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ADVANCED CONTROL OF SEVERE FLUID CATALYTIC CRACKING PROCESS FOR MAXIMIZING PROPYLENE PRODUCTION FROM 发明申请

2023-03-25 2860 2475K 0

专利信息

申请日期 2025-06-28 申请号 MX2009004863
公开(公告)号 MX2009004863A 公开(公告)日 2009-10-26
公开国别 MX 申请人省市代码 全国
申请人 SAUDI ARABIAN OIL CO
简介 With an aim to optimize propylene production, petroleum oil such as gas oil is catalytically cracked by contacting the oil with catalyst mixture consisting of a base cracking catalyst containing an stable Y-type zeolite and small amounts of rare-earth metal oxide, and an additive containing a shape-selective zeolite, in a down-flow type fluid catalytic cracking apparatus having a regeneration zone, a separation zone, and a stripping zone, wherein conversion of hydrocarbon occurs under relatively severe conditions. According to this fluid catalytic cracking process, the production of light-fraction olefins such as propylene is maximized by applying appropriate process control, monitoring, and optimizing systems. Process model and historical data to test a predictive system can provide early warning of potential performance degradation and equipment failure in the FCC unit.


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