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N-alkene(s) mixed with hydrogen isomerised to I-alkene(s) - by halide-doped alumina or silica catalyst continuously regenerated

机译:N-烯烃与氢混合异构化成I-烯烃-通过掺卤的氧化铝或二氧化硅催化剂连续再生

摘要

i-Alkenes are prepd. catalytically from n-alkenes in presence of H2 at a temp. of 400-600 deg.C. The catalyst is prepd. by copptn. of hydrated Al2O3 and/or SiO2 with NH4 salts, calcining (with loss of the latter) to give activated Al2O3 and/or SiO2, and then doping with a halide of Periodic Gps. IIIa-Va, IIb-VIIb or VIII, and/or of H. After activity loss, the catalyst is regenerated by an O2-contg. gas and a halohydrocarbon at a temp. of 400-800 deg.C.; by using a mobile bed, e.g. a fluidised bed, a purged catalyst stream may be regenerated continuously or discontinuously. Used for treating e.g. 4-8C, pref. 4-5C, esp. 4C n-alkenes and mixtures contg. them, e.g. the 4C prod. stream from steam cracking after removal of butadiene and i-butene. Yields and conversions are high. Catalyst regeneration does not require process interruption.
机译:备有i-烯烃。在一定温度下,在H2存在下从正烯烃催化400-600℃。制备催化剂。由copptn。将水合的Al2O3和/或SiO2与NH4盐混合,煅烧(不损失后者)得到活化的Al2O3和/或SiO2,然后掺入周期性Gps的卤化物。 IIIa-Va,IIb-VIIb或VIII和/或H。失去活性后,通过含O2的催化剂再生催化剂。气体和温度下的卤代烃。 400-800℃;通过使用移动床在流化床中,吹扫的催化剂流可以连续或不连续地再生。用于治疗4-8C,首选4-5C,尤其是续4C正烯烃和混合物。他们,例如4C产品。除去丁二烯和异丁烯后,蒸汽裂化产生的蒸汽产量和转化率很高。催化剂再生不需要过程中断。

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