发明授权
EP2430076B1 PRETREATMENT OF LIGNOCELLULOSIC BIOMASS THROUGH REMOVAL OF INHIBITORY COMPOUNDS
无效
木质纤维素生物质通过除去抑制剂的化合物的制备
- 专利标题: PRETREATMENT OF LIGNOCELLULOSIC BIOMASS THROUGH REMOVAL OF INHIBITORY COMPOUNDS
- 专利标题(中): 木质纤维素生物质通过除去抑制剂的化合物的制备
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申请号: EP10766534.1申请日: 2010-04-07
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公开(公告)号: EP2430076B1公开(公告)日: 2014-06-11
- 发明人: DOTTORI, Frank, A. , BENSON , Robert , Ashley Cooper , BENECH, Régis-Olivier
- 申请人: Greenfield Ethanol Inc.
- 申请人地址: 20 Toronto Street Suite 1400 Toronto, Ontario M5C 2B8 CA
- 专利权人: Greenfield Ethanol Inc.
- 当前专利权人: Greenfield Ethanol Inc.
- 当前专利权人地址: 20 Toronto Street Suite 1400 Toronto, Ontario M5C 2B8 CA
- 代理机构: Tombling, Adrian George
- 优先权: US170805P 20090420
- 国际公布: WO2010121348 20101028
- 主分类号: C08H8/00
- IPC分类号: C08H8/00 ; C08B1/00 ; C13K1/02 ; C12P7/10 ; C12P19/14 ; D21B1/36
摘要:
A process for the pretreatment of lignocellulosic biomass is disclosed. The process is intended for use in connection with biomass to ethanol processes and is directed in particular to an economical removal of inhibitory compounds generated in biomass pretreatment, which are inhibitory to downstream hydrolysis and fermentation steps. The process includes the steps of heating the lignocellulosic biomass with steam to a preselected temperature, at a preselected pressure and for a preselected time to hydrolyze and solubilize hemicelluloses in the biomass; explosively decomposing the biomass into fibers; and extracting from the resulting reaction mixture a liquefied portion of the lignocellulosic biomass before or after explosive decomposition. The liquefied portion is extracted to remove compounds from the lignocellulosic biomass which are inhibitory to enzymatic cellulose hydrolysis and sugar fermentation to ethanol. For improved efficiency and economy, the inhibitory compounds are not completely removed. Furthermore, xylose has been found to be a good indicator compound for the general level of inhibitory compounds in the reaction mixture and the extraction step is therefore controlled on the basis of the xylose content in the reaction mixture. In particular, the extracting step is discontinued once a dry matter (dm) content of xylose, as monomer or oligomer, in the reaction mixture of 4% to 8% (w/w dm) is achieved. This most economically balances the practical need for inhibitory compound removal with the economical need to control and preferably minimize the costs of the overall ethanol production process.
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