MAGNETICALLY ACTUATED AXIAL VALVE DESIGN
    1.
    发明申请
    MAGNETICALLY ACTUATED AXIAL VALVE DESIGN 审中-公开
    磁力驱动阀门设计

    公开(公告)号:WO2003060358A2

    公开(公告)日:2003-07-24

    申请号:PCT/US2003/001012

    申请日:2003-01-13

    IPC: F16K

    CPC classification number: F16K31/088

    Abstract: A magnetically actuated axial valve reduces emissions associated with valve stems while retaining a high flow efficiency. In one embodiment, a valve may have inner and outer magnet rings (22 & 23) which may be permanent magnets (12 & 13). Magnetic actuation utilizing N dFeB rare earth magnets (12 & 13) to maximize available torque in rotating an outer magnet ring 180°, thereby forcing synchronous rotation of an inner magnet ring connected to the valve rotor may be provided. A rotary position sensor may provide reliable indication of open and closed valve positions. A valve incorporating a conical sealing interface between rotating and stationary graphite halves to minimize internal leakage by providing a high degree of self-alignment and amplifying the contact force between the two halves is also provided. Methods corollary to the disclosed apparatus are also provided.

    Abstract translation: 磁力驱动的轴向阀减少与阀杆相关的排放,同时保持高的流动效率。 在一个实施例中,阀可以具有内部和外部磁体环22和23,其可以是永久磁体12和13.利用N dFeB稀土磁体12和13进行磁性驱动,以使外部磁环180°旋转的可用转矩最大化,从而 可以提供连接到阀转子的内磁环的同步旋转。 旋转位置传感器可以提供打开和关闭阀位置的可靠指示。 还提供了一种在旋转和静止的石墨半部之间结合有锥形密封界面的阀,以通过提供高度的自对准和放大两个半部之间的接触力来最小化内部泄漏。 还提供了对所公开的装置的推论。

    COAL PROCESSING TO UPGRADE LOW RANK COAL HAVING LOW OIL CONTENT

    公开(公告)号:WO2012166606A3

    公开(公告)日:2012-12-06

    申请号:PCT/US2012/039598

    申请日:2012-05-25

    Abstract: A method of treating untreated low calorific coal containing moisture and organic volatiles includes feeding untreated coal to a dryer, and drying the coal. The dried coal is subjected to a pyrolyzing step where oxygen-deficient gases are brought into contact with the coal, thereby lowering the volatile content of the coal and producing a stream of pyrolysis effluent gases. The pyrolysis effluent gases are subjected to a separation process to separate lean fuel gases from liquids and tars, wherein the separation process removes less than about 20 percent of the pyrolysis effluent gases as the liquids and tars, with the remainder being the lean fuel gases;. The lean fuel gases are returned to the dryer combustor, the pyrolyzer combustor, or the pyrolyzer.

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