-------
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
itm i
Mil K
IIWi tw
nccroioTinu
VbWWIUI I It*>1
WAIIIC
iribWk
IIMITC
Wl«i 1 V
nccroionmi
ybvwi ui iiwn
Wftl lie
IIMITC
VllilV
m^SFFrfi
/.till
wii
i rtiiFI
fui
tfuf
linens mere
LUfck. UIL • IUJ
vn
i»
nerr
t/LU 1
i 0 fi T?« rtfF
r»
FSG
jwiiiFI
ihi.li
Tirtif
net nrr
lULLMll
tin
tui
¦inn
IU.V
IM^m CT
Ufl WILLI
474 I*
II l«U
nrr r
M.U 1
flESTAtif,
M.U
Pnm
miR his
/ill
iriif
no n mi
IUU.ILVII
T)jncn
UUHkV
crrun
jw tm\
nnftwmrw 4i
I t/vruv wii. ik
C17ft
ncr r
vlu i
SifrPRESS
ii9.il
*M
PuwFSiYi /i
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r*TiF
SUTSTr
in
J.U
¦ inn
lltU
ivvim fM *m
rtmuMiL jl
ah r\
V+I.U
nrr r
iA.il 1
DfiCHAHGEGAS
711!)
P9G
POWmCYKL
tjUIIJ
MPfj l-
vsmroH
25.0
KLS
FuiniaatLS.
£33.5
CcGr
F!fi VALVE 0UH«JI
7itn
ItfiW
*
r»
nAuuenrw 4n
1 vnuiuii. m
o:4n
\J\f («U
KGF
MmrmivcnntivKKN
Mwitiik.i i Hiu« Immw
IMS
Dfwrarvi to
1 S/IIUiWtLLtk
71KIJ
iim; t
FOwFR ("VI. Tim* CfliiiT
/57*ii
uis
FuwEkLVLJK
til n.ii
irf, i
COwP Ctl TkABOh COiS.7
552.0
GTS
nouwenr^ jn
1 VIlHuiLlh
iittu
Dril r
ixMtorvi ?4 uij rm
aw I i«h t u •
«n
r«/iu
nrc
H' w
WHWWCVI w
/•to n
'M.J.U
nrr r
11U 1
yi/uinma MB j
i r
i I
l i
i b
-5
I I
I IAI III
I I
r l
5 i 7 i 5
i i
i i
—i—i
i 3il 5i
i i
l-*iri»« ft.
riiiw i
i i
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)
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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 .
- . n/jj. .
Add Oilutent (He. Air. N.) jr.21.10,m f.
Dilution Factor
o. no/ >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
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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
-------