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    • 2. 发明申请
    • PROCESS FOR SYNTHESIS OF ACROLEIN
    • ACROLEIN合成方法
    • US20120310016A1
    • 2012-12-06
    • US13577680
    • 2010-02-09
    • Takeyuki KondoHiroyuki ItoYasunari SaseToshiaki MatsuoKenichiro OkaMasayuki KamikawaMasashi Tanto
    • Takeyuki KondoHiroyuki ItoYasunari SaseToshiaki MatsuoKenichiro OkaMasayuki KamikawaMasashi Tanto
    • C07C45/00
    • B01J8/006B01J3/008B01J2219/00006C07C45/52C07C45/81Y02P20/544C07C47/22
    • An object of the present invention is to provide a technology which can suppress the blockage and abrasion of pipes and devices caused by the production of by-products and stably synthesize acrolein at a high yield, under a condition in which energy efficiency is improved by an elevated concentration of glycerol in a reaction liquid, in a process for synthesis of acrolein by reacting supercritical water and an acid with glycerol. An embodiment of the present invention includes: setting a concentration of glycerol in the reaction liquid at 30% by weight or lower; also cooling the reaction liquid to a temperature between a temperature (300° C. or lower) at which the reaction stops and a temperature (100° C. or higher) at which tar contained in the reaction liquid can keep a state in which its viscosity is sufficiently low; then separating and removing carbon particles from the reaction liquid; subsequently cooling the reaction liquid to a temperature which is a boiling point of water or lower and at which the tar component in the reaction liquid does not adhere to devices; and then decompressing the cooled reaction liquid.
    • 本发明的目的是提供一种能够抑制副产物生成引起的管道和装置的堵塞和磨损的技术,并且在能够提高能量效率的条件下以高产率稳定地合成丙烯醛 在超临界水和酸与甘油反应合成丙烯醛的方法中,反应液中甘油浓度升高。 本发明的一个实施方案包括:将反应液中甘油的浓度设定为30重量%以下; 还将反应液体冷却至反应停止的温度(300℃以下)和反应液中所含的焦油的温度(100℃以上)可以保持其状态 粘度足够低; 然后从反应液中分离除去碳颗粒; 随后将反应液体冷却至沸点低于水的温度,反应液中的焦油成分不附着在装置上; 然后减压冷却的反应液。
    • 3. 发明授权
    • Equipment and method for producing polyhydroxycarboxylic acid
    • 多羟基羧酸的制备方法和设备
    • US08153754B2
    • 2012-04-10
    • US12544477
    • 2009-08-20
    • Masayuki KamikawaToshiaki MatsuoNaruyasu OkamotoKenichiro OkaTakeyuki Kondo
    • Masayuki KamikawaToshiaki MatsuoNaruyasu OkamotoKenichiro OkaTakeyuki Kondo
    • C08G63/08B01D53/00B01J19/18
    • C08G63/785B01J4/002B01J19/24B01J2219/00006B01J2219/00777B01J2219/185C08G63/06Y02P20/582
    • An equipment for producing polyhydroxycarboxylic acid, includes a ring-opening polymerization apparatus, a liquid phase devolatilizing apparatus, and a drying apparatus, wherein an indirect heat exchanger is connected to a vent gas discharge path of the liquid phase devolatilizing apparatus. The indirect heat exchanger captures a dispersed in-process substance containing hydroxycarboxylic acid cyclic dimers and transfers the substance to the ring-opening polymerization apparatus; a wet condenser and a hot well are connected to a vent gas discharge path of the indirect heat exchanger and that of the drying apparatus, respectively. The wet condenser captures a dispersed in process substance containing the cyclic dimers with the use of a refrigerant containing hydroxycarboxylic acid corresponding to the cyclic dimers and transfers the substance to the hot well; the hot well causes hydrolysis of the cyclic dimers for generation of hydroxycarboxylic acid; the generated hydroxycarboxylic acid is mixed with a refrigerant and the mixture is circulated to the wet condenser; and hydroxycarboxylic acid is highly concentrated via circulation between the wet condenser and the hot well and then discharged.
    • 用于制备聚羟基羧酸的设备包括开环聚合设备,液相脱挥发酵设备和干燥设备,其中间接热交换器连接到液相脱挥发设备的通气气体排放路径。 间接热交换器捕获含有羟基羧酸环二聚体的分散的在线物质并将物质转移到开环聚合装置中; 湿式冷凝器和热井分别连接到间接热交换器和干燥装置的排放气体排出路径。 湿式冷凝器使用含有对应于环状二聚体的羟基羧酸的制冷剂捕获含有环状二聚体的分散过程物质,并将物质转移到热井中; 热阱引起环状二聚体的水解产生羟基羧酸; 将所生成的羟基羧酸与制冷剂混合,并将混合物循环至湿式冷凝器; 并且羟基羧酸通过湿式冷凝器和热井之间的循环高度浓缩,然后排出。
    • 4. 发明授权
    • Device and method for producing polybutylene succinate
    • 聚丁二酸丁二醇酯的制备方法
    • US08604156B2
    • 2013-12-10
    • US13503078
    • 2010-10-21
    • Masayuki KamikawaToshiaki MatsuoKenichiro OkaTakeyuki KondoYasunari SaseMasashi Tanto
    • Masayuki KamikawaToshiaki MatsuoKenichiro OkaTakeyuki KondoYasunari SaseMasashi Tanto
    • C08G63/02
    • C08G63/785B01J19/1862B01J19/20B01J2219/00006B01J2219/00083C08G63/16
    • A device and a method for producing high-quality polybutylene succinate are provided. The method for producing polybutylene succinate comprises the steps of: preparing a raw-material slurry by mixing succinic acid or a derivative thereof with 1,4-butanediol in a raw-material slurry preparation tank; storing the raw-material slurry in a raw-material slurry storage tank while maintaining flowability; carrying out an esterification reaction of the raw-material slurry in an esterification reactor; and synthesizing polybutylene succinate with a polycondensation reaction of the ester in a polycondensation reactor, in which the polycondensation reactor is divided, from the upstream side, into at least an initial polycondensation reactor, an intermediate polycondensation reactor, and a final polycondensation reactor, a catalyst is added in an amount from 1000 ppm to 3000 ppm in relation to succinic acid or a derivative thereof, the reaction time in the intermediate polycondensation reactor ranges from 0.25 hours to 0.75 hours, and the reaction temperature in the final polycondensation reactor ranges from 245° C. to 255° C.
    • 提供了一种用于生产高品质聚丁二酸丁二醇酯的装置和方法。 聚丁二酸丁二醇酯的制造方法包括以下步骤:通过在原料浆料制备槽中混合琥珀酸或其衍生物与1,4-丁二醇来制备原料浆料; 将原料浆料储存在原料浆料储罐中同时保持流动性; 在酯化反应器中进行原料浆料的酯化反应; 并将聚缩丁醛琥珀酸酯与缩聚反应器中的缩聚反应器在上游侧分离成至少初始缩聚反应器,中间缩聚反应器和最终缩聚反应器中的催化剂进行缩聚反应, 相对于琥珀酸或其衍生物以1000ppm至3000ppm的量加入,中间缩聚反应器中的反应时间为0.25小时至0.75小时,最终缩聚反应器中的反应温度为245℃ C.至255°C
    • 7. 发明申请
    • PROCESS AND SYSTEM FOR PURIFICATION OF TETRAHYDROFURAN
    • 四氢呋喃的净化方法和系统
    • US20120215012A1
    • 2012-08-23
    • US13505022
    • 2009-10-30
    • Toshiaki MatsuoKenichiro OkaMasayuki KamikawaTakeyuki KondoHiroyuki ItoYasunari SaseChiaki WatanabeTetsuji Harigai
    • Toshiaki MatsuoKenichiro OkaMasayuki KamikawaTakeyuki KondoHiroyuki ItoYasunari SaseChiaki WatanabeTetsuji Harigai
    • C07D307/08B01D3/14
    • C07D307/08C07B63/00
    • A method for purifying tetrahydrofuran from a liquid containing tetrahydrofuran and as impurities at least water, 2,5-dihydrofuran and butanol, the method comprising: a first distillation step in which the liquid is subjected to distillation using a distillation column to separate into a first bottoms product containing water as a major component and a first distillate containing tetrahydrofuran, 2,5-dihydrofuran and butanol as major components, a second distillation step in which the first distillate is subjected to distillation using a distillation column to separate into a second bottoms product containing tetrahydrofuran and butanol as major components and a second distillate containing 2,5-dihydrofuran as a major component, a third distillation step in which the second bottoms product is subjected to distillation using a distillation column to separate into a third bottoms product containing butanol as a major component and a third distillate containing tetrahydrofuran as a major component, and further comprising a recirculation step in which a part of the second top liquid is recirculated into the first distillation step as a recirculation liquid and the remaining part is discharged into the outside of the system.
    • 一种从含有四氢呋喃的液体中提取四氢呋喃的方法,至少是水,2,5-二氢呋喃和丁醇作为杂质,该方法包括:第一蒸馏步骤,其中使用蒸馏塔对液体进行蒸馏以分离成第一 含有水作为主要组分的底部产物和含有四氢呋喃,2,5-二氢呋喃和丁醇作为主要组分的第一馏出物,第二蒸馏步骤,其中第一馏出物使用蒸馏塔进行蒸馏以分离成第二塔底产物 含有四氢呋喃和丁醇作为主要组分的第二馏出物和含有2,5-二氢呋喃作为主要组分的第二馏出物,第三蒸馏步骤,其中使用蒸馏塔对第二塔底产物进行蒸馏以分离成含有丁醇的第三底部产物 主要组分和第三馏出物,其中四氢呋喃为主要成分 并且还包括再循环步骤,其中所述第二顶部液体的一部分作为再循环液体再循环到所述第一蒸馏步骤中,并且所述剩余部分被排出到所述系统的外部。
    • 9. 发明授权
    • Reaction process utilizing critical water
    • 使用临界水的反应过程
    • US08558035B2
    • 2013-10-15
    • US13148760
    • 2010-02-05
    • Takeyuki KondoHiroyuki ItoNaruyasu OkamotoYasunari SaseToshiaki MatsuoKenichiro OkaMasayuki Kamikawa
    • Takeyuki KondoHiroyuki ItoNaruyasu OkamotoYasunari SaseToshiaki MatsuoKenichiro OkaMasayuki Kamikawa
    • C07C45/52B01J19/00
    • B01J3/008B01J2219/00006B01J2219/00168C07C45/52Y02P20/544C07C47/22
    • In order to perform organic synthesis process through action with supercritical water and acid stably while suppressing a trouble caused by a by-product, a method and an apparatus are provided, including the following steps. Water is supplied to high-pressure pumps (110) and (210) from water headers (101) and (201), and a pressure-reducing valve (324) is regulated to increase the pressure to 35 MPa. Temperatures of preheaters (120) and (220) and a heater (310) are increased until the reaction solution is at a temperature of 400° C. Acid (sulfuric acid) and an organic compound raw material (glycerin) are supplied from an acid header (203) and a raw-material header (203′) for action with the supercritical water to obtain a reaction solution. The obtained reaction solution is cooled to 100 to 200° C. by first cooling (420) and a solid component included in the reaction solution is separated for removal from the reaction solution by a filter (320), and then the reaction solution is cooled to a temperature of about 100° C. or lower by second cooling (620) and pressure thereof is reduced (324). Further, the reaction solution is cooled by third cooling (720) and then a synthesized product (acrolein) is captured.
    • 为了通过超临界水和酸稳定地进行有机合成工艺,同时抑制由副产物引起的故障,提供了包括以下步骤的方法和装置。 从集水管(101)和(201)向高压泵(110)和(210)供水,调节减压阀(324)以将压力增加至35MPa。 增加预热器(120)和(220)和加热器(310)的温度,直到反应溶液处于400℃的温度。酸(硫酸)和有机化合物原料(甘油)由酸 标题(203)和原料头(203'),用于与超临界水作用以获得反应溶液。 将得到的反应溶液通过第一次冷却(420)冷却至100〜200℃,分离包含在反应溶液中的固体成分,通过过滤器(320)从反应溶液中除去,然后将反应溶液冷却 通过第二冷却(620)至约100℃或更低的温度,并且其压力降低(324)。 此外,将反应溶液通过第三次冷却(720)冷却,然后捕获合成产物(丙烯醛)。
    • 10. 发明申请
    • EQUIPMENT AND METHOD FOR PRODUCING POLYHYDROXYCARBOXYLIC ACID
    • 用于生产聚羟基羧酸的设备和方法
    • US20100076165A1
    • 2010-03-25
    • US12544477
    • 2009-08-20
    • Masayuki KAMIKAWAToshiaki MatsuoNaruyasu OkamotoKenichiro OkaTakeyuki Kondo
    • Masayuki KAMIKAWAToshiaki MatsuoNaruyasu OkamotoKenichiro OkaTakeyuki Kondo
    • C08G63/08C08G85/00B01J19/00
    • C08G63/785B01J4/002B01J19/24B01J2219/00006B01J2219/00777B01J2219/185C08G63/06Y02P20/582
    • This invention provides an equipment and a method for producing polyhydroxycarboxylic acid whereby the yield of a starting material in the process can be improved.An equipment for producing polyhydroxycarboxylic acid, comprising a ring-opening polymerization apparatus, a liquid phase devolatilizing apparatus, and a drying apparatus, wherein: an indirect heat exchanger is connected to a vent gas discharge path of the liquid phase devolatilizing apparatus; the indirect heat exchanger captures a dispersed in-process substance containing hydroxycarboxylic acid cyclic dimers and transfers the substance to the ring-opening polymerization apparatus; a wet condenser and a hot well are connected to a vent gas discharge path of the indirect heat exchanger and that of the drying apparatus, respectively; the wet condenser captures a dispersed in process substance containing the cyclic dimers with the use of a refrigerant containing hydroxycarboxylic acid corresponding to the cyclic dimers and transfers the substance to the hot well; the hot well causes hydrolysis of the cyclic dimers for generation of hydroxycarboxylic acid; the generated hydroxycarboxylic acid is mixed with a refrigerant and the mixture is circulated to the wet condenser; and hydroxycarboxylic acid is highly concentrated via circulation between the wet condenser and the hot well and then discharged, is provided.
    • 本发明提供一种生产聚羟基羧酸的设备和方法,从而可以提高该方法中原料的产率。 一种生产聚羟基羧酸的设备,包括开环聚合设备,液相脱挥发酵设备和干燥设备,其中:间接热交换器连接到液相脱挥发设备的排放气体排放路径; 间接热交换器捕获含有羟基羧酸环状二聚体的分散的在线物质并将物质转移到开环聚合装置中; 湿式冷凝器和热井分别连接到间接热交换器和干燥装置的排放气体排放路径; 湿式冷凝器使用含有对应于环状二聚体的羟基羧酸的制冷剂捕获含有环状二聚体的分散过程物质,并将物质转移到热井中; 热阱引起环状二聚体的水解产生羟基羧酸; 将所生成的羟基羧酸与制冷剂混合,并将混合物循环至湿式冷凝器; 羟基羧酸通过湿式冷凝器和热水槽之间的循环高度浓缩,然后排出。