Document mbymp3929QGvRJg0JNbQRJ4eJ
APPENDIX E
PROCESS STREAM COMPOSITION DATA SARA TITLE III, SECTION 313
1990 TOXIC CHEMICAL RELEASE INVENTORY LAKE CHARLES REFINERY
SAL 0000041
LIQUID PROCESS STREAM COMPOSITIONS LAKE CHARLES REFINERY
STREAM -------- -
* BNZ
TOL
COMPOSITION (wt %) ETB XYL CYHX CUM PCUM NAPH STY
Regular Gasoline
1 .8
9.1
2.2 10.6
BD
4.3 2.6 BD BD
Unleaded Gasoline
2.5
6.1
1.6 7.7 BD
4.3 2.0 BD BD
Super UL Gasoline 2.8
9.8
2.5 12.0
BD
4.3 2.0 BD BD
Sweet Crude
0.32
BD
BD
1.2 BD BD BD BD BD
Sour Crude
0.23
BD
BD
BD
BD
BD
BD
BD
BD
Base Gasoline
3.0 9.8
2.7 13.0 BD
4.3 2.0 BD BD
FCC Gasoline
0.8 2.7 BD 5.0 1.0 5.1 3.1 BD BD
Casinghead
1.9 6.7 BD
3.7 3.7 BD BD
1.0 BD
LSR Gasoline
3.2 3.0 BD BD
5.2 BD BD BD BD
Reformate
5.4 15.2
5.3 16.7
BD
6.8
1.7 BD
BD
Coker Gasoline
0.1 4.0 BD 6.5 1.0 1.0 3.0 BD BD
Crude Wet Gas
0.2 BD BD BD BD BD BD BD BD
Naphtha
1.0 4.5 1.0 4.0 2.0 BD BD BD BD
Jet-A
BD BD BD BD BD BD BD
3.0 BD
#2 Distillate
BD BD BD BD BD BD BD
3.0 BD
Kerosene
BD BD BD BD BD BD BD
3.0 BD
Sabine HAD
35.0 15.0 4.0 BD BD BD BD
6.0 10.0
Conoco LVT Oil
BD BD BD BD BD BD BD
3.0 BD
Thermal Gasoline 1.0 4.0 BD 6,5 1.0 1.0 3.0 BD BD
PBC (Field
1.3 3.2 BD 4.9 2.3 BD BD BD BD
Cat Poly
BD BD BD BD BD BD BD BD BD
Alkylate
BD BD BD BD BD BD BD BD BD
SLOP OIL
1.6 4.9 1.4 6.5 BD 2.15
1 BD BD
DE MINIMUS = 0.1 WT %
SAL 000004-194
GAS PROCESS STREAM COMPOSITION LAKE CHARLES REFINERY
STREAM
COMPOSITION (wt %) -----------------------------
Ethylene
Propylene
1,3-Butadiene
FCC Tail Gas P-B P-P B-B Cryo Tail Gas Cat Poly Charge Alky/Cryo Feed Alky Tail Gas Coker Wet Gas Cryo Liquid B-B to MTBE MTBE OH Poly OH SWS OH Fuel Gas
16.0 BD BD BD 15.0 BD BD BD 1.0 BD BD BD BD 9.0 3.6
12.0 33.0 68.0
5.0 7.0 50.0 8.0 30.0 7.0 5.0 5.0 5.0 20.0 25.0 5.0
0.2 0.2 0.3 0.3 BD 0.1 0.3 BD 0.1 BD 0.4 0.3 0.1 0.1 0.3
DE MINIMUS = 0.1 WT %
SAL 000004X95
LAKE CHARLES BENZENE X IN GASOLINE STREAMS
STREAM
DENSITY LB./CU. FT.
INVERSE DENSITY
UNLEADED SUPER UNLEADED REGULAR LT. STR. RUN #2CTU LT. STR. RUN CTU DENUDED CASINGHEAD CAT POLY ALKYLATE COKER GASOLINE FCC REFORMATE 95 SEV'Y REFORMATE 101 SEV'Y
47 46.38 46.38 45.07 43.77 41.94 45.35 43.47 45.56 47.61
48.8 50.1
0.0213 0.0216 0.0216 0.0222 0.0228 0.0238 0.0221 0.0230 0.0219 0.0210 0.0205 0.0200
BENZENE VOL X
2.2 2.4 1.5 1.7 3.5 1.5 <.1 <.1 0.1 0.7 3.8
6
BENZENE DENSITY
54.37 54.37 54.37 54.37 54.37 54.37 54.37 54.37 54.37 54.37 54.37 54.37
BENZENE WT. X
2.54 2.81 1.76 2.05 4.35 1.94
ERR ERR 0.12 0.80 4.23 6.51
SAL 000004196
LAKE CHARLES C7 AROMATIC (TOLUENE) X [H GASOLINE STREAMS
STREAM
DENSITY LB./CU. FT.
INVERSE DENSITY
UNLEADED SUPER UNLEADED REGULAR CASINGHEAD GASOLINE CAT POLY ALKYLATE FCC REFORMATE 95 SEV'Y REFORMATE 101 SEV'Y
45.82 46.6
45.82 43.88 45.35 43.47 46.75 48.56 50.36
0.0218 0.0215 0.0218 0.0228 0.0221 0.0230 0.0214 0.0206 0.0199
C7 AROMAT. VOL X
5.24 8.56 7.79 5.49 NO ND
2.4 13.22 14.94
TOLUENE DENSITY
53.56 53.56 53.56 53.56 53.56 53.56 53.56 53.56 53.56
NO = Not Detected
TOLUENE VT. X
6.13 9.84 9.11 6.70
ERR ERR 2.75 14.58 15.89
SAL 000004197
LAKE CHARLES C8 AROMATIC (ETHYL BENZENE AND XYLENES) X IN GASOLINE STREAMS
STREAM
DENSITY IB./CU. FT.
INVERSE DENSITY
UNLEADED SUPER UNLEADED REGULAR CASINGHEAD GASOLINE CAT POLY ALKYLATE FCC REFORMATE 95 SEV'Y REFORMATE 101 SEV'Y
45.82 48.6
45.82 43.88 45.35 43.47 46.75 48.56 50.36
0.0218 0.0215 0.0218 0.0228 0.0221 0.0230 0.0214 0.0206 0.0199
C8 AROMAT. VOL X
C8 AROMAT. DENSITY
C8 AROHAT. WT. X
ETH. BEN. WT. X
7.92 12.63 11.09 3.44 ND NO
5.06 18.46 22.21
53.56 53.56 53.56 53.56 53.56 S3.56 53.56 53.56 53.56
9.26 14.52 12.96 4.20
ERR ERR 5.80 20.36 23.62
1.57 2.47 2.20 0.55
0.75 4.89 5.67
XYLENES WT. X
7.68 12.05 10.76
3.65
5.04 15.47 17.95
ND = Not Detected
SAL 000004198
Interoffice Communication
TO: Bill Cason > Houston
FROM:
Ollie Engle - Ponca City
DATE;
January 26, 1990
SUBJECT: NPRA Survey
The aromatics and olefins for the R,NA Refinery streams and products are listed below, per your request. These data are from the Laboratory "Quality of Products - Typical Base Gasolines and Gasoline Streams" Reports of the past few years. Aromatics and olefins data are not routinely run on these streams and blends, but they should change fairly slowly, within limited ranges.
Refinery
Stream
Aromatics
Olefins
Benzene
Ponca City {1988 Data) Regular Unleaded Super Unleaded Leaded Regular Lt. Str. Run Cat Poly A1kylate FCC - H Light - #5 Light - #4&5 Heavy Reformate #2, 92 Sev'y - #3, 98 Sev'y
27 30 28
2 1 4 15
22 39 46 61
18 1.4 11 1.3 12 2.1
1 1.3 98 <0.1
1 0.2 49 0.5 41 0.8 29 0.7
1 3.3
1 3.0
Lake Charles (1983 Data) Regular Unleaded Super Unleaded Leaded Regular
LL. Sir. Run - #2CTU - #3CTU
Denuded Casinghead Cat Poly
A1kylate Coker Casoline FCC Reformate - M2, 96 Sev'y
- #3, 101 Sev'y
38 30 31
8 6 3 <1 <1 8
33 49 63
12 2.2 7 2.4
24 1.5
<1 1.7 <1 3.5
1 1 .5 97 <0.1
1 <0.1 45 0.1 34 0.7
1 3.8 1 6,0
JhM 23 `30 l?:21
SAL 000004199
a05
- 2. j a PAGE, u 0 j;
January 26, 1990 Page 2
Refinery
Stream
Aromatirs
Billings (1989 Data) Regular Unleaded - 85.5
Super Unleaded
- 87 91
- 92
Leaded Regular - 87
. 88
Lt. Str. Run - #2 Cond.
Alkylate
FCC
Reformate - 87 Sev'y
(R+M)/2
23 22
3 42 23
16 3 1
25 46
Denver (1989 Data) Regular Unleaded Super Unleaded Leaded Regular
Lt. Str. Run Cat Poly
FCC Reformate 91 Sev'y
- 93 Sev'y
21 41 22
5 1 26 42 46
01efins
17 17
9 <1 17 15 <1 <1 41
1
26 1
26 <1 98 27
1 1
Demerte
1.0 1.0 0.5 1.0 0.9 0.9 2.0 <0.1 0.6 1.6
1.3 2.6 1.3 1.4 0.3 0.8 3.2 3.0
011 ie Engle cr.: COC - RHC - WGG - RHC - TGW
JmII 23 '30 1
SAL OOOOO4200 -i 0 5 7 S 4 4 PA6E.094
CONOCO INC. PONCA CITY, OKLAHOMA REFINING TECHNICAL SERVICES LABORATORY
Pit.: File: Dace:
LC 662 ." 10/6
LABORATORY NO.: CHARGE: SUBJECT:
J-23-83 LC 49 Quality of Products - Typical Base Gasolines and Gasoline Streams Summer 1983 - Lake Charles Refinery
TABLE I BASE GASOLINES
Composition, Normal Range Stock
Regular
Unleaded
Unleaded
Composition, Vol.%
Denuded C-H. Lt. St. Run Coker Gasoline FCC Gasoline No.2 Reformate No.3 Reformate Cat Poly Alkylate Butane
Typical Inspections Gravity, API Distillation, F, 760 mm
IPB 10% Evaporated 50% Evaporated 90% Evaporated End Point Recovery, Vol.% Reid Vapor Pressure, psi Temperature for V/L of 20,
calc.
Existent ASTM Gum, mg./lOO mis. Aromatics, Vol.% Olefins, Vol.% Total Sulfur, Wt.% Benzene, Vol.%
Research Octanes Clear 0.25 gms./gal. TEL 0.5 gms./gal. TEL 1.5 gms./gal. TEL
Motor Octanes Clear 0.25 gms./gal. TEL 0.5 gms./gal. TEL 1.5 gms./gal. TEL
5-10 5-10 0-5 40-55 15-25 0-5 0-5
0-5
58.5
95 118 211 354 434
97 11.0
129
2 31 24 0.07 1-5
90.8 92.2 93.5 95.9
80.1 81.4 32.3 84.4
cc: KWM-JWB-RGB-RFC-PWL-MEO-JJM-KCH-OFE-CM-F
0-5 0-5 0-5 30-40 35-45 5-10 0-5 0-5 5-10
56.0
91 114 220 339 434
97 11.0
129 1
38 12 0.04 2.2
92.5
82.1
O00n0n0. 4*0I
0-5 15-25 10-15 25-35
0-5 25-35
5-1
58.5
92 116 222 328 427
96 11.2
129 2
30 7
0.02 2.4
96.0
86.
LABORATORY NO.: 10/6/83 Page 2
J-23-63
TABLE XI TYPICAL BASE GASOLINE STREAMS LAKE CHARLES REFINERY - SUMMER 1983
Ponca City Sample No.: Lake Charles Sample No.: Stock:
Gravity, API
Distillation, D-86, F, 760 nun
IBP 5% Evaporated 10% Evaporated 20% Evaporated 30% Evaporated 50% Evaporated 70% Evaporated 90% Evaporated 95% Evaporated End Point Recovery, Vol.%
Reid Vapor pressure, psi Sulfur, Wt.% Aromatics, Vol.% Olefins, Vol.% Existent ASTM Gum, mg./lOO mis.
Benzene, Vol.%
Research Octanes
Clear 0.25 gras./gal. TEL 0.5 gms./gal. TEL 1.5 gms./gal. TEL
1610 726 FCC
Gasoline
53.6
100 117 129 149 171 231 300 383 407 444
98
7.7 0.11
33 34
2
0.7
93.2 94.3 95.9 97.7
1603 719
No.2 Lt. St. Run Gasoline
64.0
122 156 165 176 185 205 222 245 255 276
98
5.0 <0.01
8 <1
1
1.7
63.6 66.8 69.2 78.0
Motor Octanes
Clear 0.25 gms./gal. TEL 0.5 gms./gal. TEL 1.5 gms./gal. TEL
80.3 81.5 82.2 84.0
63.1 66.6 69.6 78.3
1604 720
No.3 Lt. S t. Run Gasoline
69.8
1608 724
Denuded Casinghead
78.6
119 134 141 149 156 167 178 197 205 221
98
7.7 <0.01
6 <1
1
3.5
96 105 109 114 118 131 163 221 249 304
97
11.1 <0.01
3 1 1
1.5
70.3 73.4 76.4 84.0
74.0 77.1 80.0 87.3
68.4 71.3 74.5 81.6
72.0 75.6 79.1 85.6
SAL 000004202
LABORATORY NO.: 10/6/83 Page 3
J-23-83
TABLE II (Continued) TYPICAL BASE GASOLINE STREAMS LAKE CHARLES REFINERY - SUMMER 1983
Ponca City Sample No.: Lake Charles Stock No.: Stock:
Gravity, API
Distillation, D-86, F, 760 mm
IBP 5% Evaporated 102 Evaporated 20% Evaporated 30% Evaporated 50% Evaporated 70% Evaporated 90% Evaporated 95% Evaporated End Point Recovery, Vol.%
Reid Vapor Pressure, psi Sulfur, Wt.% Aromatics, Vol.% Olefins, Vol.% Existent ASTM Gum, mg./lOO mis.
Benzene, Vol.%
Research Octanes
Clear 0.25 gins. /gal. TEL 0.5 gms./gal. TEL 1.5 gms./gal. TEL
Motor Octanes
Clear 0.25 gms./gal. TEL 0-5 gms./gal. TEL 1.5 gms./gal. TEL
1607 723
Cat Poly Gasoline
62.8
97 -- 162 230 249 274 296 342 376 424
94
10.3 <0.01
<1 97 13
<0.1
95.3 96.7 97.5 99.4
. ~x_r
82.6 83.5 84.0 85.4
1605 721
Alkylate
71.2
79 107 136 180 207 221 230 269 341 429
97
9.4 <0.01
<1 1 2
<0.1
96.0 98.2 100.3 103-5
92.0 95.0 97.6 100.2
1606 722
Coker Gasoline
61.9
124 134 153 185 205 233 264 296 312 362
97
10.3 0.24
8 45
2
0-1
72.0 73.2 74.2 78.8
65.1 66.0 67.2 71.0
SAL 000004203
LABORATORY NO.:
10/6/83 page 4
J-23-83
TABLE II (Continued) TYPICAL BASE GASOLINE STREAMS LAKE CHARLES REFINERY - SUMMER 1983
Ponca City Sample No.: Lake Charles Sample No.: Stock
Gravity, "API
Distillation, D-86, F, 760 mm
IBP 5% Evaporated 10% Evaporated 20% Evaporated 30% Evaporated 50% Evaporated 70% Evaporated 90% Evaporated 95% Evaporated End Point Recovery, Vol.%
Reid Vapor Pressure, psi Sulfur, Wt.% Aromatics, Vol.% Olefins, Vol.% Existent ASTM Gum, mg./lOO mis.
Benzene, Vol.%
Research Octanes
Clear 0.25 gins./gal. TEL 0.5 gins./gal. TEL 1.5 gms./gal. TEL
Motor Octanes
Clear 0.25 gms./gal. TEL 0.5 gms./gal. TEL 1.5 gms./gal. TEL
Approved:
1611 727
No. 2 Reformer
Charge
57.5
129 181 208 225 234 259 283 312 321 339
97
8.2 <0.01
11 1
<1
1.0
53.8 56.4 59.4 68.7
53.4 56.3 60.8 71.4
1609 725
No. 2 Reformate
49.1
115 148 163 184 201 240 278 321 338 388
98
5.5 <0.01
49 1 2
3.8
94.7 96.3 97.7 100.0
85.2 86.6 88.0 90.5
1781 858
No. 3 Reformate
44.4
101 125 146 178 203 246 281 325 344 404
98
7.9 <0.01
63 1 1
6.0
100.9 102.0 102.8 104.3
'
89.0 89.6 90.2 92.2
Senior Technologist hp v/
Associate technologist SAL 000004204
10/6/33' tel MOTOR ANTIKNOCK SUSCEPTlBiU i y lhak 1
Attachment, Page 1 TETRAETHYL LEAD, MILLILITERS PER GALLON
0.0 0.5 1 .0 1 .5 2.0 2.5 3.0 3.5 4.0
*n rn
FIGURE
Lake C h a rle s - Summer 1983
" 0.0
ocuu
QL
0.5 1.0 1.5 2.0
GRAMS OF LEAD PER GALLON
2.5 3.0 3.5 4.0 4.c
flD
PETROLEUM CHEMICALS DIVISION
E. 1. DU PONT OE NEMOURS 4 CO. tIHC.) WILMINGTON 98, DELAWARE
SAL 000004-205
RECEIVED DEC 0 7 809
CONOCO INC. PONCA CITY. OKLAHOMA
Pit.:
TECHNICAL SERVICES LABORATORY
File:
Date:
LABORATORY NO.: L-4-89
CHARGE:
TSL-LC
SUBJECT:
Gasoline Blending Study - Lake Charles Refinery
LC 662.1 12/1/89
DISCUSSION:
Eleven samples were submitted for analysis to determine the compositional make-up of eight gasoline blending streams and three finished gasoline blends. Analyses requested were lights ends, aromatics, carbon type distribution, gravity, distillation, and vapor pressure.
ANALYTICAL DATA: Attached
REFERENCE:
Verbal request from Bill Cason, Houston. Letter to Clifford Mills from R. W. Armstrong dated 11/20/89.
Approved:
jcb cc: DRU/PFM-ESJ-SO-LTW-RWA-RHC-WWC-TGW-F
SAL 000004206
L-4-89 12/1/89
Page 2
LAKE CHARLES REFINERY GASOLINE STUDY - 11/14/89
Sample Description: Sample Number:
Poly Gaso LC 1518-89
PC 1497
ComDOsitional Analysis
Ethane Propane Propylene Iso-butane N-butane Total Butylenes Iso-pentane N-pentane Total Anylenes Cyclo pentane C6 PNO C6 Aromatic C7 PNO C7 Aromatic C8 PNO C8 Aromatic C9 PNO C9 Aromatic CIO PNO CIO Aromatic Cll PNO Cll plus Aromatic C12 plus PNO
- LV%
--
--
--
0.01
--
6.81 6.98 1.34 0.21 9.06
--
12.70
--
12.28
--
27.38
--
11.33
--
4.77
--
7.13
W-10 OVHD LC 1519-89
PC 1498
--
--
0.02 0.19
--
12.71 28.72
0.22 3.31 48.72 3.15 2.80 0.05 0.07 0.01 0.02 0.01
--
--
--
--
--
FCC Gaso LC 1520-89
PC 1499
--
--
0.39 0.63 3.08 7.77 1.17 9.62 0.57 16.92 0.50 13.18 2.40 8.73 5.06 5.36 5.39 3.20 4.24 1.88 7.98 1.93
Alkyl ate LC 1521-8'
PC 1500
--
--
2.84 14.63
--
7.36 0.23
--
--
7.54
--
11.50
--
31.83
--
7.37
--
3.34
--
4.86
--
8.50
SAL 000004207
L-4-89 12/1/89 Page 3
LAKE CHARLES REFINERY GASOLINE STUDY - 11/14/89
Sample Description: Sample Number:
Casinghead Gaso.
LC 1522-89 PC 1501
Cnmoositlonal Analysis; - LV%
Ethane
Propane
--
Propylene
--
Iso-butane
0.08
N-butane
3.46
Total Butylenes
0.04
Iso-pentane
18.04
N-pentane
13.82
Total Anylenes
0.11
Cyclo pentanes
0.96
C6 PNO
27.05
C6 Aromatic
3.27
C7 PNO
13.33
C7 Aromatic
5.49
C8 PNO
3.44
C8 Aromatic
5.27
C9 PNO
0.83
C9 Aromatic
3.09
CIO PNO
0.21
CIO Aromatic
0.74
Cll PNO
0.01
Cll plus Aromatic
0.41
C12 plus PNO
0.35
Leaded Reg. Gaso.
LC 1523-89 PC 1502
Reg. Unleaded Gaso.
LC 1524-89 PC 1503
Prem. Unleaded Gaso.
LC 1525-89 PC 1504
0.01 0.06 0.01 1.23 9.81 0.29 8.10 8.81 3.57 0.88 19.15 2.83 8.76 7.79 3.26 11.09 0.90 8.20 0.19 2.83 0.07 1.65 0.51
0.01 0.09
--
1.31 8.73 1.45 7.98 4.90 5,56 0.67 17.29
1.71 10.55
5.24 5.98 7.92 3.44 6.38 1.77 2.99 1.03 3.98 1.02
trace 0.11
--
1.65 13.43
0.19 5.41 3.00 0.91 0.26 10.46 2.63 8.40 8.56 13.30 12.63 2.22 9.38 0.66 3.06 0.58 1.98 1.18
000^08
L-4-89 12/1/89 Page 4
LAKE CHARLES REFINERY GASOLINE STUDY - 11/14/89
Sample Descriptions Sample Number:
Compositional Analysis - LV% Ethane Propane Propylene Iso-butane N-butane Total Butylenes Iso-pentane N-pentane Total Anylenes Cyclo pentane C6 PNO C6 Aromatic C7 PNO C7 Aromatic C8 PNO C8 Aromatic C9 PNO C9 Aromatic CIO PNO CIO Aromatic Cll PNO Cll plus Aromatic C12 plus PNO
No. 2 Reformate LC 1526-89 PC 1505
--
0.12
--
1.56 3.19 0.05 4.77 3.55 0.12 0.31 14.80 4.26 11.34 13.22 4.65 18.46 1.35 12.74 0.19 3.23 0.02 2.07
--
No. 3 Reformate LC 1527-89 PC 1506
--
--
--
0.73 2.32 0.04 3.20 2.05 0.12 0.17 9.70 4.38 10.93 14.94 3.89 22.21 0.86 16.32 0.11 5.12 0.06 2.85
--
Prim TWR OVHD LC 1528-89 PC 1507
--
--
--
0.29 3.75 1.30 9.73 20.70 12.80 2.74 43.07 0.83 4.63 0.05 0.05 0.02 0.03 0.01
--
--
--
--
--
$4L 00oo*?09
L-4-89 12/1/89 Page 5
LAKE CHARLES REFINERY GASOLINE STUDY - 11/14/89
Sample Description: Sample Number:
Poly Gaso LC 1518*89
PC 1497
H-10 OVHD LC 1519-89
PC 1498
RVP by Cetavap, psi Gravity, API 0 60*F
4.7 63.8
10.7 79.9
D-86 Distillation, IBP 5% Evaporated 10% Evaporated 15% Evaporated 20% Evaporated 25% Evaporated 30% Evaporated 35% Evaporated 40% Evaporated 45% Evaporated 50% Evaporated 55% Evaporated 60% Evaporated 65% Evaporated 70% Evaporated 75% Evaporated 80% Evaporated 85% Evaporated 90% Evaporated 95% Evaporated End Point Recovery, ml Residue, ml Loss, ml
*F corrected to 760 mm Ha.
105 101
144 115
161 116
173 117
184 118
196 119
209 121
224 122
237 124
248 125
258 127
265 139
273 131
280 134
287 137
295 140
304 143
316 147
334 151
367 156
423 170
98.1
98.5
1.5 1.0
0.4 0.5
FCC Gaso LC 1520-89
PC 1499
8.0 57.0
91 116 130 140 149 159 169 181 194 208 222 237 253 269 285 303 321 341 361 386 413 98.4 1,3 0.3
A1 kyl ate LC 1521-89
PC 1500
13.1 72.8
83 92 108 122 139 158 177 193 206 214 221 227 233 239 247 257 271 299 340 373 457 95.4 1.0 3.6
SAL 000004210
L-4-89 12/1/89 Page 6
LAKE CHARLES REFINERY GASOLINE STUDY - 11/14/89
Sample Description: Sample Number:
Casinghead Gaso.
LC 1522-69 PC 1501
Leaded Reg. Gaso.
LC 1523-89 PC 1502
RVP by Cetavap, psi Gravity, API @ 60F
10.4 69.3
12.7 60.8
D-86 Distillation.
IBP 5% Evaporated
10% Evaporated 15% Evaporated 20% Evaporated 25% Evaporated 30% Evaporated 35% Evaporated 40% Evaporated 45% Evaporated 50% Evaporated 55% Evaporated 60% Evaporated 65% Evaporated 70% Evaporated 75% Evaporated 80% Evaporated 85% Evaporated 90% Evaporated 95% Evaporated End Point Recovery, ml Residue, ml Loss, ml
`F corrected to 760 mm Ha.
92 82
111 95
116 105
120 113
124 121
127 130
131 138
136 148
140 158
146 168
152 179
159 191
167 204
176 219
186 235
197 251
210 268
226 285
247 301
280 321
332 375
98.2
97.6
1.0 1.2
0.8 1.2
Reg. Unleaded Gaso.
LC 1524-89 PC 1503
12.6 60.8
Prem. Unleaded Gaso.
LC 1525-89 PC 1504
13.3 57.6
82 94 105 115 124 133 143 155 168 180 194 208 223 238 253 270 287 305 324 354 412 97.2 1.3 1.5
80 91 105 119 135 153 171 187 201 213 223 232 240 249 258 269 281 296 311 330 388 95.7 1.3 3.0
SAL 0000042H
L-4-89 12/1/89 Page 7
LAKE CHARLES REFINERY GASOLINE STUDY - 11/14/89
Sample Description: Sample Number:
No. 2 Reformate LC 1526-89 PC 1505
No. 3 Reformate LC 1527-89 PC 1506
RVP by Cetavap, psi Gravity, API @ 60*F
7.4 50.0
5.0 43.5
D-86 Distillation. IBP 5% Evaporated 10% Evaporated 15% Evaporated 20% Evaporated 25% Evaporated 30% Evaporated 35% Evaporated 40% Evaporated 45% Evaporated 50% Evaporated 55% Evaporated 60% Evaporated 65% Evaporated 70% Evaporated 75% Evaporated 80% Evaporated 85% Evaporated 90% Evaporated 95% Evaporated End Point Recovery, ml Residue, ml Loss, mi
*F corrected to 760 mm Ha. 97
133 149 163 175 186 196 205 215 224 232 240 250 258 268 277 286 297 308 325 391 98.1
1.0 0.9
109 155 177 193 203 213 222 231 239 246 254 262 269 276 284 291 300 309 320 337 400 98.4 1.0 0.6
Prim TWR OVHD LC 1528-89 PC 1507
13.1 81.0
87 103 106 108 110 112 114 116 119 121 123 126 128 131 134 138 142 147 152 159 184 98.2 1.0 0.8
SAL 000004212