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    • 8. 发明授权
    • Process for producing a diaryl oxalate
    • 制备草酸二芳基酯的方法
    • US6018072A
    • 2000-01-25
    • US875823
    • 1997-08-07
    • Keigo NishihiraShuji TanakaYuki NishidaSatoru Fujitsu
    • Keigo NishihiraShuji TanakaYuki NishidaSatoru Fujitsu
    • C07C67/02C07C69/34
    • C07C67/02
    • The present invention relates to a process for producing a diaryl oxalate, characterized in that an alkylaryl oxalate is subjected to a disproportionation reaction in the presence of a disproportionation catalyst, thereby to produce a diaryl oxalate while removing a by-product comprising a dialkyl oxalate.The production process of the present invention is advantageous in that the kinds of the by-products are fewer than that in conventional production process for diaryl oxalate, and thus can be practically utilized in industry, and the diaryl oxalates such as diphenyl oxalate, produced by the production process of the present invention are very important industrial materials for producing chemical products such as carbamates.
    • PCT No.PCT / JP96 / 03636 Sec。 371日期1997年8月7日 102(e)日期1997年8月7日PCT 1996年12月12日PCT PCT。 公开号WO97 / 21660 日期:1997年6月19日本发明涉及草酸二芳基酯的制备方法,其特征在于草酸烷基芳基酯在歧化催化剂存在下进行歧化反应,从而产生草酸二芳基酯,同时除去副产物 包括草酸二烷基酯。 本发明的制造方法的优点在于副产物的种类比常规的草酸二芳基酯的制备方法少,因此可以实际应用于工业中,草酸二芳基酯如草酸二苯酯,由 本发明的生产方法是用于生产化学产品如氨基甲酸酯的非常重要的工业材料。
    • 10. 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methyl nitrite to produce dimethyl carbonate; a second step of absorbing dimethyl carbonate contained in a gas fraction withdrawn from the first step by dimethyl oxalate; a third step of regenerating methyl nitrite by contacting nitrogen monoxide contained in a gas fraction withdrawn from the second step with a molecular oxygen-containing gas and methyl alcohol; a fourth step of collecting dimethyl carbonate by distilling a liquid fraction withdrawn from the second step; and a fifth step of recovering methyl nitrite from a purge gas consisting of a portion of a regenerated gas fraction withdrawn from the third step by absorbing methyl nitrite in the purge gas by methyl alcohol to provide a methyl nitrite-containing liquid fraction and a nitrogen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。