Page 109 - Biofuels for a More Sustainable Future

96 Biofuels for a More Sustainable Future

Consumption 1t b for 0.24kWh 14.31g 9.40kWh 206.80kg 2.66kWh 31.0kJ/kg syngas, reformed

consumption 3kJ/kg syngas 600°C): e (15bar kg steam /kg syngas 140kJ/kg syngas 350°C) e (22bar 31kJ/kg syngas MJ/ 1.95 reformed

Unit Electrical: Steam 0.06 Electrical: Steam Electrical: Thermal: kg syngas

route—cont’d characteristics and H 2 into the in 800°C and the H 2 / the that the steps: two and 350°C at the and and 200°C at The 220°C 25bar, the maximize for produced accomplished of thermal energy in

thermochemical and syngas into CH4 injected is syngas 15bar at between so gases, of in Occurs reactor a in injected, is steam reactor a in liquids. FT into at occurs to catalysts (α¼0.88) diesel hydrocarbons is Distillation the provision columns.

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