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公开(公告)号:EP0392018B1
公开(公告)日:1995-09-06
申请号:EP89906454.7
申请日:1989-06-05
IPC分类号: C11B11/00
CPC分类号: C11B11/005
摘要: The invention provides a process for purifying raw lanolins containing agricultural chemicals by removing the residual agricultural chemicals therefrom, which comprises subjecting the raw lanolins to at least one of the step (1) of hydrogenation in a molten state or in an organic solvent in the presence of a hydrogenation catalyst at a temperature of 60 to 210°C under a hydrogen pressure of 1 atm or more with a hydrogen consumption of 0.001 to 0.05 wt. % based on the raw lanolin, the step (2) of distillation in vacuo at a temperature of 150 to 280°C under an absolute pressure of 10 to 500 x 10-3 mmHg, and the step (3) of adsorption on a resin selected from among those containing styrene-divinylbenzene as a skeleton, those containing acrylic ester as a skeleton and polystyrene resins and having a micropore size of about 10 to 250 Å or on a crystalline aluminosilicate having an internal diameter of about 9 to 13 Å.
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公开(公告)号:EP0392018A1
公开(公告)日:1990-10-17
申请号:EP89906454.7
申请日:1989-06-05
IPC分类号: C11B11/00
CPC分类号: C11B11/005
摘要: The invention provides a process for purifying raw lanolins containing agricultural chemicals by removing the residual agricultural chemicals therefrom, which comprises subjecting the raw lanolins to at least one of the step (1) of hydrogenation in a molten state or in an organic solvent in the presence of a hydrogenation catalyst at a temperature of 60 to 210° C under a hydrogen pressure of 1 atm or more with a hydrogen consumption of 0.001 to 0.05 wt. % based on the raw lanolin, the step (2) of distillation in vacuo at a temperature of 150 to 280 C under an absolute pressure of 10 to 500 x 10 -3 mmHg, and the step (3) of adsorption on a resin selected from among those containing styrene-divinylbenzene as a skeleton, those containing acrylic ester as a skeleton and polystyrene resins and having a micropore size of about 10 to 250 Å or on a crystalline aluminosilicate having an internal diameter of about 9 to 13 A.
摘要翻译: 一种净化羊毛脂的方法,其包括以下方法中的至少一种:1)在有机溶剂中或在60-210℃的熔融条件下,在氢气氛(1大气压或1小时)中热处理羊毛脂(A) 更高)和在氢化催化剂存在下。 H2的消耗量为羊毛脂(A)的0.001〜0.05重量%。 (A)包含至少一种农业化学品HCB,αbetamamma-BHC,γ-BHC,ALD + OLD,DDE + DDT,END,DZN,BPE,DCP和alphabeta-CVP。 2)在150-280℃下(A)的真空蒸馏(10-500×10 -MHgHg)。 3)在树脂(B)或结晶铝硅酸盐(C)上吸收(A)。 (B)是苯乙烯 - 二乙烯基苯树脂,丙烯酸酯树脂或聚苯乙烯树脂,并且具有10-250埃的细孔尺寸(C)的内径为9-13埃。
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