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    • 8. 发明申请
    • APPARATUS AND PROCESS FOR CONTROLLING TEMPERATURE OF HEATED FEED DIRECTED TO A FLASH DRUM WHOSE OVERHEAD PROVIDES FEED FOR CRACKING
    • 用于控制加热进料温度的装置和方法,所述加热进料指向一个以上提供给粉碎进料的闪光桶
    • WO2005113713A3
    • 2006-01-12
    • PCT/US2005017482
    • 2005-05-18
    • EXXONMOBIL CHEM PATENTS INCSTELL RICHARD CMCCOY JAMES N
    • STELL RICHARD CMCCOY JAMES N
    • C10G20060101C10G9/00C10G9/14C10G11/00C10G9/20
    • C10G9/206C10G9/16C10G9/20C10G2300/1033C10G2300/1044C10G2300/1055C10G2300/107C10G2300/805C10G2300/807C10G2400/20Y02P30/40
    • An apparatus and process are provided for cracking hydrocarbonaceous feed, wherein the temperature of heated effluent directed to a vapor/liquid separator, e.g., flash drum, whose overhead is subsequently cracked, can be controlled within a range sufficient so the heated effluent is partially liquid, such as from about 260 to about 540°C (500 to 1000°F). This permits processing of a variety of feeds containing resid with greatly differing volatilities, e.g., atmospheric resid and crude at higher temperature and dirty liquid condensates, at lower temperatures. The temperature can be lowered as needed by (i) providing one or more additional downstream feed inlets to a convection section, (ii) increasing the ratio of water/steam mixture added to the hydrocarbonaceous feed, (iii) using a high pressure boiler feed water economizer to remove heat; (iv) heating high pressure steam to remove heat, (v) bypassing an intermediate portion of the convection section used, e.g., preheat rows of tube banks, and/or (vi) reducing excess oxygen content of the flue gas providing convection heat.
    • 提供了一种用于裂解含烃原料的装置和方法,其中引导到蒸汽/液体分离器(例如,其塔顶馏出物被破裂的闪蒸鼓)的加热流出物的温度可以控制在足够的范围内,使得加热的流出物是部分液体 ,例如约260至约540℃(500至1000°F)。 这允许在较低温度下处理含有具有极大不同挥发性的残渣的各种进料,例如高温度下的常压渣油和粗油,以及脏液体冷凝物。 可以根据需要降低温度(i)向对流部分提供一个或多个附加的下游进料入口,(ii)增加添加到含烃进料中的水/蒸汽混合物的比例,(iii)使用高压锅炉进料 节水器去除热量; (iv)加热高压蒸汽以除去热量,(v)绕过所使用的对流段的中间部分,例如预热管排排,和/或(vi)减少提供对流热的烟道气的过量氧含量。
    • 9. 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。