发明名称 Hydroconversion multi-metallic catalyst and method for making thereof
摘要 In a process for forming a bulk hydroprocessing catalyst by sulfiding a catalyst precursor made in a co-precipitation reaction, up to 60% of the metal precursor feeds do not react to form catalyst precursor and end up in the supernatant as metal residuals. In the present disclosure, the metals can be recovered in a chemical precipitation step, wherein the supernatant is mixed with at least one of an acid, a sulfide-containing compound, a base, and combinations thereof to precipitate at least 50% of metal ions in at least one of the metal residuals, wherein the precipitation is carried out at a pre-select pH. The precipitate is isolated and recovered, yielding an effluent stream. The precipitate and/or the effluent stream can be further treated to form at least a metal precursor feed which can be used in the co-precipitation reaction. The process generates an effluent to waste treatment containing less than 50 ppm metals.
申请公布号 US9168519(B2) 申请公布日期 2015.10.27
申请号 US201113275518 申请日期 2011.10.18
申请人 CHEVRON U.S.A. INC. 发明人 Kuperman Alexander E.;Maesen Theodorus;Dykstra Dennis
分类号 B01J37/20;B01J37/34;B01J23/85;B01J23/888;B01J37/03;B01J27/051;B01J37/04;B01J37/08 主分类号 B01J37/20
代理机构 代理人 Ross Michael D.
主权项 1. A process for forming a bulk hydroprocessing catalyst, comprising: co-precipitating at reaction conditions at least one of a Group VIB metal precursor feed and at least a Promoter metal precursor feed selected from Group VIII, Group IIB, Group IIA, Group IVA and combinations thereof, to form a mixture comprising a catalyst precursor; isolating the catalyst precursor from the mixture, forming a supernatant containing at least a Promoter metal residual and at least a Group VIB metal residual in a total amount of at least 10 mole % of the metal precursor feeds; mixing the supernatant with at least one of an acid, a sulfide-containing compound, a base, and combinations thereof under mixing conditions at a temperature from ambient to 90° C. for a sufficient amount of time to precipitate at least 50 mole % of metal ions in at least one of the metal residuals, wherein the precipitation is carried out at a pre-select pH; isolating the precipitate to recover a first effluent containing less than 50 mole % of metal ions in at least one of the metal residuals in the supernatant; converting the metal ions in the precipitate or the first effluent into at least a metal precursor feed; recycling the at least a metal precursor feed from the converting step to the co-precipitating step; and sulfiding the catalyst precursor forming the bulk catalyst.
地址 San Ramon CA US