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公开(公告)号:US5264367A
公开(公告)日:1993-11-23
申请号:US882710
申请日:1992-05-14
申请人: Erik Aalrust , Wolfgang Beyer , Hans Ottofrickenstein , Georg Penk , Hermann Plainer , Roland Reiner
发明人: Erik Aalrust , Wolfgang Beyer , Hans Ottofrickenstein , Georg Penk , Hermann Plainer , Roland Reiner
CPC分类号: C11B3/003
摘要: The content of phosphorus-containing components and the iron content of an edible vegetable or animal oil, preferably an oil such as soybean oil which has been wet-refined to remove mucilage, are reduced by enzymatic decomposition by contacting the oil with an aqueous solution of phospholipases A.sub.1, A.sub.2, or B and then separating the aqueous phase from the treated oil.
摘要翻译: 含磷成分的含量和可食用植物油或动物油(优选已经湿精制以除去粘液的大豆油)的油的铁含量通过酶促分解而降低,通过使油与水 磷脂酶A1,A2或B,然后将水相与经处理的油分离。
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2.
公开(公告)号:US4741807A
公开(公告)日:1988-05-03
申请号:US907542
申请日:1986-09-15
申请人: Joachim Wilhelm , Rainer Reimert , Georg Penk
发明人: Joachim Wilhelm , Rainer Reimert , Georg Penk
CPC分类号: B01D11/0203
摘要: In a reactor, granular feedstock having particle sizes in the range from about 0.5 to 15 mm is subjected in a moving bed to a countercurrent extraction at a temperature in the range from 20.degree. to 150.degree. C. and under a pressure in the range from 50 to 400 bars by a continuously supplied solvent which is in a liquid or supercritical state. A mixture of valuable substances and solvent is withdrawn from the upper portion of the reactor. The solvent is separated from the valuable substances by a pressure relief and/or temperature rise and is recycled to the reactor. The extraction residue is withdrawn from the lower end of the reactor. Respective locks are used to charge the feedstock into the reactor and to discharge the extraction residue from the reactor. Solvent and an entrainer are supplied to the reactor at different locations. Outlet ducts having a length of 0.1 to 1 m are preferably used to deliver the feedstock onto a moving bed in the reactor so that a free space is provided over the bed.
摘要翻译: 在反应器中,将粒度在约0.5至15mm范围内的粒状原料在移动床中进行逆流萃取,温度范围为20-150℃,压力范围为 通过处于液体或超临界状态的连续供应的溶剂,50至400巴。 有价值物质和溶剂的混合物从反应器的上部排出。 通过减压和/或升温将溶剂与有价值物质分离,并再循环到反应器中。 萃取残余物从反应器的下端排出。 使用各种锁将原料装入反应器并从反应器排出萃取渣。 溶剂和夹带剂在不同的位置供应到反应器。 优选使用长度为0.1至1μm的出口管道将原料输送到反应器中的移动床上,使得在床上设置自由空间。
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