首页> 外国专利> The hydrogenation reaction catalyst, using the production method, and its catalyst, being the hydrogenation reaction catalyst which is shown with the methodological null

The hydrogenation reaction catalyst, using the production method, and its catalyst, being the hydrogenation reaction catalyst which is shown with the methodological null

机译:使用该制造方法的氢化反应催化剂及其催化剂为方法学无效的氢化反应催化剂。

摘要

Hydrogenation catalyst represented by the following Chemical Formula 1, manufacturing method thereof, and gamma using the catalyst present invention - relates to a process for the production of butyrolactone. Gamma maleic anhydride using the catalysts of the present invention produced is stabilized by silica precursor particles of manganese oxide copper oxide, zinc oxide and - according to a method of manufacturing a butyrolactone, a low ratio of hydrogen to the reaction be prepared butyrolactone - in a molar ratio of operating conditions shows high selectivity, high productivity and high yield, gamma maleic anhydride stably for a long time even without frequent reactivation operation of the catalyst can: Formula 1 CuO (a) ZnO (b) MnO 2 (c) SiO 2 (d) In (wherein, d a, b, and c are shown relative to the weight, a is 20~90, b is 0.01~10, c is 0.01~5, d is 5 to 50)
机译:由以下化学式1,其制造方法和使用本发明的催化剂表示的加氢催化剂涉及丁内酯的生产方法。通过使用氧化锰铜氧化物,氧化锌的二氧化硅前体颗粒和根据制造丁内酯的方法,低氢与反应制备的丁内酯的比例的二氧化硅将前体颗粒稳定化,使用本发明的催化剂生产的γ-马来酸酐。操作条件的摩尔比显示出高选择性,高产率和高收率,即使没有频繁的催化剂再活化操作,γ-马来酸酐也能稳定长时间保持稳定:式1 CuO(a)ZnO(b)MnO 2 (c)SiO 2 (d)在(其中,da,b和c相对于重量示出,a为20〜90,b为0.01〜10,c为0.01〜 5,d是5到50)

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