发明名称 Process for the start-up of hydrotreatment or hydroconversion units
摘要 The invention describes a process for start-up of a hydrotreatment or hydroconversion unit carried out in the presence of hydrogen, in at least 2 catalytic beds, process in which At least one bed contains at least one presulfurized and preactivated catalyst and at least one catalytic bed that contains a catalyst whose catalytic metals are in oxidized form,A so-called starting feedstock, which is a hydrocarbon fraction that contains at least 0.5% by weight of sulfur, lacking olefinic compounds and not containing an added sulfur-containing compound, passes through a first catalytic bed that contains said presulfurized and preactivated catalyst and then passes through at least one catalytic bed that contains a catalyst whose catalytic metals are in oxidized form,And the first presulfurized and preactivated catalyst bed reaches a temperature of at least 220° C.
申请公布号 US9434893(B2) 申请公布日期 2016.09.06
申请号 US201313862673 申请日期 2013.04.15
申请人 EURECAT S.A. 发明人 Dufresne Pierre
分类号 C10G65/02;C10G45/08;C10G47/02;C10G47/06;C10G45/04;C10G45/46;C10G45/60;C10G45/06;C10G47/04;C10G65/04;C10G65/10;B01J37/20;B01J23/882 主分类号 C10G65/02
代理机构 Millen White Zelano and Branigan, PC 代理人 Millen White Zelano and Branigan, PC ;Sopp John;Henter Csaba
主权项 1. A process for start-up of a hydrotreatment or hydroconversion reaction carried out in the presence of hydrogen, in at least 2 catalytic beds, comprising at least one bed contains at least one presulfurized and preactivated catalyst, and at least one catalytic bed contains a catalyst whose catalytic metals are in oxidized form, passing a starting feedstock, which is a hydrocarbon fraction that contains at least 0.3% by weight of sulfur, lacking olefinic compounds and not containing an added sulfur-containing compound, through a first catalytic bed that contains said presulfurized and preactivated catalyst and then passes through at least one catalytic bed that contains a catalyst whose catalytic metals are in oxidized form, and the first presulfurized and preactivated catalyst bed reaches a temperature of at least 220° C.,wherein the presulfurized and preactivated catalyst and the catalyst whose catalytic metals are in oxidized form are the same catalyst with the exception of their form being presulfurized and preactivated versus oxidized.
地址 La Voulte sur Rhone FR