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    • 2. 发明申请
    • SOLID AND LIQUID SEPARATION PROCESS
    • 固体和液体分离方法
    • WO2013013317A1
    • 2013-01-31
    • PCT/CA2012/050495
    • 2012-07-20
    • GREENFIELD ETHANOL INC.LEHOUX, Richard, RomeoBRADT, Christopher, Bruce
    • LEHOUX, Richard, RomeoBRADT, Christopher, Bruce
    • B01D1/26
    • B01D1/18B01D1/26B01D3/38C12C11/11C12F3/10F26B3/12F26B2200/02Y02E50/17
    • A process for separation of solid and liquid components in a distillation whole stillage utilizing airless spray drying is disclosed, which is more efficient and economical than conventional processes. In the process, distillation whole stillage resulting from distillation of fermented biomass is first subjected to an evaporation step for separating the whole stillage into a condensate and a concentrate including water, dissolved solids and suspended solids. The concentrate is then subjected to airless steam spray drying for converting the concentrate into dried solids, steam and vapors. All steam and vapors resulting from the airless steam spray drying step are then redirected as energy source to a processing step upstream of the airless spray drying step. At least some of the steam generated in the airless spray drying step is airless steam.
    • 公开了一种利用无空气喷雾干燥在蒸馏整体釜中分离固体和液体组分的方法,其比常规方法更有效和经济。 在此过程中,首先对发酵生物质蒸馏产生的蒸馏整体釜渣进行蒸发步骤,将整个釜馏塔分离成冷凝物和包含水,溶解固体和悬浮固体的浓缩物。 然后将浓缩物进行无空气蒸汽喷雾干燥,以将浓缩物转化为干固体,蒸汽和蒸气。 然后将由无空气蒸汽喷雾干燥步骤产生的所有蒸汽和蒸气作为能源重新定向到无气喷涂干燥步骤上游的处理步骤。 在无空气喷雾干燥步骤中产生的至少一些蒸汽是无空气蒸汽。
    • 10. 发明申请
    • PRETREATMENT OF LIGNOCELLULOSIC BIOMASS THROUGH REMOVAL OF INHIBITORY COMPOUNDS
    • 通过去除抑制性化合物预处理细菌生物量
    • WO2010121348A1
    • 2010-10-28
    • PCT/CA2010/000483
    • 2010-04-07
    • GREENFIELD ETHANOL INC.DOTTORI, Frank, A.BENSON , Robert , Ashley CooperBENECH, Régis-Olivier
    • DOTTORI, Frank, A.BENSON , Robert , Ashley CooperBENECH, Régis-Olivier
    • C08H8/00C08B1/00C13K1/02C12P7/10C12P19/14
    • D21B1/36C12P7/10C12P2201/00D21C1/02D21C5/005D21C11/0007Y02E50/16
    • 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.
    • 公开了木质纤维素生物质的预处理方法。 该方法旨在用于与生物质与乙醇方法有关的用途,特别涉及经济地除去生物预处理中产生的抑制性化合物,其抑制下游水解和发酵步骤。 该方法包括以预选压力将木质纤维素生物质用蒸汽加热至预选温度并预选水解和增溶生物质中的半纤维素的步骤; 将生物质爆炸分解成纤维,并从所得反应混合物中提取爆炸物分解之前或之后的木质纤维素生物质的液化部分。 提取液化部分以从木质纤维素生物质中除去抑制酶纤维素水解和糖发酵成乙醇的化合物。 为了提高效率和经济性,抑制性化合物不能完全去除。 此外,已经发现木糖是反应混合物中一般水平的抑制化合物的良好指示剂化合物,因此提取步骤是基于反应混合物中的木糖含量进行控制的。 特别是,一旦实现4%至8%(w / w dm)的反应混合物中的木糖,作为单体或低聚物的干物质(dm)含量,则提取步骤停止。 这最经济地平衡了抑制性化合物去除的实际需要与经济的控制需求并且优选地最小化整个乙醇生产过程的成本。