石油炼制与化工
石油煉製與化工
석유련제여화공
PETROLEUM PROCESSING AND PETROCHEMICALS
2015年
1期
34-38
,共5页
加氢改质%硫化%催化剂%加氢脱硫
加氫改質%硫化%催化劑%加氫脫硫
가경개질%류화%최화제%가경탈류
hydro-upgrading%sulfurization%catalyst%HDS
介绍了 FF-36和 FC-50加氢催化剂首次在中国石油锦西石化分公司加氢改质装置的使用情况，对催化剂的硫化方法和钝化步骤进行了简要介绍，详细对比了国产催化剂与进口催化剂在操作条件、产品质量和对装置能耗影响三方面的数据。结果表明，国产催化剂相对于进口催化剂在操作条件上稍微苛刻一些，在脱硫率、脱氮率和柴油十六烷值上分别提高1．63百分点、2．6百分点和8．9个单位，而在能耗上相差不大。
介紹瞭 FF-36和 FC-50加氫催化劑首次在中國石油錦西石化分公司加氫改質裝置的使用情況，對催化劑的硫化方法和鈍化步驟進行瞭簡要介紹，詳細對比瞭國產催化劑與進口催化劑在操作條件、產品質量和對裝置能耗影響三方麵的數據。結果錶明，國產催化劑相對于進口催化劑在操作條件上稍微苛刻一些，在脫硫率、脫氮率和柴油十六烷值上分彆提高1．63百分點、2．6百分點和8．9箇單位，而在能耗上相差不大。
개소료 FF-36화 FC-50가경최화제수차재중국석유금서석화분공사가경개질장치적사용정황，대최화제적류화방법화둔화보취진행료간요개소，상세대비료국산최화제여진구최화제재조작조건、산품질량화대장치능모영향삼방면적수거。결과표명，국산최화제상대우진구최화제재조작조건상초미가각일사，재탈류솔、탈담솔화시유십륙완치상분별제고1．63백분점、2．6백분점화8．9개단위，이재능모상상차불대。
The combination of hydrotreating catalyst FF-36 and hydrocracking catalyst FC-50 were first used in the hydro-upgrading unit of Jinxi Petrochemical Company. The sulfurization and passivation procedures of the catalysts are introduced. The operating conditions,product qualities and energy con-sumption of the unit using domestic catalysts were compared with the imported composite catalysts. The results show that under somewhat higher operation severity conditions the HDS rate,HDN rate and CN increment are 1.6%,2.6% and 8.9 points of the new catalysts higher than that of the reference cata-lysts,respectively. The energy consumption difference is small.
