Biomass-based hydrogen for oil refining: Integration and performances of two gasification concepts

被引:13
作者
Brau, Jean-Florian [1 ]
Morandin, Matteo [1 ]
机构
[1] Chalmers Univ Technol, Environm & Energy Dept, Div Heat & Power Technol, S-41296 Gothenburg, Sweden
关键词
Process integration; Hydrogen; Refinery; Energy systems; Modelling; Biomass gasification; ENERGY; GAS; PURIFICATION;
D O I
10.1016/j.ijhydene.2013.10.157
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
In this work, two biomass-to-hydrogen concepts are designed and their integration with a large European refinery is investigated. One concept is based on indirect, atmospheric steam gasification while the second is based on pressurized direct oxygen-steam-blown gasification. The technologies chosen for gas cleaning, upgrading and hydrogen separation also differ in the two concepts. Heat integration and poly-generation opportunities are identified by means of process integration tools and four system configurations are identified. These are compared in terms of energy and exergy performances and potential for reduction of fossil CO2 emissions at the refinery. It is found that the performance of the biomass-to-hydrogen concepts can be improved by up to 11% points in energy efficiency and 9% points in exergy efficiency. The design based on indirect gasification appears the most efficient according to both energy and exergy efficiencies. All configurations yield potential significant reductions of fossil CO2 emissions at the refinery. Copyright (C) 2013, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:2531 / 2542
页数:12
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