Reactor for oxidative conversion of hydrocarbon feeds

    公开(公告)号:US11046625B1

    公开(公告)日:2021-06-29

    申请号:US16888066

    申请日:2020-05-29

    申请人: Bio2Electric, LLC

    摘要: A system for oxidative conversion of a mixed hydrocarbon feed stream to a product stream containing at least one olefin is provided. The system includes a plurality of reactors each capable of oxidatively dehydrogenating at least a portion of a hydrocarbon in the mixed hydrocarbon feed, and each reactor able to operate at different set of reaction conditions from other reactors in the plurality of reactors. All of the reactors use the same oxygen transfer agent to produce at least one olefin. In some embodiments, at least one reactor is optimized to oxidatively couple methane to produce ethylene, while other reactors are optimized to oxidatively dehydrogenate ethane to ethylene or to oxidatively dehydrogenate propane to ethylene and/or propylene. All of the reactors feed into a single regeneration unit for the oxygen transfer agent. A method of oxidatively converting the mixed hydrocarbon feed to an olefin is also provided.

    Process for preparing oligomers of butene
    8.
    发明授权
    Process for preparing oligomers of butene 有权
    制备丁烯低聚物的方法

    公开(公告)号:US08680353B2

    公开(公告)日:2014-03-25

    申请号:US13680910

    申请日:2012-11-19

    摘要: A process for preparing oligomers by continuous oligomerization of butenes is described, wherein a) a feed stream 1) comprising 1-butene and 2-butene in a total concentration of from 10 to 70% by weight and from 10 to 60% by weight of isobutane is reacted until more than 60% by weight of the 1-butene comprised in the feed stream 1 but less than 50% by weight of the 2-butene comprised in feed stream 1 have been converted into oligomers. b) The oligomers obtained in a) are separated off and optionally passed to a further work-up and the remaining residual stream is fed to work-up by distillation. c) Isobutane is separated off by distillation from the residual stream, and d) the isobutane-depleted stream obtained after the work-up by distillation c) is reacted to form oligomers.

    摘要翻译: 描述了通过丁烯的连续低聚制备低聚物的方法,其中a)包含总重量为10-70重量%和10-60重量%的1-丁烯和2-丁烯的进料流1) 异丁烷反应直到进料流1中包含的重量百分比大于60重量%的1-丁烯,但是小于50重量%的进料流1中包含的2-丁烯已经被转化为低聚物。 b)将a)中得到的低聚物分离出来并任选地进一步处理,剩余的剩余物流通过蒸馏进料后处理。 c)通过蒸馏从残余物流分离异丁烷,和d)通过蒸馏处理后获得的异丁烷贫化物流c)反应形成低聚物。

    Catalytic Reforming
    10.
    发明申请
    Catalytic Reforming 有权
    催化重整

    公开(公告)号:US20140066676A1

    公开(公告)日:2014-03-06

    申请号:US13601281

    申请日:2012-08-31

    IPC分类号: G06G7/58 B01J8/00 C07C5/00

    摘要: Methods and systems for improved catalytic reforming are disclosed. A method of catalytic reforming includes feeding a feedstream comprising C6-convertibles to one or more reactors; contacting the feedstream with a reforming catalyst; selecting values for a LHSV, a H2/HC ratio, and a conversion of C6-convertibles from a deactivation kinetic model so as to maximize a net present amount of benzene produced over a run-length of the reforming catalyst; operating the one or more reactors at the selected LHSV, the selected H2/HC ratio, and the selected conversion of C6-convertibles; and recovering an effluent from the reactor, wherein the effluent comprises at least about 40 wt % benzene.

    摘要翻译: 公开了用于改进催化重整的方法和系统。 一种催化重整的方法包括将包含C6-可转变物的进料流进料到一个或多个反应器; 使原料流与重整催化剂接触; 从失活动力学模型中选择LHSV值,H2 / HC比值和C6-可转化物的转化率,以便最大化在重整催化剂的游程长度上产生的苯的净存在量; 在所选择的LHSV,所选择的H 2 / HC比率和所选择的C6-可转换的转化物中操作所述一个或多个反应器; 以及从所述反应器回收流出物,其中所述流出物包含至少约40重量%的苯。