公开(公告)号：US20130125877A1

公开(公告)日：2013-05-23

申请号：US13813583

申请日：2011-09-27

申请人： Hiromasa Kusuda ,  Noriaki Izumi ,  Hironori Tajiri ,  Shoji Tsujita ,  Takeshi Nishino ,  Kunihiko Tanaka

发明人： Hiromasa Kusuda ,  Noriaki Izumi ,  Hironori Tajiri ,  Shoji Tsujita ,  Takeshi Nishino ,  Kunihiko Tanaka

IPC分类号： D21C5/00

CPC分类号： D21C5/00 ,  C10L1/02 ,  C13K1/02

摘要： The hydrolytic saccharification method and hydrolytic saccharification apparatus according to the present invention use a hydraulic cylinder-type pressurized reactor as a reactor for causing cellulosic biomass to be in a supercritical or subcritical state, and use a hydraulic cylinder-type steam compressor as a source of superheated steam, such that the reactor and the compressor are operated in conjunction with each other. Surplus hydraulic pressure that is generated when hydrolysis of the cellulosic biomass is completed is recovered as compression power of the hydraulic cylinder-type steam compressor. Moreover, flash steam generated from slurry containing a hydrolysate is supplied to the hydraulic cylinder-type steam compressor for cyclic use of the flash steam.

摘要翻译： 根据本发明的水解糖化方法和水解糖化装置使用液压缸式加压反应器作为使纤维素生物质处于超临界或亚临界状态的反应器，并且使用液压缸型蒸汽压缩机作为 过热蒸汽，使得反应器和压缩机彼此结合操作。 作为液压缸式蒸汽压缩机的压缩功率，回收在纤维素生物质的水解完成时产生的剩余液压。 此外，由含有水解产物的浆料产生的闪蒸提供给液压缸型蒸汽压缩机以循环使用闪蒸。

公开(公告)号：US20130171709A1

公开(公告)日：2013-07-04

申请号：US13823436

申请日：2011-09-27

申请人： Hiromasa Kusuda ,  Noriaki Izumi ,  Hironori Tajiri ,  Shoji Tsujita ,  Takashi Nishino

发明人： Hiromasa Kusuda ,  Noriaki Izumi ,  Hironori Tajiri ,  Shoji Tsujita ,  Takashi Nishino

IPC分类号： C12P7/10

CPC分类号： C12P7/10 ,  C13K1/02 ,  Y02E50/16 ,  Y02E50/17 ,  Y02P20/544

摘要： A method for producing ethanol by alcohol fermentation of a saccharide obtained by hydrolyzing cellulosic biomass in a supercritical or subcritical state, wherein excessive decomposition and caramelization of the saccharide are inhibited to prevent a reduction in yield of the saccharide, and flash steam is effectively used. The method for producing ethanol of the present invention is characterized in that in a saccharification/decomposition step, a slurry after saccharification/decomposition, is flash-evaporated in a first flash tank so as to have a temperature of 150° C. to 200° C.; the slurry after saccharification/decomposition, which is taken from the first flash tank, is further flash-evaporated in a second flash tank so as to have a temperature of 100° C. to 120° C.; and first flash steam generated from the first flash tank is used as a heat source in the saccharification/decomposition step or a distillation step.

摘要翻译： 通过水解超临界或亚临界状态的纤维素生物质获得的糖类的醇发酵生产乙醇的方法，其中抑制糖的过度分解和焦糖化以防止糖的收率降低，并且有效地使用闪蒸。 本发明的制造乙醇的方法的特征在于，在糖化/分解步骤中，糖化/分解后的浆料在第一闪蒸罐中闪蒸，以使其温度为150℃至200℃ C。; 糖化/分解后从第一个闪蒸罐中取出的浆料在第二个闪蒸罐中进一步闪蒸，使其温度为100℃至120℃。 并且在糖化/分解步骤或蒸馏步骤中使用从第一闪蒸罐产生的第一闪蒸蒸汽作为热源。