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Control of fluid catalytic cracking process for minimizing additive usage in the desulfurization of 发明授权

2023-01-03 2290 2227K 0

专利信息

申请日期 2025-07-09 申请号 US12785647
公开(公告)号 US9764314B2 公开(公告)日 2017-09-19
公开国别 US 申请人省市代码 全国
申请人 Saeed Saad Al Alloush; Othman A Taha; M Rashid Khan
简介 A method and apparatus for the cracking of a petroleum oil feedstock to produce a desulfurized full-range gasoline product. The petroleum oil feedstock is contacted with a base cracking catalyst and an FCC additive in an FCC unit, wherein the catalyst includes a stable Y-type zeolite and a rare-earth metal oxide and the additive includes a shape selective zeolite. The catalyst, additive and petroleum oil feedstock can be contacted in a down-flow or riser fluid catalytic cracking unit, that can also include a regeneration zone, a separation zone, and a stripping zone. The FCC unit includes an integrated control and monitoring system that monitors at least one parameter selected from FCC operating parameters, feed rate, feedstock properties, and product stream properties, and adjusts at least one parameter in response to the measured parameter to increase production of desulfurized products.


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