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Advanced control of severe fluid catalytic cracking process for maximizing propylene production from 发明授权

2023-01-30 4210 1586K 0

专利信息

申请日期 2025-06-25 申请号 US11983078
公开(公告)号 US9701914B2 公开(公告)日 2017-07-11
公开国别 US 申请人省市代码 全国
申请人 M Rashid Khan; Othman A Taha
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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