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    • 4. 发明授权
    • Process for removing 2-butanol from tert-butanol/water mixtures
    • 从叔丁醇/水混合物中除去2-丁醇的方法
    • US07125474B2
    • 2006-10-24
    • US10790706
    • 2004-03-03
    • Andreas BeckmannDieter Reusch
    • Andreas BeckmannDieter Reusch
    • B01D3/42C07C29/82
    • C07C29/80Y10S203/09C07C31/12C07C31/125
    • The invention relates to a process for separating 2-butanol from an industrial mixture which includes 2-butanol, tert-butanol and water by separating water from the industrial mixture by distillation to obtain a distillate, wherein the distillate has, in terms of the 2-butanol, tert-butanol and water in the industrial mixture, a proportion by mass of water, which at a pressure, is greater than the limit concentration of the distillation boundary line connecting an azeotrope of tert-butanol and water; and an azeotrope of 2-butanol and water; subsequently changing the pressure so that the mixture has, in terms of the 2-butanol, tert-butanol and water in the distillate, a proportion by mass of water which is less than the limit concentration of the distillation boundary line connecting the distillation boundary line connecting an azeotrope of tert-butanol and water; and an azeotrope of 2-butanol and water; and subsequently distilling the mixture at the same pressure into a stream comprising 2-butanol and a stream comprising tert-butanol and water.
    • 本发明涉及一种通过蒸馏从工业混合物中分离出水以从工业混合物中分离出2-丁醇的方法,该工业混合物包括2-丁醇,叔丁醇和水,以获得馏出物,其中馏出物按照2 在工业混合物中的丁醇,叔丁醇和水,一定比例的水,其压力大于连接叔丁醇和水的共沸物的蒸馏边界线的极限浓度; 和2-丁醇和水的共沸物; 随后改变压力,使混合物以馏出物中的2-丁醇,叔丁醇和水的量计,其水的比例小于连接蒸馏边界线的蒸馏边界线的极限浓度 连接叔丁醇和水的共沸物; 和2-丁醇和水的共沸物; 随后将相同压力下的混合物蒸馏成包含2-丁醇的流和包含叔丁醇和水的流。
    • 6. 发明授权
    • Apparatus and process for purification of acrylic acid family
    • 用于纯化丙烯酸家族的装置和方法
    • US07014736B2
    • 2006-03-21
    • US10784553
    • 2004-02-23
    • Yukihiro Matsumoto
    • Yukihiro Matsumoto
    • B01D3/00C07C69/54C07C51/44C07C67/54
    • B01D3/322B01D3/14C07C51/44Y10S203/09Y10S203/22C07C57/04
    • An apparatus and a process for purification of an acrylic acid family. The apparatus is an apparatus for distillation purification of the acrylic acid family encompassing acrylic acid and its esters, and includes: a distillation column 10 to which a liquid containing the acrylic acid family is supplied, and from the column top of which a vapor is retrieved, and from the column bottom of which a liquid is retrieved; a condenser 20 which is connected to the column top side of the distillation column 10, and to which the vapor having been retrieved from the distillation column is supplied, and which condenses the supplied vapor and then refluxes a portion of the resultant condensate to the distillation column 10, and from which the residual condensate is retrieved; and a reboiler 30 which is connected to the column bottom side of the distillation column 10, and to which the liquid in the distillation column 10 is supplied, and which heat-boils the supplied liquid and then returns it to the distillation column 10; wherein the reboiler 30 is set in a number of at least two in parallel to the distillation column 10. The process uses the above apparatus.
    • 用于纯化丙烯酸族的装置和方法。 该装置是用于蒸馏纯化包含丙烯酸及其酯的丙烯酸族的装置,并且包括:供应含有丙烯酸族的液体的蒸馏塔10,并且从其塔顶返回蒸气 ,并从其底部的底部取出液体; 连接到蒸馏塔10的塔顶侧并且从蒸馏塔中回收蒸气的冷凝器20被冷凝,并且将所提供的蒸气冷凝,然后将所得冷凝物的一部分回流至蒸馏 塔10,并从中回收剩余的冷凝物; 以及与蒸馏塔10的塔底侧连接并供给蒸馏塔10中的液体并将供给的液体热沸腾后再返回到蒸馏塔10的再沸器30; 其中所述再沸器30与所述蒸馏塔10并联设置为至少两个。 该方法使用上述装置。
    • 10. 发明申请
    • Apparatus and process for purification of acrylic acid family
    • 用于纯化丙烯酸家族的装置和方法
    • US20040182693A1
    • 2004-09-23
    • US10784553
    • 2004-02-23
    • Nippon Shokubai Co., Ltd.
    • Yukihiro Matsumoto
    • C07B031/00B01D003/02B01D003/14C07C051/42
    • B01D3/322B01D3/14C07C51/44Y10S203/09Y10S203/22C07C57/04
    • There are disclosed an apparatus and a process for purification of an acrylic acid family. The apparatus is an apparatus for distillation purification of the acrylic acid family encompassing acrylic acid and its esters, and comprises: a distillation column 10 to which a liquid containing the acrylic acid family is supplied, and from the column top of which a vapor is retrieved, and from the column bottom of which a liquid is retrieved; a condenser 20 which is connected to the column top side of the distillation column 10, and to which the vapor having been retrieved from the distillation column is supplied, and which condenses the supplied vapor and then refluxes a portion of the resultant condensate to the distillation column 10, and from which the residual condensate is retrieved; and a reboiler 30 which is connected to the column bottom side of the distillation column 10, and to which the liquid in the distillation column 10 is supplied, and which heat-boils the supplied liquid and then returns it to the distillation column 10; wherein the reboiler 30 is set in a number of at least two in parallel to the distillation column 10. The process uses the above apparatus.
    • 公开了用于纯化丙烯酸族的装置和方法。 该装置是用于蒸馏纯化包含丙烯酸及其酯的丙烯酸族的装置,并且包括:供应含有丙烯酸族的液体的蒸馏塔10,并且从其塔顶返回蒸气 ,并从其底部的底部取出液体; 连接到蒸馏塔10的塔顶侧并且从蒸馏塔中回收蒸气的冷凝器20被冷凝,并且将所提供的蒸气冷凝,然后将所得冷凝物的一部分回流至蒸馏 塔10,并从中回收剩余的冷凝物; 以及与蒸馏塔10的塔底侧连接并供给蒸馏塔10中的液体并将供给的液体热沸腾后再返回到蒸馏塔10的再沸器30; 其中所述再沸器30与所述蒸馏塔10并联设置为至少两个数量。所述方法使用上述装置。