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    • 1. 发明授权
    • Process for producing polycarbonate
    • 生产聚碳酸酯的方法
    • US06740729B1
    • 2004-05-25
    • US09674725
    • 1998-06-06
    • Shuji TanakaShinichi YoshidaTamiko Nishihira
    • Shuji TanakaShinichi YoshidaTamiko Nishihira
    • C08G6400
    • C08G64/307C07C68/00C07C69/96
    • A process for preparing polycarbonate is composed of the steps of transesterifying a dialkyl oxalate and a phenolic compound to give a diaryl oxalate; decarbonylating the diaryl oxalate to give a diaryl carbonate; reacting the diaryl carbonate with a polyvalent hydroxyl compound in the presence of a catalyst containing an amine compound or an ammonium compound to give the polycarbonate, removing a phenolic by-product/amine by-product mixture; collecting the mixture; purifying the mixture so that the amount of the amine by-product in the mixture is reduced to give a phenolic by-product mixture not containing the amine by-product in an amount of more than 600 ppm; and, utilizing thus purified phenolic mixture as a whole or a part of the phenolic compound in the first step.
    • 制备聚碳酸酯的方法由将草酸二烷基酯和酚类化合物酯交换得到草酸二芳基酯的步骤组成; 使草酸二芳基酯脱碳,得到碳酸二芳基酯; 在含有胺化合物或铵化合物的催化剂存在下使碳酸二芳酯与多价羟基化合物反应,得到聚碳酸酯,除去酚类副产物/胺副产物混合物; 收集混合物; 纯化混合物,使得混合物中的副产物的量减少,得到不含胺副产物的酚类副产物混合物的量大于600ppm; 并且在第一步中利用这样纯化的酚类混合物作为整体或一部分酚类化合物。
    • 2. 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methyl nitrite to produce dimethyl carbonate; a second step of absorbing dimethyl carbonate contained in a gas fraction withdrawn from the first step by dimethyl oxalate; a third step of regenerating methyl nitrite by contacting nitrogen monoxide contained in a gas fraction withdrawn from the second step with a molecular oxygen-containing gas and methyl alcohol; a fourth step of collecting dimethyl carbonate by distilling a liquid fraction withdrawn from the second step; and a fifth step of producing and recovering methyl nitrite from a purge gas consisting of a minor portion of a gas fraction withdrawn from one of the second step and the third step by bringing the purge gas together with an ammonia-oxidation product gas into contact with methyl alcohol in a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。
    • 5. 发明授权
    • Process for continuously producing dimethyl carbonate
    • 连续生产碳酸二甲酯的方法
    • US5514829A
    • 1996-05-07
    • US344724
    • 1994-11-23
    • Keigo NishihiraShinichi YoshidaShuji Tanaka
    • Keigo NishihiraShinichi YoshidaShuji Tanaka
    • B01J8/06C07B61/00C07C68/00C07C68/08C07C69/96
    • 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 recovering methyl nitrite from a purge gas consisting of a portion of a regenerated gas fraction withdrawn from the third step by absorbing methyl nitrite in the purge gas by methyl alcohol to provide a methyl nitrite-containing liquid fraction and a nitrogen monoxide-containing gas fraction and bringing the gas fraction into contact with a molecular oxygen and methyl alcohol, to convert nitrogen monoxide in the gas fraction to methyl nitrite and to absorb this methyl nitrite by methyl alcohol, whereby methyl nitrite and nitrogen monoxide in the purge gas is recovered and reused 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,从由第三步骤抽出的一部分再生气体馏分组成的吹扫气体中回收亚硝酸甲酯,通过用甲醇吸收吹扫气体中的亚硝酸甲酯,得到含有亚硝酸甲酯的液体馏分和一氧化氮 将气体馏分与分子氧和甲醇接触,将气体部分中的一氧化氮转化成亚硝酸甲酯,并用甲醇吸收该亚硝酸甲酯,由此吹扫气中的亚硝酸甲酯和一氧化氮 在高安全性下以高效率回收和再利用。
    • 6. 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。
    • 7. 发明授权
    • Process for continuously producing dimethyl carbonate
    • 连续生产碳酸二甲酯的方法
    • US5631396A
    • 1997-05-20
    • US647164
    • 1996-05-09
    • Keigo NishihiraShinichi YoshidaShuji TanakaYutaka Asada
    • Keigo NishihiraShinichi YoshidaShuji TanakaYutaka Asada
    • B01J27/13C07B61/00C07C68/00C07C68/08C07C69/96
    • C07C68/00
    • Dimethyl carbonate ((CH.sub.3 O).sub.2 CO) is continuously produced by a catalytic reaction (first step) of CO with CH.sub.3 NO.sub.2, with a significantly reduced loss of CH.sub.3 ONO by the process including a second step wherein (CH.sub.3 O).sub.2 CO in a reaction product gas of the first step is absorbed by dimethyl oxalate while contacting the resultant liquid fraction with CO to recover CH.sub.3 ONO, a third step wherein CH.sub.3 ONO is regenerated from NO in the condensed gas fraction produced in the second step and molecular oxygen and CH.sub.3 OH introduced into the third step, the resultant regenerated gas fraction being recycled and reused as a feed gas for the first step, and a fourth step wherein (CH.sub.3 O).sub.2 CO contained in the liquid fraction of the second step is collected.
    • 通过CO与CH3NO2的催化反应(第一步)连续制备碳酸二甲酯((CH 3 O)2 CO),通过包括第二步骤的CH 3 NOO的显着降低的损失,其中(CH 3 O)2 CO在反应产物气体中的 第一步被草酸二甲酯吸收,同时使所得液体馏分与CO接触以回收CH 3 NOO,第三步是在第二步产生的冷凝气体馏分中从NO再生CH3ONO,并将第三步中引入分子氧和CH3OH, 所产生的再生气体馏分被再循环并重新用作第一步骤的进料气体;以及第四步骤,其中收集第二步骤的液体馏分中所含的(CH 3 O)2 CO。