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PROCESS FOR METHANOL COUPLED CATALYTIC CRACKING REACTION OF NAPHTHA USING A MODIFIED ZSM-5 MOLECULAR SIEVE CATALYST

机译:改性ZSM-5分子筛催化剂对甲醇催化甲醇偶联裂解反应的方法

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 63.8-89.5WT% 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 1.0-5h⁻¹.
机译:本发明提供了一种使用改性的ZSM-5分子筛催化剂的萘酚的甲醇偶联催化裂化反应的方法,该方法包括在改性的ZSM-5分子筛上的改性的ZSM-5分子筛上进行甲醇和萘的加料反应。 /或芳香烃。在此过程中,经过修饰的ZSM-5分子筛催化剂包含以重量百分比计的ZSM-5分子筛的25-80WT%,粘合剂的15-70WT%,镧的2.2-6.0WT%和1.0 ZSM-5分子筛上装载的磷的-2.8WT%。 NAPHTHA包含63.8-89.5WT%的饱和链烷烃和5.6-29.8WT%的环烷烃。在催化剂温度为550-670°C,甲醇与萘的总质量比为0.05-0.8的反应条件下,与催化剂接触期间,通过催化剂床反应的萘酚和甲醇均同时通过。萘酚和甲醇的空间速度为1.0-5h -1。

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