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    • 12. 发明申请
    • PROCESS FOR MAKING ANHYDROUS MAGNESIUM CHLORIDE
    • 制造无水氯化镁的方法
    • WO1994022763A1
    • 1994-10-13
    • PCT/CA1994000191
    • 1994-04-06
    • ALCAN INTERNATIONAL LIMITED
    • ALCAN INTERNATIONAL LIMITEDSIVILOTTI, Olivo, GiuseppeSANG, Jean, VictorLEMAY, Réjean, Joseph, Roger
    • C01F05/34
    • C01F5/34C01F5/30C01P2006/80
    • The invention relates to a process for producing anhydrous magnesium chloride involving the following combination of steps: drying impure salt containing hydrated magnesium chloride; establishing a solution of the hydrated magnesium chloride; removing insoluble impurities; reacting the solution of hydrated magnesium chloride at substantially ambient pressure and at a temperature between 10 DEG and 60 DEG C by feeding it into an ammonia saturated very low boiling point alcohol solution and in the presence of ammonium chloride while maintaining the last-mentioned solution saturated in ammonia thereby to form a precipitate of ammoniated magnesium chloride; separating the precipitate and heating it to obtain anhydrous MgCl2 and ammonia for recycling. The process can result in the production of very pure anhydrous mangesium chloride suitable, for example, for the production of metallic magnesium.
    • 本发明涉及一种生产无水氯化镁的方法,涉及以下组合步骤:干燥含有水合氯化镁的不纯盐; 建立水合氯化镁的溶液; 去除不溶性杂质; 在大约环境压力和10至60℃的温度下,将水合氯化镁溶液加入氨饱和非常低沸点的醇溶液中,并在氯化铵存在下,同时保持最后提到的溶液饱和 在氨中形成氨化氯化镁的沉淀物; 分离沉淀并加热,得到无水MgCl 2和氨回收。 该方法可以产生非常纯的无水氯化锰氯化物,其适用于例如用于生产金属镁。
    • 13. 发明申请
    • FLUID STORAGE
    • 流体储存
    • WO1994004433A1
    • 1994-03-03
    • PCT/GB1993001805
    • 1993-08-24
    • ALCAN INTERNATIONAL LIMITEDGRAY, AlanADAMS, Barry
    • ALCAN INTERNATIONAL LIMITED
    • B65D79/00
    • B65D85/73
    • A capsule (100) comprising upper (101) and lower (102) parts each having a dished formation (105, 106) and a peripheral rim, the rims being secured together so that the formations (105, 106) are at least partially in register with one another to provide at least one vented chamber (100a), means in at least one of the parts (101, 102) to communicate between the interior of the chamber (100a) and the exterior thereof and the lower part (102) having its exterior so formed as to enable it to be held in stable engagement with a surface but so that a fluid may pass freely between those parts (101, 102) of the exterior of the lower part (102) and the surface that are not in intimate engagement.
    • 一种胶囊(100),包括上部(101)和下部(102),每个部分具有盘形结构(105,106)和周边边缘,所述轮缘固定在一起,使得所述结构(105,106)至少部分地位于 彼此对准以提供至少一个排气室(100a),在至少一个部件(101,102)中的装置,用于在室(100a)的内部和其外部与下部(102)之间连通, 其外部形成为使得其能够保持与表面的稳定接合,但是使得流体可以在下部(102)的外部的那些部分(101,102)和不在下部的表面之间自由地通过 亲密接触
    • 15. 发明申请
    • PROCESS FOR THE EXTRACTION OF ALUMINA
    • 提取氧化铝的方法
    • WO1993022238A1
    • 1993-11-11
    • PCT/EP1993000999
    • 1993-04-26
    • ALCAN INTERNATIONAL LIMITEDALUMINA ESPANOLA S.A.ALVARADO-CENDAN, Jose ManuelVERGHESE, Kachappillil, Ittoop
    • ALCAN INTERNATIONAL LIMITEDALUMINA ESPANOLA S.A.
    • C01F07/06
    • C01F7/062
    • This invention relates to a process for the extraction of alumina from alumina-containing solid material, particularly the alumina-containing ores known as bauxite. The process comprises: a) providing the material in the form of a slurry (101) in an alkaline solution having a concentration of free caustic therein sufficient at the temperature reached in step (c) to dissolve alumina values, b) classifying (6) the slurry into a fine particle fraction and a coarse particle fraction, c) heating the fine particle fraction (105) to a temperature sufficient to dissolve at least some of the alumina values therein with consequential reduction in the free caustic concentration in the liquid phase of the fine fraction slurry, and d) combining the coarse particle fraction (109) from step (b) with the free caustic-depleted slurry liquid from step (c) at a temperature higher than that reached in the step (c) so as to dissolve at least some of the alumina values in the coarse particle fraction.
    • 本发明涉及从含氧化铝的固体材料,特别是称为铝土矿的含氧化铝矿石中提取氧化铝的方法。 该方法包括:a)以在步骤(c)中达到的温度足够的碱性溶液在碱性溶液中提供浆料(101)形式的材料以溶解氧化铝值,b)分级(6) 将浆料分散成细颗粒部分和粗颗粒部分,c)将细颗粒部分(105)加热到足以溶解至少一些氧化铝值的温度,从而降低液相中的游离碱浓度 所述细级浆料,和d)在步骤(c)中将步骤(b)的粗颗粒组分(109)与步骤(c)中的游离苛性碱贫化浆液以高于步骤(c)中达到的温度混合, 溶解粗颗粒部分中的至少一些氧化铝值。
    • 19. 发明申请
    • HYDROGEN REMOVAL SYSTEM FOR METAL/AIR FUEL CELL
    • 用于金属/空气燃料电池的氢去除系统
    • WO1993007652A1
    • 1993-04-15
    • PCT/CA1992000429
    • 1992-09-29
    • ALCAN INTERNATIONAL LIMITED
    • ALCAN INTERNATIONAL LIMITEDLAPP, Steven, P.
    • H01M12/06
    • H01M2/40H01M10/52H01M12/065
    • A metal/air fuel cell is described in which hydrogen is effectively removed from a cell stack and electrolyte storage tank without emitting caustic vapour or mist. The fuel cell comprises: (a) a fuel cell assembly housing, (b) a plurality of metal/air cells disposed in the housing, (c) an electrolyte storage tank, (d) a recirculation loop for continuously recirculating electrolyte from the storage tank through the metal/air cells, (e) air injection means for flowing air between the metal/air cells, (f) a degassing vessel connected to the recirculating loop to receive electrolyte containing hydrogen gas from the metal/air cells, the vessel being arranged to discharge hydrogen gas through a top opening and discharge electrolyte through a bottom outlet for return to the storage tank and this vessel being further arranged to have at least the top portion thereof bathed in air which has passed between the metal/air cells, (g) purging air means adapted to pass air through the electrolyte storage tank and then through the degassing vessel, said purging air serving to dilute the hydrogen and to remove hydrogen from the storage tank, (h) a gas discharge conduit for drawing off purge air and hydrogen discharging from the degassing vessel and (i) filter means connected to said discharge conduit for removing caustic vapour or mist from the discharging purge air and hydrogen.
    • 20. 发明申请
    • PROCESS FOR PRODUCING SILICON CARBIDE PLATELETS AND THE PLATELETS SO PRODUCED
    • 生产碳化硅钢板和生产的钢板的方法
    • WO1993002232A1
    • 1993-02-04
    • PCT/CA1992000302
    • 1992-07-15
    • ALCAN INTERNATIONAL LIMITED
    • ALCAN INTERNATIONAL LIMITEDPARENT, Luc
    • C30B25/00
    • C30B25/00C01B32/956C01P2004/03C01P2004/20C01P2004/54C01P2004/61C01P2006/80C01P2006/90C30B25/005C30B29/36
    • The invention provides a process for producing silicon carbide platelets of low iron content preferably having a size of 20 x 10 cm [20 mu m] or less, and the platelets so produced. The process comprises reacting particles of carbon from a source containing less than 0.2 % by weight of iron, with silica or a silica precursor at a temperature in the range of 1800-2100 DEG C under an inert atmosphere in the presence of 0.2-10 % by weight of an oxide or oxide precursor of Ca, Mg, Al, W, Ce or Cu; 0.1-10 % by weight of boron, relative to the weight of SiO2, and preferably 0.1-10 % by weight of the reaction mixture of alpha silicon carbide particles having a size of 5 x 10 cm [5 mu m] or less. The carbon is preferably in the form of particles of less than 50 x 10 cm [50 mu m] and the silica or precursor is preferably in the form of particles of less than about 45 x 10 cm [45 mu m]. The weight ratio of silica to carbon is greater than 1.76:1. The carbon source is preferably a pure form of carbon, e.g. graphite or amorphous carbon. The resulting small SiC platelets are substantially unagglomerated, have a high percentage (up to 95 %) of small (less than 20 x 10 cm [
    • 本发明提供了一种生产低铁含量的碳化硅小片的方法,其优选具有20×10 -4 cm 2或更小的尺寸,以及如此制备的血小板。 该方法包括在惰性气氛下,在0.2-10%(重量)的范围内,在1800-2100℃的温度下,将来自含有少于0.2重量%铁的源的二氧化硅或二氧化硅前体的碳颗粒反应, 重量的Ca,Mg,Al,W,Ce或Cu的氧化物或氧化物前体; 0.1-10重量%的硼,相对于SiO 2的重量,优选0.1-10重量%的尺寸为5×10 -4 cm 3的α碳化硅颗粒的反应混合物, 或更少。 碳优选为小于50×10 -4 cm 2的颗粒形式,并且二氧化硅或前体优选为小于约45×10 -4 cm 2的颗粒形式, 45亩]。 二氧化硅与碳的重量比大于1.76:1。 碳源优选为纯形式的碳,例如。 石墨或无定形碳。 所得到的小SiC片晶体基本上是未凝聚的,具有高(小于20×10 -4 cm [<20μm])小片的高百分比(高达95%),优选具有大于5的纵横比。 血小板可用作陶瓷,金属和聚合物基质材料的增强剂。