Transport of a wet gas through a subsea pipeline
    3.
    发明授权
    Transport of a wet gas through a subsea pipeline 失效
    通过海底管道输送湿气

    公开(公告)号:US06703534B2

    公开(公告)日:2004-03-09

    申请号:US09877798

    申请日:2001-06-08

    IPC分类号: C07C900

    摘要: A transport process for a wet gas employs a subsea heat exchanger having first and second flowpaths separated by a heat transfer surface. A cooler heat transfer medium is conveyed through the first flowpath in a liquid phase while a warmer hydrocarbon stream having a gaseous hydrocarbon phase and a liquid aqueous phase is conveyed through the second flowpath, which cools the hydrocarbon stream and heats the heat transfer medium. The heat transfer medium is converted by heating to a vapor phase, which is conveyed to a passive condenser associated with the subsea heat exchanger. The ambient temperature of the sea water submersing the condenser cools the heat transfer medium and restores it to the liquid phase for reuse in the heat exchanger. A portion of the hydrocarbon stream is converted by cooling to a plurality of solid gas hydrate particles while a solid particle medium entrained within the hydrocarbon stream prevents the build-up of gas hydrate particles in the second flowpath. The gas hydrate particles mix with the remaining liquid phase components of the hydrocarbon stream to form a gas hydrate slurry, which is withdrawn from the second flowpath and conveyed through a subsea transport pipeline.

    摘要翻译: 用于湿气体的运输方法采用具有由传热表面分开的第一和第二流路的海底热交换器。 较冷的传热介质以液相方式通过第一流路输送,而具有气态烃相和液态水相的较热烃流被输送通过第二流路,该第二流路冷却烃流并加热传热介质。 传热介质通过加热转化为气相,将其输送到与海底热交换器相关联的被动冷凝器。 浸入冷凝器的海水的环境温度冷却传热介质并将其还原到液相中以在热交换器中重新使用。 烃流的一部分通过冷却转化为多个固体气体水合物颗粒,而夹带在烃流中的固体颗粒介质阻止了第二流路中气体水合物颗粒的积聚。 气体水合物颗粒与烃流的剩余液相组分混合以形成气体水合物浆料,其从第二流动路径排出并通过海底输送管线输送。

    Production of a gas hydrate slurry using a fluidized bed heat exchanger
    4.
    发明授权
    Production of a gas hydrate slurry using a fluidized bed heat exchanger 失效
    使用流化床热交换器生产气体水合物浆料

    公开(公告)号:US06350928B1

    公开(公告)日:2002-02-26

    申请号:US09476297

    申请日:1999-12-30

    IPC分类号: C07C900

    摘要: A process is provided for converting a multi-phase fluid stream having an initial gas phase and an initial liquid phase to a gas hydrate slurry. The initial liquid phase includes an initial water and the initial gas phase includes a hydrocarbon gas. An inert solid particle medium is entrained in the multi-phase fluid stream to form a fluidizable mixture which is conveyed through the interior of a heat transfer tube enclosed within a shell. A heat transfer medium resides within the shell, but is external to the heat transfer tube in fluid isolation from the fluidizable mixture. The wall of the heat transfer tube provides a heat transfer surface for heat exchange between the multi-phase fluid stream and the heat transfer medium, cooling the multi-phase fluid stream on contact to a temperature below the gas hydrate formation temperature and converting at least a portion of the hydrocarbon gas and initial water to a plurality of solid gas hydrate particles. The solid particle medium substantially prevents accumulation of the solid gas hydrate particles on the tube wall. The fluidizable mixture is separated from the solid particle medium to recover a gas hydrate slurry containing the plurality of solid gas hydrate particles and the remaining portion of the initial liquid phase.

    摘要翻译: 提供了一种将具有初始气相和初始液相的多相流体流转化为气体水合物浆料的方法。 初始液相包括初始水,初始气相包括烃气。 惰性固体颗粒介质被夹带在多相流体流中以形成可流化的混合物,其被输送通过封装在壳体内的传热管的内部。 传热介质位于壳体内部,但在与可流化混合物流体隔离的传热管的外部。 传热管的壁提供用于在多相流体流和传热介质之间进行热交换的传热表面,将接触到的多相流体流冷却至低于气体水合物形成温度的温度,并至少转换 一部分烃气体和初始水分到多个固体气体水合物颗粒。 固体颗粒介质基本上防止固体气体水合物颗粒在管壁上积聚。 将可流化的混合物与固体颗粒介质分离,以回收含有多个固体气体水合物颗粒和初始液相的剩余部分的气体水合物浆料。

    Recovery of organic compounds using a saturator
    5.
    发明授权
    Recovery of organic compounds using a saturator 有权
    使用饱和器回收有机化合物

    公开(公告)号:US08097172B2

    公开(公告)日:2012-01-17

    申请号:US11576326

    申请日:2005-09-30

    IPC分类号: C02F1/10 C07C27/00

    CPC分类号: C07B63/00 C02F1/10

    摘要: The present invention provides an apparatus for recovering organic compounds from plant waste water. A saturator (10) is coupled to a feed gas stream (70) and a heated makeup water stream (54) which includes recoverable organic compounds. The saturator provides a saturated feed gas stream (70) which includes feed gas, steam and recovered organic compounds. A pump (30) recycles saturator water (56) and the makeup water stream (50) is added to that recycle stream (54).

    摘要翻译: 本发明提供一种从植物废水中回收有机化合物的装置。 饱和器(10)耦合到进料气流(70)和加热的补充水流(54),其包括可回收的有机化合物。 饱和器提供饱和进料气流(70),其包括进料气体,蒸汽和回收的有机化合物。 泵(30)再循环饱和器水(56)并且补充水流(50)被添加到该再循环流(54)中。

    Recovery of Organic Compounds Using a Saturator
    6.
    发明申请
    Recovery of Organic Compounds Using a Saturator 有权
    使用饱和器回收有机化合物

    公开(公告)号:US20080119574A1

    公开(公告)日:2008-05-22

    申请号:US11576326

    申请日:2005-09-30

    IPC分类号: C02F1/10 C07C27/34 B01J19/24

    CPC分类号: C07B63/00 C02F1/10

    摘要: The present invention provides an apparatus for recovering organic compounds from plant waste water. A saturator (10) is coupled to a feed gas stream (70) and a heated makeup water stream (54) which includes recoverable organic compounds. The saturator provides a saturated feed gas stream (70) which includes feed gas, steam and recovered organic compounds. A pump (30) recycles saturator water (56) and the makeup water stream (50) is added to that recycle stream (54).

    摘要翻译: 本发明提供一种从植物废水中回收有机化合物的装置。 饱和器(10)耦合到进料气流(70)和加热的补充水流(54),其包括可回收的有机化合物。 饱和器提供饱和进料气流(70),其包括进料气体,蒸汽和回收的有机化合物。 泵(30)回收饱和器水(56)并且补充水流(50)被添加到该再循环流(54)中。