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    • 2. 发明授权
    • Deacidification method
    • 脱酸方法
    • US08598376B2
    • 2013-12-03
    • US12306488
    • 2007-06-28
    • Andrew Timothy BoamFui Wen Lim
    • Andrew Timothy BoamFui Wen Lim
    • C11B5/00
    • C11B3/008B01D61/022B01D61/027B01D65/02B01D67/0088B01D71/26B01D71/44B01D71/60B01D71/64B01D71/70B01D2321/04B01D2325/027C11B3/006C11B7/0025
    • There is provided a process for reducing the free fatty acid content of natural oils by contacting the crude natural oil with a solvent to produce an oil product phase substantially depleted in free fatty acids and a free fatty acid rich solvent phase containing the extracted free fatty acids and some of the glycerides, and processing the free fatty acid rich solvent phase with a membrane to recover the glycerides from the solvent phase, comprising the steps of: (a) contacting the crude natural oil with an immiscible solvent; (b) separating the deacidifed natural oil phase from the solvent phase; (c) providing a selectively permeable membrane having a first surface and a second surface; (d) transferring a portion of the solvent and a portion of the free fatty acids and a lesser portion of the glycerides from the first surface to the second surface across the membrane by contacting the free fatty acid rich solvent phase with the first surface, wherein the pressure at the first surface is greater than the pressure at the second surface, and wherein the membrane is a selectively permeable membrane such that the membrane rejections of the free fatty acids (RFFA) and glycerides (RGLY) are greater than 0%, and the membrane rejection (RGLY) of the glycerides is at least 5% greater than the membrane rejection (RFFA) of the free fatty acids.
    • 提供了一种通过使粗天然油与溶剂接触来降低天然油的游离脂肪酸含量以产生基本上消耗游离脂肪酸的油产物相和含有提取的游离脂肪酸的游离富脂肪酸溶剂相的方法 和一些甘油酯,并用膜处理游离脂肪酸富溶剂相以从溶剂相回收甘油酯,包括以下步骤:(a)使粗天然油与不混溶的溶剂接触; (b)将脱酸天然油相与溶剂相分离; (c)提供具有第一表面和第二表面的选择性渗透膜; (d)通过使游离富含脂肪酸的溶剂相与第一表面接触,将一部分溶剂和一部分游离脂肪酸和一部分甘油酯从第一表面转移到第二表面,其中 第一表面处的压力大于第二表面处的压力,并且其中膜是选择性渗透膜,使得游离脂肪酸(RFFA)和甘油酯(RGLY)的膜排斥大于0%,以及 甘油酯的膜排斥(RGLY)比游离脂肪酸的膜排斥(RFFA)高至少5%。
    • 3. 发明申请
    • MEMBRANE MODULE
    • 膜模块
    • US20110168627A1
    • 2011-07-14
    • US13121006
    • 2009-09-24
    • Fui Wen LimAndrew Guy LivingstoneAndrew Timothy Boam
    • Fui Wen LimAndrew Guy LivingstoneAndrew Timothy Boam
    • B01D63/00B32B37/12
    • B01D67/009B01D61/027B01D63/10B01D71/64B01D2313/04
    • The present invention relates to a method for curing adhesives used in the manufacture of membrane modules containing polymeric membranes, particularly polyimide based membranes used for the nanofiltration or ultrafiltration of solutes dissolved in organic solvents using microwaves. To maximise the chemical resistance of the adhesive used in these organic solvent applications, it must be as fully reacted and crosslinked (“cured”) as possible. Typically, thermal processing (heating) of the entire membrane module is used to cure the adhesives. However, the time and temperature required to achieve this high degree of completion of reaction may damage the separation performance of the membrane contained within the membrane module. In one particular aspect, this process utilises microwaves to preferentially promote the curing of epoxy adhesives over the general heating of the membrane module.
    • 本发明涉及用于制造包含聚合物膜的膜组件的粘合剂的方法,特别是用于使用微波溶解在有机溶剂中的溶质的纳滤或超滤的聚酰亚胺基膜。 为了最大化在这些有机溶剂应用中使用的粘合剂的耐化学性,它必须尽可能完全反应和交联(“固化”)。 通常,使用整个膜组件的热处理(加热)来固化粘合剂。 然而,达到这种高度完成反应所需的时间和温度可能会损害膜组件中包含的膜的分离性能。 在一个特定方面,该方法利用微波来优先促进环氧树脂粘合剂的固化比膜组件的一般加热。
    • 4. 发明申请
    • Deacidification Method
    • 脱酸方法
    • US20100130761A1
    • 2010-05-27
    • US12306488
    • 2007-06-28
    • Andrew Timothy BoamFui Wen Lim
    • Andrew Timothy BoamFui Wen Lim
    • C11B1/10C07C53/126
    • C11B3/008B01D61/022B01D61/027B01D65/02B01D67/0088B01D71/26B01D71/44B01D71/60B01D71/64B01D71/70B01D2321/04B01D2325/027C11B3/006C11B7/0025
    • There is provided a process for reducing the free fatty acid content of natural oils by contacting the crude natural oil with a solvent to produce an oil product phase substantially depleted in free fatty acids and a free fatty acid rich solvent phase containing the extracted free fatty acids and some of the glycerides, and processing the free fatty acid rich solvent phase with a membrane to recover the glycerides from the solvent phase, comprising the steps of: (a) contacting the crude natural oil with an immiscible solvent; (b) separating the deacidifed natural oil phase from the solvent phase; (c) providing a selectively permeable membrane having a first surface and a second surface; (d) transferring a portion of the solvent and a portion of the free fatty acids and a lesser portion of the glycerides from the first surface to the second surface across the membrane by contacting the free fatty acid rich solvent phase with the first surface, wherein the pressure at the first surface is greater than the pressure at the second surface, and wherein the membrane is a selectively permeable membrane such that the membrane rejections of the free fatty acids (RFFA) and glycerides (RGLY) are greater than 0%, and the membrane rejection (RGLY) of the glycerides is at least 5% greater than the membrane rejection (RFFA) of the free fatty acids.
    • 提供了一种通过使粗天然油与溶剂接触来降低天然油的游离脂肪酸含量以产生基本上消耗游离脂肪酸的油产物相和含有提取的游离脂肪酸的游离富脂肪酸溶剂相的方法 和一些甘油酯,并用膜处理游离脂肪酸富溶剂相以从溶剂相回收甘油酯,包括以下步骤:(a)使粗天然油与不混溶的溶剂接触; (b)将脱酸天然油相与溶剂相分离; (c)提供具有第一表面和第二表面的选择性渗透膜; (d)通过使游离富含脂肪酸的溶剂相与第一表面接触,将一部分溶剂和一部分游离脂肪酸和一部分甘油酯从第一表面转移到第二表面,其中 第一表面处的压力大于第二表面处的压力,并且其中膜是选择性渗透膜,使得游离脂肪酸(RFFA)和甘油酯(RGLY)的膜排斥大于0%,以及 甘油酯的膜排斥(RGLY)比游离脂肪酸的膜排斥(RFFA)高至少5%。