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Process for the preparation of ruthenium catalysts, supported on activated carbon, which are selective in the production of light olefins from the synthesis gas

机译:活性炭负载的钌催化剂的制备方法,在从合成气生产轻质烯烃方面具有选择性

摘要

In the process for the preparation of ruthenium catalysts, supported on activated carbon, which are selective in the production of light olefins from the synthesis gas, use is made of high surface area activated carbon which is treated with inorganic acids in order to eliminate the inorganic matter and then at 1000 degree C in an inert atmosphere in order to destroy the residual surface groups. The vanadium oxide promoter is then incorporated by impregnation with a solution of ammonium vanadate in ethanol, drying in an inert atmosphere and calcining at 420 degree C. Ruthenium is deposited on this precursor either by adsorption of a solution of the Ru3(CO)12 complex in pentane or by impregnation with an ethanol solution of ruthenium trichloride. The precursors are then activated in a hydrogen flux at temperatures between 300 and 400 degree C. The CO hydrogenation reaction is carried out at atmospheric pressure in a dynamic system on stoichiometric CO:H2=1:2 mixtures. The unpromoted Ru catalyst is a typical methanation catalyst the percentage of CH4 in the reaction products is 99%. The incorporation of the vanadium oxide promoter in the ruthenium catalyst causes a significant increase in selectivity for light olefins, which rises to 75%.
机译:在活性炭上负载的钌催化剂的制备方法中,该催化剂在从合成气生产轻质烯烃的过程中是选择性的,使用高表面积的活性炭,并用无机酸处理以消除无机物。物质,然后在惰性气氛中于1000摄氏度下消灭残留的表面基团。然后通过用钒酸铵的乙醇溶液浸渍掺入氧化钒促进剂,在惰性气氛中干燥并在420℃下煅烧。通过吸附Ru3(CO)12络合物的溶液将钌沉积在该前体上在戊烷中或通过用三氯化钌的乙醇溶液浸渍。然后将前体在300到400摄氏度的温度下在氢气流中活化。CO氢化反应在大气压下在动态系统中对化学计量的CO:H2 = 1:2混合物进行。未促进的Ru催化剂是典型的甲烷化催化剂,反应产物中CH 4的百分比为99%。在钌催化剂中掺入钒氧化物促进剂会导致对轻烯烃的选择性显着提高,该选择性提高至75%。

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