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    • 1. 发明申请
    • PROCESS FOR PRODUCTION OF CYCLOOLEFIN
    • 生产环烯醇的方法
    • US20090048425A1
    • 2009-02-19
    • US11912575
    • 2006-08-18
    • Mitsuo KonishiTeruhiko Inoue
    • Mitsuo KonishiTeruhiko Inoue
    • C08G61/10
    • B01J23/46B01J23/60B01J23/96B01J27/053B01J38/64C07C5/11C07C2523/46C07C2527/053C07C2601/16Y02P20/584
    • According to the present invention, when cycloolefins are produced by partially hydrogenating a monocyclic aromatic hydrocarbon with hydrogen in the presence of a ruthenium catalyst, water, and a metal sulfate, the decrease in catalytic activity and cycloolefin selectivity is suppressed by reducing the concentration of chloride ions dissolved in the water in which the catalyst is present to 300 wt ppm or less and regenerating a part or all of the catalyst for reuse. Zinc sulfate is preferably used as the metal sulfate. Further, the raw materials and catalyst to be supplied to the reaction preferably have a reduced chloride ion content. This method can suppress the decrease in long-term catalytic activity and cycloolefin selectivity. Furthermore, the catalytic activity and cycloolefin selectivity after catalyst regeneration can be maintained at a high level. As a result, cycloolefins can be efficiently produced for a long period of time.
    • 根据本发明,当在钌催化剂,水和金属硫酸盐的存在下,通过氢气使单环芳族烃部分氢化制备环烯烃时,通过降低氯化物的浓度来抑制催化活性和环烯选择性的降低 溶解在其中存在催化剂的水中的离子为300重量ppm以下,再生部分或全部催化剂用于再利用。 硫酸锌优选用作金属硫酸盐。 此外,供给反应的原料和催化剂优选具有减少的氯离子含量。 该方法可以抑制长期催化活性和环烯烃选择性的降低。 此外,催化剂再生后的催化活性和环烯选择性可以保持在高水平。 因此,可以长时间有效地制造环烯烃。
    • 2. 发明授权
    • Process for production of cycloolefin
    • 环烯生产工艺
    • US07947859B2
    • 2011-05-24
    • US11912575
    • 2006-08-18
    • Mitsuo KonishiTeruhiko Inoue
    • Mitsuo KonishiTeruhiko Inoue
    • C07C5/11C07C5/10
    • B01J23/46B01J23/60B01J23/96B01J27/053B01J38/64C07C5/11C07C2523/46C07C2527/053C07C2601/16Y02P20/584
    • According to the present invention, when cycloolefins are produced by partially hydrogenating a monocyclic aromatic hydrocarbon with hydrogen in the presence of a ruthenium catalyst, water, and a metal sulfate, the decrease in catalytic activity and cycloolefin selectivity is suppressed by reducing the concentration of chloride ions dissolved in the water in which the catalyst is present to 300 wt ppm or less and regenerating a part or all of the catalyst for reuse. Zinc sulfate is preferably used as the metal sulfate. Further, the raw materials and catalyst to be supplied to the reaction preferably have a reduced chloride ion content. This method can suppress the decrease in long-term catalytic activity and cycloolefin selectivity. Furthermore, the catalytic activity and cycloolefin selectivity after catalyst regeneration can be maintained at a high level. As a result, cycloolefins can be efficiently produced for a long period of time.
    • 根据本发明,当在钌催化剂,水和金属硫酸盐的存在下,通过氢气使单环芳族烃部分氢化制备环烯烃时,通过降低氯化物的浓度来抑制催化活性和环烯选择性的降低 溶解在其中存在催化剂的水中的离子为300重量ppm以下,再生部分或全部催化剂用于再利用。 硫酸锌优选用作金属硫酸盐。 此外,供给反应的原料和催化剂优选具有减少的氯离子含量。 该方法可以抑制长期催化活性和环烯烃选择性的降低。 此外,催化剂再生后的催化活性和环烯选择性可以保持在高水平。 因此,可以长时间有效地制造环烯烃。
    • 5. 发明申请
    • METHOD FOR PRODUCING CYCLOOLEFIN AND PRODUCTION APPARATUS THEREOF
    • 生产环烯烃的方法及其生产装置
    • US20110130600A1
    • 2011-06-02
    • US13055103
    • 2009-06-12
    • Mitsuo Konishi
    • Mitsuo Konishi
    • C07C5/11B01J8/00
    • C07C5/11B01J23/462B01J23/96B01J38/70C07C2523/46Y02P20/584
    • There is provided a method for producing cycloolefin where the nickel which elutes in the liquid-contact portion of the reactor is removed from the reaction system of the partial hydrogenation reaction and cycloolefin can be stably produced from a monocyclic aromatic hydrocarbon over a long term. A method for producing a cycloolefin by a partial hydrogenation reaction of a monocyclic aromatic hydrocarbon in an aqueous phase, which contains a metal salt-containing acidic aqueous solution and a ruthenium catalyst in a reactor with a liquid-contact portion formed of a nickel-containing material, the method comprising a first step of bringing at least a part of the ruthenium catalyst contained in the aqueous phase into contact with oxygen, a second step of separating the aqueous phase containing the ruthenium catalyst that has been processed in the first step into a first phase containing the ruthenium catalyst at a high ratio and a second phase containing the ruthenium catalyst at a lower ratio than the first phase, and a third step of feeding the first phase to a reaction system of a partial hydrogenation reaction.
    • 提供一种生产环烯烃的方法,其中在反应器的液体接触部分中洗脱的镍从部分氢化反应的反应体系中除去和环烯烃可以从单环芳烃长期稳定地制备。 通过在含有含金属盐的酸性水溶液和钌催化剂的水相中的单环芳烃的部分氢化反应制备环烯烃的方法,所述反应器中的液体接触部分由含镍的 材料,所述方法包括使含有水相中的钌催化剂的至少一部分与氧接触的第一步骤,将在第一步骤中处理的含有钌催化剂的水相分离成第一步骤, 第一阶段以高比例含有钌催化剂,第二相含有比第一相低的钌催化剂,第三步是将第一相进料到部分氢化反应的反应体系中。
    • 7. 发明授权
    • Aromatic copolymer and composition containing the same
    • 芳族共聚物和含有它们的组合物
    • US06323300B1
    • 2001-11-27
    • US09308589
    • 1999-05-21
    • Kohei KitaTsuneaki TanabeMitsuo Konishi
    • Kohei KitaTsuneaki TanabeMitsuo Konishi
    • C08G6514
    • C08G65/44Y10T428/31551
    • Disclosed is an aromatic copolymer comprising a plurality of aromatic copolymer chains, each comprising (A) recurring 2,6-diphenylphenol units and (B) phenolic comonomer units, each comonomer unit being independently selected from the group consisting of (i) an oxyphenylene monomer unit which is monosubstituted with a monovalent aromatic group or a halogen atom, (ii) an &agr;-oxynaphthylene monomer unit, (iii) a &bgr;-oxynaphthylene monomer unit, and (iv) an oxyphenylene monomer unit which is substituted with at least one aliphatic group, wherein the amounts of (A) and (B) are from 50 to 98% by weight and from 2 to 50% by weight, based on the weight of the aromatic copolymer, provided that, when (iv) is present as the comonomer unit, the amount of (iv) is 20% by weight or less, based on the weight of (B), and wherein the aromatic copolymer has a weight average molecular weight of from 1,000 to 3,000,000. A method for producing the aromatic copolymer is also disclosed. The aromatic copolymer of the present invention has excellent electrical characteristics (such as a low dielectric constant), an excellent heat resistance, excellent film-forming properties, low water absorption properties and an excellent adhesion to other materials, and can be advantageously used as a material for various electronic parts.
    • 公开了包含多个芳族共聚物链的芳族共聚物,每个芳族共聚物链包含(A)重复的2,6-二苯基苯酚单元和(B)酚类共聚单体单元,每个共聚单体单元独立地选自(i)氧联苯单体 被单价芳族基团或卤素原子单取代的单元,(ii)α-氧基萘基单体单元,(iii)β-氧基萘基单体单元,和(iv)被至少一个脂族基团取代的氧亚苯基单体单元 基团,其中基于芳族共聚物的重量,(A)和(B)的量为50至98重量%和2至50重量%,条件是当(iv)作为 共聚单体单元,基于(B)的重量,(iv)的量为20重量%以下,并且其中所述芳族共聚物的重均分子量为1,000〜3,000,000。 还公开了制备芳族共聚物的方法。 本发明的芳香族共聚物具有优异的电特性(例如低介电常数),优异的耐热性,优异的成膜性,低吸水性和与其它材料的优异粘附性,并且可以有利地用作 各种电子零件的材料。
    • 9. 发明授权
    • Method for producing cycloolefin and production apparatus thereof
    • 环烯烃的制造方法及其制造装置
    • US09174894B2
    • 2015-11-03
    • US13055103
    • 2009-06-12
    • Mitsuo Konishi
    • Mitsuo Konishi
    • C07C5/11B01J8/00B01J23/96B01J38/70B01J23/46
    • C07C5/11B01J23/462B01J23/96B01J38/70C07C2523/46Y02P20/584
    • There is provided a method for producing cycloolefin where the nickel which elutes in the liquid-contact portion of the reactor is removed from the reaction system of the partial hydrogenation reaction and cycloolefin can be stably produced from a monocyclic aromatic hydrocarbon over a long term. A method for producing a cycloolefin by a partial hydrogenation reaction of a monocyclic aromatic hydrocarbon in an aqueous phase, which contains a metal salt-containing acidic aqueous solution and a ruthenium catalyst in a reactor with a liquid-contact portion formed of a nickel-containing material, the method comprising a first step of bringing at least a part of the ruthenium catalyst contained in the aqueous phase into contact with oxygen, a second step of separating the aqueous phase containing the ruthenium catalyst that has been processed in the first step into a first phase containing the ruthenium catalyst at a high ratio and a second phase containing the ruthenium catalyst at a lower ratio than the first phase, and a third step of feeding the first phase to a reaction system of a partial hydrogenation reaction.
    • 提供一种生产环烯烃的方法,其中在反应器的液体接触部分中洗脱的镍从部分氢化反应的反应体系中除去和环烯烃可以从单环芳烃长期稳定地制备。 通过在含有含金属盐的酸性水溶液和钌催化剂的水相中的单环芳烃的部分氢化反应制备环烯烃的方法,所述反应器中的液体接触部分由含镍的 材料,所述方法包括使含有水相中的钌催化剂的至少一部分与氧接触的第一步骤,将在第一步骤中处理的含有钌催化剂的水相分离成第一步骤, 第一阶段以高比例含有钌催化剂,第二相含有比第一相低的钌催化剂,第三步是将第一相进料到部分氢化反应的反应体系中。
    • 10. 发明授权
    • Process for the preparation of diol mixtures
    • 二醇混合物的制备方法
    • US06706932B1
    • 2004-03-16
    • US10129143
    • 2002-05-02
    • Mitsuo KonishiKoshiro YokotaEizaburou Ueno
    • Mitsuo KonishiKoshiro YokotaEizaburou Ueno
    • C07C2700
    • C07C29/149C07C51/42C07C31/207C07C31/20
    • Disclosed is a method for producing a diol mixture comprising 1,4-butanediol, 1,5-pentanediol and 1,6-hexanediol, which comprises: (A) providing a dicarboxylic acid mixture comprising succinic acid, glutaric acid and adipic acid and having a nitric acid content of 3% by weight or less, based on the total weight of the succinic, glutaric and adipic acids, wherein the dicarboxylic acid mixture is prepared by denitrating an aqueous by-product solution obtained in an adipic acid production process, and (B) subjecting the dicarboxylic acid mixture to hydrogenation in the presence of water, hydrogen gas and a hydrogenation catalyst containing an active metal species comprising ruthenium and tin, to thereby obtain a hydrogenation reaction mixture comprising a diol mixture comprising 1,4-butanediol, 1,5-pentanediol and 1,6-hexanediol.
    • 公开了一种制备包含1,4-丁二醇,1,5-戊二醇和1,6-己二醇的二醇混合物的方法,其包括:(A)提供包含琥珀酸,戊二酸和己二酸的二羧酸混合物,并且具有 基于琥珀酸,戊二酸和己二酸的总重量计,硝酸含量为3重量%以下,其中二羧酸混合物是通过对在己二酸生产过程中获得的副产物溶液进行脱硝制备的, (B)在水,氢气和含有钌和锡的活性金属物质的氢化催化剂的存在下使二羧酸混合物进行氢化,由此得到包含1,4-丁二醇的二醇混合物的氢化反应混合物, 1,5-戊二醇和1,6-己二醇。