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    • 3. 发明授权
    • Vapor drier
    • 蒸气干燥器
    • US5249371A
    • 1993-10-05
    • US779026
    • 1991-10-18
    • Yoshio SaitoMasaru UmedaKohei NinomiyaMasao Kikuchi
    • Yoshio SaitoMasaru UmedaKohei NinomiyaMasao Kikuchi
    • H01L21/304F26B21/14F26B21/06
    • F26B21/145
    • A purpose of this invention is to provide a vapor drier which can continue a process to dry efficiently objects in an extremely clean condition for a long time. A vapor drier of this invention comprises a circulating/dehydrating/refining means for refining said volatile processing liquid stored in said processing room and circulating refined fluid into said processing room, said circulating/dehydrating/refining means having at least an evaporating section to evaporate said volatile processing liquid stored in said processing room, a dehydrating section to remove water from said vapor generated in said evaporating section with a dehydrating/separating membrane, and a distilling section to distill said dehydrated vapor.
    • 本发明的目的是提供一种蒸汽干燥器,其可以持续长时间在极其干燥的条件下有效地干燥物体的方法。 本发明的蒸汽干燥机包括循环/脱水/精制装置,用于将存储在所述处理室中的所述挥发性处理液进行精炼并将精制流体循环到所述处理室中,所述循环/脱水/精制装置至少具有蒸发部分以蒸发所述 存储在所述处理室中的挥发性处理液,脱水部,用脱水分离膜从所述蒸发部中产生的蒸气中除去水,蒸馏部,蒸馏所述脱水蒸气。
    • 5. 发明授权
    • Process for recovering a lower alcohol from a catechol-lower alcohol
reaction product solution
    • 从高级酒精反应产物溶液中回收低级酒精的方法
    • US5105029A
    • 1992-04-14
    • US724934
    • 1991-07-02
    • Kohei NinomiyaKanji NakagawaYoichi Nishida
    • Kohei NinomiyaKanji NakagawaYoichi Nishida
    • B01D53/22B01D3/00B01D61/36C07C29/76C07C31/02C07C37/74C07C39/08C07C43/23C07C69/78
    • C07C29/76
    • A lower alcohol, for example, ethyl alcohol, is recovered from a reaction mixture resulted from a reaction of catechol with a lower alcohol in such a manner that the reaction mixture is distilled and separated into a distilled light vapor fraction comprising non-reacted lower alcohol and water and a residual fraction comprising a reaction product and non-reacted catechol; the distilled light vapor fraction is further distilled and separated into a distilled vapor fraction comprising the lower alcohol in an increased concentration and a residual water fraction; the distilled vapor fraction is fed to a gas-separating membrane module which allows water vapor to selectively permeate therethrough, and separated into a non-permeated fraction which comprises the lower alcohol in a high concentration, which is left in the feed side of the membrane, and a permeated fraction which comprises water in a high concentration, which is returned from the delivery side of the membrane to the further distilling step, and the non-permeated fraction is cooled and recovered.
    • 从由邻苯二酚与低级醇的反应得到的反应混合物中回收低级醇,例如乙醇,使得将反应混合物蒸馏并分离成包含未反应的低级醇的蒸馏轻蒸气馏分 和水和包含反应产物和未反应的儿茶酚的残余馏分; 进一步蒸馏蒸馏光蒸气馏分并分离成包含增加浓度的低级醇和残留水分的蒸馏蒸气馏分; 将蒸馏的蒸气馏分进料到允许水蒸气选择性渗透通过的气体分离膜组件,并分离成非渗透级分,其包含高浓度的低级醇,其留在膜的进料侧 ,以及包含高浓度的水的渗透部分,其从膜的输送侧返回到进一步的蒸馏步骤,并且将非渗透馏分冷却并回收。
    • 6. 发明授权
    • Process and apparatus for separation of volatile components
    • 用于分离挥发性组分的方法和装置
    • US4911845A
    • 1990-03-27
    • US51364
    • 1987-05-19
    • Koichi HashimotoKohei Ninomiya
    • Koichi HashimotoKohei Ninomiya
    • B01D1/28B01D5/00B01D53/22B01D53/26B01D61/36C07C29/76C07C209/86C07C211/46
    • C07C209/86B01D1/28B01D5/006B01D53/22B01D53/228B01D53/268B01D61/36C07C29/76
    • A process for the mutual separation of volatile components in a mixture comprising at least two volatile components, comprising the steps of: (1) heating a starting liquid comprising at least two volatile components to vaporize the starting liquid and form a vapor mixture comprising the volatile component, (2) compressing the vapor mixture to cause a rise in the temperature and pressure thereof, (3) applying the compressed vapor mixture to a membrane having a selective permeability to separate the vapor mixture into a membrane-permeated fraction and a non membrane-permeated fraction, (4) indirectly placing at least one of the fractions in contact with the starting liquid of step (1) via a heat transferring wall to use the heat of the contacted fraction to vaporize the starting liquid, and (5) recovering one or both of the membrane-permeated fraction and non membrane-permeated fraction; and an apparatus for a mutual separation of volatile components in a mixture comprising at least two volatile components, comprising: (1) an evaporator having at least one heat exchanger into which at least one fraction separated by a membrane separator of (3) is introduced, a starting liquid feeding side, an evaporation residue discharging side, and an optional auxiliary heater; to generate a vapor mixture, (2) a compressor to compress the vapor mixture, and (3) a membrane separator comprising a member having a selective permeability to separate the compressed vapor mixture into a membrane-permeated faction and a non membrane-permeated fraction.
    • 一种用于在包含至少两种挥发性组分的混合物中相互分离挥发性组分的方法,包括以下步骤:(1)加热包含至少两种挥发性组分的起始液体以蒸发起始液体并形成包含挥发性组分的蒸气混合物 (2)压缩蒸气混合物以使其温度和压力升高,(3)将压缩的蒸汽混合物施加到具有选择渗透性的膜上,以将蒸气混合物分离成膜渗透部分和非膜 (4)间接地将至少一个级分与步骤(1)的起始液体接触通过传热壁,以使接触部分的热量蒸发起始液体,和(5)回收 膜渗透部分和非膜渗透部分中的一个或两个; 以及用于在包含至少两种挥发性组分的混合物中相互分离挥发性组分的装置,其包括:(1)具有至少一个热交换器的蒸发器,其中引入了由(3)的膜分离器分离的至少一个馏分 起动液体供给侧,蒸发残渣排出侧和可选的辅助加热器; 以产生蒸汽混合物,(2)压缩机以压缩蒸汽混合物,和(3)膜分离器,其包括具有选择性渗透性的部件,以将压缩的蒸汽混合物分离成膜渗透部分和非渗透部分 。