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    • 1. 发明授权
    • Process for producing butyl acrylate
    • 丙烯酸丁酯的制备方法
    • US06180819B2
    • 2001-01-30
    • US09370004
    • 1999-08-06
    • William Bauer, Jr.Josefina Tseng ChapmanMario Giuseppe Luciano MirabelliJeremia Jesaja Venter
    • William Bauer, Jr.Josefina Tseng ChapmanMario Giuseppe Luciano MirabelliJeremia Jesaja Venter
    • C07C6748
    • C07C67/327C07C51/487C07C67/08C07C67/54C07C67/60Y02P20/582C07C57/04C07C69/54
    • An improved process for producing n-butyl acrylate in high yield and high purity substantially free of acrylic acid, incorporates one or more of the following new process components in an acid-catalyzed esterification process for producing n-butyl acrylate: 1. A hydrolytic recovery component, wherein heavy end adducts produced during the acid-catalyzed esterification are hydrolyzed, recovered, and recycled as valuable reactants from a hydrolytic recovery unit (HRU); 2. A cracking reactor component, preferably used with the HRU, wherein additional valuable reactants are recovered and recycled after treatment in the cracking reactor; and 3. A new distillative component, wherein a crude n-butyl acrylate stream is efficiently distilled in an aqueous mode through an acrylic acid separation column, thereby providing n-butyl acrylate substantially free of acrylic acid and in high yield. The first two components also are applicable to acid-catalyzed processes producing C1 to C4 alkyl acrylates. A continuous process producing n-butyl acrylate incorporating all new process components also is disclosed.
    • 在生产丙烯酸正丁酯的酸催化酯化方法中,以高产率和高纯度基本上不含丙烯酸生产丙烯酸正丁酯的改进方法包括一种或多种下列新方法组分:1。 水解回收组分,其中在酸催化的酯化期间产生的重端加合物被水解,回收并作为来自水解回收单元(HRU)的有价值的反应物再循环; 2。 优选与HRU一起使用的裂化反应器组分,其中在裂化反应器中处理后回收和再循环额外的有价值的反应物; 和3。 一种新的蒸馏组分,其中粗制丙烯酸正丁酯流通过丙烯酸分离塔以水溶液模式有效蒸馏,从而提供基本上不含丙烯酸的丙烯酸正丁酯,并且产率高。前两种组分也适用 产生C1-C4烷基丙烯酸酯的酸催化方法。 公开了一种生产含有所有新工艺组分的丙烯酸正丁酯的连续方法。
    • 2. 发明授权
    • Process for producing butyl acrylate
    • 丙烯酸丁酯的制备方法
    • US5877345A
    • 1999-03-02
    • US797380
    • 1997-02-07
    • William Bauer, Jr.Josefina Tseng ChapmanMario Giuseppe Luciano MirabelliJeremia Jesaja Venter
    • William Bauer, Jr.Josefina Tseng ChapmanMario Giuseppe Luciano MirabelliJeremia Jesaja Venter
    • C07C51/487C07C67/327C07C67/60C07C67/48
    • C07C67/327C07C51/487C07C67/08C07C67/54C07C67/60Y02P20/582
    • An improved process for producing n-butyl acrylate in high yield and high purity substantially free of acrylic acid, incorporates one or more of the following new process components in an acid-catalyzed esterification process for producing n-butyl acrylate:1. A hydrolytic recovery component, wherein heavy end adducts produced during the acid-catalyzed esterification are hydrolyzed, recovered, and recycled as valuable reactants from a hydrolytic recovery unit (HRU);2. A cracking reactor component, preferably used with the HRU, wherein additional valuable reactants are recovered and recycled after treatment in the cracking reactor; and3. A new distillative component, wherein a crude n-butyl acrylate stream is efficiently distilled in an aqueous mode through an acrylic acid separation column, thereby providing n-butyl acrylate substantially free of acrylic acid and in high yield.The first two components also are applicable to acid-catalyzed processes producing C.sub.1 to C.sub.4 alkyl acrylates. A continuous process producing n-butyl acrylate incorporating all new process components also is disclosed.
    • 用于以高产率和高纯度基本上不含丙烯酸生产丙烯酸酯的不饱和的不饱和单体的改进方法在酸催化的酯化方法中包含一种或多种以下新方法组分,用于生产+ E, n +丙烯酸丁酯:1.水解回收组分,其中在酸催化酯化期间产生的重端加合物被水解,回收和再循环,作为来自水解回收单元(HRU)的有价值的反应物; 2.优选与HRU一起使用的裂化反应器组分,其中在裂化反应器中处理后回收和再循环额外的有价值的反应物; 3.一种新的蒸馏组分,其中粗制的+ E,不为n +丙烯酸丁酯的丙烯酸酯料流通过丙烯酸分离塔以水模式被有效地蒸馏,从而提供基本上不含丙烯酸酯的+ E,n n + 的丙烯酸,并以高产率。 前两种组分也适用于生产C1-C4烷基丙烯酸酯的酸催化方法。 公开了一种连续的生产+ E,包含所有新工艺组分的非正丁基丙烯酸丁酯的方法。
    • 3. 发明授权
    • Process for producing butyl acrylate
    • 丙烯酸丁酯的制备方法
    • US5990343A
    • 1999-11-23
    • US49483
    • 1998-03-27
    • William Bauer, Jr.Josefina Tseng ChapmanMario Giuseppe Luciano MirabelliJeremia Jesaja Venter
    • William Bauer, Jr.Josefina Tseng ChapmanMario Giuseppe Luciano MirabelliJeremia Jesaja Venter
    • C07C51/487C07C67/327C07C67/60C07C67/48C07C27/26C07C51/42
    • C07C67/327C07C51/487C07C67/08C07C67/54C07C67/60Y02P20/582
    • An improved process for producing n-butyl acrylate in high yield and high purity substantially free of acrylic acid, incorporates one or more of the following new process components in an acid-catalyzed esterification process for producing n-butyl acrylate:1. A hydrolytic recovery component, wherein heavy end adducts produced during the acid-catalyzed esterification are hydrolyzed, recovered, and recycled as valuable reactants from a hydrolytic recovery unit (HRU);2. A cracking reactor component, preferably used with the HRU, wherein additional valuable reactants are recovered and recycled after treatment in the cracking reactor; and3. A new distillative component, wherein a crude n-butyl acrylate stream is efficiently distilled in an aqueous mode through an acrylic acid separation column, thereby providing n-butyl acrylate substantially free of acrylic acid and in high yield.The first two components also are applicable to acid-catalyzed processes producing C.sub.1 to C.sub.4 alkyl acrylates. A continuous process producing n-butyl acrylate incorporating all new process components also is disclosed.
    • 在生产丙烯酸正丁酯的酸催化酯化方法中,以高产率和高纯度基本上不含丙烯酸生产丙烯酸正丁酯的改进方法包括一种或多种以下新方法组分:1.水解回收 组分,其中在酸催化的酯化期间产生的重端加合物被水解,回收和再循环,作为来自水解回收单元(HRU)的有价值的反应物; 2.优选与HRU一起使用的裂化反应器组分,其中在裂化反应器中处理后回收和再循环额外的有价值的反应物; 3.一种新的蒸馏组分,其中粗制丙烯酸正丁酯流在水性模式下通过丙烯酸分离柱有效蒸馏,从而提供基本上不含丙烯酸的丙烯酸正丁酯,并以高产率。 前两种组分也适用于生产C1-C4烷基丙烯酸酯的酸催化方法。 公开了一种生产含有所有新工艺组分的丙烯酸正丁酯的连续方法。