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    • 1. 发明授权
    • Method of producing naphthalenedicarboxylic acid
    • 生产萘二甲酸的方法
    • US06268528B1
    • 2001-07-31
    • US09432783
    • 1999-11-03
    • Hiroshi MachidaFumiya ZaimaMasato InariHiroshi WatanabeEmiko Yokose
    • Hiroshi MachidaFumiya ZaimaMasato InariHiroshi WatanabeEmiko Yokose
    • C07C5116
    • C07C51/265C07C63/38
    • Dialkylnaphthalene is oxidized to naphthalenedicarboxylic acid in a lower aliphatic carboxylic acid solvent in the presence of a catalyst comprising a cobalt compound, a manganese compound and a bromine compound having an atomic ratio of manganese to cobalt of 0.03 to 0.5. The catalyst is supplied to the oxidation reaction zone so that the total amount of cobalt and manganese is 0.025 to 0.1 gram atom based on 1 gram mol of the dialkylnaphthalene. An oxidation product slurry is subjected to solid-liquid separation when the concentration of the naphthalenedicarboxylic acid in the slurry is 8 to 30% by weight. The process prevents the by-production of benzotricarboxylic acid such as trimellitic acid, thereby drastically reducing the incorporation of heavy metal complexes with trimellitic acid into naphthalenedicarboxylic acid crystals. The process optionally includes the addition of a polymer flocculant, this forming crystal aggregates with a large particle size and facilitating the separation of the crystals from the mother liquor.
    • 在包含钴化合物,锰化合物和原子比为锰与钴的溴化合物的催化剂存在下,在低级脂族羧酸溶剂中将二烷基萘氧化成萘二羧酸为0.03〜0.5。 将催化剂供应到氧化反应区,使得钴和锰的总量基于1克摩尔的二烷基萘为0.025至0.1克原子。 当浆料中萘二甲酸的浓度为8〜30重量%时,氧化产物浆液进行固液分离。 该方法防止苯三甲酸如偏苯三酸的副产物,从而大大降低了与偏苯三酸的重金属络合物与萘二甲酸晶体的结合。 该方法任选地包括加入聚合物絮凝剂,这种形成晶体具有大粒径的聚集体并且有利于晶体与母液的分离。
    • 2. 发明授权
    • Process for producing a hydrogenation product of an aromatic carboxylic acid
    • 制备芳族羧酸的氢化产物的方法
    • US06541662B2
    • 2003-04-01
    • US10021430
    • 2001-12-19
    • Hiroshi MachidaKo KedoFumiya Zaima
    • Hiroshi MachidaKo KedoFumiya Zaima
    • C07C6109
    • C07C51/36C07C61/12C07C61/125C07C61/09
    • A process for producing a hydrogenation product of aromatic carboxylic acid which comprises continuously producing the hydrogenation product of aromatic carboxylic acid by hydrogenating an aromatic carboxylic acid having a melting point of 250° C. or higher in a solvent in the presence of a solid catalyst, wherein the hydrogenation is conducted in a condition such that substantially the entire amount of the aromatic carboxylic acid of a raw material is dissolved in the solvent by recycling a portion of a reaction liquid taken out of a reactor into the reactor. An aromatic carboxylic acid having a high melting point and hardly soluble in solvents can be hydrogenated at a suitable reaction temperature in accordance with a continuous process without using a great amount of a solvent and the reaction product of the object compound can be produced very efficiently.
    • 一种芳族羧酸的氢化产物的制造方法,其特征在于,在固体催化剂存在下,通过在溶剂中氢化熔点为250℃以上的芳香族羧酸,连续制造芳香族羧酸的氢化物, 其特征在于,氢化反应是将从反应器中取出的反应液的一部分再循环到反应器中,将原料的芳香族羧酸的总量全部溶解在溶剂中的方式进行。 可以在不使用大量溶剂的情况下,根据连续方法在合适的反应温度下氢化不溶于溶剂的高熔点,并且可以非常有效地制备目标化合物的反应产物。
    • 3. 发明授权
    • Processes for the production of high-purity dimethyl 2,
6-naphthalenedicarboxylate and naphthalenedicarboxylic acid
    • 制备高纯度2,6-二甲酸二甲酯和萘二甲酸二甲酯的方法
    • US6013831A
    • 2000-01-11
    • US69815
    • 1998-04-30
    • Hiroshi MachidaFumiya ZaimaKengi NakayaKazuo Tanaka
    • Hiroshi MachidaFumiya ZaimaKengi NakayaKazuo Tanaka
    • C07C51/265C07C67/08C07C67/52C07C67/48
    • C07C67/08C07C51/265C07C67/52
    • A process for the production of high-purity dimethyl 2,6-naphthalenedicarboxylate, which comprises esterifying 2,6-naphthalenedicarboxylic acid obtained by liquid phase oxidation of 2,6-dialkylnaphthalene with molecular oxygen in the presence of an oxidation catalyst, with methanol and then purifying a crude ester formed by the esterification, the crude ester being purified in the presence of an aromatic hydrocarbon as a solvent, in which impurities contained in a reaction product obtained by the esterification of 2,6-naphthalenedicarboxylic acid prepared by the liquid phase oxidation of 2,6-dialkylnaphthalene are effectively removed with simple procedures, oxidation catalyst metals are recovered, a crystal of naphthalenedicarboxylic acid formed by the oxidation of dialkylnaphthalene and/or its oxide derivative can be easily separated, and the oxidation catalyst to be brought into the step of producing dimethyl naphthalenedicarboxylate is recovered in the process of the production of naphthalenedicarboxylic acid and effectively used in the process of the production of naphthalenedicarboxylic acid.
    • 一种制备高纯度2,6-萘二甲酸二甲酯的方法,其包括在氧化催化剂存在下,通过用分子氧将2,6-二烷基萘液相氧化得到的2,6-萘二羧酸与甲醇和 然后纯化通过酯化形成的粗酯,粗酯在作为溶剂的芳族烃存在下纯化,其中通过由液相制备的2,6-萘二甲酸酯化得到的反应产物中所含的杂质 通过简单的方法有效地除去2,6-二烷基萘的氧化,回收氧化催化剂金属,可以容易地分离通过二烷基萘和/或其氧化物衍生物的氧化形成的萘二甲酸的结晶,并将氧化催化剂 在生产n的过程中回收生产二甲基萘二甲酸二甲酯的步骤 邻苯二甲酸二羧酸,有效用于生产萘二羧酸的方法。
    • 4. 发明授权
    • Process for producing a high purity aromatic polycarboxylic acid
    • 高纯度芳族多元羧酸的制备方法
    • US07547803B2
    • 2009-06-16
    • US10861497
    • 2004-06-07
    • Shinichi NagaoMasato InariJitsuo OishiKenji NakayaHiroshi Machida
    • Shinichi NagaoMasato InariJitsuo OishiKenji NakayaHiroshi Machida
    • C07C51/42
    • C07C51/43C07C51/487C07C63/333C07C63/38
    • A process for producing a high purity aromatic polycarboxylic acid (APA) by purification of a crude APA comprises: (I) aging a slurry of the crude APA in a first dispersion medium at 180 to 300° C. for 10 minutes or longer under stirring; (II) introducing the aged slurry of the APA into a column for substituting dispersion media, bringing the slurry into contact with a second dispersion medium and separating the resultant fluid into a fluid of the first dispersion medium containing impurities and a slurry of the second dispersion medium containing crystals of the high purity APA; and (III) separating the crystals of the high purity APA from the slurry of the second dispersion medium. A high purity APA having excellent hue and particle diameter can be industrially advantageously produced while the construction of the process is simplified and the consumption of energy is decreased.
    • 通过粗制APA的纯化生产高纯度芳族多元羧酸(APA)的方法包括:(I)在搅拌下将第一分散介质中粗APA的浆料在180-300℃下老化10分钟或更长时间 ; (II)将APA的老化浆液引入用于代替分散介质的塔中,使浆料与第二分散介质接触,并将所得流体分离成含有杂质的第一分散介质的流体和第二分散体的浆料 含有高纯度APA晶体的介质; 和(III)将高纯度APA的晶体与第二分散介质的浆料分离。 具有优异的色相和粒径的高纯度APA可以在工业上有利地产生,同时简化了工艺的构造并降低了能量的消耗。
    • 5. 发明授权
    • Process for producing 2,6-naphthalenedicarboxylic acid
    • 2,6-萘二甲酸的制备方法
    • US6018077A
    • 2000-01-25
    • US48494
    • 1998-03-26
    • Fumio OhkoshiHiroshi OgawaKazuo TanakaMasato InariHiroshi Machida
    • Fumio OhkoshiHiroshi OgawaKazuo TanakaMasato InariHiroshi Machida
    • C07C51/265C07C51/16
    • C07C51/265
    • A process for producing 2,6-naphthalenedicarboxylic acid comprising oxidizing 2,6-dimethylnaphthalene with a gas containing oxygen in a solvent comprising a lower aliphatic carboxylic acid in the presence of a catalyst comprising cobalt, manganese, and bromine, wherein the total amount of cobalt and manganese in the catalyst is 50 to 300 mg atom per 1 g mol of 2,6-dimethylnaphthalene, a ratio by g atom of manganese to cobalt in the catalyst is 20:1 to 4:1, and the oxidation is conducted at a temperature of 200 to 250.degree. C.; and a process as described above, wherein a mother liquor which is obtained from a slurry of a product of the oxidation via a step of solid-liquid separation is recyled to a step of oxidation after heat treatment at a temperature of 150.degree. C. or higher. In accordance with the processes, accumulation of substances which affect the oxidation adversely is prevented. Moreover, a large fraction of a mother liquor of oxidation can be recycled without decrease in the yield of the reaction, and the catalyst components and the solvent components in the mother liquor of oxidation can be utilized efficiently.
    • 一种2,6-萘二甲酸的制造方法,其特征在于,在包含钴,锰,溴的催化剂的存在下,在含有低级脂肪族羧酸的溶剂中,在含有氧的气体中,使2,6-二甲基萘氧化, 催化剂中的钴和锰在每1克摩尔2,6-二甲基萘中为50〜300mg原子,催化剂中锰与钴的原子比为20:1〜4:1,氧化反应在 温度为200〜250℃。 和如上所述的方法,其中将通过固液分离步骤的氧化产物的浆料获得的母液在150℃的温度下再热处理至氧化步骤,或 更高。 根据这些方法,可以防止影响氧化的物质的积累。 此外,大部分的氧化母液可以循环使用而不会降低反应的产率,并且可有效地利用氧化母液中的催化剂组分和溶剂组分。
    • 6. 发明授权
    • Method for producing high purity terephthalic acid
    • 生产高纯对苯二甲酸的方法
    • US07262323B2
    • 2007-08-28
    • US10574273
    • 2004-09-30
    • Hideaki FujitaHiroshi MachidaNobuo NamikiYoshio Waguri
    • Hideaki FujitaHiroshi MachidaNobuo NamikiYoshio Waguri
    • C07C51/16C07C17/093A61L9/00
    • C07C51/47C07C51/487Y02P20/52C07C63/26
    • A method for producing high purity terephthalic acid wherein a slurry having an acetic acid solvent and, dispersed therein, crude terephthalic acid crystals which has been prepared by subjecting a p-alkyl benzene to a liquid phase oxidation in a solvent of acetic acid is continuously converted to a water slurry by the mother liquid exchange, and then the resultant water slurry is subjected to a hydrogenation treatment, which comprises introducing the above acetic acid slurry to a tower having a center axis having a plurality of agitating blades at the top thereof, to form a region having a high concentration of terephthalic acid crystals in the tower through the sedimentation of the terephthalic acid crystals, supplying the water for substitution to the bottom of the tower in such a manner to form an upward water flow while generating a revolving flow of the high concentration region by the rotation of the agitation blade, to thereby subject said terephthalic acid crystals and said upward water flow to a counter-flow contact, and taking out the acetic acid from a portion being upper than the supply port for the acetic acid slurry while withdrawing the terephthalic acid crystals having contacted with the upward water flow together with the water for substitution from the tower bottom. The above method allows the substitution of the acetic acid solvent of the acetic acid slurry with water, with a high substitution percentage.
    • 一种生产高纯度对苯二甲酸的方法,其中将具有乙酸溶剂和分散在其中的粗对苯二甲酸晶体的浆料在乙酸的溶剂中经由对烷基苯进行液相氧化而制备, 通过母液交换到水浆中,然后对所得水浆进行氢化处理,其包括将上述乙酸浆料引入到其顶部具有多个搅拌叶片的中心轴的塔上,至 通过对苯二甲酸晶体的沉降在塔中形成具有高浓度对苯二甲酸晶体的区域,将水替代为塔的底部,以形成向上的水流,同时产生 通过搅拌叶片的旋转而产生高浓度区域,从而使所述对苯二甲酸晶体和所述上部流动 ard水流动到逆流接触,并从乙酸浆料供应口上方的一部分取出乙酸,同时将与向上的水接触的对苯二甲酸晶体与水一起取出,以供替代 塔底。 上述方法允许乙酸溶剂的乙酸溶液用水替代,取代率高。