In situ mitigation of coke buildup in porous catalysts by pretreatment of hydrocarbon feed to reduce peroxides and oxygen impurities
AssigneeCenter for Research, Inc.
InventorsBala Subramaniam, Said Saim, Michael C. Clark
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Abstract
An improved process is provided for in situ mitigation of coke buildup and porous catalyst used for the processing of hydrocarbon feed stocks. The process exhibits improved catalyst activity over extended periods and the process comprises the pretreatment of hydrocarbon feed stocks to reduce impurities in the feed stocks in the form of peroxides and oxygen compounds that promote the formation of coke precursors, which precursors are typically in the form of olefinic oligomers. The process includes contacting the pretreated feed stream with a suitable catalyst under sub-critical, near-critical and supercritical conditions.
Claims13
In a method of carrying out a catalyzed reaction subject to catalyst deactivation by coke formation on the reaction catalyst including the steps of providing a feed stream including a reactant for the reaction and impurities comprising peroxide and oxygenate impurities, contacting said feed stream with a solid porous catalyst and causing the catalyzed reaction to occur and generate a reaction mixture, the improvement which comprises the steps of pretreating said feed stream to remove both oxygenate and peroxide impurities prior to said contacting step, and carrying out said contacting step at a catalyst temperature between 0.9-1.2 critical temperature of said reaction mixture.
In a method of carrying out a catalyzed reaction subject to catalyst deactivation by coke formation on the reaction catalyst including the steps of providing a feed stream including a reactant for the reaction and containing inherent impurities comprising peroxide impurities, contacting said feed stream with a solid porous catalyst and causing the catalyzed reaction to occur and generate a reaction mixture, the improvement which comprises the steps of employing a deoxygenated feed stream having less than about 100 ppm of said inherent peroxide impurities therein, and carrying out said contacting step at a catalyst temperature between 0.9-1.2 critical temperature of said reaction mixture.
Dependencies are inferred from the claim text.