| storage capacity biocrude
(h) |
12.00 |
| preheated biocrude
temperature
before pumping (deg. C) |
40.00 |
| guard reactor temperature |
290.00 |
| guard reactor pressure |
100.00 |
| guard reactor hydrogen consumption
(Nm3/m3 feed) |
574 |
| guard reactor hydrogen reacted
(% wt. feed) |
0.52 |
| guard reactor
catalyst WHSV
(kg/kg/h) |
0.40 |
| guard reactor
catalyst lifetime
(h) |
16000.00 |
| hydrotreating
temperature |
360.00 |
| hydrotreating
pressure |
100.00 |
| hydrotreating
hydrogen consumption
(Nm3/m3 feed) |
1747 |
| hydrotreating hydrogen reacted
(% wt. feed) |
1.57 |
| hydrotreating
catalyst WHSV
(kg/kg/h) |
0.40 |
| hydrotreating
catalyst lifetime
(h) |
16000.00 |
| hydrocracking
temperature
(deg. C) |
370.00 |
| hydrocracking
pressure (bar-g) |
100.00 |
| hydrocracking
hydrogen consumption
(Nm3/m3) |
2400.00 |
| hydrocracking hydrogen reacted
(% wt. feed) |
5.4 |
| hydrocracking
catalyst WHSV
(kg/kg/h) |
0.50 |
| hydrocracking
catalyst lifetime
(h) |
16000.00 |
| temperature at
three-phase
high-pressure separator (deg. C) |
40.00 |
| pressure at three-phase
high-pressure separator |
100.00 |
| temperature at three-phase
low-pressure separator (deg. C) |
240.00 |
| pressure at three-phase
low-pressure separator |
2.00 |
| inlet temperature at distillation
column (deg. C) |
400.00 |
| pressure distillation
column
(bar-g) |
1.013 |
| naphtha cut-off
temperature
at distillation (deg. C) |
95 |
| diesel
cut-off temperature
at distillation (deg. C) |
210 |
| heavy-fraction
cut-off boiling
point (deg. C) |
310.00 |
| diesel range
cut-off boiling
point (deg. C) |
210.00 |
| naphtha cut-off
boiling
point (deg. C) |
80.00 |
| amine absorber
temperature
(deg. C) |
40.00 |
| amine absorber
pressure
(bar-g) |
30.00 |
| make-up amine
consumption
(% wt. feed gas) |
7.00 |
| heating amine
plant (MJ/kg
feed gas) |
0.272 |
| net cooling amine
plant
(MJ/kg feed gas) |
0.40 |
| electric power
consumption
amine plant (kWh/kg feed gas) |
46.50 |
