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    • 3. 发明授权
    • Heater and method for recovering hydrocarbons from underground deposits
    • 从地下沉积物回收碳氢化合物的加热器和方法
    • US09127541B2
    • 2015-09-08
    • US13127969
    • 2009-11-02
    • Alan K. BurnhamP. Henrik WallmanJames R. McConaghyRoger L. Day
    • Alan K. BurnhamP. Henrik WallmanJames R. McConaghyRoger L. Day
    • E21B43/243
    • E21B43/243
    • Heaters are presented to aid in the recovery of hydrocarbon from underground deposits. A heater is provided to a well that has been drilled through an oil-shale deposit. A fuel and an oxidizer are provided to the heater and flue gases are recovered. The heater has a counterflow design and provides a nearly uniform temperature along the heater length. The heater may be designed to operate at different temperatures and depths to pyrolyze or otherwise heat underground hydrocarbon deposits to form a product that is easily recovered and which is useful without substantial further processing. Various counterflow heaters are described including heaters having, down the heater length, distributed reaction zones, distributed catalytic oxidation of the fuel, and discrete or continuous heat generation. The heaters may also utilize inert gases from product recovery or from heater flue gases to control the heater temperature.
    • 提供加热器来帮助从地下沉积物回收碳氢化合物。 向通过油页岩沉积物钻出的井提供加热器。 燃料和氧化剂被提供给加热器并且废气被回收。 加热器具有逆流设计,并沿加热器长度提供几乎均匀的温度。 加热器可以设计成在不同的温度和深度下操作以热解或以其它方式加热地下烃沉积物以形成容易回收的产物,并且其在没有实质的进一步加工的情况下是有用的。 描述了各种逆流加热器,其包括在加热器长度,分布式反应区,燃料的分布式催化氧化以及离散或连续发热的加热器。 加热器还可以利用来自产品回收或来自加热器烟道气体的惰性气体来控制加热器温度。
    • 6. 发明申请
    • HEATER AND METHOD FOR RECOVERING HYDROCARBONS FROM UNDERGROUND DEPOSITS
    • 从地下沉积物回收烃类的加热器和方法
    • US20120205109A1
    • 2012-08-16
    • US13127969
    • 2009-11-02
    • Alan K. BurnhamP. Henrik WallmanJames R. McConaghyRoger L. Day
    • Alan K. BurnhamP. Henrik WallmanJames R. McConaghyRoger L. Day
    • E21B43/24
    • E21B43/243
    • Heater embodiments are presented to aid in the recovery of hydrocarbon from underground deposits. In one embodiment, a heater is provided to a well that has been drilled through an oil-shale deposit. A fuel and an oxidizer are provided to the heater and flue gases are recovered. The heater has a counterflow design and provides a nearly uniform temperature along the heater length. The heater may be designed to operate at different temperatures and depths to pyrolyze or otherwise heat underground hydrocarbon deposits to form a product that is easily recovered and which is useful without substantial further processing. Various embodiments of a counterflow heater are described including heaters having, down the heater length, distributed reaction zones, distributed catalytic oxidation of the fuel, and discrete or continuous heat generation. The heaters may also utilize inert gases from product recovery or from heater flue gases to control the heater temperature.
    • 提出加热器实施例以帮助从地下沉积物回收碳氢化合物。 在一个实施例中,将加热器提供到已经通过油页岩沉积物钻孔的井。 燃料和氧化剂被提供给加热器并且废气被回收。 加热器具有逆流设计,并沿加热器长度提供几乎均匀的温度。 加热器可以设计成在不同的温度和深度下操作以热解或以其它方式加热地下烃沉积物以形成容易回收的产物,并且其在没有实质的进一步加工的情况下是有用的。 描述了逆流加热器的各种实施例,其包括在加热器长度下,分布式反应区,燃料的分布式催化氧化和离散或连续发热的加热器。 加热器还可以利用来自产品回收或来自加热器烟道气体的惰性气体来控制加热器温度。
    • 9. 发明授权
    • Recycle classifier for retorting oil shale
    • 用于蒸馏油页岩的回收分级机
    • US4440623A
    • 1984-04-03
    • US412486
    • 1982-08-30
    • P. Henrik Wallman
    • P. Henrik Wallman
    • C10G1/02C10B49/16C10B53/06
    • C10G1/02
    • Heat transfer particles of fluidizable size are selected for recycling to the pyrolysis zone to broaden usable size range of oil shale feed. These recycle particles should all be of a fluidizable size and when mixed with the raw oil shale the total amount of fluidizable particles should comprise not less than about 60 weight percent of the particles in the mixture. This process is especially useful when the heat transfer material is recycled oil shale particles. The present invention is particularly advantageous when the oil shale is pyrolyzed in a vertical retorting vessel containing a fluidized bed above a packed bed of particles.
    • 选择可流化尺寸的传热颗粒用于再循环至热解区,以扩大油页岩进料的可用尺寸范围。 这些再循环颗粒应全部具有可流化的尺寸,并且当与原油页岩混合时,可流化颗粒的总量应包含不少于混合物中颗粒的约60重量%。 当传热材料是循环油页岩颗粒时,该方法特别有用。 当油页岩在包含颗粒填充层之上的流化床的垂直蒸煮容器中热解时,本发明是特别有利的。