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    • 7. 发明申请
    • RADIATOR SCREENS
    • 散热器屏幕
    • WO2012095689A3
    • 2012-09-13
    • PCT/IB2011002997
    • 2011-12-12
    • AGCO DO BRASIL COM A IND LTDHOLLATZ BRIAN JAY
    • HOLLATZ BRIAN JAY
    • B60K11/04B60K11/08F01P11/10F01P11/12F02B29/04F02M35/00F02M35/02F02M35/10
    • F01P11/12B60K11/04B60K11/08B60Y2200/22B60Y2200/41F01P11/10F02M35/10013
    • A radiator screen arrangement (10) for a combine harvester is provided. A screen (12) through which air, which is to pass through a radiator, is drawn by a fan. Rotating means (16) are provided for rotating the screen. Blanking means (18), past which the screen is rotated, provides a blanked off area of the screen which is not subject to the induction pressure of the fan and from which particles can therefore be more easily removed. The arrangement is characterised in that the blanking means has a leading edge (18a) which is of generally spiral shape so that the particles on the outer surface of the screen which enter the blanked-off area can reach the outer periphery (12d) of the rotating screen without being exposed to the induction pressure of the fan and hence have an improved chance of being detached from the screen.
    • 提供了用于联合收割机的散热器屏幕布置(10)。 一个屏风(12),穿过散热器的空气被风扇吸入。 旋转装置(16)用于旋转屏幕。 屏幕旋转所经过的消隐装置(18)提供了不受风扇感应压力影响的屏蔽空白区域,并且因此可以更容易地从中除去颗粒。 该装置的特征在于,冲切装置具有大致为螺旋形的前缘(18a),使得进入遮蔽区域的筛网外表面上的颗粒可以到达该遮蔽区域的外周边(12d) 旋转屏幕而不暴露于风扇的感应压力,因此具有改进的从屏幕上拆卸的机会。
    • 8. 发明申请
    • CATALYZED CO2-TRANSPORT MEMBRANE ON HIGH SURFACE AREA INORGANIC SUPPORT
    • 高表面无机载体催化二氧化碳输送膜
    • WO2011059616A1
    • 2011-05-19
    • PCT/US2010/052170
    • 2010-10-11
    • BATTELLE MEMORIAL INSTITUTELIU, Wei
    • LIU, Wei
    • B01D61/00B01D53/22B01D53/62F01N3/00F02M35/00
    • B01D61/38B01D53/228B01D69/10B01D69/105B01D2257/504B01D2258/0283H01M8/0289H01M8/0662Y02C10/04Y02C10/06Y02C10/10Y02P70/56
    • Disclosed are membranes and methods for making the same, which membranes provide improved permeability, stability, and cost-effective manufacturability, for separating CO 2 from gas streams such as flue gas streams. High CO 2 permeation flux is achieved by immobilizing an ultra-thin, optionally catalyzed fluid layer onto a meso-porous modification layer on a thin, porous inorganic substrate such as a porous metallic substrate. The CO 2 -selective liquid fluid blocks non-selective pores, and allows for selective absorption of CO 2 from gas mixtures such as flue gas mixtures and subsequent transport to the permeation side of the membrane. Carbon dioxide permeance levels are in the order of 1.0 x 10 -6 mol/(m 2 sPa) or better. Methods for making such membranes allow commercial scale membrane manufacturing at highly cost-effective rates when compared to conventional commercial- scale CO 2 separation processes and equipment for the same and such membranes are operable on an industrial use scale.
    • 公开了制备该膜的膜和方法,该膜提供改善的渗透性,稳定性和成本有效的可制造性,用于从气流如烟道气流中分离CO 2。 通过将超薄的任选催化的流体层固定在诸如多孔金属基底的薄多孔无机基底上的中孔多孔改性层上来实现高CO 2渗透通量。 CO 2选择性液体流体阻塞非选择性孔,并且允许从诸如烟道气混合物的气体混合物中选择性吸收CO 2,并且随后输送到膜的渗透侧。 二氧化碳渗透水平为1.0×10 -6 mol /(m 2 sPa)或更好的量级。 与常规的商业规模的二氧化碳分离方法相比,用于制造这种膜的方法允许以高成本有效的速率进行商业规模的膜制造,并且用于相同的膜的这种膜可以在工业用量表上操作。