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    Near-critical fluid extraction process
    1.
    发明授权
    Near-critical fluid extraction process 有权
    近临界流体萃取过程

    公开(公告)号：US08580116B2

    公开(公告)日：2013-11-12

    申请号：US12278554

    申请日：2007-02-01

    申请人： Owen John Catchpole ,  John Bertram Grey ,  Nicola Emma Durling ,  Kameron Gary Dunn

    发明人： Owen John Catchpole ,  John Bertram Grey ,  Nicola Emma Durling ,  Kameron Gary Dunn

    IPC分类号： B01D11/04 ,  B01D17/00

    CPC分类号： B01D11/0203 ,  A23L33/105 ,  B01D11/0292 ,  B01D11/0403 ,  B01D11/0407 ,  B01D11/0411 ,  B01D11/0492

    摘要： A process for fractionating the constituents of a solution obtained by extracting plant or animal material with an aqueous-organic solvent where the aqueous-organic solvent is a mixture of water and a water-miscible organic solvent, generally including the steps of contacting the solution with a near-critical fluid to produce a raffinate phase containing high polarity constituents and water, and a near-critical fluid phase containing low to medium polarity constituents, separating the near-critical fluid phase from the raffinate phase, and recovering the low to medium polarity constituents from the near-critical fluid phase and the high polarity constituents from the raffinate phase.

    摘要翻译： 一种通过水溶性有机溶剂萃取植物或动物材料获得的溶液的成分分馏方法，其中水 - 有机溶剂是水和水混溶性有机溶剂的混合物，通常包括以下步骤：使溶液与 一种近临界流体，以产生含有高极性成分和水的萃余相，以及含有低至中等极性成分的近临界流体相，将近临界流体相与萃余相分离，并回收低至中等极性 来自近临界流体相的组分和来自萃余相的高极性成分。

    NEAR-CRITICAL FLUID EXTRACTION PROCESS
    2.
    发明申请
    NEAR-CRITICAL FLUID EXTRACTION PROCESS 有权
    近临界流体萃取过程

    公开(公告)号：US20100151098A1

    公开(公告)日：2010-06-17

    申请号：US12278554

    申请日：2007-02-01

    申请人： Owen John Catchpole ,  John Bertram Grey ,  Nicola Emma Durling

    发明人： Owen John Catchpole ,  John Bertram Grey ,  Nicola Emma Durling

    IPC分类号： A23L1/28 ,  B01D11/00

    CPC分类号： B01D11/0203 ,  A23L33/105 ,  B01D11/0292 ,  B01D11/0403 ,  B01D11/0407 ,  B01D11/0411 ,  B01D11/0492

    摘要： A process for fractionating the constituents of a solution obtained by extracting plant or animal material with an aqueous-organic solvent where the aqueous-organic solvent is a mixture of water and a water-miscible organic solvent, generally including the steps of contacting the solution with a near-critical fluid to produce a raffinate phase containing high polarity constituents and water, and a near-critical fluid phase containing low to medium polarity constituents, separating the near-critical fluid phase from the raffinate phase, and recovering the low to medium polarity constituents from the near-critical fluid phase and the high polarity constituents from the raffinate phase.

    摘要翻译： 一种通过水溶性有机溶剂萃取植物或动物材料获得的溶液的成分分馏方法，其中水 - 有机溶剂是水和水混溶性有机溶剂的混合物，通常包括以下步骤：使溶液与 一种近临界流体，以产生含有高极性成分和水的萃余相，以及含有低至中等极性成分的近临界流体相，将近临界流体相与萃余相分离，并回收低至中等极性 来自近临界流体相的组分和来自萃余相的高极性成分。

    Separation technology
    3.
    发明授权
    Separation technology 失效
    分离技术

    公开(公告)号：US07709668B2

    公开(公告)日：2010-05-04

    申请号：US10512221

    申请日：2003-04-11

    申请人： Owen John Catchpole ,  Andrew Douglas Mackenzie ,  John Bertram Grey

    发明人： Owen John Catchpole ,  Andrew Douglas Mackenzie ,  John Bertram Grey

    IPC分类号： C07C51/47

    CPC分类号： C11C3/10 ,  C07C51/48 ,  C07C67/58 ,  C11B7/005 ,  C11C1/025 ,  C11C1/08 ,  C07C57/12 ,  C07C57/03 ,  C07C69/587

    摘要： A process for extracting a wide range of lipophilic compounds from urea-containing solutions is described. The process utilises a near-critical fluid as the extraction solvent. The process is particularly applicable to the extraction of polyunsaturated fatty acids from the filtrate obtained upon urea fractionation, as employed in the processing of fish and other oils. In contrast to known processes, the lipophilic compounds may be extracted without the use of non-food grade solvents, and are suitable for pharmaceutical and cosmetic use.

    摘要翻译： 描述了从含尿素溶液中提取大范围的亲油性化合物的方法。 该方法利用近临界流体作为萃取溶剂。 该方法特别适用于从尿素分馏得到的滤液中提取多不饱和脂肪酸，如用于鱼类和其他油类的加工。 与已知的方法相反，亲油性化合物可以在不使用非食品级溶剂的情况下提取，并且适用于药物和化妆品用途。