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    • 3. 发明授权
    • Making discrete solid particles of polymeric material
    • 制成离散固体颗粒的聚合材料
    • US08383703B2
    • 2013-02-26
    • US12444839
    • 2007-10-04
    • Stephen Robert TennisonJonathan Robert TunbridgeRoger Nicholas PlaceOleksandr Kozynchenko
    • Stephen Robert TennisonJonathan Robert TunbridgeRoger Nicholas PlaceOleksandr Kozynchenko
    • B01F3/00
    • C08F2/18C01B32/30C01B32/336C01B32/342
    • A process is provided for producing discrete solid beads of polymeric material e.g. phenolic resin having a mesoporous structure, which process may produce resin beads on an industrial scale without aggregates of resin building up speedily and interrupting production. The process comprises the steps of: (a) combining a stream of a polymerizable liquid precursor e.g. a novolac and hexamine as cross-linking agent dissolved in a first polar organic liquid e.g. ethylene glycol with a stream of a liquid suspension medium which is a second non-polar organic liquid with which the liquid precursor is substantially or completely immiscible e.g. transformer oil containing a drying oil; (b) mixing the combined stream to disperse the polymerizable liquid precursor as droplets in the suspension medium e.g. using an in-line static mixer; (c) allowing the droplets to polymerise in a laminar flow of the suspension medium so as to form discrete solid beads that cannot agglomerate; and (d) recovering the beads from the suspension medium. Also provided is an apparatus for forming discrete solid beads of polymeric material. In other embodiments, a method is provided for carbonizing and activating carbonaceous material, and an externally fired rotary kiln for carbonizing and activating carbonaceous material.
    • 提供了一种制备聚合物材料的离散固体珠粒的方法,例如 具有中孔结构的酚醛树脂,该方法可以在工业规模上生产树脂珠而不会迅速地积聚树脂并中断生产。 该方法包括以下步骤:(a)将可聚合液体前体物流如 作为溶解在第一极性有机液体中的交联剂的酚醛清漆和六胺作为交联剂。 乙二醇与液体悬浮介质物流,液体悬浮介质是第二非极性有机液体,液体前体基本上或完全不混溶。 变压器油含有干油; (b)混合组合的流以将可聚合液体前体分散在悬浮介质中的液滴,例如 使用在线静态混合器; (c)允许液滴在悬浮介质的层流中聚合,以便形成不能聚集的不连续的固体珠粒; 和(d)从悬浮介质中回收珠粒。 还提供了一种用于形成聚合材料的离散固体珠的装置。 在其它实施方案中,提供碳化和活化碳质材料的方法,以及用于碳化和活化碳质材料的外部烧制的回转窑。
    • 4. 发明申请
    • Making Discrete Solid Particles of Polymeric Material
    • 制作聚合材料的离散固体颗粒
    • US20100086469A1
    • 2010-04-08
    • US12444839
    • 2007-10-04
    • Stephen Robert TennisonJonathan Robert TunbridgeRoger Nicholas PlaceOleksandr Kozynchenko
    • Stephen Robert TennisonJonathan Robert TunbridgeRoger Nicholas PlaceOleksandr Kozynchenko
    • C08J3/12C08J3/16C08F6/00C08J9/00B01J19/18C01B31/02
    • C08F2/18C01B32/30C01B32/336C01B32/342
    • A process is provided for producing discrete solid beads of polymeric material e.g. phenolic resin having a mesoporous structure, which process may produce resin beads on an industrial scale without aggregates of resin building up speedily and interrupting production. The process comprises the steps of: (a) combining a stream of a polymerizable liquid precursor e.g. a novolac and hexamine as cross-linking agent dissolved in a first polar organic liquid e.g. ethylene glycol with a stream of a liquid suspension medium which is a second non-polar organic liquid with which the liquid precursor is substantially or completely immiscible e.g. transformer oil containing a drying oil; (b) mixing the combined stream to disperse the polymerizable liquid precursor as droplets in the suspension medium e.g. using an in-line static mixer; (c) allowing the droplets to polymerise in a laminar flow of the suspension medium so as to form discrete solid beads that cannot agglomerate; and (d) recovering the beads from the suspension medium. Also provided is an apparatus for forming discrete solid beads of polymeric material. In other embodiments, a method is provided for carbonizing and activating carbonaceous material, and an externally fired rotary kiln for carbonizing and activating carbonaceous material.
    • 提供了一种制备聚合物材料的离散固体珠粒的方法,例如 具有中孔结构的酚醛树脂,该方法可以在工业规模上生产树脂珠而不会迅速地积聚树脂并中断生产。 该方法包括以下步骤:(a)将可聚合液体前体物流如 作为溶解在第一极性有机液体中的交联剂的酚醛清漆和六胺作为交联剂。 乙二醇与液体悬浮介质物流,液体悬浮介质是第二非极性有机液体,液体前体基本上或完全不混溶。 变压器油含有干油; (b)混合组合的流以将可聚合液体前体分散在悬浮介质中的液滴,例如 使用在线静态混合器; (c)允许液滴在悬浮介质的层流中聚合,以便形成不能聚集的不连续的固体珠粒; 和(d)从悬浮介质中回收珠粒。 还提供了一种用于形成聚合材料的离散固体珠的装置。 在其它实施方案中,提供了碳化和活化碳质材料的方法,以及用于碳化和活化碳质材料的外部烧制的回转窑。
    • 8. 发明授权
    • Fuel cell assembly
    • 燃料电池组件
    • US08318373B2
    • 2012-11-27
    • US12440691
    • 2007-09-11
    • Hanna Katariina RajantieJonathan David Brereton SharmanDavid ThompsettDavid Emmerson BrownStephen Robert TennisonBeverley SowerbyVlad Strelko
    • Hanna Katariina RajantieJonathan David Brereton SharmanDavid ThompsettDavid Emmerson BrownStephen Robert TennisonBeverley SowerbyVlad Strelko
    • H01M8/10
    • H01M8/065H01M4/8605H01M8/0232H01M8/0234H01M8/0252H01M8/026H01M8/0289H01M8/1004H01M8/1011H01M2008/1095Y02E60/523
    • An MEA comprising: (i) a central first conductive gas diffusion substrate having a first face and a second face; (ii) first and second catalyst layers each having a first and second face and wherein the first face of the first catalyst layer is in contact with the first face of the gas diffusion substrate and the first face of the second catalyst layer is in contact with the second face of the gas diffusion substrate; (iii) first and second electrolyte layers each having a first and second face and wherein the first face of the first electrolyte layer is in contact with the second face of the first catalyst layer and the first face of the second electrolyte layer is in contact with the second face of the second catalyst layer; (iv) third and fourth catalyst layers each having a first and second face and wherein the first face of the third catalyst layer is in contact with the second face of the first electrolyte layer and the first face of the fourth catalyst layer is in contact with the second face of the second electrolyte layer; and (v) first and second porous current collecting means each having a thickness of less than 400 m, and each having a first and second face and wherein the first face of the first current collecting means is in contact with the second face of the third catalyst layer and the first face of the second current collecting means is in contact with the second face of the fourth catalyst layer is disclosed and a fuel cell comprising such an MEA.
    • 一种MEA,包括:(i)具有第一面和第二面的中心第一导电气体扩散基板; (ii)第一和第二催化剂层,其各自具有第一和第二表面,并且其中第一催化剂层的第一面与气体扩散基板的第一面接触,并且第二催化剂层的第一面与 气体扩散基板的第二面; (iii)第一和第二电解质层,每个第一和第二电解质层具有第一和第二表面,并且其中第一电解质层的第一面与第一催化剂层的第二面接触,并且第二电解质层的第一面与 第二催化剂层的第二面; (iv)第三和第四催化剂层,其各自具有第一和第二表面,并且其中第三催化剂层的第一面与第一电解质层的第二面接触,并且第四催化剂层的第一面与 第二电解质层的第二面; 和(v)第一和第二多孔电流收集装置,每个具有小于400μm的厚度,并且各自具有第一和第二面,并且其中第一集电装置的第一面与第三面的第二面接触 催化剂层和第二集电装置的第一面与第四催化剂层的第二面接触,并且包括这样的MEA的燃料电池。
    • 10. 发明申请
    • Carbonising and/or Activating Carbonaceous Material
    • US20100098615A1
    • 2010-04-22
    • US12444840
    • 2007-10-04
    • Stephen Robert TennisonJonathan Robert TunbridgeRoger Nicholas PlaceAndrew John BlackburnAlan Mark Giles
    • Stephen Robert TennisonJonathan Robert TunbridgeRoger Nicholas PlaceAndrew John BlackburnAlan Mark Giles
    • C01B31/10F27B7/14
    • F27B7/167C01B32/30C01B32/336C01B32/342C01B32/39C08F2/18C10B47/30C10B53/07C10B57/12F27B7/162Y02P20/143
    • A method is provided for carbonizing and activating carbonaceous material, which comprises supplying the material to an externally fired rotary kiln maintained at carbonizing and activating temperatures, the kiln having a downward slope to progress the material as it rotates, the kiln having an atmosphere substantially free of oxygen provided by a counter-current of steam or carbon dioxide, and annular weirs being provided at intervals along the kiln to control progress of the material. There may further be provided an externally fired rotary kiln for carbonizing and activating carbonaceous material having a hollow rotary body that has a downward slope towards a discharge end thereof, and which is provided at intervals along its length with annular weirs for controlling progress of the carbonaceous material. In embodiments, there is also provided a process is for producing discrete solid beads of polymeric material e.g. phenolic resin beads having a mesoporous structure, which may be useful as feedstock for the above mentioned carbonization/activation process or which may have other utility e.g. as ion exchange resins. The process may produce resin beads on an industrial scale without aggregates of resin building up speedily and interrupting production. The process comprises the steps of: (a) combining a stream of a polymerizable liquid precursor e.g. a novolac and hexamine as cross-linking agent dissolved in a first polar organic liquid e.g. ethylene glycol with a stream of a liquid suspension medium which is a second non-polar organic liquid with which the liquid precursor is substantially or completely immiscible e.g. transformer oil containing a drying oil; (b) mixing the combined stream to disperse the polymerizable liquid precursor as droplets in the suspension medium e.g. using an in-line static mixer; (c) allowing the droplets to polymerise in a laminar flow of the suspension medium so as to form discrete solid beads that cannot agglomerate; and (d) recovering the beads from the suspension medium. There is also provided apparatus for forming discrete solid beads of polymeric material, said apparatus comprising: a first line for conveying s stream of a polymerizable liquid precursor; a second line for conveying a stream of a dispersion medium with which the polymerizable liquid precursor is substantially or completely immiscible; an in-line mixer configured to receive a combined flow from the first and second lines and to disperse the polymerizable liquid precursor as droplets in the dispersion medium; a vertical polymerization column configured to receive the dispersion medium with the droplets dispersed therein and to permit the polymerizable liquid precursor polymerize while descending the column in a descending flow of polymerization medium; and a vessel at the base of the column for receiving the descending flow of dispersion medium and collecting polymerized solid beads.