Page 108 - Biofuels for a More Sustainable Future

0.24kWh
9.40kWh
206.80kg
14.31g
1t b
for
140kJ/kg syngas
600°C):
350°C)
3kJ/kg syngas
kg steam /kg syngas
consumption
e
e
(22bar
(15bar
Electrical:
Electrical:
0.06
Steam
Steam
Unit
and
and
the
H 2 /
the
characteristics
800°C
steps:
H 2
350°C
the
and
the
into
the
two
in
and
that
injected,
at
between
syngas
injected
reactor
thermochemical 96 route—cont’d Consumption Biofuels for a More Sustainable Future and 200°C at reactor a in 2.66kWh 31kJ/kg syngas Electrical: The liquids. FT into 220°C 25bar, at occurs the maximize to catalysts (α¼0.88) diesel 31.0kJ/kg syngas, MJ/ 1.95 Thermal: for produced hydrocarbons kg syngas accompli
in
15bar
so
Occurs
and
gases,
into
is
is
a
at
steam
in
syngas
CH4
of
the objectives the Clean reactor relationship 2.01. is processed where occurs syngas reaction iron-based of the H 2 S). and
in all reforming the concentrations ratio is synthesis production utilization. through distillation (CO 2
involved Operational Convert CO. Adjust CO first 20bar second 20bar Convert with Separate removed
processes synthesis FT compounds
the Process Steam reforming gas- water Distillation the of liquids of
of Shift FT amount
Summary of bagasse. the to
4.5 conditioning Production FT liquid of refers
Table Step Syngas tonne t b , a kmol