会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 6. 发明授权
    • Method of producing compound originating from polysaccharide-based biomass
    • 生产多糖类生物质化合物的方法
    • US08497091B2
    • 2013-07-30
    • US12920128
    • 2009-02-27
    • Masayuki HanakawaShinichi MinegishiHiroyuki Kurihara
    • Masayuki HanakawaShinichi MinegishiHiroyuki Kurihara
    • C12P1/00C12P7/06C12N1/00B01D71/00
    • C12P19/40C12P7/04C12P7/06C12P7/16C12P7/56C12P13/001C12P19/04C12P19/14Y02E50/16Y02E50/17
    • A method of producing a compound originating from a polysaccharide-based biomass includes at least one of a saccharification step that produces a sugar solution containing a monosaccharide and/or an oligosaccharide from a product obtainable by hydrolyzing the polysaccharide-based biomass; a fermentation step that ferments the sugar solution containing the monosaccharide and/or oligosaccharide originating from the polysaccharide-based biomass; and a treatment that removes a fermentation inhibitor with the use of a separation membrane having a glucose removal rate and an isopropyl alcohol removal rate which simultaneously satisfy the following relationships (I) and (II) when a 500 ppm aqueous glucose solution at pH 6.5 at 25° C. and a 500 ppm aqueous isopropyl alcohol solution at pH 6.5 at 25° C. are respectively permeated through the membrane at an operation pressure of 0.5 MPa, prior to the saccharification step and/or in the step prior to the fermentation step: Glucose removal rate≧80%  (I) Glucose removal rate−Isopropyl alcohol removal rate≧20%  (II).
    • 一种生产源自多糖类生物质的化合物的方法包括从通过水解多糖类生物质获得的产物产生含有单糖和/或寡糖的糖溶液的糖化步骤中的至少一种; 发酵步骤,其发酵含有源自多糖类生物质的单糖和/或寡糖的糖溶液; 以及当pH为6.5的500ppm葡萄糖水溶液时,使用具有葡萄糖去除速率和异丙醇除去速率的分离膜除去发酵抑制剂的处理,其同时满足以下关系式(I)和(II) 25℃下的pH为6.5的500ppm异丙醇水溶液分别在糖化步骤之前和/或在发酵步骤之前的步骤中以0.5MPa的操作压力渗透通过膜 :葡萄糖去除率> = 80%(I)葡萄糖去除率 - 异丙醇去除率> = 20%(II)。
    • 9. 发明申请
    • METHOD OF PRODUCING COMPOUND ORIGINATING FROM POLYSACCHARIDE-BASED BIOMASS
    • 从多糖基生物质生产化合物的方法
    • US20110008826A1
    • 2011-01-13
    • US12920128
    • 2009-02-27
    • Masayuki HanakawaShinichi MinegishiHiroyuki Kurihara
    • Masayuki HanakawaShinichi MinegishiHiroyuki Kurihara
    • C12P1/00
    • C12P19/40C12P7/04C12P7/06C12P7/16C12P7/56C12P13/001C12P19/04C12P19/14Y02E50/16Y02E50/17
    • A method of producing a compound originating from a polysaccharide-based biomass includes at least one of a saccharification step that produces a sugar solution containing a monosaccharide and/or an oligosaccharide from a product obtainable by hydrolyzing the polysaccharide-based biomass; a fermentation step that ferments the sugar solution containing the monosaccharide and/or oligosaccharide originating from the polysaccharide-based biomass; and a treatment that removes a fermentation inhibitor with the use of a separation membrane having a glucose removal rate and an isopropyl alcohol removal rate which simultaneously satisfy the following relationships (I) and (II) when a 500 ppm aqueous glucose solution at pH 6.5 at 25° C. and a 500 ppm aqueous isopropyl alcohol solution at pH 6.5 at 25° C. are respectively permeated through the membrane at an operation pressure of 0.5 MPa, prior to the saccharification step and/or in the step prior to the fermentation step: Glucose removal rate≧80%  (I) Glucose removal rate−Isopropyl alcohol removal rate≧20%  (II).
    • 一种生产源自多糖类生物质的化合物的方法包括从通过水解多糖类生物质获得的产物产生含有单糖和/或寡糖的糖溶液的糖化步骤中的至少一种; 发酵步骤,其发酵含有源自多糖类生物质的单糖和/或寡糖的糖溶液; 以及当pH为6.5的500ppm葡萄糖水溶液时,使用具有葡萄糖去除速率和异丙醇除去速率的分离膜除去发酵抑制剂的处理,其同时满足以下关系式(I)和(II) 25℃下的pH为6.5的500ppm异丙醇水溶液分别在糖化步骤之前和/或在发酵步骤之前的步骤中以0.5MPa的操作压力渗透通过膜 :葡萄糖去除率≥80%(I)葡萄糖去除率 - 异丙醇除去率≥20%(II)。
    • 10. 发明授权
    • Spiral reverse osmosis membrane element, reverse osmosis membrane module using it, device and method for reverse osmosis separation incorporating the module
    • 螺旋反渗透膜元件,使用其的反渗透膜组件,结合模块的反渗透分离装置和方法
    • US06656362B1
    • 2003-12-02
    • US09485934
    • 2000-02-18
    • Masahiro KiharaShinichi MinegishiTakayuki Nakanishi
    • Masahiro KiharaShinichi MinegishiTakayuki Nakanishi
    • B01D6100
    • B01D65/00B01D61/022B01D63/10B01D63/12Y02A20/131
    • A spiral reverse osmosis membrane element of the present invention includes a plurality of bag-shaped reverse osmosis membranes, permeated liquid passage members arranged inside the reverse osmosis membranes, and a plurality of feed liquid passage members interposed between the reverse osmosis membranes, those membranes and passage members being wound around an outer surface of a hollow pipe in a manner that only the interiors of the reverse osmosis membranes communicate with through-holes formed in the surface of the hollow pipe. Each of the feed liquid passage members is a mesh member having series of quadrilateral meshes formed by a plurality of linear members crossing each other. Two opposite cross-points out of four cross-points of each of the quadrilateral meshes are in line in parallel with an axial direction of the hollow pipe. And relations 2 mm≦X≦5 mm and X≦Y≦1.8X are both satisfied where X denotes a distance between the cross-points in a direction perpendicular to the axial direction of the hollow pipe and Y denotes a distance between the cross-points in the axial direction of the hollow pipe.
    • 本发明的螺旋反渗透膜元件包括多个袋状反渗透膜,布置在反渗透膜内的渗透液通道构件和插入在反渗透膜之间的多个进料液通道构件, 通道构件以只有反渗透膜的内部与形成在中空管的表面中的通孔连通的方式围绕中空管的外表面缠绕。 每个进料液体通道构件是具有由彼此交叉的多个线性构件形成的一系列四边形网格的网状构件。 每个四边形网格的四个交叉点中的两个相对的交叉点与中空管的轴向平行。 并且关系2 mm <= X <= 5 mm,X <= Y <= 1.8X,其中X表示垂直于中空管的轴向方向的交点之间的距离,Y表示距离 在中空管的轴向的交叉点之间。