EPA-600/R-96-020b
GRI-95/0270.2
February 1996
Criteria Pollutant Emissions from
Internal Combustion Engines
in the
Natural Gas Industry
Volume II. Appendices
Gerald S. Workman Jr., Rachel G. Adams, and
Gunseli Sagun Shareef
Radian Corporation
P.O. Box 13000
Research Triangle Park, NC 27709
by:
EPA Contract No. 68-D2-0160
Work Assignment No. 33
GRI Contract No. 5091-254-2293
EPA Project Officer:
Charles C. Masser
Air Pollution Prevention and Control Division
U.S. Environmental Protection Agency
Research Triangle Park, NC 27711
GRI Project Manager:
James M. McCarthy
Environment and Safety Research
Gas Research Institute
Chicago, IL 60631
Prepared for:
Office of /dr Quality Planning and Standards
U.S. Environmental Protection Agency
Research Triangle Park, NC 27711
Office of Research and Development
U.S. Environmental Protection Agency
Washington, DC 20460
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TECHNICAL REPORT DATA ... .... ^ i..|. mitiBi iimiiii
(Piaae rtad Iiuavctions oh the mene before compl I III L. Ill 1 II 1 1 III 11II
1. REPORT NO. 2.
EPA-600/R-96-020b
/ PB96-168273
4. TITLE AND SUBTITLE
Criteria Pollutant Emissions from Internal Combus-
tion Engines in the Natural Gas Industry; Volume
II.. Appendices A - I
S. REPORT DATE
February 1996
6. PERFORMING ORGANIZATION CODE
7. AUTHOR(S)
Gerald S. Workman, Jr., Rachel G. Adams, and
Gunseli Sagun Shareef
B. PERFORMING ORGANIZATION REPORT NO.
275-114/298-130-33
B. PERFORMING ORGANIZATION NAME AND AOORESS
Radian Corporation
P. O. Box 13000
Research Triangle Park, NC 27709
10. PROGRAM ELEMENT NO.
11. c6NThACT/GRANT NO.
5091-274-2293 (GRI)
68-D2-0160T33 (EPA)
12. SPONSORING AGENCY NAME AND ADDRESS
EPA, Office of Research and Development*
Air Pollution Prevention and Control Division
Research Triangle Park, NC 27711
13. TYPE OF REPORT AND PERIOD COVERED
Final; 6/94 - 12/95
14. SPONSORING AGENCY CODE
EPA/600/13
is.supplementaryimotesepa project officer is C. C. Masser, Mail Drop 62, 919/541-7586.
(*)Consponsor is Gas Research Institute, 8600 West Bryn Mawr Ave., Chicago, IL
60631. GRI project manager is J. M. McCarthy. GRI report No. GRI-95/0270. 2.
16. abstractrj-^g rep0rt summarizes emission factors for criteria pollutants (NOx, CO,
CH4, C2H6, THC, NMHC, and NMEHC) from stationary internal combustion engines
and gas turbines used in the natural gas industry. The emission factors were calcu-
lated from test results from five test campaigns conducted as part of the Gas Re-
search Institute's air toxics study, three of which were cofunded by the EPA. Test
results for individual engines tested are presented, along with full load engine fam-
ily-specific emissions factors, and the calculated emission factors are evaluated re-
lative to the emission factors published in EPA report AP-42. Units tested included
eleven 2-stroke engines and five 4-stroke engines, with and without controls, and
two gas turbines.
17. KEY WORDS AND DOCUMENT ANALYSIS
a. DESCRIPTORS
b. IOENTIFIERS/OPEN ENDED TERMS
c. COSATI Field/Group
Air Pollution
Emission
Internal Combustion Engines
Gas Turbines
Natural Gas
Air Pollution Control
Stationary Sources
Emission Factors
13 B
14G
2 IK
13 G
21D
18. DISTRIBUTION STATEMENT
Release to Public
19. SECURITY CLASS {This Report)
Unclassified
21. NO. OF PAGES
451
20. SECURITY CLASS (This page)
Unclassified
22. PRICE
EPA Form 2220-1 (9-73)
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EPA Review Notice
This report has been peer and administratively reviewed by the U.S. Environmental
Protection Agency, and approved for publication. Mention of trade names or commercial
products does not constitute endorsement or recommendation for use.
This document is available to the public through the National Technical Information Service,
Springfield, Virginia 22161.
GRI Disclaimer
LEGAL NOTICE: This report was prepared by Radian Corporation as an
account of work sponsored by the Gas Research Institute (GRI). Neither GRI,
members of GRI, nor any person acting on behalf of either:
a. Makes any warranty or representation, express or implied, with
respect to the accuracy, completeness, or usefulness of the
information contained in this report, or that the use of any
apparatus, method, or process disclosed in this report may not
infringe privately owned rights; or
b. Assumes any liability with respect to the use of, or for damages
resulting from the use of, any information, apparatus, method,
or process disclosed in this report.
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Abstract
Tliis report contains emissions data for nitrogen oxides (NOJ, carbon monoxide
(CO), methane (CH4), ethane (QE^), nonmethane hydrocarbons (NMHC), and nonmethane-
ethane hy drocarbons (NMEHC) from stationary internal combustion (IC) engines and gas
turbines used in the natural gas industry. The emission factors were calculated from test
\ results based on five test campaigns conducted as part of the Gas Research Institute's air
' toxics study, three of which were cofunded by the EPA. Test results for individual engines
tested are presented, along with full load engine family-specific factors, and the calculated
emissions, factors are evaluated relative to the emission factors published in EPA report
AP-42. Units tested included eleven 2-stroke engines and five 4-stroke engines, with and
without controls, and two gas turbines. The data will enhance the current database in AP-42
for stationary IC engines. It will not only enlarge the population of engine types covered,
but will enhance the emission factor quality of several engine categories which have a limited
data set.
11
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FOREWORD
The U. S. Environmental Protection Agency is charged by Congress with pro-
tecting the Nation's land. air. and water resources. Under a mandate.of national
environmental laws, the Agency strives to formulate and implement actions lead-
ing to a compatible balance between human activities and the ability of natural
systems to support and nurture life. To meet this mandate. EPA's research
program is providing data and technical support for solving environmental pro-
blems today and building a science knowledge base necessary to manage our eco-
logical resources wisely, understand how pollutants affect our health, and pre-
vent or reduce environmental risks in the future.
The National Risk Management Research Laboratory is the Agency's center for
investigation of technological and management approaches for reducing risks
from threats to human health and the environment. The focus of the Laboratory's
research program is on methods for the prevention and control of pollution to air,
land, water, and subsurface resources; protection of water quality in public water
systems; remediation of contaminated sites and groundwater; and prevention and
control of indoor air pollution. The goal of this research effort is to catalyze
development and implementation of innovative, cost-effective environmental
technologies; develop scientific and engineering information needed by EPA to
support regulatory and policy decisions; and provide technical support and infor-
mation transfer to ensure effective implementation of environmental regulations
and strategies.
This publication has been produced as part of the Laboratory's strategic long-
term research plan. It is published and made available by EPA's Office of Re-
search and Development to assist the user community and to link researchers
with their clients.
E. Timothy Oppelt, Director
National Risk Management Research Laboratory
iii
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Contents
Volume I
Executive Summary iv
Figure xi
^Tables . .. xi
Acronyms and Abbreviations xiv
Section 1.0 Introduction 1-1
1.1 Background 1-1
1.2 Objectives and Approach 1-2
1.3 Report Contents 1-3
Section 2.0 Summary of Emission Factors 2-1
2.1 Engine Families 2-1
2.1.1 2-Stroke Engines 2-1
2.1.2 4-Stroke Engines 2-4
2.1.3 Gas Turbines 2-6
2.2 Full Load Emission Factors 2-6
2.2.1 Emission Factors 2-6
2.2.2 Test Engines/Turbines 2-9
2.2.3 Operating Data 2-10
2.3 Engine Family-Specific Emission Factors 2-10
Section 3.0 Test Results 3-1
3.1 Overview 3-1
3.2 Campaign 2 3-5
3.2.1 Site Description 3-5
3.2.2 Operating Conditions and Measurement of 02, COj, CO,
THC, and NO, 3-5
3.3 Campaign 3 3-6
3.3.1 Site Description 3-6
3.3.2 Operating Conditions and Measurement of O2, CO2, CO,
THC, and NOx 3-6
3.3.3 Measurement of Methane and Ethane Emissions 3-10
3.4 Campaign 4 3-14
3.4.1 Site Description 3-14
3.4.2 Operating Conditions and Measurement of 02, C02, CO,
THC, and NOx 3-14
iv
-------
Contents (continued)
3.4.3 Measurement of Methane and Ethane Emissions 3-23
3.5 Campaign 5 3-24
3.5.1 Site Description 3-24
3.5.2 Test Results 3-24
3.6 Campaign 6 3-26
3.6.1 Site Description 3-26
3.6.2 Engine Operating Conditions and Measurement of Oj,
COj, CO, THC, and N0X 3-26
3.6.3 Measurement of Methane and Ethane Emissions 3-33
Section 4.0 Sampling and Analytical Methods 4-1
4.1 Sampling Traverse Point Determination 4-3
4.2 Exhaust Gas Flow Rate 4-3
4.3 Exhaust Gas Molecular Weight 4-3
4.4 Exhaust Gas Moisture Content 4-4
4.5 Fuel Gas Composition and Heating Value 4-4
4.6 Exhaust Gas Composition 4-4
4.6.1 Sample Gas Extraction and Transfer 4-5
4.6.2 Calibration and Quality Control Standard Delivery 4-5
4.6.3 Measurement of 02, C02, CO, THC, and NO,
Concentrations 4-5
4.6.4 On-Site GC Analysis 4-6
Section 5.0 Quality Assurance/Quality Control and Documentation 5-1
5.1 Process Data Quality 5-1
5.2 Continuous Emission Monitors Data Quality 5-2
5.2.1 CEMS Calibration 5-2
5.2.2 CEMS Drift Checks 5-2
5.2.3 CEMS Bias Checks 5-3
5.2.4 CEMS Precision 5-4
5.2.5 Other CEMS QC 5-4
5.3 Manual Sampling Methods Data Quality 5-5
5.4 Method 18 Data Quality 5-5
Section 6.0 Evaluation and Comparison of Emission Factors 6-1
6.1 Uncontrolled Engines/Gas Turbines 6-1
6.2 Controlled Engines 6-3
6.3 Other 6-5
6.4 Conclusions 6-6
Section 7.0 References 7-1
v
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Contents (continued)
Figure
4-1 Measurement System Schematic 4-2
Tables
5-l Full Load Average Emission Factors vi
2-1 Engines Tested in Each Family 2-2
2-2 Summary of Emission Factors 2-7
2-3 Average Emission Factors 2-11
2-4 Emission Factor Range (g/hp-hr) 2-13
3-1 Engines Tested 3-2
3-2 Station 3A: Engine Operating Conditions and CEMS Results, Engine 102,
Gaoper-Bessemer LSV-16 3-8
3-3 Station 3A: Engine Operating Conditions and CEMS Results, Engine 101,
Cooper-Bessemer LSV-16 3-9
3-4 Sweet Gas Plant 3B: Engine Operating Conditions and CEMS Results,
Engine 4, Cooper-Bessemer GMWA-8 3-11
3-5 Sweet Gas Plant 3B: Engine Operating Conditions and CEMS Results,
Engine 2, Cooper-Bessemer GMV-10TF 3-12
3-6 Station 3A: GC Results 3-13
3-7 Sweet Gas Plant 3B: GC Results 3-13
3-8 Qimpaign 4: Operating Conditions and CEMS Results, Waukesha L7042GU
(Tests 1 and 2) 3-15
vi
\
\
-------
Tables (continued)
3-9 Campaign 4: Operating Conditions and CEMS Results, Waukesha L7042GU
(Test 3) 3-16
3-10 Campaign 4: Operating Conditions and CEMS Results, Engine 4,
Cooper-Bessemer GMVC-10C (Tests 7, 9, and H) 3-17
3-11 Campaign 4: Operating Conditions and CEMS Results, Engine 4,
Cooper-Bessemer GMVC-10C (Test 8) 3-18
3-12 Campaign 4: Operating Conditions and CEMS Results, Engine 8,
I-R KVS-412 (PCC) 3-19
3-13 Campaign 4: Operating Conditions and CEMS Results, Engine 9,
I-R KVS-412 (Tests 14 and 17) 3-20
3-14 Campaign 4: Operating Conditions and CEMS Results, Engine 9,
I-R KVS-412 (Tests 15 and 16) 3-21
3-15 Campaign 4: GC Results (Ethane) 3-23
3-16 Campaign 5: Operating Conditions and CEMS Results, Westinghouse 191 . . . 3-25
3-17 Station 6A: Operating Conditions and CEMS Results, Engine 10,
Clark BA-5 3-27
3-18 Station 6B: Operating Conditions and CEMS Results, Solar Taurus T-6502 . . 3-29
3-19 Station 6C: Operating Conditions and CEMS Results, Engine 15,
Cooper-Bessemer GMVC-10 3-30
3-20 Station 6C: Operating Conditions and CEMS Results, Engine 11,
Cooper-Bessemer GMVC-10 3-31
3-21 Station 6C: Operating Conditions and CEMS Results, Engine 9,
Cooper-Bessemer GMVA-10 3-32
3-22 Station 6C: Operating Conditions and CEMS Results, Engine 13,
Cooper-Bessemer GMWC-10 3-34
3-23 Campaign 6: GC Results 3-35
4-1 Target Parameters and Measurement Methods 4-1
vii
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Tables (continued)
6-1 Emission Factors for Uncontrolled Natural Gas Prime Movers:
Gsis Turbines and 2-Stroke Engines 6-2
6-2 Emission Factors for Uncontrolled Natural Gas Prime Movers:
4-Stroke Engines 6-2
6-3 Emission Factors for Controlled Natural Gas Prime Movers:
NSCR On 4-Stroke Rich-Burn Engines 6-4
6-4 Emission Factors for Controlled Natural Gas Prime Movers:
SCR On 4-Stroke Lean-Burn Engines 6-4
6-5 Emission Factors for Controlled Natural Gas Prime Movers:
"Clean Burn" On 2-Stroke Lean-Burn Engines 6-5
6-6 Emission Factors for Controlled Natural Gas Prime Movers:
"Pre-combustion Chamber (PCC)" On 4-Stroke Lean-Burn Engines 6-6
6-7 Emission Factors for Controlled Natural Gas Prime Movers:
"Clean Burn" and CO Catalyst On 2-Stroke Lean-Burn Engines 6-6
viii
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VOLUME n
Appending
A Sample Calculations A-l
B CEMS and Operation Data B-l
B. 1 Campaign 2 B-2
B.2 Campaign 3 B-3
B.3 Campaign 4 B-7
B.4 Campaign 5 B-16
B.5 Campaign 6 B-17
C CEMS Summary Data C-l
C.l Campaign 2 C-2
C.2 Campaign 3 C-3
C.3 Campaign 4 C-9
C.4 Campaign 5 C-17
C.5 Campaign 6 C-18
D GC Data D-l
D.l Campaign 3 D-2
D.2 Campaign 4 D-4
D.3 Campaign 5 D-5
D.4 Campaign 6 D-6
E GC Summary Data E-l
E.l Campaign 3 E-2
E.2 Campaign 4 E-3
E.3 Campaign 5 E-18
E.4 Campaign 6 E-19
F Raw Operating Data F-l
F. 1 Campaign 2 F-2
F.2 Campaign 3 F-9
F.3 Campaign 4 F-43
F.4 Campaign 5 F-82
F.5 Campaign 6 F-87
ix
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G Manual Measurement Data G-l
G.l Campaign 2 G-2
G.2 Campaign 3 G-4
G.3 Campaign 4 G-7
G.4 Campaign 5 G-13
G.5 Campaign 6 G-15
H Fuel Analysis Results H-l
H.l Campaign 2 H-2
H.2 Campaign 3 H-3
H.3 Campaign 4 H-14
H.4 Campaign 5 H-32
^ H.5 Campaign 6 H-36
I Quality Assurance and Quality Control (QA/QC) 1-1
I.1 Campaign 2 1-2
1.1T1 "CEMS Calibration Drift/Bias Summary 1-2
1.1.2 GC Calibration Data 1-4
1.2 Campaign 3 1-6
1.2.1 CEMS Calibration Drift/Bias Summary 1-6
1.2.2 GC Calibration Data 1-9
1.3 Campaign 4 1-10
1.3.1 CEMS Calibration Drift/Bias Summary 1-10
1.3.2 GC Calibration Data 1-13
1.4 Campaign 5 1-14
1.4.1 CEMS Calibration Drift/Bias Summary 1-14
1.4.2 GC Calibration Data 1-16
1.5 Campaign 6 1-17
1.5.1 CEMS Calibration Drift/Bias Summary 1-17
1.5.2 GC Calibration Data 1-20
x
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Contents (continued)
Volume II
Appendices
A Sample Calculations A-l
B CEMS and -Operation Data B-l
C CEMS Summary Data C-l
D GC Data D-l
E GC Summary Data E-l
F. Raw Operating Data F-l
G Manual Measurement Data G-l
H Fuel Analysis Results H-l
I Quality Assurance and Quality Control (QA/QC) 1-1
x
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Appendix A
Sample Calculations
\ This appendix includes sample calculations for load, heat input, heat rate, F(j factor,
Method 19 flow rate, wet and dry basis conversions, unit conversions, and fuel flow
calculations from an orifice meter.
Load .A-2
Heat Input A-2
Heat Rate A-2
F(j Factor A-3
Method 19 Flow Rate A-5
Unit Conversions A-5
Fuel Flow Calculations A-7
A-l
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Sample Calculations
Load
OP«"i°«HP x RMed T- x M0(*) - Load (*)
Rated HP Operating rpm
Heat Input
Fuel Flow
scf
min
x Heating Value of Fuel
Mx
scf J
'60 min
hr
MMBtu
106 Btu
= Heat Input
MMBtu
hr
Can be based on HHV or LHV
Heat Rate
Heat Input [Based on LHV]
MMBtu
hr
1
Operating HP
106 Btu
MMBtu
= Heat Rate
Btu
HP-hr
Based on LI IV
A-2
-------
F,j Factor Calculation
133
!^l(%wt. C)+3.64 (**
lb v ' |F
(%wt. H) + 0.14
scf
lb
| (%wL N) - 0.46 ^
| (%wt O)
HHV
x 385.5
scf lv 1
lb-mole "1 v
MMBtu
[scf
lb-mole J MWfuel
lb J
106 Btu
Fd
dscf @ 0% O,
MMBtu
Example Calculation of F,j Factor
Gas Analysis HHV = 1159 Btu/scf MW^ = 19.01 —-—
lb-mole
Mole %
x MW
= Weight per 100 moles
Weight %
n2
0.792
28
0.2218
1.169
C02
0.078
44
0.0343
0.1809
CH<
80.954
16
12.95
68.30
CjHe
16.423
30
4.927
25.99
C3Hg
1.479
44
0.6508
3.432
i-C4Hj0
0.04
58
0.0232
0.1223
n-C^Hjo
0.133
58
0.0771
0.4066
i-C5H12
0.035
72
0.0252
0.1329
n-C5Hn
0.048
72
0.0346
0.1825
C«+ as L(HW =
0.018
86
0.0155
0.0818
100.0 18.96 99.99
A-3
-------
N =
1.169% wt
12
12
C = _ (0.1809) + — (683) +
44
48
16
48
— (25.99) + — (3.432)
30 44
60
60
_ (0.1223) + _ (0.4066) + _ (0.1329) + _ (0.1825)
58
58
72
72
+ — (0.0818) = 75.64%
86
H = — (68.3) + — (25.99) + — (3.432) + (0.1223)
16 30 44 ' 58
+ — (0.4066) + — (0.1329) + — (0.1825) — (0.0818) = 23.05%
58 72 72 86
O = — C0.1809) = 0.1316%
44
Fd =
1.53 (75.64) + 3.64 (23.05) + 0.14 (1.169) - 0.46 (0.1316)
L159
Btu
scf
385.5 scf]
MMBtu
lb-mole
lb-mole
106 Btu
19.01 lb
= 8498
dscf
MMBtu
A-4
-------
Method 19 Flow Rate Calculation
dscf @ 0% O,
MMBtu
20.9
20.9 - 02 %
Stack Flow Rate
V
where 02% is exhaust concentration of Oj based on CEM results.
Convert ppmvw to ppmvd
ppmvw x
1
% H,0 in exhaust
= ppmvd
1 -
100
Convert ppmvd to ppmvd at 15% 02
ppmvd x 20.9 - 15 _ ppmv(j @ 15% O,
** 20.9 - 02% w 2
where 07% is dry exhaust concentration of 02 based on CEM results.
Convert ppmvd to Ib/hr
ppmvd x
1 million
10s
eit«K flow x (»¦*) 1 f lb-mole )
VminJ ( hr ) v 385.5 scfj
MW
( lb , (lb
= emission rate —
(lb-mole J Ihr
A-5
-------
Convert Ib/hr to g/Hp-hr
453.6 g
lb
1
g
operating HP HP-hr
Convert Ib/hr to Ib/MMBtu
fbl
x
hr
lb
hr
MMBtu
MMBtu
Convert lb/hr to tons/yr
PI
x
ton
[8760 hr 1
tons
hr
2000 lb
yr
yr
Convert pg/dscf to lb/hr
> g
x
g
x
lb
dscf
106 fig
453.6 g
x exhaust flow
dscf
x
60 min '
min
hr
= emission rate
rib
hr
A-6
-------
Fuel Flow Calculations From Orifice Meter
where
C0x
2 x g. x AP
x t x r x
f3600 sec]
(-hT-J
= Flow rate
P x (1-B4)
Flow rate (scfm) = — x [ 1 x LZ_1 x f460 +
hr [60 minj p4?7 J j460TT
C„ = Orifice Coefficient
ft-lb
+681
T
gc = 32.2
lbf - s2
AP = Pressure Drop Across Orifice (psia)
p = gas density
MW f lb
x
P (psia)
lb
_
1 |Ib-mole
ft3
R
psia • ft3
x T (°R)
lb-mole • °R
P = Gas Pressure (psia)
T = Gas Temperature (°R)
R = Ideal Gas Constant = 10.73
psia • ft:
lb-mole • °R
B = Ratio of Orifice Diameter to Pipe Diameter
r = Orifice Diameter
A-7
-------
Appendix B
OEMS and Operating Data
This appendix includes the run-averaged continuous emission monitoring system (CEMS)
data anil operating data (e.g., horsepower, engine speed, ambient temperature) for all engine
and turbine test runs. Chemical emissions measured include oxygen, carbon dioxide, nitrous
oxides, carbon monoxide, and total hydrocarbons. Emissions data re presented in
concentration (ppmv and percent volume), mass (lb/hr and tons/yr), and emission factor units
(g/BHP-hr).
B-l
-------
B.1 Campaign 2
Summary of CEM Test Results.
Teat Period
7
8
Engine
Cooper
Clark
Engine Type
GMVA-10
BA-6
Date
3/12/94
3/13/94
Test Time
1042-1550
1240-1810
Ambient Conditions
[Barometric Pressure (in Hg)
27.5
27.8
Ambient Temperature (°F)
60
70
Engine Operating Conditions
Brake horsepower (BHP)
984
994
Engine Speed (rpm)
283
295
IFuel Flow (scf7min) (a)
90
218
iHeat Input (MMBtu/hr) (b)
5.4
13.2
!iNGHHV(Btu/scf)
1012
1012 i
ING LHV (Btu/scf)
918
918
Exhaust Gas Conditions
Vo!. Flow (dscfm) - M 2
6050
5291 !
[Stack gas temp (F)
564
1092 !.
Moisture (%V)
5.7
9.0
jl02 (%V)
15.4
11.4
IC02 (%V)
2.3
3.9
[NOx (ppmvd)
233
1819
CO (ppmvd)
79
3i6
;THC (ppmvw)
718
219
[Exhaust Emissions
INOx (ppmvd @ 15% 02)
250
1130
[NOx (lb/hr)
10.1
68.9
[NOx (g/BHP-hr)
4.7
31.4
^JOx (tons/yr)
44
302
CO (ppmvd @ 15% 02)
85
221
iCO (lb/hr)
2.1
8.2
ICO (g/BHP-hr)
1.0
3.7
ICO (tons/yr)
9.1
35.9
THC (ppmvd @ 15% 02)
816
150
ITHC (lb/hr)
11.5
3.2
1 THC (g/BHP-hr)
5.3
1.4
'THC (tons'vr) 1
50.2
13.9
a Fuel flow measurements are approximations based on measured fuel flow to
several units,
b Based on HHV
01/30/96 ENG-SUM.WK4
B-2
-------
B.2 Campaign 3
Station 3A CEM Results
Engine 102
C-B LSV-16
|Tcct Period
2
3
(Load Condition
Full
Full
Low
bate
6/14/94
6/15/94
6/15/94
iTot Time
1600-2100
0832-1314
1437-1637
[Ambient Conditions
[Barometric Press (" Hg)
29.22
29.22
29.20
Ambient Temperature (F)
87
83
80
[Relative Humidity (%)
62.0
73.0
87.0
|Ab«olute Humidity (lb H20/1000 lb dry air)
17.87
18.35
19.74
(Engine Operating Conditions
iBrake horsepower (BHP)
4055
4202
3364
Load(%)
98.0
101
87.0
[Engine Speed (rpm)
321
325
302
Fuel Flow (scfrmin)
487 497
412
[Heat Input (VMBtu/hr) (a)
33.3
33.7
28.0
jHeat Rate(BtwBHP-hr, HHV)
8348
8145
8440
Heat R*te(Bti.BHP-hr, LH\')
7556
7372
7639
(NG HHV (Btu/scf)
1159
1148
1148
NG LHV (Btuscf)
1049
1039
1039
lExhaust Gas Conditions |
[Vol. Flow (dsofin) - M 2
7381
6947
6381 j
:VoI. Flow (dscfm) - M 19, Fd (b)
8735
8678
75261
Stack gas temp (F)
976
976
968
IMoisture (%V)
13.0
14.1
11.9,
102 (%V)
9.6
9.4
9*9 j
jC02 (%V) (t;)
6.33
6.33
6.0 i
jNOx (ppmvd)
1749
1657
825
jCO (ppmvd)
203
217
247
1THC (ppmvw)
1666
1677
1803
[Exhaust Emiuions
INOx (ppmvd 15% 02)
913
850
442
|NOx (lb/hr)
109
102.9
44.41
[NOx (g/BHP-J-ir)
12.2
11.1
6.0
INOx (lb/MMB tu)
3.3
3.1
1.6
INOx (tons/yr)
479
451
195
ICO (ppmvd @ 15% 02)
106
111
132 ;
ICO (Ib/hr)
7.7
8.2
8.1!:
ICO (g/BHP-hr)
0.9
0.9
1.1
CO (lb/MMBtu)
0.2
0.2
0.3 :
CO (tons/yr)
33.8
35.9
35.4!
THC (ppmvd @ 15% 02)
1000
1002
1097
rmc (lb/hr)
41.7
42.2
38.3
THC (g/BHP-hr)
4.7
4.6
5.2
THC (lb/MMBtu) j
1.2
1.3
1.4 !
THC (tona/vr)
182
185
1681!
a Based on HHV
b Used in emission rate calculations
c CEM analyzer not operating, FT IK C02 values shown
Note: Heating values based on 60°F reference-
Mi 9 flow rates based on 68°F reference.
11/01/95
ENG102-A.WK4
B-3
-------
Station 3A CEM Remits
Engine 101
C-BLSV-16
Test Period
1
2
3
Load Condition
Low
Full
Full
Date
6/15/94
6/16/94
6/16/94
Test Time
1831-1935
0915-1405
1415-1806
Ambient Conditions
Barometric Press (" Hg)
29.60
29.40
29.20
Ambient Temperature (F)
84
80
89
Relative Humidity (%)
72.0
78.0
58.0
Absolute Humidity (lb H20/10001b dry air)
18.48
17.58
17.90
Engine Operating Conditions
Brake horsepower (BHP)
3311
4056
4117
Load (%)
85.0
98.0
99.0
Engine Speed (rpm)
303
321
325
(Fuel Flow (sctfmin)
423
4'7S
486
Heal Input (MMBtu/hr) (a)
28.7
32.4
33.0
iHcat Rate(Btu/BHP-hr, HHV)
8800
8118
8126
[Heat Rate(Btu/BHP-hrt LHV)
7964
7347
7355
ING HHV (Btu/scf)
1148
1148
1148 |
ING LHV (Btu/scf)
1039
1039
1039;
lEzhaust Gas Conditions j
Vol. Flow (dscfin) - M 2
7125
7195
7319
[Vol. Flow (dscfin) - M 19, Fd (b)
8581
8421
8409
IStack gas temp (F)
922
962
970
'Moisture (%V)
12.2
13.5
13.5
102 (%V)
11.0
9.5
9.3 :
tC02 (%V) (c)
5.51
6.15
6.11 jj
[NOx (ppmvd)
259
1297
1544jJ
!CO (ppmvd)
209
258
2581
iTHC (ppmvw)
2269
1950
1879;
lExhaust Emissions
|NOx (ppmvd @ 15% 02)
154
671
785
'NOx (Ib/hr)
15.9
78.2
93.0
INOx (g^3HP-hr)
2.2
8.7
10.2 :
[NOx (Ib/MMBtu)
0.6
2.4
2.8
INOx (tons/yr)
69.7
342.5
407.2
jcO (ppmvd @ 15% 02)
124
134
131[:
ICO (Ib/hr)
7.8
9.5
9.41
[CO (g/BHP-hr)
1.1
.J
l.Oj'
ICO (ib/MMBtu)
0.3
0.3
0.3 !
ICO (tons/yr)
34.2
41.5
41.3-
[THC (ppmvd @ 15% 02)
1540
1167
11051
tTHC (lb/hr)
55.2
47.3
45.5-!
[THC (g/BHP-hr)
7.6
5.3
5.0 ,
iTHC (lb/MMBtu)
1.9
1.5
1.4 1
THC (tons/vr)
242:
207
199 I
a Based on HHV
b Used in emission rate calculations
c CEM analyzer not operating, FTIR C02 values shown
Note: Heating values based on 60°F reference.
M19 flow rates based on 68°F reference.
01/30/96 ENG101-A.WK4
B-4
-------
Station 3B CEM Results
Engine 4
C-B GMWA-8
Teat Period
1
2
Load Condition
Full
Low
Date
6/1 ft/94
6/18/94
Teat Time
0925-1115
1325-1523
Ambient Conditions
Barometric Press (" Hg)
29.29
29.29
Ambient Temperature (F)
85
94
Relative Humidity (%)
66.0
47.0
Absolute Humidity (lb H20/10001b dry air)
17.72
17.10
Engine Operating Conditions
Brake horsepower (BHP)
1958
1655
Load(%)
98.0
83.0
Engine Speed (rpm)
249
250
Fuel Flow (sctfmin)
244
221
Heat Input (MMBtu/hr) (a)
17.4
15.7
Heat Rate(Btu/BHP-hr, HHV)
9003
9645
Heat Rate(Btu/BHP-hr, LHV)
8196
8781
NG HHV (Bui/scf)
1206
1206
[NG LHV (Btu/scf)
1098
1098
Exhaust Gas Conditions
Vol. Flow (dscfm) - M 2
866S
8873
(Vol. Flow (dscfm) - M 19, Fd (b)
8290
8462
jStack gas temp (F)
645
610 j
[Moisture (%V)
9.3
7.8 1
102 (%V)
14.7
15.4 j
IC02 (%V) (c)
3.6
3.13
iNOx (ppmvd)
1246
384
jCO (ppmvd)
53.0
62.3
ITHC (ppmvw)
1129
1279 !
'Exhaust Emissions
NOx (ppmvd @ 15% 02)
1186
412 1
NOx (lb/hr)
74.0
23.3
INOx (g/BHP-hr)
17.1
6.4
jNOx (lb/MMBtu)
4.3
1.5
[NOx (tons/yr)
324
102
JCO (ppmvd @ 15% 02)
50.4
66.8
ICO (lb/hr)
1.9
2.3
|CO (g/BHP-hr)
0.4
0.6
|CO (lb/MMBtu)
0.1
0.1
ICO (tons/yr)
8.4
10.1 i1
!THC (ppmvd @ 15% 02)
1184
1489;
THC (lb/hr)
25.7
29.2;!
|THC (g/BHP-hr)
6.0
8.0.'
THC (lb/MMBtu)
1.5
1.9 j:
ITHC (tons/yr)
113
128!
a Based on HHV
b Used in emission rate calculations
c CEM analyzer not operating, FTIR C02 values shown
Note: Heating values based on 60°F reference.
M19 flow rates based on 68°F reference.
01/30/96 ENG4-A.WK4
B-5
\
-------
Station 3B CEM Results
Engine 2
C-B GMV-10TF
Tut Period
1
2
3
4
Load Condition
Low
Full
Full
Full
Date
6/18/94
6/19/94
6/19/94
6/20/94
Test Time
1800-1900
1105-1428
1690-2018
1240-1747
4mb4ent Conditions
Barometric Pras (" Hg)
29.29
29.36
29.36
29.41
Ambient Temperature (F)
92
91
91
91
Relative Humidity (%)
47.0
51.0
54.0
51.0
Abaolute Humidity Ob H20/10001b dry air)
15.99
16.74
17.72
16.71
Engine Operating Conditions
Brake bonepower (BHP)
894
1145
1142
1146
Load (%)
81.0
104
104
104
Engine Speed (rpm)
300
300
300
300!
Fuel Flow (sefmin)
119
146
146
141;
jHeat Input (MMBtu/hr) (a)
8.4
10.4
10.4
10.1:
iHeat Rate(Btu/BHP-hr, HHV)
9595
9192
9228
8914
jtHeat Rate(Btu/BHP-hr, LH\r)
8735
8360
8393
8108
[NG HHV (Btu/scf)
1206
1204
1204
1205 ^
!NG LHV (Btu/scf)
1098
1095
1095
1096
Exhaust Gas Conditions
fVol. Flow (dscfm) - M 2
3323
3377
3391
3217:
!VoI. Flow (dscfin) - M 19, Fd (b)
4311
3885
3890
3868
Stack gas temp (F)
595
661
660
651
iMoisture (%V)
7.5
10.3
9.3
7.8
02 (%V)
15.1
13.0
13.0
13.2
C02 (%V) (c)
3.34
4.35
4.53
4.32
NOx (ppmvd)
42.8
1287
1366
994
CO (ppmvd)
125
81.0
80.4
83.7
THC (ppmvw)
3117
828
818
865
Exhaust Emissions
NOx (ppmvd @ 15% 02)
43.5
961
1020
762 !
INOx (Ib/hr)
1.3
35.8
38.1
27.5 j;
[NOx (g/BHP-hr)
0.7
14.2
15.1
10.9|
;NOx (Ib/MMBtu)
0.2
3.5
3.7
2.71'
[NOx (tons/yr)
5.8
157
167
121
ICO (ppmvd @ 15% 02)
127
60.5
60.0
64.1
ICO (lb/hr) '
2.3
1.4
1.4
1.4.
ICO (g/BHP-hr)
1.2
0.5
0.5
0.6
ICO (lb/MMBtu)
0.3
0.1
. -0.1
0.1,
CO (tons/yr)
10.2
6.0
6.0
6.2
'THC (ppmvd @ 15% 02)
3428
689
674
718!
THC (Ib/hr)
36.2
8.9
8.7
9.0
THC (g/BHP-hr)
18.4
3.5
3.5
3.6;
THC (lb/MMBtu)
4.3
0.9;
0.8
0.9,,
THC (tons/vr)
158
39.1 1
38.3
39.6!!
a Based on HHV
b Used in emission rale calculations
c CEM analyzer not operating, FTIR C02 values shown
Note: Heating values based on 60°F reference.
M19 flow rates based on 68°F reference.
11/01/95 ENG2-A.WK4
B-6
-------
B.3 Campaign 4
Station CEM Results
Waukesha Engine
Waukesha L7042GU
Before NSCR
Test Period
3
4
Load Condition
Intermediate
Low
Sampling Legation
Before NSCR
Before NSCR
Date
8/23/94
8/24/94
Test Time
1805-2028
1020-1201
Ambient Conditions
Barometric Pressure (in. Hg)
29.47
29.55
Ambient Temperature (°F)
74
87
Relative Humidity (%)
654
36.7
Abs. Humidity (lb H20/lb drv air)
12.0
10.4
Engine Operating Conditions
Brake horcs power (BHP)
644
362
Load (%)
88
52!
Engine Speed (rpm) ~
813
779!
Fuel Flow (scfrmin) (a)
82.8
54.7|
Heat Input (MMBtu/hr) (b) **
4.95
3.28 j
Heat Rate (Btu/BHP-hr. HHV)
7809
9185 I1
Heat Rate (Btu/BHP-hr, LHV)
7035
8279 |
ING HHV (Btii/scf)
1011
1013
ING LHV (Blu'scf)
911
913
iExhaust Gas Conditions
[Vol. Flow (dscfm) - M 2 (c)
1274
¦474 '
!Vol. Flow (dscfm) - M19. Fd
716
472
IStack Gas Temperature (°F)
796
641
jMoisturc (%V)
20.7
20.5
02 (%V)
0.42
0.35,
IC02 (%V)
11.2
ll',5i
INOx (ppmvd)
2843
2542 j
ICO (ppmvd)
3714
2690
!THC (ppmvw
1048
1394 r
iExhaust Emissions
jNOx (ppmvd 15%02)
819
730!
|NOx (Ib/hr) j
25.9
8.6
jNOx (g/BHP-hr)
18.3
10 8|
INOx (Ib/MMI.iu)
5.24
2.63
INOx (tons/vr) :
114
37.8!
CO (ppmvd (a 15% 02)
1070
772:
iCO (Ib/hr) |
20.6
5.56,
CO (g/BHP-hr) ;
14.5
6.961
CO (Ib/MMBtu) j
4.16
I.70s
CO (tons/vr)
90.3!
24.3
THC (ppmvd (| 15% 02) ,
381
504
iTHC (Ib/hr)
4.19
2.07
ITHC (g/BHP-hr) j
2.96
2.59
THC (Ib/MMBtu)
0.85
0.63
THC (tons'vr) !
JM
9 1
a Fuel flow rale is suspect due to data collection difficulties,
b Based on HHV
c Used in emission calculations.
Note: Heating values based on 60°F reference.
MI9 flow rates based on 68°F reference.
10/27/95
WB-SUMWK4
-------
Station CEM Results
Waukesha Engine
Waukesha L7042GU
After NSCR
1 Test Period
2
5
iLoad Condition
Full
Full
Low-
Sampling Location
After NSCR
After NSCR
After NSCR
Date
8/23/94
8/23/94
8/24/94
Teat Time
1146-1345
1424-1722
1210-1306
1 Ambient Conditions
Barometric Pressure (in. Hg)
29.54
29.49
29.54
1 Ambient Temperature (°F)
87
87
92
Relative Humidity (%)
35.2
40.1
27.2
Abs. Humidity (lb H20/lb drv air)
10.1
11.3
9.3
Eneine Operating Conditions
Brake hores power (BHP)
692
671
359
Load (%}
95
92
51
Engine Speed (rpm J
809
811
779
Fuel Flow(scf)min) (a)
88.0
84.6
54.7 j
(Heat Input (MMBtu/hr) (b)
5.26
5.05
3.28
Heat Rate(Btu/BHP-hr. HH\')
7717
7646
9275
iHeat Rate (Btu/BHP-hr, LHV)
6952
6888
8360
NG HHV (Btu/scf)
1011
1011
1013
iNG LHV (BtWscf)
911
911
913:'
Exhaust Gas Conditions 1
!VoI. Flow (dscfm) - M 2 (c)
1274
1274
474 ¦
j vol. Flow(dscfm)-MI9. Fd
746
718
464!
'¦Stack Gas Temperature (°F)
796
796
641,
jIMoisture (%V)
20.7
20.7
20.5 j:
02 (%V)
0.04
0.06
0.001
iC02 (%V)
31.7,
11.7
12.0
NOx (ppmvd)
8.03
8.38
35.3
iCO (ppmvd)
68.5 !
69.5
35.8
!THC (ppmvw)
607
640
846
Exhaust Emissions
:NOx (ppmvd (a 15® k. 02)
2.27.
2.37]
lO.Oj
!NOx (Ib/hr)
0.07:
0.08,
0.12 1
tNOx (g/BHP-hr)
0.05
0.05
0.15;
INOx (Ib/MMBtu)
0.01 !
0.02
0.04;
'NOx (tons/vr) !
0.32 !
0.33 1
0.531
CO (ppmvd @ 15°/o 02)
19.4 |
19.7.
10.1 j!
ICO (Ib/hr)
0.38
0.39 ;
0.07
ICO (g/BHP-hr)
0.25 f
0.26.
0.09;
|C0 (Ib/MMBtu)
0.07 ^
0.08:
0.02
!C0 (tons/vr) !
1.67
1.69
0.32'
ITHC (ppmvd @ 15°/o 02)
217.
228,
301
ITHC (Ib/hr)
2.43'
2 56
1.26
iTHC (g/BHP-hr)
1.591
1.73
1.59
'THC (Ib/MMBtu)
0.46
0.51 |
0.38
ITHC (tons/vr) 1
10.6
11.21
5.5
a Fuel flow rate is suspect due to data collection difficulties
b Based on HHV
c Used in emission calculations.
Note: Heating values based on 60°F reference.
M19 flow rates based on 68°F reference.
10/27/95 WA-SUM.WK4
B-8
\
\
-------
Station CEM Results
Engine 4
C-B GMVC-IOC
[Test Period
7
9
H
I
[Load Condition
Full
Full
Full
Low
Sampling Location
Before Catalyst
Before Catalyst
Before Catalyst
Before Catalyst
bate
8/25/94
8/26/94
8/30/94
8/30/94
hfest Time
1705-1906
1310-1537
1605-1630
1656-1735
[Ambient Conditions
[Barometric Piessure (in Hg)
29.44
29.47
29.36
29.35
[Ambient Temperature (°F)
85
89
85
84
Relative Humidity (%)
37.8
40.5
294
44.8
lAbs. Humidity (lb H20/)b drv air)
10.1
12.4
8.0
11.4
lEneioe Opentine Conditions
iBrake horcspower (BHP)
1732
1674
1705
1422
Load (%)
97
93
95
79
Engine Speed (rpm)
299
300
299
299,
Fuel Flow(scf/min)
211
213
212
185
Heat Input (MMBtu/hr) (a)
126
12.7
12 7
11.0
Heat Rate (BtiVBHP-hr, HHV)
7368
7706
7550
7880
Heat Rate (Btu/BHP-hr, LHV)
6640
6945
6803
7100
tNG HHV (BtUscf)
1009
1009
1011
1011,
ING LHV (Btu/scf)
910
910
911
911!
Exhaust Gas Conditions 1
!Vol Flow (dscfm) - M 2
8486
NA,
8338
8371
Vol Flow (dscfm) - M19, Fd (b)
6920
6866
6633
6039
Stack Gas Temperature (°F)
574
517
506
5071
IMoisture (%V)
7.26
7.30
820
7.95;
102 (%V)
15.5
15.4
15.3
15.5'
!C02 (%V)
2 86
2.96
292
2 81;
[NOx (ppmvd)
39.2
34 l;
36 9
20.2:
ICO (ppmvd)
162
181
178
237
-THC (ppmvw)
1218
1559
1426
1948
lExhaust Emissions
| NOx (ppmvd (i 15% 02)
43 1
36.9
386
22 1
jjNOx (Ib/hr)
1.941
1 68
175
0 87
tNOx (g/BHP-hr)
0.51
0 45;
047
0.28
iNOx (Ib/MMBtu)
0.15!
C.I3
0.14
0 08
!NOx (tons/vr) !
8.50 !
7.35
7.67
3.83
iCO (ppmvd @ 15% 02)
179!
195
186
260'
ICO (Ib/hr) !
4.89,
5.41
5 15
6.251,
jCO (g/BHP-hr) ;
1 28!
1 47
1.37
1.991
ICO (Ib/MMBtu)
0.39 j
043
0 41 :
0.57 '
ICO (tons/vr)
21.4 1
23 7
22.5
27 4!
|THC (ppmvd @ 15% 02)
1446 ¦
1817
1624
2317;
|THC (Ib/hr)
22.6|
28.8
25.6 <
318
ITHC (g/BHP-hr) |
5.93.
7.79
682
10.2
THC (Ib/MMBtu)
1.80 [
2.26
2 02
2 88
THC (tons/vr)
99 1 1
126 1
112
139 :
a Based on HHV
b Used in emis sion calculations
Note: Two power outages occured during Run 9
Note: Heating values based on 60°F reference
M19 flow rates based on 68°F reference
10/26/95 E4B-SUMWK4
B-9
-------
Station CEM Results
Engine 4
C-B GMVC-10C
Test Period
8
10
Load Condition
Full
Intermediate
Sampling Location
After Catalyst
After Catalyst
Date
8/26/94
8/26/94
Test Time
1051-1226
1620-1821
Ambient Conditions
Barometric Pressure (in Hg)
29.47
29.45
Ambient Temperature (°F)
84
86
Relative Humidity (%)
47.8
42.6
Abs Humidity (lb H20/lb drv air)
12.5
118
Engine Operating Conditions
Brake horespower (BHP)
1773
1600
Load (%)
99
89
Engine Speed (rpm)
299
300 j
Fuel Flow (scf/min)
211
203
!Heat Input (MMBtu/hr) (a)
12.6
12 1
iHeat Rate (Btu/BHP-hr, HHV)
7199
76991
IHeat Rate (Btu/BHP-hr. LHV)
6488
6938!
iNG HHV (Btu/scf)
1009
1009
ING LHV (Btu/scf)
910
910
Exhaust Gas Conditions
!VoI Flow (dscfm) - M 2
8751
NA
iVol Flow (dscfm)- M!9. Fd (b)
6696
6592
liStack Gas Temperature (°F)
517
517
Moisture (%V)
7.26
7.30,
It02 (%V)
15 4
155
IIC02 (%V)
3.03
2.96'
[NOx (ppmvd)
44 0
33 1
-CO (ppmvd)
14.2
127,
iTHC (DDmvw)
1358
1567
!Exhaust Emissions
'NOx (ppmvd ia 15% 02)
46 9
35.9'
'NOx (Ib/hr)
2 1!
1 56.
INOx (g/BHP-hr)
0.54
0 44.
INOx (Ib/MMBtu) !
0.17
0.13
INOx (tons/vr)
9.25
6 84!'
ICO (ppmvd (a 15% 02)
15.1
13 8
iCO (lb/hr)
041 .
0.37
ICO (g/BHP-hr)
0.11
0.10
ICO (Ib/MMBtu)
0.03
003:
ICO (tons/vr)
1 81
1.60
ITHC (ppmvd @ 15% 02) j
1559
1837
|THC (lb/hr)
24.4
27.8
ITHC (g/BHP-hr) j
6.25;
7 87
THC (Ib/MMBtu)
1 94
2.29
THC (tons/vr)
107
122!
a Based on HHV
b Used in emission calculations
Note: Heating values based on 60°F reference
Ml 9 flow rates based on 68°F reference
10/26/95 E4A-SUM.WK4
B-10
-------
Station CEM Results
Engine 8
I-R KVS-412 (PCC)
Test Period
11
12
Load Condition
Intermediate
Intermediate
Date
8/27/94
8/27/94
Test Time
1108-1503
1639-1921
Ambient Conditions
Barometric Ftessure (in. Hg)
29.45 j 29.41
Ambient Temperature (°F)
91
86
Relative Humidity (%)
32.7
35.0
Abs. Humidity (lb H20/lb dry air)
10.8
9.7
Engine Oiwating Conditions
Brake horespower (BHF)
1783
1640
Load (%)
89
82
s Engine Speed (rpm)
330
330:
Fuel Flow (sof/min)
272
253|
Heat Input (MMBtu/hr) (a)
16.2
15.11
Heat Rate (Bi:u/BHP-hr, HHV)
9239
9340!
Heat Rate (Blu/BHP-hr, LHV)
8327
8418
NG HHV (Btu/scf)
1009
1009!
fNG LHV (Btu/scft
910
910'
Exhaust Gas Conditions
Vol. Flow (dscfm) - M 2
5726
5737,
!Vol Flow (dscfm) - M19. Fd (b)
4975
4706
IStack Gas Temperature (°F)
741
719;
jMoisture (%V)
111
n.r
02 (%V)
11 3
11 4:
IC02 (%V)
536
5.22'
NOx (ppmvd)
69.7
58 7
IcO (ppmvd)
352
385
ITHC (ppmvw)
1937
3290 :
lExhaust Emissions
[NOx (ppmvd @ 35% 02)
42.8
366'
NOx (Ib/hr)
248
1 98
jNOx (g/BHP-hr)
063
0.55.
(NOx (Ib/MMBtu)
0 15
0 13
fNOx (tons/vr)
109
87|
ICO (ppmvd @ 15% 02)
216
240 !¦
ICO (Ib/hr)
7 62
7.90
|CO (g/BHP-hr)
1 94
2.19'!
|C0 (lb/MMBiu)
0 47
0.52
|C0 (tons/vr)
33.4
34.6:
[THC (ppmvd >2; 15%02)
1336
2308
tTHC (Ib/hr) i
27.0
43.4 j
[THC (g/BHP-hr)
6.87
12.0 ;
fTHC (Ib/MMEttu) !
1.661
2.87 '
tTHC (tons/vr)
118
1901'
a Based on HHV
b Used in emission calculations
Note Heating values based on 60°F reference
Ml9 flow rates based on 68°F reference
10/26/95
B-ll
-------
Station CEM Results
Engine 9
I-R KVS
Test Period
13
14
17
Load Condition
Intermediate
Full
Full
Sampling Location
Before SCR
Before SCR
Before SCR
Date
8/28/94
8/29/94
8/29/94
Test Time
1254-1520
0858-0932
1613-1700
Ambient Conditions
Barometric Pressure (in. Hg)
29.46
29.47
29.37
Ambient Temperature (®F)
94
77
91
Relative Humidity (%)
27.8
52.1
31.7
Abs. Humidity (lb H20/lb drv air)
10.1
10.6
10.3
Engine Ope ratine Conditions
[Brake horespower (BHP)
1764
1840
1830
Load (%}
88
91
911
Engine Speed (rpm)
330
332
331
Fuel Flow(scf/min)
261
272
266:
Heat Input (MMBtu/hr) (a)
15.6
16.3
15.9;
Heat Rate (Btu/BHP-hr, HHV)
8950
8978
882l'
IHeat Rate (Btu/BHP-hr, LHV)
8068
8090
7948
|NG HHV (Btu/scf)
1010
1011
1011
!NG LHV (Btu/scf)
910
911
911
Exhaust Gas Conditions
j;VoI. Flow(dscfm)- M 2
4181
4259
4259!
i!Vol Flo»(dscfm)-MI9, Fd (b)
3656
3914
3754
j Stack Gas Temperature (°F)
779
779
779
Moisture (%V)
14 4
14 4
14.4:
102 (%V)
8.27
8.56
8.33]
iC02 (%V)
6 95
6.93
7.10
!NOx (ppmvd)
3351
3042
3339!
!C0 (ppmvd)
138
141
126
THC (ppmvw)
947
938
900
Exhaust Emissions
!NOx (ppmvd (a, 15% 02) ;
1566
1454
1567
fNOx (Ib/hr) !
87 7
85.2
89 71!
INOx (g/BHP-hr) |
22.6
21.0;
22.3;
INOx (Ib/MMBtu) i
5.64
5.24
5.65
'NOx (tons/vr)
384
. 373
393
iCO (ppmvd (ff 15% 02)
64.3
67 6
59 1 :
iCO (Ib/hr) J
2.19
2.41
2.06 ,
iCO (g/BHP-hr)
0.56
0.59
0 51
iCO (Ib/MMBtu)
0 14;
0 15i
0.13
jCO (tons/vr)
96!
10 6
9.02
jTHC (ppmvd @ 15% 02)
517
524
493
[THC (Ib/hr)
10.1
10.7
9.8
ITHC (g/BHP-hr) 1
2 59!
2.63
2.44
THC (Ib/MMBtu)
0.65
0.66;
0.62
THC (tons/vr)
44 I
46.81
43 01
a Based on HHV
b Used in emission calculations
Note Heating values based or 60°F reference
Ml 9 flow rates based on 68°F reference.
E9B-SUM.WK4
B-12
-------
Station CEM Results
Engine 9
I-R KVS
Test Period
15
16
Load Condition
Full
Full
ISampliag location
After SCR
After SCR
Date
8/29/94
8/29/94
Test Time
0959-1330
1413-1549
Ambient Conditions
Barometric Pressure (in Hg)
29.45
29.39
Ambient Temperature (#F)
87
93
Relative Humidity (%)
33.1
31.8
Abs Humiditv (lb H20/lb dry air)
9.3
11.2
Engine Operatine Conditions
Brake horespower (BHP)
1809
1800
Load (%)
90
90
lEngine Spe:d (rpm)
331
331
Fuel Flow (scf/min)
270
265
Heat Input < MMBtu/hr) (a)
16 1
15 8
Heat Rate (Btu/BHP-hr. HHV)
9051
8924
iHeat Rate (Btu/BHP-hr, LHV)
8156
804)
NG HHV (Btu/scO
1011
1011
NG LHV (Eitu/scf)
911
911
lExhaust Gas Conditions
iVol. Flow (dscfm) - M 2
4259
4259;
Vol Flow (dscfm) - Ml9. Fd (b)
3890
3804|
[Stack Gas Temperature (°F)
779
779
IMoisture (°/>V)
144
14 4,
!02 (%V)
8 60
8 56
liC02 (%V)
6 78
6 80
IINOx (ppmvd)
677
775 .
ICO (ppmvd t
103
102
THC (ppmvw)
949
1001
lExhaust Emissions
INOx (ppmvd @ 15% 02)
325
371;
INOx (Ib/hr)
18 8
21 1.
(NOx (g/BHP-hr)
4 73
5 32
lNOx(lb/MMBtu)
1 17
1 33
tNOx (tons/\r)
82.5
92 5
ICO (ppmvd @ 15% 02)
494
48 6,'
ICO (Ib/hr)
1.75
1 69[.
jcO (g/BHP-hr)
044
0.42;
jCO(lb/MM Btu) |
0 11
o nil
ICO(tons/vri 1
7 65
7.39''
[THC (ppmvj (a 15% 02)
532
559,
!THC (Ib/hr) j
107
11.1
'THC (g/BHP-hr) j
2.69
2 79:'
[THC (Ib/MMBtu)
0.67
0.70 ;
ITHC (tons/vr) 1
47 0
48.5 :
a Based on HHV
b Used in emission calculations
Note: Heati ig values based on 60°F reference
MIS' flow rates based on 68®F reference
10/26/95
B-13
-------
Station CEM Results
Engine 8
I-R KVS
[Test Period
A
B
C
D
E
F
G
Load/Timing
92%/r
8SV./8°
M%/5°
88%/5°
M%/8°
87%/ll°
80%/ir
bate
8/30/94
8/30/94
8/30/94
8/30/94
8/30/94
8/30/94
8/30/94
(Test Tine
0745-0815
0903*0944
1013-1042
1100-1145
1150-1228
1234.1302
1307-1339
LAmbient Conditions
(Barometric Pressure (in. Hg)
29.41
29.42
29.43
29.42
29.41
29.40
29.39
[Ambient Temperature (eF)
73
78
82
85
86
89
90
Relative Humidity (%)
66.4
55.5
47.0
43.2
40.7
37.8
36.4
Abs. Humidity flb H20/lb drv air)
11.7
11.6
11.4
11.3
11.3
11.6
] 1.4
ICncine O Derating Conditions
(Brake horespower (BMP)
1846
1693
1656
1708
1783
1687
1621
Loadf/.)
92
85
84
88
88
87
80
Engine Speed (rpm)
330
329
327
323
335
333
333
[Fuel Flow (scCmin)
267
265
276
277
276
254
247
(Heat Input (MMBtu/hr) (a)
159
15.8
16.5
16.5
16.5
15.1
14.7
b-ieat Rate (Btu/BHP-hr. HHV)
8757
9477
10094
9819
9375
9116
9226
Heat Rate (Btu/BHP-hr, LHV)
7893
8542
9098
8850
S450
8216
8315
ING HHV (Btu/scf)
1009
1009
1009
1009
1009
1009
1009
fNG LHV fBtu/scf)
910
910
910
910
910
910
910
Exhaust Gas Conditions
IVol. Flow (dscfm) - M 2
4531
4572
4553
4518
4517
4517
4579
iVol. Flow (dscfm) - M19. Fd (b)
4927
4978
5229
5143
5040
4582
4567
[Stack Gas Temperature (°F)
746
739
756
766
762
749
733
liMoisture (%V)
120
11.8
11.7
11.8
11.9
12.1
11.8
|!02 (%V)
11.3
11.5
11.6
11.4
11.2
11.1
11.3
C02 (%V)
5 19
5.06
5.01
5.13
5.23
5.30
5.12
iNOx (ppmvd)
64.6
53.3
48.7
55.7
60.0
67,0
55.1
fCO (ppmvd)
378
419
364
331
394
399
451
|THC (ppmvw)
2333
3569
4143
2897
2683
1926
3298
lEihaust Emissions
!NOx (ppmvd @ 15% 02)
39.7
33.4
30.8
34.5
36.5
40.3
34.0
INOx (Ib/hr)
2.28
1.90
1.82
2.05
2.17
2.20
1.80
fNOx (g/BHP-hr)
0.56
0.51
0.50
0.54
0.55
0.59
0.50
NOx (Ib/MMBtu)
0 14
0.12
0.11
0.12
0.13
0 15
0.12
fNOx (tons/vr)
10.0
8.32
7.99
8.98
9.48
9.63
7.89
iCO (ppmvd (3 15% 02)
232
263
230
205
240
240
278.
€0 (lb/hr) |
8.10,
9.10
8.29
7.42
8.65
7.96
8 98
CO (g/BHP-hr)
1.99 i
2.44'
2.27
1.97
2.20
2.14
2.51
CO (Ib/MMBlu)
0.51
0.58 i
0.50
0.45
0.53
0.53
0.61
ICO (tons'vr)
35.5
39.8
36.3
32.5
37.9
34.9
39.3
THC (ppmvd @ 15% 02)
1631
2534 i
2964
2033
1854
1317
2305|
[THC (lb/hr)
32.5'
50.2
61.1 '
42.1
38.2
25.0
42.5
THC (g/BHP-hr)
8.0
13.4
16.7
11.2
9.7
6.7
11.9
[THC (Ib/MMBtu)
2.04
3.17:
3 71
2,55
2.32
1.65
2.89
THC (tons/vr)
142
220
268
184
167
109
186
a Based on HHV
b Used in emission calculations
Note: Heating values based on 60°F reference.
M19 flow rates based or 68°F reference.
10/26/95 E8-PSUM.WK4
B-14
-------
Station CEM Results
Engine 1
C-B GMVA-10
((Tart Period
6
If wdlH
bate
azMP
•OS/W
flmtTm*
•9S2-IC20
kabient CMdttow
i&anmtric Pram (ml Hg)
29.52
[Ambieot Temperature (*F)
S4
Relative Humidity (%)
34.7
lAba. Humidity (lb H20/lb dry air)
19
lEaffiae OpcratMC Coadfrkw
Drake horaapoww (BHP)
1139
Lad(%)
rr
[Engine Speed (rpn)
296
jFuel Flow (acCmin) (a)
-
[Heat Input (MMBtuAr)
-
[Heat Rate (BtuBHP-hr, HHV)
-
Heat Rate (BtuBHP-hr. LHV)
-
fNG HHV (Btu/tcf)
1009
(nG LHV (Btu/scf)
910
lExhaust Gas Conditions
jvol. Flow (dacfin) - M 2
NA
[Vol. Flow (dacfin) • M19, Fd
-
[Stack Gas Temperature (*F)
517
[Moisture (%V)
7.30
02 (%V)
14.6
C02(SV)
3.43
NOx (ppmvd)
141
CO (ppmvd)
79.0
THC (pom vw)
1353
Exhaust gfPi"iA^^ 1
NOx (ppmvd @ 15S 02)
132
NOx (IMir)
"1
NOx (^BHP-hr)
»|
NOx (Ib/MMBtu)
-J
NOx (tona/yr)
"1
CO (ppmvd @15S 02)
73.9
CO (IMv)
-
CO (yBHP-hr)
-
CO (llWMMBtu)
-
CO flona/vr)
—
THC (ppmvd @ 15H 02)
1364
THC (1K1*)
-
THC (g/BHP-t)
-
THC flh/MMBtu)
-
THC (tona^vr)
-
* Fuel flow BKafuremciitj frwn thia enpoe are cooaidervd wapcct.
Due to the ccxnpttatioiul procedural employed, tbeae naccuractea
affect hut input, beat rate, exhauat flowrale, muwoq flowratea, mi
—facton; therefore, theac parameter! are lot calculated.
*dg/£n/cam;>4
Twt-rpi.rev
B-15
November 30,1995
27S-114-06-14
-------
B.4 Campaign 5
Test Period
3
4
Equipment
Turbine
T urbine
Date
10/05/94
10/05/94
Test Time
1230-1755
1843-2133
Ambient Conditions
Barometric Press (" Hg)
29.34
29.35
Ambient Temperature (F)
57.24
51.48
Relative Humidity (%)
51.26
75.12
Absolute Humidity (lb H20/1000Ib dry air)
5.11
6.04
Operating Conditions
Brake horsepower (BHP)
20000
20000
Fuel Flow (scf/mm)
3298
3298
Heat Input (MMBtu/hr)
203
203
Heat Rate(Btu/BHP-hr. HHV)
10151
10151
Heat Rate(Btu/BHP-hr. LHV)
9142
9142
ING HHV (Btu/scf)
1026
1026
NG LHV (Btu/scf)
924
924
Exhaust Gas Conditions
|Vol. Flow (dscftn) - M 2 (b)
232503
214147,
[Vol. Flow (dscftn) - M 19
185603
1844601
Stack gas temp (F)
239
430
I Moisture (%V)
4.03
4.46 |
I02 (%V. dry)
17.7
17.6
!C02 (%V, dry)
2.00
2.00
|NOx (ppmvd)
41.4
39.6
CO (ppmvd)
13.2
16 6.
ITHC (ppmvw)
ND
ND
Exhaust Emissions
NOx (ppmvd tg 15% 02)
75.6
71.9
INOx ISO (ppmvd)
75.0
73.8
iNOx (lb/hr)
68.9
60 7
INOx (g/BHP-hr) *
1.56
1.38
|NOx (Ib/MMBtu)
0.34
0.30 ,
iNOx (tons/yr)
302
266'|
CO (ppmvd la, 15% 02}
24.1
30.2 '
|CO (lb/hr)
13.4
15.5 :
ICO (g/BHP-hr)'
0.30
0.35
|CO (lb/MMBtu) !
0.07
0.08
ICO (tons/yr)
58 6
68.0
ITHC (ppmvd @ 15% 02)
-i
ITHC (lb/hr) 1
H
ITHC (g/BHP-hr) •
-
THC (lb/MMBtu) J
-
THC (tons/vr) !
Hi
a Based on HHV
b Used in emission calculations
* Calculated using rated horsepower of20,000 BHP
Note; Based on operating parameters, turbine appears to be at full load.
10/26/95
B-16
CEMCPN5.WK4
-------
GRI Campaign 6 - Station iA CEM Results
Engine 10
Clark BA-5
IfTest Period
ULoad Condition
jlSaapling Location
bate
[Test Tine
Full
Exhaust
11 AM/94
1000-1224
3
Low
Exhaust
11/04/94
1448-1603
2
Full
Exhaust
11/05/94
0936-1209
Ambient Conditions
[Barometric Pressure (in. Hg)
26.36
26.35
29.27
[Ambient Temperature (°F)
62
51
62
Relative Humidity (•/•)
62.7
93.0
29.3
Abs. Humtditv flb H20/1000 lb drv air)
8.2
8.1
3.5
Engine Opcraiinr Conditions
Brake horespower (BHP)
851
725
910
Load (*/.)
94
80
100
[Engine Speed (ipm)
299
301
299
(Fuel Flow (scf/itiin)
161
147
174
Heat Input (MMBtu/hr) (a)
9.8
8.9
10.5
Heat Rate (Btu/BHP-hr, HHV)
11627
12468
11737
Heat Rate (Btu/BHP-hr, LHV)
10529
11291
10627
NG HHV (Btu/itf)
1025
1025
1021
NG LHV (Btu/scf)
928
928
924,
Lxhaust Gas Conditions !
iVol. Flow (dscfm) - M 2
7163
7313
1
7493!
iVol. Flow (dscftn) - M19, Fd (b)
4272
4356
4679)
IStack Gas Temperature (eF)
458
436
455
iMoisture (%V)
10.4
8.8
8.0;
J02 (%V dry)
14.2
14 9
14.3!
IC02 (%V dry)
4.3
3.9
4.4|
NOx (ppmvd)
914
373
1337 [j
iCO (ppmvd) '
86.3
95.5
92.6,
THC (ppmvw) (c)
NA
NA
970,
Exhaust Emissions 1
INOx (ppmvd @ 15% 02) j
805
367
T1951'
NOx (Ib/hr) j
280
11.6
44 8
INOx (g/BHP-hr)
149
7.28
22.31:
NOx (Ib/MMBtu) 1
2.87
131
4.26 |i
INOx (tons/vr)
122
50.9
196!;
ICO (ppmvd @ 1 02)
76.0
93.9
82.8';
iCO (ItVhr)
1.61
1.81
1.89 I
ICO (g/BHP-hr)
0.86 |
1.13
0.94j|
CO (Ib/MMBtu)
0.16;
0.20
0.18
ICO (tons/vr)
7.04;
7.94
8.27
THC (ppmvd @ 15% 02) j
,
943 i
THC flb/hr) j
—
,
12.3
THC (g/BHP-hr) |
—j
6.12 |
THC (Ib/MMBtu) j
I]
1.17 i
THC ftons/vr>
53.8 1
a Based on HHV
b Used in emission calculations.
c THC analyzer equipment failure. A new instrument arrived on site late on 11/04/94.
NA - Not available
Note: Heating values based on 60°F reference.
M19 flow rates based on 68°F reference.
10/26/95
B.5 Campaign 6
E10-SUM.WK4
B-17
-------
GRI CAMPAIGN 6 /'
/
-This calculation was required to adjust for an exhaust leak present in Engine 10 at site 6A.
;
-Tests 1 and 3 were conducted before and after the exhaust leak, however, no test was conducted
before the exhaust leak during test 2. >
-A correction factor was needed to adjust the CEM exhaust concentrations in Test 2, as well as
for moisture and concentrations measured by FTIR, GC, CARB 430, and Method TO-14 for Tests 1, 2, and 3.
\
TEST 1 (before leak) 1 (after leak) 1 Ratio 3 (before leak) 3 (after leak) 3 Ratio Correction Factor
02 (%)
NOx (ppmv)
C02 (%)
CO (ppmv)
tfl - To get correction factors, the 02 ratios were averaged to give an 02 correction. The average of all the other
oS ratios for NOx, CO, and C02 were averaged to give correction factors for these compounds as well as for
moisture and compounds measured by FTIR, GC, CARB 430, and Method TO-14 for tests 1, 2, and 3.
Example for Test 2.
2 (after leak) 2 (corrected)
02=16.8 =14.3
NOx-820 =1337
C02=2.69 =4.38
CO=56.8 =92.6
14.2
16.9
0.84
14.9
17.3
0.86
0.85
914
597
1.53
373
219
1.7
1.63
4.3
2.65
1.62
3.88
2.41
1 61
1.63
86.3
51.7
1.68
95.5
59.1
1.61
1.63
-To correct for FTIR, GC, CARB 430, and Method TO-14 multiple dry concentration by 1.63.
Example:
Ethane (measured by FTIR) for Engine 10, Test 1 was 10.6 ppmv, corrected to 17.3 ppmv through the factor 1.63.
11/03/95
I FAK-OOR WK4
-------
GRI Campaign 6 - Station 6C CEM Results
Engine IS
C-B GMVC-10
[Test Period
Load Condition
Sampling Location
Date
Test Tine
9
Full
Exbaust
11/10/94
1030-1500
10
Fall
Exhaust
11/10/94
1546-1801
11
Intermediate
Exhamt
11/11/94
0930-1140
Ambient Conditions
Barometric Preerore (in. Hg)
26.72
26.64
26.66
Ambienl Temperature (°F)
53
58
53
Relative Humidity (%)
46.5
36.2
62.6
Aba. Humiditv (lb H20/1000 lb dry air)
4.4
4.2
5.8
Engine Operating Conditions
Brake horespower (BHP)
1827
1830
1523
Load (%)
102
102
85
Engine Speed (fpm)
300
300
299
Fuel Flow (sctfmin)
266
266
263
[Heat Input (MMBtuAr) (a)
16.0
16.0
16.0
Heat Rate (Btu/BHP-hr, HHV)
8900
8884
10667
(Heat Rate {Btu/BHP-hr, LHV)
8061
8046
9661
VG HHV (Btu/»cf)
1020
1020
1020
ING LHV (Btu/scf)
924
924
924
lExhsust Gas Conditions
Vol. Flow (dicfm) - M 2
7570
7588
7363
[Vol. Flow (dicfin) - M19, Fd (b)
7972
7749
8769
Suck Gas Temperature (T)
581
576
552
[Moisture (%V)
7.00
7.00
6.90 1
102 (%V dry)
15.0
14.8
15.5
|C02 (%V dry)
3.68
3.69
3.36
NOx (ppmvd)
560
638
278 ,
CO (ppmvd)
71.2
71.1
76.2
THC (ppmvw)
971
957
1300
Exhaust Emissions
!NOx (ppmvd @ 15% 02)
560
620
306 i
|NOx(lb/hr)
31.9
35.4
17.5 :
InOx (g/BHP-hr)
7.93
8.77
5.20 ,
NOx (Ib/MMBtu)
1.99
2.21
1.09 :
NOx (lom/yi)
140
155
76.5
|CO (ppmvd @ 15% 02)
71.2
69.1
83.9
CO (lb/hr)
2.47
2.40
2.91 ;
CO (g/BHP-hr)
0.61
0.59
0.87 i
CO (Ib/MMBtu)
0.15
0.15
0.18
CO (tons/YT)
10.8
10.5
12.8
THC (ppmvd @ 15% 02)
1044
1000
1538 '
THC (IMir)
20.7
19.9
30.5 i
THC (g/BHP-hr)
5.15
4.92
9.08
THC (Ib/MMBtu)
1.29
1.24
1.91 i
THC floni'vr")
?9r?
87.0
134!
a Bated on HHV
b Used in emission calculations.
Note: Heating values based on 60°F reference.
M19 flow rates baaed on 68°F reference.
01/30/96 E15-SUMWK4
B-19
-------
GRI Campaign 6 - Station 6C CEM Results
Engine 11
C-B GMVC-10
(Test Period
{Load Condition
[Sampling Location
bate
[Test Time
19
Full
Exbaast
11/15/94
1020-1120
22
Intermediate
Exhaust
11/15/94
1225-1300
21
Intermediate
Exhaust
11/15/94
1350-1415
20
Full
Exhaust
11/15/94
1622-1655
24
Fall
Exhaust
11/15/94
1730-1813
(Ambient Conditions
[Barometric Pressure (in. Hg)
27.02
26.97
26.93
26.91
26.89
[Ambient Temperature (°F)
50
55
57
55
51
Relative Humidity (%)
33.5
28.7
26.0
29.3
36.2
Ubs. Humidity (lb H20/1000 lb drv air)
2.8
2.9
2.8
2.9
3.1
[Engine Operating Conditions
Drake bores power (BHP)
1799
1569
1465
1724
1669
Load (%)
100
87
86
101
95
Engine Speed (rpm)
300
301
284
285
292
Fuel Flow (scCmin)
236
217
199
224
221
Heat Input (MMBtu/hr) (a)
14.2
13.1
12.0
13.5
13.3!
Heat Rate (Btu/BHP-hr, HHV)
8038
8474
8323
7961
8113
Heat Rate (Btu/BHP-hr, LHV)
7281
7676
7539
7211
7349
fNG HHV (Biu'scO
1021
1021
1021
1021
1021
ItNG LHV (Btu'scf)
925
925
925
925
925
IIExhaust Gas Conditions
ilVol. Flow (dscfm) - M 2
7501
7310
6833
7019
7172
(Vol. Flow (dscfm) - M19, Fd (b)
6983
6880
6243
6312
6528
iStack Gas Temperature (°F)
592
569
561
583
576
[Moisture (%V)
6.7
6.5
6.5
7.0
6.8
\Q2 {VcV dry )
14.9
15.3
15.3
14.6
14.9
£02 (%V dry)
3.8
3.6
3.5
3.9
3.7
[NOx (ppmvd)
870
309
364
1426
757
!CO (ppmvd)
63.6
77.9
74.0
57.0
65.3
THC (ppmvw)
958
1226
1092
895
973
Exhaust Emissions
fNOx (ppmvd @ 15°/«02)
857
326
380
1338
745
NOx (Ib/hr)
43.5
15.2
16.3
64.5
35.4
M)x (g/BHP-hr)
11.0
4.39
5.03
17.0
9.6:
[NOx (Ib/MMBtu)
3.05
1.16
1.35
4 77
2 65
fNOx (tons'vr)
191
66.6
71.2
282
155
CO (ppmvd @ 15% 02)
62.7
82.2
77.3
53.4
64.2
CO (Ib/hr)
1.94
2.34
2.01
1.57
1.86
CO (g/BHP-hr)
049
0.68
0.62
0.41
0.50
CO (Ib/MMBtu)
0.14
0.18
0.17
0.12
0.14
CO (tonvvr)
8.48
10.2
8.8
6.86
8.14
tTHC (ppmvd @ 15% 02)
1012
1384
1219
903
1027
fTHC (Ib/hr)
17.9
22.5
18.2
15 1
17.0
THC (g/BHP-hr)
4.51
6.49
5.62
3.98
4.61
[THC (Ib/MMBtu)
1.25
1.72
1.51
1.12
1.27
frHC (tons/vr)
78.3
98
79.5
663
74.3
a Based on HHV
b Used in emission calculations.
Note: Heating values based on 60°F reference.
M19 flow rates based on 68°F reference.
El 1-SUM.WK4
B-20
-------
GRI Campaign 6 - Station 6C CEM Results
Engine 9
C-B GMVA-IO
iTest Period
12
13
14
[Load Condition
Intermediate
Full
Full
Sampling Location
Exhaust
Exhaust
Exhaust
bate
11/11/94
11/12/94
11/12/94
ITest Time
1600-1800
1000-1405
1515-164$
[Ambient Conditions
Barometric Pi-essure (in. Hg)
26.59
26.49
26.47
[Ambient Temperature (°F)
65
57
59
Relative Humidity (•/•)
45.8
85.6
82.9
Ubs. Humidify (lb H2O/I000 lb dry air)
6.6
9.3
10.0
(Engine Operating Conditions
[Brake horespower (BHP)
1078
1232
1234
Load (%)
88
100
100
Engine Speed
-------
GRI Campaign 6 - Station 6A CEM Results
Engine 12
Clark HBA-5
Iteat Period
4
5
iLotd Condition
Low
Intel Mediate
[Sampling Location
Exhaust
ExJuust
bate
11/04/94
11/05/94
FTest Time
1702-1832
1345-IS02
Anbient Conditions
barometric Pressure (in. Hg)
26.37
26.47
[Ambient Temperature (°F)
51
71
[Relative Humidity (%)
92.3
23.2
[Abs. Humidity (lb H20/1000 ib drv air)
80
4.3
llBtiDt Opera tine Conditions
Brake borespower (BHP)
741
839
Load (%.)
75
84
Engine Speed (rpm)
297
301
Fuel Flow (scf/min)
140
150!
Heat Input (MMBtu/hr) (a)
8.5
9 0
Heat Rate(Btu/BHP-hr, HHV)
11612
10947|
Heat Rate(Btu/BHP-hr, LHV)
10516
99121!
!NG HHV (Btu/scf)
1025
1021'
NG LHV (Bru/scfl
928
924
Exhaust Gas Conditions
Vol. Flow (dscfm) - M 2 ;
4502
4473 ji
jVol. Flow (dscfm) - M19, Fd (b)
4759
4617 ,
IStack Gas Temperature {°F)
540
592!
|!Moisture (%V)
6 8
6.9;
!|02 (%V dry)
15.7
15 1
IC02 f%V dry )
3.3
3.7;
iNOx (ppmvd)
496
1030
ICO (ppmvd)
228
198
THC (uomv-v.) (c)
NA
1327!'
lExhaust Emissions i;
INOx (ppmvd (a 15% 02) ;
559
1053 j:
INOx (Ib/hr)
16.9
34.0
[NOx (g/BHP-hr) '
10.3
184
(NOx (Ib/MMBtu)
1.99
3.76 j1
INOx (tons/vr)
74 0'
149!
CO (ppmvd @ 15% 02)
258
202|
[CO (Ib/hr)
4 .73 :
3.97 ;i
ICO (g/BHP-hr)
2.90
2.15!
\CO (Ib/MMBtu) :
0.56 i
0.44
ICO (tons/vr)
20.7
17.4 ;
[THC (ppmvd @ 15% 02) ,
~i
1457,'
|THC (Ib/hr)
"1
16 4!
|THC (g/BHP-hr)
8.86
1THC (Ib/MMBtu)
"1
1.81 ;
fTHC (tons/vr)
71.8 !
a Based on HHV
b Used in emission calculations
c THC analyzer equipment failure A new instrument arrived on site late on 11/04/94.
NA « Not available
Note: Heating values based on 6Q°F reference
M19 flow rates based on 68°F reference
10/26/95
B-22
-------
GRI Campaign 6 - Station 6C CEM Results
Engine 13
C-B GMWC-10
Test Period
IS
16
17
18
23
Load Condition
Full
Full
Intermediate
Full
Full
Siimpling Location
fyliawt
Exhaust
Exhaust
Exhamt
Exhaust
Date
11/14/94
11/14/94
11/14/94
11/14/94
11/14/94
Test Time
1030-1130
1510-1549
1700-1745
1855-1925
2025-2100
Ambient Conditions
Binxnetric Pressure (in. Hg)
26.75
26.76
26.79
26.83
26.87
Ambient Temperature (*F)
62
66
64
55
51
Ri dative Humidity (%)
24.0
20.9
24.3
42.7
52.5
Am. Humiditv (lb H20/1000 lb drv air)
3.2
3.2
3.4
4.3
4.5
Eiaeine Operating Conditions
Biike horespower (BHP)
3352
3054
2822
3172
3092
Load (%)
96
95
88
91
92
Engine Speed (ipm)
250
230
230
249
240
Fviel Flow (scf/min)
459
421
389
440
426
Hisat Input (MMBtu/hr) (a)
27.8
25.5
23.6
26.6
25.8
H<»t Rate (Btu/BHP-hr, HHV)
8423
8478
8481
8527
8474
Hiat Rate (Btu/BHP-hr, LHV)
7625
7675
7677
7720
7671
NG HHV (Btu/icf)
1025
1025
1025
1025
1025
[NG LHV (Btu/scf)
928
928
928
928
928
Enhaust Gas Conditions
Vol. Flow (dscfin) - M 2
14164
12594
12422
13942
13360
Vol. Flow (dscfin) - M19, Fd (b)
13104
11888
11794
13514
12978
Stick Gas Temperature (°F)
653
651
615
621
617
Moisture (%V)
6.91
7.06
6.67
6.77
6.85
o:: (%v)
14.7
14.6
15.0
15.1
15.1
C()2 (%V)
3.84
3.96
3.66
3.68
3.72
NOx (ppmvd)
1695
2105
1425
1204
1449
CO(ppmvd)
114
119
949
105
103
!THC (ppmvw)
1710
1743
1759
1785
1754
Eihaust Emissions
jNOx (ppmvd @ 15% 02)
1605
1971
1432
1226
1464
INC)* (lb/hr)
159
179
120
116
135
NOx (g/BHP-hr)
21.5
26.6
19.3
16.7
19.8
NOx (Ib/MMBtu)
5.72
7.02
5.10
4.37
5.22
NOx (tons/vr)
697
785
527
510
590
CO (ppmvd® 15% 02)
108
111
95.4
107
104
(CO (lb/hr)
6.53
6.14
4.88
6.16
5.82
ICO (g/BHP-hr)
0.88
0.91
0.78
0.88
0.85
CCi (Ib/MMBtu)
0.23
0.24
0.21
0.23
0.23
CO (Umtvr)
28.6
26.9
21.4
27.0
25.5 !
THC (ppmvd @ 15% 02)
1739
1756
1895
1951
1902
THC(lMir)
60.0
55.5
55.4
64.4
60.9
THC (g/BHP-hr)
8.11
8.25
8.90
9.21
8.93 !
THC (lb/MMBtu)
2.16
2.18
2.35
2.42:
2.36 I
THC (tons/vrl
263
243
243
282
267!
a Ilased on HHV
b Used in emission calculations.
Not*: Heating values based on 60°F reference.
M19 flow rates based on 68°F reference.
01/30/96 E13-SUM.WK4
B-23
-------
GRI Campaign 6 - Station 6B CEM Results
Turbine
Solar Taurus
Test Period
6
7
8
Load Condition
Full
Full
Low
Saaaptiag Location
Exhaust
Exhaust
Exhaust
Date
11/07/94
11/0S/94
11/08/94
Teat Time
1709-1823
0915-1344
1700-1912
Ambient Conditions
Barometric Pressure (in. Hg)
26.51
26.50
26.47
Ambient Temperature (°F)
69
76
67
Relative Humidity (%)
44.2
47.2
45.6
Abs. Humidity (lb H20/1000 lb dry air)
7.5
104
7.2
Iurbiae Ooe ratine Conditio as
Brake Horsepower (BHP)
4803
4709
3934
Percent Load (*/•)
95
95
77
T5 Temperature (®F)
1401
1400
1305
Power Turbine Speed (rpm)
12458
12250
11567 j
Compressor Suction (psig)
463 7
478.3
471.8
Compressor Discharge (psig)
645.1
658 1
627.2!
Suction Temperature (°F)
76.5
76.8
79. r
Discharge Temperature (°F)
130.3
129.0
125.4
Fuel Flow (scf/min)
709.3
745 0
600 7
Heat Input (MMBtu/hr)
42.8
45.0
36.2
Heat Rate (Bfu/BHP-hr. HHV)
9040
9691
9355
Heat Rate (Btu/BHP-hr, LHV)
8187
8781
8475
InG HHV(Btu/scf)
1020
1021
1021
!NG LHV (Btu/scf)
924
925
925
Exhaust Gas Conditions
[Vol- Flow (dscfm) - M 2
29192
30964
27544
lVol. Flow (dscftn)- M19, Fd
25757
26581
23311:
Stack Gas Temperature f°F)
954
941
902
iMoisture (%V)
6.4
6 5
6.1
i02 (%V dry)
16.0
15 9
16.3
!C02 (%V dry)
3.2
3.2
29 '
jNOx (ppmvd)
71.5
70.8
56 0
iCO (ppmvd)
ND
ND
ND
!THC (opmvw)
ND
ND
ND
{Exhaust Emissions
NOx (ppmvd (a 15%02)
8b 5
84 1
72.3
iNOx ISO (ppmvd @ 15°/e 02)
91.3
91.8
76.4
tNOx (Ib/hr)
13.2
13 5
9.3:
(NOx (g/bhp-hr)
1.2
1.3
1.1
INOx (Ib/MMBtu)
0.3
0.3
0.3
iNOx (tons/vrl
57.8
59.0
40 9
CO (ppmvd @ 15% 02)
...J
—
[CO (Ib/hr)
—-
—
—i,
CO (g/bhp-hr)
—1
....
—i,
CO (IbWMBtu)
~~i
....
—i
CO (tons/vr)
—
1
THC (ppmvd @ 15% 02)
—
THC (ib/hr)
—
***ij
THC (g/bhp-hr)
....
THC (Ib/MMBtu)
—
-J!
THC (tons-Vr)
—
-J!
Note: Emission rates are based on the M-19 volumetric flowrate.
Turbine load is based on available load at ambient conditions during testing
Heating values based on 60°F reference.
M19 flow rates based on 68°F reference
T-SUM WK4
B-24
-------
Appendix C
CEMS Summary Data
This apjsendix presents a summary of the raw CEMS concentration data for all engine and
turbine test runs. Each summary includes the average, standard deviation, maximum, and
\ .minimum concentration (e.g., ppmv and percent volume) measured for each pollutant during
a given run. Pollutants measured include oxygen, total hydrocarbons, carbon monoxide,
carbon dioxide, nitrous oxides, and sulfur dioxide.
C-l
-------
Summary of CEM Concentrations for J
Daily Averages
Testing
C.1 Campaign 2
Date
Time
Statistic
02
THC
CO
C02
NOx
S02
(%)
(ppm)
(ppm)
(%)
(ppm)
(ppm)
3/12/94
1042-1557
Average
15.37
715.46
78.81
2.27
232.67
-0.04
Std. Dev.
0.11
117.57
14.28
0.05
34.54
0.58
RSD
0.01
0.16
0.18
0.02
0.15
-13.06
Max.
15.75
1197.27
108.46
2.39
330.25
1.19
Min.
15.13
333.58
45.88
2.11
144.23
-1.63
3/13/94
1240-1816
Average
11.44
220.22
355.46
3.86
1819.48
7.28
Std. Dev.
0.16
78.04
47.52
0.10
91.83
0.69
RSD
0.01
0.35
0.13
0.03
0.05
0.09
Max.
12.11
440.62
460.43
4.19
2092.46
8.91
Min.
11.08
31.51
247.75
3.58
1619.97
4.65
C-2
-------
CEM Summary tor GRIj
6/14/94
C.2 Campaign 3
Engine
Time
02
THC
CO
C02
NOx
(%) ,
(ppm)
(ppm)
(%)
(ppm)
Average
102
1600-2100
9.6
1666,1
202.7
7.0
1748.5
Std. Dev.
0.31
65.03
6.51
0.25
360.64
RSD
3.2%
3.9%
3.2%
3.6%
20.6%
Max
10.89
2006.05
232.29
7.41
2757.10
Min
8.83
1567.07
191.17
6.29
472.19
C-3
-------
CEM Summary for GRIi
6/15/94
Test
Engine
Time
02
THC
CO
C02
NOx
(%)
(PPm)
(ppm)
(%)
(ppm)
Full Load
Average
102
0832-1314
94
1677.1
216.5
7.3
1656.8
Std. Dev.
0.06
18.50
3.41
0.53
72.60
RSD
0.68%
1.10%
1 57%
7.21%
4.38%
Max
9.56
1725.49
2. 4.90
15.51
1803.66
Min
9.27
1627.18
208.91
7.02
1432.09
Reduced Load
Average
102
1437-1637
9.9
1802 6
246.5
7.1
824.8
Std. Dev.
0.08
39.10
2.33
0.07
75.09
RSD
0.86%
2.17%
0.94%
1.01%
9.10%
Max
10.05
2010.24
251.53
7.27
968.90
Min
9.69
1709.61
239.96
6.98
670.09
Low Load
Average
101
1831-1935
11.0
2269.2
208.7
64
259.0
Std. Dev
0.04
22.00
1.58
0.03
8.82
RSD
0.33%
0.97%
0.76%
0.53%
3.40%
Max
11.06
2321.03
211.47
6.45
279.40
Min
10.90
2225.10
205.26
6.31
233.16
C-4
-------
CEM Summary for GRI/
6/16/94
Test
Engine
Time
02
THC
CO
C02
NOx
(%)
(ppm)
(ppm)
(%)
(ppm)
Full Load
Average
101
0915-1405
9 5
19498
258.4
7.2
1297.0
Std. Dev.
0.13
29.62
5.05
0.12
159.91
RSD
1.36%
1.52%
1.95%
1.72%
12.33%
Max
9.81
2027.29
268.05
7.41
1621.88
Min
9.26
1891.11
246.73
6.91
936.34
Load Increase
Average
101
1415-1806
9.3
1879.0
257.6
7.3
1554.7
Std. Dev.
0.04
21.20
1.82
0.05
45.99
RSD
0.46%
1.13%
0.71%
0.68%
2.96%
Max
9.36
1944.55
263.07
7.39
1708.45
Min
9.13
1830.26
252.55
7.14
1452.49
C-5
-------
CEM Summary for GRIj
6/18/94
Test
Engine
Time
02
THC
CO
C02
NOx
(%)
(ppm)
(ppm)
(%)
(ppm)
Full Load
Average
4
0925-1115
14.7
112B.9
53 0
4.2
1246.3
Std. Dev.
0.04
27.81
0.86
0.02
37.22
RSD
0.2%
2.5%
1.6%
0.6%
3.0%
Max
14.75
1222.37
55.81
4.22
1330.32
Min
14.62
1078.03
50.70
4.11
1176.99
Reduced Load
Average
4
1345-1523
15.4
1264.6
61.8
3.8
390.7
Std. Dev.
0.03
52.73
2.55
0.03
17.74
RSD
0.2%
4.2%
4.1%
0.7%
4.5%
Max
15.45
1382.17
68.69
3.81
427.21
Mln
15.33
1124.32
58.80
3.71
358.02
Low Load
Average
2
1800-1900
15.1
3116.8
124.5
4.0
42.8
Std. Dev
0.02
74 50
3.29
0.02
2.03
RSD
0.1%
2.4%
2.6%
0.5%
4.7%
Max
15.10
3336.29
132.56
4.02
47.74
Min
15.02
2961.45
120.28
3.92
38.75
C-6
-------
CEM Summary for GRIj
6/19/94
Engine
Time
02
THC
CO
C02
NOx
(%)
(PPm)
(ppm)
(%)
(ppm)
Average
2
1105-1428
13 0
827.8
81 0
5 8
1286.5
Std. Dev.
0.04
19.32
0.90
0.04
36.13
RSD
0.3%
2.3%
1.1%
0.6%
2.8%
Max
13.14
894.70
82.76
5.82
1339.21
Min
12.95
792.43
7B.49
5.68
1192.30
Average
2
1630-2018
13.0
818.2
804
5.0
1366.3
Std. Dev.
0.02
13.55
1.27
0.04
53.28
RSD
0 1%
1.7%
1.6%
0.7%
3.9%
Max
13.07
851.15
82.82
5.08
1428.91
Min
12.99
782.70
78.55
4.93
1219.38
\
C-7
-------
CEM Summary for GRIi
6/20/94
Engine
Time
02
THC
CO
C02
NOx
(%)
(ppm)
(ppm)
(%)
(ppm)
Average
2
1240-1747
13.2
864.5
83.7
5.1
994.3
Std. Dev.
0.14
31.27
2.33
0.08
239.88
RSD
1.0%
3.6%
2.8%
1.5%
24.1%
Max
13.42
958.42
86.27
5.24
1408.04
Min
12.99
807.50
78.57
5.00
807.84
V \
C-8
-------
Run
Engine
Sampling
Load
Time
Number
Location
Timing
1
Waukesha
After NSCR
Full
1146-1345
Average
SD
RSD
Max
Min
2
Waukesha
After NSCR
Full
1424-1722
Average
SD
RSD
Max
Min
3
Waukesha
Betofe NSCR
Full
1805-2028
Average
SD
RSD
Max
.
Mm
CEM Summary for GRI - Camnainn A
8/23/94
Tamb
RH
BP
02
C02
CO tow
CO high
NO*
THC
FTIR
CF)
(%I__
(in Hg)
J*> _
(%)
(ppm)
(ppm)
(ppm)
(ppm)
(mm Hg)
07 25
35 20
29 54
0 04
11 69
68 53
69 32
8 03
607 41
693 51
1 62
2 87
001
0 01
0 01
1610
17 54
067
44 70
1 30
1 85%
8 15%
0 03%
13 80%
010%
23 49%
25 31%
8 30%
7 36%
0 19%
91 35
39 00
29 55
0 06
11 72
133.35
13910
10 34
750 90
697 56
84 24
28 53
29 52
0 03
11 67
33 96
516
650
455 33
691 04
86 61
40 13
29 49
0 06
11 70
69 47
63 94
8 30
639 55
681 22
2 81
4 36
001
001
0 04
19 03
16 46
0 36
40 02
3 40
3 24%
10 87%
0 03%
24 89%
0 33%
27.39%
25 74%
427%
6 26%
0 50%
90 70
48 33
29 51
0 09
11 76
197 70
162 94
10 09
744 77
690 50
81 39
33 62
29 48
0 03
11 64
36 29
26 52
7 33
493 68
675.16
74 14
65 35
29 47
0 42
11 22
3742 19
3713 63
2042 50
1048 32
605 18
2 83
7 58
0 00
001
0 02
eo 48
82 07
24 67
35 33
6 85
3 81%
11 59%
0 01%
1 78%
0 21%
2 15%
2 21%
087%
3 37%
1 00%
79 55
76 10
29 48
0 44
11 20
3996 55
3977 39
2920 88
1191 94
712 04
70 34
52 32
29 47
0 41
11.17
3557 47
3504 53
2794 23
984 52
680 70
o
u
CQ
3
-------
CEM Summary for GRI - Campaign 4
8/24/94
Run
Engine
Sampling
Load
Time
Tamb
Number
Location
Timing
(°F)
4
Waukesha
Before NSCR
52 6 %
1020-1201
Average
06 86
SD
1 92
RSD
2 22%
Max
91 52
Mm
83 63
5
Waukesha
After NSCR
52%
1210 1306
Average
92 43
SD
0 59
RSD
0 63%
Max
94 47
Win
90 96
0
1
BP
02
C02
CO low
CO high
NOx
THC
FTIR
{in Hg)
(%)
W
(ppm)
(ppm)
(ppm)
(ppm)
(mm Hg)
29 55
0 35
11 53
2755 76
2690 29
2542 36
1394 37
685 00
0 00
0 01
0 05
130 95
129 24
21 65
513 74
0 86
001%
2 50%
041%
4 75%
4 80%
0 85%
36 04%
013%
29 55
0 36
11 60
3212 48
3150 38
2579 43
2735 90
666 86
29 54
0 33
11 36
2429 60
2364 63
247594
950 24
68272
29 54
-0 03
11 99
35 76
30 69
35 33
046 39
716 23
0 00
001
0 03
23 93
41 81
16 53
396 46
31 41
001%
-21 66%
0 28%
66 92%
136 22%
46 77%
47 08%
4 39%
29 54
-0 02
1207
107 35
173 82
87 09
2029 04
842 62
29 53
-0 05
11 92
-7 62
-76 23
•17 62
208 99
669 30
RH
(%)_
36 69
2 65
7 23%
41 09
30 14
27 16
1 37
5 03%
30 51
22 51
-------
Run
Engine
Sampling
Load
Time
Number
Location
Timing
7
Engine 4
Before Cat
96 • 90 %
1705-1906
Average
SD
RSD
Max
Min
o
/
CEM Summary for GRI ¦ Camoalan 4
8/25/94
Tamb
RH
BP
02
C02
CO low
CO high
NOx
THC
FTIR
m
(%)
(in Hg)
(%)
(*)
(ppm)
(ppm)
(ppm)
(Ppm)
(mm Hg)
05 10
37 83
29 44
15 54
^ 206
162 22
104 24
39 16
1218 09
680 03
2 26
3 31
0 01
0 07
0 02
3 52
6 20
2 41
27 61
1 01
2 65%
0 74%
0 03%
0 44%
0 59%
2 17%
5 95%
6 14%
2 27%
015%
08 38
43 03
29 45
15 63
2 09
160 41
11990
43.73
1260 95
684 52
00 49
33 10
29 42
15 38
2 03
153 64
07 00
35.39
1146 39
677 51
-------
Run
Engine
Sampling
Load
Time
Number
Location
Timing
0
Engine 4
After Cat
97-100%
1051-1226
Average
SD
RSD
Max
Min
9
Engine 4
Before Cat
92-94%
1310-1403
1419-1438
1452-1537
Average
SD
RSD
Max
Min
10
Engine 4
After Cat
88-90%
1620 1821
Average
SD
RSD
Max
Min
0
1
N)
CEM Summary for GRI - Campaign 4
8/26/94
Tamb
RH
BP
02
C02
CO low
CO high
NOx
THC '
FTIR
m
<%> .
(in Hg)
(%)
(%)
(ppm)
(ppm)
(ppm)
(ppm)
(mm Hg)
84 39
47 78
29 47
15 36
3 03
1419
23 57
44 04
1357 57
683 24
1 78
2 74
0 01
0 02
0 01
0 36
2 28
2 58
28 44
0 80
2 11 %
5 74%
0 03%
0 15%
031%
2 56%
9 69%
5 87%
2 09%
012%
87 98
53 56
29 49
15 40
3 06
15 03
29 54
50 00
1420 70
684 91
81 31
42 46
29 46
15 31
3 01
1317
17 64
40 03
1304 26
601 63
89 04
40 48
29 47
15 44
2 96
180 70
154 09
34 14
1558 79
681 47
1 25
1 93
0 03
0 03
001
951
16 85
2 87
93 04
1 88
1 41%
4 77%
0 10%
0 20%
0 40%
5 26%
10 94%
8 41%
5 97%
0 28%
92 11
46 10
29 49
15 53
2 98
198 63
200 60
37 87
1746 52
687 80
85 65
3558
29 45
15 38
2 91
17098
110.15
1503
1421.13
679 42
86 17
42 55
29 45
15 47
2 96
12 71
19 78
33 07
1567 44
681 52
1 62
3 08
0 01
0 01
0 02
0 47
2 63
0 86
29 01
1 29
1 88%
7 24%
0 04%
0 07%
0 57%
3 69%
13 29%
2 61%
1 85%
019%
88 85
49 92
29 47
15 52
2 98
13 76
25 20
34 80
1623 89
686 47
82 42
37 93
29 42
15 44
2 90
11.49
12 95
31 14
1501 66
678 10
-------
CEM Summary for GRI - Camiialan i
8/27/94
Run
Engine
Sampling
Load
Time
Tamb
Number
Location
Timinq
. _..rF)
91 36
2 92
3 20%
95 94
11
Engine 8
86-90%
1108-1503
Average
SD
RSD
Max
Min
84 92
12
Engine 8
82%
1639-1921
Average
SD
RSD
Max
86 01
2 86
3 33%
90 21
Min
80 30
0
1
BP
02
C02
CO low
CO high
NOx
THC
FTIR
(,nH9) _
(%) .
(%)
(ppm)
(ppm)
(ppm)
(ppm)
(mm Hg)
29 45
11 28
5 36
351 66
352 60
69 74
1936 91
682 53
0 02
0 32
0 11
9 43
10 43
5 22
178 69
3 34
0 07%
2 85%
2 09%
268%
296%
7 49%
9 23%
0 49%
29 48
11 39
5 44
372 82
37669
76 49
2345 82
729 94
29 42
6 39
369
278 38
251 10
19 78
1636 11
678 87
29 41
11 44
5 22
385 36
374 41
58 66
3290 45
698 57
0 00
0 06
0 05
25 34
23 52
9 49
397 77
27 93
001%
0 52%
1 01%
6 57%
6 28%
16 18%
12 09%
4 00%
29 42
11 56
5 34
41898
400 75
124 14
5125 38
764 01
29 40
11 23
5 11
242 53
208 69
48 93
2749 41
675 28
RH
(%)_
32 73
6 29
19 20%
46 14
21 33
35 03
3 30
9 42%
40 53
28 34
-------
CEM Summary for GRI - Campaign 4
8/28/94
Run
Engine
Sampling
Load
Time
Tamb
RH
BP
02
C02
CO low
CO high
NOx
THC
FTIR
Number
Location
Timing
rn
(%)
(in Hg)
(%)
(%)
(PPm)
(pprn)
(ppm)
(ppm)
(mm Hg)
13
Engine 9
87 - 89 %
1254-1520
Average
94 09
27 76
29 46
8 27
6 95
137 59
106 70
3351.43
947 38
682" 57
SO
1 15
1 60
001
0 08
0 04
418
14 88
73 49
35 68
0 95
RSD
1 22%
5 77%
0 03%
0 97%
0 63%
3 04%
13 94%
2 19%
3 77%
014%
Max
96 92
30 76
29 48
8 43
7 03
144 72
137 28
3460 78
1051 58
685 29
Min
92 01
24 44
29 45
8 10
6 85
129 15
51.07
3217 99
875 95
679 15
o
t—»
4k.
-------
/
4 ¦
CEM Summary for GRI - Campalan 4
8729/94
Run
Engine
Sampling
Load
Time
Tamb
RH
BP
02
C02'
CO low
CO high
NOx
THC
FTIR
Number
Location
Timing
(T)
(%)
(in Hg)
(%)
<*>
(ppm)
(ppm)
(ppm)
(ppm)
(mm Hg)
14
Engine 9
Before SCR
92%
0850-0932
Average
77 11
52 06
29 47
0 56
6 93
141 37
69 83
3041.78
930 04
682 47
SD
1 49
2 59
0 00
0 06
v 0 03
2 31
19 95
35 59
47 54
0 55
RSD
1 94%
4 98%
001%
0 65%
v 0 46%
1 63%
28 57%
1 17%
507%
000%
Max
80 33
56 67
29 47
8 65
6 97
145 09
12024
3095 63
1035 68
683 70
Min
74 71
46 17
29 47
8 45
6 07
136 65
892
2960 03
833 32
681 59
15
Engine 9
After SCR
90 - 91 %
0959-1330
Average
86 54
33 12
29 45
8 60
6 78
103 02
56 74
67657
948 62
663 85
SD
3 24
4 92
0 02
0 06
0 05
4 56
9 25
63 67
95 90
8 29
RSD
3 74%
14 04%
0 07%
0 68%
0 67%
443%
16 30%
941%
1011%
1 21%
Max
92 28
44 71
29 47
0 76
6 04
11425
97 42
764 80
1358 76
731 61
Min
80 00
24 93
29 41
8 51
6 67
95 79
39 94
420 92
784 69
674 80
16
Engine 9
After SCR
1413-1549
Average
93 11
31 75
29 39
0 56
6 80
101.70
57 17
775 26
1001 00
687 52
SD
1 23
1 31
0 01
0 10
0 05
3 24
8 23
26 92
91 33
18 95
RSD
1 32%
4 12%
0 02%
1 15%
0 73%
3 19%
14 39%
3.47%
9 12%
2 76%
Max
96 16
34 25
29 40
0 85
6 99
111 61
60 98
833 80
1253 71
743 65
Mm
91 15,
28 41
29 38
0 24
6 65
90 46
26 36
688 40
823 71
674 88
17
Engine 9
Before SCR
1613-1700
Average
90 62
31 65
29 37
8 33
7 10
125 84
49 46
3339 11
099 64
678 10
SD
0 07
1 08
0 02
0 02
0 04
2 82
20 36
30 06
40 90
7 36
RSD
0 96%
3 42%
007%
0 29%
0 63%
2 24%
41.16%
0 90%
455%
1 06%
Max
95 50
35 71
29 52
8 39
7 14
142 29
82 32
3381 14
1017.98
602 40
Min
8930
30 20
29 37
0 29
6 02
12251
-10 32
3194.57
01400
635 71
-------
Run
Engine
Sampling
Load
Time
Number
A
Engine 0
Location
Timing
99 %/0°
0745-015
Average
SD
RSD
Max
Win
B
Engine 0
91 %/8°
0903-0944
Average
SD
RSD
Max
Min
C
Engine 0
09 % (5°
1013-1042
Average
SD
RSD
Max
Min
D
Engine 0
92-96 %/5°
1100-1137
Average
SD
RSD
Max
Min
E
Engine 0
95-96 %/0°
1150-1220
Average
SD
RSD
Max
Min
CT
Engine 6
Full / 11B
1234-1251
Average
SD
RSD
Max
Min
G
Engine 8
Red /11°
1307-1339
Average
SD
RSD
Max
Min
H
Engine 4
95 %
1555-1610
Average
SD
RSD
Max
Min
t
Engine 4
Reduced
1656-1735
Average
SD
RSD
Max
Min
CEM Summary (or GRI • Campaign 4
8/30/94
Tamb
RH
BP
02
C02
CO lew
CO high
NOx
THC
FTIR
m
(in Hg)
(%)
(%)
(ppm)
(ppm)
(ppm)
(ppm)
(mm Hg)
72 90
66 30
29 41
11 31
5 19
377 51
393 65
64 55
2333 04
600 80
0 75
1 72
0 00
0 02
0 01
4 12
5 72
1 67
47 07
1 45
1 03%
2 59%
001%
0 14%
022%
1.09%
1 45%
259%
205%
021%
74 10
70 97
29 42
11 34
5 22
307 06
411.07
60 74
2454 47
696 09
71 65
62 06
29 41
11 26
5 17
365 76
365.65
61 25
2219 26
685 78
77 93
55 50
29 42
11 48
5 06
419 34
425 85
53.30
3560 48
609 59
1 32
2 67
0 00
0 02
0 01
3.80
9 53
1 72
53 36
1 23
1 69%
4 B2%
001%
0 15%
0 23%
0 91%
224%
3 22%
1 50%
0.10%
00 30
61 47
29 43
11 52
5 10
426 77
519 90
50 16
3600 59
693 91
_ Z5_59
50 56
29 42
11 42
5 03
407 70
415 31
50.07
3386 51
607 02
02 24
47 02
29 43
11 56
5 01
364 03
308 30
40 67
4142 90
689 46
1 11
1 96
0 00
0 03
0 02
7.71
9 50
2 71
107 30
1 43
1 35%
4 17%
001%
0 23%
0 38%
2 12%
2 47%
5 50%
259%
021%
84 28
52 10
29 43
11 60
5 08
374 61
447 90
70 74
4667 06
694 51
79 49
43 33
29 42
11 44
4 98
320 56
353 98
45 96
3932 70
686 14
84 51
43 15
29 42
11 37
5 13
331 21
367 09
55 69
2096 78
689 20
1 43
2 03
0 00
0 05
0 03
12 25
9 38
1 99
104 35
1 12
1 69%
4 70%
001%
0 40%
0 50%
3 70%
2.55%
3 58%
3 60%
016%
07 24
47 79
29 43
11 44
5 22
394 33
40601
63 60
3075 36
693 26
01 47
39 29
29 42
11.21
5 10
315.77
350 36
51.00
2616 88
606 50
06 09
40 68
29 41
11 21
5 23
393 70
403 48
60 02
2682 76
609 23
1 11
1 36
0 00
0 04
0 02
4 66
5 42
2 17
9978
1 21
1 29%
3 35%
0 01%
0 32%
0 33%
1 10%
1 34%
361%
3 72%
0 10%
00 70
44 13
29 41
11 20
5 29
415.70
421 50
72 30
2834 35
692 07
03 78
37 13
29 41
11 02
5 19
302 29
304 33
56.12
213912
686 86
89 00
37 77
29 40
11 09
5 30
390 71
405 10
66 97
1925 53
600 92
0 71
0 84
0 00
0 03
002
6 23
5,00
206
64 69
1 15
0 79%
2 23%
001%
0 27%
031%
1 56%
1 41%
3 08%
3 36%
017%
90 30
39 51
29 40
11 17
5 34
40921
426 24
71 43
2033 96
692 93
07 70
35 94
29 40
11 01
5 26
381.11
391 54
62 36
1792 76
607 13
09 62
36 36
29 39
11 33
5 12
451 19
457 49
55 12
3298 08
680 09
0 76
0 90
0 00
0 02
0 01
3 89
6 70
1 24
39 34
1 47
0 05%
2 47%
001%
0 14%
0 10%
006%
1 46%
2.25%
1 19%
021%
91 30
30 75
29 40
11 37
5.15
461 66
404 10
58.70
3425 83
694 74
00 33
3402
29 39
11 29
5.09
440 04
434 40
5232
319518
686 35
05 40
42 20
29 36
15 26
2 92
17804
150 02
36 89
1425 52
686 48
0 72
1 10
0 00
0 01
0 01
231
512
347
22 56
1 43
0 84%
261%
0 01%
0 09%
0.27%
1.30%
324%
9 41%
1 58%
021%
86 60
44 70
29 36
15 29
294
102.37
170 54
40 27
1513 57
693 40
03 09
40 54
29.36
15 22
290
170 37
142 88
18 28
1374 67
684 29
03 51
44 76
29 35
15 51
201
237 35
272 01
20 22
1948 03
685 40
0 42
0 60
0 00
0 01
001
222
6 25
0 27
2490
2 09
051%
1 96%
0 00%
0 07%
0 29%
094%
2 30%
1 34%
1 28%
031%
04 69
46 62
29 35
15 54
2 03
242.18
307 60
20 73
2009 62
696 40
0272
42 63
29 35
15 48
2.79
229 84
240 72
19.65
187655
683 44
-------
CEM Summary for GRI - Campaign 5
10/05/94
Test
Engine
Load
Time
Tamh
PM
BP
02
C02
00 !isw
CC uign
NOx
li-ie.
MlR
Number
Timing
fF)
(%)
(in Hg)
_<%) _
(%)
(ppm)
(ppm)
(ppm)
(Pf*n)
(mm Hfl)
Average
57 24
51 26
29 34
17 67
i 97
1321
12 45
41 39
1 52
684 09
SD
1 22
395
0 02
0 03
0 02
260
3 45
038
1 96
0 89
3
Turbine
Full
1230-1755
RSD
7 13%
7 71%
0 06%
0 15%
1 26%
19 71%
27.73%
0 92%
129 41%
0 13%
Max
61 06
64 30
29 37
17 75
2 02
21 7B
21 10
42 43
803
689 15
Min
55 09
43 46
29 32
1760
1 92
8 31
657
40 35
005
682 43
Average
51 40
75 12
29 35
" 17 65
1 99
16 64
1677
39 60
1 25
68514
SD
1 93
6 12
0 01
0 03
0 01
2 24
2 33
050
1 22
7 70
4
Turbine
Full
1843-2133
RSD
3 75%
8 14%
0 03%
0 15%
0 65%
13 47%
1388%
1 27%
97 44%
1 12%
Max
55 29
86 99
29 36
17 69
2 03
22 70
22 16
41 65
690
731 61
Min
48 34
64 26
29 33
17 58
1 95
11 95
11 16
38 40
008
681 54
-------
Engine
Test
Test
Ambient
Number
Number
Condition
Time
Temperature
<*F)
Average
61 61
Std Deviation
3.83
Engine 10
Full
1000-1224
RSD
621
Max
6632
Min
54.74
Average
50.51
Std Deviation
0.15
Engine 10
3
Low
1448-1603
RSD
029
Max
50.84
Min
5016
Average
50 58
Std Deviation
061
Engine 12
4
Low
1702-1832
RSD
1 20
Max
52.34
Min
49.74
0
1
I—>
00
CEM Summary for 1
GRI Campaign
11/04/94
I 6A
Relative
Barometric
Fuel
Humidity
Pressure
02
C02
CO
Pressure
NOx
THC
FTIR
(%)
(in Hg)
(%)
(%)
(ppm)
(psi)
(ppm)
(ppm)
(mm Hg)
62 65
26 36
1692
2 65
51 36
4.15
596.76
-3.90
629.71
14 68
001
0 04
0 01
2 41
229
24.02
1.64
0.77
23.43
0.03
0.21
0.52
469
55.17
4.03
-42.11
012
93 49
2637
1698
2.68
56 03
545
638.85
010
631 97
46.39
26 34
16 83
2 61
45 70
-0.46
554.71
-769
627 71
92.97
26 35
17 33
2 41
59 14
-0.35
219.06
-6.62
62957
1.64
001
003
002
0.95
0.01
8.54
1.44
1 27
1.76
003
019
061
1 61
-1 74
3.90
•21 68
020
95 86
26.37
17.39
2.45
61.99
-033
241 67
-337
63631
89 84
26 34
1724
238
56 94
-0.36
203.69
•1288
627 48
92.28
26 37
15 67
333
" 22828
-0 35
495 80
-4 06
62931
2 20
001
003
001
315
0.01
13.29
1.48
0 84
2 38
0 04
018
0.37
1.38
-1 48
268
36 48
0.13
97.21
2637
1573
3.36
237.44
-0 34
530.77
-1.16
631 41
87.84
26.34
1562
331
221.08
-0 36
465.21
-7.19
627.77
O
in
O
o»
3
TJ
tt
(Q
3
o>
-------
Engine
Test
Test
Ambient
Number
Number
Condition
Time
Temperature
m
Average
62 35
Std Deviation
4 04
Engine 10
2
Full
0935-1209
RSD
7.77
Max
7057
Min
56 26
Average
71 45
Std Deviation
323
Engine 12
5
Full (80%)
1345-1802
RSD
4 53
Max
7647
Min
6601
0
1
SO
CEM Summary for 11/05/94
GRI Campaign 6A
Relative
Barometric
Fuel
Humidity
Pressure
02
C02
CO
Pressure
NOx
THC
FTIR
(%>
(in Hg)
(%>
(%)
(ppm)
(psi)
(ppm)
(ppm)
(mm Hg)
2927
26 50
1677
2.69
5677
-336
820.38
595.37
632 98
346
002
0 09
0.04
3.31
8.33
43.69
34.87
095
11 81
007
051
1.49
5 84
-248.13
5.33
5 86
0.15
36.18
26 59
1692
278
64.23
-0.29
911.21
683.42
635.90
19.75
2647
16.62
2 63
37.92
-27.87
764.73
525.41
630.75
2323
2647
15.13
3 67
197.54
-0.51
1029 54
1326 80
633 02
427
001
004
002
4.01
004
28.63
51 29
064
1837
0.05
026
067
2 03
-7.65
2.78
3.87
010
3281
26 49
1521
3.73
208 02
-0 45
1079.25
1486.21
634 96
14.83
26.45
15 05
3.62
187.57
-0.56
953.95
1183.53
631.38
-------
Engine
Number
Engine 15
Engine 15
N)
O
CEM Summary for'
GRI Campaign
11/10/94
I 6C
Barometric
Fuel
Pressure
02
C02
CO
Pressure
MOx
THC
FTIR
(in Hg)
(%)
(%)
(ppm)
(psi)
(ppm)
(ppm)
(mm Hg)
26 72
15.00
368
71.18
-30.71
559 72
970.78
630 30
004
0.10
0.04
0.90
0.00
54.99
38.56
1.41
0.15
0.65
1.19
1.27
-000
982
3.97
0.22
26 78
15.17
3.74
75.93
-30.71
662 94
1105.54
634.52
26.66
14 85
3.60
68.70
-30.71
441.92
878.23
627.02
26 64
1483
369
71.05
-30.71
637.87
957.07
628.36
0.00
003
003
1.00
000
22.04
32.04
2.21
001
018
0.71
1 40
-0.00
345
3.35
0.35
26 65
14 88
3 73
73.13
•3071
735 07
1055.16
651.31
26 63
14.78
3.63
68.53
-30.71
589.95
885.93
625.64
-------
Engine
Test
Test
Ambient
Number
Number
Condition
Time
Temperature
CF)
Average
53 06
Std Deviation
2.34
Engine 15
11
Low
0940-1140
RSD
4.41
Max
57 02
Min
4875
Average
6450
Std Deviation
1 49
Engine 9
12
Low
1600-1800
RSD
232
Max
66 80
Min
61 83
0
1
N)
CEM Summary for 11/11/94
Gfti Campaign 6C
Relative
Barometric
Fuel
Humidity
Pressure
02
C02
CO
Pressure
NOx
THC
FTtR
(%)
(in Hg)
<%)
(%)
(ppm)
G»Q
(ppm)
(ppm)
(mm Hg)
6188
26 66
15.53
3 36
76.23
-30.72
277 99
1300.42
631.91
4.70
000
0.05
004
0.95
001
922
288.31
2.82
7.60
002
0.30
1.15
1.25
-0.03
332
22.17
0.45
70.64
26 66
1565
3 42
78.66
-30.70
298 37
1891.78
64082
54.07
26.64
1545
3.30
73.37
-30.73
251.74
556.29
626.59
4576
26 59
15.06
359
69.20
295.90
299.28
2623 63
660 48
397
0.01
0 02
0 02
1.20
0.53
6.74
67.18
3.12
8 68
004
0 16
0.42
1 74
0.18
225
256
047
51 58
26 60
15.12
3.63
72 20
296.93
31617
277459
668.70
39 94
26.57
1499
354
66.04
292 36
281 67
2405.36
641.84
-------
/
/
CEM Summary for 11/12/94
GRI Campaign 6C
Engine
Number
Engine 9
Engine 9
Test
Test
Ambient
Relative
Barometric
. .
Number
Condition
Time
Temperature
Humidity
Pressure
02
CF)
(%)
(in Hg)
(%)
Average
56 63
85.60
26 49
1455
13
Full
1000-1405
Std Deviation
3 09
8 57
0 02
0.05
RSD
546
1001
009
0.35
Max
61 05
96.59
26 56
14 68
Min
52.13
73.15
26.46
14.46
Average
59 42
82.92
26.47
14 47
14
Full
1515-1645
Std Deviation
080
5.70
001
001
RSD
1 35
6.88
003
008
Max
60 45
91 61
26 48
14 49
Min
5818
76.05
26 45
14 43
to
Fuel
CO
Pressure
NOx
THC
FTIR
(ppm)
(psl)
(ppm)
(ppm)
(mm Hg)
67.64
171.89
395.93
1342.15
627.75
1 03
835
19.79
79.40
1.24
1 52
486
5.00
5.92
0.20
72 09
21232
442.61
1516.75
631.10
64.59
104.80
352.54
1123.89
624 89
67.11
5512
390 53
1308 51
626 26
1 02
62 75
11.86
6478
1.37
1 52
11385
304
4.95
0.22
69 87
167 41
421.93
1462.17
629.48
64.70
023
357.72
1101.84
622.67
-------
"Engine
Number
Test
CondHfen
Lew
FiJ Speed
low
Low Spu
Averejt
Std Delation
RSD
Aveng*
Sid Deviation
RSD
Mia
Mn
SM DtMofi
RSD
Avervga
SM Delation
RSD
Anient
Temperetin
£Q
50 39
0 83
1 85
5237
48.71
54 97
ON
t 78
56 64
52 51
57 16
066
1 15
58 11
_ 55 61
54 74
1 54
261
58 29
53 15
ReWive-
ttiridHy
__.(*]
33 50
1 37
Sid Deviation
RSD
50 65
077
1 52
52 67
49 73
O
oiroiw
CEM Summary for 11/15/94
GRI Campaign 6C
Suction
Pud
Fuel
fuel
0J«W
En*.
Speed
CO
NO*
TMC
FTIR
Prvawre
PrewuredP
Preeewe
Prvnure
<*)
(PP*">
(pp
(PP")
(mm Hg)
<*>
(VtH20)
(Ptf)
<*F)
(f*>
rn
14 91
3 76
63 64
870 04
958 49
638 58
46071
42 33
90 23
5741
707 43
296 79
210 84
002
002
2 15
32 72
83 13
1.10
063
0.11
010
038
026
662
1 14
0 16
056
3 38
3 76
8 67
017
0 14
027
019
0.65
004
621
054
1497
3 82
66 97
958 53
1319 64
643 38
462 08
42 77
90 55
S6.11
706.04
300.73
213 70
1464
3 71
58 13
784 33
817 26
635 93
459 85
4195
49.92
96 83
706.96
296 30
207 70
1531
3 57
77 88
308 58
1225 79
637 41
461.39
3832
45 57
60 18
706 40
298 76
195 66
0 03
0 02
339
16 21
116 4S
091
019
0.14
012
017
020
977
1 10
0 19
0 42
3 07
525
950
014
004
0.37
029
0 26
003
026
056
1551
360
82 74
355 08
1600 06
64068
481 79
38 68
45 91
60 45
700 89
301 90
196 41
1525
352
71 63
261 16
886 60
635 54
460 34
37 49
45 23
59 80
709 99
29S62
161 64
3 54
73 99
363 63
1091 94
636 11
461 26
35 06
41 28
61.58
704 82
263 60
16687
002
002
214
16 87
100 54
1.28
012
015
013
017
024
062
0 82
015
054
289
464
9 21
020
003
043
031
028
003
022
77 64
406 67
1417 61
640 66
461 61
35 49
4155
61.64
709 41
265 26
1519
3 50
67 87
322 23
892 39
633 56
460 92
34.71
40.92
61 25
704 29
263 39
166 32
1461
56 97
1426 37
895 18
635 84
457 91
40 27
4*11
61.20
709 52
263 98
006
0 01
1 91
70 53
44 65
234
1 63
021
022
021
254
1.11
107
040
038
3 35
4 94
499
0 37
036
051
048
045
036
636
059
1501
396
60 61
1499 52
1066 61
652 17
470 02
4136
46 40
•2 61
724 42
290 67
1454
3 84
52 06
955 00
826 99
633 92
457 35
39 49
46 44
00 69
704 53
282.19
160 79
1490
3 71
65 29
757 49
973 40
635 28
458 27
»»
4*4*
60 25
7D6.S1
290.76
169 39
003
003
218
24 78
75 79
064
085
0.11
012
012
0 47
061
093
018
0 72
334
3 27
7 79
013
014
02»
025
020
007
021
14 97
3 77
69 19
854 84
1250 52
637 99
460 05
MM
40 74
6041
707 76
293 24
19221
14 83
3 65
59 52
898 06
828 67
633 04
457 59
38 92
4610
56 96
709 69
269 26
166 57
1115*SUM.WK4
-------
CEM Summary for 1
GRI Campaign
11/14/94
I 6B
Engine
Test
Test
Ambient
Relative
Number
Number
Condition
Time
Temperature
Humidity
CF)
(%)
Average
62 08
24 82
Engine 13
15
Full
1030-1120
Std Deviation
1 51
2 40
RSD
244
966
Average
65 80
"20 91
Engine 13
16
Full/
1510-1549
Std Deviation
1 76
1 20
Low Speed
RSD
2 68
5 72
Average
63 79
24 25
Engine 13
17
Low/
1700-1745
Std Deviation
1 63
248
Low Speed
RSD
2 56
1022
Average
5463
42 74
Engine 13
18
Low
1855-1925
Std Deviation
038
1 10
Full Speed
RSD
0 70
257
Average
50 72
" 52 48
Engine 13
23
Intermediate
2025-2100
Std Deviation
0 43
112
Int Speed
RSD
086
2 14
o
Fuel
02
C02
CO
Pressure
NOx
THC
FTIR
(%)
(%>
(ppm)
(psi)
(ppm)
(ppm)
(mm Hg)
14 66
364
114.16
000
1696.92
1705 95
631 89
002
0.03
2.36
000
20.85
86.50
1 13
0 13
091
2.06
ERR
1 23
507
018
1460
396
11851
109 12
2104.70
1742 84
63257
0 02
001
259
80 50
18.07
6851
104
0 16
0.22
2.18
73.77
0.86
393
016
15 03
3 66
94 90
000
1425.03
1759 48
63339
0 03
001
248
0.00
3387
128.60
868
0 18
035
262
ERR
2.38
7.31
1.37
15 11
3.68
104.58
000
1203 53
1784.69
63376
0 02
003
2.40
0.00
31.47
156.46
102
0 13
0.92
229
ERR
261
8.77
016
1506
372
102.97
000
1449 15
1754.06
634.55
0 02
002
2.57
0.00
31.36
113 20
1.06
0 12
0.53
2.50
ERR
2.16
6.45
017
Barometric
Pressure
(in Hg)
26 75
000
000
26 76
000
001
26 79
001
0 02
26 83
000
002
26 87
001
_ 0 02
-------
Engine
Test
Test
Ambient
Number
Number
Condition
Time
Temperature
<*F)
Average
68 99
Std Deviation
098
Turbine
6
Full
1709-1823
RSD
1.41
Max
71 14
Min
67.23
n
&
CEM Summary for 11/07/94 '
GRI Campaign 6B
Relative
Barometric
Fuel
Humidity
Pressure
02
C02
CO
Pressure
NOx
THC
FTIR
(%)
(in Hg)
<%)
<%> .
(ppm)
(psi)
(ppm)
(ppm)
(mm Hg)
44 16
26 51
16.02
3.21
0.45
-30.71
71.52
-0.65
634.98
021
0.01
003
003
0.31
0.00
031
0.35
1 44
0.47
0.02
021
0.91
69.58
-0.01
044
-53.45
0.23
44 48
2651
1609
326
1.04
-30.71
72.01
-0.10
637.32
43.77
26.50
15.92
3.16
-0.22
-30.72
70.66
-1.19
631.30
-------
Engine
Number
Turbine
o
CEM Summary for'
GRI Campaign
11/08/94
I 6B
Nelative
Barometric
Fuel
Humidity
Pressure
02
C02
CO
Pressure
NOx
THC
FTIR
.._(*)_
(in Hg)
(%)
(%)
(ppm)
(psi)
(ppm)
(ppm)
(mm Hg)
47.17
2650
15.93
3 16
0.95
•30.71
7081
076
626 08
0.78
003
0,04
003
1 08
000
0.84
094
1 32
1 66
0.12
026
083
113.00
-0.01
1.19
122.83
021
48.91
26 54
15 98
325
6.78
-30.71
7224
6.65
628.81
45.83
26 45
15 83
3.12
-0.18
-30.72
68.85
-0.25
623.31
45.64
" 26 47
16 33
2 94
0.35
•30.71
56.01
064
62355
0.30
002
007
0.02
0.29
0.00
0.64
0.21
3.11
0.67
006
0.46
079
84.99
-0.00
1.14
32.53
050
46 20
2649
1645
2 99
1.01
-30.70
57.19
1.06
65637
44.95
26.45
1618
290
-0.15
-30.72
54.90
0.37
621.12
-------
Appendix D
GC Data
This ap])endix includes the run-averaged gas chromatograph (GC) data for all engine and
turbine test runs. Emissions data for methane and ethane are presented in concentration
(ppmvw, ppmvd, and ppmvd at 15% O2), mass (lb/hr and tons/yr), and emission factor units
(g/BHP -hr and lb/MMBtu),
\
D-l
-------
D.1 Campaign 3
Station 3A GC Results
GRI Campaign 3
Stack
Eifiit
Condition
Pollataat
Coac.
Cone.
Coac.
Eaiuiop Rate
(ppoivw)
(ppaavd)
(ppnvd
(215% 02)
QVk r)
(f/BHP-kr)
(Ih/MMBtu)
(toaa/yr)
102
Tat 1
Methane
1674
1924
1005
41.9
4.69
1.26
183
t LSV-16
98% Load
Ethane
24.2
27.8
14.5
1.14
0.13
0.034
498
102
Test 2
Methane
2204
2566
1316
554
5.99
1.65
243
LSV-16
101% Load
Ethane
33.6
39.1
20.1
1.59
0.17
0.047
696
101
Test 2
Methane
2023
2339
1210
490
5.49
1.51
215
LSV-16
98% Load
Ethane
31.9
36.9
19.1
1.45
0.16
0045
64
101
Test 3 iMethane
2114
2444
1243
51.2
5.64
1.55
224
LSV-16
99% Load
Ethane
33.0
38.2
194
1.50
0.17
0.05
658
10/30/95
D-2
0CSUM3 WK4
-------
Station 3B GC Results
GRI Campaign 3
Eagiae
Coadltioi
PaUataat
Cmc
Stack
Come.
Eatiuioa Rate
(fp«rw)
(ppvrd)
(ppavd
aiSH C)2>
(Ib/hr)
(f/BHP-hr)
(Ib/MMBta)
(taaa/yr)
2
Test)
Methane
2382
2575
2620
27.6
14.0
3.29
121
GMV-1OTF
81% Load
Ethane
493
533
542
108
5 46
1.28
47.1
2
Test 2
Methane
S42
604
451
5.85
2.32
0.56
25.6
OMV-IOTF
104% Load
Ethane
105
117
87.4
2.13
0.84
0.20
9.32
2
Ten 3
Methane
568
626
468
6.07
2.41
0.58
26.6
OMV-WTF
104% Load
Ethane
110
121
90 6
2.21
088
0.21
97
01/30/96
D-3
OC-SUM3 WK4
-------
D.2 Campaign 4
G C Results
Engine
Teat
Period
Sample
Location
Pollutant
Stack
Cone
(ppmvw)
Cone,
(ppmvd
(Si.lS*/* 02)
Emission Rate
(lb/hr)
(j/BHP-hr)
(toni/yr)
Engine 4
C-B
GMVC-10C
Test 7
97% Load
Before CO
Catalyst
Methane
Ethane
••
40.5
All
1.41
0.370
6.18
Engine 4
C-B
GMVC-10C
Test 9
93% Load
Before CO
Catalyst
Methane
Ethane
••
41.9
48.5
1.45
0.392
6.34
Engine 8
| I-R
1 KVS
Test 11
89% Load
Methane \ —; j
Ethane ! 53.64! 37.1 j 1.40 i 0.357
6.14
! Engine 8
I-R
! KVS
Test 12 i Methane ** ;
82% Load ' [Ethane 94.7! 66.2 2.34! 0.648
10.3
Engine 9
I-R
i KVS
Test 13 Before SCR 1 Methane **
88% Load : Catalyst iEthane 24.9 13.6 0.497 0.128; 2.18
:
Engine9 j Test 15 ! After SCR Methane j ** — — —
I-R 90% Load j Catalyst iEthane i 27.5 15.4 0.583 0.146 2.55
KVS |
** Methane measurements unavailable due to instrument malfunction
1030/95 GCSUM4.WK4
D-4
\
\
-------
D.3 Campaign 5
Test
Location
Stack flow
Pollutant
Detection Limit
Cone.
Emission Rate
(dscfm)
(ppmv)
(ppmvd)
(Ib/hr) (j/BHP-hr) | (tons/yr)
3
Turbine
232503
Methane
3
ND
1 1
H H
Ethane
1
ND
— -j
ND * NonnJctcct
10/30/95
D-5
GCCPN5 WK4
-------
D.4 Campaign 6
Gas Chromatograph Remits
GRI Campaign 6
Engine
Condition
PoDutant
Cone.
Cone.
Emiuton Rate
(ppmvw)
(ppmvd@
15% 02)
(lb/hr)
(g/BHP-hr)
(tora/yr)
Engine 11
Test 19
Methane
847
892
15.8
3.99
69.3
C-B GMVC-10
100% Load
Ethane
21.5
22.6
0.75
0.19
3.30
Engine 11
Test 20
Melhane
832
838
14.1
3.71
61.8
C-B GMVC-10
101% Load
Ethane
22.5
22.6
C7(
0.19
3.13
Engine 11
Test 21
Methane
861
970
14.4
4.45
62.9
C-B GMVC-10
86% Load
Ethane
24.2
27.3
0.76
0.23
3.31
Engine 11
Test 22
Methane
1144
1289
21.0
6.08
92.0
C-B GMVC-10
87% Load
Ethane
29.2
32.8
1.00
0.29
4.40
Engine 11
Test 24
Methane
795
838
13.9
3.78
60.9
C-B GMVC-10
99% load
Ethane
22.1
23.3
0.72
0.20
3.17
01/30/96
D-6
GC-SUM6.WK4
-------
Gas Chromatograph Reiuhs
GRI Campaign 6
ISngine
Condition
Pollutant
Cone
Cone.
Emission Rate
(ppmvw)
(ppmvd §
15% 02)
(IMir)
(g/BHP-hr)
(tona/jr)
Engine 13
Test 15
Methane
1487
1520
52.2
7.08
229
C-B GMWC-10
96% Load
Ethane
33.4
34.1
2.20
0.30
9.62
Engine 13
Test 16
Methane
1S39
1551
49.2
7.31
215
C-B 3MWC-10
95°/. Load
Ethane
34.8
35.1
2.08
0.31
9.12
Engine 13
Test 17
Methane
1598
1712
50.4
8.11
221
C-B GMWC-10
88% Load
Ethane
38.6
41.3
2.28
0.37
10.0
Engine 13
Test 18
Methane
1540
1680
55.7
7.97
244
C-B GMWC-10
91% Load
Ethane
37.3
40.7
2.53
0.36
11.1
Engine 13
Test 23
Methane
1523
1664
53.0
7.78
232
C-B GMWC-10
92% Load
Ethane
36.1
39.4
2.35
0.35
10.3
01/30/96
D-7
GC-SUM6.WK4
-------
Gas Cbromatograph Results
GRI Campaign 6
Engine
Condition
Pollutant
Cone.
Cone.
F.miscion Rate
(ppmvw)
(ppmvd @
15% 02)
(lb/hr)
(g/BHP-hr)
(tons/yr)
Engine 10
Test 1
Methane
531
522
6.32
3.37
27.7
Clark BA-5
94% Load
Ethane
7.82
7.69
0.17
0.09
0.76
Engine 10
Test 2
Methane
680
661
8.63
4.31
37.8
Clark BA-5
100% Load
Ethane
13.50
13.1
0.32
0.16
1.41
Engine 10
Test 3
Methane
760
819
9.06
5.67
39.7
Clark BA-5
80% Load
Ethane
15.80
17.0
0.35
0.22
1.55
Engine 12
Test 4
Methane
1393
1696
17.8
10.9
77.8
1 Clark HBA-5
75% Load
Ethane
33.4
40.6
0.80
0.49
3.49
; Engine 12
Tcst5
Methane
961
1050
11.9
6.44
52.1
! Clark HBA-5
84% Load
Ethane
21.4
23.4
0.50
0.27
2.18
Turbine
Test 6
Methane
ND
! Solar Taurus
95% Load i Ethane
ND
Turbine
Test 7 ! Methane
ND
Solar Taurus
95% Load
Ethane
ND
Turbine
Test 8
Methane
ND
!
Solar Taurus
77% Load i Ethane
ND
Engine 15
Test 9
Methane
718
111
15.4
3.82
67.3
C-B GMVC-10
102% Load
(300 rpm)
Ethane
18.5
19.9
0.74
0.18
3.26 j
Engine 15
Test 10 j
Methane
647
673
13.5
3.34
58.9;
C-B GMVC-10
102% Load ! Ethane
17.3
18.0
0.68
0.17
2.96
(300 rpm)
Engine 15
Test 11 , Methane
1692
1986
39.8
11.9
174 !
C-B GMVC-10
85% Load ! Ethane
38 9
45.6
1.71
0.51
7.50 1
(300 rpm)
!
!'
Engine 9
Test 12 i
vl ethane
1855 '.
2033
25.3
10.7
1
mi
C-B GMVA-10
88% Load 1 Ethane
47.1 !
51.6
1.21
0.51
5.28!
Engine 9
Test 13 i Methane
1087;
1110
14.3
5.28
62.8 j
C-B GMVA-10
100% Load 1
Ethane
26.6!
27.2
0.66
0.24
2.88
Engine 9
Test 14
Methane
1
978!
984
12.7.
4.66
55-5 j
C-B GMVA-10 :
100% Load
Ethane
26.0
26.1
0.63 i
0.23
2.76!
10/30/95
D-8
GCSUM6.WK4
-------
GRI CAMPAIGN 6
-This calculation was required to adjust for an exhaust leak present in Engine 10 at site 6A.
-Tests 1 and 3 were conducted before and after the exhaust leak, however, no test was conducted
before the exhaust leak during test 2.
-A correction factor was needed to adjust the CEM exhaust concentrations in Test 2, as well as
for moisture and concentrations measured by FTIR, GC, CARB 430, and Method TO-14 for Tests 1, 2, and 3.
TEST 1 (before leak) 1 (after leak) 1 Ratio 3 (before leak) 3 (after leak) 3 Ratio Correction Factor
02 (%) 14.2 16.9 0.84 14.9 17.3 0.86 0.85
NOx(ppmv) 914 597 1.53 373 219 1.7 1.63
C02 (%) 4.3 2.65 1.62 3.88 2.41 1.61 1.63
CO(ppmv) 86.3 51.7 1.68 95.5 59.1 1.61 1.63
O
¦b - To get correction factors, the 02 ratios were averaged to give an 02 correction. The average of all the other
ratios for NOx, CO, and C02 were averaged to give correction factors for these compounds as well as for
moisture and compounds measured by FTIR, GC, CARB 430, and Method TO-14 for tests 1, 2, and 3.
Example for Test 2.
2 (after leak) 2 (corrected)
02=16.8 =14.3
NOx=820 =1337
C02=2.69 =4.38
CO=56.8 =92.6
-To correct for FTIR, GC, CARB 430, and Method TO-14 multiple dry concentration by 1.63.
Example.
Ethane (measured by FTIR) for Engine 10, Test 1 was 10.6 ppmv, corrected to 17.3 ppmv through the factor 1.63.
11 im/nr I FAK-CDR WK4
-------
Appendix E
GC Summary Data
This api^endix presents a summary of the raw GC data. It includes the chromatograph areas
and heights used to calculate pollutant concentrations for all engine and turbine test runs.
E-l
-------
GC Summary Data for Campaign 3
Data
6/14/94
6/15/94
6/16/94
6/16/94
6/18/94
6/19/94
6/19/94
Engine
102
102
101
101
2
2
2
Load
Full
Full
Full
Full
Low
Fun
Full
Test#
1
Dup. #1
2
Dup. #2
5
Dup. #5
6
Dup. #6
8
Dup. #8
9
Dup. #9
10
Dup. #10
Time
16:10
16:40
10:10
10:30
10:50
11:15
14:30
15:45
18:10
18:30
13:20
14:15
17:30
17:50
Range
ppm
ppm
ppm
ppm
ppm
ppm
ppm
ppm
ppm
ppm
ppm
ppm
ppm
ppm
C1
1665
1695
2220
2209
1794
2273
2112
2136
2111
2720
564
571
620
569
C2
24.1
25.1
33.7
33.7
28.9
35.1
33.4
32.8
431
555
104
106
112
107
Methane
1659
1688
2209
2199
1784
2262
2102
2125
2078
2685
538
545
593
543
Ethane
24.1
24.3
33.6
33.6
28.8
35
33.3
32.6
0
0
0
0
0
0
-------
August 25, 1994: Run 23 (C1-C7 t 16 ppmV)
Concentration
Compound (ppmv) Araa Height
Methane IS.3 2359395 426763
Ethane IS.3 4173186 809332
Propane 16.3 6138160 968062
E.2 Campaign 4
Response Factor
Area Height
6.91E-06 3.82E-05
3.91E-06 2.01E-05
2.66E-06 1.68E-05
Pentane
Hexane
Heptane
16.4
16.9
14.0
9827194
16666632
22838192
1219228
1446698
1014833
1.67E-06
1.01E-06
6.13E-07
1.35E-05
1.17E-05
1.38E-05
August 25,
1994: Run
24 (C1-C7 t
100 ppmV)
Concentration
Response
Factor
Compound
(ppmv)
Area
Height
Area
Height
Methane
100
12707296
2511277
7.87E-06
3.98E-05
\ Ethane
100
24441744
4940051
4.09E-06
2.02E-05
^Propane
100
36146912
5617562
2.77E-06
1.78E-05
Butane
100
55477984
6522515
1.8E-06
1.53E-05
Pentane
100
70451136
7107283
1.42E-06
1.41E-05
Hexane
100
121871680
8048749
8.21E-07
1.24E-05
August 25, 1994: Run 31 (Unit 4 Run 1 Low Level 9 18:24:57
Concentration (ppmV)
Compound
Area
Height
Area
Height
Methane
OFF SCALE OFF SCALE
NA
NA
Ethane
41895458
6166297
171.409
124.823
Propane
47578944
7214461
131.627
128.427
Butane
81768064
7942419
147.388
121.769
Pentane
OFF SCALE OFF SCALE
0.000
0.000
Hexane
OFF SCALE OFF SCALE
0.000
0.000
August 25, 1994: Run 32 (Unit 4 Run 1 Low Level J 18:50:01
Concentration (ppmV)
Compound
Area
Height
Area
Height
Methane
OFF SCALE OFF SCALE
NA
NA
Xthaae
20217200
1979172 -
82.71ft
40.064
2ntegratad Iinprope
Sropaae
75475200
1272051 j
„JOO.SOi
22.644
Integrated Improjpe
Butane
9758970
1220798
17.591
18.717
Pentane
10834912
1272214
15.379
17.900
Hexane
12630024
1364975
10.363 -
16.959
August 25, 1994:
Run 33 (Unit 4 Run 1 Low Laval 9
Concentration (ppmV)
19:19:46
Compound
Area
Height
Area
Height
Methane
OFF SCALE OFF SCALE
NA
NA
Ethane
*199*7.20
2022515 |
335.48?
40.941
Propane
6210208
787341
17.180
14.016
Butane
5235882
646644
9.438
9.914
Pentane
5601005
657671
7.950
9.253
Hexane
5676941
575048
4.658
7.145
integrated Impropa
E-3
-------
August 26
, 1994:
Run 35 (CI
-C6 § 100
ppmV)
Concentration
Response
Factor
Compound
(ppmv)
Area
Height
Area
Height
Methane
100
14821152
2406885
6.75E-06
4.15E-05
Ethane
100
30049648
4594522
3.33E-06
2.18E-05
Propane
100
47163072
5322077
2.12E-06
1.88E-05
Butane
100
64594400
5940787
1.55E-06
1.68E-05
Pentane
100
OFF SCAL OFF SCALE
NA
NA
Hexane
100
OFF SCAL OFF SCALE
NA
NA
August 26
, 1994:
Run 49 (CI
-C7 8 100
ppmV)
Concentration
Response
Factor
Compound
(ppmv)
Area
Height
Area
Height
Methane
100
10695248
2205238
9.35E-06
4.53E-05
Ethane
100
20714880
4102766
4.83E-06
2.44E-05
Propane
100
31533600
4783184
3.17E-06
2.09E-05
Butane
100
47877984
5752483
2.09E-06
1.74E-05
Pentane
100
68225216
6946883
1.47E-06
1.44E-05
Hexane
100
1.22E 08
8121763
8.22E-07
1.23E-05
August 26, 1994: Run 50 (Unit 4 Inlet High Load 0 15
Concentration (ppmV)
Compound
Area
Height
Area
Height
Methane
OFF SCAL
OFF SCAL
NA
NA
Pthane
1718105 £
41.877
Propane
3668096
491877
11.632
10.283
Butane
3293896
414818
6.880
7.211
Pentane
3997981
462522
5.860
6.658
Hexane
5368208
559219
4.415
6.885
E-4
-------
August 21
, 1994:
Run 58 (CI
1
o
c*
*
M
o
o
ppmV)
Concentration
Response
Factor
Compound
(ppmv)
Area
Height
Area
Height
Methane
100
11570576
2309218
8.64E-06
4.33E-05
Ethane
100
22296448
4307B53
4.49E-06
2.32E-05
Propane
100
33324208
5001978
3E-06
2E-05
Butane
100
48526624
5922266
2.06E-06
1.69E-05
Pentane
100
67119680
7069267
1.49E-06
1.41E-05
Hexane
100
84309184
8363853
1.19E-06
1.2E-05
August 27, 1994:
Run 64 (Nitrogen Blank)
Concentration (ppmV)
Compound
Area
Height
Area
Height
Methane
678571
161646
5.865
7.000
Ethane
733033
170770
3.288
3.964
' " "V ~ a
Propane
1057158
178414
3.172
3.567
Butane
1393127
187341
2.871
3.163
Pentane
1507707
215975
2.246
3.055
301544 |
ESC
3.605
August 27, 1994: Run 65 (Unit 8 Run 1
13:50:22 )
Concentration (ppmV)
Compound
Area
Height
Area
Height
Methane
Off Seal
Off Scale
NA
NA
ISlsSlilslslLSI
1967345 |
45.669
Propane
3070242
390666
9.213
7.810
Butane
1749320
216895
3.605
3.662
Pentane
1665573
198844
2.481
2.813
Hexane
2131461
211182
2.528
2.525
August 2 7, 1994: Run 66 (Unit 8 Run 1 8
14:39:12 )
Concentration (ppmV)
Compound
Area
Height
Area
Height
Methane
Off Seal
Off Scale
NA
NA
,68243072
2653749 f
61.603
Propane
3892358
511659
11.680
10.229
Butane
1885128
233063
3.885
3.935
Pentane
1590826
191078
2.370
2.703
Hexane
2155859
208280
2.557
2.490
August 27, 1994: Run 68 (Nitrogen Blank)
Concentration (ppmV)
Compound
Area
Height
Area
Height
Methane
1146828
149757
9.912
6.485
Ethane
171438
37489
0.769
0.870
Propane
229028
36475
0.687
0.729
Butane
236368
30468
0.487
0.514
Pentane
1042334
124476
1.553
1.761
VwmSTT "
NA
\ - saTTsoi r«ported ~ "i
E-5
-------
August 27, 1994:
Compound
Area Height
Methane Off Seal Off Scale
Propane 4703501 515855
Butane ND ND
Pentane ND MD
Hexane ND ND
Run 69 (Unit 8 Run 2 G 16:35:10)
Concentration (ppmV)
Area Height
NA
14.114
0.000
0.000
0.000
NA
843.346
10.313
0.000
0.000
0.000
August 27, 1994:
Run 70 (Unit 8 After Restart 0
Concentration (ppmV)
Compound
Area
Height
Area
Height
Methane
Off Seal
Off Scale
NA
NA
mmmm
j 3792629 |
88.040
Propane
4805315
679380
14.420
13.582
Butane
1645142
203639
3.390
3.439
Pentane
902861
109934
1.345
1.555
Hexane
1051919
93885
1.248
1.123
17:18:47
August 27, 1994:
Run 71 (Unit 8 After Restart ®
Concentration (ppmV)
Compound
Area
Height
Area
Height
Methane
Off Seal
Off Scale
NA
NA
SBTOBBfl
4111990 1
95.453
Propane
5197370
742973
15.596
14.854
Butane
1688248
209876
3.479
3.544
Pentane
870275
106599
1 .297
1 .508
Hexane
995474
87806
1. 181
1.050
17:49:45
August 27, 1994:
Compound Area Height
Methane Off Seal Off Scale
Ethane 28733312 4337546
Propane 5456256
Butane 1756613
Pentane 1882510
Run 72 (Unit 8 After Restart 6
Concentration (ppmV)
Area Height
NA
128.869
16.373
3.620
2.805
18:26:29
781846
214257
126140
182870
NA
100.689
15.631
3.618
1.784
2.186
ntegr«t»d laptop
August 27, 1994:
Compound
Methane
Ethane
Propane
Butane
Pentane
Area
1818065
244781
248904
433129
1106837
.Hexane. 14217704
Run 73 (Nitrogen Blank)
Concentration (ppmV)
Height Area Height
439181 15.713 19.019
55272 1.098 1.283
37522 0.747 0.750
41406 0.893 0.699
71472 1.649 1.011
260840 r ML&J4 3.119
ntegrat»d Tnprog
E-6
-------
August 28,
1994: Run
86 (C1-C6
9 100 ppmV)
Concentration
Response
Factor
Compound
(ppmv)
Area
Height
Area
Height
Methane
100
12780776
2406885
7.82E-06
4.15E-05
Ethane
100
24168288
4594522
4.14E-06
2.18E-05
Propane
100
35656864
5322077
2.8E-06
1.88E-05
Butane
100
47504160
5940787
2. HE—06
1.68E-05
Pentane
100
60844832
6698496
1.64E-06
1.49E-05
Hexane
100
85781632
7471712
1.17E-06
1.34E-05
August 28, 1994: Run 94 (Nitrogen Blank)
Concentration (ppmV)
Compound
Area
Height
Area
Height
He thane
200789
45299
1.571
1.882
\.v rtane
207873
45981
0.860
1.001
Irupane
300777
48386
0.844
0.909
Butane
384771
49528
0.810
0.834
Pentane
1281490
131931
2.106
1.970
Hexane
9644326
595857
11.243
7.975
August 28, 1994: Run 95 (Nitrogen Blank)
Concentration (ppmV)
Compound
Area
Height
Area
Height
Methane
178443
39950
1.396
1.660
Ethane
158324
34021
0.655
0.740
Propane
226260
34094
0.635
0.641
Butane
565448
39300
1.190
0.662
Pentane
858382
56669
242455
1.411
0.846
0** w * A
llillll
3.245
August. 28, 1994: Run 97 (Unit 9 Inlet J
14:11:56 )
Concentration (ppmV)
Compound
Area
Height
Area
Height
Methane
Off Scale
Off Scale
HA
MA
liiaa^lKl
1146194
24.947
Propane
1601957
228545
4.493
4.294
Butane
562815
61788
1.185
1.040
Pentane
324486
39052
0.533
0.583
Hexane
1079354
106155
1.258
1.421
Imprope
August 28, 1994: Run 98 (Nitrogen Blank)
Concentration (ppmV)
Compound
Area
Height
Area
Height
Methane
1333180
294076
10
.431
12.218
Ethane
379036
78783
1
.568
1.715
Propane
368992
59583
1
.035
1.120
Butane
ND
ND
0
.000
0 .000
Pentane
ND
ND
0
.000
0.000
Hexane
ND
ND
0
.000
0.000
E-7
-------
August 29, 1994: Run 99 (C1-C6 t ppmV)
Concentration Response Factor
Compound
(ppmv)
Area
Height
Area
Height
Methane
16.3
783252
170841
2.081E-05
9.54IE—05
Ethane
16.3
450844
91687
3.615E-05
0.0001778
Propane
16.3
497372
80253
3.277E-05
0.0002031
Butane
16.3
255219
57065
6.387E-05
0.0002856
Pantana
16.4
374050
47062
4.384E-05
0.0003485
Hexane
16.9
479364
49143
3.526E-05
0.0003439
August 29, 1994: Run 101 (C1-C7 t 100 ppmV)
Concentration
Compound
Methane
Ethan#
Propana
Butane
Pentane
Baxana
(ppmv)
100
100
100
100
100
100
Area
16733856
33513360
51557088
70065024
OFF SCALE
OFF SCALE
Response Factor
Beight
2566907
4921821
6630992
8605894
OFF SCALE
OrF SCALE
Area
5.976E-06
2.9842-06
1.94E-06
1.427E-06
NA
NA
Height
3.896E-05
2.032E-05
1.508E-05
1.162E-05
NA
NA
August 29, 1994: Run 103 (Unit 9 Outlet ( 09:30:42 )
Concentration (ppmV)
Compound
Area
Height
Area
Height
Methane
OFF SCALE
OFF SCALE
NA
NA
Ethane
13341808
1914242
39.810
38.893
Propane
3812670
474997
7.395
7.163
Butane
2311710
296537
3.299
3.446
Pentane
2371272
279166
NA
NA
Hexane
15069672
1069791
NA
NA
August 29, 1994: Run 104 (Unit 9 Outlet t 10:11:55 )
Concentration (ppmV)
Compound
Area
Height
Area
Height
Methane
OFF SCALE
OFF SCALE
NA
NA
Ethane
6555584
1060823
19.561
21.553
Propane
3011496
376402
5.841
5.676
Butane
2428237
285721
3.466
3.320
Pentane
2505144
279216
NA
NA
Hexane
2222502
238147
NA
NA
August 29, 1994: Run 105 {Unit 9 Outlet ( 10:53:47 )
Concentration (ppmV)
Compound
Area
Height
Area
Height
Methane
OFF SCALE
OFF SCALE
NA
NA
Ethane
9827251
1157173
29.323
23.511
Propane
2366738
291974
4 .591
4 .403
Butane
1428736
180202
2.039
2.094
Pentane
1616426
182172
NA
NA
Hexane
1727629
174858
NA
NA
E-8
\
\
-------
August 29, 1994: Run 106 (Unit 9 Outlet « 11i49i04 )
Concentration (ppmV)
Compound
Area
Height
Area
Height
Methane
OFF SCALE
OFF SCALE
NA
NA
Ethane
10956408
1301247
32.693
26.438
Propane
2295813
235961
4.453
3.558
Butane
ND
ND
0.000
0.000
Pentane
ND
ND
NA
NA
Hexane
ND
ND
NA
NA
August 29, 1994t Run 107 (Unit 9 Outlet I 12:15>26 )
Concentration (ppmV)
Compound
Area
Height
Area
Height
Methane
OFF SCALE
OFF SCALE
NA
NA
Ethane
11171096
1329184
33.333
27.006
Propane
2009079
216747
3.897
3.269
Butane
ND
ND
0.000
0.000
Pentane
ND
ND
NA
NA
Bexane
ND
ND
NA
NA
August 29, 1994: Run 108 (Nitrogen Blank)
Concantration (ppmV)
Com'.-iund
Area
Height
Area
Height
Methane
5703517
1225823
34
.084
47.755
Ethane
596793
125235
1
.781
2.544
Propane
434527
56245
0
.843
0.848
Butane
ND
ND
0
.000
0.000
Pentane
ND
ND
NA
NA
Hexane
ND
ND
NA
NA
August 29, 1994: Run 109 (Nitrogen Blank)
Concentration (ppmV)
Compound
Area
Height
Area
Height
Methane
1152786
256495
6.889
9 .992
Ethane
318749
66199
0.951
1.345
Propane
329611
53058
0.639
0.800
Butane
ND
ND
0.000
0.000
Pentane
ND
ND
NA
NA
Hexane
ND
ND
NA
NA
E-9
-------
August 25,
Compound
Methane
Ethane
Propane
ButfUl*
Pentane
Hexane
Heptane
1994: Run 23 (C1-C7 ?
Concentration
(ppmv) Area
16.3 2359395
16.3 4173186
16.3 6136160
16.4 9827194
16.9 16666632
14.0 22838192
16 ppmV)
Response Factor
Height Area Height
426763 6.91E-06 3.82E-05
809332 3.91E-06 2.01E-05
968062 2.66E-06 1.68E-05
'r:m-
1219228 1.67E-06 1.35E-05
1446698 1.01E-06 1.17E-05
1014833 6.13E-07 1.38E-05
August 25, 1994: Run 24 (C1-C7 ? 100 ppmV)
Concentration Response Factor
Compound
(ppmv)
Area
Height
Area
Height
Methane
100
12707296
2511277
7.87E-06
3.98E-05
Ethane
100
24441744
4940051
4.09E-06
2.02E-05
Propane
100
36146912
5617562
2.77E-06
1.78E-05
Butane
100
55477984
6522515
1.8E-06
1.53E-05
Pentane
100
70451136
7107283
1.42E-06
1.41E-05
Hexane
100
121871680
8048749
8.21E-07
1.24E-05
W
August 26, 19941 Run 35 (C1-C6 I 100 ppmV)
Concentration
Response
Factor
Compound
(ppmv)
Area
Height
Area
Height
Hethane
100
14821152
2406885
6.75E-06
4.15E-05
Ethane
100
30049648
4594522
3.33E-06
2.18E-05
Propane
100
47163072
5322077
2.12E-06
1.88E-05
Butane
100
64594400
5940787
1.55E-06
1.68E-05
Pentane
100
OFF SCALE OFr SCALE
NA
NA
Hexane
100
OFF SCALE OFF SCALE
NA
NA
August 26
, 1994 > 1
Run 49 (CI-
-C7 ( 100 ppmV)
Concentration
Response
Factor
Compound
(ppmv)
Area
Height
Area
Height
Methane
100
10695248
2205238
9.35E-06
4.53E-05
Ethane
100
20714880
4102766
4.83E-06
2.44E-05
Propane
100
31533600
4783184
3.17E-06
2.09E-05
Butane
100
47877984
5752483
2.09E-06
1.74E-05
Pentane
100
68225216
6946883
1.47E-06
1.44E-05
Hexane
100
1.22E 08
8121763
8.22E-07
1.23E-05
-------
August 29, 19941 Run 99 (C1-C6 J ppmV)
Concentration Response Factor
Compound
(ppmv)
Area
Height
Area
Height
Methane
16.3
783252
170841
2.081E-05
9.541E-05
Ethane
16.3
450844
91687
3.615E-05
0.0001778
Propane
16.3
497372
80253
3.277E-05
0.0002031
Butane
16.3
255219
57065
6.387E-05
0.0002856
Pentane
16.4
374050
47062
4.384E-05
0.0003485
Hexane
16.9
479364
49143
3.526E-05
0.0003439
August 29, 1994! Run 101 (C1-C7 I 100 ppmV)
Concentration Response Factor
Compound
(ppmv)
Area
Height
Area
Height
Methane
100
16733856
2566907
5.976E-06
3.896E-05
Ethane
100
33513360
4921821
2.9B4E-06
2.032E-05
Propane
100
51557088
6630992
1.94E-06
1.508E-05
Butane
100
70065024
8605894
1.427E-06
1.162E-05
Pentane
100
OFF SCALE
OFF SCAL
NA
NA
Hexane
100
OFF SCALE
OFF SCAL
NA
NA
August 28,
1994: Run
86 (C1-C6
( 100 ppmV)
Concentration
Response
Factor
Compound
(ppmv)
Area
Height
Azea
Height
Methane
100
12780776
2406885
7.82E-06
4.15E-05
Ethane
100
24168288
4594522
4.14E-06
2.18E-05
Propane
iuO
J3636B64
5322077
2.8E-06
1.88E-05
Butane
100
47504160
5940787
2.11E-06
1.68E-05
Pentane
100
60844832
6698496
1.64E-06
1.49E-05
Hexane
100
85781632
7471712
1.17E-06
1.34E-05
August 28, 19941 Run 94 (Nitrogen Blank)
Concentration (ppmV)
Compound
Area
Height
Area
Height
Methane
200789
45299
1.571
1.882
Ethane
207873
45981
0.860
1.001
Propane
300777
48386
0.844
0.909
Butane
384771
49528
0.810
0.834
Pentane
1281490
131931
2.106
1.970
Hexane
9644326
595857
11.243
7.975
-------
w
I
t-u
K)
August 27
, 1994:
Run 58 (CI
-C6 0 100 ppmV)
Concentration
Response
Factor
Compound
(ppmv)
Area
Height
Area
Height
Methane
100
11570576
2309218
8.64E-06
4.33E-05
Ethane
100
22296448
4307853
4.49E-06
2.32E-05
Propane
100
33324208
5001978
3E-06
2E-05
Butane
100
48526624
5922266
2.06E-06
1.69E-05
Pentane
100
67119680
7069267
1.49E-06
1.41E-05
Hexane
100
84309184
8363853
1.19E-06
1.2E-05
August 27, 1994:
Run 64 (Nitrogen Blank)
Concentration (ppmV)
Compound
Methane
Ethane
Propane
Butane
Pentane
mm
Area
678571
733033
1057158
1393127
1507707
Height
Area
Height
161646
5.865
7.000
170770
3.288
3.964
178414
3.172
3.567
187341
2.871
3.163
215975
2.246
3.055
301544 |
3.605
-------
August 28
Compound
Methane
Ethane
Propane
Butane
Pentane
Hexane
August 28
Compound
Methane
Ethane
Propane
Butane
Pentane
1994: Run 94 (Nitrogen Blank)
Concentration (ppmV)
Area
Height
Area
Height
200789
45299
1.571
1.882
207873
45981
0.860
1.001
300777
48386
0.844
0.909
384771
49528
0.810
0.834
1281490
131931
2.106
1.970
9644326
595857
11.243
7.975
1994: Run 95 (Nitrogen Blank)
Concentration (ppmV)
Area
178443
158324
226260
565448
858382
Height
Area
Height
39950
1.396
1.660
34021
0.655
0.740
34094
0.635
0.641
39300
1.190
0.662
56669
1.411
0.846
242455 |
3.245
-------
August 29
Compound
Methane
Ethane
Propane
Butane
Pentane
Hexane
August 29
Compound
Methane
Ethane
Propane
Butane
Pentane
Hexane
/
t ¦
/
1994: Run 108 (Nitrogen Blank)^
Concentration (ppmV)
Area
Height
Area
Height
5703517
1225823
34.084
47.755
596793
125235
1.781
2.544
434527
56245
0.843
0.848
ND
ND
0.000
0.000
ND
ND
NA
NA
ND
ND
NA
NA
1994s Run 109 (Nitrogen Blank)
Concentration (ppmV)
Area
Height
Area
Height
1152786
256495
6.889
9.992
318749
66199
0.951
1.345
329611
53058
0.639
0.800
ND
ND
0.000
0.000
ND
ND
NA
NA
ND
ND
NA
NA
-------
August 28, 1994s Run 98 (Nitrogen Blank)
Concentration (ppmV)
Compound
Area
Height
Area
Height
Methane
1333180
294076
10.431
12.218
Ethane
379036
78783
1.568
1.715
Propane
368992
59583
1.035
1.120
Butane
ND
ND
0.000
0.000
Pentane
ND
ND
0.000
0.000
Hexane
ND
ND
0.000
0.000
-------
August 27, 1994:
Compound
Methane
Ethane
Propane
Butane
Pentane
Area
1146828
171438
229028
236368
1042334
/
* ¦
I
Run 68 (Nitrogen Blank)v\
Concentration (ppmV)
Height
Area
Height
149757
9.912
6.485
37489
0.769
0.870
36475
0.687
0.729
30468
0.487
0.514
124476
1.553
1.761
-------
/
August 27, 1994s
m
i
-J
Compound
Methane
Ethane
Propane
Butane
Pentane
Run 73 (Nitrogen Blank)
Concentration (ppmV)
Area
1818065
244781
248904
433129
1106837
Height
Area
Height
439181
15.713
19.019
55272
1.098
1.283
37522
0.747
0.750
41406
0.893
0.699
71472
1.649
1.011
260840 |
mum
3.119
-------
Method 10 Gas Chromatographic Results 'c Campaign *5
E.3 Campaign 5
Date
Unit
T«st #
Mathana. PPMV
Effian*
Propana
Butana
Pan tana
Ha*an»
Hap tan*
10/5/94
Turtjma
Quality Control
fi for Mathana
Calib. Chac*.
Oup. anaJyus
09991
4-15%
NA
NA
NA
NA
0.997
+ 1 0%
NA
0.997
~ 1.0%
<1% of Avg
NA
NA
NA
NA
NA
NA
E-18
-------
Engine #10 Run 3A (#11, 11/4/94 15:01:23)
E.4 Campaign 6
RT
Concentration
Compound
(min)
Area
(PPMV)
Methane
0.626
382404
420.28
Ethane
1.031
28739
12.31
Propane
2.467
7034
2.45
Butane
ND
ND
ND
Pentane
ND
ND
ND
Hexane
10.365
43154
15.63
Improperly
Heptane
13.908
626017
143.61
Improperly
Engine #10 Run 3B (#12, 11/4/94 15:39:20)
RT
Concentration
Compound
(min)
Area
(ppmv)
Methane
0.619
510006
561.77
Ethane
1.024
35213
15.94
Propane
2.461
8419
2.93
Butane
ND
ND
ND
Pentane
ND
ND
ND
Hexane
ND
ND
ND
Heptane
ND
ND
ND
Comments
Engine #10 Run 3C (#13, 11/4/94 16:10:22)
RT
Concentration
Compound
(min)
Area
(ppmv)
Methane
0.6Z1
378116
415.53
Ethane
1.026
29977
13.01
Propane
2.465
9903
3.45
Butane
ND
ND
ND
Pentane
ND
ND
ND
Hexane
11.046
75282
27.26
Heptane
14.025
608950
139.69
Comments
Improperly integrated
Improperly integrated
E-19
-------
Engine #12 Run 4A (#14, 11/4/94 17:12:02)
RT Concentration Comments
Compound
(min)
Area
(ppmv)
Methane
0.618
1075152
1188.43
Ethane
1.024
78034
39.95
Propane
2.46
20093
3.63
Butane
ND
ND
ND
Pentane
ND
ND
ND
Hexane
ND
ND
ND
Heptane
13.938
94383
21.65
Engine #12 Run 4B (#15, 11/4/94 17:45:20)
RT Concentration Comments
Compound
(min)
Area
(ppmv)
Methane
0.62
4938963
5472.80
Ethane
1.025
259191
141.50
Propane
2.462
77254
25.92
Butane
ND
ND
ND
Pentane
ND
ND
ND
Hexane
ND
ND
ND
Heptane
13.974
53429
12.26
Engine #12 Run 4C (#16, 11/4/94 18:08:54)
RT Concent rat ion Comments
Compound
(min)
Area
(ppmv)
Methane
0.615
1394358
1542.38
Ethane
1.021
91486
47.49
Propane
2.463
23433
4.93
Butane
ND
ND
ND
Pentane
ND
ND
ND
Hexane
ND
ND
ND
Heptane
13.98
42342
9.71
Engine #12 Run 4D (#17, 11/4/94 18:30:38)
RT Concen t ra 11on Commen t s
Compound
(min)
Area
(ppmv)
Methane
0.616
1249263
1381.49
Ethane
1.024
84524
43.58
Propane
2.466
22647
4.63
Butane
ND
ND
ND
Pentane
ND
ND
ND
Hexane
ND
ND
ND
Heptane
14.08
61552
14. 12
E-20
-------
1000 ppmv Standard—Post test
RT
Concent rat ion
Compound
-------
Methane
Ethane
Propane
Butane
Pentane
Hexane
Heptane
Methane
Ethane
Propane
Butane
Pentane
Hexane
16.3
11/04 11/04
32488
45301
135964
11/04
30684
47045
56301
63949
11/04
16182
31213
46586
60822
<32211-
11/04
16182
31213
46586
60822
11/07
14192
27608
40704
53720
62930
64892
100
p
11/04
11/04
11/04
11/05
11/05
11/07
11/08
Methane
95536
94073
94073
93740
68422
82661
81757
Ethane
189807
185384
185384
185185
175687
163932
161654
Propane
273742
267548
267548
265822
- 256368
235545
232273
Butane
358392
351515
351515
348381
(1335619
\ 306969
302856
Pentane
438427
431964
431964
429451
1660235
/ 376637
371839
Hexane
(f658T05
6640F5 ~
0b4Ubb>
501942
^1990563J
435754
431897
1000
'
6^
11/04
11/04
11/04/
11/05
11/05
11/10
Methane
905048
927712
92771/
900232
857770
857770
C640885>
Ethane
1790196
1830394
18303/4
1772947
1698373
1698373
1279745
Propane
2575274
2637850
2637-850
2550282
2432178
2432178
1831508
Butane
3377422
3464061
3464061
3344176
3199366
3199366
2383574
Pentane
4192752
4296173
4296173
4149996
3963614
3963614
2949845
Hexane
4947248
4923888
4923888
4886861
4686723
4686723
3473872 /
2000
11/05
1734171
3406936
5113325
6649475
8229450
9625126
f>P* J
11/05
1666692
3280840
4916179
6400931
7926829
9279194
11/10
1666692
3280840
4916179
6400931
7926829
9279194
11/12
1541790
3042006
4545555
5891405
7259491
8468890
11/12
1571585
3103242
4649421
5968970
7380064
8588422
11/12
1549241
3075802
4601146
5931344
7300013
8512026
11/14
1615651
3164674
4774496
6327706
8000752
9542534
10959000
E-22
\
-------
11/07
11/08
11/08
14376
13990
13590
27813
27210
26466
41516
40117
39317
54099
52819
51239
61913
60349
T51462
~~lb9023 '
14698
11/08
13864
26801
39815
52013
—52158
183855^
11/10
13895
27845
40772
59031
59934
82301
79529
11/11
13478
23737
11/11
12015
25646
34692
45747
59897
71899
11/08
11/10
11/10
11/11
7888$'
68422
76897
80597
156337
175687
159296
159365
224254:
25tfi368
238885
233669
292331
fl3356TS\
307108
301418
359102
\l660235t
394029
382801
416122-
11990563 \
506254
521841
&im
V
/382438^
814777
1261730
1565058
1752447
1760153
11/12
851957
1707167
2549461
3321141
4076989
4771901
/f034075
2076508
3100128
4089774
5033248
5872867
J
^rT/i4
i668274
/1323576
'1911283
2524576
3166800
3703336
11/14
1586870
3110000
4686643
6204544
7831821
9324954
10740736
11/15
1491551
2947805
4450115
5889789
74324321
88905541
10220664
11715^
1349055
2665917
4003160
5182672
6393024 /
7437994 /
11/11
75838
152468
220134
293620
339762
412181
11/11
72301
143178
209912
277852
331268
425471
11/12
70648
139301
215086
270829
321387
375743
11/14
685160
1354267
1959123
2609446
3291882
3910522
11/15
687880
1348913
1951856
2576493
3204414
3712880
11/15
851253
1727644
2582496
3373590
4082157
4884451
E-23
-------
11/12
13070
30661
43524
64049
72189
11/14
72865
144360
212285
282619
349974
426611
Average STD DEV %RSD
743973 218766 29.41%
1482067 432092 29.15%
2162379 635074 29.37%
2985723 670198 22.45%
3491218 1062405 30.43%
4069667 1297934 31.89%
Average STD DEV %RSD
1577330
107332
6.80%
3107806
205167
6.60%
4665622
305946
6.56%
6084777
410732
6.75%
7568071
532621
7.04%
8894889
664795
7.47%
10640133
379309
3.56%
11/12
11/14
11/15
Average
STD DEV
%RSD
11661
13080
12038
13976
1431
10.24%
26286
33671
23304
28365
3040
10.72%
33461
43411
35810
41741
4277
10.25%
50251
37783
48198
52964
6701
12.65%
54484
J&6Q&7
/ .<"59372
^X7015 3
69243
17797
25.70%
69843
f 22620
105501
82698
78.39%
82246
78764
193361
206856
106.98%
11/15
73125
143913
209164
278185
350548
424319
11/15
72096
143404
207953
270207
336950
Average STD DEV %RSD
79920
160281
221307
360787
446565
570946
8799
16521
53402
252802
314972
387792
11.01%
10.31%
24.13%
70.07%
70.53%
67.92%
E-24
-------
Number
Number
Drift Drift Drift Drift Drift
11/04
11/07
11/08
11/11
11/12
17
1.14%
1.30%
-0.90%
-14.60%
-10.78%
19
0.47%
0.74%
-1.50%
4.43%
-14.27%
17
1.46%
1.99%
-0.75%
-18.98%
19
0.02%
0.71%
-1.53%
-9.55%
15.46%
19
12.62%
1.00%
0.46%
0.44%
-14.93%
19
576.56%
133.41%
15.62%
-42.34%
-3.25%
7
610.85%
Drift Drift
11/04
11/05
11/08
11/10
11/11
11/12
11/15
17
-1.53%
-27.01%
-3.51%
-15.72%
-10.29%
-9.37%
-1.41%
17
-2.33%
-5.13%
-3.29%
-8.68%
-10.16%
-5.28%
-0.35%
17
-2.26%
-3.56%
-3.45%
4.64%
-10.17%
587.59%
-0.58%
17
-1.92%
283.38%
-3.48%
6.35%
-7.82%
1.54%
-2.87%
17
-1.47%
286.59%
-3.43%
0.20%
-13.46%
-0.81%
-3.88%
16
0.86%
296.57%
-3.65%
-2.80%
-18.47%
-11.20%
Number
Drift
Drift
Drift
11/04
11/05
11/10
11/12
11/14
11/15
13
2.50%
-4.72%
129.73%
21.38%
2.53%
23.75%
13
2.25%
-4.21%
135.96%
21.63%
2.32%
28.08%
13
2.43%
-4.63%
138.55%
21.60%
2.50%
32.31%
12
2.57%
-4.33%
ERR
23.14%
3.36%
30.94%
13
2.47%
-4.49%
140.70%
23.46%
3.95%
27.39%
13
-0.47%
-4.10%
153.39%
23.07%
5.59%
31.55%
Number
Drift
Drift
Drift
11/05
11/12
11/14
11/15
10
-3.89%
0.48%
-1.78%
-9.55%
10
-3.70%
1.11%
-1.73%
-9.56%
10
-3.86%
1.22%
-1.84%
-10.04%
10
-3.74%
0.68%
-1.95%
-12.01%
10
-3.68%
0.56%
-2.11%
-13.98%
10
-3.59%
0.51%
-2.28%
-16.34%
3
-1.99% .
E-25
\
\
-------
RT
Area for
Concent rat ion (ppmv)
Linear Regression
Compound
(nun)
16
100
1000 Comments
Intercept Slope
Correlation
Methane
0.617
15999
95536
905018
3376.417 901.8102
0.999993
Ethane
1.022
31066
189807
1790196
6776.749 1783.816
0.999989
Propane
2. 462
45916
273712
2575271
10780.84 2565.044
0.99999
Butane
5.115
60812
358392
3377422
11159.31 3363.932
0.999992
Pentane
8.746
71702
138127
4192752
12207.25 4181.236
0.999994
Hexane
11.901
14185
658105
4947248 Improperly integrated
62950.9 4893.356
0.999272 RF
Heptane
13.789
69717
Improperly integrated
0.000229
m
K>
0\
-------
GC Linear Regression Data
+ + +
| | |Linear Regression Data |
1 1
1
I Correlation!
Date |Compound|
Weight |Intercept
Slope
jCoefficient j
11/04/5141 Methane |
13376.447
901.84
10.99999257 |
I Ethane 1
16776.749
1783.82
10.99998948 |
jPropane I
110780.84
2565.04
10.99999018 I
jButane j
|14159.34
3363.93
10.99999159 I
IPentane j
112207.25
4181.24
10.99999419 |
|Hezane I
| 62950.9
4893.36
10.99927223 |
11/05/SI4I Methane I
12708.746
897.632
10.99999691 I
j Ethane |
15249.526
1767.97
10.99999512 |
j Propane |
18170.547
2542.4
10.99999721 I
jButane I
110506.25
3334.05
10.99999722 |
j Pentane j
19341.581
4141.17
10.99999676 |
j Hexane |
1-12976.2
4901.95
10.99996059 I
11/07/94|Methane |
11150.286
815.107
|two points |
I Ethane I
11641.524
1622.9
j two points |
1 Propane I
13591.429
2319.54
|two points |
j Butane I
15482.095
3014.87
I two points j
1Pentane |
13176.286
3734.61
jtwo points j
IHexane |
1-5748.38
4415.02
I two points |
11/08/94|Methane |
I 1082
806.75
I two points |
j Ethane |
11601.619
1600.52
I two points j
I Propane |
13515.857
2287.57
I two points |
I Butane |
15192.905
2976.63
|two points |
IPentane |
12879.476
3689.6
j two points |
IHexane |
I 107047
3248.5
|two points j
E-27
-------
+
111/10/94
IMethane
1 o
1868.438
|one point I
| am
I Ethane
1 o
11740.31
jone point j
1
I Propane
1 o
12548.25
1 one point I
1
I Butane
i o
13689.44
I one point 1
1
|Pentane
1 o
13745.88
jone point I
1
IHexane
1 o
15143.81
j one point 1
111/10/94
|Methane
I -836.81
1920.738
|two points |
|pm
|Ethane
1-78.2381
I 1745.2
1 two points j
1
j Propane
15054.286
12232.36
j two points j
1
j Butane
115272.33
12734.92
j two points j
1
IPentane
1-3553.43
13967.96
j two points j
I ^
j Hexane
I -1229.1
15220.63
jtwo points j
111/12/94IMethane
1/x
I 239.978
1794.998
10.99898749 |
1
I Ethane
1/x
13985.222
11556.42
10.99918467 |
1
|Propane
- 1/x
1-4843.88
12298.78
| 0.99994 |
1
IButane
"l/x
1-9150.64
13068.53
10.99802154 |
1
|Pentane
1/x
1-2430.99
I 3752.2
10.99834513 |
1
|Hexane
1/X
11059.464
14354.76
10.99915915 |
|11/14/94
|Methane
1/X
1-253.503
1758.926
10.99578562 I
1
j Ethane
1/X
17086.875
11470.03
| 0.9946894 |
1
j Propane
1/X
13236.354
12224.25
10.99467784 1
1
|Butane
1/X
1-13071.2
12961.47
10.99482159 |
1
i Pentane
1/X
1-811.183
13705.42
10.99364179 |
I
j Hexane
1/X
1-48653.5
14405.24
10.99168796 |
111/15/94
I Methane
1/X
1148.5201
1726.573
10.99926723 |
1
I Ethane
1/X
1-172.724
11432.81
10.99912562 I
1
I Propane
1/X
1-377.334
12133.65
10.99810771 |
1
I Butane
1/X
1413.7706
12821.25
10.99803006 I
1
IPentane
1/X
1-636.619
13545.99
10.99760613 |
1
+
j Hexane
1/X
1-29861.5
14231.13
10.99661577 |
\
\
E-28
-------
GC Drift Data
GC Drift Data
IDate
1 H/04 |
11/05 |
11/07
1 11/08 |
U/10 |
11/11
1 Standard
|1000 ppmv|i
2000 ppmv|
16 ppmv
|100 ppmv|
100 ppmv|
100 ppmv
IMethane
I 2.50%|
-3.89%|
1.30%
I -3.51% f
-15.72%|
-10.29%
Ethane
I 2.25%1
-3.70%|
0.74%
I -3.29%|
-8.68%|
-10.16%
Propane
| 2.43%|
-3.86%|
1.99%
I -3.45%|
4.64%|
-10.17%
Butane
| 2.57%|
-3.74%|
0.71%
I -3.48%|
6.35%|
-7.82%
Pentane
I 2.47%|
-3.68%|
1.00%
I -3.43%|
0.20%|
-13.46%
Hexane a
| -0.47%|
-3.59%|
133.41% a
I -3.65%|
-2.80%|
-18.47%
a Integrator drew baseline inconsistently because of column bleed
Drift = (Final Area - Initial Area)/Initial Area x 100
GC Drift I)a
+ + + + +
IDate | 11/12 | 11/14 | 11/15 |
+ + + + +
I Standard |2000 ppmv|2000 ppmv|2000 ppmv|
+ + + +— +
I Methane | 0.48%| -1.78%| -9.55%|
I Ethane | 1.11%| -1.73%| -9.56%|
I Propane | 1.22% | -1.84%| -10.04%[
I Butane | 0.68% | -1.95%| -12.01%|
IPentane | 0.56%| -2.11%[ -13.98%|
IHexane a | 0.51%| -2.28%| -16.34%|
a Integrate
Drift = (Fi
E-29
-------
GC DATA CAMPAIGN 6
Engine/Turbine Load
+- +
Engine 10 Run 1
?kn'
gine 10 Run 3
Engine 12 Run 4
Engine 10 Run 2
Engine 12 Run 5
Turbine Run 6
Pollutant
Stack
Cone.
(ppmvw)
CI as Methane
C2 as Ethane
C3 as Propane
C4 as Butane
C5 as Pentane
C6 as Hexane
Heptane
Sum C2-C6 as CH4
CI as Methane
C2 as Ethane
C3 as Propane
C4 as Butane
C5 as Pentane
C6 as Hexane
Heptane
Sum C2-C6 as C4
CI as Methane
C2 as Ethane
C3 as Propane
C4 as Butane
C5 as Pentane
C6 as Hexane
Heptane
Sum C2-C6 as C4
CI as Methane
C2 as Ethane
C3 as Propane
C4 as Butane
C5 as Pentane
C6 as Hexane
Heptane
Sum C2-C6 as C4
CI as Methane
C2 as Ethane
C3 as Propane
C4 as Butane
C5 as Pentane
C6 as Hexane
Heptane
Sum C2-C6 as C4
CI as Methane
C2 as Ethane
C3 as Propane
C4 as Butane
C5 as Pentane
C6 as Hexane
pCi<* [e<,\ E'30
325.79
4.80
0.00
0.00
0.00
0.00
32.76
9.72
a
a, f
465.86 b
13.75 b,f
2.95 b
0.00
0.00
14.30
94.43
122.12 b,c
49
*naly-,
0.00
0.00
0.00
14.44 d,f
165.59 d,e
g
-HP
0.00
0.00
117a h
961.00
32.02
4.47 f,i
0.00
0.11
10.33
60.06
139.97
0.00
0.00
0.00
0.00
0.00
0.89 f
-------
GC DATA CAMPAIGN 6 Stack
Cone.
Engine/Turbine Load Pollutant (ppmvw)
I Engine 12 Run 4 | |CI as Methane 11392.72 d,f I
I | |C2 as Ethane | 44.61 d I
I | |C3 as Propane | 4.61 d,f I
I | |C4 as Butane | 0.00 I
I I |C5 as Pentane I 0.00 I
N I |C6 as Hexane | 0.00 j
| | |Heptane | 14.44 d,f I
| | |Sum C2-C6 as C4 | 103.04 d I
GC DATA CAMPAIGN 6
Engine/Turbine Load
+ +
Engine 10 Run 2
Pollutant
Stack
Cone,
(ppmvw)
I CI as Methane
I 416.65
g
j C2 as Ethane
I 8.83
f/9
|C3 as Propane
I 0.33
f
|C4 as Butane
| 0.00
|C5 as Pentane
I 0.00
CD
|C6 as Hexane
I -9rTt
|Heptane
\ 76.27
|Sum C2-C6 as C4
I 65.05
h
GC DATA CAMPAIGN 6
Stack
Cone.
Engine/Turbine Load
Pollutant
(ppmvw)
|Engine 12 Run 5 |
|CI as Methane
I 961.00
i
1
1 1
|C2 as Ethane
| 32.02
i
1
1 1
|C3 as Propane
I 4.47
f,i
1
1 1
|C4 as Butane
| 0.00
f
I
1 1
IC5 as Pentane
I 0.11
f
1
1 1
|C6 as Hexane
| 10.33
1
1 Heptane
I 72.65
1
1 1
|Sum C2-C6 as C4
I 139.97
J
1
\
\
-------
Turbine Run 7
CI as Methane
C2 as Ethane
C3 as Propane
C4 as Butane
C5 as Pentane
C6 as Hexane
Sum C2-C6 as C4
0.00
0.00
0.00
0.00
0.00
0.00
0.00
Turbine Run 8
CI as Methane
C2 as Ethane
C3 as Propane
C4 as Butane
C5 as Pentane
C6 as Hexane
Sum C2-C6 as C4
0.00
0.00
0.00
0.00
0.00
0.00
0.00
Engine 15 Run 9
CI as Methane
C2 as Ethane
C3 as Propane
C4 as Butane
C5 as Pentane
C6 as Hexane
Heptane
Sum C2-C6 as C4
717.92 f,gj£
22.26 q»-
5.01
1.96#»
1.86
11.54 g
33.58
145.97 g,1
Engine 15 Run 10
CI as Methane
C2 as Ethane
C3 as Propane
C4 as Butane
C5 as Pentane
C6 as Hexane
Heptane
Sum C2-C6 as C4
646.63 d.fi
18.86 6.0
5.62 d
o.7qgr-
0.00
9.84
44.64 d
113.62 d,m
Engine 15 Run 11
CI as Methane
C2 as Ethane
C3 as Propane
C4 as Butane
C5 as Pentane
C6 as Hexane
Sum C2-C6 as C4
1692.48 a,f#
41.32 a#_
8.55 a,ff?
0.00#
0.0C*
0.00# .
108.27 a|)
Engine 15
High Rebalance
CI as Methane
C2 as Ethane
C3 as Propane
C4 as Butane
C5 as Pentane
C6 as Hexane
Sum C2-C6 as C4
814.21 b,f#
25.87
0.00i
o.ooj
o.ooj
0.00*
51.74
i D,r<
1
t
Engine 9 Run 12
I
CI as Methane
C2 as Ethane
C3 as Propane
C4 as Butane
E-32
1854.78
49.64 a,n
6.33 a,n(
0.00
a,f ,rA\
I
-------
I Engine
|
9 Run 13
|CI as Methane
1086.81
o |
j C2 as Ethane
30.56
o |
|
|C3 as Propane
4.77
f 1
I
|C4 as Butane
0.00
1
|
|C5 as Pentane
0.00
1
|
|C6 as Hexane
0.64
f 1
1
ISuro C2-C6 as C4
79.29
o,p |
+-------
|Engine
|
9 Run 14
|CI as Methane
977.62
b |
|C2 as Ethane
27.51
b I
I
|C3 as Propane
6.81
f 1
I
|C4 as Butane
5.07
f 1
I
j C5 as Pentane
0.00
1
|
|C6 as Hexane
0.00
1
1
jSum C2-C6 as C4
95.73
b |
X —— — — — — 1
+
|Engine
1
13 Run 15
I CI as Methane
4 | A * W J |
j C2 as Ethane
~~r eaM
1
|C3 as Propane
I
|C4 as Butane
i
|
j C5 as Pentane
0.00
i
I
IC6 as Hexane
ju4o \ m i
1
I Heptane
37.32
i
1
I Sum C2-C6 as C4
516.63
d,q,r |
+
K- —------
+
|Engine
1
13 Run 16
1 CI as Methane
I n
j C2 as Ethane
¦fr" ¦ |"J? #iCc
-------
GC DATA CAMPAIGN 6 Stack
Cone.
Engine/Turbine Load Pollutant (ppmvw)
+ + + +
I Engine 13 Run 15 | 1 CI as Methane 11486.77 d |
I I |C2 as Ethane | 43.04 d |
I I |C3 as Propane | 133.26 g |
I I |C4 as Butane | 2.47 f,q |
I i |C5 as Pentane | 0.00 |
I | C6 as Hexane | 0.00 ^ |
I I |Heptane | 37.32 |
I | |Sum C2-C6 as CH4 | 495.74 d,q,r |
GC DATA CAMPAIGN 6 Stack
Cone.
Engine/Turbine Load Pollutant (ppmvw)
+ + + + +
I Engine 13 Run 16 | |C1 as Methane |1539.41 a |
I I |C2 as Ethane | 44.41 a I
I I |C3 as Propane | 5.16 f I
I I jC4 as Butane | 0.00 j
| I |C5 as Pentane | 0.00 |
I | C6 as Hexane | 0.00 |
1 | |Heptane | 7.91 j
I | |Sum C2-C6 as C4 | 104.30 a |
GC DATA CAMPAIGN 6 Stack
Cone.
Engine/Turbine Load Pollutant (ppmvw)
+ "~~ "• + + — — ^ — — +
|Engine 13 Run 21 | |C1 as Methane | 861.06 t |
I I |C2 as Ethane | 29.31 t |
I I |C3 as Propane | 0.00 I
I I |C4 as Butane | 0.00 |
I I |C5 as Pentane | 0.00 j
I | |C6 as Hexane | 0.00 j
I I |Heptane | 0.00 j
I I |Sum C2-C6 as C4 | 58.62 t |
E-34
-------
Engine 13 Run 23
CI as Methane
C2 as Ethane
C3 as Propane
C4 as Butane
C5 as Pentane
C6 as Hexane
Heptane
Sum C2-C6 as C4
1523.47
t
44.98
t
7.00
f,t
0.00
47.94
0.00
4.22
350.66
t,u
846.73
btt
26.54
bW
0.00 0
0.00
f
0.00
I
0.00
b#
13.41
53.09
b
1143.92
tf
35.15
0.00
#
0.00
m
0.00
#
0.00
f v
3.92
70.30
t
Engine 3A- Run 19
rt
CI as Methane
C2 as Ethane
C3 as Propane
C4 as Butane
C5 as Pentane
C6 as Hexane
Heptane
Sum C2-C6 as C4
Engine &T Run 22
H
Cl as Methane
C2 as Ethane
C3 as Propane
C4 as Butane
C5 as Pentane
C6 as Hexane
Heptane
Sum C2-C6 as C4
Engine #8" Hun 21
»l
Cl as Methane
C2 as Ethane
C3 as Propane
C4 as Butane
C5 as Pentane
C6 as Hexane
Heptane
Sum C2-C6 as C4
861.06 t^
29.31 t#
0.00
O.OOi
0.00
0.00 -
3.92 f#
58.62 t
tf
i
Engine Run 20
II
Cl as Methane
C2 as Ethane
C3 as Propane
C4 as Butane
C5 as Pentane
C6 as Hexane
Heptane
Sum C2-C6 as C4
832.43 t£
27.34 t»
0.00 #
0.00 £
0.00 #
0.00 V
1.53 f#
54.67 t
Engine 53P Run 24
II
Cl as Methane
C2 as Ethane
C3 as Propane
C4 as Butane
C5 as Pentane
C6 as Hexane
Heptane
Sum C2-C6 as C4
794.62 t#
26.92 tjr
0.00#
0.00#
o.oor
0.00 »
0.00#
53.84 t
a average of five determinations
E-35
-------
b average of three determinations
c average without hexane is 36.34 ppmv as CH4
d average of four determinations
e average without second sample is 1370.77 ppmv CI, 43.67 ppmv C2,
4.40 ppmv C3, and 100.54 ppmv C2-C6 as CH4
f extrapolated past calibration curve
g average of seven determinations
h average without hexane is 18.32 ppmv as CH4
1 average of 10 determinations
j average without hexane is 77.99 ppmv as CH4
k average without hexane is 0 ppmv as CH4
1 average without hexane is 76.70 ppmv as CH4
m average without hexane is 54.56 ppmv as CH4
n average without first sample is 2119.61 ppmv CI, 57.28 ppmv C2,
7.91 ppmv C3, and 138.30 ppmv C2-C6 as CH4
o average of 11 determinations
p average without hexane is 75.43 ppmv as CH4
q average without second sample is 4.11 ppmv propane, 0.00 ppmv butane,
and 128.27 ppmv as CH4
r average without second sample and without hexane is 100.42 ppmv as CH4
s average without hexane is 104.30 ppmv as CH4
t average of two determinations
u average without pentane is 110.96 ppmv as CH4
E-36
-------
Appendix F
Raw Operating Data
This appendix presents the raw engine and turbine operating data. Where available, these
data include test horsepower, engine speed, percent load, cylinder temperatures, ignition
\ timing, fuel pressures, fuel temperatures, fuel flow rates, compressor suction and discharge
pressures, compressor discharge temperatures, and compressor gas flow rates.
F-l
-------
Campaign 2 Process Data
Engine Process Data
Date
Time
Engine ID
Engine Manufacturer
Engine Model
Rated @site conditions
Test Hp
Engine Speed
Percent Load
Ignition Timing (degrees)
Fuel Flow Rate (chart,5 Ref)
Fuel Pressure (chart)
Fuel Flow Rate (MSCFD, 5 Ref)
Fuel Flow Rate (SCFH, per engine)
Fuel Pressure (psig, @ manifold inlet)
Scavenger Air Pressure (psig)
Power Cylinder Temperature - Left #1 (F)
Power Cylinder Temperature - Left #2 (F)
Power Cylinder Temperature - Left #3 (F)
Power Cylinder Temperature - Left #4 (F)
Power Cylinder Temperature - Left #5 (F)
Power Cylinder Temperature - Right #\ (F)
Power Cylinder Temperature - Right #2 (F)
Power Cylinder Temperature - Right #3 (F)
Power Cylinder Temperature - Right #4 (F)
Power Cylinder Temperature - Right #5 (F)
Compressor Discharge Temp - Cyl #\ (F)
Compressor Discharge Temp - Cyl #1 (F)
Compressor Discharge Temp - Cyl Ml (F)
Compressor Discharge Temp - Cyl #4 (F)
Compressor Discharge Temp - Cyl 05 (F)
Compressor Suction Pressure ("Hg, vacuum)
Compressor Discli. Press. Stage 1 (psig)
Compressor Disch. Press. Stage 2 (psig)
71
to
Engine Process Data
Date
3/12/94
3/12/94
3/12/94
3/12/94
Time
9:45
10:40
11:55
12:45
Engine ID
HI Ref
#2 Ref
#2 Ref
#2 Ref
Engine Manufacturer
Cooper
Cooper
Cooper
Cooper
Engine Model
GMV-10
GMV-10
GMV-10
GMV-10
Rated @site conditions
Test Hp
983.6
983.6
983.6
983.6
Engine Speed
282
284
285
282
Percent Load
79.9
79.9
79.9
79.9
Ignition Timing (degrees)
10
10
10
10
Fuel Flow Rate (chart,5 Ref)
4.40
4.40
4.40
4.40
Fuel Pressure (chart)
6.25
6.25
6.25
6.25
Fuel Flow Rate (MSCFD, 5 Ref)
590.76
590.76
590.76
590.76
Fuel Flow Rate (SCFH, per engine)
5445.36
5445.36
5445.36
5445.36
Fuel Pressure (psig, @ manifold inlet)
33
33
32
Scavenger Air Pressure (psig)
1
1
1
1
Power Cylinder Temperature - Left # 1 (F)
603
601
624
618
Power Cylinder Temperature - Left tt2 (F)
456
481
502
504
Power Cylinder Temperature - Left #3 (F)
558
563
581
576
Power Cylinder Temperature - Left #4 (F)
545
547
554
557
Power Cylinder Temperature - Left 05 (F)
530
539
567
557
Power Cylinder Temperature - Right tt\ (F)
651
654
661
659
Power Cylinder Temperature - Right #2 (F)
639
642
647
650
Power Cylinder Temperature - Right 03 (F)
608
623
657
648
Power Cylinder Temperature - Right #4 (F)
644
652
671
675
Power Cylinder Temperature - Right tt5 (F)
579
583
592
587
Compressor Discharge Temp - Cyl tt 1 (F)
178
177
Compressor Discharge Temp - Cyl #2 (F)
176
174
Compressor Discharge Temp - Cyl #3 (F)
59
60
Compressor Discharge Temp - Cyl #4 (F)
58
58
Compressor Discharge Temp - Cyl 05 (F)
62
61
Compressor Suction Pressure ("Hg, vacuum)
0.5
0.5
0.5
1.0
Compressor Disch. Press. Stage 1 (psig)
28.5
29.0
26.0
24.0
Compressor Disch. Press. Stage 2 (psig)
157
158
168
155
-------
Campaign 2 Process Data
Engine Process Data
Date
Time
Engine ID
Engine Manufacturer
Engine Model
Rated @site conditions
Test Hp
Engine Speed
Percent Load
Ignition Timing (degrees)
Fuel Flow Rate (chart,5 Ref)
Fuel Pressure (chart)
Fuel Flow Rate (MSCFD, 5 Ref)
Fuel Flow Rate (SCFH, per engine)
Fuel Pressure (psig, @ manifold inlet)
Scavenger Air Pressure (psig)
Power Cylinder Temperature - Left ti\ (F)
Power Cylinder Temperature - Left #2 (F)
Power Cylinder Temperature - Left #3 (F)
Power Cylinder Temperature - Left #4 (F)
Power Cylinder Temperature - Left ft5 (F)
Power Cylinder Temperature - Right #\ (F)
Power Cylinder Temperature - Right ft2 (F)
Power Cylinder Temperature - Right #3 (F)
Power Cylinder Temperature - Right 04 (F)
Power Cylinder Temperature - Right #5 (F)
Compressor Discharge Temp - Cyl #1 (F)
Compressor Discharge Temp - Cyl Wl (F)
Compressor Discharge Temp - Cyl ft3 (F)
Compressor Discharge Temp - Cyl #4 (F)
Compressor Discharge Temp - Cyl #5 (F)
Compressor Suction Pressure ("Hg, vacuum)
Compressor Disch. Press. Stage 1 (psig)
Compressor Disch. Press. Stage 2 (psig)
3/12/94
14:30
#2 Ref
Cooper
GMV-10
983.6
282
79.9
10
4.30
6.25
577.33
5305.51
31
I
621
510
577
555
559
661
647
639
668
590
173
172
58
57
60
1.0
23.5
148
3/12/94
15:30
ft2 Ref
Cooper
GMV-10
983.6
282
79.9
10
4.30
6.25
577.33
5305.51
31
I
620
500
576
559
557
660
648
636
669
587
173
172
58
57
1.2
23.5
148
3/12/94
16:25
n Ref
Cooper
GMV-10
983.6
283
79.9
10
4.30
6.25
577.33
5305.51
31
I
621
503
576
556
556
657
644
654
674
586
173
171
57
56
59
1.0
23.5
150
3/12/94
Average
n Ref
Cooper
GMV-10
983.6
283
79.9
10
4.35
6.25
584.04
5375.44
32
1
616
494
573
554
553
658
646
640
666
587
174
172
58
60
60
0.8
25.3
154
3/12/94
Max
#2 Ref
Cooper
GMV-10
983.6
285
79.9
10
4.40
6.25
590.76
5445.36
33
1
624
510
581
559
567
661
650
657
675
592
178
176
60
71
62
1.2
29.0
168
3/12/94
Min
Wl Ref
Cooper
GMV-10
983.6
281
79.9
10
4.30
6.25
577.33
5305.51
31
1
601
456
558
545
530
651
639
608
644
579
171
169
56
56
59
0.5
23.5
147
-------
Campaign 2 Process Data
Date
Date
3/13/94
3/13/94
3/13/94
3/13/94
Time
Time
9:40
10:35
10:55
11:40
Engine ID
Engine ID
Al Recom
#1 Recom
A1 Recom
01 Recom
Engine Manufacturer
Engine Manufacturer
Clark
Clark
Clark
Clark
Engine Model
Engine Model
BA-6
BA-6
BA-6
BA-6
Rated @site conditioas
Rated @site conditions
1140
1140
1140
1140
Test Hp
Test Hp
958.5
958.5
958.5
958.5
Engine Speed
Engine Speed
295
289
286
286
Percent Load
Percent Load
88
88
88
88
Ignition Timing (degrees)
Ignition Timing (degrees)
12
12
12
12
Fuel Flow Rate (chart,5 Recomp)
Fuel Flow Rate (chart,5 Recomp)
9.20
9.25
9.25
9.05
Fuel Pressure (chart)
Fuel Pressure (chart)
6.20
6.20
6.20
6.25
Fuel Flow Rate (MSCFD, 5 Recomp)
Fuel Flow Rate (MSCFD, 5 Recomp)
1537.68
1546.04
1546.04
1524.81
Fuel Flow Rate (SCFH, per Cooper engine)
Fuel Flow Rate (SCFH, per Cooper engine)
12814.036
12883.678
12883.678
12706.766
Fuel Pressure (psig, @ manifold inlet)
Fuel Pressure (psig, @ manifold inlet)
14.0
13.8
13.8
Scavenger Air Pressure (psig)
Scavenger Air Pressure (psig)
Power Cylinder Temperature #1 (F)
Power Cylinder Temperature #1 (F)
936
928
924
931
Power Cylinder Temperature #2 (F)
Power Cylinder Temperature #2 (F)
768
754
751
751
Power Cylinder Temperature A3 (F)
Power Cylinder Temperature #3 (F)
744
735
732
734
Power Cylinder Temperature A4 (F)
Power Cylinder Temperature A4 (F)
840
827
823
823
Power Cylinder Temperature A5 (F)
Power Cylinder Temperature A5 (F)
817
804
800
800
Power Cylinder Temperature A6 (F)
Power Cylinder Temperature A6 (F)
777
761
756
754
Compressor Discharge Temp - Cyl #1 (F)
Compressor Discharge Temp - Cyl #1 (F)
213
202
199
209
Compressor Discharge Temp - Cyl A2 (F)
Compressor Discharge Temp - Cyl #2 (F)
240
249
249
252
Compressor Discharge Temp - Cyl A3 (F)
Compressor Discharge Temp - Cyl A3 (F)
Compressor Discharge Temp - Cyl A4 (F)
Compressor Discharge Temp - Cyl #4 (F)
240
248
249
251
Compressor Suction Pressure (psig)
Compressor Suction Pressure (psig)
225
228
228
228
Compressor Disch. Press. Stage 1 (psig)
Compressor Disch. Press. Stage 1 (psig)
645
645
645
645
Compressor Gas Flow (chart)
Compressor Gas Flow (chart)
7.30
7.35
7.40
7.45
Compressor Gas Pressure (chart)
Compressor Gas Pressure (chart)
6.80
6.85
6.85
6.85
Compressor Gas Flow (MMscfd)
Compressor Gas Flow (MMscfd)
70.0
71.0
71.4
71.9
Compressor Gas Temp (F)
Compressor Gas Temp (F)
49.0
49.0
49.0
49.0
Oil Heater Data
Oil Heater Data
-------
Cainp?.'«n 2 Process Data
Date
3/13/94
Time
12:05
Engine ID
tt 1 Recom
Engine Manufacturer
ft . _.t
v-iaiK
Engine Model
BA-6
Rated ©site conditions
1140
Test Hp
958.5
Engine Speed
285
Percent Load
88
Ignition Timing (degrees)
12
Fuel Flow Rate (chart,5 Recomp)
9.05
Fuel Pressure (chart)
6.22
Fuel Flow Rate (MSCFD, 5 Recomp)
1517.49
Fuel Flow Rate (SCFH, per Cooper engine)
12645.773
Fuel Pressure (psig, @ manifold inlet)
13.8
Scavenger Air Pressure (psig)
Power Cylinder Temperature/CI (F)
923
Power Cylinder Temperature ft2 (F)
749
Power Cylinder Temperature #3 (F)
732
Power Cylinder Temperature #4 (F)
824
Power Cylinder Temperature #5 (F)
800
Power Cylinder Temperature #6 (F)
756
Compressor Discharge Temp - Cyl #\ (F)
207
Compressor Discharge Temp - Cyl #2 (F)
253
Compressor Discharge Temp - Cyl #3 (F)
Compressor Discharge Temp - Cyl #4 (F)
253
Compressor Suction Pressure (psig)
228
Compressor Disch. Press. Stage 1 (psig)
648
Compressor Gas Flow (chart)
7.40
Compressor Gas Pressure (chart)
6.87
Compressor Gas Flow (MMscfd)
71.6
Compressor Gas Temp (F)
49.5
Oil Heater Data
I
KS\
3/13/94
3/13/94
3/13/94
3/13/94
3/13/94
3/13/94
3/13/94
Average
Ma*
Min
13:10
13:50
14:45
16:00
tt\ Recom
#1 Recom
tt\ Recom
#1 Recom
M\ Recom
#1 Recom
#1 Recom
Ciark
Ciark
Clark
Clark
Clark
Clark
Clark
BA-6
BA-6
BA-6
BA-6
BA-6
BA-6
BA-6
1140
1140
1140
1140
1140
1140
1140
958.5
958.5
958.5
994.2
994.2
994.2
994.2
288
295
285
295
293
296
293
88
88
88
92
92
92
92
12
12
12
12
12
12
12
9.16
9.25
9.05
9.35
9.25
9.30
9.38
6.21
6.25
6.20
6.22
6.22
6.22
6.22
1534.46
1558.51
1512.61
1567.80
1551.03
1559.41
1572.83
12787.132
12987.578
12605.112
13064.97
12925.238
12995.104
13106.89
13.9
14.0
13.8
15.0
15.0
15.0
15.0
928
936
923
942
950
935
930
755
768
749
783
785
797
803
735
744
732
765
767
780
784
827
840
823
864
865
880
883
804
817
800
838
840
853
859
761
777
754
796
798
816
821
206
213
199
202
211
213
215
249
253
240
253
255
257
258
248
253
240
254
255
257
259
227
228
225
235
235
238
238
646
648
645
648
650
650
648
7.38
7.45
7.30
7.50
7.45
7.43
7.35
6.84
6.87
6.80
7.00
7.00
7.00
7.00
71.2
71.9
70.0
74.0
73.5
73.3
72.5
49.1
49.5
49.0
50.0
50.0
50.0
50.0
-------
Campaign 2 Process Data
Date
3/13/94
Time
16:50
Engine ID
#\ Recom
Engine Manufacturer
Clark
Engine Model
BA-6
Rated @site conditions
1140
Test Hp
994.2
Engine Speed
296
Percent Load
92
Ignition Timing (degrees)
12
Fuel Flow Rate (chart,5 Recomp)
9.40
Fuel Pressure (chart)
6.22
Fuel Flow Rate (MSCFD, 5 Recomp)
1576.18
Fuel Flow Rate (SCFH, per Cooper engine)
13134.836
Fuel Pressure (psig, @ manifold inlet)
15.0
Scavenger Air Pressure (psig)
Power Cylinder Temperature #1 (F)
923
Power Cylinder Temperature Ml (F)
811
Power Cylinder Temperature #3 (F)
791
Power Cylinder Temperature 04 (F)
888
Power Cylinder Temperature #5 (F)
864
Power Cylinder Temperature #6 (F)
825
Compressor Discharge Temp - Cyl #1 (F)
210
Compressor Discharge Temp - Cyl #2 (F)
254
Compressor Discharge Temp - Cyl A3 (F)
Compressor Discharge Temp - Cyl #4 (F)
256
Compressor Suction Pressure (psig)
238
Compressor Disch. Press. Stage 1 (psig)
650
Compressor Gas Flow (chart)
7.30
Compressor Gas Pressure (chart)
7.05
Compressor Gas Flow (MMscfd)
72.5
Compressor Gas Temp (F)
50.0
Oil Heater Data
~rl
I
CTn
3/13/94
3/13/94
3/13/94
3/13/94
3/13/94
3/14/94
3/14/94
17:40
18:40
Average
Mai^
Min
8:25
9:25
01 Recom
#1 Recom
ft 1 Recom
#1 Recom
#\ Recom
#1 Recom
#\ Recom
Clark
Clark
Clark
Clark
Clark
Clark
Clark
BA-6
BA-6
BA-6
BA-6
BA-6
BA-6
BA-6
1140
1140
1140
1140
1140
1140
1140
994.2
994.2
994.2
994.2
994.2
293
296
295
296
293
295
293
92
92
92
92
92
12
12
12
12
12
12
12
9.33
9.30
9.33 ¦
9.40
9.25
9.38
9.30
6.22
6.30
6.23
6.30
6.22
6.20
6.20
1564.44
1579.47
1567.32
1596.45
1551.03
1567.77
1554.40
13037.024
13162.244
13060.978
13303.773
12925.238
13064.745
12953.319
15.0
15.0
15.0
15.0
15.0
15.0
15.0
937
938
936
950
923
939
934
808
805
799
811
783
768
769
790
784
780
791
765
760
763
887
880
878
888
864
856
857
864
860
854
864
838
832
835
824
816
814
825
796
788
789
212
224
212
224
202
209
216
250
250
254
258
250
252
248
ERR
ERR
ERR
251
251
255
259
251
251
247
240
238
237
240
235
240
230
650
650
649
650
648
648
648
7.25
7.40
7.38
7.50
7.25
6.60
6.80
7.05
7.00
7.01
7.05
7.00
7.00
6.80
72.0
73.0
73.0
74.0
72.0
65.1
65.2
50.0
50.0
50.0
50.0
50.0
52.5
52.0
-------
Gri Air Toxics Phase 2
Engine Proceae Data
Engine Proceia Data
Dat#
Date
3/12/04
3/12/94
3/12/94
3/12/94
3/12/94
3/12/04
3/12/04
3/12/04
3/12/04
3/12/04
3/12/04
Tim#
Time
045
1040
11.55
12.45
13.90
1430
15.30
16 25
Average
Max
Mln
Engine ID
Engine ID
#2 Ref
#2 Ref
#2 Ref
#2 Ret
#2 Ref
#2 Ret
#2 Ref
#2 Ref
#2 Ref
#2 Ref
#2 Rel
Engine Manufacturer
Engine Manufacturer
Cooper
Cooper
Cooper
Cooper
Cooper
Cooper
Cooper
Cooper
Cooper
Cooper
Cooper
Engine Model
Engine Model
GMV-10
GMV-10
rsMV.m
RMV.10
GMV 10
OMtVIC
GMV-10
GmV-iu
GMV-io
GMV-10
GMV-10
Engine Proceea Data
Engine Proceta Date
Data
Date
3/12/94
3/12/94
3/12/04
3/12/94
3/12/94
3/12/04
3/12/04
3/12/04
3/12/94
3/12/04
3/12/04
Time
Time
0:45
10:40
11:55
12:45
13:30
14:30
15:30
16:25
Avwege
Max
Mln
Englna ID
Engine ID
#2Ref
#2Ref
#2 Ref
#2 Ref
#2 Ref
#2 Ref
#2 Ref
#2 Ref
#2 Ref
#2 Ref
#2 Rel
Engine Manufacturer
Engine Manufacturer
Cooper
Cooper
Cooper
Cooper
Cooper
Cooper
Cooper
Cooper
Cooper
Cooper
Cooper
Engine Model
Engine Model
GMV-10
GMV-10
GMV-10
GMV-10
GMV-10
GMV-10
GMV-10
GMV-10
GMV-10
GMV-10
GMV-10
Rated r^alte eondltiont
Rated f^elte condition®
Teat Hp
Teit Hp
983 6
903.6
093 9
983 8
093.6
063 6
063 6
063.6
083 6
083 6
093 6
Engine Speed
Engine Speed
282
294
295
292
291
262
262
283
293
265
281
Percent Load
Percent Load
79 0
79 9
79 0
79 0
70 0
79 0
70.0
70.0
70.0
70 0
79 9
IgnlHon Timing (degree*)
Ignition Timing (degreea)
10
10
10
10
10
10
10
10
10
10
10
Fuel Flow Rale (chart.5 Ref)
Fuel Flow Rate (chart,S Ref)
4.40
4 40
4.40
4 40
4 30
4 30
4.30
4 30
4.35
4 40
4 30
Fuel Preaaure />-h»rt)
Fuel Preaeure (chart)
S 25
0.25
6 25
9.25
6 25
6.25
6.25
6 25
6 25
6 25
8.25
Fuel Flow Rate (M-iCFD, 5 Ref)
Fuel Flow Rate (MSCFD, 5 Ref)
590.76
590 76
590 79
590 79
577.33
577 33
577.33
577 33
(5375.4V
500 76
577 33
Fuel Flow Rate (SCFH. per engine)
Fuai Flow Rate (SCFH, per engine)
5445 39
5445 38
5445 39
5445 36
5305 51
5305.51
5305 51
530531
544536
5305.51
Fuel Preaeure (peig, (<$ manifold inlet)
Fu«l Preaeure (psfg. <§> manifold Inlet)
33
33
32
31
31
31
31
32
33
31
7»
^4
-------
Gri Air Toxics Phase 2 -
Engine Process Data
Date
Time
Engine ID
Engine Manufacturer
Engine Model
Date
3/13/94
3/13/94
3/13/94
Time
Average
Max
Min
Engine ID
#1 Recom
#1 Recom
#1 Recom
Engine Manufacturer
Clark
Clark
Clark
Engine Model
BA-6
BA-6
BA-6
Rated @site conditions
1140
1140
1140
Test Hp
994.2
994.2
994.2
Engine Speed
295
296
293
Percent Load
92
92
92
Ignition Timing (degrees)
12
12
12
Fuel Flow Rate (chart,5 Recomp)
9.33
940
9.25
Fuel Pressure (chart)
6.23
6.30
6.22
Fuel Flow Rate (MSCFD, 5 Recomp)
1567.32
1596 45
1551.03
Fuel Flow Rate (SCFH, per Cooper engine)
(13060.978
") 13303.773
12925.230
Fuel Pressure (psig, @ manifold inlet)
15.0
15.0
15 0
Scavenger Air Pressure (psig)
I
00
-------
F.2 Campaign 3
Oft Campaign #3
Tim
Nvapvair
frtf)
«Mi)
«J)
(p«0
(rpm)
(•dm)
1030
1151
68
213
360
300
130.1
1090
1141
05
210
365
300
145.4
1045
1150
66
213
350
300
130.0
1045
1142
se
215
365
300
145.4
1700
1151
55
213
360
SM
1304)
1100
1145
06
217
304
300
145.5
1715
1150
66
213
360
300
130.1
1115
1144
06
216
366
300
1453
1730
1146
66
213
360
a*
138.6
1130
1142
06
217
306
301
149.6
1745
1146
50
213
3*0
300
130.4
1145
1141
se
216
366
300
145.1
1S00
1145
58
213
365
300
13*3
1200
1142
06
216
366
300
145.6
1615
1150
66
212
366
300
130.2
1215
1145
06
219
305
300
145.0
1530
1146
85
213
366
300
138.8
1230
1140
06
217
306
301
140.4
1045
1145
66
212
360
300
136.7
1245
1140
M
216
306
300
1453
1000
1146
88
212
357
300
138.4
1300
1146
06
210
366
300
145.6
1015
1146
60
212
367
300
1303
1315
. 1144
06
210
306
300
145.5
1830
1145
55
212
367
2*0
1383
1330
1146
07
217
305
300
140.1
1045
1144
60
212
357
300
140.0
1345
1140
U
210
305
300
146 J)
2000
1146
66
212
357
300
1303
1400
1144
se
210
305
2M
145.0
2015
1143
55
212
357
300
135.5
1415
1144
S7
217
305
2*9
140.0
2025
1146
86
213
367
300
1363
1430
1140
67
210
305
200
145.0
Average
1146
67
214
300
300
1413
Awng*
1145
se'
215
306
300
145.7
F-9
\
-------
6RI Campaign #3
Compressor Station 3A
Engins1Q2 Engins 101
6/14/94
6/15/94
Run 1 Full U
Md
Fust Flow
Powsr
Run 1 Rsducsd Load
Fusl Flow
Powsr
Tims
BMEP
flpssd
(cfh)
(hP)
Tims
BMEP
3pncl
(cfh)
-------
v -
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Eayc Torj<*c (%)
l|nitioc *npiia| (degrees)
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FUEL MANIFOLD
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20.^-
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36, a
AIR rVTAKE MANIFOLD
Air Roar Rate (acta)
Air Muifold Temperature (°F)
im:
Air MuifoM frtmire (in H| oryit)
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RXHAUST MANIFOLD
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P£>
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595"
Prarare (la Hg)
Scxvcofei Air Pressure (psit)
CYLINDER TEMPERATURES
Cylinder # I
Cylinder #
Cylinder #
Cylinder #
Cylinder #
Cylinder #
Cylinder #
Cylinder #
Cylinder #
Cylinder #
Cylinder #
Cylinder #
3£
£
Compressor Capacity (MMsctJtf
E
1
:Me
Compressor Swctioo Pressure (psfr)
£L
2^
fc
Coapnwor Section Temperiiurt (°F)
w
Wzt7
ioz-
Mr
Compressor Dtscharfe Procure (p*'t)
4-3(0
^g-5
I Compressor Discharge Temperature (°F)
J2S_
22^
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774
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F-vd pAftj {itu-^fckX
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-------
Compressor Cylinder
Performance Report
Station:
Unit No.:
#4
D*e;
6I$I94
Mfg./T)pe:
Cooptr III imii OMWA-8
TertType:
Toxic Emtsnoo Toting Rm #1 Full Lo*
J lltttan.
Cyl.No.
HE/CE
IHP
RPM
Suction AEV
<*>
Discharge
AEV (%)
Suction
Termnal
Pressure
(psig)
Discharge
Tenninal
Pressure
(p**s)
Suction
Tan>.(°F)
Discharge
Temp. (°F)
(2)
Suction
Condition
a
(Z) Discharge
1
hi:
497JO
2503
72.05
36.48
73.93
189.65
74.0 T
165.0 °F
1.0000
1.0000
1
ct.
326.84
250.6
80.12
41.49
74.96
187.40
74.0 "F
165.0 "F
1.0000
1.0000
2
he;
435.57
249.1
74.50
44.43
179.81
379.95
133.0 "T
216.0 °F
1.0000
1.0000
2
CE
493.15
249.5
91.75
52.90
181.07
365.36
133.0 "F
216.0 °F
1.0000
1.0000
PbQwa)*
14.4
R factor"
459.7
(Z)«d-
1.000
Total IHP-
1952.86
@ 249.9
* Average RPM
Mechanical Efficiency =
0.95 ICoopreaor BHP -
2055.64
Total BHP Lot
id =
Coo^ressor BHP
2055.64
+
Accessory BHP
40.00
-
2095.64
Mfg. rated BHP -
2000.00
f§
250.0
RPM (Manufacture's rated qwed)
Curve BHP-
1981
Alluded BHP
1999.06
249.9
RPM (average test operating speed)
Load Step *
5
Test Torque Laid -
104.83%
NDifference «=
-3.77%
| Cylinder Capacity (Votame) I
Suction Conditions
CyL No.
immcFd
CyL No.
nmxfd
Total Capacity=
22.506
rancid
1 HE
10.836
2 HE
10.165
ICE
11.952
2 CE
12.058
BHP'imrncfd^
93.115
ToUl=
22.789
Total-
22.223
Discharge CondttkMM
CyL No.
nnmdd
CyL No.
tmmcfd
Toul Cipacity=
22.707
lDBXfd
1 HE
10.827
2 HE
10.799
ICE
11.941
2 CE
11.847
BHP/ixnmcfd=
92.291
Tcul=
22.768
ToUl=
22.646
Cylinder Flow Bdanct (Qi/Qd)
Cyl No.
QvQd
CyL No.
Qs/Qd
1
Total Capacity (Qsy(Qd)3*
0.991
1 HE
1.001
2 HE
0.941
1 CE
1.001
2 CE
1.018
I HE Qs Qd ~ CE Qs/Qd
0.750
0.800
0.850
0.900 0.950 1.000 1.050 1.100
Discharge Leakage= 1 l=Suction Leakage
1.150
1.200
1.250
F-35
-------
Compressor Cylinder
Performance Report
Station:
Unit No.:
#4
IMe:
6094
Mfe/Type:
Cooper De»euicf GMWA-8
Tert Type:
Toxic Emission Testing Run #1 Full Load
CyL No.
HE/CE
IHP
RPM
Suction AEV
Discharge
Suction
Discbarge
Suction
Discharge
(Z)
(Z)Diadurge
(%)
AEV (%)
Terminal
Pressure
(psig)
Terminal
Pressure
(PSig)
Ten^fF)
T<=H>. (°F)
Suction
Condiuan
s
Conditions
1
HE
489.35
246.6
72.87
39.11
73.97
181.17
72.0 °F
165.0 °F
1.0000
1.0000
1
CE
516.87
2463
80.12
40.63
73.93
188.57
72.0 °F
165.0 °F
1.0000
1.0000
2
HE
433.42
247.9
75.30
43.55
. 179.90
384 44
132.0 "F
214.0 °F
1.0000
1.0000
2
CE
485.40
246.4
91.30
51.12
182.15
375.01
132.0 °F
214.0°F
1.0000
1.0000
Pb(p«a)«
14.4
R factor9
459.7
(Z)rtd*
1.000
Total IHP-
1925.04
© 246.8
¦ Average RPM (Medianics! Efficiency =
0.95 {Compressor BHP *
202636
ToUl BHP Load =
Con?ressor BHP
2026.36
+
Accessory BHP
40.00
-
2066J6
Mfg. rated BHP =
2000.00
250.0
RPM (Manufacture'* rated speed)
Curve BHP =
I960
Adjusted BHP
=
1974.27
@
246.8
RPM (average test operating q>eed)
LotdSup-
5
Teat Torque Load =
104.66*/*
^Difference-
-339%
1 C^flfaider Capacity (Vohane) |
Suction Conditions
CyL No.
inancfd
Cyl. No
iinmrfd
Total Capacity^
22.339
mwirfi
1 HE
10.841
2 HE
10.246
1 CE
11.655
2 CE
11.936
BHPimmc£d=
92.500
Total=
22.496
Total-
22.182
Discharge Conditions
CyL No.
tmmcfd
Cvl. No.
mnncfd
Total Capacity^
22.415
1 HE
10.961
2 HE
10.682
1 CE
11.560
2 CE
11.629
BHP/immcfd=
92.185
Total=
22.520
Total=
22.310
Cvtindcr Flow Balance (Qs/Qd)
Cyl. No.
Qs-Qd
Cvl. No.
Qs/Qd
I
Total Capacity (Qsy(Qd)=
0.997
1 HE
0.989
2 HE
0.959
1 CE
1.008
2 CE
1.026
¦ HE Qs Qd ~ CE Qs/Qd
¦
I
, 1 , ,
0.750 0.800 0.8J0 0.900 0.950 1.000 1.050 1.100 1.150 1.200 1.250
Discharge Leakage=l l=Suction Leakage
F-36
-------
Compressor Cylinder
Performance Report
Sution:
Unit No.:
#2
Due.
6/18/94
Mfg./T>pe:
Cocjw Beoemer GMV-10TF
Tea Type:
Toxic Exninion Toting Rin #2; Full Lom
11130 am.
Cyi No.
HE/CE
IHP
RPM
Suction
AEV (S)
Discharge
AEV(%)
Suction
Termkul
Pressure
(prig)
Dttdnry
Tcnnmil
Pressure
(pag)
Suction
Tcnp. (°F)
Dtadiarge
Temp. (°F)
(Z) Suction
Conditions
(Z)DiBdune
GndUoM
1
m
164.77
300.8
61.63
29.73
87.86
219.65
74.0 "F
171.0 °F
1.0000
1.0000
1
CE
159.58
300.4
60.37
31.41
87.86
217.50
74.0 °F
171.0 °F
1.0000
1.0000
2
HE
10333
299.9
36.27
18.67
84.60
2I6JI
74.0 °F
169.0 °F
1.0000
1.0000
2
CE
230.90
301.1
84.59
42.19
85.76
220.84
74.0 °F
169.0 "F
1.0000
1.0000
3
HE
105.18
300.2
76.79
50.81
216.31
372.66
1I2.0°F
170.0 °F
1.0000
1.0000
3
CE
93.84
301.0
76.11
48.31
217.38
374.80
112.0°F
170.0 f
1.0000
1.0000
4
HE
110.93
299.6
78.34
51.69
218.45
373.73
112.0 °F
171.0 °F
1.0000
1.0000
4
CE
97.00
299.9
75.40
50.08
216.55
373.07
112.0°F
171.0 °F
1.0000
1.0000
Pb(p*ii>*=
14.7
R factor9
459.7
(Z)*d-
1.000
Tou! IHP-
1065.53
@ 300.4
« Average RPM
Medimical Efficiency -
0.95
Comprenar BHP ¦
1121.61
^oUl BHP Load "
Compreaor BHP
1121.61
+
Accasory BHP
20.00
-
1141.61
rated BHP
-
1100.00
@
300.0
RPM (Manufacture's rated qwed)
Curve BHP-
1140
Derated BHP*
110133
@
300.4
RPM (average test operating apeed)
Load Step-
6
Tot Torque Lot
id*
103.66V
^Difference =
1.61%
| Cytinder Capadty (Vohimc)
Suction Conditions
Cyl. No.
immcfd
Cyl. No.
tmmcfd
Cyl. No.
immcfd
Cyl. No.
tmmcfd
Total Capacity - 14.211 imnicfd
BHP/immcfd= 80.334
1 HE
[CE
3.741
3.558
2 HE
2 CE
2.126
4.894
3 HE
3 CE
3.653
3.376
4 HE
4 CE
3.754
3.320
Toul=
7.299
Total=
7.020
Total=
7.029
ToUl=
7.074
Discharge Conditions
Cyl. No.
imnicfd
Cyl. No.
tmmcfd
Cyi. No
immcfd
Cyl. No.
inmtfd
Toul Capacity = 14.046 imnacftl
BHP/immcfd- 81.276
1 HE
1 CE
3.489
3.547
2 HE
2 CE
2.161
4.859
3 HE
3 CE
3.679
3.265
4 HE,
4 CE
3.741
3.352
Toul=
7.036
Toul=
7.019
ToUl=
6.944
TaUl=
7.092
CMinder Flow Balance (Qi/Qd)
Cyl. No.
Qv'i^d
Cyl. No.
Qs/Qd
Cyl. No.
Q*Qd
Cyl. No.
C*Qd
Total Capacity Qs/Qd= 1.012
1 HE
1 CE
1.072
2 HE
2 CE
0.984
3 HE
3 CE
0.993
4 HE
4 CE
1.004
1.003
1.007
1.034
0.990
¦ HE Qs/Qd ~ CE Q& Qd
4
J
.
0.750 0.800 0 850 0.9<)O 09J0 1.000 1 050 1.100 1 150 1.200 1.250
Discharge Leakage=ll=Suction Leakage
F-37
\
\
-------
Compressor Cylinder
Performance Report
Sutkn: ¦
Uhk No.:
#2
D~:
6/19/94
MTg/Type:
Cooper Banner OMV-10TF
T«*Type:
Tone Eimsn Testing Run #3 ; 103 % Load; 6:00 pm.
CyL No.
HE/CE
IHP
RPM
StKXlOD
Discharge
Suction
Discharge
Suction
Dischafg*
(Z) Suction
(Z)Diacfear9E
AEV (%)
AEV (%)
Terminal
Pressure
(psig)
Tennmal
Pressure
0»&)
Temp. (°F)
Temp- (°F)
Conditions
1
HE
163.23
299.4
58.09
30.57
85.72
218.58
74.0 °F
171.01°F
1.0000
1.0000
1
CE
15932
299.8
61.22
32.21
88.88
215.24
74.0 °F
171.0 °F
1.0000
1.0000
2
HE
103.87
300.1
38.78
19.40
86.74
217J8
74.0 °F
169.0 °F
1.0000
1.0000
2
CE
229.79
300.1
84.59
43.06
86.84
221.91
74.0 °F
I69.0°F
1.0000
1.0000
3
HE
103.90
299.5
76.79
49.92
215.36
370.72
110.0 °F
168.0 °F
1.0000
1.0000
3
CE
92.85
300.6
75.40
49.19
213.22
369.65
IIO.O °F
168.0 °F
1.0000
1.0000
4
HE
110.35
299.7
78.34
52.57
219.53
371.59
110.0 °F
170.0 °F
1.0000
1.0000
4
CE
96.14
300.1
75.40
50.97
216.43
370.72
110.0 °F
170.0 °F
1.0000
1.0000
Pb (jm*)*
14.7
R fjctor=
459.7
(Z)Ad=
1.000
Toul IHP =
1059.47
@299.9
« Average RPM I
Median ical Efficiency *
0.95
Compressor BHP «=
1115.23
ToulBHPLowl-
CuiyimorBHP
1115.23
+
Accessory BHP
20.00
-
1135.23
Mfg.nUxlBHP
-
1100.00
@
300.0
RPM (Manufacture's rated q>eed)
Curve BHP =
1133
Dented BHP'
1099.71
@
299.9
RPM (average test operating speed)
Load Step-
6
Teal Torque Load -
103.23%
^Difference =
1.57%
Cylinder Capacity (Vofamw)
Sadkw Conditions
CyL No.
msDcfd
Cyl. No.
immcfd
Cvl. No.
immcfd
Cyl. No.
immcfd
Total Capacity = 14.189 immcfd
BHP/imrocfd= 80.007
1 HE
1 CE
3.437
3.636
2 HE
2 CE
2.323
4.931
3 HE
3 CE
3.642
3.291
4 HE
4 CE
3.786
3.332
Tctal=
7.073
Tc*al=
7.254
Tctal=
6.934
Total=
7.117
Disdwrge Coorfftkms
Cyl. No.
immcfd
Cyl. No.
immcfd
Cyl. No.
immcfd
Cyl. No.
immcfd
Total Capacity = 14.224 immcfd
BHP/immcfd= 79.812
I HE
ICE
3.556
3.594
2 HE
2CE
2.257
4.965
3 HE
3 CE
3.600
3.287
4 HE
4CE
3.791
3.398
Total=
7.149
Total-
7.222
Total=
6.888
Total=
7.189
Cylinder Flow Balance (Qs/Qd)
Cyl. No.
Qs/Qd
Cyl. No.
Qs/Qd
Cyl. No.
Qs/Qd
Cyl. No.
Qs/Qd
Total Capacity Q&Qd= 0.998
1 HE
ICE
0.967
2 HE
2 CE
1.029
3 HE
3 CE
1.012
4 HE
4 CE
0.999
1.012
0.993
1.001
0.981
¦ HE Qs/Qd ~ CE QsJQA
S 3
i
Z
•s
q i
_ Li,
V
i
1
0.750
0.850 0.9<>0 0.950 '-"'- 1.000 1.050 1.100
Discharge Leakage=ll=Suction Leakage
1.150
1.200
1.250
F-38
-------
Power Cylinder
Performance Report
Station: 4MMI
Unit No.:
#2
Date:
6/19/94
Mfg:
Cooper Bessemer GMV-10TF
Tvoe: GMV-10TF
Rated BHP:
1100
Cyl. No.
IH P
RPM
Compression
Pressure @
Peak Firing
Peak Pressure
Terminal
Exhaust
Pressure
TDC (psig)
Pressure (psig)
Angle (°Atdc)
Pressure
Temperature
(psig)
(psig)
(°F)
1
124.59
290.5
240.81
284.69
544.77
14°atdc
46.02
686 *F
2
127.33
290.7
247.10
280.26
516.65
17°atdc
47.07
760 °F
3
128.29
291.1
250.30
305.93
547.68
15°atdc
48.14
711 °F
4
335.02
290.6
247.23
290.04
530.85
I7°atdc
46.02
717 °F
5
133.17
290.8
237.60
281.48
535.13
16°atdc
48.16
695 °F
6
128.13
290.9
236.40
269.56
504.89
18°atdc
41.72
750 *F
7
137.18
290.6
241.61
282.24
540.96
17°atdc
48.11
693 QF
8
135.05
290.7
244.02
280.41
480.55
20°atdc
49.23
747 °F
9
135.86
290.4
240.55
288.65
558.07
16°atdc
49.18
725 °F
10
131.26
291.1
234.39
277.20
558.68
16°atdc
44.95
745 °F
Ignition Tyre:
Altronic 2
Timing:
11 Btdc
Primarv:
345 Volts
DD Indicated Horsepower (IMP) M Peak Firing Pressure H Indicated Mean Effective
" Pressure (DV1EP)
600.00
500.1
g 400.03
P
p 300.00
s
^ 200.00
100.00
0.00
Power Cylinder Summary
Hoi-sepower
Peak Firing Pressure (psig)
Compression / Tdc / Terminal Pressure
IHP (Total) -
1315.87
Maximum
Average
Minimum
Maximum
Average
Minimum
IHP (Average) =
131.59
558.68
531.82
480.55
250.30
242.00
234.39
IHP (Maximum) =
137.18
Peak Firing Pressure Angle
305.93
284.05
269.56
IHP (Minimum) =
124.59
20°atdc
16.6°atdc
14°atdc
49.23
46.86
41.72
1 23456789 10
Cylinder Number
F-39
-------
Power Cylinder
Performance Report
Station:
Compressor Station
Unit No.:
#4
Date:
6/19/94
Mfg:
Cooper Bessemer
Type:
GMWA-8
Rated BHP:
2000
Cyl. No.
IHP
R PM
Compression
Pressure @
Peak Firing
Peak Pressure
Terminal
Exhaust
Pressure
TDC (psig)
Pressure (psig)
Angle (°Atdc)
Pressure
Temperature
(psig)
(psig)
(°F)
1L
247.24
247.3
228.09
250.58
501.16
16°atdc
41.76
640 °F
2L
286.31
248.0
224.88
246.30
487.24
19°atdc
46.05
592 °F
3L
287.00
249.3
228.09
252.72
531.15
16°atdc
44.98
666 °F
4L
282.40
248.1
246.16
290.04
564.03
15°atdc
49.23
628 °F
1R
248.23
248.5
229.16
259.15
529.00
12°atdc
43.91
652 "F
2R
263.71
246.6
209.89
229.16
430.48
23°atdc
43.91
617 "F
3R
277.21
248.4
227.02
249.51
500.09
19°atdc
42.83
680 °F
4R
284.77
248.2
240.00
263.58
519.65
15°atdc
48.22
627 °F
Ignition Type:
Bendix SS
Timing:
8 Btdc
Primary:
370 Volts
BID Indicated Horsepower (IHP) H Peak Firing Pressure
Indicated Mean Effective
Pressure (IMEP)
600.00
1L
2L
3L
4L 1R
Cylinder Number
2R
3R
4R
Power Cylinder Summary
Horsepower
Peak Firing Pressure (psig)
Compression / Tdc / Terminal Pressure
IHP (Total) =
2176.87
Maximum Average
Minimum
Maximum
Average
Minimum
IHP (Average) =
272.11
564.03
507.85
430.48
246.16
229.16
209.89
IHP (Maximum) = 287.00
Peak Firing Pressure Angle
290.04
255.13
229.16
IHP (Minimum) = 247.24
23°atdc
16.9°atdc
12°atdc
49.23
45.11
41.76
F-40
\
-------
Compressor Cylinder
Performance Report
Station:
Mfg./Type:
Coopr Beaa
emer GMV-10TF
Unit No.:
Test Type:
#2 1 Date: 6/20/94
Toxic Emision Testing, Ri*» #4:103% Load, 11 rOO am.
CyLNo.
HE/CE
IHP
RPM
Suction
AEV (%)
Discharge
AEV(%)
Suction
Terminal
Pressure.
(paig)
Disdiargp
Terminal
Pressure
(paig)
Suction
Temp. CD
Disdiarge
Temp. C°F)
(Z) Suction
CandiUcDS
(Z)Dndurge
Conditions
1
fi£
162.74
300.6
38.09
29.73
84.64
219.65
73.0 °F
170.0 °F
1.0000
1.0000
1
CE
157.43
300.1
60.37
30.63
86.74
21631
73.0 "F
170.0 °F
1.0000
1.0000
2
HE
102.22
299.6
37.94
18.67
85.72
217.50
73.0 °F
168.0 °F
1.0000
1.0000
2
CE
230.13
300.8
84.00
43.06
84.64
219.65
73.0 °F
168.0 °F
1.0000
1.0000
3
HE
104.39
300.1
76.00
45.47
212.03
371.59
111.0 °F
169.0 °F
1.0000
1.0000
3
CE
92.78
2999
76.11
48 J1
213.10
370.52
lllO-F
169.0 °F
1.0000
1.0000
4
HE
110.18
300.0
77.57
51.69
217.62
373.07
lll.0°F
171.0 °F
1.0000
1.0000
4
CE
96.57
300.4
75.40
49.19
216.43
372.86
111.0 °F
171.0 "F
1.0000
1.0000
Pb(psia)«
147
R factor^
459.7
(Z)*d-
1.000
ToUl IHP *=
1056.45
@300.2
- Average RPM
Mechanical Efficiency »
0.95
Compressor BHP =
1112.05
Total BHP Load =
Compressor BHP
1U2.05
+
Accessory BHP
20.00
-
1132.05
*
Mfg, rated BHP =
1100.00
<§
300.0
RPM (Manufacture's rated ^wed)
Curve BHP =
1139
Derated BHP*
1100.68
@
300.2
RPM (average test operating q>eed)
Load Step =
6
Test Torque Load «
102.85%
^Difference®
2.37%
f Cyiinder Capacity (V'oiumf) |
Soction Conditions
Cyl. No.
immcfd
Cyl. No.
immcfd'
Cyl. No.
immcfd
Cyl. No.
insncfd
Total Capacity ~
13.954
immcfd
1 HE
3.4:!0
2 HE
2.250
3 HE
3.553
4 HE
3.715
ICE
3.5:!3
2 CE
4.810
3 CE
3.307
4CE
3.330
BHP/immcfd=
81.129
ToUl=
6.942
Toul=
7.060
Toul=
6.860
ToUl=
7.045
Dbduufe Conditions
Cyl. No.
immcfd
Cyl. No.
immcfd
Cyl. No.
immd'd
Cyl. No.
nrvncfd
Total Capaoty =
13.795
icvncfd
1 HE
3.4S3
2 HE
2.173
3 HE
3.288
4 HE
3.739
ICE
3.443
2 CE
4.936
3 CE
3.222
4 CE
3.296
BHP/nnmcfd=
82.063
Total-
6.935
Toul-
7.109
Total=
6.510
Toul=
7.036
Cylinder Flow Balance (Qs/Qd)
Cvl.No.
Cyl. No.
Qs/Qd
Cyl. No.
Qs/Qd
Cyl. No.
Qs/Qd
Total Capacity Q&/Qd=
1.012
i HE
0.979
2 HE
1.036
3 HE
1.081
4 HE
0.994
1 CE
1.023
2 CE
0.974
3 CE
1.026
4 CE
1.010
¦ HE Qs/Qd ~ CE Qs/Qd
4
$ 3
I
1
0.750 0.800 0 850 0.900 0.950 1.000 1.050 1.100 1.150 1.200 1.250
Discharge Leakage=ll=Suction Leakage
#-
F-41
-------
Compressor Cylinder
Performance Report
SUUcn.
LtoilNo.:
*2
Date:
6/20/94
Cooper Deucmcr GMV-10TF
Test Type:
Toxic Emotion Tesuig; Run #5; 98% Load; 5:00 pm.
CyL No.
HE/CE
MP
RPM
Suction
AEV(S)
Discharge
AEV(%)
Suctioc
Terminal
Pressure
(p«g)
Discharge
Terminal
Pressure
(P«g)
Suction
Temp. (°F)
Disdiarge
Teap.CF)
(Z)Suctioo
CoodftioQS
(Z) Dwcharge
Ccndkians
1
HE
17IJ3
299.9
63J9
34.00
85.72
206.79
77.0 °F
167.0 °F
1.0000
1.0000
1
CE
160.29
299.0
64.55
33.01
87.81
210.96
77.0 °F
167.0 °F
1.0000
1.0000
2
HE
114.22
299.4
43.06
24.00
85.72
203.57
77.0 °F
168.0 °F
1.0000
1.0000
2
CE
164.52
299.7
62.06
33.01
86.79
213.22
77.0 °F
168.0 °F
1.0000
1.0000
3
HE
104.18
299.6
76.00
49.92
212.26
368.78
110.0 °F
169.0 °F
1.0000
1.0000
3
CE
92.53
300.3
74.67
47.43
210.00
370.72
110.0°F
169.0 °F
1.0000
1.0000
4
HE
110.33
300.9
76.79
50.81
208.93
367.51
110.0 °F
171.0 °F
1.0000
1.0000
4
CE
96.24
300.2
75.40
49.19
212.26
369.85
110.0 °F
171.0 T
1.0000
1.0000
Pb(paa)-
14.7
R factor™
459.7
(Z)s»d=
1.000
ToUlIHP-
1013.64
@299.9
* Average RPM
Medianical Efficiency -
0.95
Compressor BHP «
1066.99
TaUl BHF Lose
l«
Connprenor BH7
1066.99
+
Accessory BHP
20.00
-
m&99*
L,
Mfg.ntedBHP
1100.00
@
300.0
RPM (Mamifadiire's rated ^>eed)
Curve BHP =:
1150
DeraLed BHP e
1099.50
@
299.9
RPM (average test operating speed)
Load Step =
7
Test Torque Load '
98.86H|
•/^Difference =
7.22 %
Cylinder Capacity (Votome)
Saction Conditions
Cyl. No.
tznmcfd
Cyl. No.
nncodd
Cyl. No.
imrodd
Cyl. No.
immcfd
Total Capacity = 13.609 nmndd
BHP/immcfd= 79.871
1 HE
ICE
3.735
3.764
2 HE
2 CE
2.532
3.591
3 HE
3 CE
3.557
3.211
4 HE
4CE
3.556
3.273
Toul=
7.500
Toto!=
6.123
Total=
6.767
TotaI=
6.829
Discharge CooditJom
CyJ No
onncfd
Cyl. No.
tmrocfd
Cyl. No.
immcfd
Cyl. No.
immcfd
Total Capacity = 13.675 immrfd
BHP/immcfd= 79.484
I HE
1 CE
3-784
3.629
2 HE
2 CE
2.624
3.667
3 HE
3 CE
3.577
3.170
4 HE
4 CE
3-633
3.268
Total=
7.413
Total=
6.291
Toul=
6.746
TotaI=
6.901
Cylinder Flow Balance (Qs/Qd)
Cyl. No.
Qs/Qd
Cyl. No.
Qs/Qd
Cyl. No.
Qs/Qd
Cyl. No.
Qs/Qd
Total Capacity Qs.Qd= 0.995
1 HE
ICE
0.987
2 HE
2 CE
0.965
3 HE
3 CE
0.994
4 HE
4 CE
0.979
1.037
0.979
1.013
1.001
¦ HE Qs/Qd ~ CE Qs/Qd
-
T—1
0.750 0.800 0.850 0.900 0.950 1.000 1.050 1.100 1.150 1.200 1.250
Discharge Leakage= 1 l=Suction Leakage
F-42
-------
Htm* of
jtr*nr
TVm
/i;*r
q: /n
'Z
/*:i> 3
/.?!(/J
w
8a0M numpwir
443
u/rj
•W
A 7
t>?p
Ea|ia< Sftti (rpcn)
861
8 6ft
S/0
VID
tf/d
Eapfte Twqw (*')
IfTLitkn 1Mn| (dcfreu)
«
,
FUEL MANIFOLD
FttcJ F»o» R»t« I'tefm) lAJLtnvtckA,
eLOf «
6
»V. */.$*!
H0&cf
4>-4l.<.4
A
to.i:
2#. O
Lr\.j
AIR INTAKE NUiNlFOLD
Air Ftov Kmc (i«ta)
Air MiatfoM Tcinpcntgn f°F)
2.6
Air MaatfoM Fnswrt (is H| orftif)
-7.0
~7.fi
•l.tb
-~4rt
-'4.0
-?iD
** -Ain
EXHAUST MANIFOLD
TuipeiMvR ("I") ziart prt 'ftZ
jeoo +
t»
/DDI) 4-
/cr,cf
/»•()
K-iK
£•5
£.2<
Compreaor Suetkn Freuure (psij) \j
^¦3
V6,n
7?. A
Comprfor Suction Temperature (°F)
95
M
/no
/0Z-
/P/
Compressor Discharge Pressure (psij)
<+>C)
4C.5
V/VS
V/fl
Cocopressor Discharfc Temperature (°F)
22#
IM
7 7/5
htff P/o W
(/Qszo
IMS'
MtUs
Fvd pAhj
20. i
»W firft—
A-'xss-"
vi.
Ttv^-a.
v
n
iS!
Ob - a
\/Lk»3^4A.
i- (%*j.,-»C
J ^iO pO^
1
-J .
r
! )
F-43
-------
CLP s.aaajaiqfe
,3wqM (*)
nMaa Ttakf (<«gwu)
,BL MANIFOLD
f i«i now Kite (acta)
* M Ttarnln ("J1)
. W Header Pianuc (p^t)
*f.,%
J Coapreoor Suctioo 1 rmvrc (pti{)
-•q.s
CoaprcMor Suctioe Temperihu* (°F)
"7
Caaprenor Disdurp Pramre (psig)
Coaprtaor Ditch*rfc Tcmpcnture (°F)
7
|
L+vUvi->£
-------
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CrJfi^C' I
iCesiiut-
Dk _
Nmi cf
TtM
*iif5T3
lO'.ZO
TtfF3
Jlibl
jXjsL
Baftx Spaed (IF")
ICTl
ib-frr*
Ea(iM Tot^ue (*)
r+
4*jujL
Ipltioa Ttauoi (4efna)
mjijI
FUEL MAN1P0LD
PMI Plow Rik («*¦) lAAi^VtvUV
<-f04£?
*1Ti^
hM.
T»-~
vatfci
1*
Mltepintvi (°F)
Y+
IWt Hwder IWun (pqfc)
A2_
?-3-
u
AIR INTAKE MANIFOLD
Air Flow Ran (acta)
Air MaoifoM Itanpeiaturt (°F)
Air Mulfold hemic (la H| or pti|)
EXHAUST M>lNTFOLD
THMpcntart ifT)
Pramt (b Hi)
Se*vea|er Air frtanift (pn^)
CYLINDER TI-MPERATURES
Cylinder # 1
Cylinder # 2
B Cylinder # 3
Cylioder # A
Cylinder # 5
Cylinder # 6
Cylioder # 7
Cylioder # 8
Cylioder# 9
Cylinder # 10
Cylioder# 11
Cylioder # 12
Cocapreawr Cij*aty (MMidb)
i
Cocnprcsor Sueboo Pressure (ptif)
3i<
3^
Coopreoor Sue boo Tcapentwrt (°F)
1
Comprtsor D»:harfe Pttsure (pdf)
J-lbO
<>OVtO
MO
Cocopreoor D»:harfe Temperature (°P)
u&tA -2Sfr4
k Li-lt
I* - ,
-KaJL
Nlrv^av-?" -W-a
sz.o
j
HVOW
fVNAjKV-c^X, \V>> ¦
4
F-45
-------
fjMj (Stttysln
"9T£<7
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i
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Begtoe-Torqvt f*>)
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tvO
l|nilkM Timing (degree*)
M.
-5S&&
5Mf
WuiF
FUEL MANIFOLD
Fuel Flo* Rite (irfm) UA^tclVtCkA.
Fuel "ftfWtMW (°F)
FutlUfder Framit (fjj)
3
JSC
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m
m
JUL
II.
3Z3
m.
3Tl:
¦m INTAKE MAN1POLD
Air Flor Rju (aefn)
Hr <17L*
U 71 *>' ^
mi
Air MuifoM Tcmpcrihirt (°F)
Trvt
Air MtnifeM Pranirc (in H| or ptif)
10.
10.-L-
4Zk
25.
¦gxftWffMANITOLP
TeapcrBturr (°P)
4u -r
Q»Hl)
Scavenger Air Prasvrt (pug)
S
UNDER TEMPERATURES
Cyliitdtr 4 1
ma.
£l
(^Cylinder# 2
£
aiQ.
SQrti.
iikdcr # 3
Cylinder # 4
^Cylinder # 3
.Hi
_sai
_s^3-
(^Cylinder *\ \
dtt »
^Lt.
-SS£-
&1-
~^o
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C°!ls
Cytimfcr * 11
• finder# 12
¦ 7//C.3
: Tipimor Capacity (MMscf^
rmprt**or Suctioo Frcsurv (pcig)
Coaprcssor Suctioo Tcmpefifi* (°F)
Z4(t>A
&>(e0
Cooprwof Discharge Pmwit (pug)
24L0
~5o£o
Coapttaof D»rh«ty Temperature (°F)
ttZZSaZZ
WT
2^
fiS^A
sz.v
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rp*A.
7TT"
F-46
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V
iMOTa
sStftrt
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126
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tta
/zk
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FUEL MANIFOLD
FmI nOW Rjk («cfm) 6C*MtfS/itt,
?7(.&J
Z7Z.U'•
Z7I.SZ
&9.6C,
ZCfi.ZJ
Z6&.&
M Ttapuunu* (°P)
PMI Header htawrt (pd|)
tU.l
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Kb. <6
IL.Z
/£..!
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AIR INTAKE MANIFOLD
Air no* R*u (Kfa)
Air MaaifoW Tcapcntura (°F)
127
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/37
/3!
f4Z
/44
Am
Air MulfoU FioniR (fcSfa-w p«ii}
2.L4
Z-b +
2-£9
2.38,
«?.*/
7.<7
2.*?
EXHAUCT MANIFOLD
TtapiiNn (°F)
I
Pimiua fa Hj)
Sca«u(cr Air Ihcnra (p*i|j
CYLINDER TEMPERATURES
Cylinder# 1
^
*7/
P62
**,2-
573
272
Cylinder 4 2
¦Pi 2.
qzt>
c
*
X
Cylinder # 4 r/r
X"
*
*"
X
y*
X
X
Cylinder 4 5
427
<736,
92 *>
<
XS9
Cylinder # U
Cceprweor Svctioe Teapenturt (°F)
17
/act
/C2.
144-
/pi
III
nz
Comprtvor Diiefcargc Fimuw (p«ii)
2lS
2d7£
easd
20*4
24£d
v?m
ZdxUt
Compresor Diiefcujc Temperature (°F)
2ZZ
zzz
22S
ZZ1
2Z
234
2AZ
/ttz Hensc f u£>
IZ43.S
IZ&L.J
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1373-4
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77.75
79.61
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C'C. " '' rT"- — F-47
-------
E\-I\E OPERATING DATA Enpnt Model. Sumtier X'iZS -
D..e gy-^-yy
Same of Data Recorder Z
CS3iO
OS-
C S iTf
a / s~~
C
It. ff—
L'gtnc Speed 'rpm)
32 7
IX 7
33^
no
SZ°r
32 1
r
j'ipne Torque ('"e) j % 5*'
7.5"
y.
. . ~
/- .V 5
fc.9
6 -9
.V
EXHAUST MANIFOLD
Temperature (°F)
Preuure (in Hg)
x jvtnger Air Pressure (psig)
i VLINDER TEMPERATURES
Cvlmder # I
*33
fr-a/
3-.?/
#3/
;--"r
CvUnder # 2
s' ^6
g-4*
«> 72
*71
T77
?7V
^ /V
Cvlmder # 3
sT-
1 3-?^
&
-Under #5
-?*!T
7 to
7 3>"
732_
7 3-5"
7x3
• under #6 ~ 77<»- 'i** ?&'
L-2L
^/7
tnl"2
-ZS'2
?r /
-.Under 0 9
5-32
^i"d.
Cvlmder # !C
? /
'7 s7/U
! 7,!//(., 7
t6
'HY/tri*
C ompressor Suction Pressure (psig)
4^3 c
lis"
0/520
*i (*/0
' >mpressor Suction Temperature (°F)
VJfrerz?
iT
¦TV
W/ 37
1(e'/ °IO
' . mpressor Discharge Pressure (jwig)
3.1" O
Z >OQp
5 / oo
^ /CO
^C5? ^
Lompressor Discharge Temperature (°F)
Zcsfin
2o(c/n^
lolc/iil
P-xket Unloader Setting
/
/
t
T urb /I <
7^,8
7 c, 7
70S
7 70
77/
¦770
7TC.
A f*.
7? /
70(*
7*1
7S%-
7 J'3
7 U exrm>
~7f,L.C3
7(*f, li-
7UU 2 3
7Luy>r
E i i
/ /' -,1.1.0 7
2 • ce
9 : ri isj
F-48
-------
4_ugiuc »ivuc.. swmoer u -J CJ
£>»•«
Name of Dau Recorder /. '/ (*
Time
/2 ¦ ' iT
/J: 20
t X. olSL
ty.co
Engine Horsepower
n-> V
nc>i
IL>/2-
Engine Speed frpm)
2> ¦J. i~
213
3 J 3
32 Y
¦333
333
Engine Torque (rr)
96,
<*;T
Ignition Timing \degrees)
)\°
//"
u °~
n"
H0
FL'EL MANIFOLD
Fuel Row Rat* (scfm)
Z/£. <*-/
ZlsCs-^Ho
26G-S?
Z4?M
Z4? 23
Z4-£3
5?^r?C»
itb.'He
9r*.n
FR TEMPERATURES
Cylinder # I
S-TO
V2A
*2.-)
%2*r
ro -r-
VZC,
Cvlinder # 2
oo?
<*<;<*
*>rt>
9 7.7
5>-7^
X7
TX. 1
*10,
Cvlinder # 10
-)X7
XfX.
¦' *Zp. >
/s.r/n.t
Compressor Suction Pressure (psig)
n/Aoo
27r
i0?5-
/
Compressor Discharge Temperature (°F")
x< 3/431
in/iic
Zxi/zs-i
m/is-t
Pocket L'nloader Setting
'd
r>
' 10
')
< I
-
/ . il :J7
I .xr /i
r-XLic*
r.itofi
«¦/ X ICO
¦7*., 7 9 ST
ILfilo
~?ls ffX/
lb 82.7
•7L.S-3V
7<*t-ni
j iC it C
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1U> Z10
nuvii
76,rA7
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7(*SJ~2-
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7L.O
76,3
7k /
7(j>0
7(o 2
T7, R
-7 7Z
7 70
7 jTS
747
7«Z
F-49
-------
F\GIV '.RATING DATA Enpnt Model/\umb«r
Name of Data Recorder Z. 1 f
Time
N» oS"-
/uzo
!(# i L>
//,vr
mo
/7vr
Engine -r power
nds-
Ml?
/V-2 V
Engsn* -i.--d(fpm)
X°i
& l.ho
6 /ji>«L
\JR INTAKE MANIFOLD
Air Flow Rate
S?n
Cvlinder # 2
k-o3
7
JT9V
6c/
Cvlinder # 4
Jl>i
Slo
-s'Srv
ST/
£3~3
Cvlmder # 5
JTTO
r 7c
i"Lr 7
Cvlinder # 6
//f. j.
Compressor Suction Pressure (psig)
2s-n
3*(odhsLo
lie'/*'0
Compressor Suction Temperature (°F)
ci7///22P
1
ZLt/zel
7
Pxket L'nloader Setting
/ C
1
/
/
'/
2
S-cJT-
j-ojr
iro3~
Pti <4-/^r^n " f-
/*_?X
Id it
Ltif
(n 17
(n/$
II
F-50
-------
Due: P V)
Name of Data Recorder _
Time
¦"& - /A
Engine Horsepower
/SrSZ
mo
Engine Speed (rpm)
J124
32.9
i
Engine Torque
w«'
Ignition Timing (degrees)
85
SB
FL'EL MANIFOLD
Fuel Flow Rjie (scfm)
Fuel Temperature (°F)
Fuel Header Pressure (j»ig)
AIR INTAKE >MANIFOLD
Air Flow Rate (acfm)
Air Manifold Temperature (°F)
Air Manifold Pressure (in Hg or psig)
Temperature (°F)
Pressure (in Hg)
Scavenpr Air Pressure (peig)
,
CYLINDER TEMPERATU RES -
Cylinder # 1
Cylinder # 2
Cylinder # 3
Cvlioder # *
j Cylinder # 5
Cylinder # 6
Cylinder # 7
Cylinder # 8
Cylinder # 9
Cylinder # 10
Cylinder # 11
Cylinder # 12
Compressor Capacity (MMscfh)
*7. S/Ss.i
Compressor Suction Pressure (psig)
Compressor Suction Temperature (°F)
&
Compressor Discharge Pressure (psigj
2/0#
2t&Z
Compressor Discharge Temperature (°F)
Zl7
r
rri/zt tfr£. £tvs
&£)3.4
6£3Z-*>
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6*43.4-
er
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&.97
7S-.<*Z-
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&.4-I
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Aruh/Lu-f T
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7S.7?
F-51
\
-------
ts\ u< >v u> •
Instruction Supplement
SPECIAL D*TA
Ompi.
I\J/ , | ' O- ' \
PhM« i
Thi following data differs from that given in the standard KVS Instruction Manual and is
veid only kx the PCC equipped KVS units listed on the tronl of this form:
I. KVS Engine Specifications
Power Valve Timing1
Wet Valve Opens - - 50.1* BTDC
Met Valve Ctoeea 168.0* ATDC
Exhaust Valve Open# . 163.4* ATDC
Exhaust VWve Closes B.I* ATDC
Fuel Valve Timing;*
Fuel Injection Valve Opens S2.5* ATDC
Inaction Begirt* 64.8* ATDC
Infection End* 138.7* ATDC
Fuel Injection Valve Ctoees 139 0* ATDC
I. MunMJ Temperatures and Preeaures
Power Cylinder Exhaust Temperature; (Ful Load A Speed)
Operating (PCC) 700 750*F (371-399*C)
Maximum (PCC) 850*F (454*C)
Fuel Gas ManHold (Fti* Load & Speed)
PCC Unit! 18.0 20.0 PSIG (I24-13B kPa)*
Air Inlet Manifold (Ftil Load & Speed)
PCC Unit* 9 6 PSIG (66.5 kPa) @ 0-1500 It (4572 m) altitude
Turbocharger Exhaust Gas Outlet Temperature;
(Full Load & Speed) PCC Units 600-700'F (316-371* C)
II. Fuel Geo Systom
PCC Regulated Supply'. ... 3 PSIG (20.7 kPa) above air manifold pressure
IV. Lubrication System
Lubricating Oil Pressures,
Napier 35-50 PSIG (241-346 kPa)
V. Other Engine Data
Maximum Operating Speed 33D RPM
Spark Plugs;
Gap Setting (PCC plugs) 0.013-0.016 inch (0.33-0.41 mm)
Tightening Torque (PCC plugs) . . . 60-80 fi bs. (68-81 Nm) tor dry threads
40-80 It.In. (54-68 N m) for lubricated threads
Ignition Timing; (Initial Setting). 12* BTDC
V). Engine mxS Rurawig Gear Bolting (Bolt Torques)
Preoombustion Chamber Stud Nuts 150 in. lbs. (17 N m)4
' Aa measured at the pushrod end of fie rocker arm. with a 0.20 inch (6.08mm) pushrod Ml.
* Baaed on 0.10 inch (2.64 mm) pushrod lift. Injection points differ Irom opening an
closing points due to design of the fuel gas valve.
' This value may change with major changes in fuel composition.
4 After prestressing by tightening to 200 in. lbs (23 N m) in stages.
PG7457PS TXT.Olik PQ Funis rt
08-~.0-1594 11:41AM 7147765020 p.01
F-52
-------
iovimi»
Equipment Specialists
4i"- 3900 STlmma Tyter, Tocas 7S701-M51
(903)581-2884
ANALYSIS SUMMARY
Cenp«V
LotP
Ma.
IgnUonTypa „
Arabian! Tamp
L7o<^XC-l* At ^n-,-1
&H(9->\6 . fH --
Found
T HP M'lDO Oi ML
1*
,*<¦
71-12
11-2 2
0,-13
V*
21 13
|(
'
SJ-ZX
?(
2-X
?> • '
X>-)3
pvO
3v»>
kam
Fnnl
M
EnglmRPM
TwMmRPU
KSNHmhp
ManloUPraa*
kUnloUTwnp
FlMlPlWi
OlPrws
OJT«tvIMOUT
Oi Filar OP
Walar Press
WH«T«npHWr
Crankcasa Press
ExhBacfc Press
AJr F®«r Pr Drop L/R
Igniion Primary
Soi'i 11
w-asW-
7.5" U C-
/0O
bO "
iUHln-
ia>/n\
rfd vohi
Tcul HP
OH
No
Bore
Rod
Dia
HP
VotumatrieEH
KVEs %VEd
Toa Press
S D
Gas Tamp
6 D
Gauga S
G*U9# D
Pocfcots
Sta9«
CcmmanU
1 HE
CE
15-
-------
( OlHPMC N t
SPECIALISTS
LOCATION Ar y,AJ
DEFICIENCIES NOTED
ANALYSIS FIELD REPORT
UNIT NO.
RECOMMENDED ACTION
DATE
g/6 ?/•?«/
MODEL L7m2.GrU< fu^ti
ACTION TAKEN
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u
M
u
2
W
—<
J
c
V
%
y
?
c
s.
_ V
4
NJ
«
C.
V
V
V
>
<
<:
t»
V
o
*
*}
1-
*
•x
s
«
s
1
«r
V
\
*
*
¦>
•s
\
c
C~
s*.
>
h
c
V
. -1
<
\
>
o
5
9
£
V
\
1
<
I-
F-5
5
«f»
r
*
*
i
>
fc
&
-------
TEST SUMMARY
Company:
Location
Date:
Atmos press:
Test Num:
Amb. Temp (DEG. F):
Clock Time (24hr.):
tgn. Timing:
AVG. RPM:
Turbo RPM:
Fuel Press (PSIG):
Fuel Temp (DEG F):
Manifold Press/Vac:
Man. Temp(DEG F):
Oil Press .(PSIG):
Oil Temp.(F in/out)
Water Press. (PSIG):
Water Temp.(F in/out)
Load Step:
IHP 1 HE
IHP 1CE
IHP2HE
IHP2CE
IMH HI It
tljgSSE
IHP4HE
IHP4CE
IHP 5HE
IHP5CE
IHP 6HE
IHP 6CE
I it •J.
Sh\!n
ti- 7
Unit ID:
Ignition Type:
Rating® RPM:
ENGINE DATA
7
10
M
IZ.
/I
11
IS
J'.sf ff*
l.Sffa
S'iOi ft"
11-i 3«Vt
21-U rtet.
31 -2Uv>i
1IJI sfci
ai-J3«T-
%12.
em
1:75 'HO
Vhc-
f Hi.
e "hc-
« 'HCr
f'ne
r "kg-
10 1
I o O 1 ere
i )
or*
1
1
I'jo /p1
•
\
1
COMPRESSOR DATA
{ L* » t)cJ
Lv*JtJ 1 U>t±JcJ
Lb d
i?< ! /7<" I7U
177 1 nti
1 77
1 77 !
i lif ! I4l» ¦
1*1 : /*7
i£f6>
/S 7
i !
1
o
o
/3
S..H |
6 'S I
i
1
i
1
i
I
1
1
i
!
1
1
j
1
I
Total IHP:
BHP:
% Rated Load:
£7Y
S7J ^
C51 i«1
' ^3
,<^3
o^7
Sft'A 1 ?*'/-
nv-
*?'/•
Comments:
r-'L Fr,:./ >*>L-
F-56
-------
Company:
Location
Date:
Atmos press:
TEST SUMMARY
UnltJQ: .
Ignition Type:
RattngQRPM:
ENGINE DATA
. MkjIUsIT
filT,B-o. L ill
in, e /ooo
Test Num:
Amb. Temp (DEG. F):
Clock Time (24hr.):
Ign. Timing
AVG. RPM:
Turbo RPM:
Fuel Press (PSIG):
Fuel Temp (DEG F):
Manifold Press/Vac:
Man. Temp(DEG F):
Oil Press.(PSIG):
Oil Temp.(F' in/out)
Water Press. (PSIG):
Water Temp.(F in/out)
Load Step:
IHP 1HE
IHP1CE
IHP 2HE
IHP 2CE
r* rw V c f c
IHP 4HE
IHP 4CE
IHP 5HE
IHP5CE
IHP 6HE
IHP6CE
o
1
H
«r
7
//: 11 a.
iZ:12a>
/.of >/*
i\s-°
?-.pr
ai-3l 'trot.
31-.? 3&i»t
21 2J*W
Tiiy'tvt
Al-US'fC
9oo
JsOl
S IO
ei«>
«i*>
91°
S/o
*
f.C-
LD*
£0 f
to 1 /•» o
Lb
win?
1
1
oo-ssr-'v3J
s COMPRESSOR DATA
* Irfl uoL !
Coe-dft)
J
La*JrJ
L..XJ
Z.
ni
1 7 ^
nv
111
1 ?«•
>77 177
1 7 U
/>!_ .
/fc °l
Ifctf
\<6o /'I
} i(&
/ZD
u*
1 IT
//M
HH
I11
I u 7
s. 7
r.H
i
iC
1
1
t
1
1
Total IHP:
BHP:
% Rated Load:
Comments:
3S"<-
6.1V
GOV
£ 0 ?
£,52. 1
c 7'
O V»
11'A
*?<;•/.
£)5V«
««'/•
9^*/»
-------
TEST SUMMARY
Company:
Location
Data:
Atmos press:
UnttID:
Ignition Type:
Rating@RPM:
L 70 m
ft fV"'» Of
n
-------
IOUi'kimi
Company:
Location
Data:
Atmos press:
incuimt
TEST SUMMARY
UnH ID:
Ignition Type:
Rating@RPM:
ENGINE DATA
JLL.
C.t &("V£L
lATO 4Mf>e 3*3
Test Num:
Amb. Temp (DEG. F):
Clock Time (24hr.):
Ign. Timing:
AVG. RPM:
Turbo RPM:
Fuel Press (PSIG):
Fuel Temp (DEG F):
Manifold Press/Vac:
Man. Temp(C)EG F):
Oil Press.(P£>IG):
Oil Temp.(F In/out)
Water Press. (PSIG):
Water Temp.(F in/out)
/
rnt*L
a 96.
W
ISlllGo
i 1 1
COMPRESSOR DATA
Load Step:
IHP 1HE
IHP 1CE
IHP 2HE
IHP 2CE
IHP 3HE
IHP 3CE
IHP4HE
IHP4CE
A«icfC /
ir
r**nfc 1-*
IHP 6HE
IHP 6CE
UulU
I
11C
i
ii ly
i
i
i i i
"^oCf
i
i
/2.5
i
II
H
i
i
//.A
1
/*./r
Total IHP:
BHP:
% Rated Load:
no /
1
HSl
i
£>7'/'
1
|
Comments:
ft .If
F-59
-------
TEST SUMMARY
Company:
Location
Date:
Atmos press:
Test Num:
Amb. Temp (OEG. F):
Clock Time (24hr.):
Ign. Timing:
AVG. RPM:
Turbo RPM.
\ Pyel Press (PSIG):
fuet Temp (DEG F):
Manifold PressWac:
Man. Temp(,DEG F):
Oil Press.(PSIG):'^;„
Oil Temp.(F in/out)
Water Press. (PSIG):
Water Temp.(F in/out)
Load Step:
IHP 1HE
IHP 1CE
IHP 2HE
IHP 2CE
IHP 3HE
IHP 3CE
IHP4HE
IHP 4CE
IHP 5HE
IHP 5CE
JHPfRE /"
IIin^oc r,s 1--'
it
'ZSIHL
Unlt ID:
Unit Type
Ignition Type:
Rating@RPM:
f »Jpr / / G-^UC SO
filWMt CPU V
/ if DO * 30
ENGINE DATA
0
1
3
H
-J1-
ID'.li «/v
S-f. Met
S-L'tiec
S-u'tmi
<-£ 'euL
2^-in
3oj)-3P2-
111- 3m-
w&i
}«>«>/
10*
M
SnoJ
30
3.1.C
7is
q.t'
/of
1.f
?.c
)•<
1 OCr
IOH
/»!
101
10)
17/3 1
I?/J*
i A n.(
It'll*
/ idsi
Hi j !U\
SA~4
J, r- *VJ
4T/»« : _$#«¦* 1
5 COMPRESSOR DATA
/HI
All CI*JK
5»r-J
.S^rtd 1 4 «*.r
1
2.3"
-J>'
1
1
IX. \ /li
/It \ 131 t*l2 1
\
1 !
i
333
23V
2J' 1 ?3e ¦ 332.
I3P ! Ill
' <<(, 1 /'ci; \ 113 'WW
' 1
-
S3U
2SC
2*7
2Sf?
\ 131 '
/9i*
ie>C
J 0 2_
>1C
/13 1 /7P
1
231
*5"/
250
ti3!
2vi
2 Of
2 I4}
2C7
i eS
2.11
/*.l
/k. O
IS- 7
IS.3
>s.» , /r. 5-
f*s~
/O. ©
H.I.
/r.
) /r.£
Total IHP:
1 IL7V
/£?/ 1 /6i7 l/fr,* /6*7 1 !
BHP:
l7(rCr
/ 75-1? 1/7/.? j /-' ' /~)2i 1
% Rated Load.
?fV-
-------
TEST SUMMARY
Company;
Location
Data:
Abnos press:
Test Num:
Amb. Temp (DEG. F):
Clock Time (24hr.):
Ign. Timing:
AVG. RPM:
Turbo RPM:
Fuel Press (PSIG):
Fuel Temp (DEG F):
Manifold Press/Vac:
Man. Temp(DEG F):
Oil Press.(PSIG):^-
Oil Temp.(F in/out)
Water Press. (PSIG):
Load Step;
IHP1HE
IHP 1CE
IHP 2HE
IHP 2CE
IHP 3HE
IHP 3CE
IHP4HE
IHP4CE
IHP 5HE
, vUni ID: - •„
UnlType
Ignition Type:
Rabng@RPM:
rum; C*ve >°
itoec J»*
ENGINE DATA
wntiit i«'
JFA
1
2ft
2 fl
•=»
H
r"
c~
9
a
/p'.eefi*
n\t* ft
ir-s* a
/i ^
/:»r
r.isr*
XMP*
c'a'pi
f a*>t
S
i-ai'L
S" Alot
S
Tiwi
S'a t*.
I
Hi J»i
z*Vi°\
1 °ti -Si*
2 91-3*0
'211-J*»
199-3"
3)
3l
3/
2 I
J)
3 /
"
30
/D.l *
/p.X
10.1.
/P.f
/e.3
/o. J
to
IO
1 o
leo
/»3
/»?
/ e(.
s«
/ c>9
/II
III
17/31
!U/3t>
K. i°
/4> /i *
- r/^9
/6/J9
ir)iy
)L/21
K./21
MillSC
tis/nS
iiuhM
/Vl/lL*
'I'tl/Ul
miiL3
/s-i/tii
/SI III.-:
' ISUjUI
I /S5//H-
: /sS" //(.O
/Si/irc>
/•;* n*) :/fy//6
COMPRESSOR DATA
'ah tint*
JC'-i
¦232.
231
i 3i
11° \ I 2.2.7 1 -J (, 1 22y
/V?
JHI 1 ,*2- /HI ! ! ,jf 137
! ' ' 1
21<
1*CP
i Ys-r*-»f
1
HD.7
J».C« i^c.3
/r.v 1/^.2-
/ i
H-7
Comments:
Total IHP.
1 /7oJ
vA
I7r7
i l<*K
/C7f
/(. if
/ U >1
ISIrS
BHP:
! /?93
Ai*
'717
1 /7W
/7C-2.
ni?
Ibt51
l It 10
/U*}
% Rated Load:
i vc
*>*
/« '/•
i 91'/-
Ik'A
97 y.
}, *j t (¦'
f "f:i> |;H AC T/'-.'-f / .
—t.'J -r j IfZrf. C*--£
¦- ^ — r• - c.
F-61
-------
TEST SUMMARY
Company:
Location
Data:
Atmos press:
Test Nurn:
Amb. Temp (DEG. F):
Clock Time (24hr.):
Ign. Timing:
AVG. RPM:
Turbo RPM:
Fuel Press (PSIG):
Fuel Temp (DEG F):
Manifold Press/Vac:
Man. Temp(DEG F):
Oil Press.(PSIG):
Oil Temp.(F in/out)
Water Press (PSIG):
Water Temp.(F in/out)
mm
\ltU
n
1/^.7 1
Unit ID:
UnH Type
Rating@RPM:
w
rAeMmt, C-+IX / D
Ahr-
•"*'< CPtl 2T
/j-PO f J»J
ENGINE DATA
/o
ll
/z.
/*>
(H
Z'.!°
t:>f
v:v
S '61 »C
S"RV>C
e; ntoc
i'aifit
C AlOC
<¦ Mr*
IW-IP!
PI 1-Vl
ZK-J O!
JtlS"!
I
I
1S.<
z*.r
^sr.r
;v
77. r
°l .M
1
*
9
2.X
lL!}c> l/C/3-
K/jv
l(r/S/
/L/*I
IC.I2"
/¦VS//SL.
I
I
' S3J /D
/Si //Is*
!
COMPRESSOR DATA
Load Step:
IHP 1HE
IHP 1CE
IHP 2HE
IHP2CE
IHP3HE
IHP 3CE
IHP4HE
IHP4CE
IHP 5CE
All CI.-m I J*"t-
I i'
IHP-eCE
.Llk.
'/?«-/ I 3
iis' ! 5J3 iir
iii : i
/w />? : /a<5 • /s7
/37 ' ,J7 '
JOI 1
i'2.
5 °? 1 ; ^ i '
/Sfi? ! /W
)W '/7<-
/7 : /92.
/f/ t /fr-fr'
i
i
/
:
!
/7,2-
IU.V
/C--F
/<^y
/C*,2-
/u
/5.r
/J.V
/*.* 1/3.2-
a, *
n,?
i
Total IHP:
BHP:
% Rated Load:
/r«>s'A l ?*"?'•
1
Comments:
-
F-62
-------
TEST SUMMARY
Company:
Location
Data:
Atmos press:
TaslNum:
Amb. Tamp (DEG. F):
Clock Time (2!4hr.):
Ign. Timing:
AVG. RPM:
Turbo RPM:
Fuel Press (PSIG):
Fuel Temp (DEG F):
Manifold Press/Vac:
Man. Temp(DEG F):
Oil Press.(PSIG):
Oil Temp.(F iiVout)
Water Press. (PSIG):
Waler Temp.(F in/out)
UnK ID:
K-iWytXW *•»¦>
Ignition Type:
Rating@RPM:
ST*
ENGINE DATA
J"/?
H
i*
7
T
/!¦.«*-
li:/??*
/\Ot> fit-,
A ,ioPr*\
f vj/1
3'.mC
u. Vf >'
f&w-
t'aiei
t a f>t
t'&ici.
«'6ro<
<¦
/'A ro<
32-l-SiX
V7-133
H7-J31
137-V3
1.X7JJJ
13oV*
ilt-HH
IV 3J4
He. H
ie
/*.v
6.h"
i*
1 11>
/ 1 o
no
/ M
ill
//V
13. tsS
-!3h<
'Z/Cf
Tl/SS I 7i/sr
7*/SS
niiif
7>-/sJ
1'iillsH
/li fl/i V
mi'/tfi
'ithSH
ft/n* 1 v»//rv
/Utjlk°l
/i«7/fre
/ .si[no; /^ln»
,TfJl7» : IS*) Ii7o\i s
COMPRESSOR DATA
Load Step:
K /t»< /{«•
J
u'/r*fb.
1
] 3
IMB0B&- /f
/r.2.
iJ r
-ft t.1 '7 r t j'oj'J
-pl L
(Jt V/
r. Uli e-t T-'-i ftf-f nek'
F-63
-------
IMCUIIIII
Company:
Location
Data:
Almos press:
) it "
7W
li 1
TEST SUMMARY
UnKID:
• *»rv>Wrt»TVP>>|i' ¦»»»
Ignition Type:
Rating@RPM:
ENGINE DATA
t0
1
|
IHP 4CE
till
1 4 H
I
i
IHP 5HE
IHP 5CE
IHPOWC /»'
IJW
li- 1
1
•
lll(*«g£ '
ts
1 U.lf
1
i
Total IHP:
BHP:
% Rated Load:
rs.it
I 5 l(
I (
ti "i
I01S
i '
lj.1t
*l")t
' I
Comments
F-64
-------
Company;
Location
Dale:
Almos press
Test Num:
Amb. Temp (DEG. F):
Clock Time (24hr.):
Ign. Timing:
AVG. RPM:
Turbo RPM:
Fuel Press (PSIG):
\ Fuel Temp (DEG F).
» Manifold Press/Vtoe:
Man. Temp(lDEG F):
Oil Press^PSIG):
Oil 1 emp.(F in/out)
Water Press. (PSIG):
Water Temp.(F in/out)
Load Step:
IHP 1HE
IHP 1CE
IHP 2HE
IHP 2CE
IHP 3HE
IHP 3CE
IHP4HE
IHP 4CE
II If* SHE I * r r*r>\ t (
innccc^-,y
tUPWICg Auof PS/
IHP 6CE
TEST SUMMARY
mil ID: _
foil Type ' "
Ignition Type:
Rating@RPM.
JA IWS V/A .
At.rA.t«i c cm H
2tob e. 4f0 AM
ENGINE DATA
0
I
A
.1
V
f. J*«»\
IJ.HS ft
\ i»
3:lS
/J Otdc
U'6H>C
li '6rOO
U 'iitc
n' aij>l
ni-m
7J 1.JJ/
U
J.I .
O.H
5.S
1 \ O
/ vV
/ v 7
I uS
/VS"
lo /sS
1o /&i>
te/sS
Id /<-S
se/sr
tie/iS 1
i se lll> o
He (It i
1 i'/ne
I^vIJlo
'
1 5 f / lift
toilns
ihi/ns
lCZ)l7c\
COMPRESSOR DATA
1 IP 13V
I 7
L( 0
34
li 1
i*i,7
If
(?
/•»/
17,1
¦JV/HVaue
lliftufjm
udtSo/^9,
1
Total IHP:
BHP. 4 IS
% Rated Load:
ts^o
/UiS
IkSi
|i
IbZT 1
l
noq
(lit
lit 0
111/.\
i
<70 ?d!
*1%
tin.
f7'/- I
!
Comments:
F-65
-------
iia-cip
TEST SUMMARY
Company:
A»6IA IS
Unit ID:
1
Location
. UflilJype
/* /(!»! v; i
Date:
tgn*pon»Type
/) 1 rrc* it- C C/»(J
Atmos press:
1 W "5
Rating@RPM:
3* »*c & i 1 «
ENGINE DATA
Test Num:
i.
3
i V
i7
Oil Press.(PSIG):
u/ss
J»/S5 I 3=/«r
3o/*.T
-Ko/sT
.WfT
.V/3-5
JO/SJ
Oil Temp.fF in/oul)
tuzhiio
1 w T 11 o 0
nl^/ ill.
I'yo/lt.i
' 5-3/76 3
/k. 2.
¦;vS//*y
/fijiol
Water Press (PSIG):
¦ ;
Water Temp (F in/out)
lil/no
'¦it," in2-
/ W'7~
.'i» // 7 i-
It'in*.
ic «//;z-
COMPRESSOR DATA
Load Step:
« £ i
5
)?*-<
5
<
IHP 1HE
76
¦> •
<- ;
"4
L. V
: -
u M
IHP 1CE
X 6 t
3 j-5
2
j: v '
'
3-3
^6 £>
2
; 5°
/
/f/t
IHP4HE
.7* 1
J!i
2 7«
1-7 2.
2 72
9 7D
2 7/
^ 7Ji
IHP4CE
US
/ S M
/uv
i o
/T/ :
/ 5" O
1 9°
!£<>
iti
I
IHP'SIIC :s'
U < i
I l> b i
ns
/7.Y !
/ 7> H .
17,2.
i 7
?4 ?
IL-H
M ^
/I V !
h.3
/1.» I
/*,*!
1 T. 1
i*.?
iM
/i. 1
1
:
IIICVOWC^a*»-
1^/9* />**> vio/»Tj»u>
IHP 6CE
1
i
Total IHP:
1 1 , =i
1 7 f 5
/c. 7?
10*7 !
/(,0
I'+i)
/ (<•%)
11,11
IKX
BHP:
\ r u *¦/
li'Jti i
/7qt.
1 s n
wn
i » e v
1 7 q '/
mo
% Rated Load:
Vc
5o 7-
9 /*/.
°i ''/j
Joy.
qpy.
^ 6 7c
?r/-
Comments
"T* l z •
wJ j C -f * 3 y*,f.
F-66
-------
Company;
Location
Dale:
Atmos press:
TestNum:
Amb. Temp (DEG. F):
Clock Time (24hr.):
Ign. Timing:
AVG. RPM:
Turtxj RPM:
Fuel Press (PSI6):
Fuel Temp (DEG F):
Manifold Press/tteerr'*
Man. Temp{DEJ3 F):
Oil Press.(PSIG):
Oil Temp.(F in/ciut)
Water Press. (F'SIG):
Water Temp.(F in/out)
Load Step:
IHP 1HE
IHP 1CE
IHP 2HE
IHP 2CE
IHP 3HE
IHP 3CE
IHP4HE
IHP4CE
tHMHE /j r <•«/£.
IHP 6HE
/^°//72- !U ill',;
TEST SUMMARY
Unit ID:
Igi
Rating@RPM:
t/L K VS.
al-ho* itr ff <;** u
3*0 o a f. 1 ito
ENGINE DATA
ID
II
i
1
3!4*Pf- , $"./<>
i/'qToc\ 11: Mel
W-13J
iJI-JJI
It 1
•
1
•j-.U
t
/¦/ ' T-6
1
1 1
1
/5-1 i ri 1
:
.272- 1
1 :
/SO : /r/
I !
j
1
1 i -
1
/*,iy
1
i ;
I
•<"ltr.il. r.
1 1
!
Total IHP:
BHP:
°/0 Rated Load:
/7sQ
7-7
'SiZ-
9 / '/• q a X.
Comments:
F-67
-------
lom»wf ar
TEST SUMMARY
Company;
Location
Dale:
Atmos press:
/? « rV I £
V • 3 O • 1 W
Unit ID:
Unit Type
Ignition Type:
Rating® RPM:
ENGINE DATA
M KVi 'j/?* <»/¦ t
f' 6 re c.
f '4fDc.
K'/lrp^
i '&rcc.
J '< f/5C
i' uroo
fir*"-
ynHl
Ui-33/
Z3l(o/3*7
Zti/lio
3ji hil
3-0
fiO
iH.S
3«
1 t* + :.*
, : / ** /
i + M.
;. i
/. .1. .. >
1 ?i..
IHP 1HE
>3
' T I
- >
T
* 5
1 1
;v
IHP 1CE
2 7 7
< i 7
JS?
t /a
3VS
1 i r
IHP 2HE
Uh
I ; 7
11
5 V
5
5"I
S V
5 1
l I /
IHP2CE
11 0
\bi
! ?: 0
^53
3"T
3ii
' ¦> u
,
IHP3HE
, J*S
¦^u
: Ps ;
¦ its
Jt »
• ZT7
. it!
IHP 3CE
I i " f i
1 u~,
' /J
/ 3
! I X
; 1 Z-
/ JL
; J 3 7
! / i ?
IHP 4HE
2 i H
Z " ''
^ 3 r J ^ ^
2 t *
2-B3
?'S
37?
! 3-:^
IHP4CE
: u ^
/ i -L
/ i
!'j +
1 S "
i |£J
i.i 1
¦ih^she'!- i
17 "J
IT
! ' -1 • n 1
¦ n 1
lU-H
tb 1
fv 7
1 I: 3
IHftSCEJ-.J
it.*
J 0 1
'¦ n 1 : It 7
1 /* .5
/S.O .
11, 3
16.9
1 : 1 '1
IHP 6HE
! i ! ¦ j t
P»u
'\ltki-"' :
Total IHP: . ( 7 i 1/
(7 15
I JQ i
IS 77
; 'f ? j
/Sx /
i<, S i
IOIO
1 4 c 1
BHP: 1 IJ(t
I T"C
n iv
ti< *7c
9S ft
1 ?S5:
1 CI ¦/¦
IJ-fe
l»f 1 € 315
ti ?.«J'-s,
' J Rfr'J / t'ct,* J l°° ^
Comments:
5? v'
q?7o
«
-------
MM-C\P
TEST SUMMARY
Company:
Location
Date:
Atmos press.
Unit ID:
Unit Type
Ignition Type:
Rating@RPM:
ENGINE DATA
"2"
1R KUSHI*-
Alis+J ,t CPU It-
Ale.
330
TrfTelJe f*
Test Num:
10
II
li.
/J
N
Amb. Temp (DEG. F):
Clock Time (24hr.):
/ r*50 a f*\
U'lbtn
1 J. la #~">
/
l.'Atf*
Ign. Timing:
AVG. RPM:
9 'A reo
< 4 TOC
1 l'«r»^
if «rot
II c. ro*-
riy- ii-*
~J?/7i*
?w /J
TurtX) RPM:
Fuel Press (PSIG):
3 0
Jo
17
11
( f
Fuel Temp (DE:G F):
Manifold PressA/ac:
7 V
b-0
It P
Man. Temp(DE:G F):
1 1 0
/O D
IJO
i i o
1X0
Oil Press.(PSIG):
i \ /-.J.
^/?i
54/7^
5J/]1
SiflJ-
Oil Temp.(F ia'oat)
I:: J 1 ¦'< f'
/VJf'llW
; u < lis
1
( M i / /5M
1
//JSV
1
Water Press. (PSIG):
: i 1
Water Temp.(Fr in/out)
^ *. 1 _
!L±-h >2-
wS-lm
/(.a.'
\u3-im
COMPRESSOR DATA
Load Step:
f • (U ,
< f. ~w
5*
1
IHP 1HE
" -
' 1
- 1
IHP 1CE
5 f J
3 '¦J
1SJ
IHP 2HE
?7
v- *•
M /
5 0
IHP 2CE
33«
US
3.S «
.
IHP 3HE
3-?7
: t
IHP 3CE
/r
/ W 1
i 3-,
li-
i
IHP4HE
1
i ^
3-xi
I
IHP4CE
' b i.
1 J 1
i it
16 1
( 1/ 1
i i
i i
4HP-SHE'1 ' i
i 5 ^
/ss
IS «
m i>
'US
: i 1
IMf-SCEj-1
It-U
1 f.J
I!--
IU-M
lu¦ M
1 1
1 ! i 1
IHP6HE
1 ; !
-IHMG£tA"c' f'"
f*/ /i' ^Su'Ik :o htTsfi '7'* .7>.-i < !tt Vim'j i* j
t
Total IHP:
& b ftf.i
— !/ "y
r 7
V7
Comments:
F-69
-------
Company:
Location
Date:
Atmos press:
Ifl-CIP
SMOAtlS'1
S ¦ 3 6 - 9 W
/v- 7
TEST SUMMARY
Unit ID:
Unit Type
Ignition Type:
Rating@RPM:
ENGINE DATA
r/-g » ¦ i ff c. P O
/pop 0l0OAfir\
Tist Num:
Amb. Temp (DEG. F):
Clock Time (24hr.):
Ign. Timing:
AVG. RPM:
Turbo RPM:
Fuel Press (PSIG):
Fuel Temp (DEG F):
Manifold Press/Vac:
Man. Temp(DEG F):
Oil Press.(PSIG):
Oil Temp.(F in/out)
1
3.
3
<*
U:oOft\
r j »/•>
S l.i XfU
(¦/.'Aim
t-i'sroc. I St.h'tOl
Jiviei
aaa • s * i
1
10
~LA 1
1
10
t.i.
T ft 1 "7
11 n
101
<1?
1
16/J 1
lUISl
i tin
/T/^a.
1 I 1
N 7 /|(S 1 | WW/Jf
lulfis t , »*7//si?
i
Water Temp.(F irVout)
f 5 5 /' i»'
!< '
COMPRESSOR DATA
Load Step:
Al L £ lc*'r<
i
' 4 '-W
^11 LptJrA '
IHP 1HE
J 1 (
::o
- J /
22. C
IH- :.:E
lu i
i i J
i '. I.
/lb
l^' .- •.=
2. 3.i
2jc i
IHP ,'CE
1 U
1 W
/<¦ 3
/*
-------
iNOiaulig Oi. Kd^xuv-auit^
Equipment Specialists
3900S.Tlmmi Tyler, Texas 75701-M51
(903)581-2884
ANALYSIS SUMMARY
Ccnpav
B^IW ^|0D
Oydt bL
.33 o
lint ( ,
WW
IgnMonlVp* _
AmbbrtTwnp
L>$ V/A
/J/Wfx- X
°r*
Found
Tamp MP
Rnal
Praourt (gnlion
Tamp HP PMk IDC Ml MM
Mm
Fouid
FM
BffcwRPM
Twfalna RPM
IGNTMng
Manlokf Praaa
MWoMTmp
Fual Praaa
OiPiwa
OJTampKOUT
oin«u>
Wtfar Pn*a
W*arTan*>*iWr
CmnkcaMPracs
ErfiDaekPract
Air Fk«r Pr Drop UR
IgnUon Primary
U7-3J2.
i
Svv
/c<
vo/
3to
f
f-J'Oiet
?e>
K>
¦jvr
7.X'
$10
/C)
WL
2.1.1-
S
no
9i7
/3 2-
t
2d*
PI
«7
3JH
A-
tn
J*!
|T
/6G»
fo~?
sr
1
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/V7
>*3>
orj
«-?
/72-
Wi
<2^7
fe
/i
ssy
/72
w£
3<-l
i
a
SrfT
/5*>
TclalHP
c*
No
Bon
Rod
Dta
HP
Votumatrie Bl
*VE« %VEd
To* Prat*
8 D
Gas Tarrp
8 D
Gau(*S
Sauga D
PedtM
Slag*
Cenmarti
1 HE
CE
lo ¦ r
JS
3"
—
—
^uy.v
317.7
"»7
-2ir
J
1
N
3<-J
90.7
5-0
wy. 1
M7J
/lo*
2 HE
CE
/».<¦
—
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wn
jTv-r
212.
1
~ ^ hfJ'J
1
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si*
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903,/
/ 7
SHE
CE
$.71H
y^S"
io27,y
I"*/'
-yj
tittr
2e>1C.1
/ r
4HE
CE
¦S", 7 f-'
-i<5i
£6»
3°.7
1
SHE
CE
6 HE
CE
7 HE
CE
SHE
CE
Total IHP .
Comp BHP . Comp IHP { 'Lti ) * fill
Conv. Fador ( i ^ ^ )
P-"T
Tola! BHP Load - Comp BHP ( Hit ) . Accessory BHP ( 7 <" ) . /£DC. BHP
c J
/-) MochBI . loial BHP Load ( )¦
* Load - Total BHP Load ( /VPfc )
Rated BHP 2.B"0
1
0 /
F-71
W Cy< IHP ( )
/ •. cu^ ^
-------
I OUIPMI » I SXCIIUI1I
ANALYSIS FIELD REPORT
LOCATION
DATE
UNIT NO.
MODEL 3~/2 idO? Hi*—
~C. X<¦«. f.0^
**./0 Ci> /
£l*A-> + ' T -~rltsr* c/
/f^K pfis-r f^e SaA/Z />!»<]
J. _£(>*. T ytX/^fO *
Tri pyf. fo*La<-r. 0 -» C« /'
/j /(/ rj* & /?>*a.AC
T'-I -7>>& /(>*>/*£ -T^A
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7| -
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/Pj0^S-r -7^* p/e/e~l
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/ ^ / 0 / • , ,/
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£tl) c.l'—e t Ofiltrt. ~t-u y fy^Ji
/
/»//omiJ j S
(^D .T^jf/ie<-r r'oc.i&s sis* s**sr~(A.
tr+ <"«>£& cJuv/e AcTi »J '
^ 6^/1/ «"• /1 fee' f~s
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P/oflgs Ojujs/i T»->—' ^ O^yo I T/W ^
T
¦yjT^te '• V.?/*.
' f> fi
f S • W .f \- I v_>
n*t : 7
/
ANALYST^
RECEIVED BY
-------
UNIT NO. %
DEFICIENCIES NOTED RECOMMENDED ACTION ACTTON TAKEN
\
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1
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DEFICIENCIES NOTED
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<
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4
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1
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<-"y
f
f7Z-
7
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2-^3
kam
Found
FM
EncMRPM
TtibinaRPM
IGNTMv
ManMdPnaa
ManlotiTamp
FualPraaa
OlPnaa
OJT«r*>KOUT
OmarOfP
TwWm nW
W<«T«tp»»UI
Cnrteaxa Plan
EidiBaekPraa
Air FtarPr Drop L/R
Ignllon Primary
A24-J3
/X'STpt-
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/r*-
3®/«-
/Vo/zT/
"BrtvJn
Total
HP
/S3
;
<*
No
Hora
M
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Vokxrmric Bf
*V& % VEd
Too Pro**
6 D
G*s Tamp
S D
GtufS
SaugaD
Podtau
Stag*
CpmMcti
IKE
CE
!'•<
fT
30
—
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2IO
1
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J7-5
3ot7,f
/$"!*
4HE
CE
s.71v
t/.U
ft •5"
S7I.7
2*71
Zir
7C. 1
fSS.)
?»^7
SHE
CE
SHE
CE
7 HE
CE
SHE
CE
Tatal IHP
/
Corp BHP * Comp IHP ( , C > ^ ) *
Coov. F*cSor ( » ^ s" )
Toial BHP load • CompBHP ( ) ~ AeoetsoryBHP ( ) . l7°j BHP
% Load ¦ Tool BHP Load ( /r)*C! ) " , M»ch Ell . Total BHP Load ( )"
Rated BMP | £) 0 i g J,? 7& Po~w Cy< IHP ( )
F-75
-------
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DEFICIENCIES NOTED RECOMMENDED ACTION ACTION TAKEN
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-------
"BSSiii
xvuwiuig 6c i^eciprocatmg
Equipment Specialists
3900 S.Tlmm» Tyto, Teutt 75701-8451
(903)581-2884
ANALYSIS SUMMARY
1/khL
toi vS" <•«»
Oiilt
lgnUonT>p* .
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MM" VC 'O
AC rrQ**i£ H CPU
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t«r» hp m idc t* nwt
ft
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-------
fOUIPMfMt SOCIALISTS
LOCATION ^
DEFICIENCIES NOTED
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ANALYSIS FIELD REPORT
UNIT NO. V
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MODEL /Sy-gx d-At UC. / d
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F.4 Campaign 5
WA 33 Site 2/GRI Campaign #5
Engine No.
Manufacturer (/if
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Rated Power UP - Ic, ,3 to pATft?
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Nat Gas Sample Collected?
Velocity Run Performed?
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Fuel Flow Rate
Engine HP
NO
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F.5 Campaign 6
ENGINE OPERATING DATA
Engine Model/Number MRa
Date: "/V/f V
Name of D>u Recorder
Time
>n>r>r>
/est o
llto
))o£~
//A©
II3J-
Engine Honepot/er
VH.3 . 2.
?*/&,. i"
vsr.r
Engine Speed (rpm)
AW
Engine Torque (%)
1A .S~
9-2
93. 9
92.9
Ignition Tuning (degrees)
11 ° Stoo
Fuel Flow (f**w) ^ P ,+ 0,0
/„/. 3
C? 1 • 6>
(p3 O
1*2- 3
U3. -3
kH.I
&%¦%
Fuel Temperature (°F)
sr-s
8 V
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3 9
Air Manifold Pressure (m Hg or(j!sIgJ)
i.is~
1.11
/. ??
/.f 9
1.91
EXHAUST MANIFOLD
Temperature (°]F)
Pressure (tn Hg'
Scavenger Air Pressure (psig)
CYLINDER TEMPERATURES
Cylinder # 1
(*2 K
ls2C,
6*9
tr x V
bZLe
(c2e,
to 3*/
Cviinder # 2
6> -3 £~~
L*U"
(c V z
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u>H(£
Cylinder # 3
(t c5~~
Go 7
XOr'C
bd
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Cviinder # 4
U A V
Cc Z 7
Le 3 c
6? £>2-
to HO
Cylinder # 5
¦£-? 7
&9
2^ CI
7o
Compressor Discharge Pressure (psig)
-?L-0
Gfr"
Lc Z
F-87
-------
ENGINE OPERATING DATA
V ..
Engine Model/Number &BA .3 /'I&'IO
Date: *U1I€I* ' .
1 Kccdnler. _
Name
ne of I
£R
Data l
X
¦A—
Time
ULlO
ax-T
iZsTO
A
113s-
Engine Horsepower
KS-T.9
-
V3S~, 1
v -1 y .
711.'7
Engine Speed (rpm)
3Q4
2>co
3co
300
2. I
2>oo
2ol
Engine Torque (%)
93. ?
If
11
AO
"
/f
AIR INTAKE MANIFOLD
Air Flow Rate (acfm)
•^Jr Manifold Temperature (°F)
/2?
!2S~
IS 1
!2 *
Ajr-ManifoW Pressure (in Hg or psig)
Lfrt
3.S4
EXHAUST MANIFOLD
Tempcra^ire (^F"V-
4,o —
Pressure (i^fig)
Scavengf/Air Assure (psig)
CYLINDER TEMPERATURES
Cylinder # I
t*zo
Lo !Lo
Cylinder # 2
(*H1
(el? S
(olL*
Cviinder # 3
(ooH
(eojr
(j>oO
X-7? W-
j£~71
Cvlmder # 4
LpSn
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kofr
Cylinder # 5
£1* 7\
.T63
CylinderV.6 f
Cylinder # yf
Cylinder # 8 \ f
Cylinder # 9
Cylinder # 10 /
Cylinder # ,rf
Cylinder'# 12 \
Compressor Capacity (MMscfh)
/
3 o.H
J1.2L
Compressor Suction Pressure (psigi
HZ !
H to
HtO
Compressor Suction Temperature (°F)
(e "7
u u>
6r
<*3
& tf~
Compressor Discharge Pressure (psigi
tp Hi
6>«!
HSL
/ */O
HH
/SLe
Pocket Unloader Setting
F-88
-------
ENGINE 0PERA11NG DATA
Engine Model/Number tt- ttO
D.lc: '
i Reorder.
Name of Data I
H Time
ts~i r
)jfio
iu>o5^
1
1
H Engine Horsepower
¦72 r. t
7?^ =,
| Engine Speed (rprn)
2o o
1
ZOO
2V
Fuel Header Pressure (psig)
/
EXHAUST MANI FOLD
Temperature (WF>
Pressure (in Hg)
Scavenger Air Pressure (psig)
CYLINDER TEMF'ERATURES
Cylinder # 1
JTfO
-TST7
Cvlinder # 2
Cylinder # 3
^7 r
S~? 4
Cylindety 6 /
Cylinder /
Cylinder # 8\, /
Cylinder # 9
Cylinder # 10 \
Cylinder \
Cyhndfff^#12 ^
Compressor Capacity (M.Mscfh)
ll.tcl
Compressor Suction Pressure (psig)
H If
*tn
HI7
HZ.D
Compressor Suction Temperature (°F)
U.Q>
<* t
Compressor Discharge Pressure (psig)
<*tS~o
CpSs~~
1$ 4~G
Compressor Discharge Temperature (°F)
IJ 5—
1 3 V
/3 5-
11 \
Pocket Unloader Setting
-
a>=
-.80 —=
-------
ENGINE OPERATING DATA
Engine Model/Number
L
Name of Dau Recoi
itot/OH
iroer
Time
iyo
¦71%
7 V.
73
Ignition Tuning (degrees)
It*
X
FUEL MANIFOLD
Fuel Flow Rate € i ^
Hl.S"
47.H
H 4
His
<4*. 1
47.JT
*/7,r
Fuel Temperature (°F)
<2jT
us"
#
H <7 3,
HXX
H
H *rr
H
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Cylinder # 3
4 7
i, 7
U> 7
Lei
L 7
Compressor Discharge Pressure (psig^
ieiTo
(cS*
to TO
Ce^£>
-------
ZNGIVE OPERATING DATA Enpne Model/Number
Dale: /< / r/
taod)
/ot5~
lozo
Engine Honepowcr
oo
loo
xx\a
Engine Torque (%)
J 00%,
<*;*/
1 Ignition Tuning (degrees)
il~
1 FUEL MANIFOLD
Fuel Fkw Rile (letrttf „ (4, O
<^9. SL
toKi'X
63 j
Fuel Temperature (°F)
22.
*0
?r
7'?
do
Fuel Header Pressure (psig)
A O
RC
HO
JLO
XUlFIow Rate Ucfm) _
Air Manifold Temperature (°F)
/.?2
l2SL
/
i32
13>U
J3S-
A" Manifold Hg or psig)
EXHAUST MANIFOLD
Temp^tujrt°F)
Press«fe7frkHg)
' Scavenger Air Pressure (psig)
J5 b H
3,±y
3.33
3.H 7
l.t/fT
3.Hf
CYLINDER TEMPERATURES
1 Cylinder # 1
9*-
L> 17
t%20
(*2 3
(e (4
L>2 1
Cylinder #2 f
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U> .y0
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foi ^L(S>
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Cylinder #4 \
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0>H7
(rH 7
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Cylinder #5 —
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fn
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& /
Cylinder # f
Cyl\tder ^7
Cylin^f i/# 8
Cylind^# 9
Cvhi^er \ 10
Cy/nder #\l ]
Cylinder # ^
Compressor Capaci:y (MMscfh)
3<£>. \ 7
3&. tie
3o.Cp
10.(0V
Compressor Suctior. Pressure (psig)
H1 U
Hn
Hn
*tJL2>
H3LT~
Compressor Suctior Temperature (°F)
&<=!
te~7
uc*
0 i
U(*
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-------
ENGINE OPERATING DATA Enpne Model/Number 3$ •*» /M !Q
Date: /' / XT
U2 0
uht
i Mo
"> 1
Engine Horsepower
.
1/Z
s.. '
Engine Speed (rpm)
3.94
IOC
Xns-l
».v --
Engine Torque (%)
'11.?
/a?C>
/&&.¥
&-• -
Ignition Timing (degrees)
FUEL MANIFOLD
Fuel Flow Rjte^ttSa*- £ |4t?
LS.o
65,-T
7 e>,o
70. 3,
w "* "
Fuel Temperature (°F)
tri
SI
Vtf
s'3
Fuel Header Pressure (psig)
A/
SLO
1*1
SLO
SLO
AIR INTAKE MANIFOLD
Air Manifold Temperature (°F)
iSt
Ho
/ HO
iHo
M\
H2>
*ir Mimfntfl Pininn (in Tig nr pjig)
EXHAUST MANIFOLD
Piewm (.» Hg)
Scavenger Air Pressure (psig)
3.3?
¦3^
LSI
Cylinder # 3
(& oL c*L
U2 /
SL 7
Cylinder # 4
l,*n
C?JG>
&^7
Cylinder # 5
f ip
v«?y
S?
6 ~7
0? 7
Compressor Discharge Pressure (psig)
"?z ~
73&
-72>D
73 o
73 3
73S-
Compressor Discharge Temperature (°F)
tso
/W?
/H9
/Sv
/St>
Pocket Unloader Setting
F-92
-------
ENGINE OPEPATING DATA
Engine Model/Number t4
Date: /1/Of/fV '
Name of Data Recorder
Time
\ih-t
)HCO
/HIT
/H2.0
H^ST
,o (
3O0
303
Engine Torque (%)
92
S2.1
Ignition Tunini; (degrees)
FUEL MANIFOLD
Fuel Flow Rate OrfiflT/J P K, C
SS'X
-&H
¦5~y, 3
rv.T
¦fi't
| Fuel Tempeniiure (°F)
QO
94e>
1
mo
Air Manifold Pressure (in Hg or psig)
EXHAUST M>^NIFOLD
Temperature (°F)
Pressure (in Fig)
Scavenger Air Pressure (ptig)
^.Vi"
2 .i-S"
d-39
a.s'z
2
CYLINDER TEMPERATURES
Cylinder # 1
Cylinder # 2
ft* 7
jr?09
SZ>S^
jT6>3
~T<*0
Cylinder # 3
-5"3 5~~
jS'Ho
irfZ-
Cylinder # 4
S~l 5T
S~t fC
TlX
jnz
Cylinder # 7
Cylinder # S
Cylinder # 9
Cylinder #10
Cylinder # 11
Cylinder # 12
Compressor Cifunty (MM&cfh)
50.01
2 9 <
A Z-ff
Compressor Suction Pressure (psig)
132.
H 2o
Hi?
US'
*12$'
Compressor Suction Temperature (°F)
U %
<<= 7
Let*
l* "7
o> &
to *
(p(*
Compressor Discharge Pressure (psig)
? H C
7 If 3
7
F.Cn =
I
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-------
ENGINE OPERATING DATA Engine Model/Number H3A-S~ lti(2
Due: uj.r/w '
Nine of Dm Recortcr
Tune
i f 3 O
/jYj"
!(eOO
iu/r
/7<2e?l
Engine Horsepower
*31
^s73
Engine Speed (rpm)
3c 1
3of
3e>/
2.CZ.
3o,
2o{
Engine Torque (%)
«-3
'9
J'S-f
S-SZ
CYLINDER TEMPERATURES
Cylinder # 1
flpO
T-T7
iZeO
Cylinder # 2
S35~
JTHo
S-37
^r-39
£~2 7
^jr
Cylinder # 3
j-/o
sol.
s~n
i~c
ToC,
Cylinder # 4
SVS-
iT4^r
-0 5T
S~-¥2-
-5~36
Cylinder 4 5
44TI
^ 5-T
HL>\
H<* 6
*/JT7
Cylinder # 6
Cylinder # 7
Cylinder # 8
Cylinder # 9
Cylinder # 10
Cylinder # 11
Cylinder # 12
Compressor Capacity (MMscfh)
25.(0 7
Z9.to
Compressor Suction Pressure (psig)
43=?
HZ?
7
L, <1 *
b 9
u> G>
(e (0
LeC*
Compressor Discharge Pressure (psig)
7 37
73
7^
7V3
?vr
7V7
7 S'O
Compressor Discharge Temperature (°F)
h4
H 2
13 7 *
/3 7
Nb> *
IH K
/V?
•*- r*
9-ct
—7.
F-94
-------
ENGINE OPERATING DATA Engine Model/Number
D..e: a far My '
Narrr of Data Recorder/ a.
Time
in/f
\710
\1H<
/
Engine Horsepower
STV*
----- ;
Engine Speed (rpm)
ZoSL
3oi
20*.
20&
- ^
Engine Torque (%)
*1. 7
¦; / -
Ignition Timing (degrees)
.
FUEL MANIFCLD
Fuel Flow Rate UaWfT A P .«
Sr.-7
jf£T
I3Z.
A3-3
vAir Manifold Pressure (in Hg or psig)
EXHAUST MANIFOLD
Temperature (^F)
Pressure (in HgX.
Scavenger Air Pntssure (psig)
2
«?,6> H
I
CYLINDER TEMPERATURES
Cylinder # 1
^3
-T7?
ftO
Cylinder # 2
sri %
fSLO
fHD
ft!
JTH9
(
Cylinder # 5
VSf
VS'f
Hit
is (a
uf
u &
Compressor Discharge Pressure (psig)
7fO
7 V7
7 V7
7H 7
Compressor Discharge Temperature (°F)
HI
)Al
/vsr
/v *-
Pocket Unloader Setting
-
' /
-------
Process Data Collection Form for Gas Turbine Testing
HP &/H.2e>o
Turbine Model/Number:
Date: H/j/H
Name of Data Recorder:
yd
&
Time
\7l5~
\~7ZO
i 7Hs~
iZOO
!V/S~
Turbine Horsepower
% Power Turbine Speed
*i(o < Le
lQ&zr
SI'Cp
£%. VL
s~^ ^
r5~-£~-~?
Compressor Suction Pressure (psig)
Hbz-q
Hb3. 7
HbiT
Compressor Suction Temperature (°F)
7S~.%
7<*. 7
7 7
7G>
7-7
Compressor Discharge Pressure (psig)
^ Y3.
Co V-5-
Compressor Discharge Temperature (°F)
U1.2
12c?. 3
/zo
\3C
Ho
iuf. Disc e ( 1 V
;qeo
/Ho /
/39
}*/oo
D'itiar^c. fr
H7
JI7
iir
hf
nti
tH. 0 (HeA ^ J'ecA
I
SLS.'Z
7 1 T—
sdg/gn
camp-o.tsi
flue. ^5°^ I?
' J
TieSoX^
irn-lT
n.7
?7-3
SXp
nr
3 7.U
.^rrc
Hc,r~
7-7
i^OC>
/too
?>%
F-96
-------
Process Data Collection Form for Gas Turbine Testing
Turbine Model/Number: TXo^Z.
Date:
Name of Data Recorder:
8
BOOSSBSSSBBSSS
Time
0 &
q&.tr
Load (%)
Average Power Turbine Speed (rpm)
xb.q
S(o. Z.
S'ST °j
FUEL MANIFOLD
Fuel Flow Rate (scfm)
Fuel Temperature (°F)
bo"
io 5L
(n 1
jC9
Fuel Pressure (upstream of meter) (psig)
Itt
1 €o
Ho
IfiO
/ro
Fuel Header Pressure (psig)
Fuel Differential Pressure (psig)
H/. f
HI, 5-
HI.6"
Fuel Meter Orifice Diameter (inches)
Fuel Meter Run Diameter (inches)
AIR INTAKE MANIFOLD
Air Flow Rate (acfm)
Air Manifold Temperature (°F)
Air Manifold Pressure (in Hg)
EXHAUST MANIFOLD
Temperature (°F)
Pressure (in Hg)
Compressor Capacity p
JT-y.O
>-?. /
JTV. (
J~Zj, $
^~7. 1
Compressor Suction Pressure (psig)
H Vo.z-
H7£i.c!
Hto, 2.
Compressor Suction Temperature (°F)
-?tr~
75~- V
?jT. 7
"7S. 7
Compressor Discharge Pressure (psig)
io(j> *4
Ce (e> S < 2~
(p (pZ- ^
l*Q>Z'9
Compressor Discharge Temperature (°F)
I2.fr--2>
J a 8--^
M?. f
°F
/too
1399
Hoo
1 Hoc
Hoo
'c-«e prrj £?sif)
//T
n*
n *
ni
Hi
I T J
sdg/gn
F-97
-------
Process Data Collection Form for Gas Turbine Testing
Turbine Model/Number: T(eJfeZ.
Date: ft/ap
Name of Data Recorder:
Time
iOAO
tOH
nco
tuf
ii %o
Turbine Horsepower
% Power Turbine Speed
%.i
U.f
Load (9c)
Average Power Turbine Speed (rpm)
7
&S~, (fi
zs, ?
257
FUEL MANIFOLD
Fuel Flow Rate (scfm)
Fuel Temperature (°F)
1
In 3
(s-3
ip I
in (O
Fuel Pressure (upstream of meter) (psig)
iff I
n
Compressor Suction Pressure (psig)
HI#.*}
mv.cs
Compressor Suction Temperature (0F)
7£~. ?
7(?, 2
7C..Z
Compressor Discharge Pressure (psig)
Le>0>2. • /
fe>(pl t z.
b>L>£), 7
IfileOi 7
Compressor Discharge Temperature (°F)
IX V.0
U7- ¥
!* 7- ?
12%* 1
/US'.3
c«,t JlixcL 7^., (rs-) "F
Hex?
A3??
)yoo
/ZTI
J /
CsV^p. DlJf k Pr <*_S (3
/ tie • b
iI(j>
no?
ilb<5
ill
A > ^
(P/3 l V ¦ *< tt
sdg/gn
camp-6tsi
F-98
-------
Process Data Collection Form for Gas Turbine Testing
Turbine "Model/Number: TUbQ 2.
Date: /'/V
Name of Data Recorder:
C4~
Time
iW'T
iP-dS
»5L/T
/?3o
Turbine Horsepower
% Power Turbine Speed
16?+
?o.d
Load (%)
Average Power Turbine Speed (rpm)
sSir
TS.3L
W-4?
0
FUEL NL"iNTFOLD
Fuel Flow Rate (scfm)
Fuel Temperature (°F)
(p (
S, (a
Compressor Suction Pressure (psig)
qyi.z
uyo>5~
VK /
Compressor Suction Temperature (°F)
¦?<£.. 2
76.?
10.V
1-6.9
77,3
Compressor Discharge Pressure (psig)
0?C>l. %
r.rt.3
Cstfr-o
Off. 9
Compressor Discharge Temperature (°F)
J2% 2-
o
i^r-o
13?. f
tar.*
Hoo
/'{CO
iQo-o
i^6V
/ijo 1
r* '
6k t j l)isch Pre^<, Cj2s/<;)
nU
,iT
iA
,tr
A ' ^
sdg/gn
camp-6.ist
F-99
-------
Process Data Collection Form for Gas Turbine Testing
Turbine Model/Number: / CScZX
Date: III
Name of Data Recorder: U>C&
Time
/ "boO
!
/53o
/3
Load (%)
Average Power Turbine Speed (rpm)
9S-.Z.
?G-3
?5". O
FUEL MANIFOLD
Fuel Flow Rate (scfm)
Fuel Temperature (°F)
o5~
us
L>1
L,0
Fuel Pressure (upstream of meter) (psig)
(XO
1 S*o
ifro
Fuel Header Pressure (psig)
Fuel Differential Pressure (psig)^.P^.(470
m.i*
3*7,5"
a.q.
3>q- (
Fuel Meter Orifice Diameter (inches)
Fuel Meter Run Diameter (inches)
AIR INTAKE MANIFOLD
Air Flow Rate (acfm)
Air Manifold Temperature (°F)
Air Manifold Pressure (in Hg)
EXHAUST MANIFOLD
Temperature (°F)
Pressure (in Hg)
Compressor Capacity (MMfipfh)-^*^ f/ji)
5S.2
Compressor Suction Pressure (psig)
Lt7?.9-
r
Compressor Suction Temperature (°F)
n.o?
?7-0
77-5
Compressor Discharge Pressure (psig)
OS9.S-
6 9.-C*
5-9-
655- 7
Compressor Discharge Temperature (*F)
izr.r
isf-i
/as-. 3
id's-- 2
£*¦ (Ts) °F~
/t/oO
t
-------
Process Data Collection Form for Gas Turbine Testing
Turbine Model/Number: T~ (0 /2—
Date: !
Turbine Horsepower
% Power Turbine Speed
<12. 6>
92.
Load(%)
Awf'ragu f'ower Turbine Speed
%O.0>
Yd.?
SO, 7
x&.ie
FUEL Mj\NIFOLD
Fuel Flow Rate (scfm)
Fuel Temperature (°F)
b 1
S"7
sr7
bo
Fuel Pressure (upstream of meter) (psig)
ItO
/ ?o
tro
/ xo
t ISO
Fuel Header Pressure (psig)
Fuel Differential Pressure (psig)
f
xiT, 7
2la t (D
Fuel Meter Orifice Diameter (inches)
Fuel Meter Run Diameter (inches)
AIR INTAKE MANIFOLD
Air Flow Rate (acfm)
Air Manifold Temperature (°F)
Air Manifold Pressure (in Hg)
EXHAUST MANIFOLD
Temperature (°F)
Pressure (in Hg)
Compressor Capacity (MMoefh)^^
Ais'.ar
H^.Lp
V9, S'
£*>, f
Compressor Suction Pressure (psig)
Hi 2 ¦ %
H 73, V
H72 ¦ t
Compressor Suction Temperature (°F)
ys'.x'
itr.c,
vy.jt
7 ST, t
~7YO
Compressor Discharge Pressure (psig)
632. 7
oir-9
/*2aU>
1*2.*, i
bz?
/ 20 °I
)Zosr~
pi^ck frets. SSi c_
/cs
/©£>
sdg/gn
camp-6.tst
F-101
-------
Process Data Collection Form for Gas Turbine Testing
Turbine Model/Number: T L>$~0Z-
Date: n/ */f/
Name of Data Recorder: lc>c£
Time
i#lS
i«ZO
/'£"/!>
ic,0d?
SStS
Turbine Horsepower
% Power Turbine Speed
SZ. (
s-i.r
SI > *7
SI.iT
ShZL
Compressor Suction Pressure (psig)
HI!.*)
men
HH
Compressor Suction Temperature (°F)
11. If
11. 7
77-U
77. u
71.S-
Compressor Discharge Pressure (psig)
M 7
3L
(0Z.I' 3
Compressor Discharge Temperature (°F)
a* 3.7
IZ2.&
A23.
I23.~7
~] S 1 C "F)
/3oS"
J3cl
I20O
1X1°!
/
f) /tr /pa)
/Otp.S
iO-7
ioi
to7
/ v -
sdg/gn
cump-6.tsi
F-102
-------
ENGINE OPERATING DATA
3OO ZP*
to So
3t
/«? £4- r i-tU.
Engine Model/NumJ
Date:
Number
><7)0 n
Hc-lo/*
Name of Data Recorder
sZ
:JS~
!cJjZ'
noo
ji
L.
/* \C
I zc
HH
noo
Enpne Horsepower
I *22,
1*2-3.
/ru-i
Enpne Speed (rpn)
2 ao
3d> I
3.oO
3a> (
^ 9
-?f?
Jo a
Enpne Torque (5)
JOLJkL
/s> f, 2.
J£hj_
Ignition Timmg (degrees)
Ltur^r-
UP^
FUEL MANIFOLD
Fuel Flow Rate (scfj
in
±£3ZL2.
j£2M&
iS'qir.o
/.T93 *.o
JSV27.0
/r?.3rc
Fuel Temperature (°F)
67
fry
6 *
A±
IP
7 O
ILL
Fuel Header Prcuure (psig)
JejL
(p */
JejL.
JeJL
AIR INTAKE MANIFOLD
Air Flow Race (acfm)
i i yjicT,
7H2
II1//C2
Air Manifold Temperature (°F)
/>¦ //».3
'fl
uzlit>2-
n s/zoz
Air Manifold Pressure (in Hg or psig)
Pressure (in Hg)
Scavenger Air Preuure (pstgf i*. M>. 0
*12.c
Z12 .C
210, O
Z$Y,o
CYLINDER TEMPERATURES
Cylinder# 1 I L
(*Z2.
UZ1
I
S~7 3
S'lO
r?7
3 C
MjO_2_
L C2_
(*ol
5r
Cylinder # 5
s-<-
(p -S"Q
ifS¦/
6' fO
L±2.
.(zjry
U>2b
Cylinder # 6
JJL.
(t>Zo
(oil
&ZO
&Z2
Cylinder # 7
(e 2>T
0 2(e
<*>L>
t, ff
Htr
3, f
-7UH
7 (el
77 /
7(*7
??/
77^
Cviir.der # 9
i'?
-k-2-JL
(p %o
JcJLL
0>%lI
b^Le
u>z Ct>
L?2. (s
kJLL
I?}*-
lerV 12
Compressor Capacity (MMscfh)
^3, ?>
97.7
Compressor Suction Pressure (psig)
-a'o y
SOI
s/O
Compressor Suction Temperature (°F)
o V
J^L
(o v
CompreMor Ditch.irge Pressure (psig)
717.0
IHl.O
7.V7.0
1HZ.0
7V^
7H7.0
y^tLco
Compressor Disch.irge Temperature (°F)
/zz.
2*£-
/3L2>
Pocket Lntoader Setting
F-103
\
-------
ENGINE OPERATING DATA Engine Model/Number /*/4~
Date /!//<>/
/JV3-
Engine Horsepower
itir. 2>
\tXe>,\
Iti,*'*
1ZI7.X
Engine Speed (rpm)
loo
3c 1
JSC/
3.0 (
J.S-7
Engine Torque (%)
IO 1
liPl
to 3
f//uW
whites'
nx/t*> 3
//.STW
ilS~//o'/
/ / 3, &
J? 33
+JZ2>o
CYLINDER TEMPERATURES
Cylinder # 1
&X7
6> 3C
(e 3 (
(si!
(*3Z
uzt
Cvlmder # 2
ix-s-yJ
i>'7V 1 <7?
.0 7
S~73
jT?6.
£~7 to
Cvhnder # 3
L>Ci>
(e o£~
kO 7
(pO*4-
G>oX
0>e>?
Leo Lfi
Cylinder # 4
(s b> Cfi
ifCe 7
bG<\
Go, jr
67/
(*7 f
Cylinder # 5
tpjs^r
(s
Us"3
lfS7
(fSZp
Cylinder # 6
&Z1
(e X
(pX(s
L? X
£.2 ?
CrXCr
bX-U
Cylinder # 7
L> V-i"
ir H L>
6W*
i"/r
iff 9
Cylinder # 8
77/
7? /
7 7V
7 7 y
77 7
77-/
11H
Cylinder # 9
(stir
&>S7
U>t7
6>9X.
Lp'gJ
L*9Z.
Cylinder # 10
(j> JjV
(s3X
L,2(o
^3 V
(dZjT~
&39
Cylinder f 11
Cytilp&4Ll2
Compressor Capacity (MMscfh)
f2..i9
92.31
93, f O
Compressor Suction Pressure (psig)
JTCC,
rsur
S'o
Compressor Suction Temperature (°F)
t*£~
(*rs=-
Compressor Discharge Pressure (psig)
nHL.o
7V7. o
Vile
7 YG>
7H(j>
7V6»
~7HU>
Compressor Discharge Temperature (°F)
12 3
J2J>
nz
Pocket L'nloader Setting
i
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I
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F-104 ~
-------
ENGINE OPERATING DATA
Engine Model/Numbi
Dale:
Name of Data
'Number.
RarQifaer- ' \ t /£
\f*/f
Time
!Hco
iHir
mio
ifoo
Engine Horsepower
i*n. ¦5"
itlL, 7
Enpne Speed (fpm)
2c (
1
±co
Engine Torque (%)
t I
Cylinder # 6
6,2%
Cylinder # 7
(*s-\
LeS~t
IsSJl
Cviinder # 8
71*
?7?r
~7 HO
17b
7 fto
Cylinder W 9
(o
lei I
<* "*/1
Cviinder # 11
Cylinder # 12
Compressor Capacity (MMscfh)
9-2. o
93,0
Compressor Suction Pressure (psig)
^ f
Compressor Suction Temperature (°F)
'
Compressor Discharge Pressure (psig)
71S~
"iff
nK
~?fS~
7V
-------
ENGINE OPERATING DATA Engine Mcxkl/Numbcn Cm\Ac -/a.
D.te: n h»fVH '
Name of Dau Recorder ^
Time
a v
/LoO
iU / 5""
10,20
i(. H 5~
I
Engine Horsepower
Enpne Speed (rpm)
3^3.
3 •
/
/
i
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EXHAUST MANIFOLD
Temperature (°F)
Pressure (in Hg)
Scavenger Air Pressure
227
22 t
2.Z1
22 7
CYLINDER TEMPERATURES
Cvtinder # 1
0,25"
Cylinder # 2
S~22-
rs<
Tzo
Cvtinder # 3
6 Id
0 to
LffC^
^ i o
(o\D
Cvimder # 4
te 72
b 72.
(*72
fc72
Cvhnder # 5
Cr 5~9
LeU-O
(els (
0,^7
(»(i>0
Cylinder # 6
(p3c>
(?30
Cylinder # ?
IsjT3
2.
&s~t
6-5"/
us"o
Cylinder # 8
7 ^2- '
777
7 fro
77 R
mi*
Cylinder # 9
(f 9 -3
Lqo
£>
iv±-~
7<4L>
7Vk
Compressor Discharge Temperature (°F)
1 2-2-
Pocket Unloader Setting
-
1
F-106
\
\
-------
ENGINE OPERATING DATA
05 2£>
D°[
Engine Model/Number 6Ml!c.-tO y^/5^
Dltc: il/ll/1* '
Name of Data Recorder l>OC-t2
***- l'c
Engine Horsepower
ITT
Engine Speed (fpn)
20 <0
2* %
199
Engine Torque (%>)
Igmuon Timing (degrees)
Fuel Flow Rate (scl
Orb
/mi
/r^a-
/fq*2.
/S^XX
Fuel Temperature ( F)
A£_
70
~7 I
17T
JZjL
?g-
72.
Fuel Header Pressure (psig)
(e V
ltd.
M.
(fS~
AIR INTAKE MANIFOLD
Air Flow Rate (a:fm)
ni/i* t
n*/» i
rz
1 M/
i
£-7 2.
Cylinder # 3
•s-g/
S~9Z
£~1Z.
^7-3
<-¦?!
-T9 /
Cylinder» 4
UZS
ieZ 7
bZZ
(*X?(
Cylinder # 6
-T7£
Sic U
1**11
£2Z
~gW_
r ¥9
4>
Cylinder# H*
Compressor Capacity (MMscfh)
Compressor Suction Pressure (psig)
6>if
Comprtisor Suction Temperature (°F)
JjljL
Jl±
t* £
Compressor Dischaije Pressure (psig)
7V7
1*/Le
7Hit
-?V te
7VO>
Compressor Dischai-ge Temperature (°F)
12^
IXO
JjJjL.
)X.
11 5T
Pocket UnlOJder Setting
Li
Bar. t\
fat da^
Th>c
-^4
-T3
0 I
Zti
77
2zcv
F-107
-------
ENGINE OPERATING DATA
Engine Model/Numbec.
Date:
Kly OP-
'/v/v
de. to
/*&-
I 5~
H3S-
A\/b
Name of Data Recorder
- St
¦Jrt
Engine Honepower
Engine Speed (fpm)
10C
*1 Y
Engine Torque (%)
Ignition Timing (degrees)
FUEL MANIFOLD
Fuel Flow Rate (scfj
'k.
I&JL0
15-
Fuel Temperature ( F)
T^r
~ipr
_2-3
Fuel Header Pressure (psig)
6V
AIR INTAKE MANIFOLD
Ajr Flow Rate (acfm)
Air Manifold Temperature (°F)
\\7J1vz
Air Manifold Pressure (in Hg or psig)
Temperature
MANTFC
re CF)
Pressure (in Hg)
Scavenger Air Pressure (jwfg) jh. HtjO
a 1 ^
£, I Lp
CYLINDER TEMPERATURES
Cylinder # 1
6'fZ
¦a <70
LtQ 0
Gfnf
Cylinder # 5
Ip32_
tfSO
Cylinder # 6
J>7
7 2^=cr
Cylinder # 7
Ml
Cylinder # 8
7 n
7V?
677
Cylinder # 10
*
b W
Cvlmder # 11
Cylinder # 12
Compressor Capacity (MMscfh)
Compressor Suction Pressure (pstg)
Compressor Suction Temperature (°F)
Com pressor Discharge Pressure (psig)
"7*7
-------
ENGINE OPERATING DATA £ o
2sd-
2SJ-
2oX
Joo
io (
Engine Torque (%)
Ignition Timing (degrees)
FUEL MANIFOLD t
fuel Row Rate (scfft)
TV
(7T
ICObZ
Fuel Temperature f°F)
iff S"
JlAl
(7T
UH
JdL
Fuel Header Pressure (psig)
cZS-
.2X1
AIR INTAKE MANIFOLD
Air Flo* Rate (acfm)
Manifold Temfwrature ( F)
Air Manifold Pressure (in Hg or psig)
EXHAUST MANIFOLD
Temperature ( F)
Pressure (in Hg)
Scivtnger Air Preisiire (e^cT /*%¦ H.
3jT
J3
-3Q>
_^L
-3 3'
CYLINDER TEMPERATURES
Cylinder # I
(p
L>%3>
(s 10
6*7
GS 1
^-3 7
^33
(£21
io* %
^3 7
^3 /
-Z2A~
_zL2^_
5~~?Lp
rm
£~7 3
Cylinder # 4
3 7«g
-S"**
UjfT?
£~9!
5~7V
Cylinder # S
5aZ
Ce ZC
JeJJL
fo 10
Cylinder # 6
Z5ZZZ
Jc2221
-6*^9
- c>
Ls> X~)
JeAZ-
_
(pit
Cvlinder # 8
&.3y
h>2~l
(*2->
feZ3
&V2-
6? (0 ¥
v
le Le'i
Le>L>(i
lei Q
£~St
£~<\l
IcO^
^77
CylmdKf'4^1
Cylin4rfV-U.
Compressor Capacity (MMscfh)
Compressor Suction Pressure (psig)
jzn
Compressor Suction Temperature (°F)
JUL
wlT
ieC*
Compressor Discharge Pressure (psig)
7V9
_zv
£
yzro
7-T^7
75^
Compressor Discharge Temperature ( F)
iz V
/a
/3.6>
/* 3
A? 2.
Pocket Unioader Setting
F-109
\
\
-------
ENGINE OPERATING DATA
Engine Model/Nui
Due: II
Name of Dau
Recorder iG
2 - -
Engine Torque (9fc)
Ignition Timing (degrees)
FUEL MANIFOLD {
Fuel Flow Rate (scfjn)
loicZ
2. S"
Ux I
Cylinder # 8
bit
Cylinder # 9
tojf
(sto S
Cylinder # 10
iT
-------
ENGINE OPERATING DATA
Engine Model/Number Crdfi fc /*!
D..e: n 13./fV
Name of Dau Recorder-
*6>C,
Engine Horsepower
to oO
I53JS
f
ML,
woo
in:
HZto
Engine Speed (rpm)
IPG
¦a.? 9
Ml
2>o3>
Z1 V«
Fuel Tempcritun: f°F)
s~x
s~r
Jljl
¦51
L>
Fuel Header Pressure (psig)
JL2-
x~>
£ 7
2.7
n n
X7
-A2_
AIR INTAKE MANIFOLD
Ajr Flow Rate (airfm)
TzZE
*S-/€(>
vsyvts
Tj/r
Ait Manifold Temperature (°F)
m/Vls
.Air Manifold Pressure (in Hg or psig)
EXHAUST MANIFOLD
Temperature (°F)
Pressure (in Hg)
-3 y
Scavenger Air Pretturt (ptigf /n 0
Jd-
21
3V
jz.
CYLINDER TEMPERATURES
Cvlmder # 1
Glo
QC.S—
^7^
4>72
tQl*
h/S-
c,iH
-T?f
lIH
i
-T73"
S?(r
Cylinder # 4
¦rva.
^7-2-
ni
-T9-S
Sf /
Cylinder # 5
^9
9
6>2-57?
Cylinder # 7
6A
6-^7
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|
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Air Flow Rate (acfm)
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Compressor Suction Temperature (°F)
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ENGINE OPERATING DATA Enpne Model/Numlyr
Dale: ^ ^
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Tune
AT/iT
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Engine Speed (rpmj
A <7 7
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Ignition Timing (decrees)
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Fuel Flow Rate (sirfrp)
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Compressor Suction Pressure (psig)
Compressor Suction Temperature (°F)
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ENGINE OPERATING DATA Enjine Model/Nunjbcr^ GrtAvJ6-|0
Name of Data Recorder Uj
Time
103Z
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Engine Honepower
Engine Speed (rpm)
Engine Torque (^e)
Ignition Timing; (degrees)
FUEL MANIFOLD
Fuel Flow Rate (scfm)
Fuel Temperature (°F)
Fuel Header Pressure (psig)
AIR INTAKE MANIFOLD
Air Flow Rate (acfm)
Air Manifold Temperature (°F)f (l/tJ)
WS
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EXHAUST MANIFOLD
Temperature (°F)
Pressure (in Hg)
Scavenger Air Pressure (psig)
CYLINDER TEMPERATURES
Cylinder # 1
Cylinder # 2
Cylinder # 3
CvJinder # 4
Cylinder # 5
Cylinder # 6
Cylinder # ?
Cylinder # 8
Cylinder # 9
Cylinder # 10
Cylinder # 11
Cylinder # 12
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Compressor Suction Pressure (psig)
Compressor Suction Temperature (°F) ^
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Name of Data Recorder
Time
K3C*
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Engine Speed (rpm)
Engine Torque (^)
Ignition Timing (degrees)
FUEL MANIFOLD
Fuel Flow Rjte (scfm)
Fuel Temperature (°F)
Fuel Header Pressure (psig)
AIR INTAKE NUNIFOLD
Air Flow Rate (acfm)
Air Manifold Trmperaturt (°F)
lo?,/\ow
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Temperature (°F)
Pressure (in Hg)
Scavenger Air Pntssure (psig)
CYLINDER TEMPERATURES
Cylinder # 1
Cylinder # 2
Cvhnder # 3
Cylinder # 4
Cylinder # 5
Cylinder # 6
Cylinder # 7
Cylinder # 8
Cylinder # 9
Cylinder # 10
Cvhnder # 11
Cylinder # 12
Compressor Capacity (MMscfh)
Compressor Suction Pressure (psig)
Compressor Suction Temperature (°F)
UK
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Compressor Discharge Temperature (°F)^
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Time
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Engine Speed (rpm)
Engine Torque (5fc)
Ignition Timing (degrees)
FUEL MANIFOLD
Fuel Row Rjte (scfm)
Fuel Temperature (°F)
Fuel Header Pressure (psig)
AIR IVTAKF MANIFOLD
Air Row Rate (aefm)
KA»r NUflifold Temperature (°F)ft/^
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Temperature (°F)
Pressure (in Hg)
Scavenger Air Pressure (psig)
CYLINDER TEMPERATURES
Cylinder # 1
Cylinder # 2
Cylinder # 3
Cylinder # 4
Cylinder # 5
Cylinder # 6
Cylinder # 7
Cylinder # S
Cylinder # 9
Cylinder # 10
Cylinder # 11
Cylinder # 12
Compressor Capacity (MMscfh)
Compressor Suction Pressure (psig)
Compressor Suction Temperature (°F) X
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Compressor Discharge Temperature (°F) )(
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F-116 "
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ENGINE OPERATING DATA &ip«« Mo^Nujibti^( 3
Name of Pat* Recorder 6r«>uJ
Time
rtoo
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/
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Temperature (°F)
Pressure (in Hg)
Scavenger Air Pressure (psig)
rvI.IMDFR TEMPERATURES
Cylinder # t
Cylinder # 2
Cylinder * 3
Cylinder # 4
Cylinder # 5
Cylinder # 6
Cylinder # 7
Cylinder # 8
Cylinder # 9
Cvlinder # 10
Cvlinder # 11
Cylinder # 12
Compressor Capacity (MMscfh)
Compressor Suction Pressure (psig)
Compressor Suction Temperature (°F) y
ujA-
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Compressor Dischaige Temperature (°F) t
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Pocket Unloader Setting
-
F-117
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ENGINE OPERATING DATA Enpne Model/Number
Date: llflHMH '
Name of Dan Recorder AJC-C^/G-SUi
Time
lozo
ZoilT
ZOHO
ZcjT^
Engine Horsepower
Enpne Speed (rpm)
Engine Torque (9c)
Ignition Timing (degrees)
FUEL MANIFOLD
Fuel Flow Rite (scfm)
Fuel Temperature (°F)
1
Fuel Header Pressure (psig)
' AIR INTAKE MANIFOLD
Air Flow Rjte (acfm)
Ait Manifold Temperature (°F)
toi/tci'
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r
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, Temperature (°F)
1 Pressure (in Hg)
1 Scavenger Air Pressure (psig)
1 CYLINDER TEMPERATURES
Cvlinder # 1
| Cylinder # 2
l Cvlinder # 3
Cvlinder # 4
Cylinder # 5
Cvlinder # 6
Cylinder # 7
' Cvlinder # 8
Cvlinder # 9
; Cylinder # 1C
Cvlinder # U
Cvlinder # 12
Compressor Capacity (MMsefh)
Compressor Suction Pressure (psig)
Compressor Suction Temperature (°F)
L> f
(< 1
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Compressor Discharge Pressure (psig)
Compressor Discharge Temperature (°F)
/2.V
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Pocket L'nloadcr Setting
1
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UNIT NO. 11
DESCRIPTION
VALUE UNITS
DESCRIPTION
VAI IIP
inkVta
UNITS
wm i tr
ENGINE SPEED
301 J)
RPM
LOINLET
136.0
DEGF
LUBE OIL PRESS
27JJ PSIG
LO OUTLET
1S5JI
DEGF
LO FILTER DIFF
2.0 PSIG
J W INLET
164.0
DEGF
FUELDIFF
43 J)
"H20
JW OUTLET
170J)
DEGF
FUEL STATIC
51.0 PSIG
FUEL GAS
58.6
DEGF
FUEL FLOW
14195.0
SCFHR
POWER CYL 1L
21S2J)
DEGF
SCAVPRESS
213J)
"H20
POWER CYL 2L
2192.0
DEGF
INLET DIFF
3.0
"H20
POWER CYL 3L
2192.0
DEGF
DISCHARGE GAS
713.0
PSIG
POWER CYL 4L
2132.0
DEGF
VIBRATION
5.0
MILS
POWER CYL 5L
66,0
DEGF
FUEL VALVE OUTPUT
62.0
X
POWER CYL 1R
2192.0
DEGF
MONTHLY FIRED HOURS
3161
HRS
POWER CYL 2R
2192.0
DEGF
POWER CYLTRABON COUNT
2823.0
QTS
POWER CYL 3R
woon
L I9&.U
DEGF
COMPCYLTRABON COUNT
1077.0
QTS
POWER CYL 4R
2192.0
DEGF
POWER CYL 24 HR. TOT
20.0
QTS
POWER CYL 5R
2192,0
DEGF
COUP CYL 24 HR- TOT
7.0 QTS
CRANKCASE COUNTS
0.0
QTS
1
3
5
7
9
11
13
15
TATIO
PRINT
F-148
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UNIT NO. 11
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
299JI
RPH
LO INLET
135J)
DEGF
LUBE OiL PRiiSS
m
PSIG
LO OUTLET
w
i\e/»c
vcur
LO FILTER DIFF
2.0
PSIG
J W INLET
164J0
DEGF
FUEL DIFF
(2J)
"H20
JW OUTLET
170 J)
DEGF
FUEL STATIC
50.0
PSIG
FUEL GAS
SBJ)
DEGF
FUEL FLOW
14141J)
SCFHR
POWER CYL 1L
21S2J8
DEGF
SCAV PRESS
212.0
¦H20
POWER CYL 2L
2192J0
DEGF
INLET DIFF
3.0
*H20
POWER CYL 3L
2192.0
DEGF
DISCHARGE GAS
713.0
PSIG
POWER CYL IL
2182.0
DEGF
VIBRATION
5.0
MILS
POWER CM
67.0
DEGF
FUEL VALVE OUTPUT
63.9
\
IV
POWER CYL 1R
7107(1
to IVkM
DEGF
HONTHLYFIRliD HOURS
3161
HRS
POWER CYL 2R
2192.0
DEGF
POWER CYL TRABON COUNT
2823.0
QTS
POWER CYL 3R
2192.0
DEGF
COMPCYLTRABON COUNT
1077.0
QTS
POWER CYL 4R
2192 J)
DEGF
POWER CYL 24 HR. TOT
20.0
QTS
POWER CYL 5R
2192.0
DEGF
COUP CYL 24 HR. TOT
U
QTS
CRANKCASE COUNTS
0.0
QTS
F-149
1
3
5
7
9
11
13
15
TATIO
PRINT
-------
UNIT NO. 11
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
301.0
RPH
LO INLET
135J)
DEGF
LUBE OIL PRESS
27 Jl
PSIG
LO OUTLET
iSujB
DEGF
LO FILTER DIFF
2.0
PSIG
J W INLET
164.0
DEGF
FUEL DIFF
43j0
¦H20
JW OUTLET
170J)
DEGF
FUEL STATIC
51.0
PSIG
FUEL GAS
58.0
DEGF
FUEL>LOW
14257.0
SCFHR
POWER CYL 1L
2182.0
DEGF
SCAV PRESS ^
211J)
"H20
POWER CYL 2L
2192j0
DEGF
INLET DIFF
3.0
' H20
POWER CYL 3L
2192.0
DEGF
DISCHARGE GAS
713.0
PSIG
POWER CYL 4L
2132.0
DEGF
VIBRATION
A
mi
MILS
POWER CYL 5L
mm a
utw. i-
FUEL VALVE OUTPUT
62.0
*
POWER CYL 1R
2192.0
DEGF
MONTHLY FIRED HOURS
3161
HRS
POWER CYL 2R
2192.0
DEGF
POWER CYLTRABON COUNT
2823.0
QTS
POWER CYL 3R
2192.0
DEGF
COUP CYL TRABON COUNT
1077J)
QTS
POWER CYL 4R
2192.0
DEGF
POWER CYL 24 HR. TOT
20.0
QTS
POWER CYL 5R
2192,0
DEGF
COUP CYL 24 HR. TOT
7J
QTS
CRANKCASE COUNTS
0.0
QTS
F-150
1
3
5
7
9
11
13
15
TATIO
PRINT
-------
UNIT NO. 11
DESCRIPTION
VALUE UNITS
DESCRIPTION
VALUE
UNITS
BfGICSPffl)
299.0 RPM
LONE
135.0
DE6F
LUBE OL PRESS
27.0 P9G
LOOUTlfT _
m
DEGF
LOFLMDFF
20 PSJG
JWNfT
m
DEGF
FIB. OFF
42.0 "H20
JW OUTLET
m
DEGF
FUEL STATIC
saopsiG
FIE GAS
58.0
DEGF
FIB. FLOW
14154J0 SCFHR
POWBICYL1L
2192J0
DEGF
SCWPRESS
211.0 "H20
POWBICYL2L
219Z0
DEGF
MHDFF
10 "H20
P0HRCYL1
2152.0
DEGF
DISCHARGE GAS
7110 PSJG
POWBICYL4L
2192.0
DEGF
VGRATION
to its
ponecvLa.
67.0
DEGF
FUBL VALVE OUTPUT
ao *
POWBICYL1R
2192.0
DEGF
MOHIHYFIB HOURS
3161 HRS
POWERCYL2R
2192.0
DEGF
POWBRCYLTRABOHCOtlff
2823.0 QTS
POHHCYL3R
2192.0
DEGF
COIP CYLTRABOII COUNT
1077.0 QTS
PWeCYL4R
2192J)
DEGF
POeCYL24»lTOT
xn (VTC
C.1MJ
pnmrvi n
i vaautv ibifli
limn
nrr r
UDir
COMP CYL 24 HR TOT
7.0 QTS
CRANKCASE COUNTS
ao QTS
11/15/94 1 0:36:02
1
3
5 7 9 11
1315
TATIQ
3RIN1
F-151
-------
UNIT NO. 11
DESCRIPTION
VALUE UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
300.0
RPM
LO INLET
135J)
DEGF
LUBE OIL PRESS
27.0 PSIG
LO OUTLET
156.0
DEGF
L 0 FILTER DIFF
2.0 PSIG
J W INLET
1(4.0
DEGF
FUEL DIFF
42.0
"H20
JW OUTLET
170 J)
DEGF
FUEL STATIC
50.0
PSIG
FUEL GAS
88J)
DEGF
FUEL FLOW
14143.0
SCFHR
POWER CYL 1L
2192.0
DEGF
SCAVPRESS
212J)
"H20
POWER CYL 2L
2192J)
DEGF
INLET DIFF
3.0
"H20
POWER CYL 3L
2192.0
DEGF
DISCHARGE GAS
713.0
PSIG
POWER CYL 4L
MM ft
AIM..U
DEGF
VIBRATION
7.0
MILS
POWER CYL 5L
m
DEGF
FUEL VALVE OUTPUT
62.0
*
POWER CYL 1R
2192.0
DEGF
MONTHLY FIRED HOURS
3161
HRS
POWER CYL 2R
2192.0
DEGF
POWER CYL TRABON COUIfT
2823.0
QTS
POWER CYL 3R
2192.0
DEGF
COMPCYLTRABON COUNT
1077.0
QTS
POWER CYL 4R
2182.0
DEGF
POWER CYL 24 HR. TOT
20.0
QTS
POWER CYL SR
2192.0
DEGF
COMP CYL 24 HR. TOT
U QTS
CRANKCASE COUNTS
0.0
QTS
11/15/94
10:40:20
1
O
5
7
9
11
13
15
TATIOI
PRINT
F-152
-------
UNIT NO. 11
DESCRIPTION
VALUE
UNITS
DESCRiPTiON
VALUE
UNITS
ENGINE SPEED
300.0
RPH
LO INLET
m
DEGF
LUBE OIL PRESS
27.0
PSIG
LOOUTLET
1SEJI
DEGF
LOFlLTtRDIff
2J)
PSIG
J W INLET
K4.0
DEGF
FUEL DiFF
42.0
"H20
JW OUTLET
170 J)
DEGF
FUEL STATIC
50.0
PSIG
FUEL GAS
SSJ)
DEGF
FWEL FLOW
14159.0
SCFHR
POWER OfLIL
21310
DEGF
SCAV PRESS
211.0
"H20
POWER CYL2L
2192.0
DEGF
1NLETDIFF
3.0
"H20
POWER CYL3L
21910
DEGF
DISCHARGED
712.0
PSIG
POWER CYL4L
2192.0
DEGF
VIBRATION
6.0
MILS
POWER CVLSL
67.0
DEGF
FUEL VALVE OUTPUT
62.0
I
POWER CYL1R
2192.0
DEGF
MONTHLY FIRED HOURS
3161
HRS
POWER CYL2R
2192.0
DEGF
POWER COIABON COUNT
2823.0
QTS
POWER CYL3R
2192.0
DEGF
COUP CYLTWflON COUNT
1077.0
QTS
POWER CYL4R
2192.0
DEGF
POWER CYL 24 HR. TOT
20.0
QTS
POWER CYLSR
2192J)
DEGF
COMPCYL24HR.TOT
7JB
QTS
CRANKCASE COUNTS
0.0
QTS
1
3
5
7
9
11
13
15
TATIO
PRINT
F-153
-------
UNIT NO. 11
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
301.0
RPM
LO INLET
135J1
DEGF
LUBE OIL PRESS
m
PSIG
LOOITTLET
156.0
DEGF
LO FILTER DIFF
2.0
PSIG
J W INLET
164.0
DEGF
FUEL DIFF
42.0
"H20
JWOUHET
170.0
DEGF
FUEL STATIC
SQ.6
PSIG
EtICI ftJK
1 WkL WW
S9j0
DEGF
FUEL FLOW
14143.0
SCFHR
POWER CYL 1L
2132.0
DEGF
SCAVPRESS
212J)
"H20
POWER CYL 2L
2192J)
DEGF
INLET DIFF
3.0
"H20
POWER CYL 3L
2192.0
DEGF
DISCHARGE GAS
713.0
PSIG
POWER CYL 4L
2182.0
DEGF
VIBRATION
6.0
MILS
POWER CYL 5L
68.0
DEGF
FUEL VALVE OUTPUT
62.0
*
POWER CYL 1R
2192.0
DEGF
MONTHLY FIRED HOURS
3162
HRS
POWER CYL 2R
2192.0
DEGF
POWER CYLTRABONCOUITT
2823.0
QTS
POWER CYL 3R
"MlWfl
4IM.V
DEGF
COMPCYLTRABON COUNT
1077.0
QTS
POWER CYL 4R
2192.0
DEGF
POWER CYL 24 HR. TOT
20.0
QTS
POWER CYL 6R
2192.0
DEGF
COUP CYL21HR. TOT
7J
QTS
CRANKCASE COUNTS
0.0
QTS
1
3
5
7
9
11
13
15
TATIO
PRINT
F-154
-------
UNIT NO. 11
DESCRIP110N
VALUE UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
300.0 RPN
LO INLET
135.0
DEGF
LUBE OIL PRESS
m PSIG
LOOUTLET
1SJ)
DEGF
LO FILTER DIFF
2.0 PSIG
JW INLET
m
DEGF
FUEL DIFF
43.0 "H20
JW OUTLET
170.0
DEGF
FUEL STATIC
51.0 PSIG
FUEL GAS
S5J!
DEGF
FUEL FLOW
14195J) SCFHR
POWER CYL 1L
2152.0
DEGF
SCAV PRESS
212.0 "H20
POWER CYL 2L
2192.0
DEGF
INLET DIFF
3.0 "H20
POWER CYL 3L
2192.0
DEGF
DISCHARGE GAS
712.0 PSIG
POWER CYL 4L
2192.0
DEGF
VIBRATION
7.0 MILS
POWER CYL 5L
66.0
DEGF
FUEL VALVE OUTPUT
63.0 \
POWER CYL 1R
2192 J)
DEGF
MONTHLY FIRE D HOURS
3162 HRS
POWER CYL 2R
2192.0
DEGF
POWER CYL TRABON COUNT
2823.0 QTS
POWER CYL 3R
2192.0
DEGF
COMP CYL TRABON COUNT
1077.0 QTS
POWER CYL 4R
2192.0
DEGF
POWER CYL 24 HR. TOT
20.0 QTS
POWER CYL 5R
2192.0
DEGF
COUP CYL 24 HR. TOT
7.0 QTS
CRANKCASE COUNTS
0.0 QTS
1
3
5
7
9
11
13
15
TATIO
PRINT
F-155
-------
UNIT NO. 11
DESCRIPTION
VALUE UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
299.0 m
LO INLET
135J)
DEGF
LUBE OIL PRESS
27.0 PSIG
LO OUTLET
157 J)
DEGF
LO FILTER DIFF
2.0 PSIG
J W INLET
164.0
DEGF
FUEL DIFF
43 J) "H20
JW OUTLET
170 J)
DEGF
FUEL STATIC
51.0 PSIG
FUEL GAS
59.0
DEGF
FUEL FLOW
14188.0 SCFHR
POWER CYL 1L
2132.0
DEGF
SCAVPRESS
211J 'H20
POWER CYL 2L
2192.0
DEGF
INLET DIFF
3.0 mM
POWER CYL 3L
2192.0
DEGF
DISCHARGE GAS
712.0 PSIG
POWER CYL 4L
2192.0
DEGF
VIBRATION
6.0 NILS
POWER CYL 5L
67.0
DEGF
FUEL VALVE OUTPUT
62.0 X
POWER CYL 1R
2192.0
DEGF
MONTHLY FIRED HOURS
3162 HRS
POWER CYL 2R
2192.0
DEGF
POWER CYLTOABON COUNT
2823.0 QTS
POWER CYL 3R
2192.0
DEGF
COMPCYLTRABON COUNT
1077.0 QTS
POWER CYL 4R
2192.0
DEGF
POWER CYL 24 HR. TOT
20.0 QTS
POWER CYL 5R
2192.0
DEGF
COUP CYL 24 HR. TOT
7J) QTS
CRANKCASE COUNTS
0.0 QTS
F-156
1
3
5
7
9
11
13
15
TATIO
PRINT
-------
UNIT NO. 11
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
300J)
RPH
LO INLET
135J
DEGF
LUBE OIL PRE SS
27.0
PSIG
LOOUILET
m
DEGF
LO FILTER DIFF
2.0
PSIG
J W INLET
m
DEGF
FUEL DIFF
43j0
¦H20
JW OUTLET
flU
DEGF
FUEL STATIC
51.0
PSIG
FUEL GAS
&0
DEGF
FUEL FLOW
H177JB
SCFHR
POWER CYL 1L
2192J
DEGF
SOW PRESS
211j0
"H20
POWER CYL 2L
2192J)
DEGF
INLET DIFF
3.0
"H20
POWER CYL 3L
2192.0
DEGF
DISCHARGE GAS
713.0
PSIG
POWER CYL
-------
UNIT NO. 11
DESCRIPTION
VALUE UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
301.0 RPN
LO INLET
1&0
DEGF
LUBE OIL PRESS
27J) PSIG
LOOUTLET
157 J)
DEGF
LO FILTER OFF
2.0 PSIG
J W INLET
164.0
DEGF
FUEL DIFF
43.0 *H20
JW OUTLET
170 J)
DEGF
FUEL STATIC
SID PSIG
FUEL GAS
S.G
DEGF
FUEL FLOW
14206J) SCFHR
POWER CYL 1L
2192J)
DEGF
SCAVPRESS
210jD "H20
POWER CYL 2L
2192JI
DEGF
INLET DIFF
3.0 "H20
POWER CYL 3L
2192.0
DEGF
DISCHARGE GAS
712.0 PSIG
POWER CYL 4L
2192.0
DEGF
VIBRATION
7.0 MILS
POWER CYL 5L
68.0
DEGF
FUEL VALVE OUTPUT
63JI \
POWER CYL 1R
2192.0
DEGF
KONTHLYFIRED HOURS
3162 HRS
POWER CYL 2R
2192.0
DEGF
POWER CYLTRABON COUNT
2823.0 QTS
POWER CYL 3R
2192.0
DEGF
COUP CYLTRABON COUNT
1077.0 QTS
POWER CYL4R
2192.0
DEGF
POWER CYL 24 HR. TOT
20.0 QTS
POWER CYL 5R
2192.0
DEGF
COMP CYL 24 HR, TOT
U QTS
CRANKCASE COUNTS
0.0 QTS
1
3
5
7
9
11
13
15
TATIO
PRINT
F-158
-------
UNIT NO. 11
DESCRIPnON
VALUE
UNITS
DESCRiPTiON
VALUE
UfiiTS
ENGINE SPEED
299.0
RPH
LO INLET
135.0
DEGF
LUBE OIL PRESS
m
PSIG
LOOUHET
157JD
DEGF
LO FILTER DIFF
2.0
PSIG
J W INLET
m
DEGF
FUEL DIFF
43.0
"H20
JW OUTLET
170 J)
DEGF
FUEL STATIC
51.0
PSIG
FUEL GAS
59 J!
DEGF
FUEL FLOW
142S8.0
SCFHR
POWER CYL 1L
2132JI
DEGF
SCAV PRESS
211.0
"H20
POWER CYL 2L
2192 J)
DEGF
INLET DIFF
3J)
"H20
POWER CYL 3L
2192.0
DEGF
DISCHARGE GAS
712.0
PSIG
POWER CYL 4L
2192.0
DEGF
VIBRATION
7.0
MILS
POWER CYL 5L
69.0
DEGF
FUEL VALVE OUTPUT
63.0
*
POWER CYL 1R
2192.0
DEGF
MONTHLY FED HOURS
3162
HRS
POWER CYL 2R
2192.0
DEGF
POWERCYLTRABON COUKT
2823.0
QTS
POWER CYL 3R
2192.0
DEGF
COUP CYL 1MBON COUNT
1077.0
QTS
POWER CYL 4R
2192.0
DEGF
POWER CYL 2-1HR. TOT
20.0
QTS
POWER CYL SR
2192.0
DEGF
COUP CYL 24IHR. TOT
7.0
QTS
CRANKCASE COUNTS
0.0
QTS
1
3
5
7
9
11
13
15
TATIO
PRINT
F-159
-------
UNIT NO. 11
DESCRIPTION
VALUE UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
299 J) RPM
L 0 INLET
1XJ
DEGF
LUBE OIL PRESS
27.0 PSIG
L O OUTLET
157J
DEGF
L 0 FILTER DIFF
2JI PSIG
J W INLET
*4j0
DEGF
FUEL DIFF
42.0 -H20
JW OUTLET
170.0
DEGF
FUEL STATIC
51.0 PSIG
FUEL GAS
an
IM
-------
UNIT NO. 11
DESCRIP110N
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
302J)
RPH
LO INLET
13(1
DEGF
LUBE OIL PRESS
2S.0
PSIG
L O OUTLET
153JB
DEGF
LO FILTER DIFF
2.0
PSIG
JWINLET
WjO
DEGF
FUELDIFF
39.0
aH20
JW OUTLET
ITOjO
DEGF
FUEL STATIC
46j0
PSIG
FUEL GAS
S1J0
DEGF
FUEL FLOW
130611
SCFHR
POWER CYL 1L
m
DEGF
SOW PRESS
m
-H20
POWER CYL2L
DEGF
INLET DIFF
3.0
"H20
POWER CYL 3L
2192.0
DEGF
DISCHARGE GAS
712.0
PSIG
POWER CYL 4L
2132.0
DEGF
VIBRATION
U
NILS
POWER CYL 5L
70.0
DEGF
FUEL VALVE OILfTPUT
58.0
*
POWER CYL 1R
2192.0
DEGF
MONTHLYFIRED HOURS
3163
HRS
POWER CYL 2R
2192.0
DEGF
POWER CYLTHABON COUNT
2823.0
QTS
POWER CYL 3R
21S2.0
DEGF
COUP CYL TRABON COUNT
1077.0
QTS
POWER CYL 4R
2192.0
DEGF
POWER CYL 24 HR. TOT
20.0
QTS
POWER CYL SR
2192.0
DEGF
COUP CYL 24 HR. TOT
7J0
QTS
CRANKCASE COUNTS
0.0
QTS
F-161
1
3
5
7
9
11
13
15
TATIO
PRINT
-------
UNIT NO. 11
DESCRIPTION
VALUE UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
3Q0D RPM
LO INLET
134j0
DEGF
LUBE OIL PRESS
28J) PSIG
LO OUTLET "
153 J)
DEGF
LO FILTER DIFF
2j0 PSIG
J W INLET
164j0
DEGF
FUEL DIFF
m "H20
JW OUTLET
170.0
DEGF
FUEL STATIC
Jfi.0 PSIG
FUEL GAS
61JI
DEGF
FUEL FLOW
12989.0 SCFHR
POWER CYL1L
2192J
DEGF
SCAY PRESS
196.0 "H20
POWER CYL 2L
2192 J)
DEGF
INLET DIFF
3.0 *H20
POWER CYL 3L
2152.0
DEGF
DISCHARGE GAS
711.0 PSIG
POWER CYL 4L
2192.0
DEGF
VIBRATION
6,0 MILS
POWER CYL 5L
70.0
DEGF
FUEL VALVE OUTPUT
S8.0 %
POWER CYL 1R
2192.0
DEGF
HONTHLYFIRED HOURS
3163 HRS
POWER CYL 2R
2192 J)
DEGF
POWERCYLTRABON COUNT
2823.0 QTS
POWER CYL 3R
2192.0
DEGF
COMPCYLTRABON COUNT
1077.0 QTS
POWER CYL 4R
2192.0
DEGF
POWER CYL 24 HR. TOT
20.0 QTS
POWER CYL SR
2192.0
DEGF
COUP CYL24HR. TOT
7J QTS
CRANKCASE COUNTS
0.0 QTS
1
3
5
7
9
11
13
15
TATIO
PRINT
F-162
-------
UNIT NO. 11
DESCRIPTION
VALUE UNITS
DESCRIPTION
VALUE
UNITS
E16INE SPEED
300J) RPM
LO INLET
m
DEGF
LUBE OIL PRESS
m m
LOOUILET
153 J)
DEGF
L 0 FILTER 01FF
2J0 PSIG
JWIKLET
1MJ
DEGF
FUEL DIFF
39.1) "H20
JWOUHET
170.0
DEGF
FUEL STATIC
m psig
FUEL GAS
W
DEGF
FUEL FLOW
13006.0 SCFHR
POWER CYL1L
2132J)
DEGF
SCAVPRESS
197JD 'H20
POWER CYL 2L
2192JI
DEGF
INLETDIFF
3.0 "HZO
POWER CYL3L
2192.0
DEGF
DISCHARGE GAS
712.0 PSIG
POWER CYL 4L
2192.0
DEGF
VIBRATION
7.0 MILS
POWER CYL5L
M
DEGF
FUEL VALVE OUTPUT
58.0 *
POWER CYL 1R
2192.0
DEGF
lOKTHLYFRED HOURS
3163 HRS
POWER CYL 2R
2192J)
DEGF
POWER CYL TCABON COUNT
2823.0 QTS
POWER CYL 3R
2192.0
DEGF
COUP CYL 1WIB0N COUNT
1077.0 QTS
POWER CYL 4R
2192.0
DEGF
POWER CYL 21HR. TOT
20.0 QTS
POWER CYL SR
2192.0
DEGF
COUP CYL 21IIR. TOT
7j0 QTS
CRANKCASE COUNTS
0.0 QTS
1115/94
12:35:13
1
3
5
7
9
11
13
15
TATIO
PRINT
F-163
-------
UNIT NO. 11
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNiTS
ENGINE SPEED
m
RPH
LOWLET
M
DEGF
LUBE OIL PRESS
28.0
PSIG
LOOUTLET
m
DEGF
LO FILTER DIFF
2J)
PSIG
J W INLET
mi
DEGF
FUEL DIFF
38j0
"H20
JW OUTLET
170.0
DEGF
FUEL STATIC
46.0
PSIG
FUEL GAS
62J)
DEGF
FUELfLOW
12953.0
SCFHR
POWER CYL 1L
2132.0
DEGF
SCAVPRESS
196J)
"H20
POWER CYL 2L
2192J)
DEGF
INLET DIFF
3.0
"H20
POWER CYL 3L
2192.0
DEGF
DISCHARGE GAS
712J)
PSIG
POWER CYL 4L
2192.0
DEGF
VIBRATION
6,0
MLS
POWER CYL 5L
71.0
DEGF
FUEL VALVE OUTPUT
58.0
*
POWER CYL 1R
2192.0
DEGF
HOMY FIRED HOURS
3163
HRS
POWER CYL 2R
2192.0
DEGF
POWER CYL TISABON COUNT
2823.0
QTS
POWER CYL 3R
2192.0
DEGF
COHP CYL TRABON COUNT
1077JD
QTS
POWER CYL 4R
2192.0
DEGF
POWER CYL 24 HR. TOT
20.0
QTS
POWER CYL 5R
2192.0
DEGF
COMP CYL 24 HR. TOT
n
QTS
CRANKCASE COUNTS
0.0
QTS
F-164
1
3
5
7
9
11
13
15
TATIO
PRINT
-------
UNIT NO. 11
DESCRIPTION
VALUE UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
302J) RPH
LO INLET
134J
DEGF
LUBE OIL PRESS
2SJ0 PSIG
LOOUIIET
1531
DEGF
LO FILTER DIFF
2.0 PSIG
J W INLET
m
DEGF
FUEL DIFF
39.0 "H20
JW OUTLET
170J
DEGF
FUEL STATIC
46.0 PSIG
FUEL GAS
62i
DEGF
FUEL FLOW
13103.0 SCFHR
POWER CYL1L
m
DEGF
SCAV PRESS
19U "H20
POWER CYL2L
im
DEGF
INLET DIFF
3.0 -H20
POWER CYL3L
m
DEGF
DISCHARGE GAS
712.0 PSIG
POWER CYL4L
2192.0
DEGF
VIBRATION
6.0 MILS
POWER CYLSL
70.0
DEGF
FUEL VALVE OUTPUT
58.0 *
POWER CYL1R
2192.0
DEGF
MONTHLY FIRED HOURS
3163 HRS
POWER CYL2R
2192.0
DEGF
POWER CYLTRABON COUNT
2823.0 QTS
POWER CYL3R
2192.9
DEGF
COHPCYLTRABON COUNT
1077.0 QTS
POWER CYL4R
2192.0
DEGF
POWER CO HR. TOT
20.0 QTS
POWER CYLSR
2192.0
DEGF
COUP CO HH TOT
71 QTS
CRANKCASE COUNTS
0.0 QTS
11/15/94
12:45:20
1
3
5
7
9
11
13
15
TATIO
PRINT
F-165
-------
UNIT NO. 11
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
30ZJI
RPM
LOINLET
WJ)
DEGF
LUBE OIL PRESS
28.0
PSIG
LO OUTLET
153 J)
DEGF
LO FILTER DIFF
2jD
PSIG
JWINLET
1W.0
DEGF
FUEL DIFF
38.0
-H20
JW OUTLET
170.0
DEGF
FUEL STATIC
1U
PSIG
FUEL GAS
62J)
DEGF
FUEL FLOW
12951.0
SCFHR
POWER CYL1L
2192J)
DEGF
SCAY PRESS
197 J)
¦H20
POWER CYL 2L
2192.0
DEGF
INLET DIFF
3J)
"H20
POWER CYL 3L
2192.0
DEGF
DISCHARGE GAS
711.0
PSIG
POWER CYL 4L
2192.0
DEGF
VIBRATION
IJ
MILS
POWER CYL SL
m
DEGF
FUEL VALVE OUTPUT
58.0
*
POWER CYL1R
2192.0
DEGF
HOimiLYFIRED HOURS
m
HRS
POWER CYL 2R
2192.0
DEGF
POWER CYLTKABON COUNT
2823.0
GTS
POWER CYL 3R
21S2.0
DEGF
COUP CYL TRABON COUNT
1077.0
QTS
POWER CYL 4R
2192.0
DEGF
POWER CYL 24 HR. TOT
20.0
QTS
POWER CYL SR
2192.0
DEGF
COUP CYL2JHR. TOT
71
QTS
CRANKCASE COUNTS
0.0
QTS
1
3
5
7
9
11
13
15
TATIO
PRINT
F-166
-------
UNIT NO. 11
DESCRIPTION
VALUE UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
3Q2J) RPH
LOMLET
134J
DEGF
LUBE OIL PRESS
2SJD PSI6
LOOiniiT
m
DEGF
LO FILTER DIFF
2.0 PSIG
JWWLET
1641
DEGF
FUEL DIFF
38J) 'H20
JW OUTLET
170.0
DEGF
FUEL STATIC
16.0 PSIG
FUEL GAS
m
DEGF
FUEL FLOW
12941.0 SCFHR
POWER CYL 1L
m
DEGF
SCAV PRESS .
196.0 "H20
POWER CVL 2L
2O2J0
DEGF
INLET DIFF
3.0 "H20
POWER CYL 3L
2192J)
DEGF
DISCHARGE GAS
711.0 PSIG
POWER CYL 4L
2192.0
DEGF
VIBRATION
6.0 MILS
POWER CYL SL
71,0
DEGF
FUEL VALVE OUTPUT
58.0 «
POWER CYL 1R
2192.0
DEGF
MONTHLY FIRED HOURS
3164 HRS
POWER CYL 2R
2192.0
DEGF
POWER CYLTRABON COUNT
2823.0 GTS
POWER CYL 3R
2132.0
DEGF
COHP CVL TRAI30N COUNT
1077.0 QTS
POWER CYL 4R
2192.0
DEGF
POWER CYL 24 HR. TOT
20.0 QTS
POWER CYL 5R
2192.0
DEGF
COHP CYL 24 H!R. TOT
7il QTS
CRANKCASE COUNTS
0.0 QTS
1
3
5
7
9
11
13
15
TATIO
PRINT
F-167
-------
UNIT NO. 11
DESCRIPTION
VALUE UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
m
RPN
LOINLET
m
DEGF
LUBE OIL PRESS
28.0 PSIG
LOOUHET
153.0
DEGF
LO FILTER DIFF
2J) PSIG
J W INLET
WjO
DE6F
FUEL DIFF
38.0
BH20
JWOUHET
170 J)
DEGF
FUEL STATIC
m PSIG
FUEL GAS
624
DEGF
FUEL FLOW
1296ZJ)
SCFHR
POWER CYL 1L
2192J)
DEGF
SCAVPRESS
197J)
"H20
POWER CYL 2L
m
DEGF
INLET DIFF
3.0
"H20
POWER CYL 3L
2192.0
DEGF
DISCHARGE GAS
712.0
PSIG
POWER CYL 4L
2192.0
DEGF
VIBRATION
6.0
MILS
POWER CYL 5L
71J
DEGF
FUEL VALVE OUTPUT
58.0
*
POWER CYL 1R
2192.0
DEGF
HOimfLYFIRED HOURS
3164
HRS
POWER CYL 2R
2192.0
DEGF
POWER CYL TRABON COUNT
2823.0
QTS
POWER CYL 3R
2192.0
DEGF
COHPCYLTRABON COUNT
1077.0
QTS
POWER CYL 4R
2192J
DEGF
POWERCOHR.TOT
20.0
QTS
POWER CYL SR
2192.0
DEGF
COHP CYL 24 HR. TOT
7.0 QTS
CRANKCASE COUNTS
0.0
QTS
1
3
5
7
9
11
13
15
TATIO
PRINT
F-168
-------
UNIT NO. 11
DESCRIPTION
VALUE UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEIED
301D RPH
LO INLET
131JD
DEGF
LUBE OIL PRESS
28J} PSIG
LO OUTLET
1S3JD
DEGF
LO FILTER DIFF
2.0 PSIG
JW INLET
m
DEGF
FUEL DIFF
m "H20
JW OUTLET
170
DEGF
FUEL STATIC
46 J) PSIG
FUEL GAS
621
DEGF
FUEL FLOW
130S8.0 SCFHR
POWER CYL1L
m
DEGF
SCAV PRESS
196 J) "H20
POWER CYL 2L
m
DEGF
INLET DIFF
3.0 'H20
POWER CYL 3L
21310
DEGF
DISCHARGE GAS
711.0 PSIG
POWER CYL4L
2192.0
DEGF
VIBRATION
6.0 MILS
POWER CYL5L
71.0
DEGF
FUEL VALVE OUTPUT
S8.0 *
POWER CYL1R
2192.0
DEGF
MONTHLY FlfifD HOURS
3164 HRS
POWER CYL2R
2192.0
DEGF
POWER CYLIRABON COUNT
2823.0 QTS
POWER CYL 3R
2192.0
DEGF
COMPCYLTOBON COUNT
1077.0 QTS
POWER CYL 4R
2192.0
DEGF
POWER QOHR. TOT
20.0 QTS
POWER CYL 5R
2192.0
DEGF
COUP CYL24HR. TOT
7J0 QTS
CRANKCASE COUNTS
0.0 QTS
1
3
5
7
9
11
13
15
TATIO
PRINT
F-169
-------
UNIT NO. 11
DESCRIPTION
VALUE UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
284.0 RPN
LO INLET
1321
DEGF
LUBE OH PRESS
26.0 PSIG
LO OUTLET
m
DEGF
LO FILTER DIFF
2.0 PSIG
J W INLET
m
DEGF
FUEL DIFF
35J1 "H20
JW OUTLET
170 J)
DEGF
FUEL STATIC
42J) PSIG
FUEL GAS
63J)
DEGF
FUEL FLOW
11949J) SCFHR
POWER CYL tL
2182.0
DEGF
SCAVPRESS
168.0 "H20
POWER CYL 2L
21910
DEGF
INLET DIFF
3.0 "H20
POWER CYL 3L
2152.0
DEGF
DISCHARGE GAS
710.0 PSIG
POWER CYL 4L
2192.0
DEGF
VIBRATION
fl MILS
POWER CYL 5L
71.0
DEGF
FUEL VALVE OUTPUT
55.0 *
POWER CYL 1R
2192.0
DEGF
MOOTHLY FIRED HOURS
3165 HRS
POWER CYL 2R
2192.0
DEGF
POWER CYLTRABON COUNT
2823.0 CIS
POWER CYL 3R
L IJ4.lt
DEGF
COUP CVL TRABON COUNT
1077.0 QTS
POWER CYL 4R
2132.fi
DEGF
POWER CYL 24 HR. TOT
20.0 QTS
POWER CYL 5R
2192.0
DEGF
COMP CYL 24 HR. TOT
7J QTS
CRANKCASE COUNTS
Oil QTS
¦¦
1
3
5
7
9
11
13
15
TATIO
PRINT
F-170
-------
UNIT NO. 11
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEIiO
284J)
RPH
LO INLET
133 J)
DEGF
LUBE OIL f¥:SS
26.0
PSIG
LOOUTLET
152J)
DEGF
LO FILTER D IFF
2.0
PSIG
J W INLET
«4J
DEGF
FUEL DIFF
35.0
"H20
JWOURET
170.0
DEGF
FUEL STATIC
42.0
PSIG
FUEL GAS
m
DEGF
FUEL FLOW
11917 J)
SCFHR
POWER CYL 1L
m
DEGF
SCAV PRESS
170 J)
"H20
POWER CYL 2L
2192J)
DEGF
INLET DIFF
3J)
"H20
POWER CYL 3L
2192.0
DEGF
DISCHARGE GAS
710.0
PSIG
POWER CYL 4L
2192.0
DEGF
VIBRATION
6J)
MILS
POWER CYL 5L
71.0
DEGF
FUEL VALVE OUTPUT
S5.0
*
POWER CYL 1R
2192J)
DEGF
KONTHLYFRED HOURS
3165
HRS
POWER CYL 2R
2192.0
DEGF
POWER CYL TRABON COUNT
2823.0
QTS
POWER CYL 3R
2192.0
DEGF
COUP CYL TRABON COUNT
1077.0
OTS
POWER CYL 4R
2192D
DEGF
POWER CYL 21HR. TOT
20.0
QTS
POWER CYL 5R
2192.0
DEGF
COHP CYL 24 HR. TOT
7j0
QTS
CRANKCASE COUNTS
II
QTS
1
3
5
7
9
11
13
15
TATIO
PRINT
F-171
-------
UNIT NO. 11
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
283Jl
RPH
LO INLET
1331
DEGF
LUBE OIL PRESS
26.0
PSIG
LO OUTLET
1524
DEGF
LO FILTER DIFF
2.0
PSIG
JWINLET
m
DEGF
FUEL DIFF
36J)
"H20
JW OUTLET
170J
DEGF
FUEL STATIC
41j0
PSIG
FUEL GAS
m
DEGF
FUEL FLOW
11901J)
SCFHR
POWER CYL 1L
21S2JI
DEGF
SCAVPRESS
157 J)
aH20
POWER CYL 2L
2132 J)
DEGF
INLET DIFF
3.0
"H20
POWER CYL 3L
2132.0
DEGF
DISCHARGE GAS
710.0
PSIG
POWER CYL 4L
2132.0
DEGF
VIBRATION
6.0
MILS
POWER CYL 5L
72,0
DEGF
FUEL VALVE OUTPUT
55.0
*
POWER CYL 1R
2102.0
DEGF
HONTKLYFIRED HOURS
3165
HRS
POWER CYL 2R
2192.0
DEGF
POWER CYLTRABON COUNT
2823.0
QTS
POWERCYL3R
21S2.0
DEGF
COHPCYLHUBON COUNT
1077.0
QTS
POWER CYL 4R
2132.0
DEGF
POWER CYL 24 HR. TOT
20.0
QTS
POWER CYL SR
2192.0
DEGF
COUP CYL 24 HR. TOT
7J
QTS
CRANKCASE COUNTS
0.0
QTS
1
3
5
7
9
11
13
15
TATIO
PRINT
F-172
\
-------
UNIT NO. 11
DESCRIPTION
VALUE UNITS
DESCRIPTION
VALUE
UNITS
EKGME SPEEiD
280 RPH
LO INLET
1331
DE6F
LUBE OIL PRIISS
26 J) PSIG
LO OUTLET
m
DEGF
L 0 FILTER DIIFF
10 PSIG
JWIKLET
mi
DEGF
FUEL DIFF
35.0 aH2D
JW OUTLET
170.0
DEGF
FUEL STATIC
41jD PSIG
FUEL GAS
63J)
DEGF
FUEL FLOW
11923JI SCFHR
POWER CYL1L
2132.0
DEGF
SCAV PRESS
m "H20
POWER CYL 2L
m
DEGF
INLET DIFF
3.0 'H20
POWER CYL 3L
21919
DEGF
DISCHARGE GAS
710.8 PSIG
POWER CYL
-------
UNIT NO. 11
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
284J)
RPM
LOINLET
132.0
DEGF
LUBE OIL PRESS
26.0
PSIG
LO OUTLET
ffiJ)
DEGF
L 0 F1LTIRDIFF
2J)
PSIG
J W INLET
m
DEGF
RJEL DIFF
XJB
"H20
JW OUTLET
170J
DEGF
FUEL STATIC
CJD
PSIG
FUEL GAS
63J!
DEGF
FUEL FLOW
11970.0
SCFHR
POWER CYL 1L
2132.0
DEGF
SCAY PRESS
163.0
"H20
POWER CYL 2L
2192.0
DEGF
INLET DIFF
3.0
'H20
POWER CYL 3L
2192.0
DEGF
DISCHARGE GAS
710.0
PSIG
POWER CYL4L
2192.0
DEGF
VIBRATION
6.0
MILS
POWER CYL 5L
72.0
DEGF
FUEL VALVE OUTPUT
55.0
%
POWER CYL 1R
2182.0
DECF
MON1HLYFIRED HOURS
3165
HRS
POWER CYL 2R
2192.0
DEGF
POWER CYL TRABON COUNT
2223.0
QTS
POWER CYL 3R
2182.0
DEGF
COHP CYL TRABON COUNT
1077.0
QTS
POWER CYL 4R
2192J)
DEGF
POWER CYL Ml TOT
20.0
QTS
POWER CYL 5R
2192.0
DEGF
COUP CYL 24 HR. TOT 7j0 QTS
CRANKCASE COUNTS 0.0 QTS
F-174
1
3
5
7
9
11
13
15
TATIO
PRINT
-------
UNIT NO. 11
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
2831
RPH
LOINLET
1321
DEGF
LUBE OIL PRESS
26 J)
PSIG
L O OUTLET
152J}
DEGF
LO FILTER DUFF
2J)
PSIG
J W DUET
#4.0
DEGF
FUEL DIFF
ay
'H20
JW OUTLET
170.11
DEGF
FUEL STATIC
41J0
PSIG
FUEL GAS
63JB
DE6F
FUEL FLOW
11919.0
SCFHR
POWER CYL 1L
2192.0
DEGF
SCAV PRESS
168.0
aH20
POWER CYL 2L
m
DEGF
INLET DIFF
3J)
"H20
POWER CYL 3L
m
DEGF
DISCHARGE GAS
710.0
PSIG
POWER CYL 4L
2192D
DEGF
VIBRATION
6.0
MILS
POWER CYL 5L
72.0
DEGF
FUEL VALVE OUTPUT
55.0
*
POWER CYL 1R
2192.0
DEGF
MONTHLYFIRED HOURS
3165
HRS
POWER CYL 2R
2192.0
DEGF
POWER CYLTKABON COUNT
2823.0
QTS
POWER CYL 3R
2192J)
DEGF
COUP CYL TMBON COUNT
1077 J)
QTS
POWER CYL 4R
2192.0
DEGF
POWER CYL 24 HR. TOT
20.0
QTS
POWER CYL SR
2192J0
DEGF
COKPCOHR.TOT
7JJ
QTS
CRANKCASE COUNTS
0.0
QTS
1
3
5
7
9
11
13
15
TATIO
PRINT
F-175
-------
UNIT NO. 11
DESCRIPTION
VALUE UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
2MJ) RPH
LO INLET
132J0
DEGF
LUBE OIL PRESS
m PSIG
LOOUTLET
m
DEGF
L 0 FILTER DIFF
ID PSIG
J W INLET
mi
DEGF
FUELDIFF
37 J) aH20
JW OUTLET
178 J)
DEGF
FUEL STATIC
43.0 PSIG
FUEL GAS
63.5
DEGF
FUEL FLOW
12325.0 SCFHR
POWER CYL 1L
2132.0
DEGF
SCW PRESS
169 J) "H20
POWER CYL 2L
2192J)
DEGF
INLET DIFF
3.0 "H20
POWER CYL 3L
2192.0
DEGF
DISCHARGE GAS
711.0 PSIG
POWER CYL «L
2192.0
DEGF
VIBRATION
6.0 MILS
POWER CYL 5L
73.0
DEGF
FUEL VALVE OUTPUT
56.0 \
POWER CYL 1R
2182.0
DEGF
HONIHLYFIRED HOURS
3165 HRS
POWER CYL 2R
2192.0
DEGF
POWER CYLTRABON COUNT
2823.fi QTS
OfflKD rvi ID
i UnLit viLtfn
44MA
L IK.U
DEGF
COUP CYLTHABON COUNT
1077J) QTS
POWER CYL 4R
2182.0
DEGF
POWER CYL 24 HR. TOT
20.0 QTS
POWER CYL 5R
2192.0
DEGF
COMP CYL 24 HR. TOT
7J QTS
CRANKCASE COUNTS
OJ) QTS
l
3
5
7
9
11
13
15
TATIO
PRINT
F-176
-------
UNIT NO. 11
DESCRIPTION
VALUE UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
286.0 RPN
LQ INLET
135.0
DEGF
LUBE OIL PRIiSS
25.0 PSIG
LOOUTUT
157.C
DEGF
L 0 FILTER DIFF
2.0 PSIG
J W INLET
164.0
DEGF
FUEL BIFF
4IJ "IB
JW OUTLET
1101
DEGF
FUEL STATIC
4?J PSIG
FUELGAS
fiiii
liv.w
ikce
VbV 1
mim
13435.9 SCFHR
POWER 01IL
2182.0
DEGF
SCAV PRESS
183.11 *H20
POWER CVL2L
21921
DEGF
INLET DIFF
m "Ha
POWER CYL 3L
2132.11
DEGF
DISCHARGE GAS
710.0 PSIG
POWER CYL 4L
2132.0
DEGF
VSfUTKM
U MILS
POWER CYL 5L
m
DEGF
FUEL VALVE OUTPUT
».0 %
POWER CYL tR
2182.6
DEGF
KOKTHLY FIRED HOURS
3167 HRS
POWER CYL 2R
2192.0
DEGF
POWER CYL TOABON COUNT
iow.v yu
POWER CYL 31
2182.0
ne/»e
ucur
COUP CYL TRiiON COUNT
1084.6 QTS
POWER CYL 4R
DEGF
POWERCYL2iiHR.TOT
20.0 QTS
POWER CYL 5R
2192,0
DEGF
00WCn.UHR.TQT
M QTS
CRANXCASE COUNTS
0.0 QTS
F-177
1
O
5
"7
#
fl
•£J
n
1 ^
i j
15
TATIO
PRINT
-------
UNIT NO. 11
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
285.0
RPH
LO INLET
135J)
DEGF
LUBE OIL PRESS
2S.D
PSIG
LO OUTLET
157.0
DEGF
LO FILTER DIFF
2.0
PSIG
J W INLET
164.0
DEGF
FUEL DIFF
41J)
¦H20
JW OUTLET
170.0
DEGF
FUEL STATIC
4?JJ
p§ic
1 VIV
FUEL GAS
53 J!
DEGF
FUEkFLOW
13422.0
SCFHR
POWER CYL 1L
2132.0
DEGF
SCAY PRESS
182.0
"H20
POWER CYL 2L
2192J0
DEGF
INLET DIFF
3.0
"H20
POWER CYL 3L
2132.0
DEGF
DISCHARGE GAS
710.0
PSIG
POWER CYL 4L
twt.u
DEGF
VIBRATION
8.0
MLS
POWER CYL 5L
74.0
DEGF
FUEL VALVE OUTPUT
59.0
\
POWER CYL 1R
2132.0
DEGF
MONTHLYFIRED HOURS
3167
HRS
POWER CYL 2R
2192.0
DEGF
POWER CYL TRABON COUNT
2843.0
QTS
OflWED rv1 ?D
1 VIltr\ WIL fa
t4AOn
ilSL.U
DEGF
MP CYL THABO! COUNT
1084.0
QTS
POWER CYL 4R
won
I. itfl.V
ncftc
MbV 1
POWER CYl 24 HR. TOT
20.0
QTS
POWER CYL 5R
2192.0
DEGF
COUP CYL 24 HR. TOT
8.0
QTS
CRANKCASE COUNTS
0.0
QTS
1
3
5
7
9
11
13
15
1
TATIO IPRINT
F-178
-------
UNIT NO. 11
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPE1ED
283.8
RP«
LO INLET
135J0
DEGF
LUBE OIL PRESS
25.3
DCIP
roiu
LOOfllET
157.0
DEGF
LO FILTER DIFF
2.0
PSIG
J W INLET
m
DEGF
FUELDIFF
41.0
"H20
JW OUTLET
170.0
DEGF
FUEL STATIC
47.0
PSIG
FUEL GAS
63.S
nccc
vbv r
FUEL FLOW
13455.0
SCFHR
POWER CYL 1L
2192JI
DEGF
SCAVPRESS
181.0
"H20
POWER CYL 2L
2192.0
DEGF
INLET DIFF
3.0
"H20
POWER CYL 3L
2192.0
DEGF
DISCHARGE GAS
710.0
PSIG
POWER CYL 4L
2192.0
DEGF
VIBRATION
$.0
MILS
POWER CYL 5L
76,0
DEGF
FUEL VALVE OUTPUT
59.0
X
POWER CYL 1R
2192.0
DEGF
MONTHLY FIRED HOURS
3167
HRS
POWER CYL 2R
2192.0
DEGF
onwrowi tdidam rniiirr
runcnuiL innoun U/uni
qoi?n
Ml.ll
rtTO
mo
DAWCD WMD
i vntn wiLt/ii
2192.0
DEGF
COS? CYLTRABON COUNT
1084.0
QTS
POWER CYL 4R
2192.0
DEGF
POWER CYL 24 HR. TOT
20.0
QTS
POWER CYL 5R
2192.0
DEGF
COUP CYL 24 HR. TOT
8.0
QTS
CRANKCASE COUNTS
0.0
QTS
1
3
5
7
9
11
13
15
TATIOj
PRINT
F-179
-------
UNIT NO. 11
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
285J)
RPH
LO INLET
m
DEGF
LUBE OIL PRESS
25.0
PSIG
L O OUTLET
157 J)
DEGF
L 0 FILTER DIFF
2.0
PSIG
J W INLET
164.0
DEGF
FUEL DIFF
40.0
"H20
JW OUTLET
170 J)
DEGF
FUEL STOIC
47.0
PQIfc
1 VIV
CIICI CiQ
i vkh wnv
63 J2
nccc
VkV 1
FUEL FLOW
13415.0
SCFHR
POSER CYL 1L
-------
UNIT NO. 11
DESCRIPTION
VALUE
UNiTS
DESCRiPTiGN
VALUE
UNiTS
ENGINE SPEEiD
285.0
RPH
LO INLET
13SL0
DEGF
LUBE OIL PRESS
25.3
PSIG
LO OUTLET
157J6
DEGF
L 0 FILTER DUFF
2J)
PSIG
J W INLET
1W.0
DEGF
FUELDIFF
40.0
¦H20
JW OUTLET
17U.0
DEGF
FUEL STATIC
47.0
PSIG
FUEL GAS
£3 n
VV.tf
nccc
VkV 1
f EL FLOW
13441.0
SCFHR
POWER CYL 1L
2132.0
DEGF
SCAY PRESS
m
"H20
POWER CYL 2L
2192J)
DEGF
INLET DIFF
3.0
"H20
POWER CYL 3L
2192.0
DEGF
DISCHARGE GAS
710.0
PSIG
POWER CYL 4L
2192.0
DEGF
VIBRATION
7.0
MILS
POWER CYL 5L
77.0
DEGF
FUEL VALVE OUTPUT
59.0
*
POWER CYL 1R
2192 J)
DEGF
MONTHLY FIRED HOURS
3167
HRS
POWER CYL 2R
2192.0
DEGF
POWER CYLTRABON COUNT
-------
UNIT NO. 11
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
285.0
RPH
LO INLET
135.0
DEGF
LUBE OIL PRESS
2S.9
PSIG
LO OUTLET
157.0
DEGF
LO FILTER DIFF
2.0
PSIG
J W INLET
164.0
DEGF
FUEL OIFF
41.0
*HZ0
JW OUTLET
170 J)
DEGF
FUEL STATIC
47.0
PSIG
FUEL GAS
ma
W.U
nccc
WkV 1
FUEL FLOW
13462.0
SCFHR
POWER CYL 1L
4ii»n
ilOL.U
DEGF
SCAY PRESS
183.0
"H20
POWER CYL 2L
2192.0
DEGF
INLET DIFF
3.0
"H20
POWER CYL 3L
2192.0
DEGF
DISCHARGE GAS
711.0
PSIG
POWER CYL 4L
2182.0
DEGF
VIBRATION
100
MILS
POWER CYL a
74=0
DEGF
FUEL VALVE OUTPUT
59.0
*
POWER CYL 1R
2192.0
DEGF
KONTHLYFIRED HOURS
3167
h'RS
POWER CYL 2R
2192.0
DEGF
nnuucD rv\ TDionu ^aiiut
rumen ul i Known U/uni
-------
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
284.0
RPN
LO INLET
m
DEGF
LUBE OIL PRESS
25.0
PSIG
LO OUTLET
157 J)
DEGF
LO FILTER DIFF
2.0
PSIG
J W INLET
1(4.0
DEGF
FUEL DIFF
41.0
¦H20
JW OUTLET
170.0
DEGF
EIICI CTITir
ivkk vmiiv
Ml)
«i.V
PCIG
1 WlXi
EIIEI CM
1 vkk unv
Vh«V
nccc
VbV 1
FUEL FLOW
1S60.fi
SCFHR
POWER CYL 1L
21310
DEGF
SCAVPRESS
183 J)
"H20
POWER CYL 2L
2192.0
DEGF
INLET DIFF
3.0
"H20
POWER CYL 3L
2192.0
DEGF
DISCHARGE GAS
710.0
PSIG
POWERFUL
WMfl
DEGF
VIBRATION
y
MILS
POWER CYL 5L
760
DEGF
FUEL VALVE OUTPUT
59.0
*
POWER CYL 1R
2192.0
DEGF
MONTHLY FIRED HOURS
3168
HRS
POWER CYL 2R
2192.0
DEGF
POWER CYL TRABON COUNT
2843.0
QTS
POWER CYL 3R
2192.0
DEGF
COHP CYL TRABON COUNT
imp
QTS
POWER CYL 4R
MOD
L Itffa.U
nECC
WLV 1
POWER CYL 24 HR. TOT
20.0
QTS
POWER CYL 5R
2192.0
DEGF
COMP CYL 24 HRL TOT
M
QTS
CRANKCASE COUNTS
0.0
QTS
11MMM 1cn^n!
11/ivf«rr iv> W> LM j
, ...... ¦ , .—, .i
1
3
5
7
9
11
13
15
TATIO
PRINT
F-183
-------
UNIT NO. 11
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
286.0
RPM
LO INLET
134.0
DEGF
LUBE OIL PRESS
25.0
PSIG
LO OUTLET
157J)
DEGf
LO FILTER DIFF
2.0
PSIG
J W INLET
164.0
DEGF
FUEL DIFF
41.0
"H20
JW OUTLET
170JJ
DEGF
FUEL STATIC
47 J)
PSIG
FUEL GAS
Ufc«V
DEGF
FUEL FLOW
13470.0
SCFHR
POWER CYL 1L
2192.0
DEGF
SCAV PRESS
183.0
"H20
POWER CYL 2L
2192J)
DEGF
INLET DIFF
3.0
'H20
POWER CYL 3L
2192.0
DEGF
DISCHARGE GAS
710.0
OPir
row
POWER CYL 4L
ft
tist.u
DEGF
VIBRATION
SO
MILS
POWER CYL 51
75,0
DEGF
FUEL VALVE OUTPUT
59.0
*
POWER CYL 1R
2192.0
DEGF
MONTHLY FIRED HOURS
3168
HRS
POWER CYL 2R
2192.0
DEGF
POWER CYL TRABOH COUfiT
I—
car
POWER CYL 4R
MWft
i. 1 rt..U
nccc
UbW 1
POWER CYL 24 HR. TOT
20.0
QTS
POWER CYL 5R
2192,0
DEGF
COMP CYL 24 HR. TOT
8.0
QTS
CRANKCASE COUNTS
0.0
QTS
11/15/54
18:55:,fl
LV
F-184
1
3
5
7
9
11
1 3J1 5
TATiOj jPRJNT
-------
UNIT NO. 11
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEIED
232.0
RPH
LO INLET
135.0
DEGF
LUBE OIL PRIESS
2s.tr
PSIG
L O OUTLET
155 J)
DEGF
L 0 FILTER DIFF
2.0
PSIG
J W INLET
164.0
DEGF
FUEL DIFF
39.0
" H20
JW OUTLET
170.0
DEGF
FUEL STATIC
47 J!
PSIG
FUEL GAS
62J)
DEGF
FUEL FLOW
13177.0
SCFHR
POWER CYL 1L
tm
DEGF
SCAV PRESS
189.0
'H20
POWER CYL 2L
2192 J!
DEGF
INLET DIFF
3.9
"H20
POWER CYL 3L
2192.0
DEGF
DISCHARGE GAS
7111
PSIG
POWER CYL 41
2182.0
DEGF
VIBRATION
y
MILS
POWER CYL 5L
72J
DEGF
FUEL VALVE OUTPUT
59.0
%
POWER CYL 1R
2192.0
DEGF
MONTHLY FIRED HOURS
3168
HRS
POWER CYL 2R
2192.0
DEGF
POWER CYL TRABON COUNT
2843.0
QTS
POWER CYL 3R
2192.0
DEGF
COUP CYLTRABON COUNT
1084.0
QTS
POWER CYL 4R
2192.0
DEGF
POWER CYL 24 HR. TOT
20.0
QTS
POWER CYL 5R
2192.0
DEGF
COKP CYl 24 HR. TOT
8.0
QTS
CRANKCASE COUNTS
0.0
QTS
11/15/94
17:30:20
F-185
1
3
5 | 7
1
i
9
11
13
15
TATIO
PRINT
-------
UNIT NO. 11
DESCRIPTION
VALUE
UNiTS
DESCRIPTION
« f ¦ ¦
VALUt
UNIT;
ENGINE SPEED
293.0
RPM
LO INLET
135.0
DEGF
LUBE OIL PRESS
26.0
PSIG
LO OUTLET
1SS.0
DEGF
LO FILTER DIFF
2.0
PSIG
J W INLET
165.0
DEGF
FUEL DIFF
40.0
"H20
JW OUTLET
170.0
DEGF
FUEL STATIC
17 ft
VI .v
PQIC
1 VIV
nin cic
1 Vbb WW
5? n
MfaaV
nccc
VbW 1
FUEL FLOW
13304.0
SCFHR
POWER CYL 1L
2192.0
DEGF
SCAV PRESS
188.0
"H20
POWER CYL 2L
2192.0
DEGF
INLET DIFF
3.0
'H20
POWER CYL 3L
2192.0
DEGF
DISCHARGE GAS
711.0
PSIG
onuucD rvi ji
runtnuiLfL
<14MA
nr/»c
i/cti r
VIBRATION
7=0
MILS
POWER CYL 5L
71,0
DEGF
FUEL VALVE OUTPUT
53.0
*
POWER CYL 1R
2192.0
DEGF
MONTHLY FIRED HOURS
3168
HRS
POWER CYL 2R
2192.0
DEGF
POWER CYL TRABON COUNT
2843.8
QTS
POWER CYL 3R
niwn
tIM.W
DEGF
COBP CYLTKABON COUNT
1984.0
QTS
POWER CYL 4R
¦mma
4. IWk.U
ncgc
MbW 1
POWER CYL 24 JR. TOT
20.0
QTS
POWER CYL 5R
2192.0
DEGF
COUP CYL 24 HR. TOT
8.0
QTS
CRASKCASE COUNTS
0.0
nyc
11/1 MM I 47- U>%\
i if iviiTf J |;. 4V j
F-186
1
J
5
7 | 9 I"! 1
j j
13
15
TATJOI
l
PRINT
\
-------
UNIT NO. 11
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
293.0
RPM
LO INLET
135.0
DEGF
LUBE OIL PRESS
28.0
PSIG
LO OUTLET
156J)
DEGF
L 0 FILTER DIFF
2.0
PSIG
J W INLET
1M.0
DEGF
FUEL DIFF
W
"H20
JW OUTLET
170 J)
DEGF
FUEL STATIC
47J)
PSIG
FUEL GAS
S2.0
DEGF
FUEL FLOW
13215.0
SCFHR
POWER Cfl.1L
2132 J)
DEGF
SCAY PRESS
190.0
"H20
POWER CVL2L
2192J)
DEGF
INLET DIFF
3.0
"H20
POWER CYL3L
2192.0
DEGF
n|0/Hl»D/»C r«P
uldwvuiuc ww
144 n
I ll.tf
nem
roio
pnwro r*J) ii
Fuitcivulw.
MM It
i 131.11
ncr r
vcur
VIBRATION
m
MILS
POWER CM
71=0
DEGF
FUEL VALVE OUTPUT
58.0
I
POWER CYL1R
2192.0
DEGF
KOTO FIRED HOURS
316S
HRS
POWER CYL2R
2192.0
DEGF
POWER CYLTRABON COUNT
*>m
ftTO
mo
Dnuucorvi ad
1 VHLil VIL WR
wiwn
ncr t
ucu r
COSPCYLTRHBON COUNT
10810
QTS
POWERCYliR
k IWk.V
DEGF
POWER CYL2IHR. TOT
20.0
QTS
POWER CYL6R
2192.0
DEGF
COMPCYL24 HR. TOT
8.0
QTS
CRANKCASE COUNTS
0.0
QTS
11/15/94
17:40:19
F-187
1
l
O
J
5
7
€
n
-3
11
i
1
13 j 15
TATIOI
PRINT
-------
UNIT NO. 11
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNFFS
ENGINE SPEED
291.0
RPH
LO INLET
135.0
DEGF
LUBE OIL PRESS
2S.0
PSIG
LO OUTLET
156.0
DEGF
LO FILTER DIFF
2.0
PSIG
J W INLET
164.0
DEGF
FUEL DIFF
39.0
"H20
JW OUTLET
170.0
DEGF
FUEL STATIC
47A
Tl *V
PCIC
1 VIW
EIIEI MQ
1 Vkk WW
»n
Vfc.V
nccc
WkV 1
nJUELFLOW
13220.8
SCFHR
POWER CYL 1L
DEGF
SCAVPRESS
189.0
*H20
POWER CYL 2L
2132.0
DEGF
INLET DIFF
3.0
'H20
POWER CYL 3L
2192.0
DEGF
DISCHARGE GAS
712.0
PSIG
POWER CYL 4L
2192.0
DEGF
VIBRATION
6.0
US
POWER CYL §L
71.6
DEGF
FUEL VALVE OUTPUT
59.0
*
POWER CYL 1R
2192.0
DEGF
NONTHLY FIRED HOURS
3168
HRS
POWER CYL 2R
2192.0
DEGF
nnwwco wi tdidaii wiiiirr
ru*»tnwiL I(uuiuh^uuhi
2843.0
ATT
MIO
DAWCD ryt 3D
i vnun wlk «m
HMO
LiSL.U
DEGF
COWPCYLTRABOS COUNT
1084.0
QTS
POWER CYL 4R
2192.0
DEGF
POWER corn TOT
20.0
QTS
POWER CYL 5R
2192,0
DEGF
COWP CYL 24 HR. TOT
8.0
QTS
CRANKCASE COUffTS
0.0
QTS
11/15/94
17:45:19
F-188
1
o
c
-J
n
1
11 I10
i i j i j
I
-* crl
¦ U|
TATIO
PRINT
-------
UNIT NO. 11
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
291.0
RPM
LO INLET
135.0
DEGF
LUBE OIL PRESS
26.0
PSIG
LOOUTLET
156.0
DEGF
L 0 FILTH IIIFF
2.0
PSIG
J W INLET
165.0
DEGF
FUEL DIFF
40.0
¦H20
JW OUTLET
170.0
DEGF
FUEL STATIC
47J!
PSIG
FUEL GAS
SLft
nccc
VbW •
FUEL FLOW
13288.0
SCFHR
POWER CYL1L
2192.0
DEGF
SCAV PRESS
188.0
•H20
POWER CYL 2L
2192J)
DEGF
INLET DIFF
3.0
"H20
POWER CYL 3L
2192.0
DEGF
DISCHARGE GAS
712.0
PSIG
POWER CYL 4L
tmn
UOL.U
DEGF
VIBRATION
7.0
NILS
POWER CYL 5L
72.0
DEGF
FUEL VALVE OUTPUT
59.0
I
POWER CYL 1R
2192.0
DEGF
MONTHLY FIE1ED HOURS
3169
HRS
POWER CYL 2R
2192.0
DEGF
POWER CYLTRABON COUNT
2343.0
QTS
POWER CYL 3R
2192.0
DEGF
COUP CYLTfiABON COUNT
1084.0
QTS
POWER CYL 4R
2192.0
DEGF
POWER CYL 24 HR. TOT
20.0
QTS
POWER CYL 5R
2192.0
DEGF
COKP CYL 24 HR. TOT
8.0
QTS
CRANKCASE COUNTS
0.0
QTS
i
17:50:29
F-189
1
O
5
7
n
3
11
13
15
TATIOi
PRINT]
1
\
-------
UNIT NO. 11
DESCRIPTION
VALUE
UH'iTS
DESCRiPTiOii
VALUE
UiiiTS
ENGINE SPEED
291.0
m
LO ISLET
135.9
DEGF
LUBE OIL PRESS
- 26.0
PSIG
LO OUTLET
156.0
DEGF
LO FILTER DIFF
2.0
PSIG
J W INLET
164.0
DEGF
FUEL DIFF
40.0
'H20
JWOUIIET
170.0
DEGF
FUEL STATIC
47 J!
DCIC
1 VIW
CIIEI M5
1 Ukb W1V
62.0
DEGF
FUEL FLOW
13242.0
SCFHR
POWER CYL 1L
2192.0
DEGF
SCAV PRESS
189.0
"H20
POWER CYL 2L
2192.0
DEGF
INLET DIFF
3.0
"H20
POWER CYL 3L
M»ll
* IVtaiH
DEGF
DISCHARGED
712.0
PSIG
POWER CYL 4L
HIM ft
L13L.U
DEGF
ViBRATiOH
M
MILS
POWER CYL 51
74,0
DEGF
FUEL VALVE OUTPUT
59.0
*
POWER CYL 1R
2192.0
DEGF
MONTHLY FIRED HOURS
3169
HRS
POWER CYL 2R
2192.0
DEGF
POWER CYL TRABON COUNT
QTS
DMUCD rvi M
I V1IU\ VIL wn
niwn
tISL.U
DEGF
CQBPCYLTRABON COUNT
1084.0
QTS
POWER CYL 4R
2192.0
DEGF
POWER CYL 24 HR. TOT
20.0
QTS
POWER CYL 5R
2192.0
DEGF
COUP CYL 24 HRL TOT
8.0
QTS
CRANKCASE COUNTS
0.0
QTS
! iihj;/w M7. K.oni
i i 1) iV/«n I 1 /. Vv>. iV
! ! i
F-190
•
1 O F
1 J D
1 i
7 fl
/ 3
11
13
15
1
TATIoj
print!
-------
UNIT NO. 11
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
292.0
RPM
LO INLET
134.0
DEGF
LUBE OIL PRESS
2S.0
PSIG
LOOUTLET
155.11
DEGF
L 0 FILTER DF:F
2.0
PSIG
J W INLET
164.0
DEGF
FUEL DIFF
40.0
"H20
JWOUTLET
170.0
DEGF
FUEL STATIC
47J)
PSIG
FUEL GAS
62.0
DEGF
FUELFLOW
13247.0
SCFHR
POWER CYL 1L
2192.0
DEGF
SCAV PRESS
190.0
"H20
POWER CYL 2L
2192.0
DEGF
INLET DIFF
3.0
"H20
POWER CYL 3L
2192.0
DEGF
ulowvvvut mo
74i n
1 li.U
noir
roiu
POWER CYL 4L
«n
tirn.u
ATf
W10
DfflKD rvI ID
i wik vn
i 134.11
DEGF
rnao rvi tpjidau rnnwT
VWMO Wlk iivtwvn WVVill
imun
IUW1.U
rvrc
M 1 V
POWER CYL 4R
wmii
4. Itffa.U
nccc
VbV 1
POWER CYL 24 HR. TOT
20.0
QTS
POWER CYL SR
2192,0
DEGF
COUP COHR. TOT
8.0
QTS
CRANKCASE COUNTS
0.0
QTS
1
3
1
P 1 7
b | /
i
n
j
11
13
15
TATIO
PRINT
F-191
-------
UNIT NO. 11
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
294.0
RPS
LO INLET
134.0
DEGF
LUBE OIL PRESS
2S.0
PSIG
LO OUTLET
-------
UNIT NO. 11
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
292.0
RPM
LO INLET
134 J)
DEGF
LUBE OIL PRESS
26.0
PSIG
LO OUTLET
M
DEGF
LO FILTER DIFI:
2.0
PSIG
J W INLET
164.0
DEGF
FUEL DIFF
to
*H20
JW OUTLET
ITOjO
DEGF
FUEL STATIC
47 J!
PSIG
FUEL GAS
62.0
DEGF
FUEL FLOW
13258.0
SCFHR
POWER CYL 1L
2152.0
DEGF
SCAVPRESS
190.0
'H20
POWER CYL 2L
2192 J)
DEGF
INLET DIFF
3.0
"H20
POWER CYL 3L
2192.9
DEGF
DISCHARGE GAS
712.0
PSIG
uauicd m/i ii
runcnuLn
mm a
IIU..U
ncr c
l/cor
VIBRATION
6,0
MILS
POWER CYL 5L
71,0
DEGF
FUEL VALVE OlFTPUT
59.0
*
POWER CYL 1R
2192.0
DEGF
MONTHLY FIRED HOURS
3169
HRS
POWER CYL 2R
2192.0
DEGF
POWER CYL MS COUNT
-------
UNIT NO. 11
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
291.0
RPM
LO INLET
m
DEGF
LUBE OIL PRESS
26.0
PSIG
10 OUTLET
155.0
DEGF
LO FILTER OIFF
2.0
PSIG
J W INLET
164.0
DEGF
FUEL DIFF
39.0
"H20
jwotrriET
170.0
DEGF
FUEL STATIC
47 A
11 .w
pcic
1 VIV
pici ««
i ubu wnv
MA
m.v
nccc
IfbW 1
FUEL FLOW
13215.0
SCFHR
POWER CYL1L
21S2.0
DEGF
SCAV PRESS
190.0
"H20
POWER CYL2L
2192.0
DEGF
INLET DIFF
3.0
"H20
POWER CYL3L
2192.0
DEGF
DISCHARGE GAS
1 It.U
ooir
roiu
nnwFD rvi ji
runtrvuinL
14MD
tIJi.U
ncrc
ucor
VIBRATION
5,0
MILS
POWER CYL5L
710
DEGF
FUEL VALVE OUTPUT
59.0
*
POWER CYL1R
2192.0
DEGF
MONTHLY FIRED HOURS
3169
HRS
POWER CYL2R
2192.0
DEGF
POWER CYLTRABOS COUNT
2843.0
QTS
POWER CYL3R
2182.0
DEGF
CQMPCYLTRABON COUNT
1084.0
QTS
POWER CYL4R
2192.0
DEGF
POWER CYL 24 HR. TOT
20.0
QTS
POWER CYL5R
2192.0
DEGF
COKPCYL24HR.TOT
8.0
QTS
CRANXCASE COUNTS
0.0
QTS
11/15/84
18:15:20
F-194
1 1 1 1
| 1 3 I 5 I 7
1
S
13
15
TATIoj
PRINT
-------
UNIT NO. 11
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
291.0
RPM
LO INLET
134J)
DEGF
LUBE OIL PRE SS
26.0
PSIG
LO OUTLET
155.0
DEGF
LO FILTER Dlf:F
2J)
PSIG
J W INLET
164 J)
DEGF
FUEL DIFF
40.0
"H20
JW OUTLET
178J)
DEGF
FUEL STATIC
4? J)
PSIG
FUEL GAS
61.0
DEGF
tJJELFLOW
13235.0
SCFHR
POWER CYL 1L
2192.0
DEGF
SCAV PRESS
189.0
¦K20
POWER CYL 2L
2192J)
DEGF
1MLET DIFF
3.0
"H20
POWER CYL 3L
2192.0
DEGF
DISCHARGE GAS
712.0
PSIG
oniucD rvi ii
rvnca
2182.0
nc/»c
i/cur
VIBRATION
y
MILS
POWER CYL 51
70,0
DEGF
FUEL VALVE OITPUT
59.0
*
POWER CYL 1R
2192.0
DEGF
MONTHLY FIRE D HOURS
3169
HRS
POWER CYL 2R
2192.0
DEGF
POWER CYL TRABON COUNT
2843.0
ATT
UIO
DAIKD rv1 W
i viikn vikim
1IJL.U
DEGF
COMP CYL TRABON COUNT
-------
UNIT NO. 11
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
298.0
RPM
LO INLET
134 Jl
DEGF
LUBE OIL PRESS
27.0
PSIG
LO OUTLET
155J)
DEGF
LO FILTER DIFF
2.0
PSIG
J W INLET
164.0
DEGF
FUEL DIFF
41.0
-H20
JW OUTLET
170.0
DEGF
FUEL STATIC
18 ft
IViV
PCIC
1 vlw
ciici r.ta
1 Vbk WW
Mil
VI «v
ncr.c
VhV 1
FUEL FLOW
13682.0
SCFHR
POWER CYL 1L
2132.0
DEGF
SCAY PRESS
201.0
¦H20
POWER CYL 2L
2132.0
DEGF
INLET DIFF
3.0
'H20
POWER CYL 3L
2192.0
DEGF
DISCHARGE GAS
713.0
PSIG
POWER CYL 4L
AIJ1.U
DEGF
VIBRATION
7.0
MILS
POWER CYL 51
71,0
DEGF
FUEL VALVE OUTPUT
60.0
*
POWER CYL 1R
2192.0
DEGF
MONTHLY FIRED HOURS
3169
HRS
POWER CYL 2R
21S2.0
DEGF
nnu/CD rvi wionu rnntrr
runcn wiL innoun uuum
OOJOrt
ftTP
DAIMCD rvi W
wn
ncf»c
tPU.U
410
i vnui \#il vn
L1 JL.U
ucvj r
rnuo rvi tparqu rnu^T
vvm wiL iitrwvn vvuni
1084.0
ATC
y i v
POWER CYL 4R
WMII
falWk.U
ncf; c
UkW 1
POWER CYL 24 HR. TOT
20.0
QTS
POWER CYL 5R
2192.0
DEGF
COUP CYL 24 HR. TOT
8.0
QTS
CRANKCASE COUNTS
0.0
QTS
11/15/94
18:25:10!
F-196
1
3
5
7
9
11
13
15
TATJOi
PRINT
-------
UNIT NO. 13
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
349.0
RPM
LOINLET
139.0
DEGF
LUBE OIL PRESS
37.0
PStG
LO OUTLET
164.0
OEGF
LO FILTER DIFF
1.0
PS)G
J W INLET
164.0
DEGF v
FUEL OFF
M.O
"H20
JW OUTLET
173.0
DEGF '
FUEL STATIC
63.0
PStG
FUEL GAS
70 JJ
DEGF
Fua FLOW
27417.0
SCFHR
POWER CYL 1L
648.0
DEGF
SCAV PRESS
192.0
"H»
POWER CYL 2L
696.0
DEGF
INLET DOT
4J3
-H20
POWER CYL 3L
658.0
DEGF
DISCHARGE GAS
714.0
PStG
POWER CYL 4L
717.0
DEGF
VIBRATION
M.O
MILS
POWER CYL 3L
A
CEGF
FUEL VALVE OUTPUT
>1.0
%
POWER CYL 1R
682.0
DEGF
MONTHLY FIRED HOURS
1S41
MRS
POWER CYL 2R
737.0
DEGF
POWER CYL TRAGON COUNT
2674.0
QTS
POWER CYL 3R
638.0
DEGF
COMP CYL TRABCN COUNT
962.0
QTS
POWER CYL 4R
885.0
DEGF
POWER CYL 24 HR. TOT
45.0
QTS
POWER CYL 5R
6S3.0
DEGF
COMP CYL 24 HR. TOT
1S.0
QTS
CRANKCASE COUNTS
0.0
QTS
11/14/94
10: 31:58
1
3
5
7
9
11
13
15
STATION
PRINT
F-197
-------
UNIT NO. 13
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
(MTTS
ENGWE SPEED
RPM
LO INLET
1S9.0
D€G F
UIBE OIL PRESS
VJt
PSIG
LO OUTLET
1H.0
DEG F
LO FILTER OFF
u
PSIG
J W INLET
1MJ
DEGF
FUEL OFF
88.0
"H20
JW OUTLET
IRI
DEO F
FUEL STATIC
(U
PSIG
FIELGAS
mo
DEGF
Fua FLOW
27679.0
SCFHR
POWER CYL 1L
ma
DEGF
SCAV PRESS
1».0
"H20
POWER ClfL 2L
C$6.0
DEGF
INLET DIFF
4.0
•H20
POWER CYL SI
•60.0
DEGF
DISCHARGE GAS
744.0
PSIG
POWER CYL 4L
71L0
DEGF
VIBRATION
310
MILS
power c\t sl
6S4.0
DEQF
FUa VALVE OUTPUT
•0.0
%
POWER CYL 1R
teij
DEGF
MONTHLY FIRED HOURS
1841
HRS
POWER CYL 2R
736.0
DEGF
POWER CYL TRABON COUNT
QTS
POWER CYL SR
6384!
DEGF
COUP CYL TRABON COUNT
882.0
QTS
POWER CY14R
W* n
DEGF
POWER CYL a HR. TOT
45.0
QTS
POWER CYL IR
65SJ
DEGF
COMP CYL 24 HR. TOT
18.0
QTS
CRANKCASE COUNTS
0.0
QTS
11/14/94
10: 38:05
' 1
1 I 3
5 I 7 i 9 I ii
13 ] 15
STATION
PRINT
F-198
-------
UNIT NO. 13
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
248.0
RPM
LO INLET
139.0
OEOF
LUBE OIL PRESS'
374
PSIG
LO OUTLET
164.0
DEOF
LO FILTER DtFF
1.0
PSIG
J W INLET
1644
OEBF
FUELDIFF
684
"H20
JW OUTLET
1710
DEOF
FUEL STATIC
844
PSIG
FUEL GAS
704
DEC F
FUEL FLOW
zm&o
SCFHR
POWER CYL 1L
OEBF
SCAV PRESS
192.0
" H20
POWER CYL 2L
•M.0
DEOF
INLET DIFF
44
"H20
POWER CYL JL
8884
OEOF
DISCHARGE GAS
7144
PSIG
POWER CYL 4L
T20X
DEOF
VIBRATION
34.0
MILS
POWER CYL 9L
tux
DEOF
FUEL VALVE OUTPUT
80.0
%
POWER CYL 1R
8844
DEGF
MONTHLY FIRED HOURS
1S41
HRS
POWER CYL 2R
7394
OEGF
POWER CYL TRABON COUNT
28744
QTS
POWER CYL 3R
8394
DEGF
COMP CYL TRABON COUNT
962.0
QTS
POWER CYL 4R
8874
OEGF
POWER CYL 24 HR. TOT
45.0
QTS
POWER CYL 5R
mo
DEGF
COMP CYL 24 HR TOT
16.0
QTS
CRANKCASE COUNTS
0.0
QTS
11/14/94
10: 41:03
1
3
5!7
i
9 I 11
13
15
STATION
PRINT
F-199
-------
UNIT NO. 13
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UMTS
ENGINE SKED
291.0
RFM
L OWLET
139.0
DEGF
LUBE OU. PRESS
I7J
PSiG
lOOUTLET
164.0
DEGF
LOFH.TERKFF
iJ>
PStG
J W INLET
114J
DEGF
FUELDiFF
9M
"MB
JW OUTLET
172J
OEOF
FUEL STATIC
44 J)
PSIG
FUEL GAS
1U
DEGF
FUaFlOW
mm
SCFHR
POWER CYl 11
SS2JB
DEGF
SCAV PRESS
"HSO
POWER CYL 2L
m.o
DEC F
INLET DIFF
4 J)
"H20
POWER CYl Si.
CS&0
DEGF
DISCHARGE GAS
7«J
PStG
POWER CYL 4L
721 Jt
DEGF
VIBRATION
SSJS
MILS
POSER CYl 3L
6S4.fi
OEOF
FUEL VALVE OUTPUT
KJS
*
POWER CYL 1R
184 A
DEGF
MONTHLY FIRED HOURS
1841
HRS
POWER CYL 2R
737.0
DEGF
POWER CYl UtABON COUNT
25744
QTS
POWER CYL 3R
$Sgjj
DEGF
COMP CYl TRABON COUNT
962.0
GTS
POWER CYl 4R
SUA
DEGF
POWER CYl 24 HR. TOT
45.0
QTS
TOWER CYl 5R
U8A
DEGF
COMP CYl 24 HR. TOT
1S.0
QTS
CRANKCASECOUNTS
0.0
QTS
11/14/94
10:46:13
1
3
5
i
7 9
11
r—T
13 | 15
STATION
PR1WT
F-200
-------
UNIT NO. 13
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNfTS
ENGINE SPEED
2SOO
RPM
LO INLET
13M
DEGF
LUBE OIL PRESS
S7X
PSKJ
LOOUTLET
154.0
DEGF
LO FILTER DIFF
10)
PSIG
J W INLET
1S10
DEGF
FUEL OFF
884)
"H20
JW OUTLET
172.0
DEGF
FUEL STATIC
MJ)
PSIG
FUEL GAS
71.0
DEGF
FUEL FLOW
2742M
SCFHR
POWER CYL 1L
661X
DEGF
SCAV PRESS
m.o
" H20
POWER CYL 2L
WS.O
DEGF
INLET DIFF
4.0
*H20
POWER CYL 1L
CS8U)
DEGF
DISCHARGE GAS
714.0
PS»
POWER CYL 4L
719.0
DEGF
VIBRATION
3&0
MILS
POWER CYL SL
6SS.G
BEOF
FUEL VALVE OUTPUT
800
%
POWER CYL 1R
683.0
DEGF
MONTHLY FIRED HOURS
1S42
HRS
POWER CYL 2R
737.0
DEGF
POWER CYL TRWON COUNT
2S74.0
OTS
POWER CYL SR
638.0
DEGF
COMP CYL TRAI30N COUNT
982.0
OTS
POWER CYL 4R
892.0
OEGF
POWER CYL 24 HR. TOT
45.0
OTS
POWER CYLJR
657.0
DEGF
COMP CYL 24 HIR. TOT
16.0
QTS
CRANKCASE COUNTS
0.0
QTS
11/14/94 10:52:43
• ¦ ¦
1
3
I I
5!7 i9
n
i
13 ! 15
i
STATION I
I
PRINT
F-201
-------
UNIT NO. 13
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
251.0
RPM
LO INLET
139.0
DEGF
LUBE (XL PRESS
37J
PSIG
LOOUTLET
164.0
OEGF
LO FILTER DIFF
1.0
PSJG
J W INLET
1SJ.C
DEGF
FUEL OFF
S6.0
"H20
JW OUTLET
172.0
DEGF
FUEL STATIC
64.0
PSIG
FUEL GAS
71 JO
DEGF
FUEL FLOW
275210
SCFHR
POWER CYL 1L
tUA
DEGF
SCAV PRESS
192.0
"H20
POWER CYL 2L
698.0
DEGF
INLET DIFF
44)
-H20
POWER CYL 3L
659.0
DEGF
DISCHARGE GAS
713.0
PSIG
POWER CYL 4L
718.0
DEGF
VIBRATION
36.0
MILS
POWER CYL 5L
653.0
OEGF
FH^L VALVE OUTPUT
80.0
%
POWER CYL 1R
C81.0
DEGF
MONTHLY FIRED HOURS
1542
HRS
POWER CYL 2R
741.0
DEGF
POWER CYL TRABON COUNT
2574.0
QTS
POWER CY11R
639.0
DEGF
COMP CYL TRABON COUNT
- 962.0
QTS
POWER CYL 4R
886.0
DEGF
POWER CYL 24 HR. TOT
4S.0
QTS
POWER CYL 9R
SS0.0
DEGF
COMP CYL 24 HR. TOT
16.0
QTS
CRANKCASECOUNTS
0.0
QTS
11/14/94
10:55:36
1 j 3
i
5
1 1
7 j 9 | 11
I i
13
15
STATION |
PRINT
F-202
-------
UNIT NO. 13
DESCRIPTOR
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
249.0
RPM
LO INLET
138.0
DEGF
LUBE OIL PRESS
37.0
PSIG
LOOUTLET
15U
0EGF
L 0 FILTER HFF
1.0
PSIG
J W INLET
166.0
DEGF
FUELNFF
$6.0
" H20
JW OUTLET
174.0
DEOF
FUEL STATIC
64.0
PSIG
FUEL GAS
710
DEGF
FUEL FLOW
27520.0
SCFHR
POWER CYL 1L
648.0
DEGF
SCAV PRESS
190.0
"H20
POWER CYL 2L
mo
DEGF
INLET DIFF
4.0
*H20
POWER CYL 3L
658.0
DEGF
DISCHARGE OAS
714.0
PSIG
POWER CYL 4L
718.0
DEGF
VIBRATION
34.0
MILS
POWER CYL SL
SS5.3
BSGF
FUEL VALVE OU1PUT
80.0
%
POWER CYL 1R
683.0
DEGF
MONTHLY FIRED HOURS
1542
HRS
POWER CYL 2R
738.0
DEGF
POWER CYL TRAI30N COUNT
2574.0
QTS
POWER CYL 3R
S33.0
DEGF
COMP CYL TRABON COUNT
982.0
QTS
POWER CYL 4R
886.0
OEGF
POWER CYL 24 Hit TOT
4S.0
QTS
POWER CYL 5R
6S7M
DtGF
COMP CYL 24 HR. TOT
1S.0
QTS
CRANKCASE COUNTS
0.0
QTS
11/14/94
11:18:58
1
—
3
5
7
9 | 11
i
13
15
STATION
| PRINT
1
F-203
-------
UNIT NO. 13
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
2S1.0
RPM
L O INLET
137.0
DEGF
LUBE OIL PRESS
37.0
PSIG
LO OUTLET
157.0
DEGF
L 0 FILTER DIFF
1.0
PSIG
J W INLET
i «.o
DEGF
FUEL WFF
S8.0
"H20
JW OUTLET
173.0
DEGF
FUEL STATIC
64.0
PSIG
FUEL GAS
64.0
DEGF
Fua FLOW
27549.0
SCFHR
POWER CYL 1L
S51.0
DEGF
SCAV PRESS
191.0
-H20
POWER CYL 2L
696.0
DEG F
INLET DIFF
4.0
-H20
POWER CYL 3L
660.0
DEGF
DISCHARGE GAS
713.0
PSIG
POWER CYL 4L
717.0
DEO f
VIBRATION
30.0
MILS
POWER CYL 5L
6SS.0
DEG F
FUEL VALVE OUTPUT
80.0
%
POWER CYL 1R
684.0
DEGF
MONTHLY FIRED HOURS
3139
HRS
POWER CYL 2R
738.0
DEGF
POWER CYL TRABON COUNT
2803.0
QTS
POWER CYL 3R
639.0
DEGF
COMP CYL TRABON COUNT
1069.0
GTS
POWER CYL 4R
890.0
DEGF
POWER CYL 24 HR. TOT
1S.0
QTS
POWER CYL 5R
SSO.O
DEGF
COMP CYL 24 HR. TOT
7.0
QTS
CRANKCASE COUNTS
0.0
QTS
[~~ 11/14/94
11: 32:38
I I
II I3
5
i
7 ! 9
i
11
1 "
13 j 15
I STATION I
PRINT
jj
F-204
-------
UNIT NO. 13
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
231.0
RPM
L O INLET
134.0
DEGF
LUBE OIL PRESS
36.0
PSJG
LOOUTLET
149.0
DEC F
LO FILTER DIFF
1.0
PSIG
J W INLET
too
DEGF
FUEL DIFF
49.0
"H20
JW OUTLET
172.0
DEGF
FUa STATIC
MX
PSIG
FUEL GAS
74 J)
DEGF
FUEL FLOW
2S2884
SCFHR
POWER CYL 1L
cs&o
DEGF
SCAV PRESS
1K.0
-H20
POWER CYL 2L
702.0
DEGF
INLET DIFF
10
*H20
POWER CYL 3L
K4.0
DEGF
OISCHARGE GAS
711.0
PSIG
POWER CYL 4L
718.0
DEGF
VIBRATION
39.0
MILS
POWER CYL SL
653.0
DEGF
.FUEL VALVE OUTPUT
73.0
%
POWER CYL 1R
$86.0
DEGF
MONTHLY FIRED HOURS
1546
HRS
POWER CYL 2R
745.0
DEGF
POWER CYL TRABON COUNT
2574.0
QTS
POWER CYLSR
DEGF
COMPCYLTRAEON COUNT
982.0
QTS
POWER CYL 4R
868.0
DEGF
POWER CYL 2t MR. TOT
45.0
QTS
POWER CYLSR
S49.0
DEGr
COMP CYL 24 HR. TOT
16.0
QTS
CRANKCASE COUNTS
0.0
QTS
11/14/94
14:51:00
1
3
5
cn
i i
13 j 15 |
i 1
STATION
! PRINT !
1 t
F-205
-------
UNIT NO. 13
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
mo
RPM
LO INLET
1J4.0
DEGF
LUBE OIL PRESS
J5J3
PStG
LOOUTLET
149.0
DEGF
IORLTERWFF
i Ja
PS)G
J W INLET
1S3.0
DEG F
FUEL DIFF
49
"H20
JW OUTLET
172J
DEGF
FUEL STATIC
64.0
PSIG
FUEL GAS
74.0
DEGF
FUEL FLOW
25226.0
SCFHR
POWER CYL 1L
C62J
DEG F
SCAV PRESS
1S4.0
"H20
POWER CYL 2L
702.0
DEGF
INLET DIFF
3J>
" H20
POWER CYL 3L
fitS.O
DEGF
DISCHARGE GAS
712.0
PSIG
POWER CYL 4L
718.0
DEGF
VIBRATION
2S.0
MILS
POWER CYL 5L
654.0
DEOF
FUEL Y^LVE OUTPUT
73.0
%
POWER CYL 1R
<88.0
DEGF
MONTHLY FIRED HOURS
154fi
HRS
POWER CYL 2R
742.0
DEGF
POWER CYL TRABON COUNT
2674.0
QTS
POWER CYL JR
DEGF
COMP CYL TRABON COUNT
982.0
QTS
POWER CYL 4R
877.0
DEGF
POWER CYL 24 HR. TOT
45.0
QTS
POWER CYL 5S
C43U3
DEGF
COMP CYL 24 HR. TOT
16.0
QTS
CRANKCASE COUNTS
0.0
QTS
11/14/94
15:00:20!
I I I
1 ! 3 I 5 I 7
i i i
9
11
I
13 i 15
i
STATION | j PFUNT
1 1
F-206
-------
UNIT NO. 13
DESCRIPTION
VALUE
UNtTS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
228.0
RPM
LO INLET
133.0
DEOF
LUBE OIL PRESS
36.0
PStG
LO OUTLET
149.0
DEGF
L 0 FILTER DIFF
1.0
PSiG
JWBB.ET
1SJ.0
DEGF
FUEL DIFF
49.0
"H20
JW OUTLET
1710
DEGF
FUEL STATIC
M.0
PSIG
FUEL GAS
74.0
DEGF
FUEL FLOW
25294.0
SCFHR
POWER CYL 1L
(S&0
DEGF
SCAV PRESS
1S6.0
•H20
POWER CYL 2L
703.0
DEGF
INLET DIFF
3.0
"H20
POWER CYL 3L
ttn
DEGF
DISCHARGE OAS
712.0
PSIG
POWER CYL 4L
7184
DEGF
VIBRATION
34.0
MILS
POWER CYL 5L
652.0
DEGF
FUEL VALVE OUTPUT
74.0
%
POWER CYL 1R
686.0
DEGF
MONTHLY FIRED HOURS
t&46
HRS
POWER CYL 2R
741.0
DEGF
POWER CYL TRAIBON COUNT
2S74.0
QTS
POWER CYL 3R
f|MHi
DEGF
COMP CYL TRABON COUNT
982.0
QTS
POWER CYL 4R
874.0
DEGF
POWER CYL 24 H!R. TOT
45.0
QTS
POWER CYL 5R
647.0
DEC r
COMP CYL 24 HR. TOT
16.0
QTS
CRANKCASE COUNTS
0.0
QTS
r 11/14/94
15:13:09
ii
3 5 7
STATION
11
13 ! 15
PRINT
F-207
-------
UNIT NO. 13
DESCRIPTION
VALUE UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
231X RPM
LO INLET
134.0
DEGF
LUBE OIL PRESS
35X PSIG
LOOUTLET
149.0
DEGF
L 0 FILTER DtFF
1J> PSIG
JW INLET
1&0
DEGF
FUEL DIFF
4»JB *H20
JW OUTLET
172.0
DEGF
FUEL STATIC
MX PSIG
FUEL GAS
74 A
DEGF
FUEL FLOW
26214.0 SCFHR
POWER CYL 1L
<66.0
DEGF
SCAV PRESS
1S6.0 "H20
POWER CYL 2L
703.0
DEGF
INLET DIFF
3.0 " H20
POWER CYL 3L
6SS.0
DEGF
DISCHARGE GAS
712.0 PSIG
POWER CYL 4L
719.0
DEGF
VIBRATION
33.0 MILS
POWER CYL 5L
654.0
DEO F
FUa VALVE OUTPUT
73 JO %
POWER CYL 1R
686.0
DEGF
MONTHLY BRED HOURS
1546 HRS
POWER CYL 2R
742.0
DEGF
POWER CYL TRABON COUNT
2574.0 QTS
POWER CYL 4ft
636.0
DEGF
COMP CYL TRABON COUNT
962.0 QTS
POWER CYL 4R
871.0
DEGF
POWER CYL 24 HR. TOT
45.0 QTS
POWER CYL 5R
649.0
DEGF
COMP CYL 24 HR. TOT
CRAHKCASECOUNTS
1S.0
0.0
QTS
QTS
11/14/94 15:15:26!
1 i 3
i
i 1
5 i 7 1 9 111
i 1
13 j 15
j STATION
PRINT
F-208
-------
UNIT NO. 13
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
230.0
RPM
L OWLET
133.0
DEGF
LUBE OIL PRESS
3&J)
PS1G
LOOUTLET
149.0
DEGF
XO FILTER DIFIF
U)
PSIG
JW INLET
163.0
DEGF
FUaDIFF
49J)
"H20
JW OUTLET
1724
DEGF
FUEL STATIC
S4.0
PSIG
FUEL GAS
74.0
DEGF
FUEL FLOW
25189.0
SCFHR
POWER CYL 1L
6SS.0
DEGF
SCAV PRESS
1SC.0
"H20
POWER CYL 2L
791.0
DEGF
MLETDIFF
10
"H20
POWER CYL SL
665.0
DEGF
DISCHARGE G4S
712.0
PSIG
POWER CYL 4L
720.0
OCG F
VIBRATION
310
MILS
POWER CYL JL
SS3.S
DEO F
^EL VALVE OUTPUT
74.0
%
POWER CYL 1R
686.0
DEGF
MONTHLY FIRED HOURS
1S4S
HRS
POWER CYL 2R
741.0
DEGF
POWER CYl TR&BON COUNT
2574.0
QTS
POWER CYL SR
635.0
DEGF
COMP CYL TRA130N COUNT
982.0
QTS
POWER CYL 4R
876.0
DEGF
POWER CYL 24 HR. TOT
45.0
QTS
POWER CYL SR
646.0
DEGF
COMP CYL 24 HR. TOT
1S.0
QTS
CRANKCASECOUNTS
0.0
QTS
r 11/14/94] 15:20:10;
! . i
Mi 13! 5 i ?; 91 n ! n 115! i
11 1 1—1—1—i—i—i 11
I ; STATION j J PRINT j j
• I I =J
F-209
\
-------
UNIT NO. 13
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
230.0
RPM
L 0 INLET
134.0
DEGF
LUBE OIL PRESS
3S.0
PSIG
LO OUTLET
149.0
DEGF
LO FILTER DiFF
1.0
PSiG
1 uI nil rr
J «« IrtuC i
10.0
DEGF
FUa DIFF
49.0
" H20
JW OUTLET
172.0
DEGF
FUEL STATIC
64.0
PSIG
FUEL GAS
74.0
DEGF
fuel FLOW
2S191.0
SCFHR
POWER CYI1L
<56.0
DEGF
SCAV PRESS
156.0
"H20
POWER CYL 2L
700.0
DEGF
INLET DIFF
3.0
" H23
POWER CYL 3L
665.0
DEGF
DISCHARGE GAS
712.0
PS!G
POWER CYL 4L
718.0
DEGF
VIBRATION
48.0
MiLS
POWER CYL SL
652.0
OEGF
FUEL VALVE OUTPUT
73.0
%
POWER CYL 1R
687.0
DEGF
MONTHLY FIRED HOURS
1547
HRS
POWER CYL 2R
745.0
DEGF
POWER CYL TRABON COUNT
2574.0
QTS
POWER CYL 3R
633.0
DEGF
COMP CYL TRA80M COUNT
982.0
CTS
POWER CYL 4R
873.0
DEGF
POWER CYL 24 HR. TOT
45.0
QTS
POWER CYL 5R
648.0
DEGF
COMP CYL 24 HR. TOT
16.C
QTS
CRANKCASE COUNTS
0.0
OTS
! 11/14/94? 15:50:51:
, I .
I I l i i 1 1 i
; station ; ; phjnt ;
F-210
-------
DESCRIPTION
VALUE
ENGINE SPEED
230.0
LUBE OIL PRESS
35.0
L 0 FILTER DIFF
1.0
FUEL DIFF
49J>
FUa STATIC
64.0
FOaFLOW
25208.0
SCAV PRESS
156.0
INLET DIFF
3.0
DISCHARGE CAS
712.0
VIBRATION
38.0
FUEL VALVE OUTPUT
73.0
MONTHLY FIRED HOURS
1S4S
POWER CYL TRABDN COUNT
2S74.0
COMP CYL TRABOM COUNT
982.0
POWER CYL 24 HR. TOT
43.0
COMP CYL 24 HR. TOT
16.0
CRANKCASE COUNTS
0.0
i 11/14/Mj 1& 30:45'
UNIT NO. 13
UNITS
DESCRIPTION
VALUE
UNITS
RPM
LO INLET
134.0
DEGF
PSIG
LO OUTLET
149.0
DEGF
PSIG
JW INLET
1C.C
DEGF
"H20
JW OUTLET
172.0
DEGF
PSIG
FUEL GAS
74.0
DEGF
SCFHR
POWER CYL 1L
664.0
DEGF
"H20
POWER CYL 2L
703.0
DEGF
"H20
POWER CYL 3L
E69.0
DEGF
PSIG
POWER CYL 4L
718.0
DEGF
MILS
POWER CYL 5L
$33.0
r\cri e
UU
-------
DESCRIPTION
ENGINE SPEED
LUBE OIL PRESS
I OBITER WFF-
FUa DIFF
FUEL STATIC
FUEL FLOW
SCAV PRESS
INLET DIFF
DISCHARGE GAS
VIBRATION
FUa VALVE OUTPUT
MONTHLY FIRES HOURS
POWER CYL TRABON COUNT
COMP CYL TRABON COUNT
POWER CYL 24 HR. TOT
COMP CYL 24 HR. TOT
CRANKCASE COUNTS
j 11/14/94f~15:45:
UNIT NO. 13
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
229.0
RPM
LO INLET
134.0
DEG F
35.0
PSIG
L O OUTLET
149.0
DEGF
1.0
PS4G
J W INLET
1C3.0
DEG F
49.0
"H20
JW OUTLET
172.0
DEGF
64.0
PSIG
FUEL GAS
74.0
DEGF
2S241.0
SCFHR
POWER CYL 1L
656.0
DEGF
15S.0
- H20
POWER CYL 2L
S39J)
DEG F
3.0
"H20
POWER CYL 3L
664.0
DEGF
712.0
PS!G
POWER CYL 4L
717.0
DEGF
36.0
MILS
POWER CYL 5L
654.0
DEGF
71.0
%
POWER CYL 1R
687.0
DEGF
1546
HRS
POWER CYL 2R
744.0
DEGF
2574.0
QTS
POWER CYL 3R
633.0
DEGF
382.0
OTS
POWER CYL 4R
876.0
DEGF
45.0
OTS
OQbycp CO
630.0
RcG r
16.5
QTS
CO
QTS
I
! 1 i 3 I 6
1 \
i , , ' i
9 1 11 1 13 ! lb ! !
: , I i
| STATION J
| PRINT j j
F-212
\
-------
UNIT NO. 13
DESCRIPTION!
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
229.0
RPM
LO INLET
134.0
DEGF
LUBE OIL PRESS
3S.0
PSIG
L O OUTLET
149.0
DEGF
10 FILTER DtFF
1.0
PSIG
J W INLET
1S3.0
DEGF
FUEL DiFh
<0.0
"H20
JW OUTLET
1710
DEGF
FUEL STATIC
64.0
PSIG
FUEL GAS
74.0
DEGF
FUEL FLOW
25480.0
SCFHR
POWER CYL 1L
663.0
DEGF
OCAV PKESS
155X
-H20
POWER CYL 2L
700.0
DEGF
:mlet di'f
10
"H20
POWER CYL 3L
(66.0
DEGF
DISCHARGE GAS
713.0
PSIG
POWER CYL 4L
716.0
DEGF
VIBRATION
32.0
MILS
POWER CYL 5L
652.0
DEG F
FUEL VALVE OUTP UT
74.0
%
POWER CYL 1R
6B4.0
DEGF
MONTHLY FIRED HOURS
1547
HRS
POWER CYL 2R
744.0
DEGF
POV/ES CYL TRAEON COUNT
2574.0
QTS
POWER CYL 3R
633.0
DEGF
COMP CYL TRABOM COUNT
982.0
QTS
POWER CYL 4R
172.0
DEGF
POWER CYL 24 HR. TOT
45.0
QTS
POWER CYL 5R
646.0
DEGF
COM? CYL 24 HR. TOT
16.0
QTS
CRAWCASE COUNTS
0.0
QTS
11/14/94* 15: 55:10'
! 1 : 3 ! 6 ! 7 i 9 : 11 i 13 : lb :
STATION
PRINT
F-213
-------
US::
IIA 4
DESCRIPTION
VALUE UNITS
QESCRiPTiOiv
MR
UNITS
rifs®
232.? ma
LCSSU
1310
BEGF
IM 0U_ PRESS
MPStG
LOOtriLET
14H.I]
OEGF
LOFLMDfF
tOPSB
J'A'iEE
M
DEG r
fuao&-f
«jo um
jwouiLtf
1/1,0
DEGF
fie stats:
&1.B PSG
rjfTT r *r:
i ULL U»ij
74.0
DEG r
Flf&FLOn'
wiiii crrun
j'wrLT\
/VV «*«
r.
•; ) j 0
yjcj
I'Mj" r
ULU r
SCAVPRE55
143.C "H28
tVfc-fiT' rH* -It
/'W'JUlC Ii.fcL
G7S.G
DEGF
fffiJETDfff
3.0 "H23
f«MRai3L
rjn n
C-r J.U
iw r
btur
OLSCHARGEGrtS
712.9 PSIG
P(MftCYi.4L
(h&O
DEGF
wnflTrn^
2M aiS
TK^'.Tn ,~v ~
f w».
• ^ l.ij
KCF
Fiav*LVEOiiMii
fij'J
WMP.CVulK
-vv.,0
fitGF
SOrtTHLYFIREDHOIiRS
1546 ffr{5
fO^'du.'rL
rm
DEGF
po^oLM^coii:^
2J74.C CT3
pcvo
m
DEGF
C0S5» CYL TRASOr: C013.T
532,C GT3
ryy\ a
EOF
FOWXtL?4HR.T'J!"
Gii
iTErt
0:G f
C0M.2iHiU!)!
cmcAsrco^T3
«\n ors
o n f>TC
U.b Wi'J
r 11:13il 5
-- ¦I .••»:.< •
j-.'-. a;i,
- j - \J ¦; - V-: ;
F-214
-------
UNIT NO. 13
DESCRIPTION
VALUE UNITS
DESCRIPTION
VALUE
UNITS
BIGIESPEB)
23MRPM
LOHH
131.0
0EGF
LUBE OL PRESS
3GlO PSG
LO OUTLET
146JI
DEGF
LOFL1ERDFF
ypsx;
JWMET
1610
DEGF
FIE OFF
410 "H20
JMfOUTLET
171J)
DEGF
FIE STATIC
64.0 PSJG
FIE GAS
74.0
DEGF
FIE FLOW
23255.0 SCFffl
PGWBICYL1L
m
DEGF
SCAVPRESS
149.0 "H20
POWBICYL2L
674.0
DEGF
NJETDFF
10-H20
POWBICYL3L
644.0
DEGF
DtSCHARGE G AS
7110 P3G
POWBICYL4L
684.0
DEGF
VHUHON
26.0 H.S
POWBICVL5L
632.0
DEGF
FIE VALVE ounur
710%
POWERCYL1R
661.0
DEGF
BOMIYFIH) HOURS
1548 HIS
POWER CYL2R
718.0
DEGF
POWBCYLTRAEONCOUKT
2574.0 QTS
POWKCYL3R
612.0
DEGF
COVCYLTRABCN COUNT
982.0 QTS
POHBICYL4R
827.0
DEGF
POWER CH 24 BITOT
45.0 QTS
POWKCYL5R
628.0
DEGF
COAP CYL 24 Ht TOT
1i0 QTS
CRAWCASE COUNTS
0.0 QTS
11114194
17:25:30
1 3
5 7 9 11
1315
TATIO
3RIN1
F-215
-------
UNIT NO. 13
DESCRIPTION
VALUE UNITS
DESCRIPTION
VALUE
UNITS
BiG HE SPEED
231.DRPM
LOME
1310
DEGF
LIE OL PRESS
36J1 PSJG
LOOUTlfT
146.0
DEGF
LOFLMDFF
1.0 PSK
JWUFI
1(3.0
DEGF
FIEDFF
42JTH20
JW OUTLET
171.0
DEGF
Flfi STATIC
64.0 PSK
FIE GAS
74.0
DEGF
FIE FLOW
23387.0 SCFffi
POHHICTLIL
639.0
DEGF
StiW PRESS
150.0 "ICO
POWWCYL2L
678.0
DEGF
KIT OFF „
10"H20
POWmCYLl
6410
DEGF
DISCHARGE GAS
7110 PSK
POWKOL4L
684.0
DEGF
VGRATION
30.0 US
POHSRCiLSL
631.0
DEGF
FIE VALVE OUTPUT
70.0 *
POHffiOLIR
661.0
DEGF
MOHIHY FRED HOURS
1548 WS
POBHICYL2R
715.0
DEGF
P0WERCYLTRA80NC0UHT
2574.0 QTS
POWER DL3R
611.0
DEGF
COW1 CYL TRABON COUNT
982.0 QTS
POKBICYL4R
838.0
DEGF
POWBICYL24HR.TOT
45.0 QTS
627.0
DEGF
COW CYL 24 HR TOT
16.0 QTS
CRANKCASE COUNTS
0.0 QTS
17:30:35
11/14/94
1 3
5 7 9 11
1315
TATIO
JRIN^
F-216
-------
UNIT NO. 13
DESCRIPTION
VALUE UNITS
DESCRIPTION
VALUE
UNITS
BiGNE SPEED
230.0 RPM
LOHET
132.0
DEGF
LUBE (H PRESS
3(L0PSK
LOOUTlfT
1461
OEGF
LOFLHDFF
10 PSK
JWHET
1610
DEGF
FIE OFF
<10 "M
JfVOUItH
1710
DEGF
FIE STATIC
64.0 PSK
FIE GAS
74.0
DEGF
FIE FLOW
23401.0 SCFHR
POMBIC\l1L
629L0
DEGF
SCAV PRESS
150JTH20
POWER CYL2L
6781
DEGF
ME OFF
10 "H20
POVeCYL3L
64Z0
DEGF
DISCHARGE GAS
7110 PSJG
POWBICYL4L
686.0
DEGF
UERATXN
25.0 ItS
P0WBRCYL5L
632.0
DEGF
FIE VALVE OUTPUT
70.0 %
POUfilCYllR
661.0
DEGF
MONMY FRED HOURS
1548 HIS
POWBICYL2R
715.0
DEGF
POHBtCYLTRIBONCOUNT
2574.0 QTS
POWmCYLJR
6110
DEGF
COW CYLTRAI30H COUNT
982.0 QTS
POHRCYL4R
841.0
DEGF
POHfflCOIRTOT
45.0 QTS
P(mCYL5R
628.0
DEGF
COftP CYL 24 HR. TOT
1t0 QTS
CRANKCASE COUNTS
0.0 QTS
11114/94
17:36:07
1
3
5
7
9
11
13
15
rATIO
3RIN"I
F-217
-------
UNIT NO. 13
DESCRIPTION
VALUE UNITS
DESCRIPTION
VALUE
UNITS
BGHSPED
7mm
LOHfT
13Z0
OBGF
LUBEOL PRESS
ay psk
LOOUILET
146.0
DEGF
LOFITKDFF
11 PSJG
JWMIT
mo
DEGF
FUELHFF
41J "HZO
jwounfT
171JJ
DEGF
FiaSTAE
64.0 PSIG
Ha GAS
m
DEGF
fie flow
232081 SCFHR
pom oi u
€410
DEGF
SCAVfflESS
150.0 "H20
pomocvia
677.0
DEGF
HJETDfF
10 "KM
POHCYLl
6410
DEGF
DISCHARGE GAS
713.0 PSK
paeai4L
683.0
DEGF
mm
24.0 MS
pomacvia
632.0
DEGF
FUBLVULVEOUIPUT
70.0 %
powrohr
662.0
DEGF
UOHMYFI® HOURS
1548 IHS
PMKW.2R
7151
DEGF
POmCYLIMBONCOWr
2574.0 QTS
POWCYL3R
6111
DEGF
CMP CYLTRABON COUNT
982.0 QIS
P0WCU4R
837.0
DEGF
POHERCYL24HR.TOT
45.0 QTS
P0«CU5R
629.0
DEGF
COMPCYL24HR.TOI
i« QTS
CRAWCASECOUNFS
0.0 QTS
11/14/94
17:41:37
1 3
5 7 9 11
1315
PATIO
3RJN!
F-218
-------
UNIT NO. 13
DESCRIPTION
VALUE UNITS
DESCRIPTION
VALUE
UNITS
BIG HE SPED
230LO RPM
LOKET
132.0
DEGF
UKOL PRESS
3t0 PS)G
LOOUTlfT
146.0
DEGF
LOHL1BIDFF
UPSK
JWHET
1610
DEGF
FUB.DFF
410 "H20
JW OUTLET
1710
DEGF
FlfiSTAIK
64.0 PSK
FIE GAS
74.0
DEGF
FUB. FLOW
23243J) SCFTR
POMfltCYLH
6310
DEGF
'SCWPRESS
1510 *H20
POWBICVL2L
678.0
DEGF
HE OFF -
10 *H20
P0HRCYL1
6410
DEGF
DISCHARGE GAS
7110 PSIG
POWBICYL4L
685.0
DEGF
VBRATION
28.0 US
POWBICYL5L
632.0
DEGF
FIB VALVE OUT1VT
mo %
POWBtCYLIR
661J)
DEGF
MONIHYFRED HOURS
1548 US
POWER CYL2R
718.0
DEGF
POHBtCYLTRtftONCOUHT
2574.0 QTS
POWBICYL3R
61Z0
DEGF
COIF CYLTRABON COUNT
982.0 QTS
POWKCYL4R
824.0
DEGF
POWHICYL24HITOT
45.0 QTS
POWER CYL5R
628.0
DEGF
COW CYl 24 HI TOT
ItO QTS
CRAfKCASE COUNTS
0.0 QTS
11/14/94 17:46:38
1 3
5 7 9 11
1315
FATIO
3RIN1
F-219
-------
UNIT NO. 13
DESCRIPTION
VALUE UNITS
DESCRIPTION
VALUE
UNITS
BKKSPEB)
232J) RPM
LOME
1310
DEGF
USEOLPRESS
36JD PSIG
LOOUILE
147J)
DEGF
LOFIMDF
1.0 PSK
JWNfT
1610
DEGF
FUB. OFF
410 "H20
JWOUTLET
171.0
DEGF
FIE STATIC
64.0 PSIG
FUB. GAS
74.0
DEGF
FIEFLOW
2365H0 SCFHR
POWBlCYLtL
628.0
DEGF
SCAV>R£SS
152.0 "H20
POWER CKL2L
679.0
DEGF
HE OFF
10 "H20
POWKOLX
645.0
DEGF
DISCHARGE GAS
7110 PSIG
P0WKCYL4L
684.0
DEGF
VHUTION
25.0 MLS
POWER 0151
631.0
DEGF
FIE VALVE OUTPUT
mo*
POWKCYL1R
662.0
DEGF
MONTHYFI® HOURS
1549 ms
POWHtOL2R
716.0
DEGF
POWKCYLTRABONCOIHT
2574.0 QTS
POWKOL3R
614.0
DEGF
COfcP CYL TRABON COUNT
9810 QTS
POWER 014R
825.0
DEGF
PGWKCYL 24 HR. TOT
45.0 QTS
P0HBICYL5R
626.0
DEGF
COIP 0124 m TOT
MLO QTS
CRANKCASE COUNTS
0.0 QTS
17:50:41
11/14/94
1 3
5 7 9 11
1315
TATIO
3RIN1
F-220
-------
UNIT NO. 13
DESCRIPTION
VALUE UNITS
DESCRIPTION
VALUE
UNITS
BKKSPffl)
226.0 RPM
LOH.ET
133.0
DEGF
LUBE OL PRESS
35JI PSG
LOOURfT
147i)
DEGF
LOFlMOfF
1.0 PSK
JWHET
1610
DEGF
FIE NT
42JTH20
JWOUIlfT
1710
DEGF
FIE STATIC
64.0 m
FIE GAS
710
DEGF
FIE FLOW
23390.0 SCFHR
POWER CYL 1L
£38.0
DEGF
SCAVPRESS
147.0 "H20
POWKCYL2L
675.0
DEGF
NfTDFF
10 "ICO
POWmCYLl
642.0
DEGF
DISCHARGE GAS
7110 PSIG
POWER CYL 4L
684.0
DEGF
VGRAT10N
E0 US
POWBICTLS.
63a0
DEGF
FUEL VALVE OUTPUT
?ao %
POHBICYL1R
660.0
DEGF
MOHTHYFRB) HOURS
1549 WS
POWER CYL 2R
7110
DEGF
POWKCYLTRAIIOtl COUNT
2574.0 QTS
POWmCYLSR
614.0
DEGF
COH'CYLTRABON COUNT
982.0 QTS
P0WERCYL4R
8310
DEGF
POHHICYL24HITOT
45.0 QTS
PffleCYL5R
626.0
DEGF
COW CYL 24 m TOT
1&0 QTS
CRAWCASE COUNTS
0.0 QTS
11114194
1?: 56:115
1 3
5 7 9 11
1315
TATIO
3RIN1
F-221
-------
UNIT NO. 13
DESCRIPTION
VALUE UNITS
¦DESCRIPTION
VALUE
UNITS
ENGNESPHD
23MRPM
LOKET
133.0
DEGF
LUBEOL PRESS
35JIPSK
LO OUTLET
147.0
DEG F
LOUT® OFF
y PSJG
JWNfT
1610
DEGF
FUB. OFF
42,0 "H20
JWOUIIH
171.0
DEGF
FIE STATIC
64.0 PSJG
FIE GAS
710
DEGF
FIE FLOW
23399.0 SCFTO
POWERCYL1L
6310
DEGF
SCIVPRESS
151 J) "H20
POHBICYL2L
677J1
DEGF
HE OFF
10 "ICO
PGMBICYL3L
644.0
DEGF
DISCHARGE GAS
713.0 PSIG
P0WBICYL4L
684.0
DEGF
VGRATION
28.0 ItS
POWSRCYL5L
631.0
DEGF
FIE VALVE OUTPUT
70.0 %
POWHICYL1R
6610
DEGF
MONTHYFie HOURS
1549 US
POWBICYL2R
7110
DEGF
POmCYLTRABONCOUKT
2574.0 QTS
P0WERCYL3R
6120
DEGF
COIf1 CYLTRABON COUNT
982.0 QTS
POWER CYL4R
831.0
DEGF
POWER CYL 24111 TOT
45.0 QTS
POWKCYL5R
628.0
DEGF
COHP CVL 24 HR. TOT
iy QTS
CRAIKCASE COUNTS
0.0 QTS
11/14/94
11:01:04
1
3
5
7
9
11
13
15
fATIO
3Rihr
F-222
-------
UNIT NO. 13
DESCRIPTION
VALUE UNITS
DESCRIPTION
VALUE
UNITS
ENGK SPEED
228.0 R*
LOHJET
133.0
DEGF
LUBEOLPRESS
35.0 PSK
LOOUTLET
147.0
DEGF
LOFL1BIDFF
1J0PSK
JWHfT
iao
DEGF
RE OFF
4Z0 "H20
OUTLET
171JJ
DEGF
FIE STATIC
64.0 PSK
FIE GAS
73.0
DEGF
Ft^FLOHT
23595.0 SCFHR
POWERCYL1L
63L0
DEGF
SCAVPRESS
148.0 "H20
POMB1CYL2L
680J
DEGF
NLETDfF ^
10 "ICO
POWBRCYLX
642.0
DEGF
DISCHARGE GAS
714.0 PSK
POWBICYL4L
681.0
DEGF
VGRATION
24.0 MLS
P0WBICYL5L
631.0
DEGF
FIE VALVE OU1PUT
71.014
POWmCYLIR
659.0
DEGF
MONTHLYFIB HOURS
1549 HtS
POWBICYL2R
716.0
DEGF
POVeCYLTMBONCOUNT
2574.0 QTS
PCWBICYL3R
eiao
DEGF
COW CYLIRAGON COUNT
982.0 QTS
P0WKCYL4R
832.0
DEGF
POWBICYL24JRTOT
45.0 QTS
POWCRCYL5R
627Ji
DEGF
COWCYL24WLTOT
1&0 QTS
CRAWCASE COUNTS
0.0 QTS
11114/94 18:05:56
1 3
5 7 9 11
1315
TATIO
5RIN~j
F-223
-------
UNIT NO. 13
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNn
ENGINE SPEED
249.0
RPM
LO INLET
136J0
DEGF
LUBE OIL PRESS
m
PSIG
LO OUTLET
150.0
DEGF
LO FILTER DIFF
1.0
PSIG
J W INLET
163.0
DEGF
FUEL DIFF
54.0
"1120
JW OUTLET
172.0
DEGI
FUEL STATIC
64.0
PSIG
FUEL GAS
71J
DEGF
FUEL FLOW
26(94.0
SCFHR
POWER CYL 1L
638J0
DEGf
SCAVPRESS
190.0
*H20
POWER CYL 2L
682.0
DEGI
INLET DIFF
4.0
"H20
POWER CYL 3L
649J)
DEGI
DISCHARGE GAS
714.0
PSIG
POWER CYL 4L
701.0
DEGI
VIBRATION
38.0
MILS
POWER CYL 5L
640.0
DEG!
FUEL VALVE OUTPUT
76.0
*
POWER CYL 1R
672.0
DEGI
MONTHLYFIRED HOURS
1550
HRS
POWER CYL 2R
717 J)
DEG!
POWER CYL TRABON COUNT
2574.0
QTS
POWER CYL 3R
622.0
DEG
COMP CYL TRABON COUNT
982.0
QTS
POWER CYL 4R
863.0
DEG
POWER CYL 24 HR. TOT
45.0
QTS
POWER CYL 5R
646.0
DEG
COUP CYL 24 HR. TOT
16.0
QTS
CRANKCASE COUNTS
0.0
QTS
1
3
5
7
9
11
13
TATIO
PR
-------
UNIT NO. 13
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
248.0
RPN
LO INLET
136JI
DEGF
LUBE OIL PRE SS
37D
PSIG
LOOVRET
150.0
DEGF
LO FILTER DIFF
lit
PSIG
J W INLET
163.0
DEGF
FUEL DIFF
53.0
*H20
JW OUTLET
172.0
DEGF
FUEL STATIC
64.0
PSIG
FUEL GAS
71J)
DEGF
FUEL FLOW
26297.0
SCFHR
POWER CYL1L
635.0
DEGF
SCAVPRESS
186 J)
"H20
POWER CYL 2L
681.0
DEGF
INLET DIFF
4.0
" H20
POWER CYL3L
646.0
DEGF
DISCHARGE GAS
714.0
PSIG
POWER CYL4L
699.0
DEGF
VIBRATION
24.0
MILS
POWER CYL5L
640J)
DEGF
FUEL VALVE OUTPUT
77.0
*
POWER CYL 1R
669J)
DEGF
MONTHLY FIRE D HOURS
1550
HRS
POWER CYL2R
716.0
DEGF
POWER CYLT1IABON COUNT
2574.0
QTS
POWER CYL3R
623.0
DEGF
COMPCYLTRABON COUNT
982.0
QTS
POWER CYL4R
860.0
DEGF
POWER CYL 24 HR. TOT
45.0
QTS
POWER CYL5R
645.0
DEGF
COMPCYL24 HfLTOT
16.0
QTS
CRANKCASE COUNTS
0.0
QTS
F-225
1
3
5
7
9
11
13
15
TATIO
PRINT
-------
UNIT NO. 13
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
217 J)
RPH
LO INLET
m
DEGF
LUBE OIL PRESS
m
PSIG
LOOUIIET
150.0
DEGF
LO FILTER DIFF
1.0
PSIG
J W INLET
163J)
DEGF
FUEL DIFF
53.0
"H20
JW OUTLET
172.0
DEGF
FUEL STATIC
64.0
PSIG
FUEL GAS
71.0
DEGF
FUEL FLOW
26316.0
SCFHR
POWER CYL 1L
637.0
DEGF
SCAVPRESS
186.0
"H20
POWER CYL 2L
6S2J)
DEGF
INLET DIFF
4.0
"H20
POWER CYL 3L
646.0
DEGF
DISCHARGE GAS
714.0
PSIG
POWER CYL 4L
699.0
DEGF
VIBRATION
35.0
NILS
POWER CYL 5L
638.0
DEGF
FUEL VALVE OUTPUT
77.0
*
POWER CYL 1R
665.0
DEGF
HQNTHLYFIRED HOURS
1550
HRS
POWER CYL 2R
717.0
DEGF
POWER CYL TRABON COUNT
2574.0
QTS
POWER CYL 3R
621.0
DEGF
COUP CYLTRABON COUNT
982.0
QTS
POWER CYL 4R
855.0
DEGF
POWER CYL 24 HR. TOT
45.0
QTS
POWER CYL 5R
646.0
DEGF
COUP CYL 24 HR. TOT
16.0
QTS
CRANKCASE COUNTS
0.0
QTS
1
3
5
7
9
11
13
15
TATIO
PRINT
-------
UNIT NO. 13
DESCRIPTION
VALUE UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPIiED
249J0 RPM
LO INLET
136J)
DEGF
LUBE OIL PIKESS
37.0 PSIG
L O OUTLET
150.0
DEGF
L 0 FILTER DIFF
1J) PSIG
J W INLET
163.0
DEGF
FUEL DIFF
53.0 "ICO
JW OUTLET
172.0
DEGF
FUEL STATIC
61.0 PSIG
FUEL GAS
70.0
DEGF
FUEL FLOW
28345.0 SCFHR
POWER CYL 1L
637.0
DEGF
SCAV PRESS
188 J) "H20
POWER CYL 2L
673.0
DEGF
INLET DIFF
4.0 "H20
POWER CYL 3L
647.0
DEGF
DISCHARGE GAS
714.0 PSIG
POWER CYL 4L
697.0
DEGF
VIBRATION
36J) MILS
POWER CYL 5L
639.0
DEGF
FUEL VALVE OUTPUT
76.0 K
POWER CYL 1R
667.0
DEGF
MONTHLY FIRED HOURS
1550 HRS
POWER CYL 2R
715.0
DEGF
POWER CYLTHABON COUNT
2574.0 QTS
POWER CYL 3R
624.0
DEGF
COMP CYL TRABON COUNT
982J) QTS
POWER CYL 4R
859.0
DEGF
POWER CYL 24 HR. TOT
45.0 QTS
POWER CYL 5R
645.0
DEGF
COMP CYL 21 HR. TOT
16.0 QTS
CRANKCASE COUNTS
0.0 QTS
F-227
1
3
5
7
9
11
13
15
TATIO
PRINT
-------
UNIT NO. 13
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
2S0.D
RPM
LO INLET
136J)
DEGF
LUBE OIL PRESS
37.0
PSIG
LO OUTLET
150.0
DEGF
LO FILTER DIFF
1.0
PSIG
J W INLET
163 J)
DEGF
FUEL DIFF
53.0
"H20
JW OUTLET
172.0
DEGF
FUEL STATIC
64.0
PSIG
FUEL GAS
70 J)
DEGF
FUEL FLOW
26485.0
SCFHR
POWER CYL 1L
633J)
DEGF
SCAY PRESS
189.0
"H20
POWER CYL 2L
676.0
DEGF
INLET DIFF
4.0
"H20
POWER CYL 3L
649.0
DEGF
DISCHARGE GAS
714J)
PSIG
POWER CYL 4L
697.0
DEGF
VIBRATION
36.0
MILS
POWER CYL 5L
639J)
DEGF
FUEL VALVE OUTPUT
76.0
X
POWER CYL 1R
668.0
DEGF
HOMILY FIRED HOURS
1550
HRS
POWER CYL 2R
715.0
DEGF
POWER CYL TRABON COUNT
2574.0
QTS
POWER CYL 3R
621 J)
DEGF
C0MPCYLTRA50N COUNT
982J)
QTS
POWER CYL 4R
862.0
DEGF
POWER CYL 24 HR. TOT
45.0
QTS
POWER CYL 5R
645.0
DEGF
COUP COHR. TOT
16.0
QTS
CRANKCASE COUNTS
0.0
QTS
F-228
1
3
5
7
9
11
13
15
TATIOI
PRINT
-------
UNIT NO. 13
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
240J)
RPH
LO INLET
135D
DEGF
LUBE OIL PRE SS
36.0
PSIG
LOOUOET
150.0
DEGF
L 0 FILTER DIFF
1.0
PSIG
J W INLET
163J)
DEGF
FUELDIFF
50.0
"H20
JW OUTLET
172.0
DEGF
FUEL STATIC
64.0
PSIG
FUEL GAS
69.0
DEGF
FUEL FLOW
25558.0
SCFHR
POWER CYL 1L
m
DEGF
SCAV PRESS
176J)
"H20
POWER CYL 2L
683J)
DEGF
INLET DIFF
4.0
"H20
POWER CYL3L
651.0
DEGF
DISCHARGE GAS
713.0
PSIG
POWER CYLIL
695.0
DEGF
VIBRATION
24.0
MILS
POWER CYL5L
639.0
DEGF
FUEL VALVE OUTPUT
74.0
X
POWER CYL 1R
672.0
DEGF
MONTHLYFIRliD HOURS
1551
HRS
POWER CYL 2R
717.0
DEGF
POWER CYL TRABON COUNT
2574.0
QTS
POWER CYL 3R
622.0
DEGF
COUP CYL TRABON COUNT
982.0
QTS
POWER CYL 4R
855J)
DEGF
POWER CYL 24 HR. TOT
45.0
QTS
POWER CYL 5R
641.0
DEGF
COUP CYL 24 HR. TOT
16.0
QTS
CRANXCASE COUNTS
0.0
QTS
F-229
1
3
5
7
9
11
13
15
TATIO
PRINT
-------
UNIT NO. 13
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
241.0
RPM
LO INLET
135J)
DEGF
LUBE OIL PRESS
36.0
PSIG
LO OUTLET
150.0
DEGF
10 FILTER DIFF
1.0
PSIG
J W INLET
163.0
DEGF
FUEL DIFF
50.0
'H20
JW OUTLET
172.0
DEGF
>UEL STATIC
64.0
PSIG
FUEL GAS
69J0
DEGF
FUEL FLOW ^
25752.0
SCFHR
POWER CYL 1L
638.0
DEGF
SCAV PRESS
175.0
"H20
POWER CYL 2L
681.0
DEGF
INLET DIFF
4.0
'H20
POWER CYL 3L
651.0
DEGF
DISCHARGE GAS
714.0
PSIG
POWER CYL 4L
694J)
DEGF
VIBRATION
29.0
MILS
POWER CYL 5L
6374)
DEGF
FUEL VALVE OUTPUT
74.0
*
POWER CYL 1R
668.0
DEGF
HONTHLYFIRED HOURS
1551
HRS
POWER CYL 2R
717.0
DEGF
POWER CYLTRABON COUNT
2574.0
QTS
POWER CYL 3R
621.0
DEGF
COUP CYL TRABON COUNT
382.0
QTS
POWER CYL 4R
851.0
DEGF
POWER CYL 24 HR. TOT
45.0
QTS
POWER CYL 5R
640.0
DEGF
COUP CYL 24 HR. TOT
16.0
QTS
CRANKCASE COUNTS
0.0
QTS
F-230
1
3
5
7
9
11
13
15
TATIO
PRINT
-------
UNIT NO. 13
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEIED
240J)
RPH
LO INLET
135J0
DEGF
LUBE OIL PRESS
36.0
PSIG
LO OUTLET
149.0
DEGF
L 0 FILTER DIFF
til
PSIG
J W INLET
163.0
DEGF
FUEL DIFF
50.0
"H20
JW OUTLET
172.0
DEGF
FUEL STATIC
64.0
PSIG
FUEL GAS
68.0
DEGF
FUEL FLOW
25582.0
SCFHR
POWER CYL 1L
641J0
DEGF
SCAV PRESS
177J)
"H20
POWER CYL 2L
SS2jO
DEGF
INLET DIFF
4.0
"H20
POWER CYL 3L
648.0
DEGF
DISCHARGE (>AS
714.0
PSIG
POWER CYL 4L
S97.0
DEGF
VIBRATION
23.0
MILS
POWER CYL 5L
640.0
DEGF
FUEL VALVE OUTPUT
74.0
X
POWER CYL 1R
671.0
DEGF
MONTHLY FIR£D HOURS
1551
HRS
POWER CYL 2R
717.0
DEGF
POWERCYL'HUBON COUNT
2574.0
QTS
POWER CYL 3R
618.0
DEGF
COMPCYLTFIABON COUNT
982.0
QTS
POWER CYL 4R
853.0
DEGF
POWER CYLiBHR. TOT
45.0
QTS
POWER CYL 5R
642.0
DEGF
COUP CYL 24 HR. TOT
16j0
QTS
CRANKCASE COUNTS
0.0
QTS
F-231
1
3
5
7
9
11
13
15
TATIO
PRINT
-------
UNIT NO. 13
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
241JI
RPM
LO INLET
m
DEGF
LUBE OIL PRESS
36J)
PSIG
LO OUTLET
149.0
DEGF
LO FILTER DIFF
1.0
PSIG
J W INLET
163.0
DEGF
FUELDIFF
49.0
"H20
JW OUTLET
171.0
DEGF
FUEL STATIC
64J)
PSIG
FUEL GAS
68J)
DEGF
FUEL FLOW
25491.0
SCFHR
POWER CYL 1L
636.0
DEGF
SCAV PRESS
176.0
"H20
POWER CYL 2L
682.0
DEGF
INLET DIFF
4.0
"H20
POWER CYL 3L
648J)
DEGF
DISCHARGE GAS
714.0
PSIG
POWER CYL 4L
696.0
DEGF
VIBRATION
28.0
MILS
POWER CYL 5L
638.0
DEGF
FUEL VALVE OUTPUT
74.0
*
POWER CYL 1R
670J)
DEGF
MOIfTHLYFIRED HOURS
1551
HRS
POWER CYL 2R
716.0
DEGF
POWER CYLMBON COUNT
2574.0
QTS
POWER CYL 3R
621.0
DEGF
COUP CYL THABON COUNT
982.0
QTS
POWER CYL 4R
B52.0
DEGF
POWER CYL 24 HR. TOT
45.0
QTS
POWER CYL 5R
640.0
DEGF
COUP CYL 24 HR. TOT
16.0
QTS
CRANKCASE COUNTS
0.0
QTS
1
3
5
7
9
11
13
15
TATIO
PRINT
-------
UNIT NO. 13
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEliD
239.0
RPH
LO INLET
m
DEGF
LUBE OIL PRJ:.SS
XI
PSIG
LO OUTLET
149.0
DEGF
L 0 FILTER DIFF
1.0
PSIG
J W INLET
163.0
DEGF
FUEL DIFF
49.0
"IB
JW OUTLET
171.0
DEGF
FUEL STATIC
64 J)
PSIG
FUEL GAS
88j0
DEGF
FUEL FLOW
25519.0
SCFHR
POWER CYL 1L
632.0
DEGF
SCAV PRESS
176 J)
"H20
POWER CYL 2L
688.0
DEGF
INI FT RIPF
IIMlli 1 MM 1
in
T»W
¦H9fl
IIMV
pnwc rv13i
1 tf llklt «TI to Vto
(UQii
VWtV
Mk V 1
DISCHARGE GAS
714.0
PSIG
POWER CYL 4L
693.0
DEGF
VIBRATION
21J)
MILS
POWER CYL 5L
m
DEGF
FUEL VALVE OUTPUT
74.0
*
POWER CYL 1R
m
DEGF
MONTHLY FIRi D HOURS
1552
HRS
POWER CYL 2R
715.0
DEGF
POWER CYLTRABON COUNT
2574.0
QTS
POWER CYL 3R
619.0
DEGF
COUP CYLTRABON COUNT
982J)
QTS
POWER CYL 4R
851J)
DEGF
POWER CYL21HR. TOT
45.0
QTS
POWER CYL 5R
640.0
DEGF
COMP CYL 24 HR. TOT
16J)
QTS
CRANKCASE COUNTS
Oil
QTS
F-233
1
3
5
7
9
11
13
15
TATIO
PRINT
-------
UNIT NO. 13
DESCRIPTION
VALUE
UNITS
DESCRIPTION
VALUE
UNITS
ENGINE SPEED
240J)
RPN
LO INLET
135J1
DEGF
LUBE OIL PRESS
36.0
PSIG
LO OUTLET
m
DEGF
LO FILTER DIFF
11
PSIG
J W INLET
163.0
DEGF
FUELDIFF
50.0
¦HZO
JW OUTLET
171.0
DEGF
mihm
64.0
PSIG
FUEL GAS
m
DEGF
FUEL FLOW
^ 25667.0
SCFHR
POWER CYL 1L
640J)
DEGF
SCAY PRESS
175.0
"H20
POWER CYL 2L
677J)
DEGF
INLET DIFF
4J)
"H20
POWER CYL 3L
648.0
DEGF
DISCHARGE GAS
710
PSIG
POWER CYL 4L
632J)
DEGF
VIBRATION
26.0
MILS
POWER CYL 5L
639J)
DEGF
FUEL VALVE OUTPUT
74.0
*
POWER CYL 1R
668.0
DEGF
MONTHLY FIRED HOURS
1SS2
HRS
POWER CYL 2R
716.0
DEGF
POWER CYLTRABON COUNT
2S74.D
QTS
POWER CYL 3R
620.0
DEGF
COMP CYL TRABON COUNT
982.0
QTS
POWER CYL 4R
853J)
DEGF
POWER CYL 24 HR. TOT
45.0
QTS
POWER CYL 5R
641.0
DEGF
COKPCYL24HR.TOT
16.0
QTS
CRANKCASE COUNTS
0.0
QTS
F-234
1
3
5
7
9
11
13
15
TATIO
PRINT
-------
11 Ml I
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F-235
\
\
-------
UNIT NO. 13
DESCRIPTION
VALUE UNITS
DESCRIPTION
VALUE
UNITS
BKKSPED
- 2310 RPM
LONJET
1310
DEGF
LUBE OL PRESS
3fL0 PSK
LO OUTLET
146J)
DEGF
LOFIimDFF
1J3 PSJG
JWHfT
1610
DEGF
FIE OFF
42JI "H20
jwrounE
1710
DEGF
FlfiSTATK
64.0 PSK
FIE GAS
74.0
DEGF
RE FLOW
23416.0 SCFHR
POWBtCYLIL
63M
DEGF
SCAVPRESS
151JJ "H20
pome oi 2L
681.0
DEGF
ME OFF
3L0 "H20
POWKCYLl
6410
DEGF
DISCHARGE GAS
7110 PSK
POKBICYL4L
687.0
DEGF
VHttlKNi
21.0 MLS
POWKCYL5L
634.0
DEGF
FUELVXLVE OUTPUT
710%
POWBICYL1R
661.0
DEGF
¦ONTltYFIE) HOURS
1548 US
POWER CYL2R
716.0
DEGF
POUeCYLIMBONCOWr
2574.0 QTS
POWKCYL3R
615.0
DEGF
COW 01TRABON COUNT
982.0 QTS
POWER CYL4R
825.0
DEGF
POWBRCYL 24 HR. TOT
45.0 QTS
POWBICYL5R
625.0
DEGF
COW CVL 24 m TOT
1&0 QTS
CRANKCASE COUNTS
0.0 QTS
11114194 17:10:19
1
3
5
7
9
11
13
15
rATIO
3RIN1
F-236
-------
UNIT NO. 13
DESCRIPTION
VALUE UNITS
DESCRIPTION
VALUE
UNITS
BBIESPffl)
23MRPM
LOME
131J0
DEGF
LUBE OL PRESS
36JD PSG
LOOUUfT
146.0
DEGF
LOFIMOF
10 PSK
JWMH
1610
DEGF
FUB. OFF
410 "H20
Jdf OUTLET
17U0
DEGF
FIE STATIC
m PSJG
FUBLGAS
74.6
DEGF
FIE FLOW
23433LD SCFHR
P0WERCYL1L
63QL0
DEGF
SCffi/PRES
150.0 "H20
POINBICYL2L
68Q.8
DEGF
NEDFF
3.0 "H20
POYBCYL1
644.0
DEGF
DISCHARGE GAS
' 7110 PSIG
POWKCYL4L
68SJ)
DEGF
VBUTION
25.0 Hi
POVeCYL5L
634.0
DEGF
FlEVXLVEOOIPirr
70.0 %
P0WERCYL1R
664J)
DEGF
MOHTTIY FRH) HXfS
1548 HRS
POWER CYL 2R
718.0
DEGF
POWERCYLTRABDN COUNT
2574.0 QTS
P0WERCYL3R
614.0
DEGF
COfeF CYL TRABON COUNT
982.0 QTS
POWER CYL 4R
828.0
DEGF
P0HKCYL24HR.T0T
45.0 QTS
P0WHICYL5R
626.0
DEGF
COW CYL24IR TOT
16.0 QTS
CRANKCASECOlfliTS
0.0 QTS
11(14194 17:15:31
1 3
5 7 9 11
1315
TATIO
3RIN1
¥-231
-------
UNIT NO. 13
DESCRIPTION
VALUE UNITS
DESCRIPTION
VALUE
UNITS
BKKSPffl)
22SL0 RPM
LOME
131.0
DEGF
LUBE 01 PRESS
aao psiG
LOOUTLET
MLO
DEGF
LOFLHDFF
U0 PSJG
JWME
163.0
DEGF
FIHDFF
41j0 "H2D
jwounn
1710
DEGF
Flfi STATIC
64.0 PSK
FUEGAS
74.0
DEGF
RE FLOW
232720 SCFHR
POWER CYL 1L
639.0
DEGF
SCAVPRESS
m "H20
POWER CYL 2L
678.0
DEGF
HEDFF
10 "H20
POWKCYL3L
644J0
DEGF
DKCHAflGE GAS
71Z0 PSJG
POWER CYL 4L
685.0
DEGF
VHUI10N
22.0 H.S
FOWBICYL5L
632.0
DEGF
FUEL VALVE OUTPUT
70.0 %
POWER CYL 1R
661.0
DEGF
MOKTH.YFIB HOURS
1548 H6
POWKCYL2R
715.0
DEGF
POMimCVLTRABONCOUKT
25/4.0 QTS
POWKCYL3R
611.0
DEGF
COW CYLTRABON COUNT
982.0 QTS
POWKCYL4R
829.0
DEGF
POWER CYL 24 fR TOT
45.0 QTS
POWER CYL 5R
627.0
DEGF
COtP CYL 24 HR. TOT
iu QTS
CRMKCASE COUNTS
0.0 QTS
11114/94 1 7:20:50
1
3
5
7
9
11
13
15
rATIO
3RIN1
F-238
-------
Appendix G
Manual Measurement Data
This appendix presents a summary of the manual velocity (Method 2) and moisture
(Method 4) data collected for each engine and turbine tested.
G-l
-------
Plant Name:
Location: Refrigeration Engine Stack
G.1 Campaign 2
Run No.
One
Date
03/12/94
Time Start
1312
Time Finish
1533
Operator
GM
Initial Leak Rate
0.008
Final Leak Rate
0.01
Duct Dimensions (ft)
0
Stack Diameter (ft)
1.29
Pitot Tube Correction Factor (Cp)
0.84
Dry Gas Meter Calibration (Yd)
0.985
Nozzle Diameter (inches)
0.1500
Barometric Pressure ("Hg)
27.5
Static Pressure ("H20)
0.1
Meter Volume (acf)
49.400
Average square root of delta p
2.1000
Average delta H (" H20)
1.10
Average: Stack Temperature (F)
564
Average DGM Temp (F)
91.0
Test Duration (minutes)
80.0
Condensed Water (g)
55.0
Filter Weight Gain (g)
N/A
PNR Weight Gain (g)
N/A
Impinger Residue (g)
N/A
% C02
2.6
% 02
15.4
% N2
82.0
Meter Volume (dscf)
42.983
Rue Gas Moisture (%)
5.7
Gas Molecular Weight (Wet) (g/g-r
28.40
Absolute Stack Pressure (" Hg)
27.51
Absolute Stack Temperature (R)
1024
Average Gas Velocity (f/sec)
172.64
Avg Flow Rate (acfm)
13,539
Avg Flow Rate (dscfm)
6,050
I Isokinetic Sampling Rate (%)
94.60
G-2
-------
Plant Name:
Location: Recompression Engine Stack
Run No.
One
Date
03/13/94
Time Start
1340
Time Finish
1554
Operator
GM
Initial Leak Rate
0.007
Final Leak Rate
0.004
Duct Dimensions (ft)
0
Stack Diameter (ft)
1.29
Pitot Tube Correction Factor (Cp)
0.84
Dry Gas Meter Calibration (Yd)
0.985
Nozzle Diameter (inches)
0.1500
^, Barometric Pressure ("Hg)
27.8
Static Pressure ("H20)
-2.6
Meter Volume (acf)
45.900
Average square root of delta p
2.3300
Average delta H (" H20)
1.00
Average Stack Temperature (F)
1092
Average DGM Temp (F)
81.5
Test Duration (minutes)
80.0
Condensed Water (g)
85.6
Filter Weight Gain (g)
N/A
PNR Weight Gain (g)
N/A
Impinger Residue (g)
N/A
% C02
4.8
% 02
11.4
% N2
83.8
Meter Volume (dscf)
41.069
Hue Gas Moisture (%)
9.0
Gas Molecular Weight (Wet) (g/g-n
28.22
Absolute Stack Pressure (" Hg)
27.61
Absolute Stack Temperature (R)
1552
Average Gas Velocity (f/sec)
236.16
Avg Flow Rate (acfm)
18,519
Avg Flow Rate (dscfm)
5,291
Isokinetic Sampling Rate (%)
103.36
G-3
-------
Plant Name: GRI Campaign #3 - Plant A
Location: Engine 102 Exhaust
G.2 Campaign 3
Run No.
One
Date
06/13/94
Time Start
1730
Time Finish
1853
Operator
GM
Initial Leak Rate
0.003
Final Leak Rate
0.004
Duct Dimensions (ft)
0
Stack Diameter (ft)
1.83
Pitot Tube Correction Factor (Cp)
0.84
Dry Gas Meter Calibration (Yd)
. Nozzle Diameter (inches)
0.968
N/A
Barometric Pressure ("Hg)
29.06
Static Pressure ("H20)
-1.5
Meter Volume (acf)
13.280
Average square root of delta p
1.5200
Average delta H (" H20)
0.50
Average Stack Temperature (F)
993
Average DGM Temp (F)
106.0
Test Duration (minutes)
N/A
Condensed Water (g)
38.7
Filter Weight Gain (g)
N/A
PNR Weight Gain (g)
N/A
Impinger Residue (g)
N/A
% C02
7.1
% 02
9.5
% N2
83.4
Meter Volume (dscf)
11.662
Flue Gas Moisture (%)
13.5
Gas Molecular Weight (Wet) (g/g-n
27.96
Absolute Stack Pressure (" Hg)
28.95
Absolute Stack Temperature (R)
1453
Average Gas Velocity (f/sec)
146.25
Avg Flow Rate (acfm)
23,157
Avg Flow Rate (dscfm)
7,036
Isokinetic Sampling Rate (%)
N/A
G-4
-------
Plant Name: GRI Campaign #3 - Plant B
Location: Engine 4 Exhaust
Type of Sample: Velocity/Moisture - High Load
Run No.
One
Date
06/18/94
Time Start
935
Time Finish
1115
Operator
GM
Initial Leak Rate
0.005
Final Leak Rate
0.006
Duct Dimensions (ft)
0
Stack Diameter (ft)
1.60
Pitot Tube: Correction Factor (Cp)
0.84
Diy Gai; Meter Calibration (Yd)
0.968
Nozzle Diameter (inches)
N/A
Barometric Pressure ("Hg)| 29.29
I Static Pressure ("H20)
8.4
| Meter Volume (acf)
40.890
1 Average square root of delta p
2.0080
| Average delta H (" H20)
1.00
| Average Stack Temperature (F)
645
Average DGM Temp (F)
90.0
Test Duration (minutes)
N/A
Condensed Water (g)
80.8
Filter Weight Gain (g)
N/A
PNR Weight Gain (g)
N/A
Impinger Residue (g)
N/A
% C02
4.2
% 02
14.7
% N2
81.1
Meter Volume (dscf)
37.292
Flue Gas Moisture (%)
9.3
Gas Molecular Weight (Wet) (g/g-n
28.22
Absoluts Stack Pressure (" Hg)
29.91
Absolute Stack Temperature (R)
1105
Average Gas Velocity (f/sec)
165.01
Avg Flow Rate (acfm)
20,006
Avg Flow Rate (dscfm)
8,665
1 Isokinetic Sampling Rate (%)
N/A
G-5
-------
Plant Name: GRI Campaign #3 - Plant B
Location: Engine 2 Exhaust
Run No.
One
Date
06/19/94
Time Start
905
Time Finish
915
Operator
GM
Initial Leak Rate
N/A
Final Leak Rate
N/A
Duct Dimensions (ft)
0
Stack Diameter (ft)
1.00
Pitot Tube Correction Factor (Cp)
0.84
Dry Gas Meter Calibration (Yd)
N/A
Nozzle Diameter (inches)
N/A
Barometric Pressure ("Hg)
29.36
Static Pressure ("H20)
9.5
Meter Volume (acf)
N/A
Average square root of delta p
1.9670
Average delta H (" H20)
N/A
Average Stack Temperature (F)
661
Average DGM Temp (F)
N/A
Test Duration (minutes)
N/A
Condensed Water (g)
N/A
Filter Weight Gain (g)
N/A
PNR Weight Gain (g)
N/A
Impinger Residue (g)
N/A
%C02
5.2
% 02
13.0
% N2
81.8
Meter Volume (dscf)
0.000
Flue Gas Moisture (%)
10.3
Gas Molecular Weight (Wet) (g/g-r
28.18
Absolute Stack Pressure (" Hg)
30.06
Absolute Stack Temperature (R)
1121
Average Gas Velocity (f/sec)
162.49
Avg Flow Rate (acfm)
7,657
Avg Flow Rate (dscfm)
3,249
Isokinetic Sampling Rate (%)
N/A
Note: The moisture data is based on the average of
the moisture measured during the two PM10 samples.
G-6
-------
G.3 Campaign 4
Plant Name: GRI Campaign #4
Location: Cooper/Bessemer #4 Engine Exhaust
Type of Sample: Velocity Full Load
Run No.
One
Date
08/25/94
Time Start
1715
Time Finish
1730
Operator
SJR/CSG
Initial Leak Rate
N/A
Final Leak Rate
N/A
Duct Dimensions (ft)
0
Stack Diameter (ft)
2.00
Pitot Tube Correction Factor (Cp)
0.84
Dry Gas Meter Calibration (Yd)
N/A
Npzzle Diameter (inches)
N/A
Barometric Pressure ("Hg)
29.54
Static Pressure ("H20)
1.2
Meter Volume (acf)
N/A
Average square root of delta p
1.2040
Average delta H (" H20)
N/A
Average Stack Temperature (F)
574
Average DGM Temp (F)
N/A
Test Duration (minutes)
N/A
Condensed Water (g)
N/A
Filter Weight Gain (g)
N/A
PNR Weight Gain (g)
N/A
Impinger Residue (g)
N/A
% C02
3.0
%02
15.3
%N2
81.7
Meter Volume (dscf)
0.000
Flue Gas Moisture (%)
7.26
Gas Molecular Weight (Wet) (g/g-mole)
28.29
Absolute Stack Pressure (" Hg)
29.63
Absolute Stack Temperature (R)
1034
Average Gas Velocity (f/sec)
96.04
Avg Flow Rate (acfm)
18,102
Avg Flow Rate (dscfm)
8,486
Isokinetic Sampling Rate (%)
N/A
The oxygen and carbon dioxide data originated from the CEM.
The moisture data originated from a moisture sample.
Sample points 1 and 12 are less than 1 inch
from the duct walls and therefore were not included.
G-7
-------
Plant Name: GR1 Campaign #4
Location: Cooper/Bessemer #4 Engine Exhaust
Velocity Full Load
Run No.
Two
Date
08/26/94
Time Start
855
Time Finish
910
Operator
SJR/CSG
Initial Leak Rate
N/A
Final Leak Rate
N/A
Duct Dimensions (ft)
0
Stack Diameter (ft)
2.00
Pitot Tube Correction Factor (Cp)
0.84
Dry Gas Meter Calibration (Yd)
N/A
Nozzle Diameter (inches)
N/A
Barometric Pressure ("Hg)
29.49
Static Pressure ("H20)
1.45
Meter Volume (acf)
N/A
Average square root of delta p
1.2080
Average delta H (" H20)
N/A
Average Stack Temperature (F)
517
Average DGM Temp (F)
N/A
Test Duration (minutes)
N/A
Condensed Water (g)
N/A
Filter Weight Gain (g)
N/A
PNR Weight Gain (g)
N/A
Impinger Residue (g)
N/A
% C02
3.0
% 02
15.3
% N2
81.7
Meter Volume (dscf)
0.000
Flue Gas Moisture (%)
7.3
Gas Molecular Weight (Wet) (g/g-mole)
28.28
Absolute Stack Pressure (" Hg)
29.60
Absolute Stack Temperature (R)
Average Gas Velocity (f/sec)
Avg Flow Rate (acfm)
977
93.72
17,666
Avg Flow Rate (dscfm)
8,751
Isokinetic Sampling Rate (%)
N/A
The oxygen and carbon dioxide data originated from the CEM.
The moisture data represents the average of the PMlO and
CARB 429 samples.
Sample points 1 and 12 are less than 1 inch
from the duct walls and therefore were not included.
G-8
-------
Plant Name: GRI Campaign #4
Location: Ingersol #8 Engine Exhaust
Type of Sample:
Velocity Full ]
Run No.
One
Date
08/27/94
Time Start
1115
Time Finish
1125
Operator
SJR/CSG
Initial Leak Rate
N/A
Final Leak Rate
N/A
Duct Dimensions (ft)
0
Stack Diameter (ft)
1.63
Pitot Tube Correction Factor (Cp)
0.84
Dry Gas Meter Calibration (Yd)
N/A
Nozzle Diameter (inches)
N/A
Barometric Pressure ("Hg)
29.47
Static Pressure ("H20)
-1.5
Meter Volume (acf)
N/A
Average square root of delta p
1.3800
Average delta H (" H20)
N/A
Average Stack Temperature (F)
741
Average DGM Temp (F)
N/A
Test Duration (minutes)
N/A
Condensed Water (g)
N/A
Filter Weight Gain (g)
N/A
PNR Weight Gain (g)
N/A
Impinger Residue (g)
N/A
% C02
5.3
% 02
11.1
%N2
83.6
Meter Volume (dscf)
0.000
Flue Gas Moisture (%)
10.8
Gas Molecular Weight (Wet) (g/g-mole)
28.07 .
Absolute Stack Pressure (" Hg)
29.36
Absolute Stack Temperature (R)
1201
Average Gas Velocity (f/sec)
119.63
Avg Flow Rate (acfm)
14,886
Avg Flow Rate (dscfm)
5,726
Isokinetic Sampling Rate (%)
N/A
The oxygen and carbon dioxide data originated from the CEM.
The moisture data represents the average of a PM10 sample
and CARB 429 sample.
G-9
-------
Plant Name: GRI Campaign #4
Location: Ingersol #8 Engine Exhaust
Type of Sample:
Velocity Full
Run No.
Two
Date
08/27/94
Time Start
2050
Time Finish
2102
Operator
SJR/CSG
Initial Leak Rate
N/A
Final Leak Rate
N/A
Duct Dimensions (ft)
0
Stack Diameter (ft)
1.63
Pitot Tube Correction Factor (Cp)
0.84
Dry Gas Meter Calibration (Yd)
N/A
Nozzle Diameter (inches)
N/A
Barometric Pressure ("Hg)
29.47
Static Pressure ("H20)
-1.5
Meter Volume (acf)
N/A
Average square root of delta p
1.3700
Average delta H (" H20)
N/A
Average Stack Temperature (F)
719
Average DGM Temp (F)
N/A
Test Duration (minutes)
N/A
Condensed Water (g)
N/A
Filter Weight Gain (g)
N/A
PNR Weight Gain (g)
N/A
Impinger Residue (g)
N/A
% C02
5.3
% 02
11.1
%N2
83.6
Meter Volume (dscf)
0.000
Flue Gas Moisture (%)
10.8
Gas Molecular Weight (Wet) (g/g-mole)
28.07
Absolute Stack Pressure (" Hg)
29.36
Absolute Stack Temperature (R)
1179
Average Gas Velocity (f/sec)
117.67
Avg Flow Rate (acfm)
14,642
Avg Flow Rate (dscfm)
5,737
| Isokinetic Sampling Rate (%)
N/A
The oxygen and carbon dioxide data originated from the CEM.
The moisture data represents the average of a PM10 sample
and CARB 429 sample.
G-10
-------
Plant Name: GRI Campaign #4
Location: Ingersol #9 Engine Exhaust
Type of Sample: Velocity Full Load
Run No.
One
Date
08/28/94
Time Start
1300
Time Finish
1320
Operator
SJR/CSG
Initial Leak Rate
N/A
Final Leak Rate
N/A
Duct Dimensions (ft)
0
Stack Diameter (ft)
1.63
Pitot Tube Correction Factor (Cp)
0.84
| Dry Gas Meter Calibration (Yd)
N/A
Nozzle Diameter (inches)
N/A
Barometric Pressure ("Hg)
29.5
Static Pressure ("H20)
-0.63
Meter Volume (acf)
N/A
Average square root of delta p
1.0600
Average delta H (" H20)
N/A
Average Stack Temperature (F)
779
Average DGM Temp (F)
N/A
Test Duration (minutes)
N/A
Condensed Water (g)
N/A
Filter Weight Gain (g)
N/A
PNR Weight Gain (g)
N/A
Impinger Residue (g)
N/A
% C02
7.0
% 02
8.6
% N2
84.4
Meter Volume (dscf)
0.000
Flue Gas Moisture (%)
14.4
Gas Molecular Weight (Wet) (g/g-mole)
27.81
Absolute Stack Pressure (" Hg)
29.45
Absolute Stack Temperature (R)
1239
Average Gas Velocity (f/sec)
93.61
Avg Flow Rate (acfm)
11,649
Avg Flow Rate (dscfm)
4,181
Isokinetic Sampling Rate (%)
N/A
The oxygen and carbon dioxide data originated from the CEM.
The moisture data represents the average of a PM10 sample
and CARB 429 sample collected on 8/29.
G-ll
-------
Plant Name: GRI Campaign #4
Location: Ingersol #9 Engine Exhaust
Type of Sample: Velocity Full Load
Run No.
Two
Date
08/29/94
Time Start
808
Time Finish
820
Operator
SJR/CSG
Initial Leak Rate
N/A
Final Leak Rate
N/A
Duct Dimensions (ft)
0
Stack Diameter (ft)
1.63
Pitot Tube Correction Factor (Cp)
0.84
Dry Gas Meter Calibration (Yd)
N/A
Nozzle Diameter (inches)
N/A
Barometric Pressure ("Hg)
29.47
Static Pressure ("H20)
-0.77
Meter Volume (acf)
N/A
Average square root of delta p
1.0800
Average delta H (" H20)
N/A
Average Stack Temperature (F)
779
Average DGM Temp (F)
N/A
Test Duration (minutes)
N/A
Condensed Water (g)
N/A
Filter Weight Gain (g)
N/A
PNR Weight Gain (g)
N/A
Impinger Residue (g)
N/A
% C02
6.9
% 02
8.6
%N2
84.5
Meter Volume (dscf)
0.000
Flue Gas Moisture (%)
14.4
Gas Molecular Weight (Wet) (g/g-mole)
27.80
Absolute Stack Pressure (" Hg)
29.41
Absolute Stack Temperature (R)
1239
Average Gas Velocity (f/sec)
95.47
Avg Flow Rate (acfm)
11,880
Avg Flow Rate (dscfm)
4,259
Isokinetic Sampling Rate (%)
N/A
The oxygen and carbon dioxide data originated from the CEM.
The moisture data represents the average of a PM10 sample
and CARB 429 sample.
G-12
-------
G.4 Campaign 5
Facility:
Date:
Loccition:
Run Number:
Sample Type:
GRI
10/5/94
Turbine
3
M-0010
Tota.l Sampling Time (min)
Corrected Barometric Pressure (in Hg)
Absolute Stack Pressure (in H20)
Stack Static Pressure (in H20)
Average Stack Temperature (°F)
Stack Area (sq in)
Actual Meter Volume (cu ft)
Average Meter Pressure (in H20)
Average Meter Temperature (°F)
Moisture Collected (g)
Carbon Dioxide Concentration (%V)
Oxygen Concentration (%V)
Nitrogen Concentration (%V)
Dry Gas Meter Factor
Nozzle Diameter (in)
Pitot Constant
168 .0
29.32
29.39
1.00
239.42
7238.23
145.828
2 . IS
69.81
127.80
2.0
17.7
80.4
1.0005
0.186
0.84
Average Sampling Rate (dscfm)
Standard Metered Volume (dscf)
Standard Metered Volume (dscm)
Stack Moisture (%V)
Mole Fraction Dry Stack Gas
Dry Molecular Weight
Wet Molecular Weight
Stack Gas Velocity (fpm)
Stack Gas Velocity (mpm)
Volumetric Flow Rate (acfm)
Volumetric Flow Rate (acmm)
Volumetric Flow Rate (dscfm)
Volumetric Flow Rate (dscmm)
Percent Isokinetic
Percent Excess Air
Fuel Factor
Ultimate C02
0.853
143.328
4 .059
4 .03
0.960
29.02
28 .58
6500.75
1981.43
326763.19
9253.93
232503.44
6584.50
97.75
494.16
1.645
12 .7
G-13
-------
Facility: GRI
Date: 10/5/94
Location: Turbine
Run Number: 3-DUP
-
Sample Type: M-0010
SSSSSSSSSSSSSSSSSSSSSSSSSSSSSSSSSSSSSSSSSSSSSSSSSSSSSS
SSSKSSSSSKSSSSSS
Total Sampling Time (min)
168.0
Corrected Barometric Pressure (in Hg)
29.34
Absolute Stack Pressure (in H20)
29.41
Stack Static Pressure (in H20)
1.00
Average Stack Temperature (°F)
429.71
Stack Area (sg in)
7238.23
Actual Meter Volume (cu ft)
135 .405
Average Meter Pressure (in H20)
2.14
Average Meter Temperature (°F)
57.42
Moisture Collected (g)
134.90
Carbon Dioxide Concentration (%V)
2.0
Oxygen Concentration (%V)
17.7
Nitrogen Concentration (%V)
80.4
Dry Gas Meter Factor
1.0005
Nozzle Diameter (in)
0.186
Pitot Constant
0.84
Average Sampling Rate (dscfm)
0.812
Standard Metered Volume (dscf)
136.359
Standard Metered Volume (dscm)
3 .862
Stack Moisture (%V)
4.46
Mole Fraction Dry Stack Gas
0.955
Dry Molecular Weight
29 .02
Wet Molecular Weight
28 .53
Stack Gas Velocity (fpm)
7645.74
Stack Gas Velocity (mpm)
2330.42
Volumetric Flow Rate (acfm)
384316.62
Volumetric Flow Rate (acmm)
10883.85
Volumetric Flow Rate (dscfm)
214146.99
Volumetric Flow Rate (dscmm)
6064.64
Percent Isokinetic
100.97
Percent Excess Air
492 .86
Fuel Factor
1.633
Ultimate C02
12 . 8
G-14
\
\
-------
Plant Name: GRI Campaign #6 Plant A
Location: Clark BA-5 #10 Engine Exhaust
G.5 Campaign 6
I Test No.
Prelimenary
One
Three
Two
| Engine Load
Full
Full
Low
Full
Date
11/03/94
11/04/94
11/04/94
11/05/94
Time Start
1520
940
1611
924
Time Finish
1546
943
1620
932
Operator
CSG
CSG
LAR
LAR/LDO
Initial Leak Rate
N/A
N/A
N/A
N/A
Final Leak Rate
N7A
N/A
N/A
N/A
Duct Dimensions (ft)
0
0
0
0
Stack Diameter (ft)
1.96
1.96
1.96
1.96
Pitot Tube Correction Factor (Cp)
0.84
0.84
0.84
0.84
Dry Gas Meter Calibration (Yd)
N/A
N/A
N/A
N/A
No:tzle Diameter (inches)
N/A
N/A
N/A
N/A
Barometric Pressure ("Hg)
26.36
26.36
26.36
26.51
Static Pressure ("H20)
-0.65
-0.6
-0.8
-0.85
Meter Volume (acf)
N/A
N/A
N/A
N/A
Average square root of delta p
1.0400
1.0500
1.0500
1.0800
Average delta H (" 1120)
N/A
N/A
N/A
N/A
Average Stack Temperature (F)
453
458
436
455
Average DGM Temp (F)
N/A
N/A
N/A
N/A
Test Duration (minutes)
N/A
N/A
N/A
N/A
Condensed Water (g)
N/A
N/A
N/A
N/A
Filter Weight Gain (g)
N/A
N/A
N/A
N/A
PNR Weight Gain (g)
N/A
N/A
N/A
N/A
Impinger Residue (g)
N/A
N/A
N/A
N/A
% C02
2.6
2.6
2.4
2.7
% 02
16.9
16.9
17.3
16.8
%N2
80.5
80.5
80.3
80.5
Meter Volume (dscf)
0.000
0.000
0.000
0.000
Hue Gas Moisture (%)
5.6
6.4
5.4
4.9
Gas Molecular Weight (Wet) (g/g-n
28.47
28.38
28.48
28.56
Absolute Stack Pressure (" Hg)
26.31
26.32
26.30
26.45
Absolute Stack Temperature (R)
913
918
896
915
Average Gas Velocity (f/sec)
82.45
83.59
82.47
85.36
Avg Flow Rate (acfm)
14,926
15,133
14,930
15,453
Avg Flow Rate (dscfm)
7,163
7,163
7313
7,493
Isokinetic Sampling Rate (%)
N/A
N/A
N/A
N/A
G-15
-------
Plant Name: GRI Campaign #6 Plant A
Location: Clark HBA-5 #12 Engine Exhaust
Velocity Profile
Test No.
Four
Five
Engine Load
Low
High
Date
11/04/94
11/05/94
Time Start
1724
1513
Time Finish
1735
1802
Operator
LAR
CSG
Initial Leak Rate
N/A
N/A
Final Leak Rate
N/A
N/A
Duct Dimensions (ft)
0
0
Stack Diameter (ft)
1.29
1.29
Pitot Tube Correction Factor (Cp)
0.84
0.84
Dry Gas Meter Calibration (Yd)
N/A
N/A
Nozzle Diameter (inches)
N/A
N/A
Barometric Pressure ("Hg)
26.37
26.47
Static Pressure CH20)
-2
-2
Meter Volume (acf)
N/A
N/A
Average square root of delta p
1.6000
1.6300
Average delta H (" H20)
N/A
N/A
Average Stack Temperature (F)
540
592
Average DGM Temp (F)
N/A
N/A
Test Duration (minutes)
N/A
N/A
Condensed Water (g)
N/A
N/A
Filter Weight Gain (g)
N/A
N/A
PNR Weight Gain (g)
N/A
N/A
Impinger Residue (g)
N/A
N/A
% C02
3.3
3.7
% 02
15.6
15.1
% N2
81.1
81.2
Meter Volume (dscf)
0.000
0.000
Flue Gas Moisture (%)
6.8
6.9
Gas Molecular Weight (Wet) (g/g-mole)
28.39
28.42
Absolute Stack Pressure (" Hg)
26.22
26.32
Absolute Stack Temperature (R)
1000
1052
Average Gas Velocity (f/sec)
133.16
138.79
Avg Flow Rate (acfin)
10,442
10,884
Avg Flow Rate (dscfm)
4,502
4,473
Isokinetic Sampling Rate (%)
N/A
N/A
G-16
-------
Plant Name: GRI Campaign #6 Plant B
Location: Solar Taurus Turbine Exhaust
TypeofSam£lejVelodtj^PTOnie_^___^_i
Test No.
Six
Seven
Eight
Engine Load
Higfr
High
Low
Date
11/07/94
11/08/94
11/08/94
Time Start
1550
810
1505
Time Finish
1626
910
1525
Operator
LAR
CSG/LDO
LAR
Initial Leak Rate
N/A
N/A
N/A
Final Leak Rate
N/A
N/A
N/A
Duct Dimensions (ft)
0
0
0
Stack Diameter (ft)
2.96
2.96
2.96
^, Pitot Tube Correction Factor (Cp)
0.84
0.84
0.84
Dry Gas Meter Calibration (Yd)
N/A
N/A
N/A
Nozzle Diameter (inches)
N/A
N/A
N/A
Barometric Pressure ("Hg)
26.5
26.54
26.54
Static Pressure ("H20)
0.9
0.9
0.9
Meter Volume (acf)
N/A
N/A
N/A
Average square root of delta p
2.3200
2.4500
2.1400
Average delta H (" H20)
N/A
N/A
N/A
Average Stack Temperature (F)
954
941
902
Average DGM Temp (F)
N/A
N/A
N/A
Test Duration (minutes)
N/A
N/A
N/A
Condensed Water (g)
N/A
N/A
N/A
Filter Weight Gain (g)
N/A
N/A
N/A
PNR Weight Gain (g)
N/A
N/A
N/A
Impinger Residue (g)
N/A
N/A
N/A
% C02
3.2
3.3
2.9
% 02
16.0
15.9
16.4
%N2
80.8
80.8
80.7
Meter Volume (dscf)
0.000
0.000
0.000
Flue Gas Moisture (%)
6.4
6.5
6.1
Gas Molecular Weight (Wet) (g/g-mole)
28.44
28.43
28.44
Absolute Stack Pressure (" Hg)
26.57
26.61
26.61
Absolute Stack Temperature (R)
1414
1401
1362 I
Average Gas Velocity (f/sec)
227.92
239.43
206.17
Avg Flow Rate (acfm)
94,106
98,857
85,124
Avg Flow Rate (dscfm)
29,192
30,964
27,544
1 Isokinetic Sampling Rate (%)
N/A
N/A
N/A
G-17
-------
Plant Name: GRI Campaign #6 Plant C
Location: Copper Bessemer #15 Engine Exhaust
_^geiofSam£le^Velodtj^Profile____ii___i_i^____
Test No.
Prelimenary
Nine
Ten
Eleven
Engine Load
Full
Full
Full
Low
Date
11/09/94
11/10/94
11/10/94
11/11/94
Time Start
1604
1130
1808
933
Time Finish
1620
1458
1818
940
Operator
LAR
CSG
LAR
LAR/LDO
Initial Leak Rate
N/A
N/A
N/A
N/A
Final Leak Rate
N/A
N/A
N/A
N/A
Duct Dimensions (ft)
0
0
0
0
Stack Diameter (ft)
1.62
1.62
1.62
1.62
PitotTube Correction Factor (Cp)
0.84
0.84
0.84
0.84
Diy Gas Meter Calibration (Yd)
N/A
N/A
N/A
N/A
NozzleDiameter (inches)
N/A
N/A
N/A
N/A
Barometric Pressure ("fig)
26.5
26.78
26.78
26.66
Static Pressure CH20)
-1.3
-1.5
-1.5
-1.3
Meter Volume (acf)
N/A
N/A
N/A
N/A
Average square root of delta p
1.6800
1.7300
1.7300
1.6600
Average delta H (" H20)
N/A
N/A
N/A
N/A
Average Stack Temperature (F)
576
581
576
552
Average DGM Temp (F)
N/A
N/A
N/A
N/A
Test Duration (minutes)
N/A
N/A
N/A
N/A
Condensed Water (g)
N/A
N/A
N/A
N/A
Filter Weight Gain (g)
N/A
N/A
N/A
N/A
PNR Weight Gain (g)
N/A
N/A
N/A
N/A
Impinger Residue (g)
N/A
N/A
N/A
N/A
% C02
3.7
3.6
3.7
3.3
% 02
14.8
15.3
14.8
15.6
% N2
81.5
81.1
81.5
81.1
Meter Volume (dscf)
0.000
0.000
0.000
0.000
Flue Gas Moisture (%)
7.2
7
7
6.9
Gas Molecular Weight (Wet) (g/g-n
28.38
28.40
28.40
28.38
Absolute Stack Pressure (" Hg)
26.40
26.67
26.67
26.56
Absolute Stack Temperature (R)
1036
1041
1036
1012
Average Gas Velocity (f/sec)
141.86
145.63
145.29
138.11
Avg Flow Rate (acfm)
17,544
18,011
17,969
17,080
Avg Flow Rate (dscfm)
7320
7,570
7,588
7,363
Isokinetic Sampling Rate (%)
N/A
N/A
N/A
N/A
G-18
-------
Plant Name: GRI Campaign #6 Plant C
Location: Copper Bessemer #9 Engine Exhaust
Test No.
12
13
14
Engine Load
Low
Full
Full
Date
11/11/94
11/12/94
11/12/94
Time Start
1830
845
1734
Time Finish
1852
900
1745
Operator
LAR
CSG
LAR/LDO
Initial Leak Rate
N/A
N/A
N/A
Final Leak Rate
N/A
N/A
N/A
Duct Dimensions (ft)
0
0
0
Stack Diameter (ft)
1.29
1.29
1.29
Pitot Tube: Correction Factor (Cp)
0.84
0.84
0.84
Dry Gas Meter Calibration (Yd)
N/A
N/A
N/A
Nozzle Diameter (inches)
N/A
N/A
N/A
Barometric Pressure ("Hg)
26.66
26.55
26.46
Static Pressure ("H20)
7
7.5
7
Meter Volume (acf)
N/A
N/A
N/A
Average square root of delta p
1.7800
1.7100
1.7100
Average delta H (" H20)
N/A
N/A
N/A
Average Stack Temperature (F)
576
586
590
Average DGM Temp (F)
N/A
N/A
N/A
Test Duration (minutes)
N/A
N/A
N/A
Condensed Water (g)
N/A
N/A
N/A
Filter Weight Gain (g)
N/A
N/A
N/A
PNR Weight Gain (g)
N/A
N/A
N/A
Impinger Residue (g)
N/A
N/A
N/A
% C02
3.5
3.9
4.0
% 02
15.0
14.7
14.5
% N2
81.5
81.4
81.5
Meter Volume (dscf)
0.000
0.000
0.000
Flue Gas Moisture (%)
7.2
8.3
8.4
Gas Molecular Weight (Wet) (g/g-n
28.36
28.28
28.28
Absolute Stack Pressure (" Hg)
27.17
27.10
26.97
9 Absolute Stack Temperature (R)
1036
1046
1050
Average Gas Velocity (f/sec)
148.21
143.45
144.07
Avg Flow Rate (acfm)
11,623
11,249
11,298
Avg Flow Rate (dscfm)
4,991
4,715
4,690
Isokinetic Sampling Rate (%)|
N/A
N/A
N/A
G-19
-------
Volumetric Flow Spreadsheet
Plant GRI - Campaign 6
Date 11/14/94
Sampling Location Engine 13
Run Number 23
Ambient Temperature (*F) 51.00
Barometric Pressure (in Hg) 26.87
Static Pressure (in H20) 4.50
Operator GSW
Time 2040-2050
02 Percent 15.06
C02 Percent 3.72
N2 Percent 81.22
Stack Moisture (%) 6.85
Mole Fraction (dry} 0.93
Molecular Weight (dry) 29.20
Molecular Weight (wet) 28.43
Stack ID (in) 23.50
Stack Area (sq ft) 3.01
Traverse
Velocity
Stack
Square
Stack Gas
Stack Gas
Point
Head dP
Ts
Root of
Velocity
Velocity
Number
(in H20)
(*F)
dP
(fps)
(fpm)
A-1
3.50
550
1.87
153.82
9229.41
A-2
4.50
640
2.12
182.03
10921.63
A-3
5.20
650
2.28
196.56
11793.66
A-4
4.50
648
2.12
182.69
10961.28
B-1
3.90
508
1.97
158.96
9537.76
B-2
4.70
642
2.17
186.20
11171.84
B-3
5.10
650
2.26
194.66
11679.71
B-4
4.30
648
2.07
178.58
10714.93
Averages
617.00
2.11
179.19
10751.28
Actual Volumetric Flow Rate (acfm) 32383.45
Standard Volumetric Flow Rate (scfm) 14374.97
Dry Standard Volumetric Flow Rate (dscfm 13360.09
\
\
G-20
-------
Volumetric Flow Spreadsheet
Plant GRI - Campaign 6
Date 11/14/94
Sampling Location Engine 13
Run Number 18
Ambien t Temperature (*F) 55.00
Barometric Pressure (in Hg) 26.83
Static Pressure (in H20) 4.10
Operator GSW
Time 1905-1915
02 Percent 15.11
C02 Percent 3.68
N2 Percent 81.21
Stack Moisture (%) 6.77
Mole Fraction (dry) 0.93
Molecular Weight (dry) 29.19
Molecular Weight (wet) 28.44
Stack ID (in) 23.50
Stack Area (sq ft) 3.01
Traverse
Velocity
Stack
Square
Stack Gas
Stack Gas
Point
Head dP
Ts
Root of
Velocity
Velocity
Number
(in H20)
CF)
dP
(fps)
(fpm)
A-1
4.00
550
2.00
164.44
9866.66
A-2
4.80
642
2.19
188.17
11290.06
A-3
5.70
652
2.39
205.98
12358.77
A*4
4.80
651
2.19
188.93
11336.08
B-1
4.20
530
2.05
166.83
10009.68
B-2
5.10
640
2.26
193.78
11626.96
B-3
5.60
650
2.37
203.98
12238.86
B-A
4.80
650
2.19
188.85
11330.98
Averages
620.63
2.20
187.62
11257.26
Actual Volumetric Flow Rate (acfm) 33907.49
Standard Volumetric Flow Rate (scfm) 15000.99
Dry Standard Volumetric Flow Rate (dscfm 13941.92
G-21
-------
Volumetric Flow Spreadsheet
Plant GRI - Campaign 6
Date 11/14/94
Sampling Location Engine 13
Run Number 15
Ambient Temperature (*F) 61.00
Barometric Pressure (in Hg) 26.75
Static Pressure (in H20) 4.50
Operator GSW
Time 1100-1115
02 Percent 14.67
C02 Percent 3.81
N2 Percent 81.52
Stack Moisture (%) 6.91
Mole Fraction (dry) 0.93
Molecular Weight (dry) 29.20
Molecular Weight (wet) 28.42
Stack ID (in) 23.50
Stack Area (sq ft) 3.01
Traverse
Velocity
Stack
Square
Stack Gas
Stack Gas
Point
Head dP
Ts
Root of
Velocity
Velocity
Number
(in H20)
(°F)
dP
(fps)
(fpm)
A-1
3.30
585
1.82
151.93
9115.84
A-2
4.30
660
2.07
179.55
10772.81
A-3
5.00
670
2.24
194.47
11668.38
A-4
3.60
670
1.90
165.02
9900.95
B-1
3.80
630
1.95
166.51
9990.55
B-2
4.50
658
2.12
183.51
11010.65
B-3
4.70
668
2.17
188.38
11302.90
B-4
3.60
669
1.90
164.94
9896.57
Averages
651.25
2.02
174.29
10457.33
Actual Volumetric Flow Rate (acfm) 31498.07
Standard Volumetric Flow Rate (scfm) 13551.01
Dry Standard Volumetric Flow Rate (dscfm 12594.31
G-22
-------
Volumetric Flow Spreadsheet
Plant GRI - Campaign 6
Date 11/15/94
Sampling Location Engine 11
Run Number 24
Ambient Temperature (*F) 51.00
Barometric Pressure (in Hg) 26.87
Static Pressure (in H20) 6.20
Operator GSW
Time 1740-1750
02 Percent 15.06
C02 Percent 3.72
N2 Percent 81.22
Stack Moisture (%) 6.76
Mole Fraction (dry) 0.93
Molecular Weight (dry) 29.20
Molecular Weight (wet) 28.44
Stack ID (in) 17.50
Stack Area (sq ft) 1.67
Traverse
Velocity
Stack
Square
Stack Gas
Stack Gas
Point
Head dP
Ts
Root of
Velocity
Velocity
Number
(in H20)
CF)
dP
(fps)
(fpm)
A-1
2.90
455
1.70
132.34
7940.37
A-2
4.00
601
2.00
167.37
10042.20
A-3
4.10
614
2.02
170.48
10229.07
A-4
4.00
615
2.00
168.47
10108.26
B-1
3.40
490
1.84
146.01
8760.63
B-2
4.30
602
2.07
173.61
10416.88
B-3
4.50
616
2.12
178.77
10726.41
B-4
4.20
615
2.05
172.63
10357.88
Averages
576.00
1.98
163.71
9822.71
Actual Volumetric Flow Rate (acfm) 16407.22
Standard Volumetric Flow Rate (scfm) 7671.19
Dry Standard Volumetric Flow Rate (dscfm 7171.80
G-23
-------
Volumetric Flow Spreadsheet
Plant GRI - Campaign 6
Date 11/15/94
Sampling Location Engine 11
Run Number 20
Ambient Temperature (*F) 55.00
Barometric Pressure (in Hg) 26.91
Static Pressure (in H20) 5.80
Operator GSW
Time 1630-1645
02 Percent 14.61
C02 Percent 3.86
N2 Percent 81.53
Stack Moisture (%) 6.98
Mole Fraction (dry) 0.93
Molecular Weight (dry) 29.20
Molecular Weight (wet) 28.42
Stack ID (in) 17.50
Stack Area (sq ft) 1.67
V
Traverse
Velocity
Stack
Square
Stack Gas
Stack Gas
Point
Head dP
Ts
Root of
Velocity
Velocity
Number
fin H20)
PF)
dP
(fps)
(fpm)
A-1
2.90
465
1.70
133.06
7983.66
A-2
3.90
608
1.97
165.81
9948.55
A-3
4.20
620
2.05
173.03
10381.95
A-4
4.00
623
2.00
169.10
10145.81
B-1
3.00
491
1.73
137.23
8233.51
B-2
4.00
612
2.00
168.24
10094.14
B-3
4.40
624
2.10
177.43
10645.93
B-4
3.90
624
1.97
167.05
10022.81
Averages
583.38
1.94
161.37
9682.04
Actual Volumetric Flow Rate (acfm) 16172.25
Standard Volumetric Flow Rate (scfm) 7507.89
Dry Standard Volumetric Flow Rate (dscfm 7019.12
G-24
-------
Volumetric Flow Spreadsheet
Plant GRI - Campaign 6
Date 11/15/94
Sampling Location Engine 11
Run Number 19
Ambient Temperature (*F) 50.00
Barometric Pressure (in Hg) 27.02
Static Pressure (in H20) 6.00
Operator GSW
Time 1035-1045
02 Percent 14.91
C02 Percent 3.76
N2 Percent 81.33
Stack Moisture (%) 6.73
Mole Fraction (dry) 0.93
Molecular Weight (dry) 29.20
Molecular Weight (wet) 28.44
Stack ID (in) 17.50
Stack Area (sq ft) 1.67
Traverse
Velocity
Stack
Square
Stack Gas
Stack Gas
Point
Head dP
Ts
Root of
Velocity
Velocity
Number
(in H20)
CF)
dP
(fps)
(fpm)
A-1
3.40
519
1.84
148.22
8893.38
A-2
4.40
605
2.10
175.87
10552.19
A-3
4.80
620
2.19
184.98
11098.77
A-4
4.80
621
2.19
185.07
11103.91
B-1
3.40
512
1.84
147.69
8861.52
B-2
4.60
613
2.14
180.50
10829.81
B-3
4.90
622
2.21
187.07
11224.17
B-4
4.60
622
2.14
181.25
10875.14
Averages
591.75
2.08
173.83
10429.86
Actual Volumetric Flow Rate (acfm) 17421.36
Standard Volumetric Flow Rate (scfm) 8023.38
Dry Standard Volumetric Flow Rate (dscfm 7501.05
G-25
-------
Appendix H
Fuel Analysis Results
This ajipendix presents the fuel analysis performed at each campaign including fuel
composition (e.g., liquid volume percent and weight percent) and higher and lower heating
values.
H-l
-------
HOENIX LABORATORIES, INC.
S 6025PRINCETON AVE. SUITES3U
A MIDLAND. TEXAS 79703 |915) 520-8803
H.1 Campaign 2
8AMPLE NUMBER:
Q5993
DATE RECEIVED:
7/6/93
CRYO RESIDUE COMPOSITE @ PLT 193
SAMPL£ I.O.:
COMPANY:
LOCAllON:
SAMPLED BY: L 8EABOURNE
PRESSURE: 630#
TIME SAMPLED:
EFFECTIVE DATE
TEMPERATURE:
DATE SAMPLED:
7/6/93
70TA13
COMMENTS:
FRACTIONAL OAS ANALYSIS
AT 14.65 AND 90 DEGREES F
COMPOUND
MOL %
QPkl
SP. Gfl.
CORRECTED
SPECIFIC GRAVITY
CARBON DIOXIDE
0.00
0.0000
nitrogen
1.64
0.0150
B.T.U./CU. FOOT:
0.0000
(H2S FREE)
METHANE
96.85
0.5309
DRY BASI6
ETHANE
2.44
0.649
0.0253
WET BASIS
PROPANE
0.07
0.019
0.0011
ISO-BUTANE
0.00
0.000
0.0000
PENTANESPLUS
N-BUTANE
0.00
0.000
0.0000
OPM:
ISO-PI-NTANE
0.00
0.000
0.0000
N-PEOTANE
0.00
0.000
0.0000
H2SPPM:
HEXANESPLUS
0.00
0.000
0.0000
100.00
0.668 0.6732
TFACTOR
0.5741
0.000
0
0.9979
ANALYST:
H-2
-------
H.2 Campaign 3
Gas Analysis
Campaign 3
Station 3A
Date
Engine
Test
Fd factor
High HV
¦
Low HV
fdsct/MMBtu)
fBtu/scf)
(Btu/scf)
6/14/94
102
1
8498
1159
1049
102
2
8498
1148
1039;
102
3
8498
1148
10391
6/15/94
101
1
8509
1148
1039J
101
2
8509
1148
1039;
101
3
8509
1148
1039'
11/17/95
H-3
C3-FD.WK4
-------
Certi ficate of Analysis No- 226:
Comoanv:
Samole of:
Samole bv:
Samole date:
For:
RADIAN CORP.
NATURAL GAS
W,GRAY of RADIAN
cp/15/94 at 1216
RADIAN CORPORATION
July 29. 1994
Date/Time of Anal:
Data Were Normalized to
C pmpjonentj
Component
l—i. st ed i i
Mole X
r> Chromatogr aphi c
Nitrogen
Carbon Dioxide
Methane
Ethane
Prooane
i-Butane
n-Butane
1-Pentane
n-Pentane
2,3-Di methyl but ane
4-Methvl-c-oentene~2
2-Methvlcentane
3-MethvlDentane
n-Hexane
Methvlcvclooentane
Cvclohexane
2-Methylhexane
3-Methvlhexane
n-Heotane
Methylcvclohexane
1.802
0.181
79.531
16.766
1.565
0.037
0.095
0.008
0.011
0.000
0.000
0.001
0.000
0.001
0.000
0.000
0.000
0.000
0.000
0.000
Weight X
2.633
0.416
66.560
26.300
3.600
0.112
0.288
0.030
0.041
0.001
0.001
0.004
0.002
0.005
0.001
0.001
0.001
0.001
0.001
0.001
100.000
100.000
H-4
-------
*-*dcje ** 1
Cer t i Tic.
o "f AnalV!
Mo.
226306
Company : RADIAN CORP.
Source : MB NO. 2 MANIFOLD
Saoiole of : NATURAL GAS
Conditions: At Pressure of 30 osio fc Temoerature of: 84 °F
Samoled By: W.GRAV of RADIAN Date: 05V15/94 Time: 1216
For
: RADIAN CORPORATION
Analysis^
Test By G.C. SPA Method 2261
Mo 17.
Nitrooen
Carbon Dioxide
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
Hexane Plus
1.802
0.181
79.531
16.766
1.565
0.037
0.095
0.008
0.011
0.004
ioo.ooo
Factors Fro* 6PA-2145, Jan. 01, 1994
6PM at 14.696 psia
4.474
0.430
0.012
0.030
0.003
0.004
0.000
4.953
Soecific Gravity at 60°F fair=l) Perfect Gas ... 0.6618
Real Gas ... 0.6637
Calculated Molecular Ueiaht
19.17
Calculated Gross
B.T.U./ft® at 14.696
osia and 60
°F
Perfect Gas
Drv basis ...
1144
Saturated basis ...
1124
Deviation Factor...
0.9968
Real Gas
Dry basis
1148
Saturated basis ...
1128
n-HEXANE
0.005 Wt. Z
0.001
Mol. Z
BENZENE
< 0.001 Wt. z
4 0.001
Mol. Z
ETHYL BENZENE
^ 0.Q01 Wt. Z
0.001
Mol. X
TOLUENE
* 0.001 Wt. Z
^ 0.001
Mol. Z
XYLENES
£ 0.001 Wt. z
* 0.001
Mol. Z
H-5
-------
Page * 2
Certi ficate of Analysi s No. 22E306
Calculated Net B.T.U./ft3 at 14.696 psia and 60 °F
Perfect Gas Dry basis ... 1036
Saturated basis ... 1018
Deviation Factor... 0.9968
Real Gas Dry basis ... 1033
Saturated basis ... 1021
Southern Petroleum Laboratories, Inc.
H-6
sua Laooratories>
-------
Cert i ficate of Analysis No. 226307
Company:
Sample of:
Sample by:
Sample date:
For:
RADIAN CORP.
NATURAL GAS
W.C.G. of RADIAN
0e/14/94 at 1300
RADIAN CORPORATION
July 29, 1994
Date/Time of Anal:
Data Were Normalized to 100.00*
Component ¦
Listed in Chromatographic Ordc
Component
Mole X
Weight X
Nitrogen
0.792
1.167
Carbon Dioxide V
0.078
0.181
Methane
80.954
68.316
Ethane
16.423
25.977
Propane
1.479
3.430
i-Butane
0.040
0.122
n-Butane
0.133
0.406
i-Pentane
0.035
0.134
n-Pentane
0.048
0.182
2.3-Dimet hylbutane
0.001
0.005
4-Methyl-c-oentene-2
0.001
0.003
2-Methvloentane
0.004
0.020
3-Methvloentane
0.002
0.010
n-Hexane
0.005
0.022
Methvlcvclopentane
0.001
0.006
Cyclohex.ine
0.001
0.004
2-Methylhexane
0.000
0.002
3-Met hy 1hexane
0.001
0.003
n-Heotane
0.001
0.006
Met hvlc yc1ohexane
0.001
0.005
100.000
100.000
/^vW
H-7
-------
Certi ficate oT Analvsis No- 226307
Comoanv : RADIAN CORP.
Source : ¦¦¦¦» ENS. NO.2 MANIFOLD
Samel* of ; NATURAL SAS
Conditions: At Pressure of 20 psia %. Temperature of; 85 °F
Samol ecf By: W.C.6. of RADIAN Date; 09/14/94 Time: 1300
For
RADIAN CORPORATION
Test By S.C. SPA Method 2261 Factors Fro* GPA-2145, Jan. 01, 1994
AnailxsisjL
Mol X
GPrt at 14.696 psia
Ni trooen
Carbon Dioxide
Methane
Ethane
Prooane
i-Butane
n-Butane
i-Pentane
n-Pentane
Hexane Plus
0.792
0.078
80.954
16.423
1.479
0.040
0.133
0.035
0. 048
0.018
4.382
0.407
0.013
0.042
0.013
0.017
0.005
100.000
4.879
Soecific gravity at 60°F (air=l) Perfect 6as ... 0.6564
Real Sas ... 0.6582
Calculated Molecular Weiaht
19.01
Calculated Gross
B.T.U./fts at 14.696
psia and 60
op
Perfect Gas
Dry basis
1155
Saturated basis ...
1135
Deviation Factor,,.
0.9968
Real Sas
Dry basis
1159
Saturated basis ...
1139
n-HEXANE
0.022 Wt. 2
0.005
Mol.
Z
BEN2ENE
<.0,001 Wt. Z
< 0.001
Mol.
z
ETHYL BENZENE
< 0.001 Wt. 2
<0.001
Mol.
z
TOLUENE
4 o.ooi wt. i
* 0.001
Mol.
z
XYLENES
z 0.001 Wt. 1
z. 0.001
Mol.
z
H-8
-------
Certi ficate of" Analysis No. 226307
Calculated Net B.T.U./ft* at 14.6% osia and 60 °F
Perfect Gas Dry basis ... 1046
Saturated basis ... 1027
Deviation Factor... 0.9968
Real Gas Drv basis ... 1049
Saturated basis ... 1030
H-9
Southern Petroleu* Laboratories, Inc.
-------
Gas Analysis
Campaign 3
Station 3B
Date
Engine
Teit
Fd factor
High HV
Low HV
(dicf/MMBtu)
(Btu/scO
fBtu/jcf)
4
1
8467
1206
1098
6/18/94
4
2
8467
1206
1098
2
1
8465
1206
1098
6/19/94
2
2
8465
1204
1095
2
3
8465
1204
1095
6/20/94
2
4
8465
1205
1096
11/17/95
H-10
C3-FD.WK',
-------
i-U/
TIME: 09:26
617 618 619 620
COMP NAME COMP CODE
C 6 +
PROPANE
I-BUTANE
N-BUTANE
NEO C5
IPENTANE
NPENTANE
NITROGEN
METHANE
C 0 2
ETHANE
108
102
103
104
107
105
106
114
100
117
101
rthaLlaiS TIME:
CYCLE TIME:
MODE:
LIQ VOL%
0.150
3.967
0.302
0.944
.000000
0.149
0.169
0.594
82.055
0.057
11.612
225
240
RUN
WEIGHT*
0.731
8.884
0.892
2.787
0.000
0.546
0.619
0.845
66.837
0.128
17.732
STREAM SEQUENCE: 1234
STREAM#: 3
CYCLE START TIME: 09:22
TOTALS 100.000 100.000
* @ 14.730 PSIA & UNCORRECTED FOR COMPRESSIBILITY
B.T.U.*
7.94
100.05
9.85
30.87
0.00
5.97
6.79
0.00
830.65
0.00
205.96
1198.07
REL DE
£
0.00£
0.06'
0.00.
0.016
0.00?
0.00-
0.004
0.005
0.45
0.00*
0. 120
0.68".
COMPRESSIBILITY FACTOR (1/2)
ACTUAL B.T.U. @ 14.730 PSIA & 60 DEG.
DRY B.T.U. @ 14.730 PSIA & 60 DEG.
SAT B.T.U. @ 14.730 PSIA & 60 DEG.
REAL RELATIVE DENSITY
UNNORMALIZED TOTAL
F CORRECTED FOR (1/2)
F CORRECTED FOR (1/Z)
F CORRECTED FOR (1/Z)
1.0032
1201.9
1201.9
1181.4
0.6818
100.98
DATE: 06/20/94
TIME: 20:07
617 618 619 620
COMP NAME COMP CODE
C 6 +
PROPANE
I-BUTANE
N-BUTANE
NEO C5
IPENTANE
NPENTANE
NITROGEN
METHANE
C O 2
ETHANE
108
102
10c
104
107
105
106
114
100
117
101
ANALYSIS TIME:
CYCLE TIME:
MODE:
LIQ VOL%
0.160
4.062
0.315
0.991
.000000
0.161
0.185
0.603
81.617
0.058
11.849
225
240
RUN
WEIGHT*
0.775
9.047
0.925
2.908
0.000
0.587
0.674
0.853
66.Ill
0.128
17.992
TOTALS 100.000 100.000
* § 14.730 PSIA & UNCORRECTED FOR COMPRESSIBILITY
COMPRESSIBILITY FACTOR (1/Z) '
ACTUAL B.T.U. @ 14.730 PSIA &
DRY B.T.U. « 14.730 PSIA &
SAT B.T.U. @ 14.730 PSIA &
REAL RELATIVE DENSITY
UNNORMALIZED TOTAL
STREAM SEQUENCE: 1234
STREAM#: 3
CYCLE START TIME: 20:03
J
B.T.U.*
8.46
102.45
10.28
32.39
0.00
6.46
7.43
0.00
826.20
0.00
210.16
1203.83
60 DEG. F CORRECTED FOR (1/Z)
60 DEG. F CORRECTED FOR (1/Z)
60 DEG. F CORRECTED FOR (1/Z)
H-ll
1.0032
1207.7
1207.7
1187.1
0.6856
100.30
REL DEM*
0.00'Te
0.06afc
0.006c
0 .01Tr
0.00'J?
0.004e
0.00«A£
0-00 F
0.45 -A
0.000S
0.12
0.683£
-------
DATE: 06/
iy/y4
rtNrt uiaia line..
—¦
TIME:
09
26
CYCLE TIME:
£40
STREAM«: 3
"1
617 618 619
620
MODE:
RUN
CYCLE START TIME:
03:22 1
COMP SAME
COMP CODE
i_i X Q VoL/o
WEIG
HT'-'t
E . T . U . *
REI-I
1
•'.151
. 7.33
7.37
0.;
r'F.v'r rti-.'c
102
. O0f.
. £»o*>
101.OS
o ¦.
'-BUTANE
103
0 ° ¦P.
0
. 337
1 0 . 37
.. *;
N - BUT AN E
104
e. Sol
. 830
31 .41
6.
NEO C5
107
. 030000
V*
. 000
0.00
Z.i.
T PEN'TANE
1 OL-
3. 150
. 543
e. oo
e K
::-?entahe
IO 6
o. 17:
")
. 525
6.87
-
NITROGEN
i t j
0. £32
e
. S40
0.00
O.i
METHANE
100
81.906
56
.592
£29.15
0-».
- - • w
117
0.057
0
. 127
0.00
e *
ETHANE
101
11.555
17
.309
207 _ 25
0.':
TOTALS 1^0.000 100.000
v
« @ 1*4.730 PSIA & UNCORRECTED FOR COMPRESSIBILITY
1200.11
COMPRESSIBILITY FACTOR il/Z)
ACTUAL B.T.U. @
DRY B.T.U. ®
SAT B.T.U. ®
REAL .LATIVE DENSITY
UNNORLnLIZED TOTAL
14 .*730 PSIA & 60 DEG. F
14.730 PSIA St 60 DEG. F
14.730 PSIA & 60 DEG. F
CORRECTED FOR (1/Z) =
CORRECTED FOR (1/2; =
CORRECTED FOR (1/Zl =
.0032
20:.?
203. S
133.4
.sesi
100.57
DATE: 06/19/94
TIME: 20:06
617 618 619 620
COMP NAME COMP CODE
C 6 +
PROPANE
I-BUTANE
N-BUTANE
NEO C5
IPENTANE
NPENTANE
NITROGEN
METHANE
C 0 2
ETHANE
TOTALS
108
102
103
104
107
105
106
114
100
117
101
* @ 14.730 PSIA & UNCORRECTED FOR COMPRESSIBILITY
COMPRESSIBILITY FACTOR (1/Z)
ACTUAL B.T.U. @ 14.730 PSIA
DRY B.T.U. ® 14.730 PSIA
SAT B.T.U. @ 14.730 PSIA
REAL RELATIVE DENSITY
UNNORMALIZED TOTAL
& 60 DEG. F CORRECTED FOR (1/Z)
& 60 DEG. F CORRECTED FOR (1/Z)
& 60 DEG. F CORRECTED FOR (1/Z)
1.0032
1204.4
1204.4
1183.9
0.6834
100.68
ANALYSIS TIME:
225
STREAM SEQUENCE:
1234
CYCLE TIME:
240
STREAM#: 3
MODE:
RUN
CYCLE START TIME:
20:02
LIQ V0L%
WEIGHT%
B.T.U.*
REL D1*^
0.158
0.768
8.35
0.005
4.009
8.956
101.09
0.061
0.320
0.943
10.44
0.0 6
0.971
2.859
31.75
0.0*5
.000000
0.000
0.00
0.000
0.155
0.568
6.23
0.0"13
0.177
0.647
7.11
0.0. H
0.593
0.842
0.00
0.005
81.936
66.583
829.44
0.4S:-
0.057
0.127
0.00
0.0 £
11.624
17.708
206.17
e.lvtf
100.000
100.000
1200.58
0. e'.b
H-12
-------
DATE: 06/le/94
ANALYSIS TIME:
STREAM SEQUENCE. 1234
TIME: 0E:12
CYCLE TIME:
Z43
STREAM#: ~
617 618 619 620
MODE:
RL N
CYCLE START TIME: '23:
08
COMP NAME COMP CODE
_ID VOLX
WEIGHT*/.
B1 T . U. # F,
EL DEf-
c a -- 10a
3.153
2.740
5.12
B.00f
PROFANE 102
4.274
9.473
107.79
0.06?
I-BUTANE 103
0.326
0.953
10.63
0.006
N-BUTANE 104
1.022
2.984
33.41
0.02E
NEO C5 107
.030000
0.000
0.2)0
0.206
IPENTANE 105
0.154
0. 557
6.16
0.003
NPENTANE 106
•2.180
0.653
7.23
0.004
NITROGEN 114
0.616
0.866
0 . 00
0.006
METHANE 100
81.163
65.428
£21.61
0.449
C 0 2 117
0.056
0.124
0.30
0 . 000
ETHANE 101
12.056
18.220
213.34
3.125
TOTALS
100.000
100.000
1208.S0
0.687
& 14.730 PSIA & UNCORRECTED FDR C3MPRE
3
SIBILI7Y
COMPRESSIBILITY FACTOR
(1/Z)
= 1.0032
ACTUAL B.T.U. S 14.730
PSIA ?< 60 DEG.
F
CORRECTED
FCR (1/Z) = 1212.7
DFY B.T.U. @ 14.730
PSIA t, 60 DEG.
F
CORRECTED
FOR (1/Z) = 1212.7
SAT B.T.U. e 14.730
PSIA & 63 DEG.
F
CORRECTED
FOR (1/2' = 1192.0
REAL RELATIVE DENSITY
= 0.6889
UNNORMALIZED TOTAL
» 101.26
DATE: 06/13/^4
TIME: IB:13
617 61£ 619 620
COMP NAME COMP CODE
C 6 + C;r-„
PROPANE "
I-BUTANE
N-BUTANE
NEO C5
IPENTANE
NPENTANE
NITROGEN
METHANE
C 0 2
ETHANE
TOTALS
108
102
.103
.104
:L07
:L05
106
J. 14
100
117
101
ANALYSIS TIME:
CYCLE TIME:
MDDE:
lid vol:-: v
a. 154
3. 351
0.301
0.925
.000000
0.151
0.175
0.619
82.343
0.058
11.425
100.000
225
240
RUN
WEIGHT'/.
0.753
8.648
0.891
2. 737
0. 000
0. 555
0.641
0.882
67.267
0.129
17.496
100.000
@ 14.730 PS IA t< UNCORRECTED FOR COMPRESSIBILITY
COMPRESSIBILITY FACTOR (1/Z)
ACTUAL B.T.U. e 14.730 PSIA
DRY B.T.U. 0 14.730 PSIA
SAT B.T.U. @ 14.730 PSIA
REAL RELATIVE DENSITY ,
UNNORMALI ZED TOTAL
STREAM SEQUENCE: 1234
STREAM#: 3
CYCLE START TIME: 18:09
B.T.U.*
8 . 14
97.11
9.82
30.23
0.00
6.06
7.01
0.00
833. 56-
0.00
202.64
1194.57
& 60 DEG. F CORRECTED FOR
«< 60 DEG. F CORRECTED FOR
it 60 DEG. F CORRECTED FOR
H-13
(1/2).
(1/Z)
(1/Z)
i.0031
-1198.3
1198.3
1177.9
¦-0.6798
1<|0.57
REL DEN^
i
0.005J
0.0585
0.0060
0.0186
0.0000
0.0038
0.0043
Q-0Q6Q
0.4561
0.0009
0.1186
k
0.678
-------
Campaign 4 Fuel Analyses
Sample Date
8/23/94
8/24/94
8/26/94
8/27/94
8/28/94
8/29/94 +
8/30/94 +
Average
Methane (mol%)
93.2940
93.1060
93.8620
93.5120
93.2740
89.9110
87.2560
93.4096
Ethane (mo!%)
2.82600
2.90000
2.53600
2.52200
2.74100
2.52500
2.45400
2.70500
Propane (mol%)
0.38300
0.45200
0.35500
0.41000
0.45400
0.41000
0.35100
0.41080
iso-Butane (mol%)
0.04259
0.04730
0.03611
0.04741
0.04689
0.04304
0.02300
0.04406
n-Butane (mol%)
0.07615
0.08192
0.05487
0.07920
0.07286
0.06869
0.04800
0.07300
iso-Pentane (mol%)
0.02177
0.02464
0.01734
0.02333
0.01412
0.02198
0.02200
0.02024
n-Pentane (mol%)
0.01902
0.02262
0.01503
0.02024
0.01081
0.01894
0.02200
0.01754
C6 plus (mol%)
0.03330
0.03208
0.02363
0.03334
0.01369
0.02921
0.02500
0.02721
C02 (mol%)
0.47100
0.71100
0.77700
0.71100
0.67800
0.69400
0.73700
0.66960
02 (mol%)
0.13700
0.16300
0.12900
0.19800
0.20300
0.82800
1.96800
0.16^00
N2 (mol%)
2.69500
2.45900
2.19400
2.44300
2.49100
5.45000
7.09400
2.45640
Real HHV, BTU/ft ~ 3
1011.2
1012.9
1009.4
1009.1
1009.7
971.8
940.7
1010.5
Real LHV, BTU/ft ~ 3
911.4
913.1
909.7
909.5
910.1
875.9
847.8
910.8
Specific Gravity
0.5924
0.5952
0.5907
0.5930
0.5934
0.6083
0.6202
0.5929
+ Sample appears to have been improperly purged; therefore, excluded from average.
-------
The Gas Company-
togiwln P^Km<
September 12,1994
Larry Ogle
Radian Corporation
Box 201088
Austin, Texas 76720
MtSmg.idJmi-
Bat 12*1
CA
9003IJW
D»ar Larry,
Attached are the hydrocarbon gas analysis results for seven of the eight samples
samples were analyzed using a HP 5880 gas chromatograph (GPA Standard
22:61-90). Daily calibration checks were performed to assure quality.
The Unit #8 sample collected by WCG at 2:00 PM on 8/30/94 was not received
until 9/6/94 and was empty (< 1 mole % hydrocarbons) when we analyzed the
sample and therefore not reported.
Aliso, the Unit #4 sample was not received until 9/6/94. The Unit #4 sample may
have leaked due to the high level of inerts (* 10 mole %). This was verified by
subsequent analyses of the sample.
The sample cylinders will be vented and sent to your attention at 8501 N. Mopac,
Austin, Texas 78759.
If you have any questions, please call at (310) 806-4364.
submitted to
during August 22 - Sept 7. All of the
Sirioerely,
Dan Meltzer
Senior Engineer
cc: Gregg A. Arney
John A. Thompson
Deanna Haines
(w/o attachments)
(w/o attachments)
H-15
-------
ENGINEERING ANALYSIS CENTER
BTU Content of Natural Gas by Gas Composition
PROJECT NO.
REPORTED BY-
REPORT DATE:
TEST LOCATION:
SAMPLE DATE:
GRI4-CAN-01
S. RAZZAK
I WAUKESHA ENGINE
8/23/94 13:45
gRSsagSa
BUiszgi
III
a»ir
Pi
asqtgMoaBg
METHANE
93.29400
imo.o
0JS39
942.3
848.4
05168
ETHANE
2.82600
1769.6
1618.7
1.0382
50.0
43.7
0.0293
PROPANE
038300
2516.1
2314.9
U226
9.6
8.9
0.0058
iso-BUTANE
0.04299
3251.9
300M
2.0068
1.4
1.3
0.0009
n-BUTANE
0.07615
32623
3010.8
2.0068
2.5
Z3
0.0015
iao-PENTANE
0.02177
4000.9
3699.0
24910
0.9
0.8
0.0005
n-PENTANE
0.01902
4008.9
3706.9
2.4910
0.8
0.7
0.0005
C6 plus
0.03330
5194.6
4411.1
3.2521
1.7
1.5
0.0011
CARBON DTOXIDE
0.47100
0.0
0
1.5196
0.0
0.0
0.0072
OXYGEN
0.13700
0.0
0
1.1048
0.0
0.0
0.0015
NITROGEN
2.69300
0.0
0
0.9672
0.0
0.0
0.0261
TotaJU
100.00
1009.1
909.6
0.5912
(4) Compressibhiy Factor (Z) for mixed gases
Total Non-Hydrocarbons
A - (Total 5G)(0.0101)
B - (ToUl Non-HQ(.0070)
3.3
0.00597
0.00023
Z - 1.00369 - A + B
0.99795
(5) Adjusted Values (14.73 psk, 60F, Grow, Dry, real volume basis)
HHV
1011.2 BTU/real cubic fool
LHV
911.4 BTU/real cubic foot
Specific Gravity
0.5924
FOOTNOTES
(1) Higher Heating Value per ideal cubic foot 6 14.696 ptia
Gas Processors Association (GPA) Standard 2145-94
(2) Lower Heating Value par ideal cubic foot 9 14.696 psia
Gas Processors Suppliers Association (GPSA) Vol. II - See. 23 - Fig.23-2 (1987)
(3) Specific Gravity
Gas Processors Association (GPA) Standard 2145-94
(4) Empirical formula for compressibility factor
American Gas Association's 'transmission Report N'o. 5.
(5) Values are adjusted to reflect real volumes rather than ideal
volumes by dividing by the compressibility factor.
ex; (BTU/Ideal Gas Volume)/Z whpn» Z«(Real Gas Volume/Ideal Gas Volume)
H-16
-------
ENGINEERING ANALYSIS CENTER
BTU Content of Natural Gas by Gas Competition
PROJECT NO.
RETORTED BY:
REPORT DATE:
TEST LOCATION:
SAMPLE DATE:
CRI4-CAN-04
S. RAZZAK
8/31/9*
\ WAUKESHA FUEL Ol«S
8/24/94 12:45
cSHfSSSz
smss
KjMjiiiWjijjs:
pPTHANE
93.10600
1010.0
9094
0J539
940.4
846.7
0.5157
Ethane
2.90000
1769.6
1618,7
1J)382
51.3
46.9
00301
; PROPANE
0.45200
2S16.1
2314.9
1.5226
11.4
10.5
0.0069
iso-BUTANE
0.04730
3251.9
30004
2.0068
1JS
1.4
0.0009
n-BUTANE
0.08192
32623
30104
2.0068
17
2.5
0.0016
iso^l'ENTANE
0.02464
4000.9
3699JO
2.4910
1.C
0.9
0.0006
n-PIiNTAN'E
0.02262
4008.9
3706.9
2.4910
0.9
0.8
0.0006
C6 plus
0.03208
5194.6
4C11.1
12521
1.7
1.4
0.0010
CARBON DIOXIDE
0.71100
0.0
0
L5196
0.0
0.0
aoios
OXYGEN
0.16300
0.0
0
1.1048
0.0
0.0
0.0018
NITROGEN
2.45900
0.0
0
0.9672
0.0
0.0
0.0238
Totals —>
100.00
1010.8
911.2
0.5939
(4) Compressiblity Factor (Z) for mixed gi
Total Non-Hydrocarbons
A * (Total SGX0 0101)
B - (Tota] Non-HQ(.0070)
3.3
0.00600
0.00023
Z - 1.00369 A + B
0.99792
(5) Adjusted Values (14.73 piia, 60F, Grot, Dry, real vohane baas)
HHV
1012.9 BTU/real cubic fool
LHV
913.1 BTU/real cubic fool
SpedCic Gravity
0.5952
FOOTNOTES
(1) Higher Heating Value per ideal cubic foot 914.696 piia
Gas Processors Association (CPA) Standard 2145-94
(2) Lower Heating Value per ideal cubic foot A 14.696 jnfa
Gas Processors Suppliers Association (GPSA) Vol. II - Sec. 23 - Fig.23-2 (1987)
(3) Specific Gravity
Gas Pirocessorsi Association (CPA) Standard 2145-94
(4) Empirical formula for compressibility factor
American Gas Association's Transmission Report No. 5.
(5) Values «e adjusted lo reflect real volumes rather than ideal
volumes by dividing by the compressibility factor.
cx; (BTU/Ideal Gas Volume)/Z where Z*(Reol Gas Volume/Ideal Gas Volum*)
H-17
-------
ENGINEERING ANALYSIS CENTER
BTU Content of Natural Go* by Gas Composition
* ir
PROJECT NO:
REPORTED BY:
REPORT DATE:
TEST LOCATION:
SAMPLE DATE;
GRI4-CAN-Q5
S. RAZZAK
8/31/94
~ COOPER ENGINE UlPPMHHfc*'#®
8/26/94 10:00
i|aj
fPP
METHANE
93.86200
1010.0
909.4
0.5S39
948.0
853.6
05199
ETHANH
2J3600
1769 Ji
1618.7
1.0382
44.9
41.1
0.0263
PROPANE
0.35500
2516.1
2314.9
1.5226
8.9
8.2
0.0054
iso-BUTANE
0.03611
3251.9
30004
2X068
1.2
1.1
0.0007
n-BUTANE
-0.05487
3262.3
3010.8
2.0068
1.8
1.7
0.0011
iao-PENTANE
0.01734
4000.9
3699.0
2.4910
0.7
0.6
0.0004
n-PENTANE
0.01503
4006.9
3706.9
24910
0.6
0.6
0.0004
C6 plus
0.02363
51944
4411.1
3.2521
1.2
1.0
0.0008
CARBON DIOXIDE
0.77700
0.0
0
L5196
0.0
o.u
0.0118
OXYGEN
0.12900
0 JO
0
1.1048
0.0
0.0
0.0014
NITROGEN
2.19(00
0JD
0
0.9672
0.0
0.0!
0.0212
Totals >
100.00
1007J
907.8
03895
Total Non-HydrocarbonG
A - (Total SGX0.0101)
B - (Total Nor-HC)(.0070)
3.1
0.00595
0.00022
Z - 1.00369 - A + B
0.99795
(5) Adjusted Values (14.73 psia. 60F, Gtoct, Dry, real volume basis)
HHV
1009.4 BTU/real cubic foot
LHV
909.7 BTU/real cubic foot
Specific Gravity
05907
FOOTNOTES
(1) Higher Heating Value per ideal cubic foot 614.696 paia
Gas Processors Association (GPA) Standard 2145-94
(2) Lower Heating Value per ideal cubic foot 6 14.696 psia
Gas Processors Suppliers Association (GPSA) Vol. II - Sec. 23 - Fig.23-2 (1987)
(3) Specific Gravity
Gas Processors Association (CPA) Standard 2145-94
(4) Empirical formula for cotnpmiibiltty factor
American Gas Association's Transmission Report No. 5.
(5) Values are adjuated to reflect real voluinei xather than ideal
volumes by dividing by Lhe compressibility factor.
ex; (BTU/Ideal Gas Volumr)/Z where Z"(Reil Gas Volume/Ideal Gas Volume)
H-18
-------
ENGINEERING ANALYSIS CENTER
BTU Content of Natural Gas by G«t Composition
PROJECT NO;
REPORTED BY:
REPORT DATE.
TEST LOCATION.
SAMPLE DATE:
CRM-CAN-06
S. RAZ2AK
8/31/94
8/27/94 1235
IINGERSOLL #9 W/F«»Fl»ii£*$(METHANE)
METHANE ' 9351200
ETHANE 232200
PROPANE 0.41000
fcw-BOTANE 0.04741
n-BUrANE 0.07920
W.-P1LMTANE 0.02333
n-PENTANE 0.02024
C6 pirns 0.03334
CARBON DIOXIDE 0.71100
OXYGEN 0.19600
NITRiDGEN 2.44300
10104
17694
2516.1
3251.9
326X3
4000.9
4008.9
5194.6
OX
0.0
0.0
9094
1618.7
2314.9
30004
30104
3699.0
3706.9
4411.1
0
0
0
03539
1.0382
15226
24068
24068
24910
24910
3JS21
1.5196
1.1043
0.9672
944.5
444
10.3
1.5
2.6
0.9
0.8
1.7
0.0
0.0
0.0
850.4
404
93
1.4
2A
0.9
0.8
1.5
0.0
0.0
0.0
0.5180
0.0262
0.0062
0.0010
0.0016
0.0006
0.0005
0.0011
0.0106
0.0022
0.0236
Totalis
100.00
1007.0
907.6
0.9917
Totnl Non-Hydrocarbon*
A - (Total SC)(0.0101)
B - (Total Non-HCX-0070)
3.4
0.00598
0.00023
Z - 1.00369 - A ~ B
0.99795
(5) Adjusted Values (14.73 psia, 60F, Grma, Dry, real volnme basis)
HHV
1009.1 BTU/raal cubic foot
LHV
9093 BTU/real cubic foot
Specific Gravity
03930
FOOTNOTES
(1) Hijfher Heating Value per Ideal cubic foot • 14496 piia
Gas Pioces9ora Association (CPA) Standard 2145-94
(2) Lower Heating Value per Ideal cubic foot • 14496 paia
Cas Piocessors Suppliers Association (CPS A) VoL II - Sec. 23 - Fig.23-2 (1987)
(3) Specific Gravity
Gas Processors Association (GPA) Standard 2145-94
(4) Empirical formula for compressibility factor
American Cas Association's Transmission Report No. 5.
(5) Values are adjusted to reflect real volumes rather than ideal
volume by dividing by the compressibility factor.
c*; (BirU/Idcal Cas Volume)/Z where Z'(Raal Cas Vohune/ldeol Cas Volume)
H-19
-------
ENGINEERING ANALYSIS CENTER
BTU Content of Natural Gas by Ga? Come
PROJECT NO
REPORTED BY:
REPORT DATE:
TEST LOCATION:
SAMPLE DATE:
GRI4-CAN-12
S.RAZZAK
8/31/94
INGERSOLL #9 W/9M9MS«IM(ftlErHANE)
8^«794 1340
ISSSmBI
S55&5*»53£
gjjjpal
dSSSttsS
METHANE
93.27400
1010.0
90M
0.5539
942.1
848.2
05167
ETHANE
2.74100
1769.6
1618.7
1.0382
483
44.4
0.0285
PROPANE
0.45400
2516.1
2314.9
15226
11.4
105
aoo«
iso-BUTANE
0.04689
3251.9
30004
24066
15
1.4
0.0009
n-BUTANE
0.07286
3262J
3010.8
241068
2.4
22
0.0015
iso-PENTANE
0.01412
4000.9
3699.0
14910
0.6
05
0.0004
n-PENTANE
0.01081
4008.9
3706.9
24910
0.4
0.4
0.0003
C6pius
0.01369
5194.6
4411.1
3.2521
0.7
0.6
0.0004
CARBON DIOXIDE
0.67800
0.0
0
15196
0.0
0.0
0.0103
OXYGEN
0.20300
0.0
0
L1048
0.0
0.0
0.0022
NITROGEN
2.49100
ox
0
0.9672
0.0
0.0
0.0241
Total* —>
100.00
10Q7.6
908.2
05921
(4) Compreasiblity Factor (Z) for mixed gates
Total Non-Hydrocarbons
A - (Total SG)(0.0101)
B - (Total Non-HC)(.0070)
3.4
0.00598
0.00024
Z -1.00369 - A + B
0.99795
HHV
—,
1009.7 BTU/real cubic foot
LHV
910.1 BTU/real cubic fool
Specific Gravity
0.5934
FOOTNOTES
(1) Higher Heating Value per ideal cubic foot •14.696 pita
Go* Processors AasocwUon (CPA) Standard 2145-94
(2) Lower Heating Value per ideal cubic foot 9 14.696 ptii
Gas Processors Suppliers Association (GPSA) VoL II - Sec. 23 - Fig.ZV2 (1987)
(3) Specific Gravity
Gas Processors Association (GPA) Standard 2145-94
(4) Empirical formula for compreailbility factor
American Gas Association's Transmission Report No. 5.
(5) Values are adjusted to reflect real volumes oather than ideal
volumes Wy dividing by tb<> compressibility factor.
ex; (BTU/Ideal Gas Vr»lume)/Z where Z"(Renl Gas Volume/Ideal Gas Volume)
H-20
-------
ENGINEERING ANALYSIS CENTER
BTC
PROJECT NO:
REPORTED BY:
REPORT DATE:
TEST LOCATION
SAMPLE DATE:
§m&gs
agss
¦TTiiir^
:^aaa»n!
Hi
|§f(g||§|
WmSS
METWiNE
87.25600
I0I0J
9094
0J539
SSIJ
793.5
0.4833
ETHANE
2.45400
1769.4
1618.7
1.0382
43.4
39.7
0.0255
PROPANE
0.35100
1516.1
Uli)
m
8.8
1.1
0.005.1
iso-BUTANE
0.02300
3251.9
3000.4
].NM
a7
0.7
O.OOOJ
n-BUl/iNB .
0.04800
32S2J
39I0J
2.0061
1.6
1.4
0.0010
ito-PENTANE
0.02200
4000.9
3699.0
2.4910
0.9
0.1
0 0005
n-PENTANE
0.02200
4001.9
3706.9
2.4910
0.9
a<
0.0005
C6pha
0.02500
9194.6
4411.1
3.2SJ1
1.3
11
0.0008
CARBON DIOXIDE
0.73700
0.0
0
1.5196
0.0
0.0
0.0112
OXYGEN
1.96800
0.0
0
1.1041
0.0
0.0
0.0217
NITROGEN
709400
0.0
0
0.9672
0.0
0.0
0.0686
Totals »
100.0000
931.9
846.2
06190
OWToliJ
S.RAZZAK
9tV94
ATION UNIT #4
«MHWWIll
8/3 (V94 a 11:10
WCG
Total Nos-Hydrocarboiis
A "(Total SGK0.0101)
B -(TotiJ Non-HCX-0070)
9.8
0.00625
0.00069
Z- 1.00369-A + B
0.99812
(5) Adjusted Values U 4 7 3 psia. 60F. Gross. Dry, tcm! volume bagia)
HHV
940.7 BTU/rea) cubic foot
LHV
>47.8 BTU/rcal cubic foot
Specific (iravity
0.6202
FOOTNOTES
(1) Hither Haatlat Value per Ideal cubic fort ® 14.696 paia
Cu Processors Association (GPA) Standard 2M5-94
(2) Lewtr Heating Vaiie per Ideal cabit foot @ 14.696 ptia
lias Processors Supplier! Association (GPSA) Vol. II. Sec 23 - Fij.23-2 (19t?)
(3) Specific Gravity
Gu Processors Association (CPA) Standard 2145-94
(4) Empirical formula for compraatlbiltty factor
American Gu Association's Transmission Report No. 5.
(5) Valuer are adjusted to rclkct ml volumes ratber thai ideal
volumes hy dividing by (he compressibility factor.
ex, (BTU/ldeal Gas Volume VZ where Z^Real Gas Volume/Ideal Gas Volume)
H-21
-------
ENGINEERING ANALYSIS CENTER
BTU Content of Natural Gas by Gas Composition
PROJECT NO:
REPORTED BY:
REPORT DATE:
TEST LOCATION:
SAMPLE DATE:
GRI4-CAN-15
S. RAZZAK
8/31/94
8/29/94 0».4~
> INGERSOLL *9 W/SCI»fii£LGA8.<
HH
gjisSBSSS
m
METHANE
89.91100
1010.0
909.4
05539
908.1
817.7
0.4980
ETHANE
2J2500
1769.6
1618.7
1JUS82
44.7
40.9
0.0262
PROPANE
0.41000
2516-1
2314.9
1322b
10.3
9J
0.0062
iso-BUTANE
0.04304
3251.9
30004
ZJOOU
1.4
1.3
0.0009
n-BUTANE
0.06869
32623
30104
2.0068
2.2
2.1
0.0014
iso-PENTANE
0.02198
4000.9
9699.0
2.4910
0.9
0.8
0.0005
n-PENTANE
0.01894
4008.9
3706.9
2.4910
0.8
0.7
0.0005
OS plus
0.02921
5194^
4411.1
3.2521
1J
1.3
0.0009
CARBON DIOXIDE
0.69400
0.0
0
1-5196
0.0
0.0
0.0105
OXYGEN
U.82800
0.0
0
1.1048
0.0
0.0
0.0091
NITROGEN
5.45000
0.0
0
0.9672
0.0
0.0
0.0527
Totala ——>
100.00
969.9
874.2
0.6071
(4) CompresaibHty Factor (Z) for mixed b»«m
Total Non-Hydrocarbons
A - (Total SG)(0.0101)
B - (Total Non-HC)(.0070)
7.0
0.00615
0.00049
Z ¦ 1.00369 - A + B
0.99805
HHV
971.8 BTU/real cubic foot
LHV
875.9 BTU/leal cubic foot
Specific Gravity
0.6083
FOOTNOTES
(1) Higher Healing Value per ideal cubic foot • 14.696 paia
Gas Procaisors Association (CPA) Standard 2145-94
(2) Lower Heating Value per ideal cubic foot 8 14.696 paia
Gas Processors Suppliers Association (GPSA) Vol. II - Sec. 23 - Fig.23-2 (1987)
(3) Specific Gravity
Gas Processors Association (GPA) Standard 2145-91
(4) Empirical formula far compxeaaibnity factor
American Gas Association's Transmission Report No. 5.
(5) Value* are adjusted to reflect real volumes rattier than ideal
volumes by dividing by the compressibility factor.
ex: (BTU/Ideal Gas Volums)/Z where Z»(Re»l Gas Volume/Ideal Gas Volume)
H-22
-------
A
Page # 1
CERTIFICATE OF ANALYSIS NO. 228192
Company :
RADIAN CORP.
Source :
Ingersoil #9 W/SCR
Sample of :
Fuel Gas
Sampled By:
LD of Radian Date:
08/29/94
Remarks :
GRI4-CAN-16; Radian
Lab. #2
For :
RADIAN CORPORATION
Test By G.C
GPA Method 2261
Factors 3
Analysis:
Mol %
Nitrogen
0.443
Carbon Dioxide
0.610
Methane
95.587
Ethane
2.703
Propane
0.463
i-Butane
0.056
n-Butane
0.056
i-Pentane
0.020
n-Pentane
0.016
Hexane Plus
0.046
100.000
Factors From 6PA-2145, Jan. 01, 1994
6PM at 14.650 psla
0.719
0.127
0.018
0.018
0.007
0.006
0.020
0.915
0.5830
0.5840
Specific Gravity at 60 Deg. F (air-1) Perfect Gas ..
Real Gas
Calculated Molecular Weight ... 16.88
Calculated Gross B.T.U. / Cu. ft at 14.650 psia and 60 Deg. F
Perfect Gas
Real Gas:
Normal Hexane
Benzene
Ethyl Benzene
Toluene
Xylenes
Dry basis
Saturated basis .
Deviation Factor.
Dry basis
Saturated basis .
Wt. I
0.023
0.001
*0.001
* 0.001
<0.001
1030
1012
0.9978
1032
1014
H-23
-------
—————Page # 2
CERTIFICATE OF ANALYSIS NO. 228192
Calculated Net B.T.U. / Cu. ft at
Perfect Gas Dry basis
Saturated basis .
Deviation Factor.
Real Gas
Dry basis
Saturated basis
14.650 psia and 60 Deg. F
928
912
. 0.9978
930
914
Southern Petroleum Laboratories, Ins.
H-24 ' /
-------
Page 1
Company:
Sample of:
Sample by:
Sample date:
Remarks:
For:
CERTIFICATE OF ANALYSIS NO. 228192
RADIAN CORP.
Fuel Gas
LD of Radian
08/29/94 at 9:45
GRI4-CAN-16; Radian Lab.
#2
RADIAN CORPORATION
September 26, 1994
Normalized to 100.00%
Components Listed In Chromatographic Order
Component
Mole %
Weight %
Nitrogen
0.443
0.734
Carbon Dioxide
0.610
1.589
Methane
95.587
90.801
Ethane
2.703
4.812
Propane
0.463
1.210
i-Butane
0.056
0.194
n-Butane
0.056
0.194
i-Pentane
0.020
0.087
n-Pentane
0.016
0.067
2,2-Dimethylbutane
0.001
0.003
2,3-Dimethylbutane
0.001
0.003
4-Methyl-c-pentene-2
0.001
0.004
2-Methylpentane
0.004
0.021
3-Methylpentane
0.002
0.012
n-Hexane
0.005
0.023
2,2-Dimethylpentane
0.000
0.001
Methylcyclopentane
0.002
0.011
2,4-I'imethy lpentane
0.000
0.001
Benzene
0.000
0.001
Cyciohexane
0.003
0.013
2-Me~hylh«xane
0.001
0.006
2,3-Dimethylpentane
0.000
0.002
1,1-Dimethylcyclopentane
0.000
O.OOl
3-Methylhexane
0.001
0.006
3,4-Dimethyl-c-pentene-2
0.000
0.002
lc, 3-Dime1:hylcyclopentane
0.000
0.001
It,2-Dimethylcyclopentane
0.000
0.002
n-Heptane
0.002
0.009
Methylcyclohexane
0.003
0.018
3,4-Dimethylhexane
0.000
0.002
lc,2t,3-Trimethylcyclopentane
0.000
0.002
3-Ethylhexane
0.001
0.003
n-Octane
0.000
0.002
n-Nonane
0.000
0.001
H-25
-------
Page 2
CERTIFICATE OF ANALYSIS NO. 228192
Component
Mole %
Weight
n-Decane
0.000
0.002
1-Methyl-2-i-propylbenzene
0.000
0.001
Unknown IC11
0.000
0.002
Unknown IC11
0.000
0.003
Unknown IC11
0.001
0.007
1,2-Dimethyl-4-ethylbenzene
0.001
0.007
Unknown IC11
0.000
0.002
Uhknown IC11
0.000
0.001
1,i-Dimethyl-3-ethylbenzene
0.000
0.002
1-Ethyl-2-±-propylbenzene
0.000
0.001
n-Undecane
0.010
0.090
1-Ethyl-4-i-propylbenzene
0.001
0.008
(2-Methylbutyl)benzene
0.002
0.013
1,2,3,5-Tetramethylbenzene
0.000
0.003
1-t-Butyl-2-methylbenzene
0.000
0.001
A2
0.001
0.005
Unknown IC12
0.000
0.004
A3
0.000
0.002
A4
0.000
0.003
1-Methyl-3-n-butylbenzene
0.000
0.002
1,3-Di-i-propylbenzene
0.000
0.003
l-Methyl-2-n-butylbenzene
0.000
0.001
1,2,3,4-Tetrahydronaphthalene
0.000
0.001
Naphthalene
0.000
0.002
100.000
100.000
H-26
-------
CORfORATIO
Chain of Custody Record
r '
Pago
of
PROJE^y
r- n ~t" _ ' 11
1-7 Wi/O^uyv T
COLLECTED BY (9ian»tute)
K&AA^r Ko^ycfc----
FIELO SAMPLE I D.
SAMPLE MATRIX
c,m-pir)i- 10
B
cittntf^ ,F/£^V
WoUry
DATE/TIME
go 1-94
T/WTttTTT
SAM ID NO.
REMARKS (tor lab use only)
i
K)
I I
I
J»K> .
a
13
&L
r^Lc
5T3;
imr
iuii
ToP r
7
7
•>/
7
ft
. „ T7oT3
PUjux. Tki ML, (L+<
li
y/
/
V.
) t
y-^y-9^
/
7
Fju*&*yv UefCJjuL
Ji
hTFT
"S
JJL
i.
<^t»^ -cJcy
>Uk
—5 vm it
REMARKS , ' ' O fl
Be CtXAt&uiL/ jl/c^ tOCA^i^ fljJttiAj Ccyy-^cn^-rto^
RELINQUISHED BY:
DATE
TIME
OPJl)
RECEIVED BY:
DATE TIME RELINQUISHED BY:
DATE TIME RECEIVED BY:
DATE TIME
RELINQUISHED BY:
DATE
TIME
LABUSE ONLY
El TIMS|THK"C|
phjaMb
T)M6
//CO
AIRBttX NO.
$CAL#
*)0w
CONDITIO#
l£
*
-------
RADIAN
CORPORATION
Canist?'
tScWC
AUSVOC
Chain of Custody
Project: (^^
(TM» FPAS
TBA)
To Br Completed By Field Sample
Date:
vField ID:
~
Sample^Coilected:'
Sampling Site:
OVA Reading (Peak):
Sampler's Initials:
Type of Sample (Circle onef. Ambient o soint Source
C,^4-C4M-07,
-^tarfTir^., D
UnmlbsU. f/el a$kj-TVtl H\tM-T
(Routine J6up ^ Blank)
End Timar / ^ ! Iff
kv /hdu^JL,
o Be Compleled By Lab (Part One)
1. Canister cleaned
2. Canister blanked
3. Canister humidified
4. Canister reblanked
5. Canister evacuated
6. Canister shipped
7. Canister received
8. Analysis completed
9. Sample discarded
Data/lnit.
&nz,-±
'JL=Cl
f'&+
£'
cA
Value
(ppbV-C)
10
Initial Lab VFR #
Pressure
— /V^29/
< ' PSIG Cleaned: .
APL - //¦fg .PSIG Blanked: .
APF - w./*- _PSIG Calibrated:.
APL - APF --Q lcJ psiG Turns - .
mL/min ¦
Date/lntt.
o Be Completed By Lab (Part Two)
Parameter
Dilution 1
Initial Pressure
Final Pressure
-j.Um _
Add DilutenvfHpAir, N.) ^/- ,J_
- - ^ 0.37
-------
RADIAN
COB»OBATIOM
/
Canister
n*'
AUSVOC
Chain of Custody
¦»
Project:.
(TM \ FP,
*
FPAS
TEA)
Ord* One;
Field ID:
Sample Collected:
Sampling Site:
OVA Reading (Peak):
Sampler's Initials:
Dup Blank)
G>fcT4-LftAj-0/a Routine) Dui_
•»«~« Rn.rtTinr.A- 15 / "Z-O Pnrf Tima- I ^
(ii^Jp/rfcai£.V)L - &Atcl CAkiifT
Type of Samplfl (Circle oney. Amhi»nt^ir*Point ^urcetefybify):
Field Pressures (POIQ
Comments: SOW?/t
!
*
m
333
Date/lnlt.
1. Canister ileariBd
2. Canister blanked
3. Ca^ster humidified
4. Canister reblanked
5. Canister evacuated
6. Canister shipped
7. Canister received
8. Analysis completed
9. Sample discarded
Value
(ppbV-C)
Initial Lab
Pressure
VFR #
Da
m&r?-
c<
-/Y//T. _ PSIG Cleaned:
-pfr
_PSIG Blanked: _
v'T fc- PSIR Calibrated:.
APL
APF
APL - APF - Q.Of PSIG Turns -
mL/min
e/lnit.
To Be Completed By Lab (Part Two)
Parametur
Dilution 1
Initial Pressure
Final Pressure
- W. /rM .
- v);
FINAL Dilution Factor
Dilution Date
Dilution Time
Initials
M
W
Dilution 2
REPORT
H-29
Dilution 3
DHutton 4
-------
C0«»e*«TIOM AUSVOC
*?/ Chain of Custody
Canister #• f & < Project:
FPAS TBA)
'¦ \t J
lo fie Completed By Field Sampler
i
V
/ft
Circt* On*:
Field ID: L ' rsfej5/-c'4/U'6t
^(Routine) Pup Blank)
Sample Collected: Date: . Start Time* >',yr . End Time:
Sampling^Brte:
11 C^. ' C-CL-f
OVA Reading (Peak): """
Sampler's Initials:
Type of Sample (Circle onef. Ambient c lint Sourgp*(ipecify):
1&5&
Field Pressures (PSIQ): Comments: "7^0 of^>
(h^ yluA- . '
^ rn^Mrg^ fjuti f yns
o Be Completed By Lab (Part One)'
Date/lnit.
1. Canister cleaned
2. Canister blanked
3. tanister humidified
4. Canister reblanked
5. Canister evacuated
6^ Canister shipped
7. Canister received
8. Analysis completed
9. Sample discarded
Hit-ther
OriiBl/Z^Z
Value
(ppbV-C)
javy
Initial LJb
Praakura
- K
APL - //--jf?
APF 2 // -^°
VFR#
APL - 4PF
PSIG Cleaned: .
PSIG Blanked: .
PSIG Calibrated:.
6. Of PSIG Turns - .
mL/min ¦
Date/lnit.
To Be Completed By Lab (Part Two)
Parameter
Initial Pressure
Final Pressure
Add Diiutei
Vufcon Facl
- iNAL Dilution Facte*
Dilution Date
Dilution Time
Initials
Dilution 1
- /'/.WW
- j. S-r //IT
Dllutiorvf
Dilution 3
Dilution 4
io< fHe^ir, N.)
2i.zo#/tf "77
&oT
itinrv Fartrv
we*/
r/Yj
REPORT
H-30
-------
08/3J/S4 10i2«ill
BKMtiwnaorr xkvorm&tiob phockbsipo stbtkm (mips) pmi x a
BTU FOVT2HB BOOK RKPORT
08/01/94 TO 08/31/94 Q-
<<7TKN in, 247:l CDSTOKtJt XDi BOCAI/n8
ID Lilb eff«ctlT« D«t* Bet laortd BTO BOV CDJ M XXTKUB
: w¦ ^ ¦¦¦¦¦¦¦
10409 MGAC-A. 08/01/94 08/01/94 0S/09/94 1043 0.603 1.16 1.04 93.(9
(10690 «J\C A. 08/09/94 08/09/94 OS/17/94 1040 0.601 1.1 J 1.10 93.(4
•*« ERO OP RliTORT »»*
X n
w a
I—*
?
N
n
H
f>J
fij
0
1
vH
I
n
OJ
i
s
-------
Page # 1
H.4 Campaign 5
Company
Source
Sample of : Natural Gas
CERTIFICATE OF ANALYSIS NO. 229244
RADIAN CORP.
Field: Turbine Fuel Gas Test # 3
Sampled By: JM of Radian Date: 10/05/94 Time: 14:50
For : RADIAN CORPORATION
Test By G.C. GPA Method 2261 Factors From GPA-2145, Jan. 01, 1994
Analysis:
Mol %
GPM at 14.696 psia
Nitrogen
Carbon Dioxide
Methane
Ethane
Propane
i-Butane
n-Butane
1.278
0.057
95.346
3.100
0.197
0.010
0.012
100.000
Specific Gravity at 60 Deg. F (air=l) Perfect Gas
Real Gas
0.827
0.054
0.003
0.004
0.888
0.5770
0.5780
Calculated Molecular Weight .
16.71
Calculated Gross B.T.U. / Cu. ft at 14.696 psia and 60 Deg. F
Perfect Gas Dry basis ... 1024
Saturated basis ... 1006
Real Gas
Deviation Factor... 0.9979
Dry basis ... 1026
Saturated basis ... 1008
Wt%
Normal Hexane
Benzene
Ethyl Benzene
Toluene
Xylenes
<0.001
<0.001
^0.001
zO.OOl
^0.001
H-32
-------
Page 1
Company:
Sample of:
Sample by:
Sample date:
For:
V
Component
CERTIFICATE OF ANALYSIS NO. 229244
RADIAN CORP.
Natural Gas
JM of Radian
10/05/94 at 14:50
RADIAN CORPORATION October 19, 1994
Normalized to 100.00%
Components Listed in Chromatographic Order
Mole %
Weight %
Nitrogen
1.278
2.142
Carbon Dioxide
0.057
0.150
Methane
95.346
91.532
Ethane
3.100
5.578
Propane
0.197
0.520
i-Butane
0.010
0.035
n-Butane
0.012
0.042
i-Pentane
0.000
0.001
n-Pentane
0.000
0.001
2-Methylpentane
0.000
0.000
3-Methylpentane
0.000
0.000
n-Hexane
0.000
0.000
100.000
100.000
H-33
-------
Page # 2
CERTIFICATE OF ANALYSIS NO. 229244
Calculated Net B.T.U. / Cu. ft at 14.696 psia and 60 Deg. F
Perfect Gas Dry basis ... 922
Saturated basis ... 906
Deviation Factor.
0.9979
Real Gas
Dry basis
Saturated basis
924
908
Southern Petroleum Laboratories, Inc.
H-34
S
-------
>hajp of Custody Record
Page.
(aw* *3
NO. OF CONTAINERS
mm m
/////////
SITE •
COLLECTED BY (S/pntfurajQ rfi, VCvX >-
/
FIELD SAMPLE I D. SAMPLE MATRIX DATE/TIME
/ SAM ID NO.
f REMARKS ffor lab use only)
"Tori/m
fjljinji (jHQ
lo/s/
H
h
fl H*x
REMARKS
RELINQUISHED BY:
LlMCS.
DATE
Ufl
TIME
i
RECEIVED BY: DATE
riME RELINQUISHED BY: DATE TIME RECEIVED BY:
DATE
TIME
RELINQUISHED By(
DATE
TIME
m
LAB USE ONLY
RECEIV£0 *0* LABORARWY fff.
OWE
TIME
AIRBILL NO. | OPENED BY;
DATE
tJME
TEMP«C
Wm«
COMOtTlON
REMARK3' A J
jt ^ a\M 6to-sM .f <5®c, M, itirfj J
Po-£ - i/jsM W iMf *: ^
p eeA
V>v /
o^
* ^&>'£
?7
&>
o
8
-------
Source: WALLS
Station #: UNIT 10 FUEL GAS
Station Name: UNIT 10 FUEL GAS
Field:
H.5 Campaign 6
Report Date: 11/04/1994
Sample Date: 11/04/94
Flowing Pressure: 30 psig
Flowing Temp.: 60 F
Method: c:\ezchrom\methods>
File: c:\ezchrom\chronO
Gas Analysis by Chromatograph
Name
Mole %
BTU
SG
GPM
Nitrogen
1.
097
0.000
0.011
Methane
94.
240
956.199
0.522
C02
1.
303
0.000
0.020
Ethane
2.
765
49.156
0. 029
0. 741
H2S
0.
000
0.000
0. 000
Propane
0.
410
10.364
0. 006
0. 113
i-Butane
0.
056
1.829
0.001
0.018
n-Butane
0.
062
2.032
0. 001
0. 020
i-Pentane
0.
018
0.724
0.000
0.007
n-Pentane
0.
013
0. 524
0. 000
0. 005
Hexanes-Plus
0.
036
1.855
0.001
0.016
Ideal Total
100.000 1022.682 0.592
0.919
Gross BTU/Real Cu. Ft.
(@ 60 deg F. 14.730)
Dry ¦ 1024.908
Sat. = 1008.275
Actual * 1024.908
( 0.000 lbs. water/MMCF)
Gasoline Content
Propane GPM = 0.113
Butane GPM = 0.038
Gasoline GPM = 0.027
26# Gasoline GPM - 0.047
Total GPM » 0.178
Real Specific Gravity Calculated * 0.5927
On-Slte Specific Gravity * 0.0000
Gas Compressability = 0.9978
Remarks:
H-36
-------
Source: WALLS
Station #: UNIT 10 FUEL GAS
Station Name: UNIT 10 FUEL GAS
Field:
Report Date: 11/04/1994
Sample Date: 11/04/94
Flowing Pressure: 30 psig
Flowing Temp.: 60 F
Method: c: AezchromXmethods^
File: c s\ezchrom\chrora\l
Gas Analysis by Chromatograph
Name
Mole *
BTU
SG
GPM
Nitrogen
1.090
0.000
0.011
Methane
94.254
956.341
0.522
C02
1.302
0.000
0.020
Ethane
2.756
48.996
0.029
0.739
H2S
0.000
0.000
0.000
Propane
0.428
10.819
0.007
0.118
1-Butane
0.055
1.797
0.001
0.018
n-Butane
0.062
2.032
0.001
0.020
i-Pentane
0.018
0.724
0.000
0.007
n-Pentane
0.013
0.524
0.000
0.005
Hexanes-Plus
0.022
1.134
0.001
0.010
Ideal Total
100.000 1022.365 0.591
0.916
Gross BTU/Real Cu. Ft.
<@ 60 deg F, 14.730)
Dry * 1024.588
Sat. ¦ 1007.960
Actual - 1024.588
C 0.000 lbs. water/MMCF)
• Gasoline Content
Propane GFM ¦ o.118
Butane GPM ¦ 0.038
Gasoline GPM - 0.021
26# Gasoline GPM ¦ 0.041
Total GPM « 0.177
Real Specific Gravity Calculated * 0.5924
On-Site Specific Gravity « 0.0000
Gas Compressability « 0.9978
Remarks:
H-37
-------
Source:
Station #:
Station Name:
Field:
JONES
14-480-01-3
2
SUCT
Report Date: 11/04/1994
Sample Date: £5/11/94.
Flowing Pressure: 500 P6lg
Flowing Temp.: 60 F
Method: c:\ezchrom\methods >
File: c:\ezchrom\chrom\14480.1
Gas Analysis by Chromatograph
Name
Mole %
BTU
SG
GPM
Nitrogen
1.498
0.000
0.014
Methane
94.328
957.091
0.522
C02
0.999
0. 000
0. 015
Ethane
2.642
46.970
0.027
0.708
H2S
0.000
0.000
0. 000
Propane
0.357
9.024
0.005
0. 099
i-Butane
0.073
2.385
0. 001
0.024
n-Butane
0.060
1.966
0.001
0.019
i-Pentane
0.013
0.523
0.000
0. 005
n-Pentane
0.010
0.403
0.000
0. 004
Hexanes-Plus
0.020
1. 031
0. 001
0.009
Ideal Total
100.000 1019.392 ,0.589^ 0.867
c
Gross BTU/Real Cu. Ft.
(@ 60 degjf, 14.730)
Dry « Cin?i ^7ft- ,
Sat. - 1005.000
Actual = 1021.578
( 0.000 lbs. water/MMCF)
Gasoline Content
Propane GPM » 0.099
Butane GPM ¦ 0.043
Gasoline GPM ¦ 0.017
26# Gasoline GPM « 0.036
Total GPM * 0.159
Real Specific Gravity Calculated = 0.5899
On-Site Specific Gravity = 0.0000
Gas Compres6ability = 0.9979
Remarks:
H-38
-------
Source:
Station #:
Station Name:
Field:
WALLS
UNIT 10 FUEL GAS
UNIT 10 FUEL GAS
Report Date: 11/04/1994
Sample Date: 11/04/94
Flowing Pressure: 30 psig
Flowing Temp.: 60 F
Method: c:\ezchrom\methods>
File: c:\ezchrom\chrom\l
Gas Analysis by Chromatograph
Name
Mole %
BTU
SG
GPM
Nitrogen
1.090
0.000
0.011
Methane
94.254
956.341
0.522
C02
1.302
0.000
0.020
Ethane
2.756
48.996
0.029
0.739
H2S
0.000
0.000
0.000
Propane
0.428
10.819
0.007
0.118
i-Butane
0.055
1.797
0.001
0.018
n-Butane
0.062
2.032
0.001
0.020
i-Pentane
0.018
0.724
0.000
0.007
n-Pentane
0.013
0. 524
0.000
0.005
Hexanes-Plus
0.022
1. 134
0. 001
0.010
Ideal Total
100.000 1022.365 .91
1.916
Gross BTU/Real Cu. Ft.
(3 60 deg F, 14.730)
Dry - 1024.588 ^ '
Sat. - 1007.960
Actual * 1024.588
( 0.000 lbs. water/MMCF)
Gasoline Content
Propane GPM « 0.118
Butane GPM * 0.038
Gasoline GPM « 0.021
26# Gasoline GPM - 0.041
Total GPM » 0.177
Real Specific Gravity Calculated « 0.5924
On-Site Specific Gravity * 0.0000
Gas Compressabillty = 0.9978
Remarks:
H-39
-------
5amp/t Collected
***********************************************************************
STREAM * 1 Nov. 7, 1994 9:35 00-000-00 0 Record: 23
Batch J-2 Schedule 2205
COMP
UM0L%
M0L%
GPM
SUMMA
r y
H2S
0.00
0.00
0.000
N2
1.33
1.33
0.000
Base Mol %
100.48
CI
94.50
94.04
0.000
Total GPM
0.917
C02
1.26
1.25
0.000
Real SPGR
0.593
C2
2.76
2.75
0.736
Real BTU
1020
C3 v
IC4 v
0.51
0.51
0.141
Total SPHT
1.304
0.04
0.04
0.013
Z
0.9978
NC4
0.06 -
0.06
0.019
IC5
-0.00
0.00
0.000
NC5
0.00
'•O.OO
0.000
C6+
0.02
0.02
0.009
Total Normalized Mol% = 100.00
ARC-00000-0-94-311-311-J-01-00-00000
0000 0133 9404 0125 0275 0051 0004 0006 0000 0000 0002 0593 00917 1020
***********************************************************************
STREAM # 1 Nov. 7, 1994 9:48 00-000-00 0 Record: 24
Batch J-2 Schedule 2205
COMP
UM0L%
M0L%
GPM
SUMMA
R Y
H2S
0.00
0.00
0.000
N2
1.03
1.03
0.000
Base Mol %
100.24
CI
94.64
94.42
0.000
Total GPM
0.889
C02
1.26
1.26
0.000
Real SPGR
0.590
C2
2.78
2.77
0.741
Real BTU
1021
C3
0.43
0.42
0.116
Total SPHT
1.304
IC4
0.04
0.04
0.013
Z
0.9978
NC4
0.06
0.06
0.019
IC5
0.00
0.00
0.000
NC5
0.00
0.00
0.000
C6+
0.00
0.00
0.000
Total
Normalized Mol% = 100
.00
ARC-00000-
-0-94-311-
311-J-01
-00-00000
0000
0103
9442 0126
0277 0042 0004 0006 0000 0000
0000 0590 00889 1021
H-40
-------
Source:
Station #:
Station Name:
Field:
WALLS
TURB.
TURB.
Report Date: 11/07/1994
Sample Date: 11/07/94
Flowing Pressure: 30 pelg
Flowing Temp.: 60 F
Method: c:\ezchrom\methods'1
File: c:\ezchrom\chrom\4
Gas Analysis by Chromatograph
Name
Mole %
BTU
SG
GPM
Nitrogen
2.239
0.000
0.022
Methane
93.676
950.476
0.519
C02
0. 584
0.000
0.009
Ethane:
2. 990
53.156
0.031
0. 802
H2S
0. 000
0. 000
0.000
Propane
0.326
8.240
0.005
0.090
A-
0.075
2. 450
0.002
0.025
n-Butaine
0.065
2.130
0.001
0. 021
i-Pentane
0.015
0.603
0.000
0.006
n-Pentane
0.012
0.483
0.000
0.004
Hexanes-Plus
0.018
0.928
0.001
0.008
Ideal Total
100.000 1018.467 0.589
0.954
Gross BTU/Real Cu. Ft.
(0 60 deg F, 14.730)
Dry - 1020.633
Sat. » 1004.070
Actual « 1020.633
( 0.000 lbs. water/MMCF)
Gasoline Content
Propane GPM * 0.090
Butane GPM ¦ 0.045
Gasoline GPM * 0.018
26# Gasoline GPM « 0.038
Total GPM « 0.153
Real Specific Gravity Calculated * 0.5905
On-Site Specific Gravity = 0.0000
Gas Compressabllity * 0.9979
Remarks:
H-41
-------
Source:
Station #:
Station Name:
Field:
WALLS
TURB.
TURB.
Report Date: 11/07/1994
Sample Date: 11/07/94
Flowing Pressure: 30 psig
Flowing Temp.: 60 F
Method: c: \ezchrom\inethods,>
File: c:\ezchrom\chrom>
Gas Analysis by Chromatograph
Name
Mole %
BTU
SG
GPM
Nitrogen
2. 315
0.000
0.022
Methane
93.628
949.989
0.519
C02
0. 548
0.000
0.008
Ethane
2. 999
53.316
0.031
0.804
H2S
0.000
0.000
0.000
Propane
0.325
8.215
0.005
0. 090
1-Butane
0.078
2. 548
0.002
0.026
n-Butane
0.064
2.098
0. 001
0.020
i-Pentane
0.014
0. 563
0.000
0.005
n-Pentane
0.011
0.443
0. 000
0.004
Hexanes-Plus
0.018
0.928
0. 001
0.008
Ideal Total
100.000 1018.099 0.589
0.957
Gross BTU/Real Cu. Ft.
60 deg F. 14.730)
Dry = 1020.262
Sat. ¦ 1003.705
Actual « 1020.262
( 0.000 lbs. water/MMCF)
Gasoline Content
Propane GPM = 0.090
Butane GPM * 0.046
Gasoline GPM = 0.017
26# Gasoline GPM * 0.037
Total GPM = 0.153
Real Specific Gravity Calculated * 0.5905
On-Site Specific Gravity = 0.0000
Gas Compressability = 0.9979
Remarks:
H-42
-------
Source:
Station #:
Station Name:
Field:
WALLS
TURB.
TURB.
Report Date: 11/08/1994
Sample Date: 11/08/94
Flowing Pressure: 30 psig
Flowing Tenp.: 60 F
Method: c:\ezchrom\»ethods>
File: c:\ezchrom\chromV
Gas* Analysis by Chromatograph
Name
Mole %
BTU
SG
GPM
Nitroisen
2.221
0.000
0.021
Methane
93.363
947.300
0.517
C02
0.607
0.000
0.009
Ethane
3.428
60.943
0.036
0.919
H2S
0.000
0. 000
0.000
Propane
0. 299
7. 558
0.005
0. 083
i-Butane
0. 035
1.143
0.001
0.011
n-Butane
0. 027
0. 885
0.001
0. 009
i-Pentane
0. 007
0. 281
0.000
0.003
n-Pentane
0.005
0.201
0.000
0.002
Hexanes-Plus
0.008
0.412
0.000
0.003
Ideal Total
100.000 1018.724 0.590
1.029
Gross BTU/Real Cu. Ft.
(0 60 deg F, 14.730)
Dry - 1020.894
Sat. « 1004.327
Actual = 1020.894
( 0.000 lbs. water/MMCF)
Gasoline Content
Propane GPM * 0.083
Butane GPM « 0.020
Gasoline GPM » 0.008
26# Gasoline GPM « 0.016
Total GPM ¦ 0.110
Real Specific Gravity Calculated ¦ 0.5908
On-Site Specific Gravity * 0.0000
Gas Compressability = 0.9979
Remarks:
H-43
-------
Source: WALLS
Station #: | TUHB.
Station Name: TURB.
Field:
Report Date: 11/08/1994
Sample Date: 11/08/94
Flowing Pressure: 30 pslg
Flowing Temp,: 60 F
Method: c:\ezchrom\methods\i
File: c:\ezchrom\chromN
Gas Analysis by Chromatograph
Name
Mole %
BTU
SG
GPM
Nitrogen
2.199
0.000
0.021
Methane
93.395
947.625
0.517
C02
0.599
0.000
0.009
Ethane
3.435
61.068
0.036
0.921
H2S
0.000
0.000
0. 000
Propane
0.294
7.432
0.004
0.081
i-Butane
0.033
1.078
0. 001
0. 011
n-Butane
0.027
0.885
0. 001
0. 009
i-Pentane
0.007
0.281
0.000
0.003
n-Pentane
0.005
0.201
0.000
0.002
Hexanes-Plus
0.006
0.309
0. 000
0. 003
Ideal Total
100.000 1018.879 0.590
1.028
Cross BTU/Real Cu. Ft.
(@ 60 deg F, 14.730)
Dry = 1021.048
Sat. = 1004.479
Actual = 1021.048
( 0.000 lbs. water/MMCF)
Gasoline Content
Propane GPM « 0.081
Butane GPM - 0.019
Gasoline GPM * 0.007
26# Gasoline GPM * 0.016
Total GPM « 0.108
Real Specific Gravity Calculated = 0.5905
On-site Specific Gravity * 0.0000
Gas Compressability = 0.9979
Remarks:
H-44
-------
Source:
Station #:
Station Name:
Field:
WALLS
16-320-01
Report Date: 11/09/1994
Sample Date: 11/09/94
FUEL Flowing Pressure: 30 pslg
Flowing Temp.: 60 F
Method: c:\ezchrom\methods\i
Files c: \ezchrom\chrom\
Gas Analysis by Chromatograph
Name
Mole %
BTU
SG
GPM
Nitrogen
1.314
0.000
0.013
Methane
93.561
949.309
0.518
C02
1.205
0.000
0.018
Ethane:
3.400
60.445
0.035
0.911
H2S
0.000
0.000
0.000
Propane
0.366
9.252
0.006
0.101
i-Butiine
0.044
1.437
0.001
0.014
n-Buteine
0.051
1.671
0.001
0.016
1-Pent.ane
0.016
0.643
0.000
0.006
n-Pentane
0.012
0.483
0.000
0.004
Hexanes -Plus
0.031
1. 597
0.001
0.014
Ideal Total
100.000 1024.839 0.594
1. 067
Gross BTU/Real Cu. Ft.
(@ 60 deg F, 14.730)
Dry = 1027.080
Sat. = 1010.411
Actual ¦ 1027.080
( 0.000 lbs. water/MMCF)
Gasoline Content
Propane GPM =* 0.101
Butane GPM * 0.031
Gasoline GPM * 0.024
26# Gasoline GPM « 0.040
Total GPM ¦ 0.155
Real Specific Gravity Calculated * 0.5948
On-Slte Specific Gravity ¦ 0.0000
Gas Compressablllty ¦ 0.9978
Remarks::
H-45
-------
WALLS
16-320-01
Source:
Station #:
Station Name:
Field:
Method: c:\ezchrom\methods
File: c:\ezchrom\chrom
Report Date: 11/09/1994
Sample Date: 11/09/94
Flowing Pressure: 30 pslg
Flowing Temp.: 60 F
Gas Analysis by Chromatograph
Name
Mole %
BTU
SG
GPM
Nitrogen
1.300
0.000
0.013
Methane
93.578
949.482
0.518
C02
1.197
0.000
0.018
Ethane
3.400
60.445
0.035
0.911
H2S
0. 000
0. 000
0.000
Propane
0. 371
9. 378
0.006
0. 102
1-Butane
0. 043
1. 405
0.001
0.014
n-Butane
0.051
1. 671
0.001
0.016
i-Pentane
0. 016
0.643
0.000
0.006
n-Pentane
0.012
0. 483
0.000
0.004
Hexanes-Plus
0. 032
1.649
0.001
0.014
Ideal Total
100.000 1025.156 0.594
1.068
Gross BTU/Real Cu. Ft.
(@ 60 deg F, 14.730)
Dry = 1027.400
Sat. ¦ 1010.724
Actual » 1027.400
( 0.000 lbs. water/MMCF)
Gasoline Content
Propane GPM = 0.102
Butane GPM = 0.030
Gasoline GPM = 0.024
26# Gasoline GPM = 0.040
Total GPM *= 0.157
Real Specific Gravity Calculated = 0.5947
On-Site Specific Gravity « 0.0000
Gas Compressability = 0.9978
Remarks:
H-46
-------
Source: WALLS
Station #: 16-320-01
Station Name:
Field:
Method: c:\ezchrom\methods\4
File: c:\ezchrom\chrom\
Report Date: 11/10/1994
Sample Date: 11/10/94
FUEL Flowing Pressure: 30 pslg
Flowing Temp.: 60 F
Gas Analysis by Chromatograph
Name
Mole %
BTU
SG
GPM
Nitrogen
1.187
0.000
0.011
Methane
94.366
957.477
0.523
C02
1.390
0.000
0.021
Ethane
2.494
44,338
0. 026
0.669
H2S
0.000
0.000
0.000
Propane
0.391
9. 883
0.006
0.108
1-Butane
0. 056
1.829
0.001
0.018
n-Butane
0.064
2.098
0.001
0.020
i-Peritane
0.018
0.724
0.000
0.007
n-Pentane
0.014
0. 564
0. 000
0. 005
Hexanes-Plus
0.020
1.031
0.001
0.009
Ideal Total
100.000 1017.944 0.591
0. 836
Gross BTU/Real Cu. Ft.
(0 60 deg F, 14.730)
Dry = 1020.142
Sat. » 1003.589
Actual * 1020.142
( 0.000 lbs. water/MMCF)
Gasoline Content
Propane GPM * 0.108
Butane GPM • 0.039
Gasoline GPM = 0.020
26# Gasoline GPM * 0.041
Total GPM ¦ 0.167
Real Specific Gravity Calculated * 0.5920
On-Site Specific Gravity * 0.0000
Gas Compressability « 0.9978
Remarks:
H-47
-------
Source: WALLS
Station #: 16-320-01
Station Name:
Field:
Method: c:\ezchrom\methods''
File: c:\ezchrom\chroml
FUEL
Report Date: 11/10/1994
Sample Date: 11/10/94
Flowing Pressure: 30 psi*
Flowing Temp.: 60 F
Gas Analysis by Chromatograph
Name
Mole %
BTU
SG
GPM
Nitrogen
1.161
0.000
0.011
Methane
94.430
958.126
0.523
C02
1. 380
0.000
0.021
Ethane
2.475
44.001
0.026
0.663
H2S
0. 000
0,000
0.000
Propane
0.382
9.656
0.006
0.106
1-Butane
0. 055
1.797
0.001
0.018
n-Butane
0,064
2.098
0.001
0.020
i-Pentane
0. 019
0. 764
0.000
0.007
n-Pentane
0. 014
0. 564
0.000
0.005
Hexanes-Plus
0.020
1. 031
0.001
0. 009
Ideal Total
100.000 1018.035 0.591
0.828
Gross BTU/Real Cu. Ft.
(@ 60 deg F, 14.730)
Dry • 1020.232
Sat. * 1003.678
Actual « 1020.232
( 0.000 lbs. water/MMCF)
Gasoline Content
Propane GPM » 0.106
Butane GPM « 0.038
Gasoline GPM - 0.021
26# Gasoline GPM ¦ 0.041
Total GPM « 0.165
Real Specific Gravity Calculated = 0.5916
On-Site Specific Gravity = 0.0000
Gas Compressability * 0.9978
Remarks:
H-48
-------
:* ****** * * * * *: * :i: * * * * * * * * ** * >K ** * * * ** * * * ** * * * * -X ft * * * * * * ********************
STREAM tt 2 Nov. 15. 1994 8s S3 OO-OOO-OO O Record s SA
Batch 3—999 Schedule 1J.01
COMI"'
UROL?:
MO! "-
(3 FT"!
S Li II rl A Ft Y
H2S
N2
CI
002
C2
03
:i:c4
"i*fC4
:i:c5
NCS
OA-*-
0.00
1 „ 06
94-71
1.21
2.. 90
0.46
0.04
O., OA
O.. 00
0 00
O „ 00
0 . ooo
0.. ooo
1 :•.. ooo
0 . 000
O „ 770
0. 127
0.013
0.. 019
¦j „ <>00
o.. ooo
0.. 000
Base Hoi 'i
Total GPM
Real SRGR
Real BlU
Total SPHT
Z
100.43
0.92v
0. : .:.v i
1023
1. 3ok
0-997;!;
l otal I Iorrn¦¦:). 1 :i. z«t:l I'lo 1
100 .. O'O
ARC -00000 •• O- 94--31 A--319-¦ J--'.'.I. -¦ -0OO0
0000 0.1.05 ! 0120 0288 (>¦ o004 0006 Oooo OOOo >'.» ¦ <„¦ ¦•i*-- I 0O929 1023
;KW ** * * * * * :¦{ : * * >! : .t * * * * * * * * * * ;t; * * * * * *:+: -x s. * :7: ***************** t t
-;'I REAM ft 2
!i.? I r-h ;r "999
Itjv.'. 15., 19V.;
Schociul110:1
00—OOt. ¦
Ro cor a ::
'OMR
i-12!:;
1-12
C1
ou2
C2
C3
I 04
l-1
ii.: 5
NO '5
C6+
!.!! lf M.
000
! .. 02
<;• a.. ;
1 ..21
2..91
o.. 46
o „ 04
o.. OA
0.. 00
0.. oo
0.. 00
i'l I j
o., oo
1 . 01
<:>a ..33
1 .20
2.. 90
0.4 A
0.. 04
O. OA
0 ..OO
0.. 00
0 „ 00
Ul-T!
£ U lvl lY! H R Y
O.. OOO
O .. Ooo
0.. ooo
0.. 000
0 .. 12 7
0 .. 013
•;>.. <;• 1 y
O.. ooo
0 .. O00
¦ooo
"jase i-lol
Total Cvl-TI
Keal BPljR
Rv?al l:! U
Total BP KIT
1 OO .
0.935
O./ 1.
102-!
i „ 30'-;
0..997H
Total Normalized lvlo.I.100.. 0
ARO 000000 - 94 -31A - 319-2T -01
0000 0101 9433 012O 0290 004..:
'004 OOO A OO'OO OOoO 0000 0 591 00935 1024
H-49
-------
**#***#***•*******•«**********************************#****«******#*#*#*
S PRE AH tf :l. Nov. 15. 1994 8s40 OO--0OO-OO 0 Kecord: 3S
Batch J—999 Schedule 1101
tf******#****#********************************************#**#**#*******
Warning, NO FLOW DETECTED AT SAMPLE INJECT
Flow Switch -- 1.00
COMP UriOI.. "; Hi Mi. ." . WN i:> U I'! I'l A K Y
I-I2B
0.. oo
0.. 00
0 „ 000
N2
2. OA
2.04
0 . ooo
Base I'loi "..
100.70
C1
92.60
91 ..97
0000
Total LiPII
1.169
C02
2.. 01
2.. OO
0 .. H '
Ksal SPGR
0.621
2.00
1 .. V V
0.. :,2
v\ 1 BTLJ
1033
C3
1 .,01
i.. no
0.. 2
Tata. 1 SPI-IT
1 .303
:i ry:
0.. 2. '
0.. vo
<) .. I' V. '.Vi
v..
0.9977
NC4
0.. 20
0.. 20
0.. <>63
! L'f.
0.. 20
o.. 20
.. '.v 7 3
ncs
o.. 20
o.. 20
o.. o .:
O.. 20
o.. 20
O .. ' ¦'
Total
Horma l x ;vei:l I'loi
•-: 100..
. 00
,"iRC OOOOO- O--94-"31
19--J-01 -
-OO — OOOOO
O000 '
02i.'4 9197 0 200
1901'.
'0 O''./1/;!( ' 00
O020 OO20 0020 0621 Oll6
V lO-.:>,:>
H-50
-------
Source: WALLS
station #: 16-320-01
Station Name:
Field:
I. FUEL
Report Date: 11/14/1994
Sample Date: 11/14/94
Flowing Pressure: 30 P6lg
Flowing Temp.: 60 F
Method: c: \ezchrom\methods>
File: c:\ezchrom\chronO
Gas Analysis by Chromatograph
Name
Mole %
BTU
SG
GPM
Nitrogen
1.
112
0. 000
0.011
Methane
94.
260
956.401
0.522
C02
1.
274
0.000
0.019
Ethane
2.
744
48.783
0.028
0.736
H2S
0.
000
0.000
0.000
Propane;
0.
411
10.389
0. 006
0.114
i-But.ari"
0.
066
2. 156
0.001
0.022
n-Butane
0.
070
2.294
0.001
0.022
i-Pentane
0.
021
0.844
0. 001
0.008
n-Pentcine
0.
016
0.644
0.000
0.006
Hexanes-Plus
0.
026
1.340
0. 001
0.011
Ideal Total
100.000 1022.852 0.591
0.918
Gross BTU/Real Cu. Ft.
<@ 60 deg F. 14.730)
Dry - 1025.077
sat.. = 1008.441
Actual = 1025.077
( 0.000 lbs. water/MMCF)
Gasoline Content
Propane GPM = 0.114
Butane GPM * 0.044
Gasoline GPM = 0.025
26# Gasoline GPM = 0.047
Total GPM = 0.182
Real Specific Gravity Calculated = 0.5925
On-Site Specific Gravity = 0.0000
Gas Compressability = 0.9978
Remarks:
H-51
-------
Source:
Station #:
Station Name:
Field:
WALLS
16-320-01
FUEL
Report Date: 11/15/1994
Sample Date: 11/15/94
Flowing Pressure: 30 psig
Flowing Temp.: 60 F
Method: c:\ezchrom\methods\l
File: c:\ezchrom\chromV
Gas Analysis by Chromatograph
Name
Mole %
BTU
SG
GPM
Nitrogen
1.
198
0
.000
0.012
Methane
94.
402
957
.842
0. 523
C02
1.
306
0
.000
0.020
Ethane
2.
554
45
. 405
0. 027
0. 685
H2S
0.
000
0
.000
0.000
Propane
0.
347
8
.771
0.005
0.096
i-Butane
0.
07C
2
.287
0.001
0.023
n-Butane
0.
068
2
.229
0. 001
0. 021
i-Pentane
0.
019
0
.764
0. 000
0. 007
n-Pentane
0.
014
0
.564
0. 000
0. 005
Hexanes-Plus
0.
022
1
. 134
0. 001
0. 010
Ideal Total
100.000 1018.995 0.590
0. 847
Gross BTU/Real Cu. Ft.
(@ 60 deg F, 14.730)
Dry = 1021.195
Sat. = 1004.624
Actual * 1021.195
( 0.000 lbs. water/MMCF)
Gasoline Content
Propane GPM * 0.096
Butane GPM = 0.044
Gasoline GPM = 0.022
26# Gasoline GPM = 0.043
Total GPM = 0.162
Real Specific Gravity Calculated = 0.5915
On-Site Specific Gravity = 0.0000
Gas Compressability = 0.9978
Remarks:
H-52
-------
Appendix I
Quality Assurance and Quality Control (QA/QC)
This appendix presents the CEMS calibration drift and bias summaries and GC calibration
data. The CEMS drift tables include the analyzer range, calibration drift for zero and span,
and the span concentration. The CEMS bias tables include the analyzer range, QC input,
QC res])onse, percent bias, and the relative standard deviation. Where available, the GC
QA/QC summary tables present linearity, drift, standard deviation, and relative standard
deviation.
1-1
-------
1.1.1 CEMS Calibration Drift/Bias Summary
1.1 Campaign 2
CALIBRATION DRIFT
GRI CAMPAIGN 2 CALCULATED
Calibration Drift
Span
RESPONSE (PPM)
Dalle
Analyzer
Ranae
Zero
Span
Concentration
ZERO
SPAN
03-12-94
02
25
-0.18
-0.28
20.9
-0.044
20.83
C02
20
0.03
-0.05
17.97
0.005
17.96
CO
20000
-0.03
-4.26
20000
-6.817
19149
NOx
1000
0.22
-10.36
936
2.249
832.4
-
THC
10000
-0.03
0.59
998.7
-2.83
1057.6
03-13-94
02 '
25
•0.09
-0.32
20.9
-0.022
20.82
C02
20
0.08
0.45
17.97
0.015
18.06
CO
20000
-0.01
-0.17
20000
-1.849
19966
NOx
2500
-0.02
-1.83
936
-0.452
890.2
THC
10000
0.01
0.09
998.7
1.019
1007.61
Note: Drift calculated for only those runs performed at loads greater than
90 percent and speeds greater than 95 percent except as noted in
the report.
sdg/gri-epa
dr*ft'fm*l-rpl.w33
1-2
July 1995
298-130-33-06
-------
QC BIAS
GRI CAMPAIGN 2
Date
Analyzer
Ranae
QC Input
Response
Bias (%)
RSD (%)
03-12-94
02
25
14.02
14.03
0.04
—
C02
20
10
8.53
-7.35
—
CO
20000
15020
13778
-6.21
—
NOx
1000
248
244
-0.40
—
THC
10000
667.7
545.7
-1.22
—
03-13-94
02
25
14.02
14.08
0.24
—
C02
20
10
8.5
-7.50
—
CO
20000
15020
13846
-5.87
—
NOx
2500
786
747.7
-1.53
—
THC
10000
165.7
150.6
-0.15
-
Note: Bias calculated for only those runs performed at loads greater than 90 percent
and speeds greater than 95 percent except as noted in the report.
1-3
-------
1.1.2 GC Calibration Data
iCBM QC SUMMARY
CALIBRATION GASES
02
CO
COS
THC
NOx
.SO 2
CC20348
AAM348
BBC703
02 %
THC PPWV
CO PPKV
CO 2 *
NOX "PPWV
S02 PPWV
02 %
THC PPKV
CC PPMV
CO 2 *
NOX PPMV
S02 PPKV
02 %
THC PPMV
CO PPMV
CO 2 %
NOX PPMV
S02 PPMV
02 %
THC PPMV
CBRT.
OBSERVED
%
CONC.
CONC.
RBC.
14.02
14.13
100 . 8
165.7
144 . 6
87.3
1S020
13603
90 . 6
10
8.2
82 . 0
786
701 . 3
99.4
1997
2024
101 .4
CBRT.
OBSBRVBD
%
CONC.
CONC.
RBC.
14 . 02
14.23
101 . 5
667.7
623.5
93 .4
1502 0
13 S 6 3
90 . 3
10
8.47
04.7
786
790
100 . S
1997
2066.S
103 . 5
CBRT.
OBSBRVBD
%
CONC.
CONC.
RBC.
14 . 02
14.07
100.4
667.7
550
83 . 6
15020
13843
92.2
10
9.4
94 . 0
240
242.7
97.9
1997
2048
102 . 6
CBRT.
OBSBRVBD
%
CONC.
CONC.
RBC.
14 . 02
14.03
100 . 1
667 .7
54S . 7
01 . 7
02 , CO, C02 CYL. #ALM032250
THC CYL.#ALM03 9815 (497ppi CH4) \
NOx CYL.#1L3824
S02 CYL.MCC105415
AM3TBK 02 ANALYZBR PAIL8D DURING TBS
THC CYL.#ALM39877 (2003ppm CH4)
COMMENT
02 ON SBRVOMSX ANALYZER
C02 SPAN CUT TO 1/2 IN CAL. TO 8NABL
1-4
-------
CO PPMV
- 15020
13778
91.7
C02 %
10
8.53
85.3
NOX PPMV
241
244
98.4
S02 PPMV
1997
2027
101.5
C02 SPAN RETORNED TO NORMAL
1-13-94
CERT.
OBSERVED
%
COMMENT
CONC.
CONC.
REC.
02 %
i4.o:i
14. 75
105.2
02,CO,C02 CYL.«ALM005823 SANE CONC
THC PPMV
165.7
ISO. 6
90.9
THC CYL.#ALM03981S (497pp® CH4)
CO PPMV
1S02O
13846
92 .2
C02 %
10
8.5
85.0
NOX PPMV
78C
747.7
95.1
NOX CYL.#1L3824
S02 PPMV
199?
2030
101.7
3-14*94 CBRT.
CONC.
02 % 14.02
THC PPMV 165.7
CO PPMV 1S020
C02 % 10
NOX PPMV 801
S02 PPHV 1997
OBSERVED %
CONC. R8C.
14.1 100.6
176.6 106.6
14007 93.3
6.53 85.3
810.7 101.2
2022 101.3
COMMENT
NOX CYL.#1L14416
1-15-94
CBRT.
OBSERVED
%
CONC.
CONC.
RBC.
02 %
14.02
14 .4
102.7
THC PPMV
467 . 3
412 .4
88.3
CO PPMV
15020
13SS9
90.3
C02 %
10
8.3
83.0
NOX PPMV
248
225.5
90.9
S02 PPMV
1997
1993
99.8
COMMHNT
THC CYL.#AAL20403 (1402ppn CH4)
CBRT. OBSERVED %
CONC. CONC. R8C.
1-5
-------
1.2.1 CEMS Calibration Drift/Bias Summary
I.2 Campaign 3
CALIBRATION DRIFT
GRI CAMPAIGN 3
Calibration Drift
Span
Date
Analyzer
Range
Zero
Span
Concentration
6-14-94
02
25
0.17
0.12
20.9
C02
20
-0.21
-0.67
18
CO
1000
-0.01
-0.69
900
NOx
10000
0.05
-0.63
5003
v.
THC
10000
-0.06
-0.11
2003
6-15^94
02
25
0.03
-0.34
20.9
C02
20
-0.23
0.59
18
CO
1000
-0.02
-1.36
900
NOx
10000
-0.05
-6.9
5003
THC
10000
0.06
-0.15
2003
6-16-94
02
25
0.13
-0.84
20.9
C02
20
-0.16
-0.13
18
CO
1000
-0.01
-1.47
900
NOx
10000
0.15
-6.16
5003
THC
10000
0.05
-0.28
2003
6-18-94
02
25
0.19
-0.34
20.9
C02
20
0.23
0.18
18
CO
1000
-0.02
-0.99
900
NOx
10000
0.23
-2.83
5003
THC
10000
0.05
-0.62
2003
6-19-94
02
25
0.02
-0.43
20.9
C02
20
-0.36
0.89
18
CO
1000
-0.01
0.20
901
NOx
10000
0.15
-0.75
2005
THC
10000
0.08
-0.72
5028
6-20-94
02
25
0.11
-0.58
20.9
C02
20
0.06
0.14
18
CO
1000
-0.01
-0.58
900
NOx
10000
0.11
-4.24
5003
THC
10000
0.07
-0.69
2003
VOLTAGE RESPON
y
b
ZERO
SPAN
25.02
0.0013
0.0001
0.831
201.64
0.0297
-0.0005
0.09
100.46
0.6843
-0.0074
8.982
2588.55
-6.3511
0.0084
0.748
975.1
50.0853
-0.0427
5.031
Note: Drift calculated for only those runs performed at loads greater than
90 percent and speeds greater than 95 percent except as noted in
the report.
1-6
-------
QC BIAS
GRI CAMPAIGN 3
Date
Amilyzer
Range
QC Input
Response
Bias (%)
RSD (%)
6-14-94
02
25
3
3
0
0.50
25
3
2.97
-0.12
25
7.5
7.49
-0.04
—
C02
20
3.5
3.9
2
2.74
20
3.5
4.12
3.1
20
7.49
7.79
1.5
—
CO
1000
350
335
-1.5
—
1000
500
463
-3.7
0.86
1000
500
471
-2.9
NOx
10000
936
1041
1.05
-
THC
10000
917
927
0.1
—
6-15-94
(52
25
3
2.99
-0.04
—
25
7.5
7.51
0.04
-
C02
20
3.49
4.08
2.95
—
20
7.49
8.07
2.9
—
CO
1000
500
472
-2.8
—
1000
350
344
-0.6
—
NOx
10000
936
1101
1.65
0.05
10000
936
1100
1.64
THC
10000
917
965
0.48
—
10000
1402
1435
0.33
—
6-16-94
02
25
3
3.01
0.04
—
25
7.5
7.52
0.08
0.13
25
7.5
7.5
0
C02
20
3.49
3.99
2.5
-
20
7.49
7.83
1.7
2.91
20
7.49
8.3
4.05
CO
1000
350
343
-0.7
0.44
1000
350
346
-0.4
1000
500
472
-2.8
—
NOx
10000
936
1018
0.82
-
10000
2005
1946
-0.59
2.53
10000
2005
2047
0.42
THC
10000
917
933
0.16
—
10000
1402
1415
0.13
-
Note: Bias calculated for only those runs performed at loads greater than 90 percent
and speeds greater than 95 percent except as noted in the report.
1-7
-------
QC BIAS
GRI CAMPAIGN 3
Date
Analyzer
Range
QC Input
Response
Bias (%)
RSD (%)
6-18-94
02
25
7.5
7.5
0
0.07
25
7.5
7.49
-0.04
C02
20
7.49
8
2.55
0.12
20
7.49
8.02
2.65
CO
1000
350
344
-0.6
0.43
1000
350
347
-0.3
NOx
10000
2005
2030
0.25
0.37
10000
2005
2015
0.1
THC
10000
917
927
0.1
1.15
10000
917
906
-0.11
6-19-94
02
25
7.5
7.49
-0.04
25
7.5
7.61
0.44
0.78
25
7.5
7.48
-0.08
C02
20
7.49
9.53
10.2
20
7.49
7.76
1.35
9.08
20
7.49
8.09
3
CO
1000
350
348
-0.2
1000
350
381
3.1
4.89
1000
350
341
-0.9
NOx
10000
936
1000
0.64
10000
936
874
-0.62
6.32
10000
936
1005
0.69
THC
10000
917
886
-0.31
10000
917
830
-0.87
3.75
10000
917
908
-0.09
6-20-94
02
25
7.5
7.52
0.08
0.13
25
7.5
7.5
0
C02
20
7.49
8.02
2.65
0.00
20
7.49
8.02
2.65
CO
1000
350
345
-0.5
0.00
1000
350
345
-0.5
NOx
10000
936
997
0.61
0.45
10000
936
1006
0.7
THC
10000
917
958
0.41
2.10
10000
917
999
0.82
Note: Bias calculated for only those runs performed at loads greater than 90 percent
and speeds greater than 95 percent except as noted in the report.
1-8
-------
IJZJ2 GC Calibration Data
GC QA/QC Surrmary Table
GRI Campaign 3
GC Linearity GC Drift
Date Methane Ethane Methane Ethane
6-14-94 0.99995 0.99997 1.3 1.3
6-15-94 0.99986 0.99998 -4.6 -4.3
6-16-94 0.99992 0.99999 6.3 5.1
6-19-94 0.99996 0.99994 10 9.5
V V
1-9
-------
1.3.1 CEMS Calibration Drift/Bias Summary
CALIBRATION DRIFT
GRI CAMPAIGN 4
Calibration Drift
Span
Date
Analyzer
Range
Zero
Span
Concentration
8-23-94
02
25
0.16
-1.04
20.9
C02
20
0.05
-0.15
18
CO
20000
0.24
0.69
20000
NOx
10000
0.02
0.10
5003
THC
10000
1.18
-1.28
9026
8-25-94
02
25
0.04
1.20
20.9
C02
20
-0.20
-1.75
18
CO
20000
0.03
1.22
20000
NOx
10000
0.04
-2.04
5003
THC
10000
-0.14
-0.91
9026
8-26-94
02
25
-0.04
-0.60
20.9
C02
20
-0.10
0.95
18
CO
100
-2.84
-1.92
99
NOx
10000
0.00
0.16
5003
THC
10000
0.19
0.41
9026
8-27-94
02
25
-0.12
-1.96
20.9
C02
20
0.60
0.40
18
CO
500
0.83
-0.39
500
NOx
10000
0.07
0.53
5003
THC
10000
0.06
-0.39
9026
8-29-94
02
25
-0.12
-1.40
20.9
C02
20
0.35
0.95
18
CO
500
-0.39
-1.45
500
NOx
10000
0.06
0.03
5003
THC
10000
-0.09
-0.14
9026
8-30-94
02
25
-0.36
-1.72
20.9
C02
20
-0.05
-1.00
18
CO
500
0.03
-0.12
500
NOx
10000
-0.01
-0.20
5003
THC
10000
0.18
0.31
9026
Note: Drift calculated for only those runs performed at loads greater than
90 percent and speeds greater than 95 percent except as noted in
the report.
1-10
-------
QC BIAS
GRI CAMPAIGN 4
Date
Analyzer
Range
QC Input
Response
Bias (%)
RSD (%)
8-23-94
G2
25
10
10.06
0.24
25
10
9.93
-0.28
0.54
25
10
9.97
-0.12
C02
20
7
7.07
0.35
20
7
7.06
0.30
0.37
20
7
7.01
0.05
CO
20000
10000
9883
-0.59
20000
10000
9747
-1.27
0.67
20000
10300
9741
-2.80
NOx
10000
938
939
0.01
10000
938
942
0.04
3.21
10000
938
1006
0.68
THC
10000
917
1059
1.42
10000
917
940
0.23
5.14
10000
917
968
0.51
10000
497
586
0.89
—
8-25-94
C)2
25
10
10.06
0.24
0.65
25
10
9.93
-0.28
C02
20
7
6.91
-0.45
0.95
20
7
6.78
-1.10
CO
20000
10300
10165
-0.68
1.41
20000
10100
9883
-1.09
NOx
10000
509
519
0.10
2.77
10000
509
491
-0.18
10000
936
956
0.20
—
THC
10000
917
880
-0.37
—
8-26-94
C2
25
10
9.84
-0.64
0.25
25
10
9.89
-0.44
C02
20
7
7.03
0.15
0.64
20
7
7.12
0.60
CO
20000
10000
9866
-0.67
2.22
20000
10300
10313
0.07
NOx
10000
938
957
0.19
—
10000
509
515
0.06
—
THC
10000
917
908
-0.09
—
10000
2003
2058
0.55
0.44
10000
2003
2076
0.73
Note: Bias calculat ed for only those runs performed at loads greater than 90 percent
and speeds greater than 95 percent except as noted in the report.
1-11
-------
QC BIAS
GRI CAMPAIGN 4
Date
Analyzer
Range
QC Input
Response
Bias (%)
RSD (%)
8-27-94
02
25
3
2.87
-0.52
—
C02
20
15
15.04
0.20
-
20
3.5
3.52
0.10
—
CO
500
99.7
99.8
0.02
—
500
91
84.31
-1.34
—
NOx
1000
509
518
0.90
—
100
78
84
6.00
-
10000
503
521
0.18
—
10000
938
967
0.29
—
THC
10000
917
920
0.03
0.38
10000
917
913
-0.04
10000
2003
1996
-0.07
—
8-29-94
02
25
10
10.03
0.12
—
C02
20
7
7.07
0.35
—
20
15
15.03
0.15
-
CO
500
90
79.6
-2.08
—
NOx
10000
503
526
0.23
—
100
78
85.7
7.70
—
THC
10000
917
901
-0.16
1.26
10000
917
924
0.07
8-30-94
02
25
3
2.92
-0.32
—
25
10
9.9
-0.4
0.00
25
10
9.9
-0.4
C02
20
7
6.96
-0.20
0.07
20
7
6.97
-0.15
20
3.5
3.49
-0.05
—
20
15
14.78
-1.10
—
CO
500
100
101.5
0.30
—
500
90
86
-0.80
—
NOx
10000
938
943
0.05
—
10000
503
505
0.02
—
100
78
82.9
4.90
—
THC
10000
917
902
-0.15
0.78
10000
917
888
-0.29
10000
2003
2004
0.01
-
Note: Bias calculated for only those runs performed at loads greater than 90 percent
and speeds greater than 95 percent except as noted in the report.
1-12
-------
1.3.2 GC Calibration Data
GRI Campaign 4 GC QC/QA Data
Precision Data for 16.3 ppmv Standard on 8/25
Average STD DEV %RSD Number
Methane 2657496 317507 11.95% 5
Ethane 4356863 173339 3.98% 5
Drift Data for 100 ppmv Standard
08/28
Methane -5.23%
Ethane -4.28%
Zero Nitrogen Concentration (ppmv)
Methane
Ethane
08/26
ND
ND
08/26
ND
ND
08/27
ND
1
08/28
ND
ND
08/28
ND
1
08/28
ND
2
08/28
ND
1
1-13
-------
1.4 Campaign 5
1.4.1 CEMS Calibration Drift/Bias Summary
CALIBRATION DRIFT
GRI CAMPAIGN S CALCULATED
Calibration Drift
Span
RESPONSE (PPM)
Date
Analyzer
Ranoe
Zero
Span
Concentration
ZERO SPAN
10-05-94
02
25
-0.40
-0.52
20.85
-0.1 20.72
C02
20
-0.10
-0.85
18.2
-0.02 18.03
CO
20000
-0.01
-0.01
500
-1.27 498.29
NOx
10000
-0.00
-0.21
2392
-0.03 2370.61
THC
10000
0.02
-0.10
917
1.5 906.8
Note: Drift calculated for only those runs performed at loads greater than
90 percent and speeds greater than 95 percent except as noted in
the report.
1-14
-------
QC BIAS
GRI CAMPAIGN 5
Date
Analyzer
Range
QC Input
Response
Bias (%)
RSD (%)
10-5-94
02
25
9.99
10.04
0.20
0.20
25
9.99
10
0.04
25
14.01
13.89
-0.48
0.18
25
14.01
13.94
-0.28
C02
20
5
5.18
0.90
—
20
10.01
9.98
-0.15
20
10.01
9.91
-0.50
0.31
20
10.01
9.97
-0.20
CO
20000
51
47.19
-0.02
20000
51
47.2
-0.02
3.63
20000
51
50.92
-0.00
NOx
10000
51
48.38
-0.03
—
10000
939
965
0.26
0.42
10000
939
957
0.18
THC
10000
497
502
0.05
10000
497
508
0.11
1.14
10000
497
494
-0.03
Note: Bias calculated for only those runs performed at loads greater than 90 percent
and speeds greater than 95 percent except as noted in the report.
1-15
-------
1.4.2 GC Calibration Data
GC QA/QC Summary Table
GRI Campaign 5
GC Linearity
Methane Ethane
10-04-94 0.9991 NA
10-06-94 0.997 NA
\
-------
1.5 Campaign 6
1.5.1 CEMS Calibration Drift/Bias Summary
CALIBRATION DRIFT
Calibration Drift
Span
Date
Analyzer
Range
Zero
Span
Concentration
11-05-94
02
25
-0.20
-0.16
20.85
0751-1249
C02
20
-0.10
-0.11
18.2
CO
500
0.66
•0.18
452
NOx
1000
0.10
0.87
890
THC
2500
-3.05
1.45
2003
11-05-94
02
25
-0.08
-1.32
20.85
1323-1842
C02
20
0.20
-0.25
18.2
CO
500
0.47
0.36
452
NOx
2500
0.05
-0.62
2480
THC
2500
1.73
1.45
2003
11-07-94
02
25
-0.44
-1.84
20.85
C02
20
0.25
•0.20
18.2
CO
100
0.64
-0.75
90.7
NOx
250
-0.13
0.91
213
THC
100
-1.55
-1.36
92.9
11-08-94
02
25
-0.12
0.36
20.85
C02
20
0.15
1.15
18.2
CO
100
-0.20
0.79
90.7
NOx
250
0.25
-2.90
213
THC
100
0.01
-2.32
92.9
11-10-94
02
25
-0.20
-0.68
20.85
C02
20
0.05
-2.20
18.2
CO
100
-0.53
1.18
90.7
NOx
1000
-0.02
0.65
890
THC
2500
0.02
-0.55
2003
11-12-94
02
25
-0.08
-0.64
20.85
C02
20
0.20
-1.70
18.2
CO
100
0.41
1.64
90.7
NOx
1000
0.01
0.82
890
THC
2500
0.49
-1.09
2003
11-14-94
02
25
-0.52
0.08
20.85
C02
20
0.30
0.50
18.2
CO
100
0.79
-0.83
90.7
NOx
1000
0.49
-1.39
890
THC
2500
-0.09
2.43
2003
11-15-94
02
25
0.12
-0.04
20.85
C02
20
-0.05
-0.35
18.2
CO
100
0.96
0.10
90.7
NOx
1000
0.22
-1.56
890
THC
2500
-0.13
-2.23
2003
y
24.91
19.62
484.22
b
-0.141
-0.029
5.6297
Voltage Response
ZERO SPAN
97.75 1.9024
111.38 -76.98
0.0036
0.0005
-0.0048
•0.0091
0.0029
0.841
0.928
0.92
9.174
8.015
Calc. Response
ZERO
SPAN
•0.05082
20.80881
•0.01929
18.17826
3.305444
451.1121
1.012875
898.6609
-76.6542
815.7335
•0.02
20.52
0.04
18.15
2.36
453.79
1.18
2464.56
43.15
2039.19
-0.11
20.39
0.05
18.16
0.64
89.95
-0.33
215.27
-1.55
91.54
-0.03
20.94
0.03
18.43
-0.2
91.49
0.63
205.75
0.01
90.58
-0.05
20.68
0.01
17.76
-0.53
91.88
-0.17
896.55
0.44
1989.31
-0.02
20.69
0.04
17.86
0.41
92.34
0.08
898.24
12.21
1975.84
-0.13
20.87
0.06
18.3
0.79
89.87
4.94
876.06
-2.19
2063.69
0.03
20.84
-0.01
18.13
0.96
90.8
2.16
874.35
-3.33
1947.26
Note: Drift calculated for only those runs performed at loads greater than
90 percent and speeds greater than 95 percent except as noted in
the report.
1-17
-------
QC BIAS
GRI CAMPAIGN 6
Date
Analyzer
Ranae
QC Input
Response
Bias (%)
RSD (%)
11-05-94
02
25
14.01
14.22
0.84
25
14.01
14.09
0.32
0.40
25
14.01
14.11
0.40
C02
20
10.01
10.19
0.90
20
10.01
10.1
0.45
0.44
20
10.01
10.09
0.40
CO
500
90.7
91.89
0.24
500
90.7
89.39
-0.26
1.14
500
90.7
91.04
0.07
NOx
1000
509
517.02
0.80
1.65
1000
509
500.2
-0.88
THC
2500
917
897.47
-0.78
—
2500
1402
1439.38
1.50
—
11-07-94
02
25
14.01
14.14
0.52
0.11
25
14.01
14.17
0.64
C02
20
10.01
10.28
1.35
0.10
20
10.01
10.3
1.45
CO
100
51.2
51.53
0.33
0.78
100
51.2
52.34
1.14
NOx
250
77.5
83.57
2.43
0.19
250
77.5
83.89
2.56
THC
100
92.9
93.14
0.24
0.44
100
92.9
92.32
-0.58
11-08-94
02
25
14.01
14.03
0.08
25
14.01
13.97
-0.16
0.19
25
14.01
14.02
0.04
C02
20
10.01
10.18
0.85
20
10.01
10.17
0.80
0.30
20
10.01
10.24
1.15
CO
100
51.2
52.18
0.98
100
51.2
52.5
1.30
0.26
100
51.2
52.26
1.06
NOx
250
77.5
83.54
2.42
250
77.5
82.43
1.97
1.42
250
77.5
80.7
1.28
THC
100
92.9
93.15
0.25
100
92.9
90.49
-2.41
1.41
100
92.9
90.34
-2.56
Note: Bias calculated for only those runs performed at loads greater than 90 percent
and speeds greater than 95 percent except as noted in the report.
1-18
-------
QC BIAS
GRI CAMPAIGN 6
Date
Analyzer
Ranae
QC Input
Response
Bias (%)
RSD (%)
11-10-94
02
25
14.01
14.07
0.24
25
14.01
13.99
•0.08
0.23
25
14.01
14.03
0.08
C02
20
10.01
10.1
0.45
20
10.01
9.94
-0.35
0.81
20
10.01
9.92
-0.45
CO
500
51.2
51.18
-0.00
500
51.2
53.13
0.39
2.29
500
51.2
50.3
-0.18
NOx
1000
509
515
0.60
1000
509
516
0.70
0.33
1000
509
519
1.00
THC
2500
1402
1398
-0.16
2500
1402
1392
-0.40
0.44
2500
1402
1407
0.20
11-12-94
02
25
14.01
14.15
0.56
25
14.01
14
-0.04
0.44
25
14.01
14.05
0.16
C02
20
10.01
10.09
0.40
20
10.01
9.99
-0.10
0.50
20
10.01
9.98
-0.15
CO
500
51.2
52.09
0.18
0.29
500
51.2
52.39
0.24
500
90.7
90.46
-0.05
-
NOx
1000
509
518
0.90
1000
509
519
1.00
0.50
1000
509
524
1.50
THC
2500
1402
1405
0.12
2500
1402
1404
0.08
0.29
2500
1402
1396
-0.24
11-14-94
o;>.
25
14.01
14.17
0.64
0.14
25
14.01
14.21
0.8
CG2
20
10.01
10.15
0.70
0.49
20
10.01
10.25
1.20
CO
500
90.7
88.58
-0.42
1.00
500
90.7
90.37
-0.07
NOx
1000
509
518
0.90
0.68
1000
509
511
0.20
THC
2500
1402
1443
1.64
0.07
2500
1402
1441
1.56
11-15-94
02
25
14.01
14.04
0.12
0.50
25
14.01
14.18
0.68
C02
20
10.01
10.12
0.55
0.10
20
10.01
10.1
0.45
CO
500
90.7
88.98
-0.34
1.05
500
90.7
60.86
0.03
NOx
1000
509
518
0.90
0.38
1000
509
522
1.30
THC
2500
1402
1417
0.60
1.03
2500
1402
1388
-0.56
Note: Bias calculated for only those runs performed at loads greater than 90 percent
and speeds greater than 95 percent except as noted in the report.
1-19
-------
GC Drift Data GC Drift Data
Date
Date
11/04
11/05
11/07
11/08
11/10
11/11
11/12
11/14
11/15
Standard
Standard
1000 ppmv
2000 ppmv
16 ppmv
100 ppmv
100 ppmv
100 ppmv
2000 ppmv
2000 ppmv
2000 ppmv
Methane
Methane
2.50%
-3.89%
1.30%
-3.51%
-15.72%
-10.29%
0.48%
-1.78%
-9.55%
(T
Drift = (Final A Drift = (Final Area - Initial Area)/lnitial Area x 100 2
I* o
3
N)
O
-------
Methane
Ethane
GRI Campaign 6 GC Drift Summary
Average STD DEV
Methane 13976 1431
Ethane 28365 3040
%RSD Number
10.24% 17
10.72% 19
Drift Drift Drift Drift Drift
11/04 11/07 11/08 11/11 11/12
1.14% 1.30% -0.90% -14.60% -10.78%
0.47% 0.74% -1.50% 4.43% -14.27%
Precision
11/04
-100.00%
4.58%
Average STD DEV
Methane 79920 8799
Ethane 160281 16521
Drift Drift
%RSD Number 11/04 11/05 11/08 11/10 11/11 11/12 11/15
11.01% 17 -1.53% -27.01% -3.51% -15.72% -10.29% -9.37% -1.41%
10.31% 17 -2.33% -5.13% -3.29% -8.68% -10.16% -5.28% -0.35%
to
Average STD DEV %RSD Number
Methane 743973 218766 29.41% 13
Ethane 1482067 432092 29.15% 13
Drift Drift Drift
11/04 11/05 11/10 11/12 11/14 11/15
2.50% -4.72% 129.73% 21.38% 2.53% 23.75%
2.25% -4.21% 135.96% 21.63% 2.32% 28.08%
Average STD DEV
Methane 1577330 107332
Ethane 3107806 205167
%RSD Number
6.80% 10
6.60% 10
Drift Drift Drift
11/05 11/12 11/14 11/15
-3.89% 0.48% -1.78% -9.55%
-3.70% 1.11% -1.73% -9.56%
-------
GC Linear Regression Data
GRI Campaign 6
Date
Compound
Weight
Linear Regression Data |
Intercept
Slope
Correlation 1
Coefficient
11/04/94
Methane
Ethane
3376.447
6776.749
901.84
1783.82
0.99999257
0.99998948
11/05/94
Methane
Ethane
2708.746
5249.526
897.632
1767.97
0.99999691
0.99999512
11/07/94
Methane
Ethane
1150.286
1641.524
815.107
1622.9
two points |
two points
11/08/94
Methane
Ethane
1082
1601.619
806.75
1600.52
two points
two points
11/10/94
am
Methane
Ethane
0
0
868.438
1740.31
one point
one point
11/10/94
pm
Methane
Ethane
-836.81
-78.2381
920.738
1745.2
two points
two points
11/12/94
Methane
Ethane
1/x
1/x
239.978
3985.222
794.998
1556.42
0.99898749
0.99918467
11/14/94
Methane
Ethane
1/x
1/x
-253 .503
7086.875
758.926
1470.03
0.99578562
0.9946894
11/15/94
Methane
Ethane
1/x
1/x
148.5201
-172 .724
726.573
1432.81
0.99926723
0.99912562
1-22
-------
GC Calibration Summary
GRI Campaign 6
Compound
Concentration
ppmv
No. of
Injections
Area Resp
Average
%RSD
Methane
V
0
2
0
16.3
17
13976
10.24%
100
17
79920
11.01%
1008
13
743973
29.41%
2000
10
1577330
6.80%
Linearity (R Sq
uared)
0.9987793
Ethane
0
2
0
16.3
19
28365
10.72%
- '' 100
17
160281
10.31%
1039
13
1482067
29.15%
2000
10
3107806
6.60%
Linearity (R Squared)
0.9978751
1-23
-------
| |