# !APR 0l11lO9 

# Georgia Department of Natural Resources Environmental Protection Division. Air Protection Branch 4244lntemational Parkway. Suite 120. AUanta. Georgia 30354 404/363-7000. Fax: 404/363-7100 Noel Holcomb, Commissioner 

### Carol A. 

### Couch, Director 

## MEMORANDUM: 

## fO:,! THROUGH: FROWl: Karen Hays 

# r(.)**,~** Ross Winne, DeAn.n.)a.Qser.V(S 

# W Dave Sheffield 

## 1::1 t:(

# Y**SLJ~~ECT:** 

## SOURCE TEST REPORT REVIEW The following test has been reviewed and was conducted 

## inan acceptable fashion for the purpose intended COMPANY NAME Southern Natural Gas-Wrens Compressor Station COMPANY LOCATION Wrens. GA SOURCE TESTED Emission Unit COOS 

### I 

## Oxidation Catalvst POLLUTANT DETERMINED Carbon Monoxide REPORT REVIEWED BY Dave Sheffield TEST WITNESSED BY Not Witnessed DATE(S) OF TEST December B. 200B DATE RECEIVED BY APB February 2.2009 MAXIMUM EXPECTED 3530 Horsepower OPERATING CAPACITY OPERATING CAPACITY 3407.67 Horsepower ALLOWABLE EMISSION RATE ·93%DRE APPLICABLE REGULATION

. 40 CFR Part 60 Subpart

# zzzz.

. RICE MACT; Permit**4922-16~002B-V-02-0** 

## and

CONTROL EQUIPMENT A.ND MONITORING DATA

TEST RUN # 

## 3AS TEMPERATURE Inlet 

## ,oA Outlet 3AS MOISTURE Inlet :%) Outlet 3AS FLOW RATE Inlet 'ACFM> Outlet 3AS FLOW RATE

. Inlet :DSCFM) Outlet =>OLLUTANT Inlet :ONCENTRA TION :PPM) Outlet :MISSION RATE Inlet :PPM @ 

## 15% 02} Outlet JESTRUCTION :FFICIENCY(%) )THER INFORMATION



# ::c: Ross Winne**~eference** 

## Number: 200900102 V-02-2 During the tests, the average catalyst bed inlet temperature was 791.0 degrees F. and the average pressure drop across the bed was 3.16". Engine monitoring data during the tests, as per permit condition 5.2.4, was average RPM of 1001.67. the average inlet temperature was 63.67 degrees F., average suction pressure of 847.67 psig, and average discharge pressure of 1090.33 psis. 1A 2A 3A 

## AVERAGE

282.58 312.55 298.56 297.89

15.95 15.04 14.95 15.31 214.02 216.69 203.41 211.37

12.00 10.19 10.10 10.76 94.845

; 

## 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: 16300028 "Printed: 

## 3/31/20090,. 0,._ 

## c.

... 0,._ 

## "- '-**~** Co Co. 

### c... 100 Roo..o 

### c.... c.o. Ceo. Reo.- 

## c.-.

c.- 

# ..., R..o.oo.

## cc...

'.1 UnearHy Check

0,._ c,.

... 

## c._ '-**~** 

## "- c..._ c...

... c..._ Spec: Flue gas**~** IndIcaIed bygas analyzer c::or-nrallon 01 .ero gaslndlcaled bygas lI'IIIl)'zer Concen1rat!on 01 tnld-tevel gas lndlcaled by gas .-.aIyZer Concen1rat!on 01 $pangas indicated by gas analyzer Ac1uaI**~oI$pangas** Ac1uaI**~ofzercgas** Ac1uaI concentration 01 mJd.levelgas A_e0I1n1Ua1 and !InaIzere ched<s A-.ge0I1n111a1 and final span ched<s ComIt:1ed IIue gas_ CO InIerf1nnce

.... ponse. % CO response 10 NO $pan gas. ppm CO concentration 01 NO $pan gas. ppm NO coo_,balloll01 NO In stack gas. ppm NO
coo

..... ,b&!Ioo' 01 CO In stack gas. ppm CO CO restlOf'IS81o NO. spangas. ppm CO _01NO, span gas. ppm NO, _01NO, In_gas. ppm NO, NO

_ ...... response. % NO _10 NO. spao gas. ppm NO coneenf1a1lon 

### orNo,. In stack gas. ppm No,. Unealfty.%

11.1 C8IlbrIIIon Conec:tlons

v

11.2CO lnIerfenmc:a Response:
100 ({Rco..., I 

### c.... Xc,.,.1Ccosl' 1R<:o-.1 c..,,,, X c.-/CcoslIX100

Rc-o 

### c....CCeo. 

### • Rc-o. 

## c.-.

c.- 100 Spec:
11.S NO Interl

__Response:**~I** c.-l X(c.-/c.....JX 100



### •Facility Location Source Date/TIme Run 

## I EPO Reference #I

1.3 Stability Check
elapsed TIme (min) .,..,..,.;,;,;;.,.".,,..,...,;..;;,;..,,,......,..; 1 2 3 4 5 

### e 7 8 9 10 11 12 13 14 115 11l 17 11l 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 3fl 37 38 39 40 41 42 43 44 45 4fl 47 48

Actual concentration oflpan gas

15-mlnute Stabllty Period
Minimum

.. Maximum

..
MaxDev

.. Spec

3O-fnlnute Stabllty Period

Minimum Maximum

MaxOev Spec Stablity TIme • 

# ..FaCIlity Location Source Date/lime 

### Run 

## I EPD Reference # 

### · o\Jtfl

## etll Natural Gas Wrens**·Comp""ssor~tatiOrt** 

### COmp, 

### t:1l9.No. 5



### 12108tOS Pre.cataly$t 

### 200900102

10.4 Pretest Calibration Error Check

Initial NO Cell Temperature Spec 

### = Response limes NO 

### CO 

### NOt NO: 

### '" 

# = '" TIme required to respond 

### to 95% step change in analyzer response for both zero and span gases Time required to respond 

### to 95% step change In analyzer response for both zero and span gases TIme required 

### to respond 

### to 95% step change In analyzer response for zero gas

Zero Span 

### =

Pretest calibration Error Check

C RZ,,", 

### '"
LZero 

### C

RSpan
CMA

Zero Error 

## ,.

Spec Zero Span Error 

### =

Spec Span 11me required to respond 

### to 90% step change In analyzer response for span gas

1 0.4 Post test Calibration Error Check

Final NO Cell Temperature Spec Spec Post Test calibraHon Error Check**~Zero** LZero 

### ,.**~Span** 

### '" 

### C

MA
Zero Error 

### =

Spec 

### = Zero Span Error 

### =

Spec 

### '" Span F.Facility Location Source Date/Time Run 

## I EPD Reference if tn**~turaf** Gas



### .tenS CClmptessor Station 

### CC/mp;Er!g:No.6



### 121OSlO8**~..()atalyst ~SOOt02** 

### January 30, 2009

Ross Winne Program Manager

. Georgia Environmental Protection Division 4244 International Parkway Suite 120 Atlanta, Georgia 30354

Re: Southern Natural Gas Company Wrens Compressor Station, Jefferson County Title V Permit No. 4922-163-0028-V-02-0 Annual RICE MACT Compliance Test Results

Dear Mr. Winne: 

# A tsouthern 

# ep Natural Gas

enBPasocompany

,. 

# RECEIVED 

# -1ft)m 81m! 

# ISMP

Attached are tables of results of the Annual RICE MACT testing at Wrens Compressor Station. CO tests were performed on-site December 8, 2008, using a portable analyzer for Emission Unit C005 (Compressor Engine No.5). 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 478-477-1748.

# V~&L
Thomas C. Dender**~tor,** 

### Southeast Division EWP/ga

UPS: 1Z3345691391136815

CC: 

### Air and EPCRA Enforcement Branch

- U. S. EPA Region 4 Sam Nunn Atlanta Federal Center 61 Forsyth Street, SW Atlanta,**G~orgia** 

### 30303-3104
UPS: 1Z3345691394346422

Southern Natural Gas Colonial Brookwood Center 569 Brookwood VIllage, Suite 501 Birmingham, Alabama 35209 PO Box 2563 Birmingham. Alabama 35202.2563

## GEPO January 30, 2009 Page 2



### Emission Unit C005 (Compressor Engine No.5) Wrens Compressor Station Permit No. 4922-163-0028·V-02-O Date Tested: December 

### 8, 2008 CO Results

Percent Reduction Across the Catalyst Run #1 94.76 

### Run #2 95.62 

### Run 

### #3 95.37 

### Average 

### 95.25 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

Wrens Compressor Station

# '-;;~~(JZ5~8!6i73'**'}~**

# ......**,(~((** q

# ~ j) 

# 7J

Facility Name:

_________________________________ _ Highway 17 North Wrens 30833 

### Facility Address:

__ 

# --:-=

_______________ 

# =

____ --:;-,.......

______ _ Address City Zip 

### Facility Contact;..,:.;;.;R;;;;an;.;.;d

.. Y...;B;.;u;;.;;;tts=--

___________ _ Phone No. 706·547·2135



### PART A

Emission Point (one only): Emission Unit C005 / Oxidation Catalyst

Carbon Monoxide (CO) Reduction 12/8/08 Pollutant (one only): Date test performed

.... :

_____ _ Applicable Rule(s), Regulation(s) or Permit Conditions: Permit 

### # 4922·J63-0028-V·02.Q Condjtjon 4 2 2 (Annual) (Indicate Permit # and Condition #'s)
Maximum expected operating capacity:

___ 1 O

...**~_VO_I** 

### ... 

### o_ad...:.,..!..p_lu_s_or_m

......

in

... us_1 0

... 0/1

... 0

_________________ _ 

### Average load for 3 runs 

## =96.53% (see data summary page) Operating capacity during test: Computed allowable emission rate(s) or limitation(s): Redyction ofCarbon Monoxide (Co) by 93% or more (Determined for each applicable rule, regulation or permit condition using same units) Reported emissions to atmosphere: % reduction across the catalyst for the average of3 runs equals 95.25% (see data summary page) (In same units as rule, regulation or permit condition)


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

PARTB

For any facility operating under a Part 70 Permit, Condition 8.8.3 ofthat permit requires the following certification should be signed by a responsible official and included with the report:

I certify that based on my information and beliefformed after reasonable inquiry, the statements and information in this report are true, accurate, and complete.

# ~&L**------------------------~** 

## Thomas C. Dender**Director~** 

## Southeast Division /'**/3~6c?** 

## NAME SIGNATURE TITLE DATE

Rev. 05/30/06

# II



# I General Information Pre-Catalyst

IGeneral Iriformation 

# I 

# I Unit Information 

# I

Start 

### Dater----r.Bec-08 COmpanyr----sNG---
stationjW'RENSUnit No.r- 

### 5

ManUfacturerr-'

## CATERPILLAR--"**Modelr-~~G-3a12-LE---** I 

## Analyzer Information 

# I Serial Number,'"

## .-~ ---:.-**RatedBHPr----~-** 

### ManufacturerrENERAc'-



### Mode1r

Serial Numberf-- 700162
Analystr HANSEN**RatedRPMl-.......,..100~0** 

### ---

Rated BSFCr

Yearlnstalledl 

# -6600 ..•

----

2004



## Calibration Gas Selection Criteria 

# I

co

NO



## 02 Expected 

### Max Reading

7528.73

2009.87

11.90 Selection Criteria

Effluent concentration must.be greater than**~5%** 

### ofthe span gas,or Span gas should not be greater than tWice the concentration equivalent ofthe permit limit

Effluent c()ncentration must be greater than 25% ofthe span gas, or Span. gas should not 

### be greater than twice thetoncentrationequivalentofthe permit limit

Effluent concentration must 

### fall Within 

### +1-10% 02 ofthe span gas.



## Calibration Gas Information 

# I

Gases must 

### be EPA Protocol G1 or G2 

### Span Gas 

### Mid Gas
Concentration Must be <


### . Bottle No. Must be 

### > COncentration Must be < 

### Bottle No. CO (ppm)1 

## 454 16067.46 

## SLMDrH408 181.6 

### 219272.4 

## BtMOO3210'

NO (ppm) 208 281.38 LL19680

N02 

### (ppm) 196 281.38 BLMOOO817



### 02 (%)1 

### 20.9 Ambient Air 

### AMBIENI 8.36 

### 10.5 12.64 BLMUOOt04

## · .......

# ~**·/I·~~·············· ~~**  

# ·epaso General Information 

# Post-Catalyst

IGeneral Information 

# I I Unit Information 

# I

Start Date 7-0ec-08 Unit No. 5 

# ----..,.--

------------------- CompanY

__**..;;.S.;...NG~**__ Manufacturer CATERPILLAR



# ------------------- Station WRENS 

# -----_
.... Model G-3612-LE

### ------~--~------- 

# I Analyzer Information 

# I Serial Number

Manufacturerr-ENERAC- RatedBHP 3530



# ------------------- MOdeif'" 700 Rated RPM

___ -..;.100.;.;· .;...0

_____ _
Serial Numberr 700161 RmedBSFC

______**·.;...66.;.;O.;...O~**___ _ Analyst HANSEN Year Installed .2004**~------~~----~**

# 1~-=_=_==C==ali_·b=r=a=tt=·o=n_=G=a=s=S=e_~=c_n_·o=n=C_=ri=te_n_·a __ 

# ==

__... 

# 1

.

Sal.action Criteria

mit

### ~--Effluent concentration must be greater than25% ofthe span gas/or CO (LI .),

. Span gas should not 

### be greater than twicethe concentration equivalent ofthe permit "mit



### , . N

. Limit

### ,~~"".~~**;;.-~-~.**Effluent concentration must be greater than 25% ofthe span gas, or

.



## Ox « )
, . Span gas should not be greater than twice the concentration equivalent ofthe permit limit

O2 (Eatlmate) 

### 11.90 Effluent concentration must fall within**tl"100~02** 

### of the span gas. 

# I Calibration Gas Information 

# I

Gases mUlt be EPA Protocol G1 or G2 

### Span Gas Mid Gas
Concentration Must be < Must be > Concentration Must 

### be <

### Bott~No. CO (ppm)1 

# nnu 1054.02 40.36 

## 50.2 60.54 

## SLMOO4M2

NO (ppm)1**~lll:!** 

### 281.38**C[H'~SSCi**

### N~(ppm)l**H~tI** 

### 281.38 

## EJCt;illlllt'lSt i02 (%)1**20J~** 

### AmblantAJr 

## AMEJiENi 8.36 

## 10.5 12.54 

## BLMUOO7tJ4

# A 

# elpasO

General Infonnation 

# oatel 1-0ec-08
CompanySNG

Station WRENS



### Unit 5



# Data Entry 

# I

Standard CO Response Concentration CO Zero 0.00 1.00 CO Span 454.00 453.00 COMJd 219.00 220.00 OzZero 0.00 OzSpan 20.90 OzMid 10.50 

# I Calculations

Standard Analyzer Concentration Response CO Zero 0.00 1.00 CO Span 454.00 453.00 CO Mid 219.00·· 220.00 ozZero 0.00 0.10 OzSpan 20.90 21.00 OzMld 10.50 10.60 

# LinearityCbeck Pre-Catalyst

Anal 

# zer Info

Manufacturer ENERAC

Model Number 700

Serial Number 700162
Analyst HANSEN



# Response Time

OzResponse

128.00

0.10 21.00 10.60

Absolute Percent Allowable Difference Dlference Difference 1.00 0.22% 2.50% 1.00

. 0.22% 2.60% .1,00 0.22% 2.50%

.. 0.10

.. 0.48% 2.50% 0.10 0.48% 2.60% 0.10 0.48% 2.50%

.. Seconds

PASS?



## YES YES YES YES YES YES

# ~ 

# elpaso**.~** General Information 

# I

Date 7-Dec-08



# ------ CompanY

__ 

### ..;.,S.;,..N..;.,G

__ 

## station _-..;..W-.R.;.;;;E;.;..;N;.;;;.S

__ Unit 

### 5



# ------

II Data Entry

Standard CO Response Concentration CO Zero 

### 0.00 0.00 CO Span 

### 100.90 101.00 CO Mid 

### 50.20

. 50.00 Oa lero 

### 0.00 OaSpan 

### 20.90 Oa Mid 

### 10.50



# Calculations

Standard Analyzer Concentration Response CO Zero 

### 0.00 0.00 CO Span 

### 100.90 101.00·· CO Mid 

### 50.20 50.00 Oa Zero 

### 0.00 0.00 OaSpan 

### 20.90 20.90 O

2 

### Mid 

### 10.50 10.50 

# Linearity Check Post-Catalyst

Anal 

# zer Info

Manufacturer ENERAC

Model Number 700

Serial Number 700161 Analyst**HANSf~.N**



# Response Time

OaResponse



### 148.00

0.00 20.90 10.50

Absolute Percent Allowable Difference Dlference 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%

.. 

### Seconds

PASS?



## YES YES YES YES YES YES

# A

. 

# elpaso
I**~** General Information

Datel 7-Dec-08
Company SNG

Station WRENS

Unit 

### 5



# Data Entry

Elapsednme

(Minutes) 

### 1 

## 2 3 4 

### 5 

# e 7 

### 8 9 

## '10

11 

## 12 13 14 

### 15 Analyzer Response 

## 453 453 453 453 453 453 453 453 453 453 453 453 454 453 453



# Calculations

Stability Period

15 Minutes 

## Maximum Response



## 454.00 

# I

I

I

Minimum Response



## 453.00 Calculated 

## Deviation

0.22% 

# CO Stability Check


# I Pre-Catalyst

Analyzer Information

Manufacturer

Model Number

Serial Number Analysj Span Gas Cone

..

Elapsed Time

(Minutes) 

### 16 17 18 

### 19 

## 20 21 

## 22 23 

## 24 25 26 27 

## 28 29 

## 30

Allowable 

## Deviation

1.00% 

### ENERAC



## 700

700162

HANSEN


## 454

Analyzer Response

PASS?

YES 

# I

# A 

# elpaso

'1



# I General Information

Date 7-Dec-08
Company SNG

Station WRENS

Unit 

### 5



# Data Entry

Elapsed Time

(Minutes) 1 

### 2 

## 3 4 5 

## 6 7 

### B 9 

### 10 11 

## 12 13 14 

### 15 Analyzer 

### Response 

## 101 101 101 101 101 102 

## 102 101 101 101 101 102 102 102 101 

# I

I

Stab1J1ly Time**r'···-·<-····f:oo~'·-··-"**



### Stability Period Maximum Response

15 Minutes 

### 102.00 Minimum Response



### 101.00 Calculated Deviation



## 0.99% 

# co Stability .Check 

# Post-Catalyst

Manufacturer

Model Number

Serial Number Analyst Span Gas Cone.

Elapsed Time

(Minutes) 

### 16 17 18 19 20 

## 21 22 

## 23 24 25 26 27 28 29 

## 30

Allowable Deviation



## 1.000/0 ENERAC

700

700161
HANSEN

100.9

Analyzer Response

PASS?



### YES

# elpaso
I General Information 

# I

Dater 7 -Dec-OB
Company

__ .**.;..;S;:;.;.N.;.;;G~**

### __ Station

_____**WR;.;;.;.;.E;;;;N~S~**

### ____ 

### Unit 5 

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

# I Pretest 

# I

Gas Concentration NO Response
NO Span 

### 208 209 N02Span 

### 196 CO Zero 

### 0.00 CO Span 

### 454.00 O:zZero 

### 0.00 O2 

### Span 

### 20.90

Gas Concentration 

### Analyzer Response CO Zero 

### 0.00 1.00 CO Span 

### 454.00 453.00 O2 

### Zero 

### 0.00 0.00 OlSpan 

### 20.90 20.90



## r-po;t Test: Run 3 Drift 

# I

Gas Concentration 

### Analyzer Response COlero 

### 0.00 2.00 

# co Span 

### 454.00 455;00 OlZero {).OO 

### 0.00 OzSpan 

### 20.90 21.00 

# I' Interferance Check 

# I Calibration Error Pre-Catalyst 

# I Analyzer Information 

# I

Manufacturer ENERAC



### Model Number 700

Serial Number 700162
Analyst HANSEN

N02 Response CO Response 

## 02 Response


### 1 195 

### 0 1 453 

# I 0 

### 20.9

Absolute Pfjrcent 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 

### 2.00 0.44% 3.00% 1.00 0.22% 5.00% 0.00 0.00 0.30 0.10 0.10 0.50

CO Interferance

_________**-=O.:.:.0:.:.9·.:.:~** 

### __________ 

## PASS Allowable PASS? 

## YES YES YES YES

PASS?



## YES YES YES YES

5.00%

# elpaso
I General Information 

# I

Date 

### _---.;.7..,.;-Oe;..;;,.;..1>.,,;.08,;;..·

__ Company

_____**.....;S=.;.N.;..;;G~**

### __**Station_.......;W;.;.·;..;.RE;;;.;N..:..;S~_**



# r Pretest 

# I

Gas Concentration NO ResponSe
NO Span 

### 208 

# I 208 N02Span 

### 196 COlero 

### 0.00 CO Span**100~90** 

### ozZero 

### 0.00 OzSpan 

### 20.90

Gas Concentration Analyzer, Response COlero 

### 0.00 

### "J.OO 

# co Span 

### 100.90 101.00 Ozlero 

### 0.00 0.10 ·OzSpan 

### 20.90 21.00 

# r**':'~- ~**  -,. -,- 

# I Post Test: Run 3 Drift

Gas Concentration Analyzer Response COlero 

### 0.00 1.00 

## co Span 

### 100.90 102.00 OJlero 

### 0.00 0.10 OzSpan 

### 20.90 21.00 

# Calibration Error 

# Post-Catalyst

Manufacturer 

### ENERAC

Model Number

# ---""-----

Serial Number 

### 700161 ----.,..;...;...;;..;.;;..;;.-- 

### Analyst_---..

.........;;;,;;;;.;.

__ _

N02 Response CO Response 02 Response


### 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 a.10 0.30 ' 0.10 0.10 a.50

Absolute Percent Allowable Difference Difference ' Difference 

### 1.00 0.99% 

### 3.00% 1.10 1.09% 5

.. 00% 0.10 0.10 0.30 0.10 0.10 0.50



# I"

-.**-I~~erferance** Check 

# I

co Int8rferance

### --------~~--------- PASS , • Allowable PASS? YES YES

. YES

YES

PASS?

YES YES YES YES



### 5.00%i 

# A

. 

# elpaso

Geaet-allnformatioo 

## Dalel 4·Qec..06

. CotnpanJ lING



# ......

UIIiI IS

Data Entry

Lodtloft 

# - COfppmJ

lD:2S:IXI 

# I 43500 lD:2II:IXI 435.00 11.nc..r_ tC:27:1X1 436.00



# - ID:2II:OO 435.00 

### "- 435.110**.~A_** 435.47 

# - '.03% AIIowIIblIo UOIO
,0;JIi:IXI 

# I 437.00 IO:4O:IXI 436.00 lD:41:1X1 43500 10:42:1X1 437.00.



# A_
438.110 3-Rain

__ 435.47 v...- 0.31% 

# - 11'-
H:II5:IXI


### J 435.00 11:111:00 434.00 lU%oflltaoil l1:l11:1X1 43300 f1:011:1X1 433.00 

# - 

# -- 434.00 3-RAII1

__ 435.47 

# - 0.34% 

# - t.DD!O

lNSTIlUcrUONS 

## Pretest Stratification Determination

Pre-Catalvst**~**__ ..:ECOII=::....;._**~N~**__**~~~**__ _

. _""-"-..-,20=1536=-_

lUll 11.40 11<10 11.40 11.36 11.110 8.53% II.DD!O

11.40 11.30 11.20 11.30 11.32 11.30 US% 6,00%

lUO 11.20 11.30 11.30 1'22 11.311 .0.71%

5'- 

# A 

# elpaso

Generallnfonnatioa

unl

__ .::IS_-,-

Data Entry

lI.$.3%ofl_

tMa_ TIma

11:22:1X1 

# I

11:23:1X1 11:24:1X1 11:25:00

A_ 3-RunA-.ge Vlllance Allowable

10:39:1X1 

# I

'0.:40;00. lD:41:1X1 10:42:00

A_ge

..

Run

......... 

# -**~**

UM:IXI 

# I

l1:Ofl:DO .' U:lI7:QO l1:DO:fIO

A

..,. "",,-nogo 

# v_ AIIowIbIa CO (ppm)

17.00 1700 17.00 17.00 17.00 17.13 1.04% B.DD!O

17.00 1600 Ie 00 1600 17.BO 17.13 Ul2% 5,00% 

## Pretest Stratification Determination

Post-Catalvst

11.20 1100 1120 1110 11.18 lUB 0.11% UO'll.

11.2U 11,30 11.20 1120 11.22 11.18 0.36% 6.00% Analyzer Information 

# I

Iotodel Number A • _I Numb« 11953 OCVNX

·P-'_hIIIIoric:aI

____ -. ..._of-.and priorto ldartlllll tho_

.... INn,

# ._1Ion
_oltho """USlllack mUll be complotold. Data multbe collected II

__",1I.1'lIo,1O'lIo,_U.3%.rtho_ldla_

...__Iho

___ .blllo

...dollCllvaryllrD1OntlhanB'!C.. To-""",lIalllhlo,lnlll'ltholotllprollll Intolho••""uol IlIUm II Ihe flrsl

__poInt_nd_tor

..._1

......-(&1

___1ha

____ d onlhe Cal Em>rtabj. Cohct_ (CO, NO. Noz, lIId 021'01" parlod of I minutes ,lid record on IhIa rorm. RoIpHl 1ha

_ ._torlhe

___ poInls

..... ___ In I'!C..Ihen

__"'"CII1I be

.. "",led

# "'.1Iingle

_ point • not.

.. ch lasl !\1ft mull be

.. "",led Itilia 1h

... 1nI

...... points

.. told above.

### U 

### General Information I 

# Datel 8-Dec-08
Comparw SNG

station WRENS

Unit 5



### Data Entry 

# I

nma 

## co (ppm, 

### I 11:56:00 273 "11:57:00 273

11:58:00 278 11:59:00 272 12:00:00 275 12:01:00 268 12:02:00 280 12:03:00 277 12:04:00 280 12:05:00 285 12:06:00 279 12:07:00 278 12:08:00 276 12:09:00 265 12:10:00 264 12:11:00 278 12:12:00 279 12:13:00 278 12:14:00 282 12:15:00 276 12:16:00

. 279 12:17:00 278 12:18:00 283 12:19:00 275 12:20:00 274 12:21:00 282 12:22:00 275 12:23:00 273 12:24:00 275 12:25:00 279 12:26:00 283

GIaCone. O,(%} 13.3 13.3 13.2 13.3 13.2 13.2 13.2 13.1 13.1 13.2 13.1 13 12.9 13.2 13.2 13.1 13.1 13 13.2 13.1 13 13.1 13.2 13.2 13.3 13.3 13.3 13.3 13.3 13.3 13.3

Analyzer Response 

## co Zero 0.00 

# r 1.00 CO Span 454.00 

# I 457.00 

### OzZsro 0.00 0.00 Oz8pan 20.90 21.10 NO (ppm, 55.2 51.5 50.1 58.8 51 49.2 49 57.4 61.6 51.5 65.9 82.2 56 58.2

. 55.6 64.5 56 57.6 59.8 60.3 55.5 SO.4 54.3 58.6 51.7 53 59.3 55.8 51 51.9 56.1



### Absolute Difference 1.00 3.00 0.00 0.20 

# I

Analyzer acapoll8e

NOz,ppm) 0.3 0.5 0.8 1.1 0.9 0.8 1.3 1.6 1.8 1.3 2.4 1.9 2.1 2 1.8 2.1 2.3 2.4 3 2.7 2.1 2.4 2 2.1 2.6 2.8 3.5 3.1 3.4 2.9 2.5

Percent Difference

0.22% 0.66% 0.00 0.20 Time 12:27:00 12:26:00 12:29:00 12:30:00 12:31:00 12:32:00 12:33:00 12:.34:00 12:35:00 12:36:00 12:37:00 12:38:00 12:39:00 12:40:00 12:41:00 12:42:00 12:43:00 12:44:00 12:45:00 12:46:00 12:47:00 12:48:00 12:49:00 12:&0:00 12:51:00 12:52:00 12:53:00 12:54:00 12:55:00 12:56:00 12:57:00

Average Minimum Maximum 

### StdDev

AlloWable Difference

3.00% 5.00% 0.30 0:50 

# RunIA Pre-Catalyst

Analyzer Information

Manufacturer

Model Number
Serial Number
Analyst

CO (ppm, 278 284 282 289 281 287 294 284 283 282 293 285 286 290 293 283 287 274 293 285 287 289 290 288 291 293 293 288 291 293 291



### 282.58 268.00 

### 294.00



### U8

PASS?



### YES 

### YES YES YES ENEAAC

700

700162

HANSEN

0.(%)

13.1 13.1 13.2 13.2 13.1 13.1 13.1 13.1 13.1 13.1 13 13 13 13.1 13.1 13.1 13 13.1 13.1 13 13 13.1 13.1 12.9 13 12.8 12.9 12.8 12.8 12.9 13



### 13.11 12.80 

### 13.30 0.13

GeaCheck



### PASS 

# I

NO(ppm) NO, (ppm)

56.8 54.6 48.8 52.9 61.4 52 53.8 61.2 58.8 53 51.3 56.9 57.2 49.5 52.9 61.1 58.6 51.9 53.2 56.7 54.3 49.1 59 60.6 55 53.9 55.3 61.1 60.2 54 60.3



### 55.75 48.80 

### 65.90 

### US 3.1 3.3 3.1 3.7 3.1 3.9 3.2 2.5 2.7 3.3 2.8 2.8 3.5 2.9

. 2.7 3.1 3.7 3.6 3.1 3.5 4 3.2 <4 3.5 3.4 3.1 3 3.1 4.3 3.3 3.1

2.65 

## o.so ·4.30 

### 0.91

# 6

.. 

# elpaso
I Generallnformation 

# I

Date 8-Dec-08



# I Company SNG
Stafio.n WRENS

Unit 5



### Data 

### Entry

nme 11:56:00 11:57:00 11:58:00 11:59:00 12;00:00 12:01:00 12;02:00 12;03:00 12:04:00 12:05:00 12:06:00 12;07:00 12:08;00 ·'2:09;00

12:10:00 12:11:00 12:12;00 12:13:00 12:14:00 12:15:00 12:18:00 12:17:00 12:18:00 12:,9:00 12:20:00 12:21:00 12:22:00 12:23:00 12:24:00 12:25;00 12:26:00 corpI'm, 15.91 15.9 15.63 15.16 15.03 14.94

15 15.79 15.59

15 15.29 14.53 14.81 14.99 15.17 15.23 14.67 14.71 15.22 15.46 15.43 14.87 15.0B 15.3 15.62 16.19 15.94 15.57 14.9 15.31 16.07 

# I

0,(%) 13.02 13.06 13.1 13.12 13.1 13.08 13.03 13.04 13.02 13.08 13.02

13 13 13.02 13.07 13.1 13.08 13.02 13.04 13.06 13.07 13.07 13.11 13.1 13.09 13.1 13.1 13.09 13.09 13.07 13.11 NOfppm} 58.03 58.15 55.09 56.25 57.09 56.3 57.34- 56.00 59.68 59.77 57.7 62.13 60.94 62.8 61.33 60.2 61.97 61.63 61.14 59.92 58.81 59.68 57.54 56.23 56.61 56.86 57.8 57.44 58.00



### , 58.36 56.58 

### Analyzer ltcspOl18e
NOa(ppm) 1.11 1.34 1.44 1.64 1.86 2.03 2.28 2.33 2.69 2.93 2.87 3.32 3.47 3.64 3.77 3.81 4.11 4.27 4.33 4.28 4.26 ·4036 4.32 4.22 4.25 4.37 4.55 4.6 4.75 4.74 4.55 Time 12:27:00 12:28:00 12:29:00 12:30:00 ·'2:31:00 12:32:00 12:33:00 12:34:00 12:35:00 12:36:00 12:37:00 12;38:00 12:39:00 12:40;00 12:41:00 12:42:00 12:43:00 12:44:00 12:45:00 12:48:00 12:47:00 12:48:00 12:49:00 12;60;00 12:61:00 12:62:00 12:53:00 12:54:00 12:55:00 12;56:00 12:57:00 

# RuulH Post-Catalyst 

# I Analyzer Information 

# I

Manufacturer ENERAC

ModeJ Number 700
SerlafNumber 700181 Analyst. HANSEN



## c°fppm) 

## o %**~(** 

### ) .' NO( ) 

# ° ( [ppm N , ppm 16.03 13.1 56.49 4.47 15.93 13.14 54.69 4.36 15.84 13.12 57.31 4.58 16.56 13.12 54.8 4.42 16.49 13.1 54.64 4.46 16.29 13.1 57.77 4.65 16.11 13.01 58.22 4.63 16.89 13.04 67.12 4.52 16.04 13.07 57.31 4.64 16.03 13.05 58.67 4.84 16.9 13.07 57.28 4.81 17 13.06 55.91 4.69 16.79 13.03 57.01 4.8 16.77 13.05 57.79 4.93

17 13.07 56.17 4.76 18.51 13.11 56.08 4.74 16.47 13.11 55.44 4.79 16.9 13.06 58.05 4.99 17.06 13.09 56.96 5.01 17.46 13.05 55.8 4.84 16.74 13.04 59.75 5.21 16.8 13.04 57.42 5.04

, 16.49 13.05 60.72 5.27 16.34 13.01 5.24 16.63 12.94 59.18 5.11 16.46 12.95 59.41 5.23 16.87 12.99 58.71 5.21 17.14 13 58.17 5.13 16.82 12.99 61.42 5.41 16.25 13.01 60.14 5.39 16.67 13.02 60.2 5.31

..

# A, 

# elpaso
I General Information 

# I

Oatel 8-0ec-08
Company SNG

Station WRENS

Unit 5 

# I DataEn!2 

# I

TIme CO (ppm) 

### I 13:47:00 315 13:48;00 306 13:49:00 309 13:50:00 302 13:51:00 317 13:52:00 310 13:53:00 308 13:54:00 308 13:55:00 315 13:56:00 311 13:57:00 311 13:58:00 312 13:59:00 314 14:00:00 307 14:01:00 317 14:02:00 319 14:03:00. 310 14:04:00 305 14:05:0.0 312 14:06:00 319 14:07:00 314 14:08:00 311

. 14:09:00 308

14:10:00 318 14:11:00 310 14:12:00 310 14:13:00 314 

## . 14:14:00 321 14:15:00 311 14:16;00 311 14:17:00 315



# I Drift Check: 0Etional 

# I

GasConc. Analyzer

### ~onse"_C COlero 0.00 2.00 

# co Span 454.00 

## J 455.00 

### OzZero 0.00 0.00 O2 Span 20.90 ! 21.00 

# Run2A Pre-Catalyst 

# I Analyzer Information

Manufacturer ENERAC

Model Number 700

Serial Number 700162 Analyst HANSEN



### Analyzet.Response

O2 (%)

12.5 12.5 12.5 12.5 12.5 12.5 12.5 12.5 12.5 12.4 12.4 12.4 12.5 12.5 12.4 12.4 12.4 12.4 12.3 12.5 12.5 12.4 12.4 12.4 12.4 12.4 12.4 12.4 12.3 12.3 12.4

..



### AbsolUte Difference 2.00 1.00 0.00 0.10 

### Time 14:18:00 14:19:00 14:20:00 14:21:00 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;44:00 14:45:00 14:46:00 14:47:00 14:48:00


### Average



### . Minimum Maximum StdDev

Percent Difference

0.44% 0.22%

0.00 0.10**CO~m)** 317 309 308 320 310 312 314 318 309 309 314 315 308 312 314 318 310 311 315 320 312 310 317 317 308 310 316 315 309 314 317



### 312.55 302.00 321.00

4.12



### Allowable Difference

3.oooAl 5.00% 0.30 0.50 

# I

O 2 (%) 12.5 12.5 12.4 12.5 12.5 12.4 12.4 12.5 12.4 12.4 12.4 12.4 12.2 12.2 12.3 12.3 12.3 12.3 12.2 12.3 12.2 12.2 12.3 12.4 12.3 12.3 12.3 12.2 12.3 12.4 12.3



### 12.39 12.20 12.50 0.09

.PASS?

YES YES YES YES 

## Gas Check

PASS

PASS

# I General Information 

# I·.

Date 8-Dec-08


### CQmpany SNG

Station

## _..;;.:;.;;.;.;;;;=-..,.... Unit

___ 5;.......o

__



## Data En

Time 13:47:00 13:48;00 13:49:00 13:50:00 13:51:00 13:52:00 13:53:00 13:54:00 13:55:00 13:56:00 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 

# co (ppm) 15.75 15.7 15.4 15.3 15.34 15.29 15.3 15.28 15.31 15.3 15 14.8 14.85 14.77 14.83 14.84 14.81 14.76 14.8 14.8 14.79 14.8 14.82 14.84 14.83 14.84 14.86 14.9 14.87 14.85 14.86



# I Drift Check: Optional 

# I

CO Zero CO Span 

### O

2 Zero 

### OzSpan Gas Cone.
0.00 100.90 0.00 20.90 Al'!alyxer 

### Resnonse ',,'**r-~-** 

## I 1.00 

# I 102.00 0.00 21.00 

# Run2B Post-Catalyst

Manufacturer ENERAC

Model Number 700
Serial Number 700161 --.""';"';;';;"';"'-'---**Ana1yst_....;HA;..;;.;.;N.;,.:S:;.;:E:.;;N~_**



### Ana1y:r:er Response



### O

2 (%) 12.42 12.41 12.39 12.4 12.44 12.45 12.43 12.46 12.45 12.4 12.39 12.4 12.38 12.46 12.41 12.39 12.37 12.37 12.35 12.4 12.41 12.38 12.42 12.4 12.39 12.36 12.39 12.37 12.33 12.3 12.3

Absolute Diffenmce 1.00 1.10 0.00 0,10 . 

### Time 14:18:00 14:19:00 14:20:00 14:21:00 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 14:44:00 14;46:00 14:46:00 14:47:00 14:48:00 

### Average Minimum



### . MaXim1llJi StdDev

Percent Difference

0.99% 1.09% 0.00 0.10 CO (ppm) 14.98 14.99

15 15.03 15.05 15.1 15.09 15.1 15.08 15.11 15.07 15.03 15.03 15.04 15.03 15.02

15 14.97 14.99 15.06 16.1 16.11 15.12 15.14 15.16 15.13 15.1 15.07 15.04 15.06

15



### 15.04 14.76 15.7S 0.21

Allowable Difference

3.00% 5.00% 0.30 0.50 O 2 (%) 12.39 12.41 12.42 12.44 12.46 12.44 12.38 12.42 12.4 12.39 12.39 12.37 12.34 12.35 12.31 12.32 12.3 12.31

1.3 12.29 12.28 12.28 12.29 12.31 12.31 12.3 12.29 12.26 12.29 12.32 12.3



### 0.19 1.30 

### 0.46 1.41



### YES YES PASS YES YES PASS

# • elpaso
I General Information 

# I

catel 8-Dec-08
Company 

### SNG

Station WRENS



### Unit 5 

# I**Dat~** 

## Entry 

# I

TIme CO (ppm) 

### 1 15:35:00 285 15:36:00 283 15:37;00 278 15:38:00 283 15:39:00 290 15:40:00 288 15:41:00 279 15:42:00 284 15:43:00 285 15:44:00 287 15:45:00 282 15:46:00 281 15:47:00 286 15:48:00 289 15:49:00 276 15:50:00 283 15:51:00 282 15:52:00 290 15;53:00 28S 15:54:00 278 15:55:00 261 15:56:00 292 15:57:00 26a 15:58:00 285 15:59:00 288 16:00:00 299 1.6:01:00 296 16:02:00 292 16:03:00 295 16:04:00 306 16:05:00 304



# I Drift Check:

# Re~uired 

# I

Gas Cone. Analyzer Response 

### COlero 0.00**r--~·-·**

. 2.00 caSpln 454.00 , 455.00 

### 02 lero 0.00 I 0.00 OzSpan 20.90 

# I 21.00 

# Run3A Pre-Catalyst 

# I Analyzer Information 

# I

Manufacturer ENERAC



### Model Number 700


### SertalNumber 700162
Analyst HANSEN**~erRe8poDBe ~(%,**  12.2 12.2 12.2 12.2 12.2 12.2 12.2 12.1 12.2 12.3 12.3 12.2 12.2 12.3 12.2 12.2 12.3 12.3 12.3 12.2 12.2 12.2 12.3 12.1 12.2 12.3 12.3 12.3 12.3 12.3 12.3

Absolute Difference 2.00 1.00 0.00 0.10 

### Time 16:06:00 16:07:00 16:08:00 16:09:00 16:10:00 16:11:00**1~:12:00** 16:13:00 16:14:00 16:15:00 16:16:00 16:17:00 16:18:00 16:19:00 16:20:00 16:21:00 16:22:00 16:23:00 16:24:00 16:25:00 15:26:00 16:27:00 16:28:00 16:29:00 16:30:00 16:31:00 16:32:00 16:33:00 16:34:00 16:3S:oo 16:36;00 

### Average Minim

. um Maximum

·Std Dev'

Percent Difference

0.44% 0.22%

0.00 0.10 

### CO (ppm) 298 302 309 307 302 302 312 310 304 312 314 314 300 311 307 317 307 312 311 319 306 313 316 318 305 314 317 305 314 315 318


### 298.56 216.00 319.00 

### 13.26

Allowable l)lfference

3.00% 5.00% 0.30 .0.50**.~(%)** 12.3 12.3 12.2 12.2 12.2 12.3 12.3 12.3 12.3 12.3 12.3 12.3 12.2 12.2 12.2 12.3 12.3 12.1 12.2 12.2 12.2 12.1 12.3 12.4 12.2 12.2 12.3 12.2 12.1 12.2 12.2



### 12.24 12.10 12.40 

### 0.07

PASS? Gla Check 

### YES YES PASS 

### YES YES PASS

# etpaso

I



# I General Information

Date

. 8·Dec-08
Company SNG

Station WRENS

Unit 5

### DataEn~

Time 15:35:00 15:36:00

. 15:37:00 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 

# I



# I

CO (ppm) 14.62 14.6 14.55 14.56 14.61 14.6 14.62 14.65 14.64 14,65 14,65 14.65 14.65 14.68 14.65 14.69 14.68 14.8 14.81 14,8 14.8 14.82 14.83 14.82 14,8 14.95 14,99

15 15,2 15 15,1



# I Drift Check: Required 

# I

CO Zero 

## co Span 

### O2 

### Zero O:z.Span GasConc.
0.00 100.90 0.00 20.90 Analyzer. Response 

# r 1,00 

# I 102.00 

# I 0.10 .21.00 

# Run3B Post-Catalyst 

# I Analyzer Information

Manufacturer ENERAC

Model Number 700

Serial Number 700161 Analyst HANSEN



### Arudyzer Response

O2 (%) 12,19 12.18 12.16 12.17 12.15 12.18 12,19 12.18 12,18 12.19 12.17 12.18 12.17 12.16 12.17 12,14 12.19 12,2 12.14 12,17 12.12 12.1 12.09 12.11 12.13 12.16 12.2 12.22 12.19 12,17 12,16

Absolute Difference 1,00 1.10. 0.10 0;10 Time 16:06:00 16:07:00 16:08;00· 16:09:00 16:10:00 16:11:00 16:12:00 16:13:00 16:14:00 16:15:00. 16:16:00 16:17:00 16:18:00 '16:19:00

16:20:00 16:21:00 16:22:00 16:23:00 16:24:00 16:25:00 16:26:00 16:27:00 16:28:00 16:29:00 16:30:00 16:31:00 16:32:00 16:33:00 16:34:00 16:35:00**1~:36:00** 

### Average 

### Minimum Maximum 

### StdDev

Pe,..ent Differencct .0.99%

1.09% 0.10 0.10 

### CO (ppm) 15.09 15.16 15.17 15.15 15.16 15.18 15.23 15.19 15,18 14.96 15.08 15.12 15.14 15.16 15.16 15.1 15.13 15.15 15.16 15,19 15,18 15,16 15.13 15,09 15.12 15.1 15.16 15.17 15.21 15.2 15,21



### 14.95 14.55 

### 15.23 0.23

AIIQwable Difference

3.00% 5.00% 0.30 0:50 

# I

O 2 (%) 12.21 12,23 12.18 12,14 12.16 12.15 12.17 12.19 12,2 12.18 12.22 12.2 12.2 12.17 12,14 12.6 12,13 12.08 12,11 12.1 12,12 12.14 12.18 12.13 12.11 12.15 12.2 12.19 12.21 12.22 12.2



### 12.17 12.08 12.60 0.07

PASS? Gas Check 

### YES YES PASS YES YES PASS

# A 

# elpaso Data Summary


# I Generallnrormation 

# I 

# I Unit Information 

# I



# I Start bate H)ec-08 Unit No.

___ .-,;5=-_-,-_
Company SNG Manmadurer

__**-=CA~T~E=R~P~IL=LA~R** 

### __ _ Station WRENS MOdel

__ ..::G:.;;-3::::6:.:.1::;2-::.LE=-

__ _

Serial Number



# -------- Pre-Control Post-Control Manufacturer ENERAC ENERAC Rated BHP 3530

Mode! 700 700 

### RatadRPM

______**~=-** 

## __**~_** Sertal Number 700162 700161 Rated BSFC

__**...--!=~**__ Analyst HANSEN



### Test Data

Run Pate Time 

# I

General 

### nata 123 12nU08 12nU08 12nUOS 11:1515 AM 1:"7 PM 3:315 PM
Ambient Temperatura 

### t'F}

# r~-·"· Barometric pressura ("/ig)**s3.cio--~~-----' '~** 
AmblentRe,la,live,' Hum,(dlty,(%) 78.00 71.00 7000 CatalyllttnJetT 

### (IF) 789.00 787.00 797.00

CaIaIylltAP("H:zO) 318 3.23 3.07 

### Hol'18power

# r·""--34s6.00-~--**Ope:~~ta.**__ ,--3284:00--'-- Speed 1001.00 1001.00 1003,00 % Load • 97.90% 98.67% 93.03% % TOlqLIII 97.81% 98.57% 82.75%

# ~:~**!--~-- ~~~::--.-~-"~-** **1~1~:0 "---~-~--~~8:0** **"-"-~**
Sud. Prailil. (psIg) 828.00 821.00 894.00

Suet. Temp. 

### (IF) 63.00 64.00 64.00 Disc. Press. (psig) 

# I 1100.00 110300 1068.00

Disc. Temp. 

### fF} 

## I 104.00 107.00 89.00

Fuel Pressura (paig) Fuel, OIfferenllal**("H~)** Fuel Temperatura fF} PRESS TAP?,(1-lJP.2-0N) Pipe 10 (In.) Orriflce IO(!n.) Fuel Use

- Panel (lIdh) Fuel Use

- Calculaled (scIh)

%Oz

% 0, Coneetac:l

" 

### CO

CO Corrected

CO 

### 0 115% 02
CO Reduction CO Reduction PASS? 

### Fuel Data 

# r----·-- ,:........-

# ......

# ----- 

# I

I 

# I i 26030.00 24700.00 2566000

1A IB 2B 3A 38 EmissioDS 

### Data

13.11 13.08 IUS 12.f9 12.24 ", 12.17

13.08 12.. 12.16 12.09 12.21 12.G7

,,' 282.158 16.15 S12.115 1LD4 298.68 lUI**1"~82.0t** 115.G0**~12.G8** 14.09 298.06 14.01

212.'" 11.11 2115.54 .8.44 IOU1 8.38
84.76% 815.112% 15.37%' 83.00% 83.00% 83.00%

YES YES YES Average

.1.33

73.00 781.00 US

3407.67 1001.67 86.113% 8U7%

1 44.10 17a.oO 847.67 63.87 109D.S3 100.00

26470.00

12.6& 12.47 '12.115 12.17 297.80 ,115.31 297.38 

# "'.17 210.16 8.8& 86.25% 83.00%

YES NOTE. Ifthis Is an Initial test or a post-c:atalyst change test, IIlen communicate new catalyst differential pralllSura average to Automation personnel so that control system can be update with 

### new baseline. 1%**~** 

### % % 

### PI (Pte)

(Post) (Pre) (Post) pm (Pte) pm (post)

m (Pre) m (Post) pi) 

### l:1li 101

pm

# .'6% 02 (pte) 

# ppm. '15% 02 (Post) 

### 1"4 1"4 C.lculated

RequIred

### GAS COMPOSITION Constituent M wei hted MW

NITROGEN 

### 0.4060 28.0134 11.3734 CARBON DIOX. 

### 0.9267 44.01 40.7841 METHANE 

### 95.9931 16.04315 1540.0317

ETHANE 

### 2.1375 30.0703 64.2753 PROPANE 

### 0.2948 44.0975 12.9999 I·BUTANE 

### 0.0628 58.1246 3.6502 N-BUTANE 

### 0.0690 58.1246 4.0106 I-PENTANE 

### 0.0276 72.1518 1.9914 N-PENTANE 

### 0.0178 72.1518 1.2843

HEXANE + 

### 0.0645 95.958 6.1893 99.9998 MW 

### 1686.5902
Upper Dry Heat Value btu/dscf Mole Weight

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

### -2.8359 Density 

### 4.4789 Ib/scf



### C+H/4 

### 202.8415

Total Carbons 102.3387 

### Total H 

### 402.0113

Constituent 

# I LHVideal 

## H LHV(il ideal 

### H LHV{i} real 

# I

NITROGEN 

### 0.00 0.00 CARBON OIOX. 

### 0.00 

## 0.00 METHANE 

### 913 87641.70 -4269.85

ETHANE 

### 1624 3471.30 -169.12 PROPANE ... 

### 2322 684.53 -33.35 I-BUTANE 

### 3010 189.03 -9.21 N-BUTANE 

### 3020 208.38 -10.15 I-PENTANE 

### 3711 102.42 -4.99 N-PENTANE 

### 3718 66.18 -3.22

HEXANE 

### + 

### 4904 316.31**~15.41** 

### LHVreal 

### -451531 Constituent 

## SG 

# HiiAf b

NITROGEN

.. 

### 0.96723 0.0044 CARBON DIOX

.. 

### 1.51955 1.408166985 0.0197 METHANE 

### 0.55392 53.17249795 0.0116

ETHANE 

### 1.03824 2.219238 0.0239 PROPANE 

### 1.52256 0.448850688 0.0344 f-BUTANE 

### 2.00684 0.126029552 0.0458 N·BUTANE 

### 2.00684 0.13847196 0.0478 I-PENTANE 

### 2.49115 0.06875574 0.0581 N-PENTANE 

### 2.49115 0.04434247 0.0631 HEXANE 

### + 3.3127 0.21366915 0.0802 SGreal 

### -2. 1049; 

# .

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 seth) Fuel Flow scfm) #VALUEI #VALUEI #VALUEI PIPE 1.0. 

### 0.00 0.00 0.00 ORIFICE 1.0. 

### 0.00 0.00 0.00 PRESS TAP? (1-UP 2-DNl 

### 0.00 0.00 0.00 SP. GRAVITY -2.84 -2.84 

### -2.84 BETA #DIVIOI #OIViOI #DIV/OI 

### K #DIV/OI #DIVlO! #DIVIOI 

### K1 #DIVIot #0IV/O! #0IV/O! Bc #DIVIOI #DIV/O! #DIVlO! E

.. 

### #DIV/OI #DIV/OI #DIVlO! kflang #DIVIOI #DtVlOI #DIVIOI 

### Ko #DIVlO! #DIVlO! #DIV/O! Fb #DIVlO! #DIVIOI #DIV/OI BB #DIVlO! #DIV/O! #DIV/O! Fr #DIVlO! #DIVIOI #DIVIOI Fpb 

### 1.00 1.00 1.00 Ftb 

### 1.00 1.00 1.00 Ftf 

### 1.06 1.06 1.06 FG #NUM! #NUMI #NUM! Fpv 

### 1.00 1.00 1.00 R #DIV/OI #DIV/OI #DIV/O! QY #DIV/Of #DIVIOI #DIV/OI C #DIV/O! #DIV/O! #DIVIOI Qth Qfm #VALUEI #VALUE! #VALUEI K1 for BETA 

### < 

### 0.5 #DIVlO! #DIVIOI #DIVIOI K1 for BETA> 

### 0.7 #DIVlO! #DIV/O! #DIV/O! QY (DOWNSTREAM TAP) #DIVIOI #DIVIOI #DIV/O! Atm. Press for calcs (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. 

### %: 0.735410 Hydrogen 

# wt. %: 0.240264

Oxygen 

## Wt. %: 0.017582 Nitrogen 

### Wt. 

### %: 0.006743 1.0000

1686.5902 btu/dscf**--"';'#~V~A~L~U~E';"'I**

### --dscfIMMbtu

HHVideal



### 1010 1769.6 2516.1 3251.9 3262.3 4000.9 4008.9

5278

b(i) 

### 0.0017864 0.01825599 1.11351996 0.05108625 0.01014112 0.00287624 0.0032982 0.00160356 0.00112318 0.0051729 1.2088638 HHV(i) ideal 

### 0 0 96953.031

3782.52 741.74628 204.21932 225.0987 110.42484 71.35842 340.431 HHV real



### Compressibility 

### -20.52571035 HHV(i) real 

### 0 0 -4723.49 -164.28 -36.14 -9.95 -10.97· -5.38 -3.48 -16.59 -4990.27

# ·

.

### 2 glbhp-hr Ib/hr ppm 2 Calculated Panel Heat Rate Curve

# A 

# elpaso Continuous Monitoring System Performance Evaluation Worksheet forNESHAP Compliance


# General Inforamtion



# I

I IGeneral Information 

# I**Date[-~----'-~~ 'CompanYr--SNG--~'** 


### Stationl"WRENS"-


## Analyzer Information

. ,**~-.I'!_':-,.w**__""--"'-.
_.

_ 

### Manufacturer,**MOdef~** 

### ••**-~--** 

### .•**~-.**


### Serial**Numberr~-----­ Analyst!~~""·**  

### - ._ •. ,



## Test Data
Elapsed Time ActualTlme

...**E.!!f!1--.,~held** 

### $oF) 0:01 

# I
0:02 

### 0:03 0:04 

### 0:05 0:06 

### 0;07 0:08 

### 0:09 0:10 0:11 

### 0)'12 

# I

I Unit Information

., r-"-

...... _-_.'-- 

### Manufacturerj CATERPILLAR**MOdelr---'--~-** 

# '" vel"$!on!

Rated

### BHpr--~~ Rated RPMr----""'1'O'OO---

.
Rated 

### BSFCi-

..... 

# sei"oo-**~** 

# . ,

Calculations 

# I

CMSAverage 

### 101 F Handheld 

### 101

. Average. F 

## Absolute Difference 

### °1 F Allowable Difference* 

### °1 

## F


## PASS?

0:13* Allowable difference is 

### 5% of 0:14 reading. 0:15 

### Average 15 min.

# elpaso

II General Information 

# I Datel

COmpany

__**...;.S.;....NG~_.;....**



### Station WRENS



# ------ Unit 5**--~---** 

# II Pre-Cat Analyzer Info 

# I

Manufacturer ENERAC

Model Number SO-Nov-01

Serial Number 700162
Analyst HANSEN 

# I Pre-Catalyst Analeer 

# I

Time CO Audit (ppm) 02 "lIdit (%) r-""'·""-

.. 'lI

...'-'

....... "'-

..**~'.\'_~-··--** ....'.jO<'

...**-------~-.**____ M' 

## I

Average Minimum Maximum StdDev 

# Performance Audit Analysis



# I

I

Audit Reference Numbe1r-----



### Date Received 

# I

Received 

### From 

# I

Post-Cat Ana1l:zer Info 

# I

Manufacturer ENERAC

Model Number 3()"Nov"()1

Serial Number 700161 

### Analyst HANSEN**Post-Cata~t Ana~zer**  

# I**r_!~me** 

# ..**~~ud!!Jee!!!L_9.t!'udit (~."'"**  i



### Average 

### Minimum Maximum StdDev

# elpaso Horsepower Prediction

Horsepower Determination



# BHP=[PsLANT 

# 2LIR: 1

# ~l~J .••.I+R-),

# _R":J

..[.1+LF+ WF 1.·



# l+NF)+HPo-R 33000117-

# 1 

# "t

. 17Mech 

# J

. .


### Equation Coefficients 

# -,

Ideaf Horsepower Calculation Coefficients SHP 

# .. Brake horsepower Calculated L '"**Lenmhofcomp~ssorstroke(Ftl** Constant 

### A =**A~a** of**comp~sor** piston lin.2 } Constant N II Actualrevolution Derminute (RPM) Measured R

..**Comp~ssion** ratio of engine calculatedtrom tile equat/oo[ 

### R=Po/Ps ] Calcualted 

### Ps II Suction pressure (PSIA) 

### I PSIS 

### + 14.73

### J

.. Measured PD II Discharge pressure (pSIA) (PSIS 

### + 14.73 

### J Measured



### n 

# .. Polytropic exponent from tile equation of state relation [ P\I"

.. Constant (11::1.28) 

### 1 Constant

Unit SpecifCalculation Coeffictents I1MEcH 

# =Mechanicel effiCIency (0.95 for**recip~ting.** separable gas**comp~ssors)** Constant

WF 

# .. Waste factor calculated from tile relationship 

### I WF

.. K 1100{R·1) 1 Constant 

### NF 

# .. SDeed factor computed from curve coefficients Constant

K

.. Waste "K" factor entered from enaine curve coefficients Constant IF 

## '" Pulsation loading factor computed from curve .coefficients

.. Constant HPo-R 

### = Residual horsepower from deactivated**comp~ssor** cylinder end Constant m

.. Clearance volume measured as a fraction of piston displacement Constant 

# I**~easutetnent1>evises**
Value Device ; Accuracy

N Maanetic Pickup +/·0.5 RPM Ps**Pressu~** Transmitter +/. 0.1 

### % of full scale Po Pressure Transmitter +/. 0.1 % of full scale

# ... 

# ,,'



# .. 

# elpaso Horsepower Measurement

II Hot'Sepower Determination 

# I

BHP 

# =

# (~~O)(**q~J** I Equation Coefficients 

# I

'. 

### Horsepower Calculation Coefficients

BHP 

# = Brake horsepower Calculated 

### p 

# = Mean effective pres.ureofcompression 

### I expansion 

### strokes Measured L 

# = Length of compressor stroke (in.) Constant

.'. 

### A 

# = Area of compressor piston (In. 2) 

### Constant 

### N 

# = Actual reVolution 

## per minute (RPM)

.. 

### Measured 

### 396,000 

# =Constant Constant

Unit 

### Specif Calculation Coefficients 

### '1MECHI= IMechanical efficiency 

### (0.95 for reciprocating.seperable gas compressors) tConstant



## Measurement Devises

Value Device Accuracy 

### N Encoder +/-0.5 RPM Ps Engine analyzer +/-1.0 %01fuJI scale 

### Po Engine analyzer +/- 1.0 % of full Scale**.~"-** ....-

....**-.-.~.-** ..-.- ...- ..**~.~".--** ..-..-

..**-,-~.-.--,----,** ..- .•..**-----.--~---** _______...•.

__..__. ____**~_**...•**~_._._**..**~~ _~** ___**~_.--.J**