会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 4. 发明授权
    • Preparation of (meth)acrylates
    • (甲基)丙烯酸酯的制备
    • US06512138B1
    • 2003-01-28
    • US09567983
    • 2000-05-10
    • Albrecht DamsHeinrich AichingerHolger HerbstGerhard NestlerJürgen Schröder
    • Albrecht DamsHeinrich AichingerHolger HerbstGerhard NestlerJürgen Schröder
    • C07C6952
    • C07C67/08C07C67/327C07C69/54
    • The process for the esterification of (meth)acrylic acid with an alkanol in the presence of an esterification catalyst, in which unconverted starting compounds and the (meth)acrylate to be formed are separated off by distillation and an oxyester-containing bottom product is formed and is separated off, and (a) in the bottom product separated off, the oxyesters present are cleaved, if required after the addition of (meth)acrylic acid and/or oligomeric (meth)acrylic acid, directly in the presence of acid catalysts differing from (meth)acrylic acid and/or oligomeric (meth)acrylic acid, and the cleavage products are removed, a cleavage residue remaining, or (b) the oxyesters are first removed by distillation from the cleavage product separated off, a distillation residue remaining, and the oxyesters removed are cleaved, if required after addition of (meth)acrylic acid and/or oligomeric (meth)acrylic acid, in the presence of acid catalysts differing from (meth)acrylic acid and/or oligomeric (meth)acrylic acid, and the cleavage products are removed, a cleavage residue remaining, is carried out in such a way that the cleavage residue obtained in step (a) or the cleavage residue obtained in step (b) is hydrolytically cleaved together with the resulting distillation residue in the presence of water and acids or bases.
    • 在酯化催化剂存在下,(甲基)丙烯酸与烷醇的酯化反应的方法,其中未转化的起始化合物和待形成的(甲基)丙烯酸酯通过蒸馏和含有含氧酯的底部产物分离出来 并分离出来,(a)在分离出的底部产物中,如果需要,在酸催化剂存在下直接加入(甲基)丙烯酸和/或低聚(甲基)丙烯酸后,存在的氧化酯被切割 与(甲基)丙烯酸和/或低聚(甲基)丙烯酸不同,除去裂解产物,剩余的裂解残余物或(b)氧酯首先通过蒸馏从分离的裂解产物中除去,蒸馏残余物 除去(甲基)丙烯酸和/或低聚(甲基)丙烯酸之外,如果需要,在不同于(甲基)丙烯酸和/或低聚(甲基)丙烯酸的酸催化剂的存在下, 甲基)丙烯酸,并且去除裂解产物,残留切割残余物,使得步骤(a)中获得的裂解残基或步骤(b)中获得的裂解残基与 在水和酸或碱的存在下产生蒸馏残余物。
    • 5. 发明授权
    • Method for producing (meth) acrylic acid esters
    • (甲基)丙烯酸酯的制造方法
    • US07268251B2
    • 2007-09-11
    • US10479562
    • 2002-05-28
    • Matthias GeisendoerferAlbrecht DamsGerhard Nestler
    • Matthias GeisendoerferAlbrecht DamsGerhard Nestler
    • C07C69/52
    • C07D211/94C07C67/54C07C213/06C07C213/10Y02P20/582C07C69/54C07C219/08
    • The invention relates to a method for producing (meth)acrylic acid esters IV by means of transesterification of a (meth)acrylic acid ester I with an alcohol R2OH comprising at least one more carbon atom than the alcohol constituents (R1O—) in the (meth)acrylic acid ester I to be subjected to transesterification, in the presence of a catalyst or a catalyst mixture. Either essentially the (meth)acrylic acid ester I is separated and then the catalyst used is separated by distillation (catalyst separation), or the catalyst used is separated by distillation first (catalyst separation), and then essentially the (meth)acrylic acid ester I is separated, from the reaction product of the transesterification. Constituents from the mixture obtained, which have a lower boiling point than the (meth)acrylic acid ester IV, are essentially separated by distillation (separation of constituents at low boiling point), and the (meth)acrylic acid ester IV is then purified by distillation (purification by distillation).
    • 本发明涉及一种通过(甲基)丙烯酸酯I与醇R 2 OH的酯交换反应制备(甲基)丙烯酸酯IV的方法,其包含至少比另一个碳原子多 在(甲基)丙烯酸酯I中,在催化剂或催化剂混合物的存在下进行酯交换反应的醇成分(R 1 O - O-)。 基本上分离(甲基)丙烯酸酯I,然后通过蒸馏(催化剂分离)分离所用的催化剂,或者首先通过蒸馏分离催化剂(催化剂分离),然后基本上将(甲基)丙烯酸酯 我与酯交换的反应产物分离。 得到的沸点比(甲基)丙烯酸酯IV低的混合物的成分基本上通过蒸馏分离(低沸点成分分离),然后将(甲基)丙烯酸酯IV纯化 蒸馏(通过蒸馏纯化)。
    • 10. 发明授权
    • Rectificative separation of fluids comprising (meth) acrylic monomers
    • 包含(甲基)丙烯酸单体的流体的精馏分离
    • US07351310B2
    • 2008-04-01
    • US10658257
    • 2003-09-10
    • Joachim ThielAlbrecht DamsJuergen Schroeder
    • Joachim ThielAlbrecht DamsJuergen Schroeder
    • B01D3/34B01D5/00C07C51/42
    • C07C51/44B01D3/14B01D5/0063C07C45/81C07C45/82C07C51/43C07C67/54Y10S203/22C07C47/22C07C57/04C07C69/54
    • A process for rectificatively separating fluids including (meth)acrylic monomers in a rectification column by directly cooling the vapor including (meth)acrylic monomers rising to the top of the rectification column to form top condensate including (meth)acrylic monomers, the condensation space at the top of the column being separated from the region of the rectification column containing the separating internals only by at least one chimney tray from which the top condensate formed is removed from the rectification column, which includes effecting the direct cooling of the vapor in the condensation space in at least two spray zones which are spatially successive and are flowed through by vapor by spraying supercooled top condensate including added polymerization inhibitor, and the temperature of the sprayed supercooled top condensate becoming lower from spray zone to spray zone in the flown direction of the vapor.
    • 通过将上升到精馏塔顶部的(甲基)丙烯酸单体直接冷却的蒸汽直接冷却,形成精馏塔中的(甲基)丙烯酸单体,形成包含(甲基)丙烯酸单体的顶部缩合物, 柱的顶部仅由至少一个烟囱式塔板从含有分离内部件的精馏塔的区域分离出,从该澄清塔中形成的顶部冷凝物从精馏塔从精馏塔排出,其中包括直接冷却冷凝物中的蒸气 至少两个喷雾区的空间,其空间连续并通过喷雾通过喷雾过冷顶部冷凝物(包括加入的阻聚剂)而流过,并且喷射的过冷顶部冷凝物的温度从喷射区域向喷雾区域的流动方向变低 汽。