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Catalytic method of naphtha catalytic cracking reaction of methanol coupling with modified ZSM-5 molecular sieve catalyst

机译:改性ZSM-5分子筛催化剂催化甲醇石脑油催化裂化反应的方法

摘要

The present invention provides a process for methanol coupled catalytic cracking reaction of naphtha using a modified ZSM-5 molecular sieve catalyst, comprising performing a co-feeding reaction of methanol and naphtha on the modified ZSM-5 molecular sieve catalyst to produce low carbon olefins and/or aromatic hydrocarbons. In the process, the modified ZSM-5 molecular sieve catalyst comprises, in term of weight percent, 25-80wt% of a ZSM-5 molecular sieve, 15-70wt% of a binder, and 2.2-6.0wt% of lanthanum and 1.0-2.8wt% of phosphorus loaded on the ZSM-5 molecular sieve. The naphtha comprises 63.8-89.5 wt% of saturated chain alkanes and 5.6-29.8wt% of cyclic alkanes. The naphtha and methanol concurrently pass through the catalyst bed, which are reacted during contacting with the catalyst under a reaction condition of a reaction temperature of 550-670°C, a mass ratio of methanol to naphtha of 0.05-0.8, and a total mass space velocity of naphtha and methanol of 1.0-5 h -1 .
机译:本发明提供了使用改性的ZSM-5分子筛催化剂的石脑油的甲醇偶联催化裂化反应的方法,包括在改性的ZSM-5分子筛催化剂上进行甲醇和石脑油的共进料反应以生产低碳烯烃和/或芳香烃。在该方法中,改性的ZSM-5分子筛催化剂以重量百分比计包含25-80wt%的ZSM-5分子筛,15-70wt%的粘合剂,以及2.2-6.0wt%的镧和1.0。 -2.8wt%的磷负载在ZSM-5分子筛上。石脑油包含63.8-89.5wt%的饱和链烷烃和5.6-29.8wt%的环状烷烃。石脑油和甲醇同时通过催化剂床,它们在与催化剂接触期间在550-670℃的反应温度,甲醇与石脑油的质量比为0.05-0.8和总质量的反应条件下反应。石脑油和甲醇的空速为1.0-5 h -1。

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