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    • 1. 发明申请
    • PARTICLE PUMP METHODS AND DEVICES
    • 颗粒泵方法和装置
    • WO2011024145A4
    • 2011-06-30
    • PCT/IB2010053864
    • 2010-08-27
    • INBICON ASFINK JENSNIELSEN POULSEN NIELS
    • FINK JENSNIELSEN POULSEN NIELS
    • B01J8/00C10J3/48C10J3/50
    • B01J8/002B01J3/02B01J8/0015B01J8/0035B01J2208/00743B01J2208/00752B01J2208/00761B01J2208/00769B65G53/48C12P2201/00Y02E50/32Y10T137/87917
    • Methods and devices are provided for transfer of particulate material, such as biomass feedstocks, into and out of pressurized reactors. Improved sluice devices have an L- shaped sluice chamber having an upper, vertical component in communication with a horizontal loading chamber and a lower component in communication with a vertical reactor inlet or outlet. Piston valves seal the sluice inlet and outlet by axial displacement across the vertical component of the sluice chamber and across the vertical reactor inlet or outlet. Relative to other methods for reactor unloading, these devices consume less steam and significantly reduce furfural content of unloaded, pretreated biomass. An optional hybrid plug/sluice method of biomass feeding using the devices permits biomass loading at sluice pressures intermediate between atmospheric and reactor pressure, thereby reducing "pump cycle" time and increasing biomass throughput capacity.
    • 提供的方法和装置用于将诸如生物质原料的颗粒物质转移到加压反应器中和从加压反应器中排出。 改进的闸门装置具有L形闸门室,其具有与垂直反应器入口或出口连通的水平加载室和下部部件连通的上部垂直部件。 活塞阀门通过轴向位移将闸门入口和出口密封在闸室的垂直部件上,并穿过垂直的反应器入口或出口。 相对于反应堆卸载的其他方法,这些装置消耗较少的蒸汽并显着减少未加载的预处理生物质的糠醛含量。 使用这些装置的生物质进料的可选的混合塞/水闸方法允许在大气压和反应堆压力之间的闸门压力下生物质负载,从而减少“泵循环”时间并增加生物质通量能力。
    • 2. 发明申请
    • PARTICLE PUMP METHODS AND DEVICES
    • 粒子泵方法和装置
    • WO2011024145A3
    • 2011-05-05
    • PCT/IB2010053864
    • 2010-08-27
    • INBICON ASFINK JENSNIELSEN POULSEN NIELS
    • FINK JENSNIELSEN POULSEN NIELS
    • B01J8/00C10J3/48C10J3/50
    • B01J8/002B01J3/02B01J8/0015B01J8/0035B01J2208/00743B01J2208/00752B01J2208/00761B01J2208/00769B65G53/48C12P2201/00Y02E50/32Y10T137/87917
    • Methods and devices are provided for transfer of particulate material, such as biomass feedstocks, into and out of pressurized reactors. Improved sluice devices have an L- shaped sluice chamber having an upper, vertical component in communication with a horizontal loading chamber and a lower component in communication with a vertical reactor inlet or outlet. Piston valves seal the sluice inlet and outlet by axial displacement across the vertical component of the sluice chamber and across the vertical reactor inlet or outlet. Relative to other methods for reactor unloading, these devices consume less steam and significantly reduce furfural content of unloaded, pretreated biomass. An optional hybrid plug/sluice method of biomass feeding using the devices permits biomass loading at sluice pressures intermediate between atmospheric and reactor pressure, thereby reducing "pump cycle" time and increasing biomass throughput capacity.
    • 提供了用于将粒状材料(例如生物质原料)转移进出加压反应器的方法和装置。 改进的水闸装置具有L形水闸室,其具有与水平加载室连通的上部垂直部件和与垂直反应器入口或出口连通的下部部件。 活塞阀通过轴向移动穿过闸门室的垂直部件并穿过垂直反应器入口或出口来密封闸门入口和出口。 与其他反应堆卸载方法相比,这些设备消耗的蒸汽更少,并显着降低未经处理的预处理生物质的糠醛含量。 使用该装置的生物质进料的可选混合塞/水闸方法允许在大气压和反应器压力之间的闸门压力下的生物质装载,由此减少“泵循环”时间并增加生物量通过能力。
    • 3. 发明申请
    • NON-STERILE FERMENTATION OF BIOETHANOL
    • 生物柴油的非纯化发酵
    • WO2009090480A3
    • 2009-09-03
    • PCT/IB2008003536
    • 2008-12-18
    • INBICON ASLARSEN JAN
    • LARSEN JAN
    • C12P7/06C12P7/10
    • C12P7/06A01N43/08A01N61/00A01N65/00A01N65/44C12N1/22C12P7/10C12P2201/00Y02E50/16Y02E50/17
    • A range of concentrations exists in which fermentation inhibitors derived from pretreatment of lignocellulosic feed stocks inhibit growth of lactic acid bacteria without affecting fermentive yeast. By optimizing levels of fermentation inhibitors to fall within this range, yeast fermentations of lignocellulosic biomass can be conducted under non-sterile conditions with ethanol yields comparable to those achieved under sterile conditions. Optimised inhibitor levels can be achieved by controlling the water/biomass ratio of a lignocellulosic biomass during and after pretreatment, for example by washing the fiber fraction of a previously pretreated lignocellulosic biomass with a pre-defined amount of fresh water or recycled process solutions. Crude extracts of liquid fraction or process solutions from pretreatment of lignocellulosic biomass can also provide an effective anti-baterial treatment for first generation starch fermentations.
    • 存在一定范围的浓度,其中衍生自木质纤维素原料的预处理的发酵抑制剂抑制乳酸菌的生长而不影响发酵酵母。 通过优化发酵抑制剂的含量落在此范围内,木质纤维素生物质的酵母发酵可以在非无菌条件下进行,乙醇产量与在无菌条件下达到的相似。 优化的抑制剂水平可以通过在预处理期间和之后控制木质纤维素生物质的水/生物量比来实现,例如通过用预定量的淡水或再循环的处理溶液洗涤先前预处理的木质纤维素生物质的纤维部分。 来自木质纤维素生物质预处理的液体馏分或处理溶液的粗提取物也可为第一代淀粉发酵提供有效的抗物质处理。
    • 7. 发明申请
    • NON-STERILE FERMENTATION OF BIOETHANOL
    • 生物乙醇的非无菌发酵
    • WO2009090480A4
    • 2009-11-12
    • PCT/IB2008003536
    • 2008-12-18
    • INBICON ASLARSEN JAN
    • LARSEN JAN
    • C12P7/06C12P7/10
    • C12P7/06A01N43/08A01N61/00A01N65/00A01N65/44C12N1/22C12P7/10C12P2201/00Y02E50/16Y02E50/17
    • A range of concentrations exists in which fermentation inhibitors derived from pretreatment of lignocellulosic feed stocks inhibit growth of lactic acid bacteria without affecting fermentive yeast. By optimizing levels of fermentation inhibitors to fall within this range, yeast fermentations of lignocellulosic biomass can be conducted under non-sterile conditions with ethanol yields comparable to those achieved under sterile conditions. Optimised inhibitor levels can be achieved by controlling the water/biomass ratio of a lignocellulosic biomass during and after pretreatment, for example by washing the fiber fraction of a previously pretreated lignocellulosic biomass with a pre-defined amount of fresh water or recycled process solutions. Crude extracts of liquid fraction or process solutions from pretreatment of lignocellulosic biomass can also provide an effective anti-baterial treatment for first generation starch fermentations.
    • 存在一系列浓度,其中源自木质纤维素原料的预处理的发酵抑制剂抑制乳酸菌的生长而不影响发酵性酵母。 通过优化发酵抑制剂的水平以使其落入该范围内,木质纤维素生物质的酵母发酵可以在非无菌条件下进行,其中乙醇产率与无菌条件下获得的乙醇产量相当。 通过在预处理期间和之后控制木质纤维素生物质的水/生物质比率,例如通过用预定量的淡水或回收的工艺溶液洗涤先前预处理的木质纤维素生物质的纤维部分,可以实现优化的抑制剂水平。 来自木质纤维素生物质预处理的液体馏分或工艺溶液的粗提物也可为第一代淀粉发酵提供有效的抗菌处理。