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公开(公告)号:US4762467A
公开(公告)日:1988-08-09
申请号:US944630
申请日:1986-12-19
申请人: Hans Ackermann , Ralf Koecher , Udo Steinberner , Otto Michel
发明人: Hans Ackermann , Ralf Koecher , Udo Steinberner , Otto Michel
CPC分类号: F04F5/52
摘要: In a jet pump, the suction pressure (Po) generated may be kept constant within predetermined limits and times by varying the pressure ratio f(p) providing a prescribed value for the pressure ratio f(p) is determined by computer-aided iterative changing of an existing value of the pressure ratio f(p) using an algorithm and a measured value for the pressure (Pe) of the delivery fluid.
摘要翻译: 在喷射泵中,通过改变提供压力比f(p)的规定值的压力比f(p),通过计算机辅助的迭代变化来确定所产生的吸入压力(Po)保持恒定在预定的极限和时间内 使用算法的压力比f(p)的现有值和输送流体的压力(Pe)的测量值。
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公开(公告)号:US4595461A
公开(公告)日:1986-06-17
申请号:US599089
申请日:1984-04-11
申请人: Lutz Jeromin , Wilhelm Johannisbauer , Klaus Thorausch , Franjo Skrapac , Helmut Hartmann , Karl Hentschel , Otto Michel
发明人: Lutz Jeromin , Wilhelm Johannisbauer , Klaus Thorausch , Franjo Skrapac , Helmut Hartmann , Karl Hentschel , Otto Michel
CPC分类号: C07C51/445 , C07C51/44 , Y10S203/16 , Y10S203/20 , Y10S203/90
摘要: A process for the nondegenerative distillation of C.sub.6 -C.sub.24 -fatty acids, of the type obtained by splitting natural fats and oils or by synthetic processes, such as for example the oxidation of paraffins, the crude product is thermally dried under reduced pressure, the dried and heated crude product is subjected to fractional evaporation in falling-film evaporators, optionally in the presence of superheated steam, and the various vapor fractions are deposited in condensers. The thermal drying process is conducted at a temperature of 60.degree.-80.degree. C. and a pressure of 90-100 mbars. The de-watered crude product is fractionated in a film-forming evaporator and, after distillation, passes to a rectification column which condenses the low boiling constituents as the main runnings.
摘要翻译: 通过分离天然脂肪和油或通过合成方法(例如石蜡氧化)得到的类型的C 6 -C 24脂肪酸的非退化蒸馏方法,粗产物在减压下热干燥,干燥 并且加热的粗产物在降膜蒸发器中任选地在过热蒸汽的存在下进行分级蒸发,并且各种蒸气馏分沉积在冷凝器中。 热干燥过程在60-80℃的温度和90-100mbar的压力下进行。 脱水的粗产物在成膜蒸发器中分馏,并在蒸馏之后进入精馏塔,其将低沸点组分作为主要流路冷凝。
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公开(公告)号:US4655879A
公开(公告)日:1987-04-07
申请号:US664902
申请日:1984-10-26
申请人: Rolf Brockmann , Lutz Jeromin , Wilhelm Johannisbauer , Helmut Meyer , Otto Michel , Juergen Plachenka
发明人: Rolf Brockmann , Lutz Jeromin , Wilhelm Johannisbauer , Helmut Meyer , Otto Michel , Juergen Plachenka
IPC分类号: B01D3/14 , B01D3/32 , C07C27/00 , C07C29/80 , C07C29/88 , C07C31/22 , C07C67/00 , B01D3/34 , B01D1/22
CPC分类号: B01D3/322 , B01D3/148 , C07C29/80 , Y10S203/20
摘要: An improved process for purification of glycerol obtained from natural sources comprising alkalizing a glycerol-containing crude mixture in the presence of air for oxidation, evaporating the mixture in a thin-layer evaporator with redistillation of the residue, rectification and reevaporation in a packed column characterized by low-pressure-loss plates with a falling-film evaporator designed for internal and external partial condensation and to separate off unwanted constituents of the mixture, bleaching the product with activated carbon and separating the bleach in known manner.
摘要翻译: 从天然来源纯化甘油的改进方法,包括在空气存在下使含甘油的粗混合物碱化以进行氧化,在薄层蒸发器中蒸发混合物,重新蒸馏残余物,在填充塔中进行精馏和再蒸发 通过设计用于内部和外部部分冷凝的降膜蒸发器的低压损耗板和分离混合物的不需要的成分,用活性炭漂白产物并以已知的方式分离漂白剂。
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