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1. 发明授权

US4532112A Process for producing antimony trioxide having a low alpha-ray strength 失效
标题翻译：具有低α射线强度的生产三氧化锑的方法
公开(公告)号：US4532112A
公开(公告)日：1985-07-30
申请号：US612256
申请日：1984-05-21
申请人： Hiroshi Nakahira , Shigeki Kubo
发明人： Hiroshi Nakahira , Shigeki Kubo
IPC分类号： C08K3/00 , C01G30/00 , C01G49/06 , C08K3/22 , H01L23/556 , C01G
CPC分类号： H01L23/556 , C01G30/005 , C01P2004/61 , H01L2924/0002
摘要： At least an equivalent amount of concentrated hydrochloric acid is added to antimony trioxide containing a substance emitting alpha rays, and they are stirred. Any undissolved residue is removed to prepare an aqueous solution of antimony chloride. Water is added to the solution, or a distillate obtained by distilling it at a temperature of at least 135.degree. C. The quantity of the water is at least 10 times by volume as much as the solution, or at least 20 times by volume as much as the distillate. The solution or distillate and the water are stirred at a temperature of at least 60.degree. C. to cause precipitation of antimony trioxide, and the precipitate is separated by filtration. The precipitate is washed with at least 10 times by weight as much warm water having a temperature of 60.degree. C., and dried. This antimony trioxide has an alpha-ray strength not exceeding 0.01 C/cm.sup.2 per hour, does not contain more than 1 ppm of any impurities such as arsenic, lead or soluble chlorine, and has a large average particle size.
摘要翻译：将至少等量的浓盐酸加入到含有发射α射线的物质的三氧化锑中，并搅拌它们。除去任何未溶解的残余物以制备氯化锑水溶液。将水加入到溶液中，或通过在至少135℃的温度下蒸馏得到的馏出物。水的量为溶液的至少10倍体积，或至少20体积％就像馏出物一样。将溶液或馏出物和水在至少60℃的温度下搅拌，以使三氧化锑沉淀，并通过过滤分离沉淀物。用至少10倍重量的温度为60℃的温水洗涤沉淀物并干燥。该三氧化锑的α射线强度不超过0.01C / cm 2 /小时，不含有砷，铅或可溶性氯等杂质的1ppm以上，平均粒径大。

2. 发明授权

US4675171A Production of finely-divided particulate bismuth oxide 失效
标题翻译：细碎的颗粒状氧化铋的生产
公开(公告)号：US4675171A
公开(公告)日：1987-06-23
申请号：US805098
申请日：1985-12-05
申请人： Shigeki Kubo , Osamu Yamamoto
发明人： Shigeki Kubo , Osamu Yamamoto
IPC分类号： B01J12/02 , B22F9/12 , C01B13/20 , C01B19/00 , C01G29/00 , C01B27/00
CPC分类号： C01B19/004 , B01J12/02 , B22F9/12 , C01B13/20 , C01G29/00 , C01P2004/32 , C01P2004/61 , C01P2004/62
摘要： Finely-divided particulate bismuth oxide is produced by the steps of heating bismuth at 800.degree. C. or above in a first compartment of a sealed vessel divided into two compartments by a partition wall, the two compartments communicating with each other by a hole provided on the partition wall, feeding an inert gas such as nitrogen and argon into the first compartment so that the bismuth vapor formed by heating bismuth has a bismuth concentration of 0.1 to 0.5 g/liter, blowing air into the bismuth vapor introduced from the first compartment into the second compartment through the hole on the partition wall, permitting the air to mix with the bismuth vapor to form bismuth oxide and simultaneously cooling the thus formed bismuth oxide to 250.degree. to 300.degree. C., discharging by suction the bismuth oxide from the sealed vessel at a flow rate of 1 to 5 m/sec, and cooling the discharged bismuth oxide by supplying cooling air outside the sealed vessel.
摘要翻译：精细分散的颗粒状氧化铋是通过以下步骤制造的：通过在分隔壁分成两个隔室的密封容器的第一隔室中将800℃或更高的铋加热的步骤，两个隔室通过设置在分隔壁将氮气和氩气等惰性气体供给到第一隔室，使得通过加热铋形成的铋蒸气的铋浓度为0.1〜0.5g / l，将空气吹入从第一隔室引入的铋蒸气第二隔室通过分隔壁上的孔，允许空气与铋蒸气混合以形成氧化铋，同时将由此形成的氧化铋冷却至250℃至300℃，通过从密封的氧化铋中抽出氧化铋容器，以1〜5m /秒的流速，通过在密封容器外部供给冷却空气来冷却排出的氧化铋。

3. 发明授权

US07332248B2 Active material for positive electrode for non-aqueous electrolyte secondary battery and method of manufacturing the same 有权
标题翻译：非水电解质二次电池用正极活性物质及其制造方法
公开(公告)号：US07332248B2
公开(公告)日：2008-02-19
申请号：US10739269
申请日：2003-12-19
申请人： Katsuya Kase , Shigeki Kubo , Hirofumi Iisaka , Ko Nozaki , Satoru Suzuki , Manabu Yamada
发明人： Katsuya Kase , Shigeki Kubo , Hirofumi Iisaka , Ko Nozaki , Satoru Suzuki , Manabu Yamada
IPC分类号： H01M4/58
CPC分类号： H01M4/525 , C01G53/42 , C01P2002/52 , C01P2002/88 , C01P2004/61 , C01P2006/40 , C01P2006/82 , H01M4/131 , H01M4/485 , H01M10/052 , H01M2004/021
摘要： A method of manufacturing a non-aqueous electrolyte secondary battery is provided wherein the positive electrode is made from a lithium-metal composite oxide represented by the general formula Lix(Ni1-y, Coy)1-zMzO2 (0.98≦x≦1.10, 0.05≦y≦0.4, 0.01≦z≦0.2, in which M represents at least one element selected from the group consisting of Al, Mg, Mn, Ti, Fe, Cu, Zn and Ga), and having an average particle diameter of 5 μm to 10 μm a C-amount of 0.14 wt % or less measured by way of the high-frequency heating-IR absorption method, and a Karl Fischer moisture content of 0.2 wt % or less when heated to 180° C. and the method comprising the steps of applying a paste of active material for positive electrode to electrode plate to make an electrode, then drying the electrode, and pressing and then installing the electrode in a battery, in a work atmosphere having an absolute moisture content of 10 g/m3 or less.
摘要翻译：提供一种制造非水电解质二次电池的方法，其中正极由通式为Li x-x（Ni 1-y）表示的锂金属复合氧化物制成， O> O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O，，，，，，， 0.05≤y≤0.4,0.01≤z≤0.2，其中M表示选自Al，Mg，Mn，Ti，Fe，Cu，Zn和Ga中的至少一种元素），并且具有通过高频加热 - 红外吸收法测定的平均粒径为5〜10μm，C量为0.14重量％以下，卡尔费休水分含量为0.2重量％以下时，加热至180℃ 并且所述方法包括以下步骤：将正极活性物质的糊剂施加到电极板以制造电极，然后干燥电极，然后在具有绝对水分的工作气氛中按压然后将电极安装在电池中含量为10g / m 3以下。

4. 发明授权

US4666575A Method of recovering gallium from scrap containing gallium 失效
标题翻译：从含镓的废料中回收镓的方法
公开(公告)号：US4666575A
公开(公告)日：1987-05-19
申请号：US886153
申请日：1986-07-16
申请人： Shigeki Kubo
发明人： Shigeki Kubo
IPC分类号： C01G15/00 , C01G28/00 , C22B7/00 , C22B58/00 , C25C1/22 , C25C1/00
CPC分类号： C01G28/007 , C01G15/00 , C22B58/00 , C22B7/002 , C25C1/22 , Y02P10/212
摘要： Scrap containing gallium and arsenic is treated with chlorine gas to form a crude gallium and arsenic chloride mixture. Arsenic chloride and impurities having a lower boiling point than that of arsenic chloride are removed from the mixture by vaporization so that crude gallium chloride may be obtained. The crude gallium chloride is purified by distillation. The purified gallium chloride is electrolyzed to yield metallic gallium. If the scrap has a molar gallium/arsenic ratio exceeding 1, arsenic chloride or metallic arsenic or both are added to the scrap before it if treated with chlorine gas.
摘要翻译：含有镓和砷的废料用氯气处理，形成粗的镓和砷的氯化物混合物。通过蒸发从混合物中除去具有比氯化砷低的沸点的氯化砷和杂质，从而可以获得粗的氯化镓。粗制氯化镓通过蒸馏纯化。将纯化的氯化镓电解得到金属镓。如果废料的镓/砷比率超过1，则在用氯气处理之前，向废料中加入氯化砷或金属砷或二者。

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