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    • 1. 发明申请
    • CHEMO-ELECTRIC CELL WITH AT LEAST ONE GAS ELECTRODE
    • 具有至少一个气体电极的化学电池
    • WO1984002429A1
    • 1984-06-21
    • PCT/SE1983000434
    • 1983-12-07
    • AB OLLE LINDSTRÖMLINDSTRÖM, Olle
    • AB OLLE LINDSTRÖM
    • H01M08/02
    • H01M4/8626C25B1/46C25B9/06H01M8/00H01M10/4214H01M12/00
    • With known gas electrodes for fuel cells, metal/air cells etc. the gaseous reactant is transported to the reaction sites in the electrode by diffusion. These electrodes are named gas diffusion electrodes. The invention is a further development of gas electrodes with integrated gas and electrolyte chambers whereby the diffusion process is replaced by a convection process. The new gas convection electrode is furnished with means for forced transport of gas from an upstream chamber (11) through the active part of the electrode (9) to a downstream chamber (12). One or both sides of the electrode is at the same time in contact with the electrolyte in bipolar or monopolar embodiments. A selective gas permeable membrane (36) on the upstream side of the electrodes is used in one embodiment in order to separate non-desirable components present in the reaction gas.
    • 使用已知的燃料电池气体电极,金属/空气电池等,气态反应物通过扩散传输到电极中的反应部位。 这些电极称为气体扩散电极。 本发明是具有集成气体和电解质室的气体电极的进一步发展,由此扩散过程被对流过程替代。 新的气体对流电极装备有用于将气体从上游室(11)强制输送通过电极(9)的有源部分到下游室(12)的装置。 在双极或单极实施例中,电极的一侧或两侧同时与电解质接触。 在一个实施方案中,在电极的上游侧使用选择性气体渗透膜(36),以分离存在于反应气体中的不希望的组分。
    • 2. 发明申请
    • CHEMOELECTRIC CELL WITH FUEL CONTAINER
    • 带燃料容器的电解槽
    • WO1990014694A1
    • 1990-11-29
    • PCT/SE1990000319
    • 1990-05-14
    • AB OLLE LINDSTRÖMLINDSTRÖM, Olle
    • AB OLLE LINDSTRÖM
    • H01M08/06
    • H01M8/08H01M8/2455
    • Fuel cells with alkaline electrolyte may subject liquid fuels like methanol and glycol to ''cold combustion'' at comparatively high power densities. The acid reaction products produced from the fuel dissolved in the electrolyte, however, neutralize the electrolyte so as to impair its function. The cell according to the invention is furnished with a separate container (5) for an aqueous phase containing the fuel. This aqueous phase also contains a base for neutralization of the acid reaction products. The cold combustion is taking place in a ''cell-sandwich'' (1) comprising a hydrophobic air cathode, an electrolyte consisting of an alkali hydroxide in an aqueous solution which is contained in a microporous separator (3) and the fuel anode (4). One side of the fuel anode (4) is in direct contact with the separator (4). The other side of the fuel anode is in direct contact with the aqueous phase in the container (5).
    • 具有碱性电解质的燃料电池可以使液体燃料如甲醇和二醇在相当高的功率密度下“冷却”。 然而,从溶解在电解质中的燃料产生的酸反应产物中和电解质以损害其功能。 根据本发明的电池具有用于含有燃料的水相的单独的容器(5)。 该水相还含有用于中和酸反应产物的碱。 冷燃烧是在包含疏水性空气阴极的电池 - 三明治(1)中进行的,包含在微孔隔板(3)和燃料阳极(3)中的水溶液中由碱金属氢氧化物组成的电解质 4)。 燃料阳极(4)的一侧与分离器(4)直接接触。 燃料阳极的另一侧与容器(5)中的水相直接接触。
    • 4. 发明申请
    • CATALYTICALLY ACTIVE MATERIAL
    • 催化活性材料
    • WO1989009650A1
    • 1989-10-19
    • PCT/SE1989000184
    • 1989-04-06
    • AB OLLE LINDSTRÖMLINDSTRÖM, Olle
    • AB OLLE LINDSTRÖM
    • B01J21/18
    • B01J37/084B01J21/18
    • The green parts of living plants, here called phytobiomass, maintain through photosynthesis life on earth. Chlorophyll is a protein which collects energy from the sunshine required for the synthesis of to begin with carbohydrates from carbon dioxide and water. The phytobiomass also contains transport paths for reactants, intermediates and end-products. Chlorophyll or phytobiomass can according to the invention after pyrolysis be used as catalytically active materials for chemical and electrochemical processes. The catalytical activity of these abundant and very cheap materials is in certain applications on the same level as of the noble metal catalysts. Typical applications are as catalytically active materials for air electrodes for fuel cells or for denitrification of flue gases.
    • 活植物的绿色部分,这里称为植物生物量,通过光合作用在地球上保持生命。 叶绿素是从二氧化碳和水合成碳水化合物所需的阳光中收集能量的蛋白质。 植物生物量还包含反应物,中间体和终产物的转运途径。 热解后,根据本发明的叶绿素或植物生物量可用作化学和电化学方法的催化活性材料。 这些丰富且非常便宜的材料的催化活性在某些应用中与贵金属催化剂的水平相同。 典型应用是用于燃料电池的空气电极或烟道气脱氮的催化活性材料。
    • 5. 发明申请
    • BURNER FOR WOOD LOGS
    • 燃烧器木材日志
    • WO1989005424A1
    • 1989-06-15
    • PCT/SE1988000666
    • 1988-12-07
    • AB OLLE LINDSTRÖMLINDSTRÖM, Olle
    • AB OLLE LINDSTRÖM
    • F24B01/193
    • F24B1/193F23G5/42F23H13/02
    • The burner is intended for combustion of wood logs or other similar solid fuels. The burner which will be called the basket burner is shaped as an open inclined basket (1) comprising a bottom plate (3) and a backing plate (4) which are inclined towards the horizontal plane, respectively the vertical plane, so that the connection between the bottom plate and the backing plate constitutes the lowest part of the basket. The backing plate forms a chute or hold for the package of wood logs. The two plates contain holes for air. The fuel is piled up against the backing plate and is supported by the bottom plate so as to form a compact bundle of parallel wood logs with minimized surface/volume ratio. The design of the basket burner makes the wood logs serve as efficient supporting burners for each other. Thanks to the shape of the basket burner the burning wood logs are successively brought towards each other and towards the lowest part of the basket burner during the combustion. At the end of the combustion there remains an upright layer of burning char which radiates heat towards the space in front of the fireplace which facilitates rapid lighting of a new charge of wood.
    • 燃烧器用于木材原木或其他类似固体燃料的燃烧。 将被称为筐式燃烧器的燃烧器成形为包括分别垂直于水平面倾斜的底板(3)和背板(4)的开放倾斜篮(1),使得连接 在底板和背板之间构成篮子的最低部分。 背板形成用于木材原木包装的滑槽或保持架。 两个板包含空气孔。 燃料堆积在背板上并由底板支撑,以形成具有最小表面/体积比的平行木材原木的紧密束。 篮式燃烧器的设计使木材作为相互有效的支撑燃烧器。 由于篮式燃烧器的形状,燃烧的木材在燃烧期间相继地朝向篮子燃烧器的最低部分。 在燃烧结束时,仍然有一个直立的燃烧焦炭层,向壁炉前面的空间辐射热量,这有助于快速照亮新的木材。
    • 6. 发明申请
    • GASIFIER
    • 气化炉
    • WO1994026849A1
    • 1994-11-24
    • PCT/SE1994000420
    • 1994-05-06
    • AB OLLE LINDSTRÖMLINDSTRÖM, Olle
    • AB OLLE LINDSTRÖM
    • C10J03/02
    • C10J3/26C10J3/02C10J2300/0913C10J2300/0956
    • Gasification of biofuels to a fuel gas with a high calorific value is taking place in at least two steps. One step is carried out in counter-current with the pre-pyrolysis for release of carbon dioxide. A second step with complete gasification is carried out in co-current. The gasifier, which can be called the counter-current/co-current gasifier, is supplied with a second counter-current section (3) for pre-pyrolysis with conduits (8 and 9) for supply and removal, respectively, of gas and a co-current section (5) for final gasification with a conduit (10) for gasification air and a conduit (11) for removal of fuel gas.
    • 将生物燃料气化成具有高热值的燃料气体至少在两个步骤中进行。 一步一步地与用于释放二氧化碳的预热解反向进行。 完成气化的第二步是并流进行。 可以称为逆流/并流气化器的气化器被提供有用于预热解的第二逆流段(3),其中管道(8和9)分别用于气体和/ 用于最终气化的用于气化空气的导管(10)和用于除去燃料气体的导管(11)的并流部分(5)。