APPARATUS AND PROCESS FOR CONTROLLING TEMPERATURE OF HEATED FEED DIRECTED TO A FLASH DRUM WHOSE OVERHEAD PROVIDES FEED FOR CRACKING
    2.
    发明授权
    APPARATUS AND PROCESS FOR CONTROLLING TEMPERATURE OF HEATED FEED DIRECTED TO A FLASH DRUM WHOSE OVERHEAD PROVIDES FEED FOR CRACKING 有权
    用于控制加热使用FLASH鼓物质的温度的方法和设备,用于裂化塔顶产品原料的DELIVERS

    公开(公告)号:EP1765958B1

    公开(公告)日:2009-04-15

    申请号:EP05750608.1

    申请日:2005-05-18

    IPC分类号: C10G9/20

    摘要: 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.

    PROCESS FOR CRACKING SYNTHETIC CRUDE OIL-CONTAINING FEEDSTOCK
    6.
    发明公开
    PROCESS FOR CRACKING SYNTHETIC CRUDE OIL-CONTAINING FEEDSTOCK 审中-公开
    方法合成原油的裂化包含物质的使用

    公开(公告)号:EP2106432A1

    公开(公告)日:2009-10-07

    申请号:EP07864851.6

    申请日:2007-11-29

    IPC分类号: C10G69/06

    CPC分类号: C10G69/06 Y10S585/921

    摘要: 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.