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    • 11. 发明授权
    • Method of preparing sodium formyl acetone and 4,4-dimethoxy-2-butanone
    • 制备甲酰基丙酮和4,4-二甲氧基-2-丁酮的方法
    • US5276200A
    • 1994-01-04
    • US961402
    • 1992-10-15
    • Keigo NishihiraShuji TanakaMasahiro Kondo
    • Keigo NishihiraShuji TanakaMasahiro Kondo
    • C07C45/68C07C45/71C07C45/72C07C49/175C07C49/24C07C45/64
    • C07C49/24C07C45/68C07C45/71C07C45/72C07C49/175
    • The present invention provides a method of preparing sodium formyl acetone using acetone, methyl formate and sodium methoxide as raw materials. A mixture consisting of an acetone and a methyl formate is supplied to a methanol solution of sodium methoxide, or an acetone and a methyl formate are separately supplied simultaneously to the methanol solution of sodium methoxide. The resultant mixture is sufficiently stirred over a predetermined period of time so as to carry out the reaction to form sodium formyl acetone. Also provided is a method of preparing 4,4-dimethoxy-2-butanone. In this method, the reaction mixture obtained in the reaction to form sodium formyl acetone is directly charged into a reaction vessel simultaneously with sulfuric acid to neutralize and acetalize sodium formyl acetone contained in the reaction mixture so as to obtain 4,4-dimethoxy-2-butanone.
    • 本发明提供使用丙酮,甲酸甲酯和甲醇钠作为原料制备甲酰基丙酮钠的方法。 将由丙酮和甲酸甲酯组成的混合物供应到甲醇钠的甲醇溶液中,或者丙酮和甲酸甲酯分别同时供应到甲醇钠的甲醇溶液中。 将所得混合物在预定的时间内充分搅拌,以进行反应以形成甲酰基丙酮钠。 还提供了制备4,4-二甲氧基-2-丁酮的方法。 在该方法中,将形成甲酰基丙酮的反应中得到的反应混合物与硫酸同时直接加入到反应容器中,中和反应混合物中所含的甲酰基丙酮缩醛,得到4,4-二甲氧基-2 丁酮。
    • 16. 发明授权
    • Process for continuously producing dimethyl carbonate
    • 连续生产碳酸二甲酯的方法
    • US5534648A
    • 1996-07-09
    • US345568
    • 1994-11-28
    • Keigo NishihiraShinichi YoshidaShuji Tanaka
    • Keigo NishihiraShinichi YoshidaShuji Tanaka
    • C07C68/00C07C69/96
    • C07C68/00
    • A process for producing dimethyl carbonate is carried out by a first step of catalytically reacting carbon monoxide with methyl nitrite to produce dimethyl carbonate; a second step of absorbing dimethyl carbonate contained in a gas fraction withdrawn from the first step by dimethyl oxalate; a third step of regenerating methyl nitrite by contacting nitrogen monoxide contained in a gas fraction withdrawn from the second step with a molecular oxygen-containing gas and methyl alcohol; a fourth step of collecting dimethyl carbonate by distilling a liquid fraction withdrawn from the second step; and a fifth step of producing and recovering methyl nitrite from a purge gas consisting of a minor portion of a gas fraction withdrawn from one of the second step and the third step by bringing the purge gas together with an ammonia-oxidation product gas into contact with methyl alcohol in a methyl nitrite-recovering column, to thereby produce and recover methyl nitrite contained in the recovering column with a high efficiency at a high level of safety.
    • 通过使一氧化碳与亚硝酸甲酯催化反应的第一步骤来制备碳酸二甲酯的方法来制备碳酸二甲酯; 从草酸二甲酯中吸收从第一步骤中排出的气体馏分中所含的碳酸二甲酯的第二步骤; 通过使从第二步骤抽出的气体馏分中含有的一氧化氮与含分子氧的气体和甲醇接触来再生亚硝酸甲酯的第三步骤; 通过蒸馏从第二步骤中抽出的液体馏分收集碳酸二甲酯的第四步骤; 以及第五步骤,通过将吹扫气体与氨氧化产物气体一起与氨氧化产物气体接触而从由第二步骤和第三步骤之一抽出的少部分气体馏分组成的吹扫气体中生产和回收亚硝酸甲酯, 甲基亚硝酸甲酯回收塔中,从而以高效率高度安全地产生和回收回收塔中所含的亚硝酸甲酯。
    • 19. 发明授权
    • Process for producing alkyl nitrite
    • 亚硝酸烷基酯的制备方法
    • US06191302B1
    • 2001-02-20
    • US09176372
    • 1998-10-21
    • Keigo NishihiraShuji TanakaShinichi Yoshida
    • Keigo NishihiraShuji TanakaShinichi Yoshida
    • C07C20302
    • C07C201/04C07C203/00
    • An alkyl nitrite can be produced on an industrial scale with a high efficiency and with a low yield of by-products by the process wherein nitrogen oxide-containing feed gas is brought into an alkyl alcohol liquid in a distillation column reactor while circulating a liquid fraction, produced in the reactor and containing the alkyl alcohol, through a circulation path including a lower section of the reactor and a cooler to remove the reaction heat vigorously generated in the reactor, and while controlling the weight ratio of the circulating liquid fraction to the total alkyl alcohol fed into the reactor to 50:1 to 200:1, the molar ratio of the total alkyl alcohol fed to the reactor and contained in the circulating liquid fraction to nitrogen oxide in the feed gas to 20:1 to 150:1, and the content of the alkyl alcohol in the liquid fraction to 15 to 60% by weight; and the resultant gas fraction containing the target alkyl nitrite is collected from the reactor.
    • 亚硝酸烷基酯可以在工业规模上以高效率和低产率的副产物生产,其中将含氮氧化物的进料气体在蒸馏塔反应器中进入烷基醇液体,同时使液体馏分 在反应器中生产并含有烷基醇,通过包括反应器的下部的循环路径和冷却器,以除去在反应器中剧烈产生的反应热,同时控制循环液体馏分与总的重量比 将进料到反应器中的烷基醇的摩尔比为50:1至200:1,进料到反应器中并且包含在循环液体馏分中的总烷基醇与进料气体中的氮氧化物的摩尔比为20:1-150:1, 并且液体馏分中的烷基醇的含量为15〜60重量% 从反应器收集含有目标亚硝酸烷基酯的所得气体馏分。