Reactor systems for syngas fermentation processes: A review

被引:138
作者
Asimakopoulos, Konstantinos [1 ]
Gavala, Hariklia N. [1 ]
Skiadas, Ioannis V. [1 ]
机构
[1] Tech Univ Denmark, Dept Chem & Biochem Engn, Soltofts Plads 229, DK-2800 Lyngby, Denmark
关键词
Synthesis gas; Syngas fermentation; Bioreactor configurations; Biochemicals; Biofuels; Mass transfer; MONOXIDE MASS-TRANSFER; HOLLOW-FIBER MEMBRANE; SYNTHESIS GAS FERMENTATION; CLOSTRIDIUM-CARBOXIDIVORANS P7; CARBON-MONOXIDE; BUTANOL PRODUCTION; ETHANOL-PRODUCTION; TRICKLE-BED; TRANSFER COEFFICIENT; BIOFILM REACTOR;
D O I
10.1016/j.cej.2018.05.003
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Implementation of biofuels as an alternative to fossil fuels has been established as an answer to climate change by limiting GHG emissions. Syngas fermentation has emerged as a promising process for the conversion of waste biomasses to valuable products with bioethanol being on the main focus. However, the bottleneck of the mass transfer of syngas compounds H-2 and CO along with low production yields has set barriers to the development of an industrial scale plant. Recent research indicates that many different methodologies spring up in order to face this important challenge. The aim of this review is to assemble all these techniques applied in syngas fermentation, focusing on the different bioreactor configurations operated in continuous mode for the production of liquid and gas biofuels. This article also outlines the so far entrepreneurial initiatives and the progress made towards the commercialization of the process.
引用
收藏
页码:732 / 744
页数:13
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