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    • 2. 发明申请
    • Method of preparing polycarbonate resin
    • 聚碳酸酯树脂的制备方法
    • US20060089484A1
    • 2006-04-27
    • US11255515
    • 2005-10-21
    • Mijeung HongJong Hun KimSung Kyou ParkBoo Gon Woo
    • Mijeung HongJong Hun KimSung Kyou ParkBoo Gon Woo
    • C08G64/00
    • C08G64/307C08G64/186C08G64/205
    • A method of preparing a high molecular weight polycarbonate resin is provided. In the method, a condensation polymerization process is used so that a mole fraction of arylcarbonate existing in a terminated group of a reaction side product having a degree of polymerization of less than 3 obtained as a result of transesterification and in a non-reacted diarylcarbonate is reduced. As a result, a high molecular weight polycarbonate can be obtained by solid state polymerization. A polycarbonate with an identical molecular weight can be produced in a substantially short time, compared with a polycarbonate produced through solid state polymerization without condensation polymerization. In addition, the non-use of a poisonous phosgene contributes to stability. Furthermore, quality polycarbonate may be guaranteed.
    • 提供了制备高分子量聚碳酸酯树脂的方法。 在该方法中,使用缩聚方法,使得存在于作为酯交换反应的结果得到的聚合度小于3的反应副产物的末端基团中的芳基碳酸酯的摩尔分数和未反应的碳酸二芳基酯的摩尔分数为 减少 结果,可以通过固态聚合获得高分子量聚碳酸酯。 与通过不进行缩聚的固相聚合制造的聚碳酸酯相比,可以在短时间内生产具有相同分子量的聚碳酸酯。 此外,不使用有毒光气有助于稳定。 此外,可以保证质量的聚碳酸酯。
    • 4. 发明授权
    • Method of preparing polycarbonate resin
    • 聚碳酸酯树脂的制备方法
    • US07332559B2
    • 2008-02-19
    • US11255515
    • 2005-10-21
    • Mijeung HongJong Hun KimSung Kyou ParkBoo Gon Woo
    • Mijeung HongJong Hun KimSung Kyou ParkBoo Gon Woo
    • C08G64/00
    • C08G64/307C08G64/186C08G64/205
    • A method of preparing a high molecular weight polycarbonate resin is provided. In the method, a condensation polymerization process is used so that a mole fraction of arylcarbonate existing in a terminated group of a reaction side product having a degree of polymerization of less than 3 obtained as a result of transesterification and in a non-reacted diarylcarbonate is reduced. As a result, a high molecular weight polycarbonate can be obtained by solid state polymerization. A polycarbonate with an identical molecular weight can be produced in a substantially short time, compared with a polycarbonate produced through solid state polymerization without condensation polymerization. In addition, the non-use of a poisonous phosgene contributes to stability. Furthermore, quality polycarbonate may be guaranteed.
    • 提供了制备高分子量聚碳酸酯树脂的方法。 在该方法中,使用缩聚方法,使得存在于作为酯交换反应的结果得到的聚合度小于3的反应副产物的末端基团中的芳基碳酸酯的摩尔分数和未反应的碳酸二芳基酯的摩尔分数为 减少 结果,可以通过固态聚合获得高分子量聚碳酸酯。 与通过不进行缩聚的固相聚合制造的聚碳酸酯相比,可以在短时间内生产具有相同分子量的聚碳酸酯。 此外,不使用有毒光气有助于稳定。 此外,可以保证质量的聚碳酸酯。
    • 5. 发明授权
    • Method of producing unsaturated acid from olefin
    • 从烯烃生产不饱和酸的方法
    • US07816559B2
    • 2010-10-19
    • US11378438
    • 2006-03-17
    • Boo Gon WooJun Seok KoKyoung Su HaSeong Pil KangSeok Hwan ChoiYoung Bae Kim
    • Boo Gon WooJun Seok KoKyoung Su HaSeong Pil KangSeok Hwan ChoiYoung Bae Kim
    • C07C51/16
    • B01J8/067B01J2208/00212B01J2208/025C07C51/215C07C51/252C07C57/04
    • Disclosed is a shell-and-tube heat exchanger type reactor that can be used for a process of producing unsaturated acids from olefins via fixed-bed catalytic partial oxidation, which comprises at least one reaction tube, each including at least one first-step catalyst layer, in which olefins are oxidized by a first-step catalyst to mainly produce unsaturated aldehydes, and at least two second-step catalyst layers, in which the unsaturated aldehydes are oxidized by a second-step catalyst to produce unsaturated acids, wherein a first catalyst layer of the second-step catalyst layers, disposed right adjacent to the first-step catalyst layer, has an activity corresponding to 5˜30% of the activity of the catalyst layer having a highest activity among the second-step catalyst layers. A method of producing unsaturated acids from olefins by using the reactor is also disclosed.
    • 公开了一种壳管式热交换器型反应器,其可用于通过固定床催化部分氧化由烯烃生产不饱和酸的方法,其包括至少一个反应管,每个反应管包含至少一个第一步催化剂 层,其中烯烃被第一步催化剂氧化以主要产生不饱和醛,以及至少两个第二步催化剂层,其中不饱和醛被第二步催化剂氧化以产生不饱和酸,其中第一 与第一级催化剂层相邻设置的第二级催化剂层的催化剂层的活性相当于第二级催化剂层中活性最高的催化剂层的活性的5〜30%的活性。 还公开了通过使用反应器由烯烃生产不饱和酸的方法。
    • 6. 发明授权
    • Method of producing unsaturated acid in fixed-bed catalytic partial oxidation reactor with enhanced heat control system
    • 固定床催化部分氧化反应器生产不饱和酸的方法,采用增强型热控系统
    • US07262324B2
    • 2007-08-28
    • US11019363
    • 2004-12-23
    • Kyoung Su HaGeon Yong KimSeong Pil KangBoo Gon Woo
    • Kyoung Su HaGeon Yong KimSeong Pil KangBoo Gon Woo
    • C07C51/16B01J8/04
    • C07C45/35C07C51/252C07C47/22C07C57/04
    • The present invention provides a process of producing unsaturated acids from unsaturated aldehydes by fixed-bed catalytic partial oxidation in a shell-and-tube heat exchanger-type reactor, as well as a shell-and-tube heat exchanger-type reactor for use in the process. In the invention, second-stage reaction zone of mainly producing unsaturated acids by the catalytic vapor phase oxidation of an unsaturated aldehyde-containing gas mixture produced in a first-stage reaction zone with molecular oxygen is divided into two or more shell spaces by at least one partition. Each of the divided shell spaces is filled with a heat transfer medium, and the heat transfer medium in each shell space is maintained at isothermal temperature or a temperature difference of 0-5° C. Also, in order to protect catalyst layers from a highly exothermic reaction, the process is performed at a limited temperature difference between the temperature at a hot spot and the temperature of the heat transfer medium. Also, in order to facilitate the removal of heat generation at a location where the partition is placed, a reaction inhibition layer is disposed in that location. The improved heat control system for reactors provided according to the present invention can secure the heat stability of the catalyst layer, reduce the amount of byproducts, and increase the yield of a final product.
    • 本发明提供了一种在壳管式热交换器型反应器中通过固定床催化部分氧化由不饱和醛生成不饱和酸的方法,以及用于在管式热交换器型反应器中使用的管壳式热交换器型反应器 的过程。 在本发明中,通过在分子氧的第一阶段反应区中产生的不饱和醛的气体混合物的催化气相氧化主要生成不饱和酸的第二阶段反应区至少分成两个或更多个壳层空间 一个分区。 每个分开的壳体空间填充有传热介质,并且每个壳体空间中的传热介质保持在等温温度或0-5℃的温差。此外,为了保护催化剂层免受高温 放热反应,该过程在热点温度与传热介质的温度之间的有限温度差下进行。 此外,为了便于在隔离物的位置除去发热,在该位置设置反应抑制层。 根据本发明提供的用于反应器的改进的热控制系统可以确保催化剂层的热稳定性,减少副产物的量,并且提高最终产品的产率。
    • 8. 发明授权
    • Method for producing (meth) acrylic acid
    • (甲基)丙烯酸的制造方法
    • US07632968B2
    • 2009-12-15
    • US11192223
    • 2005-07-28
    • Seong Pil KangSeok Hwan ChoiKyoung Su HaJun Seok KoYoung Bae KimBoo Gon WooMin Jeong Park
    • Seong Pil KangSeok Hwan ChoiKyoung Su HaJun Seok KoYoung Bae KimBoo Gon WooMin Jeong Park
    • C07C51/42
    • C07C51/44C07C51/48C07C57/04
    • Disclosed is a method for producing (meth)acrylic acid comprising a process of recovering (meth)acrylic acid as aqueous (meth)acrylic acid solution from a (meth)acrylic acid-containing gas mixture produced by the catalytic gas phase oxidation of at least one reactant selected from the group consisting of propane, propylene, isobutylene and (meth)acrolein, wherein the recovering process comprises the steps of: (1) feeding the (meth)acrylic acid-containing gas mixture into a quenching tower and condensing it in the quenching tower so as to recover an aqueous (meth)acrylic acid solution from the bottom of the quenching tower, in which some of the recovered aqueous (meth)acrylic acid solution is recycled to the upper portion of the quenching tower so as to condense the (meth)acrylic acid-containing gas mixture; (2) passing the uncondensed part of the (meth)acrylic acid-containing gas mixture from the top of the quenching tower to a distillation tower; and (3) heating the bottom of the distillation tower to separate water-containing impurity components from the uncondensed (meth)acrylic acid-containing gas mixture and to discharge them from the top of the distillation tower. A system used for carrying out the method is also disclosed.
    • 公开了一种制备(甲基)丙烯酸的方法,包括从(甲基)丙烯酸水溶液中回收(甲基)丙烯酸作为(甲基)丙烯酸水溶液的方法,所述方法至少由 一种选自丙烷,丙烯,异丁烯和(甲基)丙烯醛的反应物,其中回收方法包括以下步骤:(1)将含(甲基)丙烯酸的气体混合物进料到淬火塔中并将其冷凝 淬火塔,以从骤冷塔的底部回收(甲基)丙烯酸水溶液,其中一些回收的(甲基)丙烯酸水溶液被循环到淬火塔的上部以冷凝 (甲基)丙烯酸气体混合物; (2)使来自(甲基)丙烯酸的气体混合物的未冷凝的部分从淬火塔的顶部通到蒸馏塔; 和(3)加热蒸馏塔的底部以将含水的杂质组分与未冷凝(甲基)丙烯酸的气体混合物分离并从蒸馏塔的顶部排出。 还公开了用于执行该方法的系统。
    • 9. 发明授权
    • Process for preparing unsaturated carboxylic acid esters and apparatus
for preparing the same
    • 不饱和羧酸酯的制备方法及其制备方法
    • US5645696A
    • 1997-07-08
    • US346191
    • 1994-11-21
    • Boo Gon WooKwang Ho ParkHwa Myung JooHan Sun Lee
    • Boo Gon WooKwang Ho ParkHwa Myung JooHan Sun Lee
    • B01J8/02B01J8/04B01J31/08C07C67/08C07C69/52C07C69/54B01D3/34
    • B01J8/0496B01J8/0453C07C67/08B01J2208/00247B01J2208/00283Y02P20/582
    • The present invention relates to a process for continuously preparing unsaturated carboxylic acid esters by esterifying an (aliphatic) alcohol having 1 to 8 carbon atoms with an unsaturated carboxylic acid in the presence of a cation exchange resin catalyst, characterized in that the process is conducted by continuously circulating said reactants in contact with said catalyst from the top to the bottom through a reactor which is composed in the form of a fixed bed divided into 1 to 10 steps wherein each step comprises a catalyst bed, a filter and a air inlet, and has a thermal insulating outer wall, supplying a vaporizing heat for extraction of water, which is produced during the reaction, through a heat exchanger outside the reactor, circulating the reactants between the reactor and the heat exchanger by means of a circulating pump, contacting an azeotropic mixture of water vaporized by the heat exchanger and an alcohol with an alcohol circulating in a column tower or a raw alcohol supplied from an alcohol inlet located on the top of the column tower to recycle the high boiling component into the reactor and, at the same time, to transfer the light component to the upper part of the column in which the light component is condensed, separating the condensate into an organic layer and water in a decanter, and then recycling the organic layer into the reactor and removing the water produced during the reaction, and a novel apparatus for carrying out this process.
    • 本发明涉及在阳离子交换树脂催化剂存在下,通过用不饱和羧酸酯化具有1〜8个碳原子的(脂肪族)醇来连续制备不饱和羧酸酯的方法,其特征在于,该方法是通过 将所述反应物与所述催化剂从顶部到底部连续循环通过以固定床形式分成1至10个步骤的反应器,其中每个步骤包括催化剂床,过滤器和进气口,以及 具有绝热外壁,通过在反应器外部的热交换器提供在反应期间产生的用于萃取水的汽化热,借助于循环泵将反应物循环在反应器和热交换器之间, 由热交换器蒸发的水的共沸混合物和在柱塔或粗酒精中循环的醇的醇 从位于塔塔顶部的酒精入口引出,将高沸点组分循环到反应器中,同时将光组分转移到其中冷成分的塔的上部,分离 将冷凝物倒入有机层中并在滗析器中加水,然后将有机层再循环到反应器中并除去反应期间产生的水,以及用于实施该方法的新型装置。