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    Process of thermally cracking hydrocarbons using particulate solids as heat carrier
    61.
    发明授权
    Process of thermally cracking hydrocarbons using particulate solids as heat carrier 失效
    使用颗粒固体作为热载体热裂解烃的方法

    公开(公告)号：US4828681A

    公开(公告)日：1989-05-09

    申请号：US5332

    申请日：1987-01-15

    Applicant: John B. Yourtee ,  John M. Matsen

    Inventor： John B. Yourtee ,  John M. Matsen

    IPC: C10G9/28 ,  C10G9/32

    CPC classification number: C10G9/28 ,  C10G9/32

    Abstract: The invention relates to carrying out thermal cracking of hydrocarbons, or other thermal conversions of organic substances in a reactor, for which a suitable reaction time is extremely short, e.g. of the order of milliseconds. Particulate solids are used as heat carrier and as feed an organic substance is used in the form of a gas which may contain some liquid; the hot particulate solids are introduced at low or no velocity into contact with the gas, which is at substantially higher velocity; the solids accelerate in passing through the reactor but the reaction is terminated substantially before the solids attain the velocity of the product gas. Contact times are short so that the solids do not accelerate to erosive speeds. The velocity differential enhances the heat transfer rate which makes short reaction times feasible.

    Abstract translation: 本发明涉及在反应器中进行碳氢化合物的热裂解或有机物质的其他热转化，其中合适的反应时间非常短，例如 的毫秒级。 颗粒状固体用作热载体，并且当进料时，有机物质以可能含有一些液体的气体的形式使用; 以低或无速度引入热的颗粒固体与气体接触，气体的速度基本上更高; 固体通过反应器加速，但是在固体达到产物气体的速度之前基本上终止反应。 接触时间短，使得固体不会加速到侵蚀速度。 速度差异提高了传热速率，使反应时间短可行。

    Catalytic fluid coking and gasification process
    64.
    发明授权
    Catalytic fluid coking and gasification process 失效
    催化液焦化和气化过程

    公开(公告)号：US4325815A

    公开(公告)日：1982-04-20

    申请号：US183435

    申请日：1980-09-02

    Applicant: William J. Metrailer

    Inventor： William J. Metrailer

    IPC: C10G9/32 ,  C10B55/10 ,  C10J3/54 ,  C10G9/28

    CPC classification number: C10J3/54 ,  C10B55/10 ,  C10J3/482 ,  C10J3/78 ,  C10K1/024 ,  C10K3/04 ,  C10J2300/093 ,  C10J2300/0933 ,  C10J2300/0943 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0966 ,  C10J2300/0976 ,  C10J2300/1606 ,  C10J2300/1807

    Abstract: An integrated catalytic fluid coking and gasification process is provided in which a portion of the coke produced in the coker is steam gasified to produce a hydrogen-containing gas and a catalytic partially gasified coke. Subsequently, a portion of the catalytic partially gasified coke is burned to provide heated partially gasified coke which is recycled to the gasification zone. A portion of the catalytic partially gasified coke is passed from the gasification zone to the coker to contact the coker vapor phase product comprising normally liquid hydrocarbons and to crack at least a portion of the normally liquid hydrocarbons. Optionally, solid fines recovered from the gaseous effluent of the gasification zone may be recycled to the carbonaceous chargestock of the coker.

    Abstract translation: 提供了一种综合的催化流体焦化和气化方法，其中在焦化器中产生的一部分焦炭被蒸汽气化以产生含氢气体和催化部分气化的焦炭。 随后，一部分催化部分气化的焦炭被燃烧以提供加热的部分气化的焦炭，其被再循环到气化区。 催化部分气化的焦炭的一部分从气化区通入焦化器，以与包含常规液体烃的焦化气相产物接触并裂解至少一部分常规液体烃。 任选地，从气化区的气态流出物回收的固体细粉可以再循环到焦化器的碳质装料中。

    Liquid yield from pyrolysis of coal liquefaction products
    65.
    发明授权
    Liquid yield from pyrolysis of coal liquefaction products 失效
    煤液化产物热解产生液体产物

    公开(公告)号：US4244805A

    公开(公告)日：1981-01-13

    申请号：US45683

    申请日：1979-06-05

    Applicant: William J. Metrailer

    Inventor： William J. Metrailer

    IPC: C10G1/00 ,  C10G9/28 ,  C10G57/00

    CPC classification number: C10G1/002

    Abstract: The quantity and quality of liquids produced from solid coal can be enhanced by a process comprising a liquefaction zone and a pyrolysis reactor, preferably a fluid coking zone, wherein the heavy liquids obtained in the pyrolysis reactor, e.g., 1000.degree. F.+ materials having a Conradson Carbon content of at least 15 wt. % are recycled to the liquefaction zone, rather than to the pyrolysis reactor, for further treatment under hydrogenation conditions and, consequently, conversion of the heavy liquids to lower boiling liquids which may be removed from the pyrolysis reactor feed by distillation is achieved.

    Abstract translation: 可以通过包括液化区和热解反应器，优选流体焦化区的方法来提高从固体煤产生的液体的量和质量，其中在热解反应器中获得的重液体，例如1000°F。具有 Conradson碳含量至少为15wt。 ％被再循环到液化区而不是热解反应器，用于在氢化条件下进一步处理，从而实现重液体转化成可通过蒸馏从热解反应器进料中除去的低沸点液体。

    Reduction of sulphur oxides
    66.
    发明授权
    Reduction of sulphur oxides 失效
    减少硫氧化物

    公开(公告)号：US3810972A

    公开(公告)日：1974-05-14

    申请号：US22882972

    申请日：1972-02-24

    Applicant: EXXON RESEARCH ENGINEERING CO

    Inventor： HUMPHREY R ,  MOSS G

    IPC: B01D53/50 ,  C01B17/04 ,  C10G9/28

    CPC classification number: C01B17/0482 ,  B01D53/508

    Abstract: A SUBSTRATE IS COKED BY CONTACT WITH OIL AT CRACKING TEMPERATURE, AND THE COKED SUBSTRATE IS THEN CONTACTED WITH SULPHUR OXIDES-CONTAINING GASES TO REDUCE THE SULPHUR OXIDES TO SULPHUR (WHICH IS RECOVERED) AND TO OXIDIZE COKE TO CARBON OXIDES. THE CRACKED OIL VAPORS ARE ALSO RECOVERED. THE PROCESS IS OPERATED EITHER CYCLICALLY. INTERMITTTENLY OR CONTINOUSLY.

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