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    • 4. 发明授权
    • Chemical conversion in presence of nuclear fission fragements
    • 存在核裂变的化学转化
    • US3228850A
    • 1966-01-11
    • US2412660
    • 1960-04-22
    • SOCONY MOBIL OIL CO INC
    • FELLOWS ALBERT T
    • B01J19/08B01J37/34C01B3/34C01B32/40C01C1/04C07C2/00C07C5/27C07C51/353C10G15/10C10G35/16C10G49/00G21C3/04G21C3/06G21C3/28G21C3/62G21C3/64G21C9/00G21D9/00
    • G21D9/00B01J19/081B01J37/34C01B3/342C01B32/40C01C1/0494C07C2/00C07C5/27C07C51/353C10G15/10C10G35/16C10G49/00C10G49/002G21C3/044G21C3/06G21C3/28G21C3/626G21C3/64G21C9/00Y02E30/37Y02E30/38Y02P20/582Y10S204/90Y10S204/904Y10S204/905Y10S376/901Y10S376/903Y10S376/904C07C55/02
    • 970, 864. Reactors. SOCONY MOBIL OIL CO. Inc. Oct.28, 1960 [Oct.29, 1959; Oct. 30, 1959; April 22, 1960 (3)]. No. 37213/60. Heading G6C. In a nuclear reactor, the recoil energy of nuclear fission fragments is used to effect chemical reactions. The fission process may be either sustained by an external neutron source or be selfsustaining. The fission fragments are retained within the reactor to prevent contamination of the chemical conversion products. Temperature control of the process is effected either by the circulation of a coolent or by the removal of heat by the flow of the chemical reactants. The latter may act as a moderator for the fission process or a solid moderator may be introduced. As shown, Fig. 1, the vessel 10 contains a non-self-sustaining reactor for effecting the required chemical reaction on the fluids passed through the vessel by the pipes 66, 67. To maintain fission reaction, reactors are supplied from an outside source, not shown. Fluid chemical conversion products are passed from separator 68 to heat exchanger 78 to recovery system 83 from which the reactants are recycled by pump 65. The bars 100 in 10 may consist of enriched uranium oxide contained in particles of microporous alumina. Reactant hydrogen and the alumina functions as a moderator but carbon particles may be added. A coolant fluid is circulated round the space 25, for example, heavy water, molten bismuth or sodium, biphenyl, or a mixture of sodium nitrate, sodium nitrite and potassium nitrate. The fluid is passed through the heat exchanger 29 by the pump 28. The fission material is supplied from hopper 35 and passes the concrete shield 23, steel sheet 22 and graphite blocks 12 by conduit 34. Discharge is effected through 46 to the tank 47. Lock chambers 53, 90 are filled with an inert gas such as helium, carbon dioxide. The neutron flux in vessel 10 is controllable by the rods 111, 112 of boron or cadmium. The alumina particles are arranged so as to retain the fission fragments within the body of each particle and the gaseous fragments diffuse out. The particles are porous and may also be formed of siliceous earth, ceramic materials in gels of silica..The capture cross-section of the particles for thermal neutrons is below 10 barns and a catalyst may be added such as platinum or nickel. In a second embodiment, not shown, the fission reaction is self sustaining. The fluids to be reacted upon by the neutron flux pass downwards through the fission material to permit a higher velocity through the device without disturbance of the fission material. Control may be effected by adjustable rods of fissionable material. Examples of the chemical reactions effected by the arrangement and the conversion of methanol to diethylene glycol, ethanolhexane to butanediols, nitrogen and oxygen to their oxides, nitrogen and hydrogen to ammonia, carbon monoxide and hydrogen to methane, methane to hydrogen. In addition dehydrogenation, aromatization and dealkylation of hydrocarbons may be effected. U.S.A Specifications 2,384,941, 2,580,429, 2,580,806 and 2,856,367 are referred to.
    • 7. 发明授权
    • Liquid fuel reforming apparatus
    • 液体燃料重整装置
    • US5752157A
    • 1998-05-12
    • US662239
    • 1996-06-14
    • Takeshi YamashitaHiro Yamashita
    • Takeshi YamashitaHiro Yamashita
    • C10G32/02C10G35/16C10L1/00F02M27/04F23K5/08B01J19/08
    • F02M27/04C10G35/16
    • A liquid fuel reforming apparatus comprising a bobbin main body containing a fuel passage through which a liquid fuel such as gasoline and a combustible gas passes; a coil having a predetermined number of winding formed around the bobbin main body; and a multi-faced magnetic metal material sealed in the fuel passage, which permits passage of the liquid fuel being brought into contact therewith; wherein the liquid fuel is adapted to be reformed by applying a predetermined voltage across the coil to induce a magnetic field and effect magnetization of the multi-faced magnetic metal material contained in the fuel passage and by allowing the liquid fuel to flow through the fuel passage in contact with the magnetized multi-faced magnetic metal material. The multi-faced magnetic metal material may be replaced with a multi-faced material of an amorphous metal alloy.
    • 一种液体燃料重整装置,包括:筒管主体,其包含燃料通道,液体燃料如汽油和可燃气体通过该通道; 具有绕线轴主体形成的预定数量的绕组的线圈; 以及密封在所述燃料通道中的多面磁性金属材料,其允许与其接触的液体燃料通过; 其中所述液体燃料适于通过在所述线圈上施加预定电压而被重整,以引起磁场并且影响包含在所述燃料通道中的所述多面磁性金属材料的磁化,并且允许所述液体燃料流过所述燃料通道 与磁化的多面磁性金属材料接触。 多面磁性金属材料可以用非晶态金属合金的多面材料代替。
    • 8. 发明授权
    • Electrical device for conversion of molecular weights using dynodes
    • 使用倍增极转换分子量的电气设备
    • US5141715A
    • 1992-08-25
    • US682386
    • 1991-04-09
    • William M. SackingerBrian L. MorganRobert W. Airey
    • William M. SackingerBrian L. MorganRobert W. Airey
    • B01J19/08C07C2/80C10G35/16
    • B01J19/088
    • An electrical device is provided for the conversion of molecules of one molecular weight into molecules of another molecular weight. A reaction chamber comprises an array of dynodes, each of which possesses a plurality of apertures. External voltages are available which are applied between dynodes, producing an electric field. During operation, electrons and ions strike the interior surfaces of the dynode apertures, ionizing neutral molecules absorbed on the surfaces, which are desorbed by the energy of the impact, and which are accelerated by the electric field to a new dynode surface location, where they combine with absorbed molecules there to form a variety of new, larger molecules, or different, smaller molecules. Certain ones of the ions created are repetitively moved to one end of the device, where they may be pumped away separately. The controlled electron and ion impact ionization in the device can also produce reactions among several molecular species which would be unlikely or impossible under normal chemical equilibrium conditions, or with normal catalysts.
    • 提供电子装置用于将一个分子量的分子转化成另一个分子量的分子。 反应室包括一组倍增极,每个具有多个孔。 外部电压可用于倍增电极之间,产生电场。 在操作期间,电子和离子撞击倍增极孔的内表面,电离中性分子吸收在表面上,这些分子被冲击的能量解吸,并被电场加速到新的倍增极面位置, 与吸收的分子结合形成各种新的,更大的分子或不同的较小的分子。 产生的某些离子被重复地移动到装置的一端,在那里它们可被单独泵送。 器件中受控的电子和离子冲击电离还可以在几种分子物质之间产生反应,这在常规化学平衡条件下或与正常催化剂不太可能或不可能。
    • 10. 发明授权
    • Utilization of nuclear fission for chemical reactions
    • 利用核裂变进行化学反应
    • US3228849A
    • 1966-01-11
    • US2412460
    • 1960-04-22
    • SOCONY MOBIL OIL CO INC
    • FELLOWS ALBERT T
    • B01J19/08B01J37/34C01B3/34C01B32/40C01C1/04C07C2/00C07C5/27C07C51/353C10G15/10C10G35/16C10G49/00G21C3/04G21C3/06G21C3/28G21C3/62G21C3/64G21C9/00G21D9/00
    • G21D9/00B01J19/081B01J37/34C01B3/342C01B32/40C01C1/0494C07C2/00C07C5/27C07C51/353C10G15/10C10G35/16C10G49/00C10G49/002G21C3/044G21C3/06G21C3/28G21C3/626G21C3/64G21C9/00Y02E30/37Y02E30/38Y02P20/582Y10S204/90Y10S204/904Y10S204/905Y10S376/901Y10S376/903Y10S376/904C07C55/02
    • 970, 864. Reactors. SOCONY MOBIL OIL CO. Inc. Oct.28, 1960 [Oct.29, 1959; Oct. 30, 1959; April 22, 1960 (3)]. No. 37213/60. Heading G6C. In a nuclear reactor, the recoil energy of nuclear fission fragments is used to effect chemical reactions. The fission process may be either sustained by an external neutron source or be selfsustaining. The fission fragments are retained within the reactor to prevent contamination of the chemical conversion products. Temperature control of the process is effected either by the circulation of a coolent or by the removal of heat by the flow of the chemical reactants. The latter may act as a moderator for the fission process or a solid moderator may be introduced. As shown, Fig. 1, the vessel 10 contains a non-self-sustaining reactor for effecting the required chemical reaction on the fluids passed through the vessel by the pipes 66, 67. To maintain fission reaction, reactors are supplied from an outside source, not shown. Fluid chemical conversion products are passed from separator 68 to heat exchanger 78 to recovery system 83 from which the reactants are recycled by pump 65. The bars 100 in 10 may consist of enriched uranium oxide contained in particles of microporous alumina. Reactant hydrogen and the alumina functions as a moderator but carbon particles may be added. A coolant fluid is circulated round the space 25, for example, heavy water, molten bismuth or sodium, biphenyl, or a mixture of sodium nitrate, sodium nitrite and potassium nitrate. The fluid is passed through the heat exchanger 29 by the pump 28. The fission material is supplied from hopper 35 and passes the concrete shield 23, steel sheet 22 and graphite blocks 12 by conduit 34. Discharge is effected through 46 to the tank 47. Lock chambers 53, 90 are filled with an inert gas such as helium, carbon dioxide. The neutron flux in vessel 10 is controllable by the rods 111, 112 of boron or cadmium. The alumina particles are arranged so as to retain the fission fragments within the body of each particle and the gaseous fragments diffuse out. The particles are porous and may also be formed of siliceous earth, ceramic materials in gels of silica..The capture cross-section of the particles for thermal neutrons is below 10 barns and a catalyst may be added such as platinum or nickel. In a second embodiment, not shown, the fission reaction is self sustaining. The fluids to be reacted upon by the neutron flux pass downwards through the fission material to permit a higher velocity through the device without disturbance of the fission material. Control may be effected by adjustable rods of fissionable material. Examples of the chemical reactions effected by the arrangement and the conversion of methanol to diethylene glycol, ethanolhexane to butanediols, nitrogen and oxygen to their oxides, nitrogen and hydrogen to ammonia, carbon monoxide and hydrogen to methane, methane to hydrogen. In addition dehydrogenation, aromatization and dealkylation of hydrocarbons may be effected. U.S.A Specifications 2,384,941, 2,580,429, 2,580,806 and 2,856,367 are referred to.