Comparative techno-economic analysis of biohydrogen production via bio-oil gasification and bio-oil reforming

被引：87
作者：
Zhang, Yanan [1 ]
Brown, Tristan R. [2 ]
Hu, Guiping [3 ]
Brown, Robert C. [1 ,2 ]
机构：
[1] Iowa State Univ, Dept Mech Engn, Bioecon Inst, Ames, IA 50011 USA
[2] Iowa State Univ, Bioecon Inst, Ames, IA 50011 USA
[3] Iowa State Univ, Ames, IA 50011 USA
来源：
BIOMASS & BIOENERGY | 2013年 / 51卷
基金：
美国国家科学基金会;
关键词：
Fast pyrolysis; Bio-oil; Reforming; Gasification; Biohydrogen; HYDROGEN-PRODUCTION; BIOMASS GASIFICATION; STEAM GASIFICATION; FAST-PYROLYSIS; AQUEOUS FRACTION; PERFORMANCE; CAO;
D O I：
10.1016/j.biombioe.2013.01.013
中图分类号：
S2 [农业工程];
学科分类号：
0828 ;
摘要：
This paper evaluates the economic feasibility of biohydrogen production via two bio-oil processing pathways: bio-oil gasification and bio-oil reforming. Both pathways employ fast pyrolysis to produce bio-oil from biomass stock. The two pathways are modeled using Aspen Plus (R) for a 2000 t d(-1) facility. Equipment sizing and cost calculations are based on Aspen Economic Evaluation software. Biohydrogen production capacity at the facility is 147 t d(-1) for the bio-oil gasification pathway and 160 t d(-1) for the bio-oil reforming pathway. The biomass-to-fuel energy efficiencies are 47% and 84% for the bio-oil gasification and bio-oil reforming pathways, respectively. Total capital investment (TCI) is 435 million dollars for the bio-oil gasification pathway and is 333 million dollars for the bio-oil reforming pathway. Internal rates of return (IRR) are 8.4% and 18.6% for facilities employing the bio-oil gasification and bio-oil reforming pathways, respectively. Sensitivity analysis demonstrates that biohydrogen price, biohydrogen yield, fixed capital investment (FCI), bio-oil yield, and biomass cost have the greatest impacts on facility IRR. Monte-Carlo analysis shows that bio-oil reforming is more economically attractive than bio-oil gasification for biohydrogen production. (C) 2013 Elsevier Ltd. All rights reserved.
引用
收藏
页码：99 / 108
页数：10
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