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    • 55. 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。
    • 56. 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。
    • 57. 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 。
    • 58. 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
    • US20050267312A1
    • 2005-12-01
    • US10974015
    • 2004-10-27
    • Shuhei YadaYasushi OgawaKenji TakasakiYoshiro Suzuki
    • Shuhei YadaYasushi OgawaKenji TakasakiYoshiro Suzuki
    • C07B61/00C07C45/33C07C45/35C07C45/82C07C47/22C07C51/16C07C51/235C07C51/25C07C51/44C07C57/05C07C57/055
    • C07C45/33C07C45/35C07C51/44C07C47/22C07C57/04
    • 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 a low-boiling fraction separation step in the process and ensuring a continuous stable operation of the plant, and has excellent 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 the high-boiling components contained in a bottom liquid obtained from the purification step, said low-boiling fraction separation step comprising a plurality of low-boiling fraction separation steps which are disposed in parallel with each other and operated at the same time.
    • 提供了一种制备(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低沸点馏分分离步骤的失败而整体上停止用于生产的设备的操作,并确保 工厂连续稳定运行,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,所述低沸点馏分分离步骤包括多个低沸点馏分分离步骤,它们各自与 其他并在同一时间运行。
    • 60. 发明申请
    • Method for handling (meth) acrylic ester-containing solution
    • (甲基)丙烯酸酯溶液的处理方法
    • US20050189296A1
    • 2005-09-01
    • US11015744
    • 2004-12-20
    • Shuhei YadaKenji TakasakiYoshiro SuzukiYasushi Ogawa
    • Shuhei YadaKenji TakasakiYoshiro SuzukiYasushi Ogawa
    • B01D11/04C07C67/48B01D11/00
    • B01D11/0426B01D11/0488C07C67/48C07C69/54
    • The present invention provides a method for handling a (meth)acrylic ester-containing solution in which the (meth)acrylic ester-containing solution is treated by at least one process selected from washing, neutralization and extraction, the said method being capable of ensuring a stable continuous operation of the treating system for a long period of time without deteriorating a liquid-liquid separation efficiency and a distillation efficiency in subsequent steps while inhibiting the formation of sludge, when waste water or a waste aqueous solution obtained by recovering effective ingredients from the (meth)acrylic ester-containing solution treated by said at least one process is recycled to the previous process and reused therein. The above waste water or waste aqueous solution is previously cooled to a temperature of 10 to 50° C. and then solids are removed therefrom prior to recycling the waste water or waste aqueous solution to the previous process and reusing the same therein.
    • 本发明提供一种处理含(甲基)丙烯酸酯的溶液的方法,其中使用选自洗涤,中和和萃取的至少一种方法处理含(甲基)丙烯酸酯的溶液,所述方法能够确保 在废水或通过回收有效成分得到的废水水溶液的同时抑制污泥的形成,在长时间内稳定地连续操作处理系统,而不会降低后续步骤中的液 - 液分离效率和蒸馏效率 通过所述至少一种方法处理的(甲基)丙烯酸酯溶液被再循环到先前的方法中并重新使用。 将上述废水或废水水溶液预先冷却至10〜50℃的温度,然后在将废水或废水溶液再循环至先前的方法之前将固体除去,并将其再次使用。