Energy Conversion Using Rankine Cycle System
    3.
    发明申请
    Energy Conversion Using Rankine Cycle System 审中-公开
    使用兰金循环系统的能量转换

    公开(公告)号:US20120047889A1

    公开(公告)日:2012-03-01

    申请号:US12870036

    申请日:2010-08-27

    IPC分类号: F01K25/06 F01K23/06

    摘要: A process for recovering waste heat in an organic Rankine cycle system which comprises passing a liquid phase working fluid through heat exchange in successive communication with two or more process streams which thus heat the working fluid, removing a vapor phase working fluid from the heat exchanger, passing the vapor phase working fluid to an expander wherein the waste heat is converted into mechanical energy, and passing the vapor phase working fluid from the expander to a condenser wherein the vapor phase working fluid is condensed into the liquid phase working fluid.

    摘要翻译: 一种用于在有机朗肯循环系统中回收废热的方法,其包括使液相工作流体通过热交换与两个或更多个工艺流连续连通,从而加热工作流体,从热交换器除去气相工作流体, 将气相工作流体通入膨胀器,其中废热被转化为机械能,并将气相工作流体从膨胀器传递到冷凝器,其中气相工作流体被冷凝成液相工作流体。

    PROCESS FOR RECOVERING CATALYTIC PRODUCT
    9.
    发明申请
    PROCESS FOR RECOVERING CATALYTIC PRODUCT 有权
    回收催化产品的方法

    公开(公告)号:US20120138509A1

    公开(公告)日:2012-06-07

    申请号:US12960012

    申请日:2010-12-03

    IPC分类号: C10G47/00 C10G31/00

    摘要: A process is disclosed for recovering product from catalytically converted product streams. An integrated debutanizer column provides an LPG stream, a light naphtha stream and a heavy naphtha stream. The integrated debutanizer column may comprise a dividing wall column. The light naphtha stream may be used as an absorbent for a primary absorber column which provides advantageous operation.

    摘要翻译: 公开了从催化转化产物流中回收产物的方法。 综合的脱丁烷塔提供LPG流,轻石脑油流和重石脑油流。 整合的脱丁烷塔可以包括分隔壁塔。 轻石脑油流可以用作主吸收塔的吸收剂,其提供有利的操作。

    PROCESS FOR RECOVERING FCC PRODUCT
    10.
    发明申请
    PROCESS FOR RECOVERING FCC PRODUCT 有权
    恢复FCC产品的方法

    公开(公告)号:US20110108457A1

    公开(公告)日:2011-05-12

    申请号:US12614907

    申请日:2009-11-09

    IPC分类号: C10G55/06

    CPC分类号: C10G11/18 C10G7/00 C10G31/06

    摘要: A process is disclosed for recovering product from catalytically converted product streams. Gaseous unstabilized naphtha from an overhead receiver from a main fractionation column is compressed in a compressor. Liquid unstabilized naphtha from the overhead receiver and liquid naphtha fraction from the compressor are sent to a naphtha splitter column upstream of a primary absorber. Consequently, less naphtha is circulated in the gas recovery system.

    摘要翻译: 公开了从催化转化产物流中回收产物的方法。 来自主分馏塔的塔顶接收器的气态未稳定石脑油在压缩机中被压缩。 来自塔顶储存器的液体不稳定石脑油和来自压缩机的液体石脑油馏分被送到主吸收器上游的石脑油分离塔。 因此,较少的石脑油在气体回收系统中循环。