liAR 1)2008 

Georgia Department of Natural Resources 

Environmental Protection Division • Air Protection'"Bfa11ch 

4244 International Parkway. Suite 120. Atlanta. Georgia 30354 

404/363-7000. Fax: 404/363-7100 

Noel Holcomb, Commissioner 

Carol A. Couch, Ph.D., Director 

tMEtJl°RANDUM: 

'TO: 

THROUGH: 

FROM: 

Karen Hays ('J...tl) ,() 

Ross Winne, DeAnna Oser P U . fJ!:::! 

Daniel McCain fiY'. . SUBJECT: SOURCE TEST REPORT REVIEW 

The following test has been reviewed and was conducted in an acceptable fashion for the purpose intended. 

COMPANY NAME 

COMPANY LOCATION 

SOURCE TESTED 

POLLUTANT DETERMINED 

REPORT REVIEWED BY 

TEST WITNESSED BY 

DATE(S} OF TEST 

DATE RECEIVED BY APB 

MAXIMUM EXPECTED 

OPERATING CAPACITY 

OPERATING CAPACITY 

ALLOWABLE EMISSION RATE 

APPLICABLE REGULATION 

CONTROL EQUIPMENT 

AND MONITORING DATA 

TEST RUN# 

GAS TEMPERATURE Inlet 

(oF) Outlet 

GAS MOISTURE Inlet 

(%) Outlet 

GAS FLOW RATE Inlet 

(ACFM) Outlet 

GAS FLOW RATE Infet 

(DSCFM) Outlet 

POLLUTANT Inlet 

CONCENTRATION 

(PPM @ 15% 02) Outlet 

EMISSION RATE Inlet 

(NfA) Outlet 

DESTRUCTION 

EFFICIENCY (%) 

OTHER INFORMATION 

cc: Ross Winne 

Reference Number: 200800189 

Southern Natural Gas-Hall Gate Compressor Station 

Milledgeville, GA 

Compressor Engine No. 3 

Carbon Monoxide 

Daniel McCain 

Daniel McCain 

December 20, 2007 

February 8, 2008 

4730 Horsepower 

4441.33 Horsepower 

93% DRE 

Permit No. 4922-009-0035-V..Q2-O; Condition 3.2.1 

40 CFR Part 63 Subpart ZZZZ 

Oxidation Catalyst (C003C) 

Catalyst Bed Inlet Temperature = 777.67 deg F, Pressure Drop Across the Bed = 

2.73 in. H20, Engine Speed = 1000.67 

1 2 3 AVERAGE 

239.82 238.31 240.45 239.52 

7.34 7.52 7.17 7.34 

96.933, 

The RICE MACT requires that the catalyst bed percent reduction be tested by 

measuring the carbon monoxide concentration before and after the bed. 

Consequently, the air flow was not measured. The minumum reduction is 93 

percent. 

AIRS Number: 00900035 

Printed: 3/11/2008 
SOURCE EMISSIONS TEST AUDIT 

FOR: Southern Natural Gas - Hall Gate 

Milledgeville, GA 

Compressor Engine (C003) 

December 

Submitted: 

20, 

1117/08 

2007 ~ 

By: Daniel McCain 

Source and Information: 

The facility assists in the transport of natural gas through a pipeline by receiving low pressure 

inlet natural gas and compressing the natural' gas to increase the pressure in the pipeline to 

maintain the downstream flow. The facility uses three compressor engines to compress the gas. 

These engines are COOl, C002, and C003. 

Test Requirements and Procedures: 

The facility is subject to the requirements of Penn it No. 4922-009-0035-V -02-0. According to 

the pennit, Engine C003 is subject to Condition 3.2.1, which requires a reduction of CO 

emissions by 93% or more under Subpart ZZZZ and PSD avoidance. To assure compliance with 

this condition, the facility elected to conduct a test for CO at the inlet and outlet of the catalyst 

for the engine. The test method used was ASTM Method 06522-00. 

Audit Results: 

I arrived on site at about 9:20 a.m. and was met by Mr. Jim Wilson and Mr. Loren Hansen of 

Southern Natural Gas. Mr. Hansen was to conduct the testing. After arriving on site the facility was 

attempting to start the engine up. After the engine had been started and the proper pressure was 

attained Mr. Hansen prepared to start Run 1. During the first run, Mr. Hansen planned on recording 

NOx, CO, NO, N02, and 02 in order to use that run as an interference check for each analyzer being 

used. Each subsequent run would consist of recordings that only included CO. As the first run was 

underway, Mr. Hansen noticed that the NO was high and the N02 was low at the inlet of the catalyst, 

while the N02 was high and the NO was low at the outlet. Mr. Hansen stopped Run I and attempted . 

to detennine if there was a problem with any of the set up or equipment that may explain the NOx 

gas values. After period of time of checking the equipment and set up, Mr. Hansen determined that 

the values must be accurate since the set up was correct and the equipment was functioning properly. 

As he prepared to start Run 1, the engine had to be shut down and another engine had to be brought 

online to maintain the proper pressure for the pipeline. I departed the facility at about 3 :00 p.m. 

When I departed, Mr. Wilson and Mr. Hansen were still waiting to get the engines started up and 

running under the proper conditions again. 
Source Emissions Test Audit- Methods 3A, 6C, 7E, 10 & 20 

ISMP·33 

Rev. 7/07 

Company: Sbl.tf~ ~+ly!( C~ Company Contact:· _~.AC.J,.!!:MJo...-"w~1.:..:16~Yl=--__ ...:....-__ 

Address: tfIIill-t~1lL ,J ,~ Test Team: 5'0\... ~~ t\r .... l~( Ge.t 

Source Tested: ~ C60> Team Leader: Lo('tM Ii ~ 

Date: (/-1).0/. 1- Test Auditor(s): ~vt. McCa..~ 

1.' Applicability 

Which Method{s) does this audit cover? 3A 0 6C D7E D 10 D 20 0 - 4bnt, bbS'~~~tI 

Is this a low emitting source (<= 20 ppm)? Yes I No (Method 7E only) 

2. Measurement System Performance Specifications 

Calibration Error: 

System Bias: 

Drift: . IIiterference 

N02 to NO Converter EfI.: . 

<± 2.0% (or <= 0.5 ppmv) ofthe calibration span 

<± 5.0% (or <= 0.5 ppmv) for low and upscale cal gases 

<± 3.0% (or <=0.5 ppmv) of the calibration span 

< 2.5% (or <0.5ppmv or <0.2 ppmv) of the calibration span 

>=90% 

3. Apparatus and Calibration Gases 

Sample probe construction material? Glass 0 Stainless 0' Other 0 

Sample probe heated? ~/No.· 

ltPs/No 

Temperature: 

Sample line heated? Temperature: 

. Sample line construction material? Teflon 0' Stainless DOther D 

Particulate filter? Yes ~. In-stack 0 Out-of-stack 0 Heated? Yes I No 

Is concentration detennined on wet or dry basis? Wet!2( Dry ~ 

If dry basis, is moisture removal system adequate? ~No 

If wet basis, is a dilution probe system used? Yes/~ . 

Is sample pump non-reactive to gas stream sampled? ~/No· 

Is flow rate control adequate? ~/No 

Page 1 of 5 
When was the converter efficiency test conducted? Date: ~ lyw'~ 

Which test method was used? N02 gas in calibration mode? Yes / No 

N02 gas before dilution point for dilution systems? Yes / No 

Tedlar Bag Procedure Yes / No Test Time Length (minutes): 

7. System Bias and System Calibration Error Checks 

ISMP·33 

Rev . . 7/07 

Note: A system bias check is conducted on a non-dilution sampling system. A calibration error check 

is conducted on a dilution sampling system. 

Which cal gas best approximates measured emissions? 

Record calibration data in the table at the end. 

8. Determination of Stratification 

Mid-Level 0 

High-Level 0 

When was the stratification test conducted? Date / Time /Vof.~ (;.r lJT'#t., ~~. 

How many points were sampled? 12 o 3 o Other: ..... ____ -'--_ 

How were point locations determined? 

Was each point sampled for twice the system response time? Yes/No 

What was the mean concentration for the points sampled? 

Point and Mean Concentrations Required Sampling Point(s) for Test Runs 

Concentration at each point is <= ±5.0% of Single point that most closely matches the 

mean concentration or <= ±<>.5 ppm mean 

(whichever is less restrictive) = unstratified 

Concentration at each point is <= + 10.0% of Three (3) points at 16.7, 50.0, and 83.3 percent 

. mean concentt:ation or <= +1.0 ppm of measurement line 

(whichever is less restrictive) = minimally. 

stratified 

Concentration at each point is > + 10.0% of Twelve (12) points according to Table 1·1 or 

mean concentration or > +1.0 ppm (whichever Table 1·2 in Method 1 

is less restrictive) =stratified 

9. Sample Collection 

Is the sampling rate within 10% of the flow rate determined during the system response time check? Y~/No . 

Was the sampling system purged for at least two times the system response time with the probe in the 

stack before starting to record data for the test run? ~I No 

Page 3 of5 
Calibration Certified System 

Gas Level cal gas . Response 

(units) Time 

(units) 

Run#= Low-level 

gas 

Gas = Upscale 

gas 

Run # = Low-level 

gas 

Gas = Upscale 

gas 

Run # = Low-level 

gas 

Gas = Upscale 

gas 

Run # = Low-level 

gas 

Gas = Upscale 

gas 

Initial 

values 

System 

-BiasI or 

Cal EiTorz 

(% of cal 

span) 

Final 

values 

System 

BiasI or 

Cal Errorz 

(% ofca,l 

span) 

ISMP-33 

Rev. 7/07 

Drift (% of 

cal span) 

D= ISBfinal 

'- SBil 

Note: Response time should be the time it takes measured concentration to reach 95%'ofupscale gas 

or 5% of the low~level gas or 0.5 ppm (whichever is less restrictive) of the certified gas 

concentration, whichever is longer. 

I Refers to the pre- and post-run system bias checks of a non-dilution system. 

2 Refers to the pre- and post-run system calibration error checks ofa dilution'system. 

Page 5 of5 
February 6, 2008 

Mr. James Eason , 

Stationary Source Unit Manager 

Georgia Environmental Protection Division 

4244 International Parkway 

Suite 120 

Atlanta, Georgia 30354 

Re: Southern Natural Gas Company 

Hall Gate Compressor Station, Baldwin County 

Title V Permit No, 4922~009-0035-V-02-0 

Annual RICE MACT Compliance Test Results 

Dear Mr. Eason: 

'KdF 2Q:lgObl'i 

At ISouthern ep Natura! Gas an EI Peso company 

Attached are tables of results of the Annual RICE MACT testing at Hall Gate Compressor Station. CO 

tests were performed on-site December 20, 2007, using a portable analyzer for Emission Unit C003 

(Compressor Engine No, 3), As shown on the following table, all average results are within permitted 

limits. 

I certify that based on information and belief formed after reasonable inquiry, the statements and 

information in this document are true, accurate, and complete. 

If you have any questions. please contact Mr, Wayne Parrott at 478-477~1221 ext 2024. 

Very truly yours, A /l 

~&:L- Thomas C. Dender 

Director, Southeast Division 

EWP/bg 

UPS No.: 1Z 334 569 02 9258 9935 

Cc: US EPA Region IV 

Air and EPCRA Enforcement Branch 

Sam Nunn Atlanta Federal Center 

61 Forsyth Street, SW 

Atlanta, GA 30303·3104 

UPS No.: 1Z334 569 02 94274888 

Southern Natural Gas 

1900 5'" Avenue Birmingham. Alabama 35203 

PO Box 2563 Birmingham. Alabama 35202.2563 
Emission Unit C003 (Compressor Engine No.3) 

Hall.Gate Compressor Station 

Permit No. 4922-009-0035-V-02-O 

Date Tested: December 20,2007 

CO Results CO Permit 

Limit 

Percent Reduction Across 

the Catalyst 

Run #1 96.94 

Run #2 96.84 

Run #3 97.02 >=93.00% 

Average 96.93 









323.00 

323.00 

324.00 

324.00 

:"~'323:~ /7X,"~<?'" 

32S.40 

'O~06%' 

'5~bo%,' 

321.00 

320.00 

321.00 

321.00 

, "~20;6b'., 

3~.4Q .. ·· 

0.87$ 

5.00% 

326.00 

327.00 

327.00 

325.00 

",326;00' '. 

323.40·,." 
19 41 

345 20 41 

345 19 41 

344 20 41 

343 19 41 

344 12.4 19 41 

343 12.5 19 41 

345 12.4 20 41 

346 12.5 19 40 

348 12.4 18 40 

346 12.4 18 40 

345 12.4 19 41 

346 12.4 19 41 

348 12.4 19 41 

346 12.4 18 40 

346 12.4 19 41 

345 12.4 19 41 

348 12.4 18 40 

345 12.4 19 41 

344 12.4 19 41 

348 12.4 19 40 

343 12.4 19 41 

346 12.4 19 41 

345 12.4 19 41 

344 12.4 41 

345 12.4 41 

344 12.4 41 

344 12.4 41 

344 12.4 41 

346 12.4 41 

344 12.5 41 
11.00 12.40 43.00 14.00 11.00 44.00 

11.00 12.40 44.00 14.00 10.00 44.00 14.00 

11.00 12.40 43.00 14.00 10.00 44.00 14.00 ",.,..' 

~;' 

11.00 12.40 44.00 15.00 10.00 44.00 14.00 t, 11.00 12.40 44.00 14.00 10.00 44.00 14.00 

11.00 12.40 43.00 14.00 10.00 44.00 15.00 ~" l " 

11.00 12.40 43.00 14.00 10.00 12.30 45.00 15.00 

11.00 12.40 43.00 14.00 10.00 12.30 44.00 14.00 ~, 

11.00 12.40 44.00 14.00 10.00 12.30 44.00 14.00 ~', 

11.00 12.40 44.00 14.00 10.00 12.30 44.00 14.00 :F," 

11.00 12.40 43.00 14.00 11.00 12.40 43.00 14.00 :1' r 11.00 12.40 43.00 14.00 11.00 12.40 43.00 14.00 ~ ~~ .:,' 

11.00 12.40 42.00 14.00 10.00 12.40 43.00 14.00 !': 

11.00 12.40 43.00 14.00 11.00 12.30 44.00 14.00 

11.00 12.40 42.00 14.00 10.00 12.30 43.00 14.00 :i f ~~~ ,:', 0" 

11.00 12.40 43.00 14.00 11.00 12.30 44.00 14.00 it; 

'f-",_ 

11.00 12.40 43.00 14.00 10.00 12.40 43.00 14.00 ;f';'~ 

11.00 12.40 44.00 14.00 11.00 12.30 44.00 14.00 

11.00 12.40 44.00 14.00 10.00 12.30 43.00 14.00 :~: ~ 

11.00 12.40 44.00 14.00 10.00 12.40 43.00 14.00 " ;~:' 

i. 

11.00 12.40 44.00 14.00 10.00 12.30 44.00 14.00 

11.00 12.40 43.00 14.00 10.00 12.30 44.00 14.00 

11.00 12.40 44.00 14.00 10.00 12.40 43.00 14.00 

11.00 12.40 43.00 14.00 10.00 12.30 43.00 14.00 

10.00 12.40 44.00 14.00 10.00 12.30 44.00 14.00 

10.00 12.30 44.00 14.00 10.00 12.30 43.00 14.00 

10.00 12.40 43.00 14.00 10.00 12.30 44.00 14.00 

11.00 12.40 43.00 14.00 10.00 12.30 44.00 14.00 

10.00 12.40 43.00 14.00 11.00 12.30 44.00 14.00 

11.00 12.40 44.00 14.00 11.00 12.30 44.00 14.00 
342 

12.4 342 

12.4 341 

12.4 343 

12.4 340 

12.5 340 12.4 

12.4 342 12.5 

12.4 342 12.4 

12.4 343 12.5 

12.5 342 12.5 

12.4 343 12.5 

12.4 343 12.5 

12.4 343 12.5 

12.4 344 12.5 

12.4 342 12.5 

12.4 342 12.5 

12.4 341 12.5 

12.4 344 12.5 

12.4 345 12.5 

12.4 342 12.5 

12.4 342 12.5 

12.4 341 12.5 

12.4 340 12.5 

12.5 342 12.5 

12.4 340 12.5 

12.5 340 12.4 

12.4 342 12.5 

12.4 343 12.5 

12.4 341 12.5 

12.5 343 12.5 

12.5 340 12.5 
'f 

, ~~W·, 

-1~' 

---1:63~ 1~-

__ 1i.'QQ:OQ 

11!QJ,OQ, " 

,11~ 

-' ~<Q3ioO; 

"GaSConc. 

am 

~ GilD , _~1'.QO 

- 12.40 

11.00 12.30 

11.00 12.30 

,11.00 12.30 

11.00 12.30 

11.00 12.30 

11.00 12.30 

11.00 12.30 

11.00 12.30 

11.00 12.30 

11.00 12.30 

11.00 12.30 

11.00 12.30 

11.00 12.30 

11.00 12.30 

11.00 12.30 

11.00 12.30 

11.00 12.30 

11.00 12.30 

11.00 12.30 

11.00 12.30 

11.00 12.30 

11.00 12.30 

11.00 12.30 

11.00 12.30 

11.00 12.30 

11.00 12.30 

11.00 12.30 

11.00 12.30 

11.00 12.30 

11.00 12.30 

'Rwi2B '., , . '. 

','Poe;t .. Catalyst 

'·,'ibne'< 

" 217:Gl.:oO ~. 1 ." '.,' ~ '. 

t' ,: '. ,1l7t~:QQ 11.00 12.30 ~,~, 

•••• 

11.00 12.30 i'~ 

f 11.00 12.30 I, 

[ 11.00 12.30 f 11.00 12.30 

r ,17:,Q:OQ ' 11.00 12.30 i.' 

f 17:1.1;01} " 11.00 12.30 ~, tt:~ 11.00 12.30 r. 1~:j~m, 11.00 12.30 

f 1:1: tft.:OIl 11.00 12.30 ~' ,f~:tS:® 11.00 12.30 

k 11:f6!OO 11.00 12.30 

~ '11;1i

1:00 11.00 12.30 ~ -nm);Oo: 11.00 12.30 ~" 

i~ -j1:19-,.9P 11.00 12.30 

,j ,17~q;0() 11.00 12.30 -iu . • 'n:21,OO, 11.00 12.30 ~: ti\ :17:~QQ 11.00 12.30 

t 

f' 17:23:OQ 11.00 12.30 ~,\, 17:?4:QO ,,' 11.00 12.30 

I, ,17:25;00 - 11.00 12.30 \, 

k 11:26.-00 11.00 12.30 -\':' 

f 17:ai:OO 10.00 12.30 k'-'" 17:211:00 -"', 10.00 12.30 , f 

~ 1taoo 10.00 12.30 It 

t __ 17;~ 11.00 12.30 

,1!:~t:Q() - 11.00 12.30 

l::~ , 17:32:00 10.00 12.30 

17~;oO- 11.00 12.30 

"1,7:34100, 10.00 12.30 

lO.92 
345 12.5 

346 12.6 

346 12.5 

346 12.5 

344 12.5 

345 12.5 

344 12.5 

344 12.5 

345 12.5 

347 12.5 

346 12.5 

345 12.5 

345 12.5 

346 12.5 

344 12.5 

344 12.5 

343 12.5 

346 12.5 

344 12.5 

345 12.5 

345 12.5 

344 12.5 

345 12.5 

344 12.4 

343 12.5 

343 12.5 

347 12.5 

345 12.5 

343 12.5 
, ':-'-,," 

) Oai%) , ,COusPm) 

10.00 12.40 10.00 12.30 

11.00 12.40 10.00 12.30 

11.00 12.40 11.00 12.30 

11.00 12.30 10.00 12.30 

11.00 12.30 10.00 12.30 

11.00 12.30 10.00 12.30 

11.00 12.30 11.00 12.30 

11.00 12.30 10.00 12.30 

11.00 12.30 10.00 12.30 

11.00 12.30 11.00 12.30 

11.00 12.30 10.00 12.30 

11.00 12.30 10.00 12.30 

11.00 12.30 10.00 12.30 

11.00 12.30 10.00 12.30 

11.00 12.30 10.00 12.30 

11.00 12.30 10.00 12.30 

11.00 12.30 10.00 12.30 

11.00 12.30 10.00 12.30 

11.00 12.30 10.00 12.30 

11.00 12.30 10.00 12.30 

11.00 12.30 10.00 12.30 

10.00 12.30 10.00 12.30 

10.00 12.30 10.00 12.30 

11.00 12.30 10.00 12.30 

11.00 12.30 10.00 12.30 

10.00 12.30 10.00 12.30 

10.00 12.30 10.00 12.30 

10.00 12.30 10.00 12.30 

10.00 12.30 10.00 12.30 

10.00 12.30 10.00 12.30 

10.00 12.30 10.00 12.30 
780.00 

2.70 

>,e;::,"11?Jiiiiwsm1li' .~' 

4362.00 
GAS COMPOSITION (Based onEPA standard conditions of 14.696 psia and 68 f 

Constituent MokFraction . MW welahtedMW 

NITROGEN 0.3573 28.0134 10.0082 

CARBON DIOX. 0.6797 44.01 29.9139 

METHANE 96.9378 16.04315 1555.1882 

ETHANE 1.6228 30.0703 48.7972 

PROPANE 0.2158 44.0975 9.5159 

I-BUTANE 0.0486 58.1246 2.8258 

N-BUTANE 0.0531 58.1246 3.0837 

I-PENTANE 0.0229 72.1518 1.6487 

N-PENTANE 0.0149 72.1518 1.0772 

HEXANE + 0.016136 95.958 1.5484 

99.9690 MW 1663.6073 

Upper Dry Heat Value btu/dscf Mole Weight 

Low Dry Heat Value btu/dscf EPA F-Factor (calc) 

SpecHic GravHy -2.8710 

Density 4.4147 Ib/scf 

C+Hl4 201.7676 

Total Carbons 101.5344 Total H 400.9327 
ORIFICE FLOW CALCULATIONS 

Run Number 1 2 3 

Supply Pressure (PSIG) 0.00 0.00 0.00 

Differential (-H2O 0.00 0.00 0.00 

Temperature (OF 0.00 0.00 0.00 

Fuel Flow scfh) 

Fuel Flow scfm) IVALUEI IVALUEI IVALUEI 

PIPE 1.0. 0.00 0.00 0.00 

ORIFICE 1.0. 0.00 0.00 0.00 

PRESS TAP? (1-UP ,2-DN) 0.00 0.00 0.00 

SP. GRAVITY .. 2.87 -2.87 -2.87 

BETA IDIV/oI IDIVIOI IDIVIOI 

K IDIV/o! IDIV/OI IDIV/oI 

K1 IDIVIOI IDIVIOI IDIV/oI 

Be IDIV/oI IDIV/o! IDIVIOI 

E ,DIVIOI 'DIVIOI 'DIVIO! 

kflana WIVIO! 'DIVlC! 'DIVIO! 

Ko IDIVlO! IDIVlO! IDIV/o! 

Fb IDIVlO! IDIVIOI 'DIVlO! 

BB IDIV/o! IDIVlO! IDIVIOI 

Fr IDIVIO! IDIVlO! IDIVlOl 

Fpb 1.00 1.00 1.00 

Ftb 1.00 1.00 1.00 

Ftf 1.06 1.06 1.06 

FG #NUM! INUMI INUM! 

Fpv 1.00 1.00 1.00 

A IDIV/ol IDIVlO! IDIV/OI 

QV 'DIVIOI IDIVlOI IDIVlO! 

C ID I VIa! IDIVlOI IDIVlO! 

Qfh 

Qfm IVALUEI IVALUEI flVALUEI 

K1 for BETA < 0.5 IDIV/OI #DIVIOI #DIV/o1 

K1 for BETA > 0.7 flOIV/O! IDIVIOI IDIV/OI 

QV (DOWNSTREAM TAP) 'DIVlO! IDIVIOI IDIVIOI 

Atm. Press for cales (psia) 0.00 0.00 0.00 
DENSITY 

0.07433 

0.11677 

0.04256 

0.07978 

0.11700 

0.15422 

0.15422 

0.19144 

0.19144 

0.32146 

Carbon Wt. %: 0.737980 

Hydrogen Wt. %: 0.242930 

Oxygen Wt. %: 0.013074 

Nitrogen Wt. %: 0.006016 

1.0000 

1663.6073 btu/dscf --~'V~A~l~U=E::;"1 --dscfIMMbtu 

HHVideal 

1010 

1769.6 

2516.1 

3251.9 

3262.3 

4000.9 

4008.9 

5278 

b(i) 

0.001571962 

0.013390228 

1.124478886 

0.038784203 

0.007423245 

0.002226659 

0.002535933 

0.001327643 

0.000942083 

0.001294107 

1.193974949 

HHVCil ideal 

0 

0 

97907.21335 

2871.653792 

542.9542512 

158.0976223 

173.0748019 

91.4245659 

59.852877 

85.165808 

HHVreal 

Compressibility 

-19.9987371 

HHVCi} real 

0 

0 

-4895.67 

-143.59 

-27.15 

-7.91 

-8.65 

-4.57 

-2.99 

-4.26 

-5094.79 
2 gtbhp-hr 

Ib/hr 

ppm 

2 Calculated 

Panel 

Heat Rate Curve 




..