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    • 52. 发明申请
    • Process for producing (meth)acrylic acid and (meth)acrylic esters
    • 制备(甲基)丙烯酸和(甲基)丙烯酸酯的方法
    • US20050267309A1
    • 2005-12-01
    • US11027685
    • 2005-01-03
    • Shuhei YadaKenji TakasakiYasushi OgawaYoshiro Suzuki
    • Shuhei YadaKenji TakasakiYasushi OgawaYoshiro Suzuki
    • B01D3/14B01D3/32B01J19/00C07B61/00C07C51/16C07C51/215C07C51/235C07C51/25C07C51/44C07C57/05C07C67/08C07C69/52C07C69/54
    • C07C51/215B01D3/14B01D3/322B01J19/002B01J2219/00006C07C51/252C07C67/08C07C57/04C07C69/54
    • There is provided a process for producing (meth)acrylic acid and (meth)acrylic esters, which can be operated in a continuous and stable manner for a long period of time. In a process for producing (meth)acrylic acid and (meth)acrylic esters comprising the steps of (A) reacting propane, propylene, or isobutylene and/or (meth)acrolein, with molecular oxygen or a molecular oxygen-containing gas by gas-phase catalytic oxidation method to produce crude (meth)acrylic acid; (B) purifying the resultant crude (meth)acrylic acid to produce a (meth)acrylic acid product; and (C) reacting the crude (meth)acrylic acid with alcohol to produce (meth)acrylic esters, in case of stopping a plant used in any one of the steps (B) and (C) disposed in parallel with each other, a resultant surplus crude (meth)acrylic acid being temporarily stored in a tank, and after restoring the stopped plant, the crude (meth)acrylic acid stored in a tank being fed to the plant used in the step (B) and/or the plant used in the step (C), wherein a production capacity of the plant used in the step (A) is designed so as to be lower than a total consumption capacity of the plants used in the steps (B) and (C).
    • 提供一种生产(甲基)丙烯酸和(甲基)丙烯酸酯的方法,其可以长时间连续稳定地操作。 在制备(甲基)丙烯酸和(甲基)丙烯酸酯的方法中,包括以下步骤:(A)使丙烷,丙烯或异丁烯和/或(甲基)丙烯醛与气体与分子氧或含分子氧的气体反应 相催化氧化法生产粗(甲基)丙烯酸; (B)纯化得到的粗制(甲基)丙烯酸,生成(甲基)丙烯酸产物; 和(C)使粗制的(甲基)丙烯酸与醇反应制备(甲基)丙烯酸酯,在停止在彼此平行设置的步骤(B)和(C)中任一步骤中使用的植物的情况下, 所得到的剩余的粗(甲基)丙烯酸暂时储存在罐中,并且在恢复停止的植物之后,储存在进料到步骤(B)中使用的植物的罐中的粗(甲基)丙烯酸和/或植物 在步骤(C)中使用,其中步骤(A)中使用的设备的生产能力被设计为低于步骤(B)和(C)中使用的设备的总消耗能力。
    • 58. 发明申请
    • Method for producing (meth)acrylic acid
    • (甲基)丙烯酸的制造方法
    • US20070055079A1
    • 2007-03-08
    • US11508247
    • 2006-08-23
    • Shuhei YadaKenji TakasakiYoshiro SuzukiYasushi Ogawa
    • Shuhei YadaKenji TakasakiYoshiro SuzukiYasushi Ogawa
    • C07C51/42
    • C07C51/46C07C57/04
    • The present invention provides a method for suppressing an undesirable polymerization reaction of (meth)acrylic acid in a purification step for producing (meth)acrylic acid and for avoiding troubles due to clogging of devices or the like, to thereby attain a stable continuous operation. The present invention provides a method for producing (meth)acrylic acid comprising: distilling a water-containing liquid of (meth)acrylic acid containing (meth)acrylic acid and water by using a distillation column in the presence of an azeotropic solvent boiling together with at least water to remove water from the water-containing liquid of (meth)acrylic acid through azeotropy with the azeotropic solvent, in which the water-containing liquid of (meth)acrylic acid is distilled in the presence of the azeotropic solvent after distillation by the azeotropic solvent is carried out in the distillation column.
    • 本发明提供一种抑制(甲基)丙烯酸在制造(甲基)丙烯酸的纯化步骤中不期望的聚合反应的方法,并且避免了由于装置等的堵塞而引起的麻烦,从而获得稳定的连续操作。 本发明提供一种(甲基)丙烯酸的制造方法,其特征在于,在与共沸溶剂一起沸腾的共沸溶剂的存在下,使用蒸馏塔,蒸馏含(甲基)丙烯酸和水的(甲基)丙烯酸的含水液体, 至少要通过与共沸溶剂共沸以从(甲基)丙烯酸的含水液体中除去水,其中(甲基)丙烯酸的含水液体在蒸馏后在共沸溶剂存在下被蒸馏, 共沸溶剂在蒸馏塔中进行。