知搜-全球专利检索

  1. 登录
  2. 注册

搜索结果

314 条记录 (耗时 0.031 秒)

    Method Of Fuse Oil Decanting In An Ethanol Plant
    41.
    发明申请
    Method Of Fuse Oil Decanting In An Ethanol Plant 审中-公开
    保险丝滗析在乙醇厂的方法

    公开(公告)号：US20100004491A1

    公开(公告)日：2010-01-07

    申请号：US12494689

    申请日：2009-06-30

    申请人： D. Christopher Romer

    发明人： D. Christopher Romer

    IPC分类号： C07C29/74 ,  B01D3/32

    CPC分类号： C07C29/76 ,  B01D3/002 ,  C10L1/328 ,  C07C31/08

    摘要： An apparatus including an ethanol stream, wherein said ethanol stream contains greater than 5% of water; a dehydration means, wherein the water content of said ethanol stream is reduced to less than 5%; a desiccation means, wherein the water content of said ethanol stream is reduced to less than about 1%; a 200 proof receiver, wherein said 200 proof receiver comprises a sample port or a sensor to allow the percentage of water in the ethanol to be determined, and wherein said 200 proof receiver comprises an outlet; a heat exchanger to heat said ethanol stream with less than 1% water, and a mixing manifold downstream of said heat exchanger, wherein said heated ethanol stream with less than 1% water is combined with fusal oils from a fusal oil decanter is provided.

    摘要翻译： 一种包括乙醇流的装置，其中所述乙醇流含有大于5％的水; 脱水装置，其中所述乙醇流的水含量降低至小于5％; 干燥装置，其中所述乙醇流的水含量降低至小于约1％; 200检验接收器，其中所述200检验接收器包括样本端口或传感器，以允许确定乙醇中的水的百分比，并且其中所述200检验接收器包括出口; 提供了一种用于以小于1％的水加热所述乙醇流的热交换器，以及在所述热交换器下游的混合歧管，其中具有小于1％的水的所述加热的乙醇流与来自一种除油器的脱脂油组合。

    Rectification apparatus using a heat pump
    42.
    发明申请
    Rectification apparatus using a heat pump 失效
    使用热泵的整流装置

    公开(公告)号：US20090308100A1

    公开(公告)日：2009-12-17

    申请号：US11919400

    申请日：2006-04-28

    申请人： Erik Jensen

    发明人： Erik Jensen

    IPC分类号： F25J3/02

    CPC分类号： B01D3/002 ,  B01D1/16 ,  B01D1/28 ,  B01D3/007 ,  B01D5/0015 ,  Y02B30/52

    摘要： An apparatus for stripping and strengthening and subsequent condensing and final strengthening of an easily vaporizable component of a preferably aqueous mixture permits the heat necessary for stripping and strengthening to be transferred through a common heat transmission body (3), where the heat is derived from condensing the vapour generated by stripping and strengthening, which vapour via compression using a heat pump (26) has obtained the increase in boiling point necessary for condensation. The apparatus is comprised of two sections, namely a stripping and strengthening section or first section (1) and a condensing and final strengthening section or second section (2), said sections being joined around a common heat transmission body (3) forming a dividing wall, each section being further defined by a horizontal partially cylindrical housing (13) and an end wall at each end. Each of the sections is provided with an atomizing rotor (4) adapted to throw liquid from each side from the bottom of the horizontal partially cylindrical housing (13) inward against the common heat transmission body, an axial liquid channel (5) providing a continuous passage of liquid through the apparatus extending along the bottom.

    摘要翻译： 用于汽提和强化以及随后的优选含水混合物易挥发的组分的冷凝和最终强化的装置允许汽提和强化所需的热量通过共同的热传递体（3）传递，其中热源自冷凝 通过汽提和强化产生的蒸汽，通过使用热泵（26）压缩的蒸汽获得了冷凝所需的沸点的增加。 该设备包括两个部分，即剥离和加固部分或第一部分（1）和冷凝和最终加强部分或第二部分（2），所述部分围绕公共传热体（3）连接，形成分隔 每个部分由水平部分圆柱形的壳体（13）和每个端部的端壁进一步限定。 每个部分设置有雾化转子（4），其适于将液体从水平部分圆柱形壳体（13）的底部向内抵靠公共传热体向内引导;轴向液体通道（5），其提供连续 液体通过沿底部延伸的装置。

    ETHANOL PLANT RETROFIT WITH VAPOUR SEPARATION MEMBRANES
    43.
    发明申请
    ETHANOL PLANT RETROFIT WITH VAPOUR SEPARATION MEMBRANES 审中-公开
    乙醇植物与蒸气分离膜改造

    公开(公告)号：US20090301970A1

    公开(公告)日：2009-12-10

    申请号：US12481178

    申请日：2009-06-09

    申请人： Gaetan Noel

    发明人： Gaetan Noel

    IPC分类号： C02F1/04

    CPC分类号： B01D3/002 ,  B01D3/145

    摘要： A system and process removes water from an aqueous fermentation product, for example ethanol, using distillation upstream of a first membrane separation unit to produce hydrous alcohol. Optionally, molecular sieves may be used to further dewater the hydrous alcohol. Another system or process removes water from hydrous ethanol using molecular sieves with a second membrane separation unit to process a regeneration stream. Optionally, there may be a distillation column in the regeneration stream upstream of the membrane separation unit. Further optionally, additional hydrous ethanol may be process through the distillation column or second membrane separation unit, by-passing the molecular sieve unit. These systems and processes may be combined and may be used, individually or together, to retrofit an existing ethanol plant.

    摘要翻译： 系统和方法使用第一膜分离单元上游的蒸馏产生含水醇从水性发酵产物例如乙醇中除去水。 任选地，分子筛可用于进一步脱水含水醇。 另一种系统或方法使用具有第二膜分离单元的分子筛从含水乙醇中除去水以处理再生流。 任选地，在膜分离单元上游的再生流中可以存在蒸馏塔。 另外任选地，另外的含水乙醇可以通过蒸馏塔或第二膜分离单元进行处理，旁通分子筛单元。 这些系统和方法可以组合并且可以单独地或一起用于改造现有的乙醇装置。

    PROCESS FOR PRODUCING ETHANOL FROM CORN DRY MILLING
    45.
    发明申请
    PROCESS FOR PRODUCING ETHANOL FROM CORN DRY MILLING 有权
    从玉米干燥生产乙醇的方法

    公开(公告)号：US20090081749A1

    公开(公告)日：2009-03-26

    申请号：US12324015

    申请日：2008-11-26

    申请人： Dan W. Verser ,  Timothy J. Eggeman

    发明人： Dan W. Verser ,  Timothy J. Eggeman

    IPC分类号： C12P7/10

    CPC分类号： C12P7/06 ,  B01D3/002 ,  C07C29/149 ,  C12P7/14 ,  C12P7/54 ,  C12P7/62 ,  Y02E50/16 ,  Y02E50/17 ,  Y02P20/127 ,  C07C31/08

    摘要： A process for producing ethanol by the conversion of carbohydrates from a corn dry milling process in which the bottoms fraction from distillation of ethanol in a conventional yeast fermentation is used in a process including a combination of biochemical and synthetic conversions. The process results in high yield ethanol production with concurrent production of high value coproducts. An acetic acid intermediate is produced from bottoms fraction, followed by conversion of the acetic acid into ethanol using esterification and hydrogenation reactions. Coproducts of the process include a high protein content solids fraction produced in the fermentation.

    摘要翻译： 通过转化来自玉米干磨法的碳水化合物生产乙醇的方法，其中在常规酵母发酵中从蒸馏乙醇的塔底馏分用于包括生化和合成转化的组合的方法中。 该方法产生高产乙醇生产，同时生产高价值的副产物。 由塔底馏分产生乙酸中间体，然后使用酯化和氢化反应将乙酸转化成乙醇。 该方法的副产物包括在发酵中产生的高蛋白质含量的固体含量。

    COMPOSITIONS AND METHODS FOR THE BIOSYNTHESIS OF 1,4-BUTANEDIOL AND ITS PRECURSORS
    46.
    发明申请
    COMPOSITIONS AND METHODS FOR THE BIOSYNTHESIS OF 1,4-BUTANEDIOL AND ITS PRECURSORS 有权

    公开(公告)号：US20090075351A1

    公开(公告)日：2009-03-19

    申请号：US12049256

    申请日：2008-03-14

    申请人： Mark J. Burk ,  Stephen J. Van Dien ,  Anthony P. Burgard ,  Wei Niu

    发明人： Mark J. Burk ,  Stephen J. Van Dien ,  Anthony P. Burgard ,  Wei Niu

    IPC分类号： C12N1/21 ,  C12P7/52 ,  C12P7/18

    CPC分类号： C12N15/52 ,  B01D3/002 ,  C12N9/0006 ,  C12N9/0008 ,  C12N9/88 ,  C12N9/93 ,  C12N15/70 ,  C12N15/81 ,  C12P7/18 ,  C12P7/42 ,  C12P7/52 ,  C12P17/04 ,  C12Y101/01061 ,  C12Y102/01076 ,  C12Y401/01071 ,  C12Y602/01004 ,  Y02P20/52

    摘要： The invention provides a non-naturally occurring microbial biocatalyst including a microbial organism having a 4-hydroxybutanoic acid (4-HB) biosynthetic pathway having at least one exogenous nucleic acid encoding 4-hydroxybutanoate dehydrogenase, succinyl-CoA synthetase, CoA-dependent succinic semialdehyde dehydrogenase, or α-ketoglutarate decarboxylase, wherein the exogenous nucleic acid is expressed in sufficient amounts to produce monomeric 4-hydroxybutanoic acid (4-HB). Also provided is a non-naturally occurring microbial biocatalyst including a microbial organism having 4-hydroxybutanoic acid (4-HB) and 1,4-butanediol (BDO) biosynthetic pathways, the pathways include at least one exogenous nucleic acid encoding 4-hydroxybutanoate dehydrogenase, succinyl-CoA synthetase, CoA-dependent succinic semialdehyde dehydrogenase, 4-hydroxybutyrate:CoA transferase, 4-butyrate kinase, phosphotransbutyrylase, α-ketoglutarate decarboxylase, aldehyde dehydrogenase, alcohol dehydrogenase or an aldehyde/alcohol dehydrogenase, wherein the exogenous nucleic acid is expressed in sufficient amounts to produce 1,4-butanediol (BDO). Additionally provided is a method for the production of 4-HB. The method includes culturing a non-naturally occurring microbial organism having a 4-hydroxybutanoic acid (4-HB) biosynthetic pathway including at least one exogenous nucleic acid encoding 4-hydroxybutanoate dehydrogenase, succinyl-CoA synthetase, CoA-dependent succinic semialdehyde dehydrogenase or α-ketoglutarate decarboxylase under substantially anaerobic conditions for a sufficient period of time to produce monomeric 4-hydroxybutanoic acid (4-HB). Further provided is a method for the production of BDO. The method includes culturing a non-naturally occurring microbial biocatalyst, comprising a microbial organism having 4-hydroxybutanoic acid (4-HB) and 1,4-butanediol (BDO) biosynthetic pathways, the pathways including at least one exogenous nucleic acid encoding 4-hydroxybutanoate dehydrogenase, succinyl-CoA synthetase, CoA-dependent succinic semialdehyde dehydrogenase, 4-hydroxybutyrate:CoA transferase, 4-hydroxybutyrate kinase, phosphotranshydroxybutyrylase, α-ketoglutarate decarboxylase, aldehyde dehydrogenase, alcohol dehydrogenase or an aldehyde/alcohol dehydrogenase for a sufficient period of time to produce 1,4-butanediol (BDO). The 4-HB and/or BDO products can be secreted into the culture medium.

    ETHANOL PROCESSING WITH VAPOUR SEPARATION MEMBRANES
    48.
    发明申请
    ETHANOL PROCESSING WITH VAPOUR SEPARATION MEMBRANES 失效
    用蒸汽分离膜进行乙醇加工

    公开(公告)号：US20080207959A1

    公开(公告)日：2008-08-28

    申请号：US12038284

    申请日：2008-02-27

    申请人： Pierre Plante ,  Bruno de Caumia ,  Christian Roy ,  Gaetan Noel

    发明人： Pierre Plante ,  Bruno de Caumia ,  Christian Roy ,  Gaetan Noel

    IPC分类号： C07C29/88

    CPC分类号： C07C29/76 ,  B01D3/002 ,  B01D3/14 ,  B01D3/145 ,  Y10S203/08 ,  C07C31/08

    摘要： A process for separating vapours, for example for separating water from ethanol, uses a gas separation membrane unit. Permeate from the membrane unit is compressed and may be used for example as heating steam for distillation. The membrane unit may have two or more stages. Permeate from a stage may be condensed and used for example as fermentation make up water, compressed and fed to the permeate from an upstream stage or heating steam, or fed to another membrane stage for further dewatering. The gas separation membrane unit may be used to remove water from a fermentation broth that has been partially dewatered, for example by one or more of a distillation column or molecular sieve.

    摘要翻译： 用于分离蒸气的方法，例如用于将水与乙醇分离的方法使用气体分离膜单元。 来自膜单元的渗透物被压缩，并且可以用作例如用于蒸馏的加热蒸汽。 膜单元可以具有两个或更多个阶段。 来自阶段的渗透物可以被浓缩并用于例如发酵组合水，压缩并从上游阶段或加热蒸汽进料到渗透物中，或者进料到另一个膜级进一步脱水。 气体分离膜单元可以用于从已经部分脱水的发酵液中除去水，例如通过一个或多个蒸馏塔或分子筛。

    Ethanol distillation with distillers soluble solids recovery apparatus
    49.
    发明申请
    Ethanol distillation with distillers soluble solids recovery apparatus 有权
    乙醇蒸馏用酒糟可溶性固体回收装置

    公开(公告)号：US20070000769A1

    公开(公告)日：2007-01-04

    申请号：US10546846

    申请日：2004-03-29

    申请人： Christopher Brown

    发明人： Christopher Brown

    IPC分类号： B01D3/00

    CPC分类号： B01D3/002 ,  B01D3/005 ,  B01D3/146 ,  B01D3/148 ,  B01D3/322 ,  B03D1/02 ,  B03D1/1431 ,  Y02E50/17 ,  Y10S203/08

    摘要： The present invention relates to a system for producing ethanol from an organic source and that operates to purify and dry ethanol from a beer source. The system for producing substantially anhydrous ethanol comprises: (a) a first distillation stripping column that operates between 160 to 220 degrees F.; (b) a second distillation rectifying column having a higher operating temperature than said stripping column; (c) a molecular sieve dehydration means in fluid communication with said rectifying column; and (d) an energy control means.

    摘要翻译： 本发明涉及一种用于从有机源生产乙醇并用于从啤酒来源净化和干燥乙醇的系统。 用于生产基本上无水乙醇的系统包括：（a）在160至220华氏度之间运行的第一蒸馏汽提塔; （b）具有比所述汽提塔更高的操作温度的第二蒸馏精馏塔; （c）与所述精馏塔流体连通的分子筛脱水装置; 和（d）能量控制装置。