p.1 

OAR Box 1413 

Prepped by Ollie Stewart 

Document Number: 

48) 11-1-48 

Docket Number: 

A-94-52 

Printed 7/9/2008 3:11:22 PM Sheet 48 of 114 
A • 

P.2 

A^fy-5-?- • 

3T-2' V8, 

,Incinerator Efficiency Sampling 

•Fibercast Company 

Sand Springs, OK 

April 10, 1992 

; Armstrong Environmental, Inc. 

j Project W-1181-92 

Report Prepared For: 

Mr. Larry Moore 

Fibercast Company 

25 South Main 

Sand Springs, OK 74063 

Report Prepared April 15, 1992 by: 

i Armstrong Environmental, Inc. 

4747 Irving Blvd. #204 

Dallas", Texas 75247 

(214) 631-0021 
P.3 

TABLE OF CONTENTS 

I. INTRODUCTION 

Page 

1 

II. SUMMARY 2 - 4 

III. PROCEDURES 

IV. APPENDICES 

A - CALCULATION SUMMARIES 

B - STRIP CHART SUMMARIES 

C - FIELD DATA SHEETS 

D - STANDARD GAS CERTIFICATIONS 

E - INCINERATOR PARAMETERS 

F - EQUIPMENT CALIBRATIONS 

6-11 

12 - 20 

21 - 28 

29 - 32 

33 - 34 

35 - 40 

2_ 
P.4 

1^ INTRODUCTION 

A series of tests were performed on the incinerator inlet and 

exhaust, stacks at the Fibercast Company facility located in Sand 

Springs r_ OK on April 10, 1992. 

The purpose of this test series was to determine the incinerator 

destruction efficiency. The incinerator is manufactured by Anguil 

Energy Systems and is a Model 150, serial # CNM 067. It is 

equipped with a nickel catalyst bed and variable speed fan. 

Incinerator parameters during testing are located in the summary 

tables. ; •_ ' 

Testing was conducted following procedures detailed in 40:CFR. 

Emissions testing was performed by Larry Whicher, Tom Armstrong, 

and Dan Barrera of Armstrong Environmental, Inc. using two 

Beckman Model 400A hydrocarbon analyzers and a NAPP tfodel 31 

Method 5 samplingitrain. 

Testing was performed over a four hour period. 

Submitted by: 

Armstrong Environmental, Inc. 

Larr^y Whicher 

Project Manager 

LW/ms 

. i3. 
P.5 

II. SUMMARY 

A series of tests were performed on the inlet and exhaust ducts 

of the^incinerator at the Fibercast Company facility located in 

Sand Springs, OK on April 10, 1992. 

Sampling was performed following USEPA test methods as detailed 

in Title 40: Code of Federal Regulations (40:CFR). 

Three runs were performed simultaneously on the inlet and 

exhaust. All three run were one hour in duration with the 

exception of run 3. During run three concentrations were above 

scale on the inlet for a period of six minutes. Full scale 

concentrations were used in averaging the chart during this time 

period. (Destruction efficiency during this period was still over 

95%) . 

Results of the test series indicate the following : 

Run# 

Exhaust Emissions, lbs/hr 

Inlet Emissions, lbs/hr 

Destruction Efficiency, % 

1 

4.47 

150.70 

97.03 

2 

4.49 

136.62 

96.71 

3 

5.65 

216.75 

97.39 

Avg. 

4.87 

168.23 

97.04 

I 
P.6 

SUMMARY OF EMISSIONS TEST DATA 

TABLE: 1 

PLANT: .Fibercast Company, Sand Springs, OK 

LOCATION,: Incinerator Inlet 

OPERATOR-: L. Whicher, T. Armstrong, D. Barrera 

TEST DATE: April 10, 1992 

REPETITION: i 1 2 

INCINERATOR PARAMETERS 

Burner Temperature, F 

Cat Bed, Out 

Fan Speed, % 

STACK GAS 

Temperature, F 

Velocity, fps 

Volume Flow, acfm 

scfm 

scfh 

Moisture, % 

C02, % 

02, % 

SAMPLE 

Start Time, hrs:min 

Finish Time, hrs:min 

VOC as C3H8 

Concentration, ppm 

Emissions, lb/hr 

676 

756 

39 

78.7 

10.70 

2745.4 

2603.8 

156226 

1.4 

0.0 

21.0 

8:36am 

9:36am 

8486.62 

150.70 

675 

767 

38 

78.4 

10.83 

2779.6 

2637.9 

158272 

1.4 

0.0 

21.0 

9:50am 

10:53am 

7593.92 

136.62 

675 

811 • 

35 -

87.0 

10.94 

2806.5 • 

2624.4 

157463 

1.3 

0.0 

21.0 

11:10am 

12:16pm 

12110.39 

216.75 

J 
P.7 

SUMMARY OF EMISSIONS .TEST DATA 

TABLE: 2 

PLANT: Fibercast Company, Sand Springs, OK 

LOCATION: Incinerator Inlet <3M.TI^>T TvXOPERATOR-: L. Whicher, T. Armstrong, D. Barrera 

TEST DATE: April 10, 1992 

REPETITION: 1 2 

INCINERATOR PARAMETERS 

Burner Temperature, F 

Cat Bed, Out 

Fan Speed, % 

STACK GAS 

Temperature, F 

Velocity, fps 

Volume Flow, acfm 

scfm 

scfh 

Moisture, % 

C02, % '. 

02, % 

SAMPLE 

Start Time, hrs:min 

Finish Time, hrs:min 

VOC as C3H8 

Concentration, ppm 

Emissions, lb/hr 

676 

756 

39 

376 

11.65 

5360.5 . 

3258.1 

195488 

2.0 

0.0 

20.0 

8:36am 

9:36am 

201.10 

4.47 

675 

767 

38 

375 

13.38 

6157.3 

3716.8 

223005 

2.8 

0.0 

20.0 

9:50am 

10:53am 

177.21 

4.49 

675 

811 -

35 -

370 

1.1.78 

5422.2 ' 

3299.5 

197968 

2.6 

0.0 

20.0 

11:10am 

12:16pm 

250.99 

5.65 
P.8 

III. PROCEDURES 

The procedure for emissions sampling followed USEPA test methods 

as detailed in Title 40: Code of Federal Regulations. The 

following methods were used: 

Method Title > 

1 Sample and Velocity Traverses for Stationary Sources 

2 Determination of Stack Gas Velocity and Volumetric 

Flow 

3 Gas Analysis for C02, 02, Excess Air and Dry'Molecular 

Weight \ 

4 Determination of Moisture Content in Stack Gases 

25A Determination of Total Gaseous Organic Concentration 

Using a Flame Ionization Analyzer 

C02 and 02 were determined using Fyrite analyzers. 

Velocity traveres were performed at 16 points, 12 points per 

traverse on both the inlet and the exhaust. The traverses were 

done during the run with a standard pitot. 

Moisture on the exhaust was determined by pulling a known amount 

of stack gas through the back half of a Method 5 sampling train. 

The first and second impinger contained 100 mis of H20, the third 

was empty, and the fourth impinger contained 200 grams of silica 

gel. Moisture on the inlet was determined using wet bulb/dry bulb 

calulations. 

The concentrations on the incinerator exhaust and inlet were 

taken using two Beckman Model 400A Continuous FID analyzers. The 

analyzer on the inlet was spanned with 9992 ppm, 988.4, and 202.7 

ppm propane in nitrogen standards.The exhaust analyzer was 

spanned with 988.4 ppm, 202.7 ppm, and 27.2 ppm propane in 

nitrogen gas standards. Tedlar gas bags were used to span the 

analyzers from the end of the teflon sample line. 
P.9 

APPENDIX A 

•«• •7,;;-;,77. :,.,.,__ v 

tf 
P.10 

Fibercast 

Incinerator 

Repetition #1 

4/10/92 

MOLECULAR WEIGHT-OF STACK GAS, DRY BASIS, MD 

(.44 * %C02) + (.32 * % 02) + (.28 * (N2 + CO)) = 28.84 

MOLECULAR WEIGHT OF STACK GAS, WET BASIS, MS 

MD * (1 - BWS) + (18 * BWS) = 28.68824 

STACK GAS PRESSURE, IN HG, PS 

PBAR + (STATIC/13.6) = 29.3625 ; 

STACK GAS VELOCITY, FPS 

85.49 * CP * (SQR P(TS / (PS * MS))) = 10.70058 

VOLUME FLOW RATE, ACFM 

60 * AS * VS = 2745.406 

VOLUME FLOW RATE, SCFH 

3600 * (1 - BWS) * VS * AS * ((528 * PBAR) / (TS * 29.92)) = 156225.9 

%C02 = 0 

%02 = 21 

%CO = 0 

%N2 = 79 

STACK TEMPERATURE, F = 78.7 

SQUARE ROOT OF DELTA P = .1581 

STATIC PRESSURE, IN H20 = -.51 

BAROMETRIC PRESSURE, IN HG = 29.4 

PERCENT WATER VAPOR (BWS * 100) = 1.4 

AREA OF STACK, SQUARE FT. = 4.2761 

PITOT CO-EFFICIENT, CP = .99 

1 
Fibercast 

Incinerator Inlet 

Repetition #2 

4/10/92 

MOLECULAR WEIGHT" OF STACK GAS, DRY BASIS, MD 

(.44 * %C02) + (.32 * % 02) + (.28 * (N2 + CO)) = 

MOLECULAR WEIGHT OF STACK GAS, WET BASIS, MS 

MD * (1 - BWS) + (18 * BWS) = 28.68824 

STACK GAS PRESSURE, IN HG, PS 

PBAR + (STATIC/13.6) = 29.36471 

STACK GAS VELOCITY, FPS 

85.49 * CP * (SQR P(TS / (PS * MS))) = 10.83388 

VOLUME FLOW RATE, ACFM 

60 * AS * VS = 2779.604 

VOLUME FLOW RATE, SCFH 

3600 * (1 - BWS) * VS * AS * ((528 * PBAR) / (TS * 

%C02 = 0 

%02 = 21 

%CO = 0 

%N2 = 79 

STACK TEMPERATURE, F = 78.4 

SQUARE ROOT OF DELTA P = .16012 

STATIC PRESSURE, IN H20 = -.48 

BAROMETRIC PRESSURE, IN HG = 29.4 

PERCENT WATER VAPOR (BWS * 100) = 1.4 

AREA OF STACK, SQUARE FT. = 4.2761 

PITOT CO-EFFICIENT, CP = .99 

V. -1 

7 

28.84 

29.92)) = 

.. -•;••-.., : :•••:: • 

% 

X 

-

• 

158272 

_•' 

'.... •.;-••—-V.-•-; • v.* 

•* 

.0 

P.11 

•Ji 

y 

t % 

r-' 

i | 

t*' 
P.12 

Fibercast 

Incinerator Inlet 

Repetition #3 

4/10/92 

MOLECULAR WEIGHT OF STACK GAS, DRY BASIS, MD 

(.44 * %C02) + (.32 * % 02) + (.28 * (N2 + CO)) = 28.84 

MOLECULAR WEIGHT OF STACK GAS, WET BASIS, MS 

MD * (1 - BWS) + (18 * BWS) = 28.69908 

STACK GAS PRESSURE, IN HG, PS 

PBAR + (STATIC/13.6) = 29.36691 

STACK GAS VELOCITY, FPS 

85.49 * CP * (SQR P(TS / (PS * MS))) = 10.93872 

VOLUME FLOW RATE, ACFM 

60 * AS * VS = 2806.505 

VOLUME FLOW RATE, SCFH 

3600 * (1 - BWS) * VS * AS * ((528 * PBAR) / (TS * 29.92)) = 157462.6 

%C02 = 0 

%02 = 21 

%CO = 0 

%N2 = 79 

STACK TEMPERATURE, F = 87 

SQUARE ROOT OF DELTA P = .16043 

STATIC PRESSURE, IN H20 = -.45 

BAROMETRIC PRESSURE, IN HG = 29.4 

PERCENT WATER VAPOR (BWS * 100) = 1.3 

AREA OF STACK, SQUARE FT. = 4.2761 

PITOT CO-EFFICIENT, CP = .99 

If 
P.13 

Fibercast 

Incinerator Exhaust i 

Repetition #1 ' 

4/10/92 •__. | 

MOLECULAR WEIGHT~ OF STACK GAS, DRY BASIS, MD 

(.44 * %C02) + (.32 *! % 02) + (.28 * (N2 + CO) ) = 28.8 

i 

MOLECULAR WEIGHT OF STACK GAS, WET BASIS, MS 

MD * (1 - BWS) + (18 * BWS) = 28.58292 

i 

STACK GAS PRESSURE, IN HG, PS 

PBAR + (STATIC/13.6) = 29.39853 

STACK GAS VELOCITY, FPS 

85.49 * CP * (SQR P(TS / (PS * MS))) = 11.64832 

i 

VOLUME FLOW RATE, ACFM 

60 * AS * VS = 5360.485 

VOLUME FLOW RATE, SCFH 

3600 * (1 - BWS) * VS;* AS * ((528 * PBAR) / (TS * 29.92)) = 195488.4 

%C02 = 0 

%02 = 20 

%CO = 0 j 

%N2 = 80 , 

STACK TEMPERATURE, F = 376.4 

SQUARE ROOT OF DELTA P = .13795 

STATIC PRESSURE, IN H20 = -.02 

BAROMETRIC PRESSURE, IN HG = 29.4 

PERCENT WATER VAPOR (BWS * 100) = 2.01 

AREA OF STACK, SQUAREiFT. = .7.6699 

PITOT CO-EFFICIENT, CP = .99 

/2-
P.M 

Fibercast 

Incinerator Exhaust 

Repetition #2 

4/10/92 

MOLECULAR WEIGHT OF STACK GAS, DRY BASIS, MD 

(.44 * %C02) + (.32 * % 02) + (.28 * (N2 + CO)) = 28.8 

MOLECULAR WEIGHT OF STACK GAS, WET BASIS, MS 

MD * (1 - BWS) + (18 * BWS) = 28.49652 

STACK GAS PRESSURE, IN HG, PS 

PBAR + (STATIC/13.6) = 29.39816 

STACK GAS VELOCITY, FPS 

85.49 * CP * (SQR P(TS / (PS * MS))) = 13.37986 

VOLUME FLOW RATE, ACFM 

60 * AS * VS = 6157.331 

VOLUME FLOW RATE, SCFH 

3600 * (1 - BWS) * VS * AS * ((528 * PBAR) / (TS * 29.92)) = 223005.4 

%C02 = 0 

%02 = 20 

%CO = 0 

%N2 = 80 

STACK TEMPERATURE, F = 375.3 

SQUARE ROOT OF DELTA P = .15832 

STATIC PRESSURE, IN H20 = -.025 

BAROMETRIC PRESSURE, IN HG = 29.4 

PERCENT WATER VAPOR (BWS * 100) = 2.81 

AREA OF STACK, SQUARE FT. = 7.6699 

PITOT CO-EFFICIENT, CP = .99 

10 

/3 
P.15 

Fibercast 

Incinerator Exhaust 

Repetition #3 

4/10/92 

MOLECULAR WEIGHT" OF STACK GAS, DRY BASIS, MD 

{.44 * %C02) + (.32 * % 02) + (.28 * (N2 + CO)) = 28.8 

MOLECULAR WEIGHT OF STACK GAS, WET BASIS, MS 

MD * (1 - BWS) + (18 * BWS) = 28.51812 

STACK GAS PRESSURE, IN HG, PS 

PBAR + (STATIC/13.6) = 29.39779 '-

STACK GAS VELOCITY, FPS 

85.49 * CP * (SQR P(TS / (PS * MS))) = 11.78249 

VOLUME FLOW RATE, ACFM 

60 * AS * VS = 5422,229 

VOLUME FLOW RATE, SCFH 

3600 * (1 - BWS) * VS * AS * ({528 * PBAR) / (TS * 29.92)) = 197968.2 

%C02 = 0 

%02 = 20 

%CO = 0 

%N2 = 80 

STACK TEMPERATURE, F = 370.3 

SQUARE ROOT OF DELTA P = .13989 

STATIC PRESSURE, IN H20 = -.03 V; 

BAROMETRIC PRESSURE, IN HG = 29.4 

PERCENT WATER VAPOR (BWS * 100) = 2.61 

AREA OF STACK, SQUARE FT. = 7.6699 

PITOT CO-EFFICIENT, CP = .99 

11 

IH 
P.16 

APPENDIX B 

. ! 

/5 
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34 
Scott Specialty Gases a division of 

Scott Environmental Technology, Inc. 

120 0 COMBERMERE STREET. TROY, MICHIGAN 48084 (313) 680-205 0 

luitoier t 

ARHSTRONB ENVIROMENTAL 

TOH ARKSTRONB 

4747 IRVING BLVD 

SUITE 204 

DALLAS, TI. 75247 • I " 

tilt CERTIFICATE OF ANALYSIS - EPA PROTOCOL GASES tttt 

PERFORMED ACC0RDIN6 TO SECTION 3.0.4 

Certified Per Traceability Procedure I 61 

Protocol I 1 

File I P0405B 

Certified Accuracy 1 X NBS Traceable 

Shipped Froa l Scott Troy 

Our Project I I 520722 

Your P.O. I i 1002 

Expiration Date i 9-14-92 

Cylinder Hueber ALH-004374 

Cylinder Preiiure 1900 psig 

6) 

REFERENC E 8T D ANALYZE R 

SRH I 

(CRN I) 

tttttttttttttttttttttttttttttttttttttttttttt 

CERTIFIED t 

COMPONENT CONC. t 

?R0PANE 9BB.4 PPN. t 2446 

: • . » GHISt 

BALANCE 6AS l NITROGEN I 

tmiftfmttttittmmttmttttuttttttttt 

CYLINDER 

NUNBER CONC. H^ODE&SERlAg 

BECl(fi?N/400/lo02059 

ZERO 

6AS 

dV) 

0.00 

0.00 

0.00 

ANALYSIS 

. > 

. TEST 

W S :. 

CiVJ 

97.90 

97.90 

97.90 

DATE i 3^45 9i 

,' REFERENCE REFERENCE 

RESULTS ! 

PPN ! 

6AS 

CONC. 

GAS 

(•V) 

990.3 : 

990.3 : 

990.3 ! 

973.3 PPH 96.40 

96.40 

96.40 

RESULTS 

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975.1 

975.1 

CALCULATED 

RESULTS 

9BB.4 

9BB 

9BB.4 

.4. J ,i . 

i'!«-' U-,i 

AVERA6E t 9BB.4 PPN 

I 6KIS - GASHANUFACTURER'S INTERNAL BIANDARD ,.., „ Analyst i S^_Z^>rk j 

T M on(y lUbUlty of thU Company for f _u_ which faili lo comply with 

ANALYTICAL PRINCIPLE 

FLANE IONIZATION DETECTOR • 

o 

CALIBRATION CURVE 1 it DEGREE 

SRH I CONC. SPLIT DVH FITTED PERCENT 

(CRN I) PPM PT (X) |iV) VALUE ERROR 

2646 

1012 

973.2 

799.B •• 

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 ; > 975 0.2 0 

roVed By t _ 

by tho Company, 
P.39 

---. CERTIFICATION ANALYSIS 

*

T_ "EPA PROTOCOL #1" OR0ER# 1920907 

CYLINDER NUMBERS: CC-100764 ' 

CERTIFIED CONCENTRATION: 202.7 PPM PROPANE 

BALANCE GAS: .- NITROGEN ^ 

CYLINDER PRESSURE: 2015 PSI 

DATE OF CERTIFICATION: FEBRUARY 3, 19S2 

CERTIFICATION EXPIRATION: AUGUST 3. 1993 

SRM INFORMATION: 

SRM NUMBER CYL. NUMBER CONCENTRATION 

26.44 CAL-3109 244.2 PPM C3H8/N2 

THIS.ASSAY/CERTIFICATION WAS PERFORMED ACCORDING TO 

SECTION- 3.0.4*. 

BY MICHAEL SICKMILLER. QUALITY CONTROL SUPERVISOR 

INSTRUMENTS USED: 

TOTAL HYDROCARBON: HORIBA 0PE-4O5XB0R0 ANALYTICAL 

TOTAL HYDROCARBON 

SERIAL # 850U90110 

CALIBRATION 01-20-92 

EPA408 - <32^^yS^ 

MICHAEL SICKMILLER " ^ 

QUALITY CONTROL SUPERVISOR 

31 • •J-.--.:jr-
Scott Specialty Gases Scott Environmental Technology, 

a division of Shipped Froi I Scott HlcbifiB 

Inc. 

Oar Project I « 520722 

itoitr i " 

DRH81R0HB EH7IR0HAEHIAL 

- TOI ARHSIR0H6 

' 4747 IRVIHB ILVI 

IALUS, TI. 75217 

1200 COMBERMERE STREET. TROY. MICHIGAN 48084 (313)580-2050 

ttt t CERTIFICATE OF AHALTSIS • EPA PROTOCOL EASES ttt t 

PERFORMED ACCORDING TO SECTION 3.0.4 

Certified Pir Inceibilil/ Proc....* I Gi 

Protocol I 1 

f l U I P04054 

Certified Accoricjr 1 I KBS Trimbl e 

• r 

Toor P.O. I I 1002 

Eiplrttioa tit e I 9-14-92 

Cylinder Haiber i ALM10174 

Cylinder Preiiart . 1700 pii| 

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COHPOKEHT 

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I NSIRUHENTATIO H 

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FIBERCAST COMPANY 

CATALYTIC INCINERATOR DAILY LOG 

•" I 

» ft^ (Compliance. T««T "\ • Week of B Monday i Tuesday (Wednesday Thursday i Friday 

Casting flach 

I Mold Temperature jl 

ine HI 8 — 1 

§ Exhaust To jj| 

190° F 

HOTES: a) Epoxy exhaust to Atmosphere, Epoxy mold temperature range is.235* -.250* F. 

b) Vinyl Ester exhaust to Incinerator, Vinyl Ester temperature range 

yyy\ : - r is 185 * - 200 * F . .-•=••••- y-yy:.• .---e "•'•'••• •/•--.:-•-•••-•.-'-• yy-vy : -y-y : ••}••••"-••'•• -<•••-

c). The Resin Plant and Premix Mixers go to the Incinerator all the time. . 

d) .Atm.= Atmosphere: Inc.= Incinerator 

•••...'• • • ••' RAK:4/?2 

- ' n* V2_ 
P.44 

APPENDIX F 

*/3 
P.45 

SUMMARY-QE-ERE,METER_.BQX-CALIBRA1IQM_. 

METER BOX NUMBER: 2 

CALIBRATION DATE:4/3/92 

CALIBRATED BY:Larry Whicher 

BAROMETRIC.PRESSURE: 29. 8 

*********************************************** 

* * 

* DELTA H = ORFICE PRESSURE * 

* VW = VOLUME OF WET GAS METER * 

* TW = AVERAGED TEMPERATURE OF WET METER * 

* . VD = VOLUME OF DRY GAS METER * 

* TD = AVERAGED TEMPERATURE OF DRY GAS METER * 

* TIME = DURATION OF EACH POINT RUN * 

* * 

******************************************************* 

POINT 1 

DELTA H = .5 VW= 5 TW = 58.5 

VD = 5.316 TD = 65 TIME = 11.7 TEST METER Y = 

METER BOX Y = .9416627 

METER BOX H = 1.491361 

.99 

POINT 2 

DELTA H = 1 VW= 5 TW = 58.8 

VD = 5.299 TD = 67 TIME = 8.93 

METER BOX Y = .9475238 

METER BOX H = 1.732987 

TEST METER Y = .991 

POINT 3 

DELTA H = 1.5 VW= 10 TW = 61 

VD = 10.741 TD = '78.8 TIME = 14.41 

METER BOX Y = .9515955 

METER BOX H = 1.669207 

TEST METER Y = .992 

POINT 4 

DELTA H = 2 VW= 10 TW = 62 

VD = 10.744 TD = 81 TIME = 12.83 TEST METER Y = 

METER BOX Y =.9522139 

METER BOX H = 1.763884 

.992 

POINT 5. 

DELTA H = 3 VW= 10 TW = 62.3 

VD = 10.648 TD = 82.3 TIME = 10.58 

METER BOX Y = .9621328 

METER BOX H = 1.79695 

TEST METER Y = .994 

POINT 6 

DELTA H = 4 VW= 10 TW = 62.8 

VD = 10.597 TD = 83.5 TIME = 9.03 TEST METER Y 

METER BOX Y = .9665823 

METER BOX H = 1.744818 

= .995 

AVERAGE Y = .9536185 

AVERAGE H = 1.699868 35 

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SUMMARY OF POST' METER BOX CALIBRATION 

METER BOX NUMBER : 2 

CALIBRATIOlfcDATE: 04/11/9 2 

CALIBRATEp-lSY: Dan Barrera 

BAROMETRIC PRESSURE (inch Hg): 29.6 

************************************************************** 

* * 

* DELTA H = ORFICE PRESSURE * 

* VW = VOLUME OF WET GAS METER * : i * 

* TW = AVERAGED TEEMPERATURE OF WET METER " * 

* VD = VOLUME OF DRY GAS METER * 

* TD = AVERAGED TEMPERATURE OF DRY GAS METER * 

* TIME = DURATION OF EACH POINT RUN * 

* - * 

************************************************************** 

POINT 1 

DELTA H = 1 VW = 10 TW = 79.5 

VD = 10.383 TD = 82.75 TIME = 17.46 TEST METER Y = .991 

METER BOX Y = .9578151 

METER BOX H = 1.75081 

POINT 2 

DELTA H = 1 VW = 10 TW = 79.75 

VD = 10.507 TD = 90 TIME = 17.15 TEST METER Y = .991 

METER BOX Y = .9587104 

METER BOX H = 1.66847 

•POINT- 3 • 

DELTA H = 1 VW = 10 TW = 80.2 5 

VD = 10.527 TD = 95 TIME = 17.2 3 TEST METER Y = .991 

METER BOX Y = .9646943 

METER BOX H = 1.671994 

AVERAGE Y = .9604066 

AVERAGE H = 1.697091 

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