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    • 41. 发明授权
    • Process for producing (meth)acrylic acid or (meth)acrolein
    • (甲基)丙烯酸或(甲基)丙烯醛的制造方法
    • US07563927B2
    • 2009-07-21
    • US11547004
    • 2004-10-27
    • Yasushi OgawaShuhei YadaYoshiro SuzukiKenji TakasakiKimikatsu Jinno
    • Yasushi OgawaShuhei YadaYoshiro SuzukiKenji TakasakiKimikatsu Jinno
    • C07C51/16
    • C07C45/35C07C51/215C07C51/252C07C47/22C07C57/04
    • A producing method of (meth)acrolein or (meth)acrylic acid where by use of a multi-tubular reactor that has a plurality of reaction tubes filled with a catalyst, catalytic gas phase oxidation of propylene, propane, isobutylene or (meth)acrolein is carried out in the presence of a composite oxide catalyst by use of molecular oxygen or a gas containing molecular oxygen, in which method (meth)acrolein or (meth)acrylic acid can be obtained stably in high yield for a long period of time without allowing the activity of the catalyst to decrease locally (disproportionately) and extremely. A temperature difference between a temperature of a heat medium at the beginning of operation and a peak temperature of the catalyst is set in a range of 20 to 80° C., and during operations a change of the peak temperature T of the catalyst in a tube axis direction is maintained in a definite range.
    • (甲基)丙烯醛或(甲基)丙烯酸的制备方法,其中通过使用多管反应器,其具有填充有催化剂的多个反应管,丙烯,丙烷,异丁烯或(甲基)丙烯醛的催化气相氧化 通过使用分子氧或含分子氧的气体在复合氧化物催化剂存在下进行,其中可以以高产率长时间稳定地获得(甲基)丙烯醛或(甲基)丙烯酸,而不用 允许催化剂的活性局部(不成比例地)减少和极度降低。 操作开始时的热介质的温度与催化剂的峰值温度之间的温差设定在20〜80℃的范围内,在操作中,催化剂的峰值温度T的变化为 管轴方向保持在一定范围内。
    • 48. 发明授权
    • Processes for producing (meth)acrylic acid
    • (甲基)丙烯酸的制造方法
    • US07015357B2
    • 2006-03-21
    • US10898341
    • 2004-07-26
    • Shuhei YadaKenji TakasakiYasushi OgawaYoshiro Suzuki
    • Shuhei YadaKenji TakasakiYasushi OgawaYoshiro Suzuki
    • C07C51/42C07C57/02
    • C07C51/44C07C57/04
    • In the purification and distillation step of acrylic acid (including (meth)acrylic acid), stable continuous operation for a long period is enabled by inhibiting the undesirable polymerization reaction of acrylic acid thereby to prevent the device from a trouble such as clogging. A process for producing acrylic acid which comprises purifying crude acrylic acid prepared by vapor-phase catalytic oxidation by distillation, wherein the concentration of β-acryloxypropionic acid in the feed stream to a distillation column mainly for the separation of water from acrylic acid is controlled to be at most one-fiftieth of the concentration of acrylic acid; the concentration of β-acryloxypropionic acid in the feed stream to a distillation column mainly for the separation of acetic acid from acrylic acid is controlled to be at most one-fortieth of the concentration of acrylic acid; and the concentration of β-acryloxypropionic acid in the feed stream to a distillation column mainly for the separation of acrylic acid from water, acetic acid and a solvent is controlled to be at most one-fiftieth of the concentration of acrylic acid.
    • 在丙烯酸​​(包括(甲基)丙烯酸)的纯化和蒸馏步骤中,通过抑制丙烯酸的不期望的聚合反应,能够长时间的稳定的连续操作,从而防止装置等堵塞的问题。 一种制备丙烯酸的方法,其包括通过蒸馏气相催化氧化制备的粗丙烯酸的纯化,其中将主要用于从丙烯酸分离水的蒸馏塔的进料流中的β-丙烯酰氧基丙酸的浓度控制为 至多为丙烯酸浓度的五十分之一; 将主要用于从丙烯酸分离乙酸的蒸馏塔的进料流中的β-丙烯酰氧基丙酸的浓度控制在丙烯酸浓度的至多四十分之一; 并且将主要用于将丙烯酸与水,乙酸和溶剂分离的蒸馏塔的进料流中的β-丙烯酰氧基丙酸的浓度控制在丙烯酸浓度的至多五十分之一。
    • 49. 发明授权
    • Method for handling high-viscosity substances
    • 高粘度物质处理方法
    • US06989463B2
    • 2006-01-24
    • US10978281
    • 2004-11-01
    • Shuhei YadaYasushi OgawaKenji TakasakiYoshiro Suzuki
    • Shuhei YadaYasushi OgawaKenji TakasakiYoshiro Suzuki
    • C07C57/02C07C51/42C07C69/34C07C67/48
    • C07C51/50C07C67/62C07C57/04C07C69/54
    • There is provided a method for handling high-viscosity substances discharged from a production process of acrylic acid or esters thereof by gas-phase catalytic oxidation, which method is improved such that upon transporting the high-viscosity substances in a molten state to a storage tank through a pipeline, the retention or clogging of the high-viscosity substances in the pipeline can be effectively prevented without adding a solvent thereto, resulting in smooth transportation thereof through the pipeline.In the method for handling high-viscosity substances discharged from a production process of acrylic acid or esters thereof by gas-phase catalytic oxidation according to the present invention, when the high-viscosity substances are transported to a storage tank through a pipeline, contents of acrylic acid polymers and a polymerization inhibitor in the high-viscosity substances are controlled to not less than 40% by weight and not less than 4% by weight, respectively, and the high-viscosity substances are maintained at a temperature of not less than 110° C.
    • 提供了一种通过气相催化氧化处理由丙烯酸或其酯的生产方法排出的高粘度物质的方法,该方法得到改进,使得在熔融状态下将高粘度物质输送到储罐 通过管道,可以有效地防止管道中高粘度物质的滞留或堵塞,而不需要加入溶剂,从而使其通过管道的顺利输送。 在根据本发明的通过气相催化氧化处理由丙烯酸或其酯的制备方法排出的高粘度物质的方法中,当高粘度物质通过管道输送到储罐时, 高粘度物质中的丙烯酸聚合物和阻聚剂分别控制在不低于40重量%且不小于4重量%,并且高粘度物质保持在不低于110℃的温度 C。
    • 50. 发明申请
    • Process for producing (meth)acrolein or (meth)acrylic acid
    • 制备(甲基)丙烯醛或(甲基)丙烯酸的方法
    • US20050267313A1
    • 2005-12-01
    • US10985015
    • 2004-11-10
    • Shuhei YadaYasushi OgawaKenji TakasakiYoshiro Suzuki
    • Shuhei YadaYasushi OgawaKenji TakasakiYoshiro Suzuki
    • C07B61/00C07C45/33C07C45/35C07C45/82C07C47/22C07C51/16C07C51/25C07C51/44C07C57/05
    • C07C45/33C07C45/35C07C51/252C07C47/22C07C57/04
    • There is provided a process for producing (meth)acrolein or (meth)acrylic acid which is capable of avoiding stoppage of operation of a plant for production thereof as a whole due to failure of an oxidation reaction step in the process and ensuring a continuous stable operation of the plant, and is excellent in economical aspects. The process for producing (meth)acrolein or (meth)acrylic acid according to the present invention sequentially comprises an oxidation reaction step of subjecting a raw gas to gas-phase catalytic oxidation; a reaction gas cooling step of cooling the resultant reaction gas; a low-boiling fraction separation step of separating low-boiling components from the reaction product; a purification step of separating and removing high-boiling components from the reaction product; and a high-boiling fraction decomposition step of decomposing high-boiling components contained in a bottom liquid obtained from the purification step, said oxidation reaction step comprising a plurality of oxidation reaction steps which are disposed in parallel with each other and operated at the same time.
    • 提供了一种生产(甲基)丙烯醛或(甲基)丙烯酸的方法,其能够避免由于该方法中的氧化反应步骤失败而导致植物整体生产的停止,从而确保连续稳定 工厂运行,经济性好。 根据本发明的(甲基)丙烯醛或(甲基)丙烯酸的制备方法依次包括使原料气体进行气相催化氧化的氧化反应步骤; 反应气体冷却步骤,冷却所得到的反应气体; 将低沸点组分与反应产物分离的低沸点馏分分离步骤; 从反应产物中分离除去高沸点组分的纯化步骤; 以及分解由纯化工序得到的底液中含有的高沸点组分的高沸点馏分分解步骤,所述氧化反应步骤包括彼此平行并且同时操作的多个氧化反应步骤 。