# APR 012009 

# Georgia Department of Natural Resources Environmental Protection Division • Air Protection Branch 4244lntemational Parkway. Suite 120 • Atlanta. Georgia 30354 

### 4041363-7000 • Fax: 404/363-7100 Noel Holcomb, Commissioner Carol A. Couch. Director:"'- 

### MEMORANDUM: TO: Karen Hays 

## fYi)/

# ~ THROUGH: Ross Winne, 

# 1; DeAa ose.rV(f 

# UV FROM: Dave Sheffield 

# .DS SUBJECT: SOURCE TEST R ORT 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 Inlet (DSCFM) Outlet POLLUTANT CONCENTRATION Inlet (PPM) Outlet EMISSION RATE Inlet (PPM @ 

### 15% 02) Outlet DESTRUCTION EFFICIENCY (%) 

### OTHER INFORMATION



## cc: Ross Winne Reference Number: 200900101 Southern Natural Gas-Hall Gate Compressor Station Milledaevilie. GA Emission Unit C003 I 

### Oxidation Catalvst Carbon Monoxide Dave Sheffield Not Witnessed



## . December 9. 2008

.. 

### February 2.2009 4730 Horsepower

4459 Horsepower 93% ORE 40 CFR Part 60 Subpart

# zzzz.

- RICE MACT; Permit 4922-OO9-0035-V-02-O During the tests, the average catalyst bed inlet temperature was 767.0 degrees 

## F. and the average pressure drop across the bed was 2.80". Engine monitoring data during the tests, as per permit condition 5.2.4, was average RPM of 1000.0, the average inlet temperature was 61.0 degrees 

## F., average suction pressure of946.33 psig, and average discharge pressure of 1040.0 psig. 1A 2A 

### 3A AVERAGE



### 306.31 286.32 323.73 304.45

0.00 0.00 0.00 0.00 212.62 213.83 217.05 214.50

0.00 0.00 0.00 0.00 100

The RICE MACT requires that the catalyst bed percent reduction be tested by measuring the carbon monoxideConcentration before and afterthe bed. Consequently, the air flow was not measured. The minumum reduction is 93 percent.

AIRS Number: 00900035 Printed: 41112009

### January 30, 2009

Mr. Ross Winne Program Manager Industrial Source Monitoring Program 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-O Annual RICE MACT Compliance Test Results

Dear Mr. Winne: 

# A.

# ~Southern 

# e

. . Natural Gas 

# P anElPaaocompany



# RECEIVED 

# FEB 022009 

# fSMp

Attached are the table of results, test report transmission summary, and test report from the Annual RICE MACT testing at Hall Gate Compressor Station. 

### CO tests were performed on-site December 9, 2008, using a portable analyzer for Emission Unit C003 (Compressor Engine No.3). 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.

Ifyou have any questions, please contact Mr. Wayne Parrott at 478-475-1748. Very truly yours,

# ~&:L Thomas C. Oender Director, Southeast Division 

## Ii.lJl EWP/ga

UPS No.: 1Z3345691391136815

Cc: Air and EPCRA Enforcement Branch

- U. S. EPA Region 4 Sam Nunn Atlanta Federal Center 61 Forsyth Street, SW Atlanta, Georgia 30303-3104
UPS No.: 1Z3345691394346422

Southern Natural Gas Colonial Brookwood Center 569 Brookwood Village, SUite 501 Birmingham. Alabama· 35209 PO Box 2563 Birmingtlam, Alabama 35202.2563

### GEPD 

### January 30, 2009 Page 2

Emission Unit C003 (Compressor Engine No.3) Hall Gate Compressor Station Permit No. 4922-009-0035-V-02-O Date Tested: December 9, 2008 CO Results

Percent Reduction Across the Catalyst Run #1 

### 100.17 Run #2 

### 100.18 Run 

### #3 100.18 Average 100.18 CO Permit Limit

>=93.00 

### %

## TEST REPORT TRANSMISSION SUMMARY (Submit separate summary sheet for each pollutant test report)

Submit to: ISMP Database Ross Winne, Program Manager Industrial Source Monitoring Program 4244 International Parkway, Suite 120 Atlanta, GA 30354 

## -----_0!!

## -~4!~6Cfm~V-r!J:l- 

# - - --- No. 

# po

Hall Gate Compressor Station FacilityName:

_________________________________ _ 180 JM Walker Road, NE M ilJedgeville 31061 Facility Address:

__

### --:"=~--------------=--__:_-~~------- Address City Zip 

### Facility Contact:_

.... R

.... an

.... d;;A.Y...;;B

....

u

.... tt

.... 

### s

___________ _ Phone No. 706-547-2135



## PART A

Emission Point (one only): Emission Unit C003 I

### Oxidation Catalyst

Carbon Monoxide (CO) Reduction 1219108 

### Pollutant (one only): Date test performed,.;,.:

_____ _ Applicable Rule(s), Regutation(s) or Pennit Conditions: Pennit 

### # 4922-002-003S-V=02-O Condjtion 4,2,2 

### (Annual) (Indicate Permit # and Condition #'s)

Maximum expected operating capacity:_l_QOIl_Yo_I_oad....;..,:..pl_u_s_or_m_i_n_us_l_QIl_Yc_D

_________________ _ Average load for 3runs = 

### 94.27% (see data summary page) Operating capacity during test: Computed allowable emission rate(s) or limitation(s):Reduction OfeamOD Monoxjde (CQ) 

### by 93% 

## or more (Determined for each applicable rule, regulation or permit conditionusing same units) Reported emissions to atmosphere: %reduction across the catalyst for the average 

### 00runs equals 100.18% (see data summary page) (In same units as rule, regulation or pennit condition)


## The test report should include a compilation ofall CEMS data, control devise parameters and process operating data related to the test.

PARTB

For any facility operating under a Part70 

## Permit, Condition 8.8.3 

## ofthat permit requires the following certification should be signed by a responsible official and included witb the report:
I 

## certify tbat based on my information and beliefformed after reasonable inquiry, the statements and information in this report are true, aecurate, and complete.

Thomas C. Dender

# /~~ Director, Southeast

# Division//5ntJ~?



# ------------------- NAME SIGNATURE TITLE DATE

Rev, 05130/06

## ~.~-",l- ..

## ~-. -,.----------------- 

# ,etp.I

..a.

# so

..,' ' General InfOrmatiOnJ

I

H 

# Pre-Catalyst

IGeneral Information 

# I Unit Infonnation

Companyr--sNG--
StationjliA[LGATE ,- Unit**Nor~'** •



## Analyzer Information 

# I

.**SeriaINUinber"'I--~**

# _w_._._._.---

, 

## . RatedBHPi-4730 -_.-

Modeli 

## 700 Rated 

# RPMi' 1000

r--

.....**~----"'"** "SeriaINumberl 700162

w·

...... ·,··.....·, 

### Analystr 

### HANSEN'- Yearlnstafled[


## Calibration Gas Selection Criteria 

# I

CO

NO



### 02 Expected Max Reading

53705.69

12782.31

11.90 Selection 

### Criteria

Effluent concentrationmust be greaterthan25% ofthe span gas, or Span gas should not be greaterthan twice the concentration equivalent ofthe permit limit

Effluent concentration must be greater than 25% ofthe span gas I or Span gas should not be greater than twicethe concentration equivalent ofthe permit limit

Effluent concentration mustfall within +/- 10% 

### 02 ofthe span gas.



### Mid Gas

Must be 

### » Concentration Must be < Bottle No.



### 181.6 

### 219 272.4 

### BLM003210

8.36 

### 10.5

# Pr-~~----------------------------------------------------------------------- 

# A

. 

# 'el1paso General Information Post-Catalys



# I IGeneral Information 

# I I Unit Information

Start Date 7 -Dec-08
Company SNG

Station HALLGATE 

## Analyzer Information 

# I

Manufacturerr""

### ENE~

.**Model~** 700-

Serial Numberr-ro016'-
Analyst

__ H...;;A_N.....;S...;;E_N.;......_



## Calibration Gas Selection Criteria

PennIt Limit 1---·_·

..

# ·8

. . I IIfbhp-hr

.. Basis L:'::-:

___ •

__ Selection Criteria Unit No. 

### 3

Manufacturer CATERPILLAR

Model G-3616

Serial Number

Rated BHP 4730

Rated RPM 1000

Rated BSFC 7200

Year Installed 

## 2004**r--·-·-'-~Effluent** concentration must be greaterthan 25% ofthe span gas, or CO (Limit)

# I 20.00 Span gas should not be greaterthan twice the concentration equivalent ofthe permit limit

N**Llmlt)r-<~------Effluent** concentration must be greater than 25% ofthe span gas, or

.



### Ox ( 

# i 7.82 Span gas should not be greaterthan twice the concentration equivalent ofthe permit limit

O2 (estimate) 11.90 Effluent concentration rnust fall within +/- 100Al. 02 ofthe span gas.



## !1I:==C_a_li='b_r=au='o=n=G_a_s_I""n"",fo_rma==t1=' o_n===lll

Gases must be EPA Protocol G1 or G2 

### SpanGas
Concentration Must be < CO (ppm)} 

### HliUI 7618.80

NO (ppm)r 

### 2rJB 1789.62

N02 (ppm)1 

## 11m 1789.52

02 

### (%)1 

### 20.9 AmbIentAir BoHle No. 

### BAC4360 

## Ll1gMo

BLMOO'OS17

AMBIENI Must be > 40.36

8.36 

### Mid 

### Gas '
Concentration Mustbe < BoHle No. 

## 50.2 6Q.54 

### SLM004902

10.5 12.64 

### BLMUOO?04 

# I

# ,**~** .• 

# elJ,aso

I General Information 

# I

Datel 7-Dec-08
Company SNG



### Station HAlLGATE

Unit 3



## Data Entry 

# I

Standard CO Response Concentration COlero 0.00 1.00 CO Span 454.00 453,00 CO Mid 219.00 219.00 ozZero 0.00 OzSpan 20.90 OzMld 10.50



## Calculations 

# I

Standard 

### Analyzer Concentration Response COlero 0.00 1.00 CO Span 454.00 453.00 CO Mid 219.00

.. 219.00 Ozlero

.. 

### 0.00

. 0.10 OzSpan 20.90 21.00 OzMid 10.50 10.60 

# I Linearity Check Pre-Catalyst

Anal 

## zer Info

Manufacturer ENERAC

Model Number 700

Serial Number 700162
Analyst HANSEN

O2 

### Response

128 Seconds

0.10 21.00 10.60

Absolute Difference 1.00 1.00 0.00

. 0.10

0.10 0.10 Percent Diference

..•. 

### 0.22% '0.22%

0.00% 0.48% 0.48% 0

..48% Allowable Difference

2.50% 2;50% 2.50% 2.50% 2.50% 2.50% PASS?

YES YES

. YES 

## YES YES

. YES 

# r

# A

.. 

# elpaso

II General Information

Date 7 -Dec-Q8
Company SNG

Station 

### HALLGATE

Unit 

# a·


# r- Data Entry

# ~ Standard

. CO Response Concentration CO Zero 0.00 0.00 CO Span 100.90 101.00 COUid 50.20 50.00 O2

## Zero

. 0.00 O2 

### Span 20.90 O2 

### Mid 10.50



# II Calculations

.. 

### Standard Analyzer Concentration

.. Response CO Zero 0.00· 0.00

. CO Span 100.90 101.00

CO Mid 50.20· 50.00 O2 

### Zero 0.00· 0.00 O2 

### Span 20.90 20.90 O2 

### Mid 10.50 ·10.50 I 

# Linearity Check 

# Post-Catalyst

.Anal 

## zer Info

Manufacturer ENERAC

ModeJ Number 700

. Serial Number 700161 

### Analyst HANSEN·



# ...**~** Response Time

0 1 

### Response

148

0.00 20.90 10.50

. Absolute Percent Allowable

Difference Diference Difference 0.00

... 0.00% 2.50% 0.10 0.10% 2.50% 0.20 0.20% 2.50% 0.00 0,00% 2.50% 0.00 0.00% .2.50% 0.00 0.00% 2.50%

..... 

# I

Seconds

PASS?



## ..YES·

YES YES YES YES YES 

# r

# ~r-~.----------------------------------------------------------------~

# ~ 

# elpaso I General Information 

# I

Datel 7-0ec-08
Company SNG

Station HALLGATE

Unit. 

### 3 

# I Data

## Entry

Elapsed Time Analyzer

(Minutes) Response 

### 1 453 2 453 3 453 4 453 5 453 6 453 7 

### 453 8 453 '9 453

10 453 

## 11 453 12 453 13 453 14 453 15 453



## Calculations

Stability Time



### Stability Period

15 Minutes Maximum Response



### 453.00 

# I

-,

Minimum Response,



### 453.00 Calculated Deviation



### 0.00%

. 

# CO Stability Check 

# Pre-Catalyst

Manufacturer

Model Number

Serial Number
Analyst Span Gas Conc.

Elapsed Time

(Minutes) 

### 16 11 18 19 20 21 22 

### 23 24 25 26 27 28 29 30

Allowable Deviation



### 1.00% ENERAC

700



### 100162**HANS~N**



### 454

Analyzer**Rese.~n!~** 

### "



### PASS?

,YES

# ~~----------------------------------------------------------~ I 

# ',A 

# elpaso I General Infonnation 

# I

. Date 7.;.Dec-OB
Company SNG

Station HALLGATE

Unit 3



## DataEntry 

# I

Elapsed Time Analyzer Response (Minutes) 

### 1 

### 2 

### 3 I.**~'--wr--** 

### 101 

### 101 

### 4 

## 5 6 7 

### 8

1:.1 

### 10 

### 11 

### 12 13 14 

### 15 

# f 101 • 101 

# I · 102 

### 102 I 

### 101 101 

### 101 101 102 102 102 

### 101 

# I Calculations

Stability Period



### 16 Minutes Maximum Response

·102.00 Minimum Response

101,00 Calculated Deviation

# co Stability Check



# .Post-Catalyst 

# I Analyzer Infonnation 

# I

Manufacturer ENERAC

Model Number 700

Serial Number 700161
Analyst HANSEN
Span Gas Cone.

.. 100.9

Elapsed Time

(Minutes) 16 17 

### 18 19 20 21 

### 22 

### 23 24 25 26 27 

### 28 29 

### 30

Allowable Deviation Analyzer**Resp~!!!!_**



## PASS?

### i

... ..., .... - 

# ,elpaso
I General Information 

# I

oatel 7-Dec-08
Company SNG

Station HALLGA TE



### Unit 3



## Pretest

Gas Concentration NO Response NO Span 208 209 N02Span

. 

### 196 CO Zero 0.00 CO Span 454.00 02 lero 0.00 OzSpan 20.90

Gas Concentration Analyzer Response COlero 0.00 1;00 CO Span 454.00 453.00 ozZero 0.00 0.00 OzSpan 20.90 20.90

# ~ PostTest: Run 3 Drift 

# I

Gas Concentration Analyzer Response CO Zero 0.00 0.00 CO Span 454.00 453.00 oaZero 0.00 0.10 O2Span 20.90 21.00 

# I Interferance Check 

# I I 

# Calibration Error Pre-Catalyst 

# I Analyzer Information 

# I

Manufacturer ENERAC

ModeJ Number 700

Serial Number 700162
Analyst HANSEN

N02Response CO Response 02 Response
1 195 0 1 453 0 20.9

Absolute Percent Allowable Difference Difference Difference 1.00 .0.22% 3.00% 1.00 0.22% 5.00% 0.00 0.00 0.30 0.00 0.00 0.50

Absolute Percent Allowable Difference Difference Difference

. 0.00 0.00% 3.00%

1.00 0.22% 5.00% 0.10 0.10 0.30 0.10 0.10 0.50



# co Intenerance**--------~~~--~---** PASS Allowable PASS? YES YES YES YES

PASS?

YES YES YES YES



### 5.00%

# ·elpaso
I General Infonnation 

# I

Date 7,.Oec-08


### Company SNG

station 

### HALLGATE



### Unit 3 

# I Pretest 

# I

Gas Concentration NO Response
NO Span 

### 208 N02Span 

### 196 COlero 

### 0.00 CO Span 

### 100.90 Ozlero 

### 0.00 OzSpan 

### 20.90

.Gas Concentration Analyzer Response COlero 

### 0.00 1.00 CO Span 

### 100.90 101.00 ozZero 

### 0.00 0.10 OzSpan 

### 20.90 21.00 

# I PostTest: Run 3 Drift 

# I

Gas Concentration Analyzer Response 

# co Zero 

### 0.00 0.00 CO Span 

### 100.90 101.00 ozZero 0.00 0.00 OzSpan 

### 20.90 21.00 

# ! Interferance Check 

# I I 

# Calibration Error Post-Catalyst 

# I Analyzer Infonnation 

# I

Manufacturer ENERAC

Model 

### Number 700



### Serial 

### Number 700161 Analyst HANSEN

N02 Response CO Response 02 Response

. 

# r 1 196 0 1 

### 101 0.1 21

Absolute Percent Allowable Difference Difference Difference 

### 1;00 0.99% 3.00% 0.10 0.10% 5.00% 0.10 0.10 0.30 0.10 0.10 0.50

.Absolute Percent Allowable Difference Difference Difference 

### 0.00 0.00% 3.00% 0.10 0.100h 5.00% ,0.00 0.00 0.30 0.10

. 0.10 ," ·0.50

CO Interferance #DIY/Of**----~~~~~------** #DIVIOI .Allowable PASS? YES YES YES YES

PASS?

YES YES YES YES

# A 

# elpaso

I General Infonnation 

# I

Datel 4-0ec-06
Company SNG

Station HALLGATE



### Unit 3 

# --...;;...-- 

# I DataEntry 

# I

Location

10:25:00 435.00 10:26:00 435.00 16.7% ofStack 10:27:00 436.00
Diameter 

### 10:28:00 436.00 Average 435.60 3-Run Average 435.47 Variance Allowable

10:39:00 437.00 10:40:00 436.00 50% ofStack 10:41:00 436.00

Diameter 

### 10:42:00 437.00 Average 436.80 3...;RunAverage 435.47 Variance 0.31% Allowable 5.00%

11:05:00 435.00 11:06:00 434.00
83.3% ofStack 11:07:00 433.00
Diameter 

### 11:08:00 433.00 Average 434.00 3-Run Average 435.47 Variance 0.34% Allowable 5.00% 11.30 11.40 11.40 11.40 11.36 11.30

11.40 11.30 11.20 11.30 11.32 11.30

11.10 11.20 11;30 11.30 11.22 11,30

# Pretest Stratification Determination Pre-Catalyst

al 

## erInformation

Manufacturer ENERAC

Model Number 30-Nov-01

Serial Number 700162**Analyst~....;HA;..;;;...;;.N~S;;.;;;E;;.;.;N~...;.** 

# r

('.

# A 

# elpaso

Date 4-Dec-06
Company SNG



### Unit 3


# ---------

DataEntry

Location

16.7% 

### ofStack Diameter

50% ofStack Diameter

83.3% 

### ofStack Diameter 10:25:00 10:26:00 10:27:00 10:28:00

10:39:00 10:40:00 10:41:00 10:42:00 Average 3-Run Average Variance Allowable

11:05:00 11:·06:00 11:07:00 11:0B:00 Average 3-Run Average Variance Allowable 17.00 17.00 17.00 17.00 17.00 17.53

18.00 18.00 18.00 17.00 17.BO 17.53 

### 1.52% 5.00%

17.00 1B.00 18.00 18.00 17.80 17.53 

### 1.52% 5.00% 

# Pretest Stratification Determination Post-Catalyst

.

11.20 11.00 11.20 11.10 11.16 11.18

11.20 11.10 11.10 11.20 11.16 11.18

. 0.18% 5.00%

11.20 11.30 11.20 11.20 11.22 11.18 

### 0.36% 5.00% • ft

## .-.h.1'7·er Information

Manufacturer ENERAC

Model Number 30-Nav-01

Serial Number 700161 

# --------...,..-- Analyst

__ 

### H_A_N_S

.....

E_N

__



# f':I 

# A, 

# elpaso
I General Information 

# I

oatel ,9-Dec-OB Company SNG

Station HALLGATE

Unit 3



### DataEntty 

# I

nne CO (ppm) 

### I 13:51:00 297 13:52:00 299 13:53:00 302 13:54:00 302 13:,55:00 299 13:56:00 299 13:57;00 304 13:58;00 302 13:59:00 304 14:00:00 306 14:01;00 304 14:02:00 305 14:03:00 309 14:04:00 306 14:05:00 307 '.;06;00 305 '.:07:00 309 14:08:00 307 14:09:00 311 14:10:00 305 14:11:00 307 14:12:00 306 14:13:00 230 14:14:00 309 14:15:00 312 14:16:00 309 '.:17:00 308 14:18;00 309 14:19:00 311 14:20:00 308 '.:2':00 309



# IDrift Check: Optional

# I 

# ° 1%) 2 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.• 12.4 12.• 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.• 12.4 12.4 12.4

Analyzer Gall Cone. Response 0.00**["~" ·2.riO-"·~**  

## coZero CO Span ozZero O,Span 454.00 458.00 0.00 0.10

, 20.110 

## I 21.00 

# t

Analyzer Response

NO (ppm) NO (ppm) TIme 1 51.5 51.6 51 50 51.7 53.1 51.1 52.1 49.7 51.5 49.6 61.2 50.1 52.1 .9 51.5 51.2 50.8 52.2 51.3 51.3 50.5 31.3 50.6 50.9 51.2 50.2 51.9 50.1 49.8 49.1

Absolute Difference 2.00

•.

00 0.10 0.10 0 0 0 0.2 0 0 0 0 0 0 0.1 0.3 0 0 0.4 0 0 0.3 0 0.7 0.2 0.8 0.9 0.7 0.4 0.7 0.7 0.9 0.2 1.6 1.2

Percent Difference

0.44% 0.86% 0.10 0.10 14:22:00 14:23:00 14:24:00 14:25:00 14:26;00 14:27:00 14:28:00 14:29:00 14:30:00 14:31:00 14:32:00 14:33:00 14:34:00 '.:35:00 '.:36:00 14:37:00 14:38:00 '.:39:00 14:40:00 14:41:00 14:42:00 14:.3:00 14:44:00 14:45:00 14:46:00 14:47:00 14:46:00 14:49:00 '.:50:00 14:51:00 14:52:00
,Average Minimum Maximum StdDev

Allowable DIfference

3.00% 5.00% 0.30 0.50 

# RunlA Pre-Catalyst

Ana!lzer Information

Manufacturer

Model Number

Serial Number
Analyst

CO (ppm) 307 310 306 311 315 314 310 312 312 311 308 309 312 311 311 312 311 305 307 312 311 310 305 308 309 306 306 309 306 309 306

306.31 

### 2.30.00 315.00 10.55

PASS?



### YES YES 

### YES YES 

### ENERAC

700

700162
HANSEN

0,(%,

12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.3 12.3 12.4 12.4


### 12.40 12.30 

### 12.40 0.02

Gas Check



### PASS
PASS 

# I

NO (ppm) NO, (ppm)

49.9 1.6 49.3 1.1 49.5 1.5 49.3 1.4 48.4 1.7 49.3 1.2 47.9 1.3 49.4 1.5 47.8 1.3 48.5 2.6 49 1.5 50.4 1.5 51.3 1.2 48.6 1.4 48.7 1.5 : 47.3 1.8 50 1.7 44 2.5 69.9 1.9 48.2 2.2 .9.9 2.7 51.2 1.5 50.8 2.9 47.5 3.2 50.5 1.8 49 2.9 47.8 3 49.3 2.6 49.1 2.4 48.3 2.2 49.9 2.3

50.01 1.13 

### 3150 0.00 (lUO 3.20**~.82** 0.96I!

# ~ 

# ·elpaso

I Generallnformation 

# I

I Date 9-Dec-08 Company 

### SNG

Station 

### HALLGATE

Unit 3**DataEn~**

TIme 13:51:00 13:52:00 13:53:00 13;54:00 13:55:00 13:58:00 13;57:00 13:58:00 13:59:00 14:00:00 14;01:00 14:02;00

. 14:03:00 14:04:00 14:05:00 14:06:00 14;07:00 14:08:00 14:09:00 14:10:00 14:11:00 14:12:00 14:13:00 14:14;00 14:15:00 14:16:00 14:17:00 14;18;00 14:19:00 14:20:00 14:21:00 CO (ppm) 

### a 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 

# I



# IDrift Check Ol!tionall

Gas Conc.
COlero ·0.00 

# r co Span 100.90 

## , O:zlero 0.00 

# I OaSpan 20.90 O2 (%) 13 12.98

13 12.99 12.99 12.99 "

13 13 13 13.02

13 13 13 13 13 13 12.99

13 13 13 12.92 12.9 12.9 12.9 12.97 12.91 12.9 12.92 12.92 12.91 12.93

Analyzer**~.!Iponae**

0.00 101.00 0.00 21,00 NO (ppm) 52.59 52.71 51.25 53.28 53.49 53.34 53.51 51.44 51.85 52.16 53.36 52.69 52.35 51.95 53.15 53.26 53.02 52.78 53.76 53.64 52.88 52.85 53.3 52.76 53.12 52.98 52.76 52.44 52.1 61.37 52.19

. Absolute Dfffentnce 0.00 0.10 0.00 0.10 

# RuntH 

# Post-Catalyst 

# I Analyzer Information 

# I

Analyzer Response

NO, (ppml 1.34 1.47 1.51 1.7 1.81 1.9 2.04 1.97 2.01 2.13 2.26 2.25 2.29 2.38 2.45 2.47 2.52 2.57 2.73 2.82 

## 2.n 2.68 2.76 2.72 2.75 2.73 2.71 2.74 2.69 2.7 2.84

Percent

. Dlffentnce

0.00% 0.10% 0.00 0.10 .Time 14:22:00 14:23:00 14:24:00 14:25:00 14:26:00 14:27:00 ' 14:28:00 14:29:00 14:30;00 14:31;00 14:32:00 14:33:00 14:34:00 14:35:00 14:36:00 14:37:00 14:38:00 14:39:00 14:40:00 14:41:00 14:42:00 14:43:00 14:4-4:00 14:45:00 14:46:00 14:47:00 14:48;00 14:49:00 ' 14:50:00 14:51:00 14:62:00

Average Minimum Maximum

StdDev

Anowable Dlffentnce

3.00% fl.OO% 0.30 O.flO Manufacturer

Model Number
Serial Number
Analyst



## co (ppm) 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 ,0

0 0 0 0

0.00

. 0.00 0.00 0.00

PASS?

YES YES 

### VES VES ENERAC

,,' 700

700161


### HANSEN

0,(%)

12.9 12.9 12.93 12.9 12.91 12.93 12.94 12.93 12.9 12.93 12.9 12.91 12.9 12.91 12.91 12.9 12.92 12.9 12.91 12.92 12.91 12.91 12.91 12.91 12.91 12.9 12.91 12.9 12.9 12.93 12,91

12.94 12.90 13.02 0.04

Gas Check

PASS

PASS NO (ppm) H0 2 (ppm) 52.13 51,61 51.38 51.91 51.09 50.99 51.17 50.65 51.39 51.26 51.64 52.78 53.91 51.35 51.4 52.64 54.84 53.2 53.29 53.91 54.82 55.94 54.95 54.7 53.65 52.88 52.45 63.43 52.51 52.99 54.52

52.75 50.66 55.94

LIt 2.91 2.83 2.88 2.9 2,81 2.86 2.95

3 3.09 3.01 2.99 3.11 3,36 3.09 3.06 3.18 3.49 3.4 3.43 3.45 3.52 3.7 3.7 3.69 3.75 3.6 3.57 3.64 3.64 3,65 3.75

2.82 t.34 3.75 0.62**.~**

### Tune CO (ppm) 

### I 15:06:00 287 15:07;00 284 15:08:00 287 15:09:00 276 15:10:00 285 15:11:00 285 15:12:00 288 15:13:00 287 15:14:00 285 15:15:00

. 290 15:16:00 275 15:17:00 293 15:18:00 291 15:19:00 290 15:20:00 288 15:21:00 2S8 15:22;00 288 15:23:00 289 15:24:00 289 15:25:00 288 15:26:00 285 15:27:00 284 15:28:00 

### 282 15:29:00 286 15:30:00 285 15:31:00 286 15:32:00 285 15:33:00 278 15:34:00 290 15:35:00 287 15:36:00 " 286



# I Drift Check: O£tional 

# I

Gas Conc. Analyzer

# rYCOZ8ro 0.00 

## co Span 454.00 

# I**~og.** Ozlero 0.00 0,10**O~Span** 20.90' 21.00 

### Ana.J.pet Response

O2 (%)

13 13 13 12.9 12.9 13 13 13.1 13.1 13 12.9 13 13 13 13.1 13 13 13.1 13 13 13 13 13 13 13 13 13 12.9 13 13 13



### Absolute Difference HIO 2,00 0.10 0.10 11me 15:37:00 15:36:00 15:39:00 15:40:00 15:41:00 15:42:00 15:43:00 15:44:00 15:45:00 ' 15:46:00 15:47:00 15:48:00 15:49:00 15:50:00 15:51:00 15:52:00 15:53:00 15:54:00 ,15:55:00

15:56:00 15:57:00 '15:58:00 15:59:00 16:00;00 16:01:00

, 16:02:00

16:03:00 16:04:00 16:05:00 16:06:00 16:07:00 

### Average 

### Minimuin 

### ldaxiIDum StdDev

'Percent Olfference

0.22% 0.44%

0.10 0.10 CO (ppm) 287 289 287 287 287 287 284 287 276 285 285 286 287 285 288 2B5 288 287 285 290 286 287 289 285 291 275 293 291 290 288 

### 286


### 286.32 275.00 293.00



### 3.78



### AllOwable Difference

3:00%' 5.00% 0.30 0.50 Oz(%) 13 13 13 13 13 13 13 13 12.9 12.9 12.9 12.9 12.9 12.9 13 13 13 13.1 13.1 13 13.1 13 13 13 13 12.9 13 13 13 13.1 13


### 13.00 12.90 13.10 0.06

PASS?



### YES YES YES YES. 

# r

Gas

.Check 

# r""l
PASS
PASS" 

# A 

# elpaso
I



# I General Information

Date 9·Dec-08 Company SNG

Station HALLGATE

Unit 3**Da~En!2:**

Time 15:06:00 15:07:00 15:08:00 15:09:00 15:10:00 15:11:00 15:12:00 .15:13:00 15:14:00 15:15:00 15:16:00 15:17:00 15:18:00 15:19:00 15:20:00 15:21:00 15:22:00 15:23:00 15:24:00 15:25:00 15:26:00 15:27:00 15:28:00 15:29:00 15:30:00 15:31:00 15:32:00 15:33:00 15:34:00 15:35:00 15:36:00 

# I

I

co (ppm) 

### 0 0 0

.' 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0



# I DriftCheck: 0etional·1

Gas Cone. Analyzer



# _

Re·eon!!....,. CO 

### Zero 0.00 

# r**1~2%** CO Span 100.90 O2 

### Zero 0.00 0.00 O2 Span 20.90 21.00 O 2 (%) 13.24 13.2 13.2 13.2 13.2 13.2 13.2 13.19 13.2 13.2 13.19 13.16 13.2 13.2 13.2 13.2 13.2 13.2 13.2 13.19 13.2 13.21 13.22 13.2 13.2 13.2 13.2 13,24 13.3 13.26 13.24

Absolute Difference 13.00 1.10 0,00 0.10 

# I Run2B 

# Post-Catalyst

Ana!lzer Information

Manufacturer

Model Number
Serial Number Analyst



# nrne 15:a7:00 15:38:00 15:39:00 15:40:00 15:41:00 15:42:00 15:43:00 15:44:00 15:45:00 15:46:00 15:47:00 15:48:00 15:49:00 15:50:00 15:51:00 15:52:00 15:53:00 15:54:00 15:55:00 15:56:00 15:57:00 15:58:00 15:59:00 16:00:00 16:01:00 16:02:00 16:03:00 16:04:00 16:05:00 16:06:00 16:07:00
Average 

### Minimum Maximum 

### StdDev

Percent

. Difference 0.00% 1.09% 0.00 0.10 ENERAC

700

700161
HANSEN



### co (ppm) 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0

0.00 0.00 0.00 

### 0.00

AlloWable DIff8rence



### S.oooAj 5.00% 0.30 0.50 

## , 

# I 

# r

O2 (%)

13.2 13.24 13.2 13.2 13.24 13.2 13.23 13.23 13.2 13.21 13.22 13.24 13.21 13.22 13.2 13.21 13.21 13.2 13.17 13.18 13.17 13.19 13.19 13.2 .13.2

13.2 13.14 13.16 13.2 13.2 13.2

13.20 13.14 13.30 0.02

PASS? Gas 

# n Check 

### YES YES PASS YES YES PASS.s

f-!'" 

# A 

# elpaso

I G1:nerallnformatioD 

# I
Datel 9-Dec-Oe Company SNG

Station HALlGATE
Unit 3 

# I**DataEn~** 

# I

l1me 

## co (ppm) 

### I 16:38:00 291 16:37:00 291 16:38:00 289 16:39;00 292 16:40:00 289 16:41:00 292 16:42:00 290 16:43:00 290 16:44:00 289 16:45:00 288 16:48:00 292 16:47:00 

### 305 16:48:00 311 16:49:00 306 16:50:00 307 16:51:00 305 16:52:00 386 16:53:00 333 16:54:00 328 16:55:00 325 16:56:00 321 16:57:00 339 16:58:00 324 16;59:00 328 17:00:00 326 17:01:00 339 17:02:00 ··335 17:03:00 338 17:04:00 344 17:05:00 354 17:06:00 331



# I Drift Checlc Required 

# I

coZero 

## co Span oaZero 0,Span Gas Cone.
0.00 454.00

0.00 20.90 

### Analyzer 

# r' Response

-- 0.00 

# I 453.00 0.10 

### I 21.00 

# Run3A Pre-Catalyst 

# I Analyzer Information

Manufacturer ENERAC

Model Number 700
Serial Number 700162 Analyst HANSEN



### Analyzer Response
0,(%)

13 13.1 13.1 13.1 13 13 13 13 13 13 13.1 12.6 12.6 12.6 12.6 12.6 12.5 12.2 12.2 12.3 12.3 12.1 12.3 12.3 12.2 12.2 12.3 12.2 12.1 12 12.1



### Absolute Difference

. 0.00 1.00 0.10 0.10 Time ··'7:07:00 11:08:00 11:09:00 17:10;00 17:11:00 17;12:00 17:13:00 17:14:00 17:15:00 17:16:00 17:17:00 17:18:00 11:19:00 17:20:00 17:21:00 17:22:00 17:23:00 17:24:00 17;25:00 17:26;00 17:27:00 17:28:00 17:29:00 17:30:00 17:31:00 17;32:00 11:33:00 17:34:00 17:35:00 17:36:00 17;tmoo 

### Avcrage Minimum Maximum 

### StdDev



### Perceitt Difference

0.00% 

### 0.22% 0.10 0.10 CO (ppm) 347 340 338 343 339 342 340 341 341 335 339 339 337 330 332 330 335 330 330 327 324 327 323 326 325 324 321 320 

### 320 325 321



### 323.73 288.00 386.00 19.84

Allowable .Dlfferenee 3.00% 5.00% 0.30 0.50 

# I

11.7 11.7 11.7 11.7 11.7 11.7 11.7 11.7 11.7 11.7 11.7 11.7 11.7 11.6 11.S 11.6 11.6 11.6 11.6 11.6 11.6 11.6 11.6 11.6 11.6 11.6 11.6 11.5 11.6 11.6 11.6



### 12.10 11.50 13.10 0.54

..PASS?

'YES

. YES

YES YES Gas Cheek

PASS

PASS**~** 

# A

.



# ..elpaso
I

I GeneralInformation

Date S-Dec-08

. Company SNG

Station HALLGATE

Unit 3



### Data En!2:.

TIme 16:36:00 16:37:00 .16:38:00 16:39:00 16:40:00 16;41;00 18:42:00 16:43:00 16:44:00 16:45:00 16:46;00 16:47:00 16:48:00 18:49:00 16:50:00 16:51:00 16:52:00 16:53:00 16:54:00 16:55:00 16:56:00 16:57;00 16:58:00 16:59:00 17:00:00 17:01:00 17:02:00 17:03:00 17:04:00 17:05:00 17:06:00 

# I



# I

CO (ppm) 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0

. 0 0 0 0



# I Drift Check:

## Re~uited 

# I

GasCone. Analyzer

# r~Pflo~· COlero 0.00 CO Span 100.90 101.00 Oalero 0.00 0.00 OaSpan 20.90 

## I 21.00 

# Run3B Post-Catalyst 

# I Ana!l!:er Information

Manufacturer ENERAC

Model Number 700
Serial Number 700161 Analyst

AnalyzerResponse

O2 

### (%, 13.32 13.31 13.31 13.3 13.32 13.46 13.62 13.72 13.78 13.81 13.65 13.58 13.61 13.62 13.59 13.57 13.61 13.56 13.44 13.39 13.31 13.18 13.11 13.18 13.18 13.11 13.1 13.1 13.1 13.1 13.1

Absolute i)ifference 0.00 0.10 0.00 0.10 TIme 17:07:00 17:08:00

. 17:09:00 17:10:00 .17.:11:00 17:1;2:00 17:13:00 .17:14:00 17:15:00 17:16:00 17:17:00 17:18:00 17:19:00 17:20:00 17:21:00 17:22:00 17:23:00 17:24:00 17:25:00 17:26:00 17:27:00 17:28:00 17:29:00 17:30:00 17:31:00 17:32:00 17:33:00 17:34:00 17:35:00 17:36;00 17:37:00
Average Minimum Maximum Std Dev



### Percent

. '.Difference

'0.00% 0.11'%

0.00'· 

### 0.10 CO (ppm) 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0

0.00 

### 0.00 0.00 0.00

Allowable OifferenCe

3.00% 5.00% 0.30 0.50 

# I

Oti%l 13.11 , 13.1 13.1 13.1 13.1 13.09 13.08 13.11 13.1 13.11 13.17 13.14 13.14 13.18 13.1 13.13 13.12 13.13 13.16 13.19 13.2 13.19 13.19 13.16 13.2 13.15 13.16 13.19 13.2 13.2 13.19

.13.27 13.08 

### 13.81 0.21

PASS? Gas Check 

## {'1 YES YES PASS YES YES 

### PASS

# Data Summary**~** 

# elpaso

I



# I



# I GeneralInformation 

# I 

# I Unit Information 

# I

Stillt Date 7-1Jec..{J8 Unit No. 3 Company SNG Manufacturer CATERPILLAR

Station HALlGA TE Model G-3616**Ana~zer** 

### Information 

# I Serial Number p..control**Post~ntrol** Manufacturer ENERAC ENERAC RatedBHP .730

Model. 700 700 Rated RPM 1000

Serial Number 700162 700161 RatedBSFC 7200 Analyst HANSEN



### TestData 

# I
GeneralData Run 'I 2 , Date 1219108 1219108 1219108 Time 1:51PM 1:08 PM 4:U PM AmbientTemperature fF)**r~'~w**

# .." 61.00**64.00-~---** Barametric PI1I!ISUfII ("Hg) 

# I

Ambient Relative HumIdIty(%) 71.00 Catalyst In/eI:

T.fF) " 762.00

CataIystAP**("~)** 2.70 7600 769.00 2.80 Operatingnata 74.00 770.00 2,90 

# Horae=**r-·--·-~9~0~~-·-·-~~~·--·-~~~~~ --~.-'---=--.~<-** 
% Load • 93.32% 04.59% 04.90% % Torque 93.41%04.40%

. 85.00% AMPc;.;

### r-'--'~-"---'

# .**-'---;;:-;--"""-'N---~1106** ---
AMT fF) 

### ! 168.00 171.00 173.00 suet. PI1I!IS. (psig). ',938.00 945,00 956,00

Suet. Temp. fF) 81.00 61.00 61.00 Dlsc.Press.(PSlg) 

# I

1130.00 113900 1151.00

pisc.Temp.fF) 91.00 91.00 91.00 FuelData
Fuel Presslll8(psig) FuelDifferential t"M) Fuel temperature ("F) PRESS TAP? (1-t1p,a-DN) Pipe 10 (In.) OnifiCe 10 (In.) Fuel Use

- Panel (dl) Fuel Use

- Calculated (scIh) 31640.00 31910.00 32170.00

1A 1B 2A 2B 

### aB Emissions Data
'KoO:r 12.40 .12.14 U.OO 13.20 12.10 13.27

% O:rCoIT1lClBd 12.3li 12.86 12.15 'IU2 .12.0S 13.19

.. CO 308.31 • .00 Z88.J2 0.00 

### ·'a3.n 0.00
COComldad 308.82**~.60** 286.77 ,0.&0 S2UO .o.liO

.. '.

COO1li'Ko OZ 211.84 • .0.37 212M

. .0.•**·218~2** . .0.38
CO Reduc:tion 100.17% 100.18% .. 10D.18% CO Reduc:tion ".GO%. 13.00% 13.00% PASS? YES YES

.. YES

....... Average

12.17

16.17 787.00 2.80

4459.00 1000.00 84.27% .14.27% 1 10.&1 170.87 848.33 11.00 1140.00 81.00

"906.87

t2.GO 13.14 1lA5 13.06 .'. 30US 0.00

. .305.96 .o.liO 213.lili

..CU8 100.18% 83.00%

YES

.. NOTE. IfttllS Is an Initialtest ora post.catalystchange test. tIlen communicate new catalyst dl!l8rential pressure everege to Automation pe!SOIlnelso thatcontrol system can be update with new baseHne.

. Fuel Determination 

### ·1 Panel

### m~ ••••••

__

# .E**~(**Pre)

(post) (pre) Post) 1%

# ~p; 1)1)1 

# r

P p iDpm (Pre)

m (POtIt) m (pre) m{Post) 

# r

m 015%02 (Pre) P pm • 111%

### oa (Post) 1% Calculated 

### 1% RequiredGAS COMPOSITION**(e,,~,,<:;j** tlillJ'/;**~t,i)n,L;ti** Lv:;clllizlI,'. {)[i'LL

... L**~** in!} tiL ! Constituent Mol. Fraction 

# I MW 

# II weighted MW 

# I 

# r

NITROGEN 0.4150 28.0134 11.6249 CARBON DlOX. 0.9453 44.01 41.6010 METHANE 95,9503 16.04315 1539.3443

ETHANE 2.1097 30.0703 63.4394 PROPANE 0.3548 44.0975 15.6467 I-BUTANE 0.0665 58.1246 3.8645 N-BUTANE 0.0730 58.1246 4.2430 I-PENTANE 0.0320 72.1518 2.3055 N-PENTANE 0.0202 72.1518 1.4579

HEXANE + 0.025978 95.958 2.4928 99.9926 

### MW 1686.0201
Upper Dry Heat Value btu/dsef Mole Weight

Low Dry Heat Value btu/dsef EPA F-Factor (calc) Specific Gravity -2.8399 Density 4.4748 Ib/sef

C+H/4 202.6564

Total Carbons 102.2268 Total H 401.7184

Constituent LHVideal LHV(i) ideal 

# I LHV!il real 

# I

NITROGEN 0.00 0.00 CARBON DIOX. 0.00 0.00 METHANE 913 87602.58 -4275.48

ETHANE 1624 3426.16 -167.21 PROPANE 2322 823.89 -40.21

. I-BUTANE 3010 200.12 -9.77

N-BUTANE 3020 220.46 -10.76 I·PENTANE 3711 118.58 -5.79 N-PENTANE 3718 75.13 -3.67

HEXANE + 4904 127.40 -6.22 LHVreal -451910 ent 

### SG b NITROGEN 0.96723 0.401379171 0.0044 CARBON DIOX. 1.51955 1.436372872 0.0197 METHANE 0.55392 53.1487658 0.0116 ETHANE 1.03824 2.190377004 0.0239 '

.. PROPANE 1.52256 0.540236262 0.0344 I·BUTANE 2.00684 0.133426764 0.0458 N-BUTANE 2.00684 0.146497313 0.0478 I-PENTANE 2.49115 0.079602207 0.0581 N-PENTANE 2.49115 0.050336177 0.0631

HEXANE + 3.3127 0.086057321 0.0802 SGreat -2.839946

### ORIFICE FLOW CALCULATIONS 

# r 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 (seth) Fuel Flow (sctm) #VALUEI #VALUEI #VALUEI PIPE I.D. 0.00 0.00 0.00 

### ORIFICE I.D. 0.00 0.00 0.00 

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

### SP. GRAVITY -2.64 -2.84 -2.84 BETA #DIVlO! #DIVlO!

. #DIVIOI K #DIVlO! #DIVIOI #DIV/OI K1 #DIVIOI #DIVlO! #DIVIOI Be #DIVlO! #DIVIOI #DIVIOI E #DIVIOI #DIVIOI #DIVlO! kfIang #DIV/OI #DIVlO! #DIV/O! Ko #DIV/OI #DIVIOI #DIV/OI Fb #DIVIOI #DIVIOI #DIV/O! BB #DIVIOI #DIVIOI #DIV/OI Fr #DIVIOI #DIV/OI #DIV/OI Fpb 1.00 1.00 1.00 Ftb 1.00 1.00 1.00 Ftf 1.06 1.06 

### 1.06 FG #NUMI #NUMI #NUMI Fpv 1.00 1.00 1.00 

# r
R #DIVlO! #DIVlO! #DIV/O! QY #DIVIOI #DIV/O! #DIV/OI C #DIVlO! #DIV/O! #DIV/OI Qfh Qfm #VALUE! #VALUE! #VALUE! K1 for BETA < 

### 0.5 #DIV/O! #DIVlO! #DIVlO! K1 for BETA> 0.7 #DIVIOI #DIVlO! #DIV/OI QY (DOWNSTREAM TAP) #DIVlO! #DIVIOI #DIVlO! Atm. Press for cales (psia) 0.00 0.00 0.00



# r
1DENSITY 0.07433 0.11677 0.04256 0.07978 0.11700 0.15422 0.15422 0.19144 0.19144 0.32146 Carbon Wt. 

### %: 0.734995 Hydrogen

# wt. %: 0.240170

Oxygen Wt. 

### %: 0.017940 Nitrogen Wt. 

### %: 0.006895 1.0000

1686.0201 btu/dscf**---#~V~A~L~U~E':""!**

### --dscf/MMbtu

HHVideal 

# I

1010 1769.6 2516.1 3251.9 3262.3 4000.9 4008.9

5278

b(i) 0.001825903 0.018621661 1.11302297 0.050421878 0.012205842 0.003045059 0.003489352 0.001856527 0.001274999 0.002083436 1.207847627 HHV'1l ideal 

### 0 0 96909.75856 3733.328659 892.7651181 216.2058234 238.1446377 127.8447586 81.0038334 137.111884 HHVreal

Compressibility ·20.48953646

# I HHV(i) real 0 0 -4729.72 -182.21 -43.57 -10.55 -11.62 -6.24 -3.95 -6.69 -4994.56 

# r

### " 

# r

f

### 1 g/bhp-hr Ib/hr ppm 

### 2 Calculated Panel Heat Rate CurveA,"

. '., 

## Continuous Monitoring System Perform.a.nee, Evalu,a,'tion

.**..,._~** 

## Worksheet forNESHAP Compliance 

# elpaso General Inforamtion

IGeneral Information 

# I

Dater---.;...._

.._-- companyr---'


## Stationr--

.._- 

## Analyzer Information 

# I

Manufacturerr--

r·

..**·"-~---'~·-·** 

### Serial Number!**Analystr---~** 

### •



## TestData 

# I

Elapsed Time

.Actual TlmeCMS fF) 

### Handheld (OF) 

### 0:01**r---·---~---"·---·'---** 

### 0:02 

# I
0:03 I 0:04 0:05 0:06 0:07 

### 0:08 0:09 0:10 0:11 0:12 0:13 

### 0:14 0:15 

### Average 15 min. '.' 

## Unit Information 

# I

Unit No,r--'-**!.--.---~----** 

### Mahufacturer,**Modelr~'-'-'- versionr~-----­** 



### Rated BHPr-----

Rated**RPMr---"---'---~** 

### Rated**BSi=cl~-'-'**

### -"**-~...;-----.".**


### Year 

## 'nstalledr-----



## Calculations

CMSAverage

Handheld 

### Average

',' 

### Absolute Difference Allowable Difference"

PASS?

"


### "Allowable difference Is 5% of reading.



# '. p F

0

### F

0F
,', 0

### F

### t



### •

..

# elpaso
I Horsepower Prediction

Horsepower Determination


# BHP::=[PsLANf..l1 

# IR.q-;/

# -l-.{·**l+R-~ ~R~"J.[1+LF+WF11.** +NF)+HIE-R 3300011]-1.

. . . TJMech 

# J

I I

Ideal HOl'8epowerCalculation Coefficients •.

... BHP 

### '" Brake horsePOWer

. Calculated L = Lenath of comMlssor stroke (Ft) Constant A = Area ofCOtnDressor lliston (In.2) Constant N II; Actualrevolution DermInute (RPM} 

## .... Measul8d R= Compression ratioQf engine calculated from the equation ( R=Po/Ps ) Calcualted p • 

# .. Suctlon.pressure(pSIA} 

### I PSlG 

### + 14.731 Measured P" 

# .. Dischargepressure (pSIA) {PSIG 

### +f4.73

### J Measured

...

11 = Polytropic exponentfrom the eguationofstate relation (

### PV'l '" Constant (11=128) 

### J Constant

.

. UnitSpeelfCalculation Coefficients

I"IMECH = Mechanical efficiency (0.95 for reciprocating, separable gas compressors) Constant

WF 

### "" Waste factor calculatsd from the relationshlD' WF

.. K 11OOrR-1} 1 Constant

.. 

### NF 

# = Speed factor computed from curve coeffICients Constant K 

# =Waste"K" factorentered from engine curve coefficients Constant 

### LF 

# = Pulsation Ioadina factor computed from curve coefficients Constant HPD-R 

## '" Residual horsepowerfrom deactivated compressorcylinder end

.. Constant
m 

# = Clearance volume measured as a fractlon of piston displacement Constant 

# I Measurement Devises

.value Device

... Accuracy

N

.. Magnetic Pickup +/. 0.5 RPM P

s Pressure Transmitter

.. +/

..0.1 % offull scale Po Pressure Transmitter +/-0.1 % offull scale ..



### (-I

. I

# elpaso Horsepower 

# Measurement
# I HorsepowerDetermination 

# I

( PLAN.

# J(' ·1

...

# J

.. BHP == 

# 396,000 1Jmech 

# I Equation Coefficients 

# II

Horsepower Calculation Coefficients .' 

### SAP 

# = Brake horsepower Calculated



## ... p 

# =Meari effective pressure ofcompression 

### I expansion strokes Measured 

### L 

## = length ofcompressor stroke (in.) Constant 

### A 

### = 

### Area ofcompressor pistOn 

### (in.2) > 

### .'. Constant 

### N 

# =Actualravolutlonperminute (RPM) .•.• 

## . .'

'.' 

### Measured i 

### 396,000 

# =Constant

.. ' .. 

### Constant

Unit Speclf Calculation Coefficients 

### IlMecHI == 

### IMechanlcal efficiency (0.95 for reciprocating,seperable gas compressors) IConstant 

# I Measurement Devises 

# I

Value Device

..... 

### Accuracy 

## i

.C 

### N Encoder . , 

### +/- 0.5 RPM

. I 

## P

s Engine analyzer

. ' .... 

### +/-1.0 % offullscale 

## !
Po Engine analyzer

, .,. 

### +/-1.0% offull scale!


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# ) "



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