Method and System for Steamcracking
    1.
    发明公开

    公开(公告)号:US20240158700A1

    公开(公告)日:2024-05-16

    申请号:US18548888

    申请日:2022-03-08

    申请人: LINDE GMBH

    摘要: A method of steam cracking using a steam cracking arrangement including an electric cracking furnace without a convection zone and a quench cooling train is proposed, wherein a process gas stream is passed through the cracking furnace and the cooling train. The cooling train is operated to comprise at least two distinct cooling steps arranged in either order, wherein in a first cooling step at least a part of the process gas stream withdrawn from the electric cracking furnace is cooled against vaporizing boiler feed water at an absolute pressure level between 30 and 175 bar and wherein in a second cooling step at least a part of the process gas stream withdrawn from the electric cracking furnace is cooled against a superheated mixture of feed hydrocarbons and process steam used in forming the process gas stream which is thereby heated to a temperature level between 350 and 750° C.

    Steam Cracking with Supplemental Electrical Heating

    公开(公告)号:US20230013408A1

    公开(公告)日:2023-01-19

    申请号:US17861168

    申请日:2022-07-09

    IPC分类号: C10G9/36 C10G9/24

    摘要: A hybrid steam cracking process including, in addition to combusting a fuel in a steam cracker furnace to provide thermal energy to the radiant and convection sections, heating a segment of an external furnace piping using an electrical heating device. The external furnace piping can include, e.g., the hydrocarbon-containing feed inlet piping, the cross-over piping, the radiant section inlet piping, and the radiant section outlet piping. Capacity and selectivity of the steam cracker furnace can be enhanced compared to conventional steam cracking process without electrical heating. The technology can be conveniently deployed in existing conventional steam cracking facilities.

    Process for catalytic reaction of heavy oils
    7.
    发明授权
    Process for catalytic reaction of heavy oils 失效
    重油催化反应方法

    公开(公告)号:US4482450A

    公开(公告)日:1984-11-13

    申请号:US538361

    申请日:1983-10-03

    CPC分类号: C10G45/18 B01J23/90

    摘要: A process for catalytic reaction of heavy oils and a particulate solid medium, which comprises withdrawing a part or the whole of the used medium from the reactor, separating the withdrawn particles into the particles which have been rendered magnetic by the deposition thereon of nickel, vanadium, iron and copper originally contained in the heavy oils, and non-magnetic particles, using a high gradient magnetic separator which is so designed that a ferromagnetic matrix is placed in a uniform high magnetic field, and returning the non-magnetic particles of the medium into the reactor for re-use.

    摘要翻译: 一种重油和一种颗粒状固体介质催化反应的方法,包括从反应器中取出一部分或全部使用的介质,将取出的颗粒分离成通过镍,钒沉积而成为磁性的颗粒 ,最初包含在重油中的铁和铜以及非磁性颗粒,使用高梯度磁选机,其被设计成使铁磁性基质置于均匀的高磁场中,并且使介质的非磁性颗粒返回 进入反应堆再次使用。