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Typical Component Data
Default date for gasoline components
are included in the programs. Those data, based on a 1989 National
Petroleum Refiners Association Survey, are reproduced here.
Data in the programs for toluene, oxygenates and
pressurizing agent cannot be changed. Hydrocarbons included in the
pressurizing agent composition are listed below.
Typical Component Inspection Data
Component Octane Properties
| # |
Component ID |
Type |
RON |
MON |
| == |
=========== |
==== |
===== |
==== |
| 1 |
Alkylate |
ALKY |
93.20 |
91.10 |
| 2 |
Lt. Reformate |
LTRF |
82.80 |
77.50 |
| 3 |
Hvy. Reformate |
HYRF |
104.90 |
94.50 |
| 4 |
FBReformate |
FBRF |
97.70 |
87.40 |
| 5 |
Lt. Cat Cracked |
LTCC |
92.60 |
80.80 |
| 6 |
Hy Cat Cracked |
HYCC |
91.90 |
81.30 |
| 7 |
FB Cat Cracked |
FBCC |
92.10 |
80.70 |
| 8 |
Lt. Str. Run |
LTSR |
74.10 |
72.10 |
| 9 |
Polymer |
POLY |
94.40 |
81.90 |
| 10 |
Isoparaffinic |
ISOP |
85.40 |
82.80 |
| 11 |
Raffinate |
RAFF |
60.00 |
59.40 |
| 12 |
Coker |
COKE |
82.00 |
74.50 |
Component Reid Vapor Pressure Properties
| # |
Component ID |
Type |
RVP |
SpGr |
API |
Arom |
Olef |
| == |
=========== |
==== |
==== |
===== |
==== |
=== |
=== |
| 1 |
Alkylate |
ALKY |
7.90 |
0.6998 |
70.70 |
0.0 |
0.0 |
| 2 |
Lt. Reformate |
LTRF |
7.90 |
0.7347 |
61.10 |
31.0 |
0.0 |
| 3 |
Hvy. Reformate |
HYRF |
1.30 |
0.8565 |
33.70 |
87.0 |
0.0 |
| 4 |
FB Reformate |
FBRF |
5.30 |
0.8012 |
45.10 |
63.0 |
0.0 |
| 5 |
Lt. Cat Cracked |
LTCC |
9.90 |
0.7071 |
68.60 |
14.0 |
40.0 |
| 6 |
Hy Cat Cracked |
HYCC |
2.60 |
0.8076 |
43.70 |
60.0 |
17.0 |
| 7 |
FB Cat Cracked |
FBCC |
7.10 |
0.7531 |
56.40 |
29.0 |
29.0 |
| 8 |
Lt. Str. Run |
LTSR |
13.30 |
0.6665 |
80.80 |
3.0 |
0.0 |
| 9 |
Polymer |
POLY |
9.10 |
0.7093 |
68.00 |
0.0 |
95.0 |
| 10 |
Isoparaffinic |
ISOP |
15.60 |
0.6438 |
88.30 |
0.0 |
0.0 |
| 11 |
Raffinate |
RAFF |
3.90 |
0.6991 |
70.90 |
6.0 |
0.0 |
| 12 |
Coker |
COKE |
13.00 |
0.6823 |
75.90 |
4.0 |
35.0 |
Component ASTM Distillation (Degrees Fahrenheit)
| # |
ComponentID |
IBP |
5% |
10% |
20% |
30% |
40% |
50% |
60% |
70% |
80% |
90% |
95% |
FBP |
Res |
Rec |
| == |
============ |
==== |
==== |
==== |
==== |
==== |
==== |
==== |
==== |
==== |
==== |
==== |
==== |
==== |
==== |
==== |
| 1 |
Alkylate |
100 |
132 |
158 |
176 |
192 |
205 |
216 |
224 |
233 |
260 |
289 |
316 |
345 |
1.0 |
98.0 |
| 2 |
Lt. Reformate |
100 |
120 |
137 |
150 |
161 |
172 |
182 |
192 |
204 |
220 |
237 |
253 |
270 |
1.0 |
98.0 |
| 3 |
Hvy. Reformate |
243 |
256 |
266 |
279 |
289 |
294 |
299 |
309 |
320 |
334 |
347 |
361 |
374 |
1.0 |
98.0 |
| 4 |
FB Reformate |
100 |
136 |
169 |
196 |
220 |
239 |
256 |
272 |
289 |
311 |
334 |
356 |
379 |
1.0 |
98.0 |
| 5 |
Lt. Cat Cracked |
90 |
105 |
117 |
127 |
135 |
149 |
162 |
181 |
201 |
228 |
258 |
282 |
305 |
1.0 |
98.0 |
| 6 |
Hy Cat Cracked |
184 |
206 |
224 |
246 |
264 |
286 |
307 |
319 |
330 |
356 |
385 |
412 |
440 |
1.0 |
98.0 |
| 7 |
FB Cat Cracked |
100 |
115 |
128 |
147 |
165 |
194 |
220 |
250 |
284 |
324 |
366 |
398 |
430 |
1.0 |
98.0 |
| 8 |
Lt. Str. Run |
92 |
99 |
104 |
110 |
116 |
121 |
125 |
133 |
142 |
153 |
164 |
175 |
186 |
1.0 |
98.0 |
| 9 |
Polymer |
100 |
116 |
149 |
188 |
223 |
230 |
236 |
264 |
296 |
319 |
346 |
391 |
436 |
1.0 |
98.0 |
| 10 |
Isoparaffinic |
88 |
92 |
95 |
99 |
102 |
105 |
108 |
114 |
120 |
130 |
138 |
147 |
156 |
1.0 |
98.0 |
| 11 |
Raffinate |
100 |
142 |
176 |
182 |
188 |
193 |
198 |
207 |
217 |
233 |
250 |
266 |
283 |
1.0 |
98.0 |
| 12 |
Coker |
94 |
103 |
110 |
118 |
126 |
133 |
139 |
148 |
159 |
171 |
184 |
196 |
209 |
1.0 |
98.0 |
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Pressurizing agent composition - volume percent
Ethane . . 0.00
Propene . 0.00
Propane . 0.50
IsoButane . 3.50
IsoButene . 0.00
1-Butene . 0.00
N-Butane . 95.00
T-2-Butene . 0.00
C-2-Butene . 0.00
I-Pentane . 1.00
N-Pentane . 0.00
C5 Olefins . 0.00
C6+ . . . 0.00
Note: Pressurizing agent properties are generated based on the volumetric
composition as shown by the sample here.
The programs make available typical inspection data.
The user can update inspection data at any time.
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