMP
RATIO
tCU FTI (CU FT)
-------
STATIONS GULF
PROCESS! GULF BALANCED
LOCATION* UNIVERSITY + BOUNDARY DATF: 6/13/74
LICENSE
NUMBER
CUM753
! 0238796
73 5GO W
28 88E X
! VEU721
1 U40716
87764 N
j 1220FK
247ADR
TTF-876
; 585G8T
XTL389
..MIL
OZT057
RETURNED
VAPOR
CCU FT)
.10
.96
.10
.89
1.44
-.18
1.75
.22
.54
1.74
.30
1.48
0.00
.05
STANDARD
RETURNED
VAPOR
(CU FT1
.10
.96
.10
.89
1.43
-.18
1.74
.22
.54
1.72
.30
1.47
O.QQ
.05
RET VAP
TO
OISPL LIQ
RATIO
(CF/CF)
.13
.72
.04
.80
.58
-.17
.76
.43
.31
.90
.79
.83
Q. 00
.04
PILL
RATE
(GPM)
,.17
6.59
5.57
5.72
5.31
5.71
5.70
4.15
5.20
5.57
4.20
5.50
*.«
5.70
VEH TANK-
UNO TANK
(
9
11
11
15
15
15
13
17
10
7
2
3
i*
13
TEMP
DEG F
.CO
.00
.00
.00
.00
.00
.00
.00
.00
.00
.00
.00
.00
.00
VAPOR VAP MASS
MASS TO
OISP LIQ
RATIO
) (GM) (GM/GAL)
3
31
3
30
-6
58
7
17
57
10
0
1
.23
.18
.27
.69
.68
.01
.55
.02
.99
.97
.30
.81
.00
.61
.57
3. 12
.16
3. 70
2.51
-.76
3.42
1. 85
1.38
4.03
3.57
3.60
0.00
.17
VEH TANK-
OISP LIQ
; TEMP -: .:>;£ - ',
(OEG F)
6.
1C.
10.
i,.
13.
14.
12.
15.
9.
6.
1.
2.
13.
12.
00
00
00
00 .;••->;
00
00
00
00
00
00
30
ao
i
CO
-------
STATIONS GULF
PROCESSt GULF BALANCED
LOCATION* UNIVERSITY
BOUNDARY
DATE* 6/13/74
LICENSE
NU MBE R
RETURNED STANDARD
VAPOR RETURNED
VAPOR
(CU FT) (CU FT)
86467P
728FEA
TST284
H54055
7410ZE
534BXV
74 3CT T
7350QK
103APD
587KAC
TAA480
049DZN
378GNZ
508KHV
o
i
1.90
.98
.10
1.75
0.00
.28
.46
.64
1.24
.43
1.34
.83
1.40
0.00
1.33
.97
.10
1.73
0.00
.28
.46
.63
1.23
.46
1.33
.88
1.39
0.00
RET VAP
TO
OISPL LIQ
RATIO
CCF/CF)
.96
.28
.12
.93
0.00
.36
.«
1.08
1.03
.,*
.82
.67
.75
0.00
3
7
5
3
3
5
3
5
5
6
8
3
*
FILL
RATE
VEH TANK- VAPOR
UNO TANK MASS
TEMP
(GPM) (OEG F) (GM>
.98
.01
.56
.96
.26
.27
.52
.93
.37
.91
.40
.71
.47
••
12
-9
-9
8
-7
2
-1
-6
1
5
0
12
*99
r n c. ~z i r
• 0 U O O • • 3 U
.00 33.16
.00 2.75
.CO 49.17
.00 0.00
.00 3.45
.00 12.98
.CO 18.05
.00 36.37
.CO 14.76
.CO 39.35
.iiC 26.72
.CO 45.15
.99 0.00
VAP MASS VEH TANK-
TO DISF LIQ
DISP LIQ TE
RATIO
(GM/GAL) (OEG
4.34 3.
1.29 11.
.46 -12.
3.54 -12.
0.00 5.
1.48 -9.
l.M,
4.14 -8.
3.88 0.
3.29 3.
2.73 -2.
3.25 11.
0.00 *99.
M'P ' •••••*:
00
00
ao
on
ao
00
ao
ao
00
00
00
0?
00
99
-------
STATION: GULF ___PROCESS: GULF BALANCED LOCATION: UNIVERSITY * BOUNDARY DATE? 0/13/74
LICENSE
NUMBER
RETURNED STANDARD
VAPOR RETURNED
VAPOR
CCU FT)
-------
STATION! GULF
PROCESS: GULF BALANCED
LOCATION: UNIVERSITY + BOUNDARY DATE: &/i3/7<»
LICENSE
NUMBER
RETURNED STANDARD RET VAP FILL VEH TANK- VAPOR VAP MASS VEH TANK-
VAPOR RJIURNEO_ _J.o_ M.LL _ _UND JANK_ MASS TO DISP LTQ
"VAPOR" ~ "DISPL LIQ" -" ~~~ ~ '"TEHP ~ " OISP LIQ TEMP
RATIO RATIO
(CU FT) (CU FT) (CF/CF) (GPM)
-------
STATION! GULF
PROCESS: GULF BALANCED
LOCATION* UNIVERSITY 4- BOUNDARY
DATES 6/14/74
LICENSE
NUMBER
j
76 635 H
f" 60 3GB Y
XME767
£8261*6
: 130HQE
313HPO
045CWP
12831R
32 391 E
C49FNU
811HSO
44 053 F
70CKFC
724CTU
o
t*>
RETURNED
VAPOR
CCU FT)
O.CO
.55
1.08
.44
0.00
1.22
.32
.Si,
2.04
.36
.56
.12
.14
1.04
STANDARD
RETURNED
VAPOR
(CU FT)
0.00
.56
1.09
.<*<*
0.00
1.23
.32
.54
2.04
. 36
.56
.12
.14
1.04
RET VAP
TO
DISPL LIQ
RATIO
CCF/CF)
0.00
.8t*
.96
• <»0
0.00
.76
.63
.94
.9<+
.77
.39
.06
.19
.83
FILL
RATE
(GPH)
5.07
5.45
6.80
6.15
5.54
5.54
4.56
3.69
8.15
5.25
2.56
5.72
5. kit
5.37
VEH TANK-
UNO TANK
TEMP
(OEG FJ
*99.99
2.00
-4.00
-8.00
3. CO
7.00
0.00
-4. CO
-4.00
-5.00
3.00
3. CO
23. OQ
14.00
VAPOR
MASS
(GM)
O.OG
18.69
36.04
14.63
c.oo
42.46
10.76
17.88
70.79
11.55
19.35
3.90
5. 34
37.55
VAP MASS
TO
nisp LIQ
RATIO
(GM/GAL)
0.00
3.74
4.24
1.78
0.00
3.54
2 . 83
4.16
4. 34
3. 30
4.12
.27
.99
3.99
VEH TANK-
DISP LIQ
TEMP - ..;:-/'
-------
STATIONt GULP
PROCESS* GULF BALANCED
LOCATION: UNIVERSITY
BOUNDARY
DATES
LICENSE RETURNED
NUMBER VAPOR
(CU FT)
P29192
| 680GOC
DZ N80 0
379HMW
GR EAT £
105JSX
00 J97 7
UZA117
0<»5GXH
BTJ-788
RQX838
WT K<»1 k
060HZL
55 <+CO A
o
V
1.96
1.36
.08
1.6,
.80
1.76
.60
O.fiQ
Q.OO
0.00
.26
.33
O.GC
0.00
STANDARD
RETURNED
VAPOR
-------
STATION* GULF
PROCESS: GULF BALANCED
LOCATION: UNIVERSITY «• BOUNDARY
DATE! 6/14/74
LICENSE
NUMBER
I
TWA441
I 36-0699
M12136_ ..._ _.
ZZW270
373COR
235JEG
OZV830
916CFV
632AVL
VI X95 7
KPF346
WJX321
RSS989
WBF«4
o
f
RETURNED
VAPOR
(CU FTI
.02
1.13
.44
0.00
.82
0. 00
0.00
1.02
0.03
.12
.80
1.10
.78
.08
STANDARD
RETURNED
VAPOR
(CU FT)
.02
1.09
.44
0.00
.81
Q. 30
0.30
1.01
Q.OO
.12
.79
1.09
.77
.08
RET VAP
TO
OISPL LIQ
RATIO
(CF/CF)
.01
.51
.86
0.00
.73
0.00
o.oa
.56
0.00
.47
*99.99
.57
.96
.31
FILL
RATE
(GPM)
4.8G
5.37
4.56
5.43
6.72
5.61
4.30
5.63
4.99
3.26
O.GO
5.16
8.00
2.35
VEH
UNO
TANK-
TANK
TEMP
(D&G F)
25.
6.
6.
12.
11.
11.
22.
20.
5.
6.
6.
I.7 r
12.
15.
00
00
00
00
00
00
00
00
00
00
00
00
00
00
VAPOR VAP
MASS
-------
STATION: GULF
PROCESS: GULF OALANCED
LOCATION: UNIVERSITY
BOUNDARY
DATE: 6/14/74
LICENSE
NUMBER
77 111 R
7560^0
XNDH19
0233401
TV 502 9
VEP825
WIW853
XV0904
804GJO
624EOY
VES152
43 2GJ H
RDJ199
XOR989
RETURNED
VAPOR
(CU FT)
J.OO
.02'""
-.76
.98
.04
.94
a. co
.02
0.00
1.68
.06
1.05
.16
.22
STANDARD
RETURNED
""VAPOR
(CU FTI
0 . 0 U •
.02 "
.75
.97
.04
.93
0.00
.02
Q.OO
1.65
.06
1.04
.16
.22
RET VAP
TO
aiSPL LIQ
RATTO
(CF/CF)
0. Ou
.02
.53
.66
.03;
.73
*99.99
.04
0.00
.77
.03
. 36 '
.62
.43
^ILL
RATE
(GPM)
5.13
5.28
5.58
5.03
4.93
4.96
G.C 0
3.04
5.14
5.33
5.60
4.55
5.7C
4.15
V£H TANK-
LI ND TANK
(
14
13
12
23
15
16
13
10
35
12
11
4
6
18
TEMP
DEC F)
.CO
.00
.00
.03
.CO
.GO
.CO
.00
.GO
.CO
.CO
. u u
.CO
.GO
VAPOR
MASS
VAP
MASS
TO
OISP LIQ
0
23
34
1
34
0
0
57
1
24
5
7
(GM)
• 0 C
.71
.OC
.97
.43
.97
.00
.73
.00
. 16
.69
.?5
• V4 v
.31
RA
(G
n
o
- •
2
3
3
*999Q
0
3
2
2
2
TIO
M/GALI
. 00
.08
•&2
.21
•~12
.68
.99
.'19 ""
.00
.57
.11
. 66
. 89
. G 5
VEH T
DIS°
ANK-
LIO
TEMP
(DFG
3 •
T •
6.
17.
9."
10.
7.
"4".
6.
5.
-2.
1.
.._ ___
F)
00
__
30
00
__..
00
00
00
00
3D
00
30
GO
00
co
00
-------
STATION: GULF PROCESS: GULF BALANCED LOCATIONS UNIVERSITY
BOUNDARY
DATE:
LICENSE
NUMBER
XVC286
093GFK
117KPH
OV9512
232GSN
KTR796
216KXG
EHV401
265KXL
8708ML
225HQB
77263V
78059V
SMI602
o
co
RETURNED
VAPOR
(CU FT)
0.00
.86
0.. 00.
.12
.02
.87
.67
1.02
.3k
.15
.
-------
STATION: GULF
PROCESS* GULF BALANCED
LOCATION: UNIVERSITY * BOUNDARY DATE:
LICENSE
NUMBER
TtfW7i»<»
281BIJ
KSU028
962GAP
TXG511
RETURNED
VAPOR
CCU FTI
0.00
1.05
i.<+o
1.56
.02
STANDARD
RETURNED
VAPOR
(CU FT)
0 .uG
l.Q*
1.33
1.5**
.02
RET VAP
TO
OISPL LIQ
RATIO
(CF/CF »
0.00
.91
.73
.75
.03
CILL
RATE
(GPM)
5.57
5.2*.
7.05
6.16
5.7C
VEH TANK-
UNO TANK
TEMP
(DEG F)
*99.99
15. CO
13.00
17. OD
3 £• . 0 0
VAPOR
MASS
(GM)
G.QG
38.63
<46.25
52.1,2
.68
VAP MASS
TO
DISP LIQ
RATIO
(GM/GAL)
0. CO
I..02
3.28
3.*»0
.12
VEH TANK-
OISP LIQ
TEMP
(DEG F)
*99.99
8.00
6. OP
10. On
31.00
o
CO
ro
O
-------
STATION* STANDARD.
PROCESS! STANDARD BALANCED
LOCATION: BALTIMORE .+. LAKE MURRAY DATE: 6/17/7<+
LICENSE
NUMBER
kkVJEL
M» 763 S
359KZC
918KKL
730HNF
890«»6N
WS U77 3
932HWN •
5k 9 JL 3
XXX
57 tf KM K
205JRT
MWBP
1587*. V
0
CO
ro
RETURNED
VAPOR
(CU FT)
. 76
.5k
1.3U
2.56
1.16
2.23
.37
1.00
.36
.3k
.55
1.01
.39
1.95
STANDARD
RETURNED
VAPOR
(CU FT)
.76
.5k
1.33
2.52
1.1k
2.25
.36
.99
.36
.3*4
.5k
1.00
.37
1,93
RET VAP
TO
QISPL LIQ
RATIO
(CF/CF)
1.16
.79
.50
.32
.33
. 75
.32
.7k
.76
.72
.5k
.66
.63
1.76
FILL
RATE
(GPM)
k . 9 C
5.56
7. 20
..,,
5.89
6.00
5.67
6.67
7.0 G
7.jO
6.0G
5.95
1+.56
5.35
VFH TANK-
UNO TANK
TEMP
(DEG F)
9. GO *
-5.00 *
15.00
5.0C
17.00
l.CC
7.00
15.00
<4.CO
17. GO
27.00
23.00
25.00
-1.00
VAPOR
MASS
(GM»
9999.99
9999.99
37.07
62.17
39.01
72.? 6
ll.<»7
31.76
11.27
9 . & C
19. G5
35.05
*..*.
61.3^
VAP HASS
TO
DISP LIQ
RATIO
(GM/GAL)
*9999. 99
*9999.99
1SH 7
• o f
k. 03
3.79
3.21
1.35
3.1fl
3.22
?. 7k
2.5k
3.22
2.55
7.5k
VEH T.ANK-
OISP LIQ
TEHP
(OFG F)
6.00
-8.90
12.30
2.00
13. ao
-2.00
3.00
11.00
0.00
12.00
21.00
'18.00
20 .00
-6.00
-------
STATION: STANDARD PROCESS: STANDARD BALANCED
LOCATION? BALTIMORE + LAKE MURRAY DATEJ 6/17/74
LICENSE
NU M8E R
292GOZ
545HTC
570CYM
V28979
786KXO
C12JOH
VNX430
315KZB
519KZE
DUL602
ZQM799
590BAG
675EAU
22 8LK V
o
i
OJ
ro
ro
RETURNED
VAPOR
ICU FT)
-.34
1.68
2vl7
.70
1.29
.38
1.00
2.01
1.99
0.00
1.20"
.17
1.27
.29
STANDARD
RETURNED
VAPOR
(CU FT)
-.34
1.65
2.14
.69
1.27
.37
.99
1.98
1.96
O.iJJ
1.19
.17
.29
RET VAP
TO
DISPL LIQ
RATIO
(CF/CF)
-.48
.71
.90
l.OC
•57
.54
.96
.76
.85
0.00
.39
.13
.41
5
5
5
2
5
5
"5
5
6
e
5
6
5
^TLL
RATE
(GPM)
.20
.80
.62
.97
.33
.67
.6 8
.43
.80
.rc
.17
.16
.47
VEH TANK-
UNO TANK
(
20
2
3
11
18
7
"9
22
10
12
in
8
TEMP
DEG F)
.CO
.00
.00
.00
.00
. oc
.00
.00
.cc
.00
.GO
.CO
.00
VAFOR
MASS
CGM)
-11.27
64.18
30.72
22.56
51.30
35.72
76.93
76.17
0.00
6.79
11.15
VAF MASS
TO
OISP LIQ
RATIO
IGM/GflL)
-2.17
3.69
4. 53
4.34
3.07
2.83
,.6,
3.97
4.43
o. on
4.81
.69
2.54
2. 14
VFH TANK-
OISP LIQ
TEMP
(OEG
-3.
11.
^
-6.
3.
11.
0.
-2.
*99.
12.
-1.
6.
3.
5.
. — -
F)
00
90
.PI
00
30
on
00
00
99
00
00
on
an
00
. . —
-------
STATION: STANDARD
PROCESS* STANDARD BALANCED
LOCATION: BALTIMORE «• LAKE MURRAY DATE: 5/i7/7<*
LICENSE
NUMBER
295KQQ
RETURNED
(CU FT>
.07
STANDARD
RETURNED
VAPOR
(CU FT)
.07
RET VAP
TO
OISPL LIG
RATIO
(CF/CF)
.0*4
FILL
RATC
!CPM,
5.53
Vr.H TANK-
UNO TANK
TEMP
(DEG F)
*99.99
VAPOR
MASS
(GM>
2.39
VAP HASS
TO
OISP LIQ
RATIO
(GM/GAL)
.22
VEH TANK-
OISP LTQ
TEMP
(OEG e)
*99. 99
co
ro
to
-------
STATION* STANDARD
PROCESS* STANDARD BALANCED
LOCATION: BALTIMORE
LAKE MURRAY DATE: 6/15/71*
LICENSE
NUMBER
5970WY
915HWP
751GGX
427KQR
172FVP
031H01
074KQ5
679GTH
903KLW
678GUP
572FFR
C82JOK
311JLE
723HPP
o
CO
ro
RETURNED
VAPOR
(CU FT)
.Li
2.67
2.23
2.70
.85
2.19
1.33
2.78
.20
.74
1.10
.23
1.22
.83
STANDARD
RETURNED
VAPOR
(CU FD
.01
2.65
2.21
2.67
2.16
1.31
2.76
.20
.73
1.09
.23
1.20
.82
RET VAP
TO
DISPL LIO
RATIO
(CF/CF)
.01 3
1.07 5
.94 5
.95 5
1.03' 5
.83 5
1.01
1.02
.34
.76
.-33
.20
.59
.71
3
6
c
6
5
5
4
5
RA
TE
(GPM)
.64
.84
.71
.55
.63
.69
.64
.06
.73
.17
.11
.06
.56
.32
VFH
UNO
TANK- VAPOR VAP MASS VFH TANK-
TANK MASS TO OISP LIQ
TEMP
(OEG F)
-l.GO
-10.
-7.
-4.
-10.
6.
3.
-3.
14.
12.
10.
15.
26.
16.
CO
00
CO
OG
00
00
CO
00
oc
00
00
GO
CO
DISP LIQ TEMP
RATIO
(GM> (GM/GAL) (OEG F)
.24 .02 -6.
76.63 4.14 -15.
6u . 45 3.43 -12 .
73.16 3.52 -7.
23.03 3.78 -12.
61.58 3.33 3.
38.u6 3.93 -3.
78.47 3.88 -9.
5.71 1. 33 _ _9_.
24.22 3.36 5.
36. 01 3. 67 " ~3i
7.5G .87 .8.
44. 74 2. 94 20 .
29.65 3.45 11.
0
0
OD
00
0
0
0
0
r\
0
0
a
00
00
0
0
0
0
"o
0
0
0
0
0
-------
STATION! STANDARD
PROCESS: STANDARD BALANCED
LOCATION: i34LTIMORF
LAKE MURRAY DATE: 6/18/71*
LICENSE
NUMBER
ZN026<*
701BLK
SPOOK J
U38CTY
RETURNED
VAPOR
fCU FT)
1.35
!.!<»
1.83
.67
STANDARD
RETURNED
VAPOR
(CU FT)
1 . 33
1.12
1.81
.66
RET V4P FILL
TO RATE
OISPL LIQ
RATIO
(CF/CF) (GPH)
.83 5 . b A
.55 5.07
.88 5.^C
.66 *99.99
VcH TAMK-
UNC TANK
TEMP
(DEC- F)
16. CO
23.00
3.00
19.00
VAPOR
MASS
(GM)
-------
STATION* STANDARD
PROCESS: STANDARD BALANCED
LOCATION: BALTIMORE «• LAKE MURRAY DATE: 6/19/71+
LICENSE
NUMBER
€388293
17 OFT 0
8U2GOZ
6<»5KZR
603ESM
399CQQ
NOZ7C7
5<»5HTC
103AFM
239CTV
G1157327
260KZE
M5jrc
302JQU
RETURNED
VAPOR
(CU FT)
1.G8
.52
.01
2.,,
.72
.8<+
1.28
1.26
.9<+
1.32
.25
1.17
2.30
2.01
STANDARD
FETURNEO
VAPOR
CCU FT)
1.10
.53
.01
2. ,7
.73
.*<+
1.28
1.26
,9i»
1.32
.25
1.16
2.29
2.00
RET VAP
TO
OISPL LIQ
RATIO
(CF/CF)
.»,
.<+!
.01
1.3P
.57
1.21
.*,
.63
.77
.77
.13
1.0.1
.98
.90
FILL
RATE
-------
STATION: STANDARD PROCESS? STANQARO 3Ai_ANCEp . ....LOCATION:.3ALTi«QRs_*_. LAKE...HURRAY DATE:, 6/ig/7<*
LICENSE
NUMBER
F42556
545JSK
603G8Y
C38KQR
UUP038
438JUA
999HGP
338JQN
907KES
SrtKNK
122JQV
105HDT
RKPSflO
534KZR
o
i
OJ
ro
••4
RETURNED
VAPOR
CCU FT)
.39
.24
.63
.0%
1.20
'••: 1.06
.76
1.68
l.fl<*
1.20
.85 '"
. .1.0.6
.32
.28
. . . -_ . ,.
STANDARD
RETURNED
VAPOR
(CU FT)
.39
.2k
.63
.0,
1.19
1.05
.75
1.67
1.03
1.19
-«v •
1.05
.32
.28
RET VAP
TO
OISPL LIQ
RATIO
(CF/CF)
.13
.15
.90
..3
.85
1.05
.81
.99
1.06
.7,
.63"
.«*
.53
.2k
CILL VFH TANK-
RATE UNO TANK
TEMP
(GPM) (Dr.G F)
5 . k 5 -15.00
5.58 -4. CO
7.<+3 4. G 0
3.53 *99.99
6.3C -7.00
\
5 . Q 0 - 7 . G 0
k.67 13.CO
6.30 -3.00
4.61 l.CO
6 . u 0 16.30
3.6<+ 17.CC
5.82 24. CO
k . 1 5 7 • w 0
5 . k 3 <» . 0 0
VAPOR VAP MASS
MASS TO
DISP LIO
RATIO
(GHI (GM/GAL)
10.17 .64
6.3fi .53
15. S4 3.05 '
1.1
-------
STATION: STANOARO ..PR.OCE.SSJ ..STANOARQ. BALANCE])
LOCATION: BALTIMORE «• LAKE MURRAY DATE: &/t9/7<+
LICENSE RETURNED STANDARD
NUMBER VAPOR RETURNED
VAPOR
-------
ST ATI 0 N t__ I£XAfiQ_ ._. ERQCES. 5 *.._£ N V.I R OJLIC.S 1 L.Q.CAILQ N.?. 3 ALT I MORE . t. F L E 1C HER
0 A IE. _L_6/L2_0 /Z4_
LICENSE
NUM3ER
6518EB
124ELL
62 3HT S
FWA684
THE7K
48825L
WYM083
WJ U45 6
770KLB
305HOS
WSC130
STEAM 2
MH1510
93 353 G
RETURNED
VAPOR
(CU FT)
*99.99
8.27
4.40
5. 11
3.C8
.97
1.67
16.67
17.45
6.97
3.6V"
2.62
10.46
*99.99
STANDARD RET VAP FILL
RETURNED TO RATE
VAPOR
(CU FT)
*99.99
7.81
4.13
4.77
2.85
.91
*99.99
15.35
16.16
6.51
3.33
..2.41
9.33
*99.99
DISPL LIQ
RATIO
(CF/CF) (GPM)
*99.99
3.89
8.59
5.67
1.72
3.76
*99.99
7.66
6.76
2.47
6.91
5. 00
5.29
*99.99
7.2C
7.50
7.2C
6.30
6.76
7.20
6.00
4.39
7.67
7.16
2.16
.J? •!./_'.
*99.99
VEH TANK-
UNO TANK
TEMP
(OEG F)
7.00
5.00
8.00
c.oo
6.00
7.00
9.00
17.00
13.00
19.00
1C. CO
14.0.0..
6. CO
5.00
*9999
125
25
37
41
4
*9999
246
200
64
13
8b
*9999
VAFOR
MASS
(GM)
.99
.15
.66
.28
.22
.99
.11
.64
.00
.76
« 06
."+5
."99
VAP
MASS
TO
VEH TANK-
DISP LIQ
O.ISP LIQ TEMP
RATIO
(GM/GAL) (OEG F)
*9999
8
7
5
3
2
*9999
16
11
3
3
5
6
*9999
.99
.34
.13
. 88
.33
.34
.99
.41
.21
.25
.82
•.1.8
.22
.99
4.
2.
4.
-4.
2.
2.
2.
12.
7.
14.
5.
3.
2.
00
00
OQ
00
00
00
00
3C
00
00
__
QQ
00
ro
vo
-------
STATION: TEXACO
PROCESS* ENVIRCNICS
LOCATION: BALTIMORE + FLETCHER
QATEl 6/2C/74
LICENSE
NUMBER
RETURNED
VAPOR
STANDARD
RETURNED
: VAPOR
,j£. (CU FT1
314GXE
PHBllO
662FZG
384KLQ
77458U
DYN439
53013L
571HOT
496JQS
14 382 R
37 778 W
UKW764
ZXM762
963GOY
0
to
. 1-.*.
1.
1.
2.
4.
5.
9.
2.
12.
1.
5.
7.
5.
62
60
C6
30
05
34
30
13
28
97 ~
67
75
22
(CU
12
1
10
2
3
4
8
2
12
1
5
7
4
FT»
.57
.46
.33
.93
.40
.74
.91
.56
.01
.73
.32
.29
.13
.78
RET VAP
TO
FILL
RATE
OISPL LIQ
RATIO
(CF/CF)
5.
3.
2.
3.
3.
4.
5.
4.
5.
3.
4.
5.
3.
11
07
03
32
18
13
48
18
5C
77
71
23
08"
(GPM)
6.42
S.64
5 . 95
8.64
9.26
9.60
7.12
5.20
5.40
6.29
7.20 ""
5. '3 3
4.35
VFH TANK-
UNO TANK
TEMP
(OEG R
6. GO
G.QO
17.00
34.00
19.00
9. DO
22.00
6. CO
16.00
3.03
23.00
13.00
9.00
21.00
VAPOR
MASS
VAP MASS VEH TANK-
TO QISP LIQ
OISP LIQ TEMP
RATIO
(
104.
14.
64.
3.
22.
34.
63.
53.
17.
98.
7.
32.
55.
47.
GM')
02
51
38
31
35
53
15
68
73
51
31
33
00
(GM/GAL* (OEG
5.65
4.03
2.24
4.13
3.96
7.14
4.54
4.91
5.71
2.C9
3.91
5.42
4.05
•-
2.
-4.
13.
».
14.
4.
17.
1.
11.
_ o
i- •
18.
8.
4.
16.
- - -.
F)
00
00
on
00
00
on
•30
OH
00
no
on
o_n _
00
00
-------
STATION: TEXACO PROCESS* ENUIRONICS _ .LOGATION:J BALTIMORE + FLETCHER
DATE! 6/20/71*
LICENSE
NUMBER
•:
973JQP
i FPN866
234HKK
716KPH
744GOX
76 DBS 8
444JLC
SNP596
475KLX
46287P
726PVX
785JLA
TAM267
AZV456
RETURNED
VAPOR
(CU FT)
3.54
5.99
2.03
2.26
5.34
6.18
2.C7
5.40
20.60
13.37
8.04
6.50
1.69
1.90
STANDARD
RETURNED
VAPOR
(CU FT)
3.26
5.55
1.94
2.03
4.98
5.69
1.90
4.97
19.03
12.34
7.49
6.05
1.59
1.76
RET VAP
TO
DISPL L
RATIO
(CF/CF)
3.3d
5.77
4.04
4.33
5.47
4.63
3.96
4.48
7.23
5.16
4.79
5.08
6.62
2.43
CILL
RATE
IQ
(GPM)
9.19
5.76
8.64
9.0C
7.7C
6.90
7. an
6.92
4.38
6.14
6.27
6.28
7.20
10.80
VEH TANK- VAPOR
UNO TANK MASS
TEMP
(DEG F)
12.00
17.00
17.00
15.00
26.00
16.00
17.00
22.00
17. CO
15.00
11. GJ
16.00
18. CO
12.00
«GM)
39.
37.
16.
14.
41.
52.
9.
43.
137.
172.
59.
43.
3.
13.
74
31
06
31
17
98
35
70
78
26
13
79
30
63
\/AF
MASS VEH TANK-
TO OISP LIQ
DISP LIQ TEMP
RATIO
(GM/GAL) (OEG F)
5.
5.
4.
3.
6.
5.
2.
5.
6.
9.
4.
4.
1.
2.
38
18
47
89
05
76
74
27
99
62
97
92
83
52
7.
12.*
12.
10.
21.
11.
12.
17.
12.
10.
6.
11.
13.
7.
00
oo ;•;
00
on
00
00
00
oo "•'•'•
ad
oc
00
M
00
00
o
CO
-------
STATION! TEXACO .. PROCESS? ENVIRONICS
LOCATION: BALTIMORE * FLETCHER
DATE? 6/20/74
LICENSE
NUMBER
KOW808
17662 T
20 263 T
400JSJ
WAC301
TC8765
710KLT
731ELS
398DLD
Q81073
VNV049
KGS913
r>
i
OJ
u>
RETURNED
VAPOR
CCU FT)
1.07
2.62
3.65
3.49
2.03
2.21
2.13
5.55
2.02
2.86
11.11
4. 83
STANDARD
RETURNED
VAPOR
(CU FT)
.99
2.42
3.36
3.22
1.87
2.07
1.97
5.13
1.86
2.68
10.23
4.49
RET VAP
TO
DISPL LIQ
RATIO
(CF/CF)
4. 1C
3.36
3.65
6.69
3.88
4.30
2.95
4.00
3.37
5.57
4.97
3.7*3
^ILL
RA T E
(GP'M)
7.20
8.10
8.28
8.64
6.75
5.40
8.57
6.4G
8.64
*.,.
6.51
10.68
VEH TANK-
UNO TANK
TEMP
IOEG F)
13.00
26.00
19.00
25. CO
3C.CO
21. OC
22.00
19.00
12. OC
12.00
22. OC
11.00
VAPOR
MASS
(G.M)
2.04
16.30
26.10
..«
18.33
16.05
19.35
50. 39
18.31
16.54
74.05
37.19
VAP MASS
TO
DISP LIQ
RATIO
(GM/GALI
1.13
3.02
3.78
2.31
5.09
4.46
3. 87
5.25
5.G9
4.62
4.81
4. 18
VEH TANK-
DISP LIQ
TEMP
(OEG F)
8.00
21.30
14.00
20.00
25.00
16.00
17.00
14. OD
7.00
7.00
17.00
6.05?
-------
STATION: UNION .76 . PROCESS: PROCESS PRODUCTS
LOCATION: WARING
ZTON
LICENSE
NUMBER
960KZO
L36087
609677
72C85W
955KLP
OE RE EN
TAC138
RUU483
866DNO
233HMS
68CGOC
14 C 22V
833FVQ
350G08
o
CO
CO
Cv>
RETURNED STANDARD
VAPOR RETURNED
VAPOR
(CU FT) .
-------
STATION: UNION 76
PROCESS: PROCESS PRODUCTS
LOCATION: WARING + ZION
DATE: &/2**/7<+
LICENSE
NUMBER
73 14 6 W
OVC759
02389^7
WC MSL M
RETURNED STANDARD
VAPOR RETURNED
VAPOrT
VAP MASS
TO
DIS'P" LIQ "
RATIO
CGM/GAL)
VEH TANK-
giSP LIQ.
TFHtP
<_QEG F
^ft.^S ^.83 2.00
69.91 ........... "^.89 "ITTcH
71.36 . >.76 ..... J.4 . Q 0 ..
21.97 6.28 25.00
17.56 3.51 "a'Tv1-"
39.11 4.5C '.?.._03.
* 9999. 99 *9999.99 83.00
o
CO
-------
APPENDIX C-4
VAPOR COLLECTION RATIOS
C-4
-------
STATION:. STANDA.R.O PRQ.C.ESS: INTERMA^K
LOCATION: CARMEL VALLEY .*. .15
DATE:
LICENSE
NUMBER
932HHN
080EAT
E 3 3097i.
059KFQ
YYG563
GQP31G
61969
COLLECTION RATIOS
GM/GAL
2<+6.
* 39 .
325.
178.
21.7.
130.
191.
161.
U59.
212.
255.
ISC.
3«.5.
326.
76
99
lu
77
37
C^
61
7*4
91
3H
10
29
Ob
39
CF/
270.
*99.
333.
136.
. 2<»7.
2j2.
201.
219.
56Q.
237.
27
-------
STATIONI STANDARD
PROCESS: INTERMARK
LOCATION! CARMEL VALLEY
15
DATE* &/ 6/7<+
LICENSE
NUM9ER
96695E '
xrvoso
R27816
TUCKIE
9500VE
V *i A 6 3 6
026SHA
2«Acy
588YHU
Q29ESQ
2LX232
838GOA
830HPA
651FVR
COLLECTION
GH/GAL
251.25
203.59
296.67
335. t»5
361.18
312.77
328.79
mo. 95
239.65
250.«»7 . ' '""
3^.50
260.90
319.16
336.65
RATIOS
CF/CF
2^.73
186.6?
277.10
373.2?
390.53
338. 35
363. 19
. 105.86
225.71
236.90
316.^^
262.80
273.67
3 00. 7?
o
ja.
ro
-------
STATION! STANDARD
PROCESS I INTERMA^K
LOCATIONS CARMEL VALLEY + 15
QATEt 6/ 6/74
o
LICENSE
NUMBER
829360
902QOT
1335VV
.HM.X668
XDU752
296KBI
.SKE220 .......
«+153
<*152
136LEC
329HQA
CU0923
T0523697
COLLECTION RATIOS
GM/GAL CF/CF
322.19 32^.55
2«»9,9.9. 259.52
2^.5k 232.33
318.20 332.08
2.31-55. .222.37
350.02 J96.91
.277..M._... _ 281.15
361. <*3 <*C5.7}
779.06 "90P.i»ir"
350.59 377.73
22«».89 21u.ia
3-4C.86 361.75
302.02 328.35
00
-------
ST ATI 0N.l_SJjAN0_ARQ PROGE;SS_l__IN.TERMARK__ LOCAJ_10Ni_.CARHEL_V_ALLEY _#•_.15. 0A_TE t_6/_J&/7f*_
_____^ _ ___..„„_.___..._„_„.„
NUM3ER GM/GAL CF/CF
~~~ "*»060KA"~ ~"~ 276"^5 "" ~279"."4"5"
2JZ8J1Q1, 360.73 3
-------
STATION! .UNION 76 _. PROCESS: PROCESS PRODUCTS
LOCATION.: WARING + ZION
OATEt 6/11/7U
LICENSE
NUMBER
ZMPU01
079EQU
1*1160
937JFS
672GXG
mjE,.
O^IGOA
TGT771
&62JQT
U22HOS
736JLA
072FKX
539ESK
613KAC
COLLECTION
GM/GAL
*99.99
101.21
94.95
9C.U3
92.03
i=z.8.
S8.5U
91.18
1-07.81
S3. 01
11U.56
10C.2Q
32.61
82.31
RATIOS
CF/CF
*99.99 " ".
150.77
132.01
122.18 " ~
119.59
1 1 5 . 5 H
13C.72
171.75
152. UU
127. t»6
17U.11
152.21
16U.72
136.5?
01
-------
STATIONS UNION 75 PROCESS: PROCESS PRODUCTS
LOCATION: WARING + ZION
HATE: 6/11/74
LICENSE
NUM3ER
<*3 20<+ U
799JEH
RJP777
059GJX
WLN696
WBF900
100LR1221
117GXA
COLLECTION RATIOS
GM/GAL CF/CF
36.23 ibk.b5
86.^2 176'7H
87.63 1&Q.<*T.
»^».29 125.30
72.16 lif*2^
lu6.i*J 131.93
131.5ft 17U.7V
116. Qi* 178.«8^
1C8.8C! 163.26
37.06 152.63
106.k5 189.45
96.Cl
-------
STATION*
PROCESS* GULP BALANCED
LOCATION! UNIVERSITY + BOUNDARY DATE? 6/12/74
LICENSE
NUMBER
1043376
711KLQ
12331R
72506W
603G3Y
TRN863
312HPO
0 Q 0020
117JC72
90JOSM
KOY327
162DVQ
205JRT
264FNL
COLLECTION
GM/GAL
60.13
55.50
69.54
' *99.99
21.65
77.91
66.83
61.14
52.31
71. 83
34.9?
81.75
113.63
74.02
RATIOS
CF/CF
62.23 " ~~~
55.75
71. 34
*99.9'}
24.91
61.91
67.65 '
60.24
52. G 2
70.45 "
93.06
«4.01
1G9.43
74.11
o
I
-------
STATION* GUI.17
PROCESS: GULF BALANCED
LOCATION: UNIVERSITY + BOUNDARY
DATE: 6/12/7**
LICENSE
NUMBER
60421F
<*i*6JEC
526GGC
236KLM
1Q1ASI
6 5 3 F 3 X
' ZQ0792
V297<+1
RG059<+
8639<*e:
63<30LX
550KPG
611GGS
li»6HDT
COLLECTION
GM/GAL
5C.96
105.51
105.13
98.31
O.OC
97.16
-12.63
13«».63
112.78
65.39
37.32
<*1.82
!!•«*.<*&
a.2i*
>
RATIOS
CF/CF
51.8?
103.79
IOC. 63
89.11
0.0^
99. 9 LI
-11.06
131.77
159. 3^
" 64/32 " ~ ""~" " "
91. 2 3
39.99
99.06
4. OH
o
I
oo
-------
STATION: GULF
PROCESS« GULF BALANCED
LOCATION! UNIVERSITY *• BOUNDARY DATE! 6/12/7U
o
I
VO
LICENSE
NUMBER
159KZQ
COLLECTION RATIOS "
GH/GAL CF/CF
1U6.71
-5.3G
96.0"
-U.90
AVERAGr.
67. 9
-------
STATION: GULF
PROCESS: GULF BALANCED
LOCATION: UNIVERSITY *• BOUNDARY
DATE: 6/13/71*
LICENSE
NUM3ER
0.72737
7873<+L
105HDT
93229G
QMV735
9990UH
KUL505
909JSZ
3760CJ
663KHW
TXG71
-------
STATION: GULF
PROCESS I ..GULF B AL A NG£ 0
LOCATION: UNIVERSITY
30 UN OAR Y
LICENSE
NUM3EP
OUM753
0238796
735GDW
2388EX
VEU721
u»m*
1220FK
»7.0R
TTF-376
535G8T
XTL389
OZTC57
f
COLLECTION
GM/GAL
16.95
98.32
123.23
82.50
~ £ 3 . .33
110.98
62.^7
43.06
120.
-------
STATION: GULF
PROCESS* GULF BALANCED
LOCATION* UNIVERSITY + BOUNDARY DATE? 6/13/74
o
i
_i
ro
LICENSE
NUMBER
86467P
728FEA
TST284
H54055
_?>1QZE
5343XV
743CTT
735DQK
537KAC
378GNZ
508KHV
COLLECTION RATIOS
GM/GAL CF/CF
117.90
85.92
0. OG
37.19
46.18
111.26
1*5.03
1C7.88
94.86
73.95
103.84
*99.99
90.
0.
36.
51.
121.
106.
108.
100.
75.
105.
*99.
43
00
3^
05
42
23
94
36
23
60
99
-------
STATIONS GULP
PROCESS: GULF BALANCED
LICENSE
NUMBER
389CEC
55278S
ZRDLR2733
VNM013
FQAQ5«
9625AP
226^70
OZN598
111KLP
246
-------
STATION! GULF
PROCESS* GUL17 BALANCED
LOCATION: UNIVERSITY * BOUNDARY DATE: 6/13/74
LICENSE
NIIM3ER
48457W
WRY045
XQR052
228KZC
236ANU
«7«,
VSL427
COLLECTION
GM/GAL
145.33
6.17
*99.99
3.61
21.87
5o.56
74. 30
RATIOS
CF/CF
115.81
5.33
'99.99
^.57 -
?3.97
Do. 2 3
77.5i+
AVERAGE
75.^9
73.6^,
o
I
*»
-------
STATIONI GULF
PROCESS: GULF BALANCED
LOCATION: UNIVERSITY
BOUNDARY
DATE: &/i<»/7<*
LICENSE
NUMBER
76625H
6G3G3Y
XWE767
E326^6
130HQE
312HPO
0«*5CH>
12831R
3 2 391 E
OWNU
S11HSD
^053F
700KFC
72<4CTU
COLLECTION RATIOS
GM/GAL CF/CP
*99.99
103.79
106.33
^2.^
0.00
1 J C . 6 7
7^.23
10^.29
106.62
8U.1B
110.37
7.31
37.6k
12^.29
*99.9^
98.15
97.13
38.15
C . 3 1
31.75
67.7-?
95.27
92. M
7<,.8<,
9.S.U7
6.93
35.3?
112. <,?
f
in
-------
STATION! GULF
PROCESS: GULC
LOCATION: UNIVERSITY * BOUNDARY OATEJ
LICENSE
NUMBER
P29192
630GOC
DZN300
379HMW
CREATE
1Q5JSX
OOJ977
UZA117
0<»5GXH
BTJ-788
RQX308
HTKI.H
060HZL
55i*COA
COLLECTION
GH/GAL
137.
1 0 i 9 .
130.
130.
iiO.
116.
G.
e.
31.
3^.
0.
0.
<*6
92
72
5C
19
8-J
<*5
00
00
90
25
U 0
00
RATIOS
CF/CF
122.
97.
116.
S3.
93.
100.
0.
*99.
C.
?9.
29.
C.
0.
31 " ~~
«1
60
16
37
23
7^
0'>
99
00
57
7/4
o^ "
00
o
-------
STATION.: GULF
PROCESS* GULF BALANCED
LOCATION* UNIVERSITY + BOUNDARY
DATE: 5/14/74
LICENSE
NUMBER
TWA441
36-0699
M12136
ZZW270
373COR
235JEG
OZV830
9i6CPtf
632AVL
VI X 95 7
KPP346
WJX321
RSS989
W3^424
COLLECTION
GM/GAL
2.67
70.72
119.91
c.on
107.79
0 . iiii
G.OO
92.43
O.OC
64.72
*99.99
87.47
137.57
.45.63.
RATIOS
CF/CF
2.61
62.00
105.12
c.on
96.95
c . o :
o.dn - • - -
82.15
0.00
.53.44 " ' :
*99.99
79.59
121.7-1
43.42
r>
i
-------
STATION: GULF
PROCESS: GULF BALANCED
LOCATION: UNIVERSITY * BOUNDARY
DATE!
LICENSE
NUH9ER
77111R
756CYO
XN0019
0233<+01
TV5029
VEP32C
WIW853
XVD93**
SO'tGJD
6^EOY
VES152
,3?5JH
RDJ199
XOR989
COLLECTION
GM/GAL
c.oo
2.143
78.23
111.79
3.86
116. n-j
*99.99
5.61
P.Ou
in 6. a 6
3.25
72.27
ttl.23
67.52
RATIOS
CF/CF
O.QO
2.21
67.72
1C. 6. 5 3
3.1.9
101.27
*99.99
if. 80
0 . 0 i-!
99.34 ":
3.59
96.39
73.76
63.V9
r>
i
i
oo
-------
STATION: GULF
PROCESS: GULF BALANCED
LOCATION: UNIVERSITY * BOUNDARY
OATEt 6/lW7<»
LICENSE
NUMBER
XVC236
093GFK
117KPH
OV9512
232GSN
216KXG
EHY'tDl
265KXL
8703ML
225HQ8
77263V
73059V
SMI602
COLLECTION
GM/GAL
0.00
109.51
O.CO
40.25
4.91
94.23
97.56
167.21
43.85
* 99 . 99
58.10
*99.99
*99.99
* 99 • 99
RATIOS
CF/CF
C.OQ
93.8?
0.00
4?. 45 " ~ "
<*.37
78. 44
88.51
143. 71
35.40
*99.99
51.31
*99.99
*99.99
*99.99
o
I
-------
STATION* GULF
PROCESS* GULF BALANCED
LOCATION: UNIVERSITY + BOUNDARY
DATE:
o
I
ro
o
LICENSE
NUM3ER
2813IJ
K3U028
962GAP
TXG511
AVERAGE
COLLECTION RATIOS
GM/GAL CF/CF
*99.99 *99.99
123.55 I.08'?2*
98.11 9<+.C2
107.3k 103.53
5.25 6.Of
62.16' 56.24'
-------
STATION: STANDAR3
PROCESS: STANDARD BALANCED
LOCATION: BALTIMORE
LAKE MURRAY DATE: 6/i7/7i»
LICENSE COLLECTION RATIOS
NUM3ER GM/GAL
*»<+9JEL *52
<»<,763S *<*7
359KZC 6C
91P.KKL 11U
7JOHNF 12<»
3 9 C 4 •;> N « 7
WSU778 36
932HWN 101
5'-f9JL8 89
XXX 8fi
2Q5JRT 113
69<,HOF . 95
1587'T\/ 195
.59
.2*f
.69
.63
.^9
.io
. 63
.52
.^4?
.69
.7.^
.16
.A5
CF/CF
*99.99 "—
*99.99
72.4+5
111.11
122.33
0^.35
39.11 ~~
10^.91
88.7*
10*+. 19
95.«+6
112. <»a
117.9^
1^-6.23
o
I
ro
-------
STATION: STANDARD PROCESS: STANDARD SALANCEQ
LOCATION: BALTIMORE *• LAKE MURRAY DATE: 6/i7/?a
o
LICENSE
NUMBER
292GOZ
5>5HTC
570CYM
V2(3979
736KXO
Gi^JOH
VNX^JO
315KZ3
519KZE
OUL6C2
ZQM799
5903AG
675EAU
228L
99.56
1C5.^
69.61
7 6 . .? H
111. Ul
86.03
*99.9)
0.01
1C2.01
16.38
53.95
52. 3^
ro
ro
-------
STATION: STANOARO PROCESS: STANDARD OALANCED LOCATION: BALTIMORE + LAK? MURRAY DATES &/17/7**
f
ro
LICENSE COLLECTION RATIOS
NUMBER GM/GAL CF/CP
395KQQ *99.99 *99.99
AVERAGE 86.02 82.63
-------
STATION* STANDARD PROCESS* STANDARD BALANCED
LOCATION: BALTIMORE + LAKE HURRAY DATE:
LICENSE
NUMBER
597DWY
915HHP
751GGX
<+27KQR
172FVP
03 Irio1
COLLECTION RATIOS
GM/GAL CF/CF
679GTH
9Q3KLW
678GUF
572FFR
311JLE
723HPR
.62
97.56
90.15
91.72
95.87
105.26
97.Ul
99. 31*
105.63
26.76
107.33
110.22
.73
99.92
91.13
U0.15
100.13
i •:• &. 9 7
112.36
103.55
46.67
96. 19
1Q 1. k ;i
26. 33
101.95
100.8?
o
f
ro
-------
STATION: STANDARD PROCESS: STANDARD BALANCED LOCATION: BALTIMORE «• LAKE MURRAY nATE» 6/18/7^
' 'LICENSE COLLECTION "RATIOS
NUM3ER GM/GAL CF/CF
ZN026<* 119. 09 117.^3
7013LK 5.96 99.33
^33CTY 101.86 99.31
AVcRAGF Z7. i<~> 86.65
ro
en
-------
STATION! STANDARD PPOCESSl STANDARD EALANCEO
LOCATION: BALTIMORE + LAKE HURRAY DATE: 6/19/7*+
LICENSE
NUMBER
0388293
170^TO
842GOZ'
645KZR
603ESH
3,*W
NOZ707
545HTC
103AFM
239CTV
G1157827
260KZE
405JYC
302JQU
COLLECTION
GM/GAL
*99.99
1ft. 61
-.9.99
99.00
57.01
1,6.6*
79.90
96.43
112.89
113.02
9.91
78.45
1GC.47
75.00
PATIOS
CF/CF
*99.99
39. 7d
*99. 99
1 G 4 . :3 3
61.43
i«.2J
86.30
102.93
120.61
105.24
12.12
91.03
1G6.S?
80.46
o
ro
-------
STATION! STANDARD
PROCESS* STANDARD BALANCED
LOCATION: BALTIMORE «• LAKE MURRAY DATE: 6/19/74
LICENSE
NUMBER
F42556
545 JSK
603G3Y
038KQR
UUPQ88
43iiJlJA
999HGP
338JQN
907KES
574KMK
122JQV
105HDT
RKP830
.S3«Z«
0
COLLECTION RATIOS
G MX GAL CF/C-
13.
12.
81.
*99.
.76.
-17.
1C3.
99 .
112.
117.
97.
79.
68.
30.
80
67
68
99
63
11
32
3?
21
02
25
20
19
61
15.15
14.06
99.64
'99.99
7*.4?
95.47
103.3^
lG4.3n
115.1 9
1Q9.45
94.31
82.60
64.33
28. (l^
I
ro
-------
STATIONS STANDARD PROCESS! STANDARD BALANCED LOCATION? BALTIMORE «• LAKE MURRAY DATE: 6/19/7V
o
f
ro
OP
LICENSE
NUMBER
PHP979
033KZB
RSK*+21
KKG377
COLLECTION RATIOS
GM/GAL CF/CF
AVERAGE
1G7.59
25.33
99. 28
38.a**
112.50
23.77
76.12
160.76
23.7?
95.52
35.<*1
1C7.7G
2<». 3 2
-------
STATION* TEXACO
PROCESS: ENVIRONICS
LOCATION! 3ALTIMORE.+ FLeTCH.ERV DATE.? ..6/20/7J*_
LICENSE
NUMBER
5513EB
12<*ELL
623HTS
THE7K
WYM038
770KLB
305HOS
WSC130
STEAH2
MW1510
93353G
COLLECTION RATIOS
GM/GAL CF/CC
*99.99 *99.99
237.36 A67.67.
207.87 *68.15
155.82 618.55
9>»7.?. 206.6?..
06.6'-» *»52. 22
*99.99 •99.99
531.83 *05.99
339.68 886.23
108.32 372.39
112.92 87^.67
161.30 680.35
179.1W o<+6.63
*99.9:) *99.99
ro
vo
-------
STATION* TEXACO
PROCESSt ENtflRONICS
LOCATION: BALTIMORE + FLETCHER
DATE* 6/20/7<+
o
1
If)
o
LICENSE
NUMBER
31<+GX£
PH3110
662FZG
34IHCLQ
77i,58U
0,N,39
530 13L
571HDT
V96JQS
1^3*2R
37778W
UKW76**
ZXM732
963GOY
COLLECTION
GM/GAL
16C.84
1U6. 81
172.16
95. 35
137.76
115. V9
2^8.71
127.69
156.97
15*1.79
73.81
119. 9
-------
STATION: TEXACO
PROCESS! ENVIRONIGS
LICENSE
NUMBER
973JQP
PFN366
716KFH
7503S3
SNP596
W5KLX
*»62S7P
726FVX
735JLA
TAM267
AZV456
LOCATIONS BALTIMORE. •*• FLETCHER DATE!. 6/2_0/.7«f_
COLLECTION RATIOS "
GM/GAL C^/CF
163.C5
-------
STATION: TEXACO
PROCESS: ENVIRCNICS
LOCATION: BALTIMORE t FLETCHER
DATES 6/20/7<»
LICENSE
NUMBER
KOW408
1766?T
2Q263T
<»OOJSJ
WAC301
TGB765
710KLT
731ELS
3980LO
Q81070
VNVO^g
KGS913
COLLECTION
GM/GAL
.^.82
111. 8S
126.12
3U.33
2Q1.57
153.01
13<».82
175.00
i5*.n
1^0.05
167.53
125.00
RATIOS
CF/CF
5^8. 0^ - - —
593. <*?
5^9.19
*5?.98
760.25
675.71
U71.51
6ul.52
507. 9H
730.80
798.56
«6.6.?
AVERAGE
157.32
65C.11
CO
ro
-------
STATION: UNION /&
PROCESS: PROCESS PRODUCTS
LOCATION: WARING * ZTON
DATE: &/2<»/7<*
LICENSE
NUMBER
960KZD
L36087
609677
72085W
9.55KLP
Dt RE£N
TAC138
RUU<»88
8660ND
'233HMS
6SOGOC
l<*022tf
833FVQ
35CG08
f
CO
<*»
COLLECTION
GM/GAL
7U.81
1Q9.26
12C.69
10^.60
117.35
1J1.99
139.15
99.55
112.7?
111.12
177. 3i»
102.59
199.77
131.29
RATIOS
CF/CF
115.91
13S./f5
177. <*?
li»6. 76
165.72
172.0 2
16<,.<,5 "
152.87
178.05
123.5? :
13S.5T
112.96
275. it 9
158. 9<+
-------
STATIONS UNION 76 PROCESS: PROCESS PRODUCTS LOCATION: WARING * ZIOM
DATE! 6/24/7*+
LICENSE
NUMBER
OVC759
WCfcSLM
COLLECTION RATIOS
GM/GAL Cp/CF
137. i«6
15 0.11
158.63
107. 8<»
*99.99
186.57
1V7 . 6 7
2^9.96
273.93
226.31
177.13
o
CO
AVERAGE
133.73
176.19
-------
APPENDIX C-5
CALCULATION METHODS
The method of calculating performance for each column of Appendix C-4 is
as follows:
1. Returned Vapor = Vapor Volume After -
Vapor Volume Before
2. Standard Return Vapor =
[Ret. Vap.] [29.92 + (Vap.Ret.Press, x 0.07355)] x [540]
[29.92] x [470 + Vap. Temp.]
3. Ret. Vap. to Displ. Liq. Ratio =
(Ret. Vap.)
(Gal.Fill) x (0.1337)
4. Fill Rate =
[Gal. Fill]
[Fill Time]
5. Veh. Tank - Und. Tank Temp. =
Veh. Tank - Underground Tank Temperature
6. Vapor Mass =
(Std. Ret. Vapor) x (Cone.) x (55.648)
7. Vapor Mass to Disp. Liq. Ratio =
(Vapor Mass)
(Gal. Fill)
8. Veh. Tank - Disp. Liq. Temp =
Vehicle Tank - Dispensed Liquid Temperature
C-5-1
-------
The returned vapor for the Environics data was additionally corrected for
the fill time to total nozzle time according to the following:
Returned Vapor =
(Vap.Vol.After - Vap.Vol.Before) x/ Fl11 Tlme \
YTot. Nozzle Time /
The method for calculating collection ratios was as follows:
(Vap.Mass/Disp.Liq ) Actual ,QQ
GM/GAL =
(Vap.Mass/Disp.Liq) Baseline
(Ret. Vap. To Disp. Liq Ratio) Actual
CF/CF = x 100
(Ret. Vap. To Disp. Liq. Ratioj Baseline
C-5-2
-------
\
APPENDIX D
RVP ANALYSIS
-------
0
LOB ANGELES AREA -
SPRUCE S-1153
HARBOR AREA-TERMINAL 5-8SB3
JOS. H. McCABE JOS. H. MCCABE, JR.
APPROVED AND LICENSED BY
THC NEW YORK PRODUCE EXCHANGE
INSPECTORS OF PETROLEUM
LOS ANGELES AREA
P. Q. BDX 1146 - 115 AVALDN BLVD.
WILMINGTON. CALIF. 9O744
SERVING THE PETROLEUM INDUSTRY FOR OVER 6O YEARS
DEPENDABLE INSPECTION SERVICE AT ALL PORTS ON THE ATLANTIC, OULr AND PACIFIC COASTS
LABORATORIES
KENILWORTH. N.J.
PHILADELPHIA, PA.
HAMMOND. INO.
NEW ORLEANS. LA.
CORPUS CMRISTI. TEX.
PASADENA (HOUSTON), TEX.
WILMINGTON, CALIF.
TAMPICO. MEX.
SEATTLE. WASH.
PORTLAND, ORE.
CHICAGO. ILL.
BOSTON. MASS.
WEST HAVEN. CONN.
LABORATORY ANALYSIS REPORT
BAMPLE DESIQNATEO BY CLIENT AS
FROM
FOR
GASOLINE
June 18, 1974
Submitted by T R W Systems
Analysis
P. 0. NO. 206 JA 4E
ANY KINO UNLESS PERMISSION FOR THE PUBUBHINO OR AOVCRTI8INO OF AN APPROVED ABSTRACT HAB BEEN OBTAtNCO, IN WRITING FROM C. W. BAVBObT A CO., INC.
Samples marked:
Union Station - end of day
Inter mark - Standard Bulk Terminal
91
Gulf Station- Before drop
Gulf from Bulk Station
G J X
Mercury Brougham Gulf Sta. San Diego
Reid Vapor Pressure @ 1QO°F,
8.6
8.9
8.1
8.1
8.1
7.4
7.6
NOTE: Also received 2 - 1/2 pint samples - unable to read identification
(Ink washed out)
E.W.
INC.
D-l
FORM 14-CAL (BEV. 1/73)
-------
AND FATS.
LOB ANGELES AREA -
SPRUCE S-11S3
HARBOR AREA-TERM IN ALS-B 363
JOS. H. McCABE JOS. H. McCABE, JR.
APPROVED AND LICENSED BY
THE NEW YORK PRODUCE EXCHANGE
INSPECTORS OF PETROLEUM
LOS ANGELES AREA
P. Q. BOX 1146 - 115 AVALDN BLVD.
WILMINGTON. CALIF. 9O744
SERVING THE PETROLEUM INDUSTRY FOR OVER 6O YEARS
DEPENDABLE INSPECTION SERVICE AT ALL PORTS ON THE ATLANTIC, OULF AND PACIFIC COASTS
LABORATORIES
KENILWORTH, N.J.
PHILADELPHIA, PA.
HAMMOND, IND.
NEW ORLEANS, LA.
CORPUS CHRIST), TEX.
PASADENA (HOUSTON), TEX.
WILMINGTON, CALIF.
TAMPICO, MEX.
SEATTLE. WASH.
PORTLAND, ORE.
CHICAGO, ILL.
BOSTON, MASS.
WEST HAVEN, CONN.
SAMPLE DESIGNATED BY CLIENT AG
FROM
LABORATORY ANALYSIS REPORT
GASOLINE June 26, 1974
Submitted by T R W Systems
FOR
Analysis
P. 0. NO. 206 JA 4E
Chev. 6/18/74
Std. Bulk Term. 6/18/74 1192
Chev Vega 2300 License 909JS
Chev 3/4 Ton P.U. Lie. 45280L
Ford.1972 572 FFR
Calif. 603 GBY
KTR 796
312 HPO
TVS 029
932 KWN
918 KKL
574 KMK
ZND 264
Unmarked Bottle
Unable to read - submitted 6/14/74
Unable to read - submitted 6/14/74
Reid Vapor Pressure @ 100°F,
8.9
9.1
8.6
8.1
8.6
8.8
8.7
6.6
8.4
8.8
8.5
8.2
8.6
Insufficient sample
8.6
8.8
D-2
FORM 14-CAL (REV. 1/73)
E.W.
INC.
MCMBC0S Or A. S. T. M.~-A. P. I. .9- A. C.
IN WdlTINO.
-------
AND FATS.
LOS ANGELES AREA -
SPRUCE 5-1153
HARBOR AREA -TERMINAL 5-B3B3
JOS. H. MCCA8E JOS. H. "cCABE, JR.
APPROVED AND LICENSED BY
THE NEW YORK PRODUCE EXCHANGE
INSPECTORS OF PETROLEUM
LD5 ANGELES AREA
P. O. BOX 1146 - 115 AVALDN BLVD.
WILMINGTON. CALIF. 9O7-.''
SERVING THE PETROLEUM INDUSTRY TOR OVER 6C YEARS
DEPENDABLE INSPECTION SERVICE AT ALL PORTS ON THE ATLANTIC, OULF AND PACIFIC COAST6
KENILWORTH, N.J.
PHILADELPHIA, PA.
HAMMOND. IND.
NEW ORLEANS l.«
CORPUS CHRISTI. TEX.
PASADENA (HOUSTON). TEX.
WILMINGTON. CALIF.
TAMPICO. ME*.
SEATTLE. WASH.
PORTLAND. ORE.
CHICAGO, ILL.
BOSTON, MASS.
WEST HAVEN. CONN.
SAMPLE DESIGNATED BY CLIENT AS
FOR
LABORATORY ANALYSIS REPORT
GASOLINE
June 28, 197^
Submitted by T R W
6/27/74.
Analysis.
Systems
P.O.NO. 206 JA -4E
Reid Vapor Pressure @ 100 °F.
1974 FORD 907KES - 6/19/74.1000
1973 DODGE 438 JUA-6/19/74.0855
1972 FORD 603 GBY -6/19/74.0805
1972 FORD 662 FZG -6/20/74.1110
* NO. 12
NO. 101
NO. 200
No.256
8.6
8.7
8.0
8.2
0.2
8.3
8.6
7.9
* Sample No. 12 API @ 60 °F. 10.0
apparently water, slight gasoline odor.
E.W.
D-3
FOBM H-CAL (REV. t / 73 )
IN WBITINO.
-------
APPENDIX E
SAMPLE DATA SHEETS
-------
DAILY STATION DATA SHEE1
Station Name
Vapor Recovery System
Dry Bulb Temp.
Wet Bulb Temp.
Amp. Pressure
Wind Velocity
Overcast
Tank 1
Tank 2
Tank 3
Tank 4
Pump Gallonage 1
2
Date
Installed Date
AM Noon PM
Hrs Hrs Hrs
op op op
op op • op
11 Hg " Hg " Hg
ft/sec ft/sec ft/sec
% % %
Start of Day End of Day
gal °F gal °F
gal °F gal °F
gal °F gal °F
gal °F gal °F
gal gal
gal gal
Station Personnel
Station Personnel
Test Personnel
Visitors (long term)
Visitors (part time)
Remarks:
E-l
-------
VEHICLE COLLECTION DATA SHEET
Time:
Lie. # State
Make Model
Year ^
Station:..
Date:
Pump No.
Local/Freeway Driving
Vehicle
Tank Temp. __°F
Leak Check: Pressure
RVP Sample: Yes
Gallons
Distance Travelled
Fill Pressure: Max
_in. H20 Flow
in. H20 Avg
cc/min
Total Nozzle Time:
Type of Nozzle Fit
Spitback: Yes
Vapor Return
Vapor Temp
No Value
Fill Time
min.
mm.
sec.
No
Volume Meter: After _
Before
Total
Concentration: Average
sec.
Amount
Liquid Temp
L3
ft*
ft*
ft*
Expl. Reading
in. H20
E-2
-------
TANK DROP DATA SHEET
Station
Time
Date
Underground Tank Temperature (°F)
Tank 1 initial final
X
Tank 2 initial
Tank 3
initial
final
final
Tank Truck Temperature (°F)
Tank 1 initial
Tank 2 initial
Tank 3 initial
Size of Underground Tanks (gal) Tank 1
Average monthly throughput total
Ambient Temp. °F
Tank 2
gal
Ambient Pressure
Tank 3
in. Hg
If secondary equipment starts during drop, record time of:
Start up Shut off
Underground Tank Volumes (gal)
Initial Tank 1
Final . Tank 1
Drop Time (min.) Initial Tank 1
Final Tank 1
Tank 2
Tank 2
Tank 2
Tank 2
Tank 3
Tank 3
Tank 3
Tank 3
Monitor During Drop: Underground Tank Pressure
Truck Tank Pressure
Explosmeter Readings at Joints
Temp
Temp
At inlet to control device or vent of vapor balance
System monitor: Hydrocarbon concentration (%}
Vapor Pressure (in H20)
Vapor Temperature (°F)
Vapor Volume (ft3)
max.
max.
max.
final
final
final
avg.
avg.
avg.
initial
final
E-3
-------
TAJIK DROP DATA SHEET (COflTD)
At Outlet Monitor: Hydrocarbon Concentration (%) max. avg,
Vapor Pressure (in H^O) max. avg,
Vapor Temperature (°F) max. avg,
o
Vapor Volume (ft ) initial final
E-4
------- |