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Fluid bed catalytic cracking process characterized by a high selectivity to olefins

机译:流化床催化裂化工艺具有对烯烃的高选择性的特点

摘要

The invention relates to a fluid catalytic cracking process for the preparation of good quality hydrocarbon fractions with a high octane number starting from heavy hydrocarbon fractions of a poorer quality characterized in that the heavy hydrocarbon fraction is put in contact, under cracking conditions, with a catalytic composition comprising a conventional FCC catalyst and a quantity of between 3-60% of a hydrothermally stable microporous material containing titanium.
机译:本发明涉及一种流化催化裂化方法,用于从质量较差的重质烃馏分开始制备具有高辛烷值的高质量烃馏分,其特征在于,重质烃馏分在裂化条件下与催化剂接触。该组合物包含常规的FCC催化剂和3-60%的含钛的水热稳定微孔材料。

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