当代化工
噹代化工
당대화공
CONTEMPORARY CHEMICAL INDUSTRY
2013年
2期
208-211
,共4页
宋永一%方向晨%郭蓉%刘继华
宋永一%方嚮晨%郭蓉%劉繼華
송영일%방향신%곽용%류계화
催化剂级配%清洁柴油%催化剂%加氢精制%加氢脱硫
催化劑級配%清潔柴油%催化劑%加氫精製%加氫脫硫
최화제급배%청길시유%최화제%가경정제%가경탈류
Catalyst stacking technology%Clean diesel%Catalyst%Hydrotreating%Hydrodesulfurization
为满足炼油企业生产国Ⅳ及欧Ⅴ标准清洁柴油的需要,抚顺石油化工研究院(FRIPP)开发了适合不同原料、分别以W-Mo-Ni(Mo-Ni)及Mo-Co为活性金属的FHUDS系列催化剂,并根据加氢反应器内催化剂床层不同的工况条件和反应特点,结合不同类型催化剂的脱硫反应机理,开发了生产超低硫柴油的 S-RASSG 催化剂级配技术.工业应用结果表明:采用 S-RASSG 技术及配套的 FHUDS-2/FHUDS-5以及新一代FHUDS-6/FHUDS-5催化剂体系,加工常压柴油掺兑质量分数40%左右催化柴油及焦化汽柴油或减压柴油的高硫混合油,在反应器入口压力8.0 MPa,主催化剂体积空速1.85~2.25 h-1、平均反应温度350℃左右等条件下,可以长周期稳定生产硫质量分数小于50μg/g、满足国Ⅳ标准的低硫柴油;加工常压柴油掺兑质量分数30%左右减压柴油及少量焦化柴油的混合油,在反应器入口压力8.0 MPa,主催化剂体积空速1.85 h-1、平均反应温度350℃左右等条件下,可以稳定生产硫质量分数小于10μg/g、满足欧Ⅴ标准的超低硫柴油.S-RASSG催化剂级配技术为炼油企业生产满足国Ⅳ和欧Ⅴ标准的超低硫柴油提供了有力的技术支撑.
為滿足煉油企業生產國Ⅳ及歐Ⅴ標準清潔柴油的需要,撫順石油化工研究院(FRIPP)開髮瞭適閤不同原料、分彆以W-Mo-Ni(Mo-Ni)及Mo-Co為活性金屬的FHUDS繫列催化劑,併根據加氫反應器內催化劑床層不同的工況條件和反應特點,結閤不同類型催化劑的脫硫反應機理,開髮瞭生產超低硫柴油的 S-RASSG 催化劑級配技術.工業應用結果錶明:採用 S-RASSG 技術及配套的 FHUDS-2/FHUDS-5以及新一代FHUDS-6/FHUDS-5催化劑體繫,加工常壓柴油摻兌質量分數40%左右催化柴油及焦化汽柴油或減壓柴油的高硫混閤油,在反應器入口壓力8.0 MPa,主催化劑體積空速1.85~2.25 h-1、平均反應溫度350℃左右等條件下,可以長週期穩定生產硫質量分數小于50μg/g、滿足國Ⅳ標準的低硫柴油;加工常壓柴油摻兌質量分數30%左右減壓柴油及少量焦化柴油的混閤油,在反應器入口壓力8.0 MPa,主催化劑體積空速1.85 h-1、平均反應溫度350℃左右等條件下,可以穩定生產硫質量分數小于10μg/g、滿足歐Ⅴ標準的超低硫柴油.S-RASSG催化劑級配技術為煉油企業生產滿足國Ⅳ和歐Ⅴ標準的超低硫柴油提供瞭有力的技術支撐.
위만족련유기업생산국Ⅳ급구Ⅴ표준청길시유적수요,무순석유화공연구원(FRIPP)개발료괄합불동원료、분별이W-Mo-Ni(Mo-Ni)급Mo-Co위활성금속적FHUDS계렬최화제,병근거가경반응기내최화제상층불동적공황조건화반응특점,결합불동류형최화제적탈류반응궤리,개발료생산초저류시유적 S-RASSG 최화제급배기술.공업응용결과표명:채용 S-RASSG 기술급배투적 FHUDS-2/FHUDS-5이급신일대FHUDS-6/FHUDS-5최화제체계,가공상압시유참태질량분수40%좌우최화시유급초화기시유혹감압시유적고류혼합유,재반응기입구압력8.0 MPa,주최화제체적공속1.85~2.25 h-1、평균반응온도350℃좌우등조건하,가이장주기은정생산류질량분수소우50μg/g、만족국Ⅳ표준적저류시유;가공상압시유참태질량분수30%좌우감압시유급소량초화시유적혼합유,재반응기입구압력8.0 MPa,주최화제체적공속1.85 h-1、평균반응온도350℃좌우등조건하,가이은정생산류질량분수소우10μg/g、만족구Ⅴ표준적초저류시유.S-RASSG최화제급배기술위련유기업생산만족국Ⅳ화구Ⅴ표준적초저류시유제공료유력적기술지탱.
To meet the requirement for the production of Euro-Ⅳ and Euro-V clean diesel for refineries, Fushun research institute of petroleum & petrochemicals (FRIPP) has developed FHUDS series catalysts with W-Mo-Ni (Mo-Ni) or Mo-Co as active metals, which have a strong adaptability to different feedstocks. Based on different operating conditions and reaction characteristics of different catalyst beds in running cycle and in consideration of ultra desulfurization mechanisms of different types of catalysts, S-RASSG diesel ultra deep desulfurization technology with different catalyst stack loading has been developed by FRIPP. The commercial application results show that: when S-RASSG catalyst stack technology and its associated FHUDS-2/FHUDS-5 and FHUDS-6/FHUDS-5 catalysts are applied, the high sulfur feed blended with 60% SRGO and 40% LCO, coker diesel or vacuum tower diesel can be processed to stably produce product diesel with sulfur lower than 50×10-6 which meets Guo-Ⅳstandard specifications at reactor inlet pressure of 8.0 MPa, main catalyst LHSV of 1.85~2.25 h-1, and WABT of 350 ℃, etc. The product diesel with less than 10×10-6 sulfur, which meets Euro-Ⅴ standard ,can be produced with feed blended with 70%SRGO, 30%vacuum tower diesel and a small quantity of coker diesel under the conditions of reactor inlet pressure of 8.0 MPa, main catalyst LHSV of 1.85 h-1,WABT of 350 ℃, etc. S-RASSG catalyst stack technology has provided a strong technology support for production of Euro-Ⅳ and Euro-Ⅴdiesels for refineries..