Isobutanol from glycerine - A techno-economic evaluation of a new biofuel production process

被引:16
作者
Bauer, Fredric [1 ]
Hulteberg, Christian [1 ]
机构
[1] Lund Univ, Dept Chem Engn, SE-22100 Lund, Sweden
关键词
Glycerine; Isobutanol; Biofuel; Process integration; Techno-economic analysis; CRUDE GLYCEROL; CLOSTRIDIUM-PASTEURIANUM; BIODIESEL; FERMENTATION; CONVERSION; FEEDSTOCK; ETHANOL; FUTURE; FUELS;
D O I
10.1016/j.apenergy.2014.02.037
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The paper presents a new thermochemical process for the production of isobutanol, which is an excellent biobased gasoline blendstock. The main feedstock for the process is glycerine, obtained as a byproduct in biodiesel production, being used together with methanol. The process was modeled in Aspen Plus. The process design is characterized by a high level of process integration, pinch analysis being used to optimize the process from the start. A techno-economic evaluation of the process, both in a stand-alone plant and in a plant integrated with an existing petro-refinery was conducted, the estimates for the production cost of isobutanol obtained being 892 $/m(3) for a refinery-integrated case and 1017 $/m(3) for a stand-alone case. A sensitivity analysis using Monte Carlo methodology showed the production cost estimates to be highly robust. Use of isobutanol rather than fossil gasoline was found to result in 53% reduction in GHG emissions. (c) 2014 Elsevier Ltd. All rights reserved.<>
引用
收藏
页码:261 / 268
页数:8
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