首页> 外国专利> PROCESS AND SYSTEM FOR CONVERSION OF CRUDE OIL TO PETROCHEMICALS AND FUEL PRODUCTS INTEGRATING STEAM CRACKING, FLUID CATALYTIC CRACKING, AND CONVERSION OF NAPHTHA INTO CHEMICAL RICH REFORMATE

PROCESS AND SYSTEM FOR CONVERSION OF CRUDE OIL TO PETROCHEMICALS AND FUEL PRODUCTS INTEGRATING STEAM CRACKING, FLUID CATALYTIC CRACKING, AND CONVERSION OF NAPHTHA INTO CHEMICAL RICH REFORMATE

机译:原油与汽油化学转化的过程和系统,包括蒸汽裂解,流体催化裂解以及萘酚转化为化学富集重整的过程

摘要

Process scheme configurations are disclosed that enable conversion of crude oil feeds with several processing units in an integrated manner into petrochemicals. The designs utilize minimum capital expenditures to prepare suitable feedstocks for the steam cracker complex. The integrated process for converting crude oil to petrochemical products including olefins and aromatics, and fuel products, includes mixed feed steam cracking, fluid catalytic cracking and conversion of naphtha to chemical rich reformate. Feeds to the mixed feed steam cracker include light products from hydroprocessing zones within the battery limits, recycle streams from the C3 and C4 olefins recovery steps, and raffinate from a pyrolysis gasoline and FCC naphtha aromatics extraction zone within the battery limits. Chemical reformate from straight run naphtha streams is used as an additional feed to the aromatics extraction zone and or the mixed feed steam cracker.
机译:公开了工艺方案配置,其使得能够将具有几个处理单元的原油原料以集成的方式转化为石油化学产品。该设计利用最小的资本支出来为蒸汽裂解装置生产合适的原料。将原油转化为石化产品(包括烯烃和芳烃以及燃料产品)的综合过程包括混合进料蒸汽裂解,流化催化裂解以及将石脑油转化为富含化学物质的重整产品。进入混合进料蒸汽裂解装置的进料包括来自电池极限范围内加氢处理区的轻质产品,来自C3和C4烯烃回收步骤的再循环料流以及来自处于电池极限范围内的热解汽油和FCC石脑油芳烃萃取区的提余液。来自直馏石脑油料流的化学重整产品用作芳烃萃取区和/或混合进料蒸汽裂解器的额外进料。

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