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    • 1. 发明申请
    • PROCESS FOR STEAM CRACKING OF HYDROCARBON FEEDSTOCKS CONTAINING ASPHALTENES
    • 含有ASPHALTEN的油料进料的蒸汽破碎过程
    • WO2008131330A2
    • 2008-10-30
    • PCT/US2008061007
    • 2008-04-21
    • EXXONMOBIL CHEM PATENTS INCMCCOY JAMES NSTELL RICHARD C
    • MCCOY JAMES NSTELL RICHARD C
    • C10G9/36C10G2400/20
    • A process for cracking a hydrocarbon feedstock containing asphaltenes, wherein the asphaltenes are removed from the feedstock before the hydrocarbons undergo steam cracking. The process includes: (a) heating an asphaltene-containing hydrocarbon feedstock upstream with respect to a plurality of pyro lysis furnaces comprising at least two pyro lysis furnaces to form a vapor phase that is essentially free of asphaltenes and a liquid phase containing asphaltenes; (b) separating the vapor phase from the liquid phase; (c) transferring at least a portion of the separated vapor phase in parallel flow to at least two of the plurality of pyrolysis furnaces; and (d) cracking at least a portion of the hydrocarbons contained in the separated vapor phase in the at least two of the pyrolysis furnaces to form a cracked product. Several pyrolysis furnaces, e.g., from three to ten pyrolysis furnaces, can be used in the practice of the present invention.
    • 一种用于裂化含有沥青质的烃原料的方法,其中在烃经历蒸汽裂化之前,沥青质从原料中除去。 该方法包括:(a)相对于包含至少两个热解炉的多个热解炉在上游加热含沥青质烃原料以形成基本上不含沥青质的气相和含有沥青质的液相; (b)将气相与液相分离; (c)将至少一部分分离的气相以平行流转移到多个热解炉中的至少两个; 和(d)裂解所述至少两个所述热解炉中分离的气相中包含的至少一部分烃形成裂化产物。 在本发明的实践中可以使用几个热解炉,例如三到十个热解炉。
    • 7. 发明申请
    • PROCESS FOR CRACKING SYNTHETIC CRUDE OIL-CONTAINING FEEDSTOCK
    • 破碎含油原料的方法
    • WO2008091439A1
    • 2008-07-31
    • PCT/US2007/085826
    • 2007-11-29
    • EXXONMOBIL CHEMICAL PATENTS INC.KEUSENKOTHEN, Paul, F.MCCOY, James, N.GRAHAM, James, E.REIMANN, Chad, D.
    • KEUSENKOTHEN, Paul, F.MCCOY, James, N.GRAHAM, James, E.REIMANN, Chad, D.
    • C10G69/06
    • C10G69/06Y10S585/921
    • A process for steam cracking liquid hydrocarbon feedstocks containing synthetic crude oil comprises i) hydroprocessing a wide boiling range aliquot containing a) normally liquid hydrocarbon portion substantially free of resids and b) thermally cracked hydrocarbon liquid, boiling in a range from 600° to 1050°F, to provide a synthetic crude oil substantially free of resids; ii) adding to the synthetic crude oil a normally liquid hydrocarbon component boiling in a range from 100° to 1050°F; and iii) cracking the mixture resulting from ii) in a cracker furnace comprising a radiant coil outlet to provide a cracked effluent, wherein the cracking is carried out under conditions sufficient to effect a radiant coil outlet temperature which is greater than the optimum radiant coil outlet temperature for cracking the synthetic crude oil separately. A method for upgrading synthetic crude for use in cracking is also provided, as well as a feedstock for cracking.
    • 一种用于蒸汽裂解含有合成原油的液体烃原料的方法包括:i)加氢处理宽沸点等分试样,其含有基本上不含残渣的通常为液体烃部分,和b)热裂化烃液体,沸点在600°至1050° F,提供基本上不含残渣的合成原油; ii)向合成原油中加入在100°F至1050°F范围内沸腾的常规液体烃组分; 和iii)在包含辐射线圈出口的裂化炉中裂解由ii)产生的混合物以提供裂化流出物,其中裂化在足以实现大于最佳辐射线圈出口的辐射盘管出口温度的条件下进行 分别裂解合成原油的温度。 还提供了用于提高用于裂化的合成粗品的方法以及用于裂化的原料。