NONAQUEOUS ELECTROLYTE SOLUTION FOR SECONDARY BATTERY AND NONAQUEOUS ELECTROLYTE SECONDARY BATTERY
    1.
    发明申请
    NONAQUEOUS ELECTROLYTE SOLUTION FOR SECONDARY BATTERY AND NONAQUEOUS ELECTROLYTE SECONDARY BATTERY 审中-公开
    用于二次电池和非电解电解质二次电池的非电解电解质

    公开(公告)号:US20160126592A1

    公开(公告)日:2016-05-05

    申请号:US14766482

    申请日:2014-02-03

    Abstract: A nonaqueous electrolyte solution for a secondary battery, including an electrolyte, a solvent and an additive, and a nonaqueous electrolyte secondary battery including the nonaqueous electrolyte solution. The additive contains a compound represented by the following formula (I): wherein n represents an integer of 1 to 4, in the case of n=1, R1 represents a halogen atom or the like, in the case of n=2, R1 represents an alkaline earth metal atom or the like, in the case of n=3, R1 represents a trivalent transition metal atom or the like, in the case of n=4, R1 represents a tetravalent transition metal atom or the like, and R2 represents an alkylene group of 1 to 6 carbon atoms or an alkenylene group of 2 to 6 carbon atoms.

    Abstract translation: 包括电解质,溶剂和添加剂的二次电池用非水电解液和包含非水电解质溶液的非水电解质二次电池。 添加剂含有下述式(I)所示的化合物:其中n表示1〜4的整数,n = 1的情况下,R 1表示卤素原子等,n = 2的情况下,R 1 表示碱土金属原子等,在n = 3的情况下,R1表示三价过渡金属原子等,在n = 4的情况下,R 1表示四价过渡金属原子等,R2表示 表示1〜6个碳原子的亚烷基或2〜6个碳原子的亚链烯基。

    METHOD FOR PRODUCING OLIGOSILANE
    4.
    发明申请

    公开(公告)号:US20200062602A1

    公开(公告)日:2020-02-27

    申请号:US16335990

    申请日:2017-09-19

    Abstract: A method for producing an oligosilane including a reaction step of introducing a fluid containing a hydrosilane into a continuous reactor provided with a catalyst layer inside to produce an oligosilane from the hydrosilane and discharging a fluid containing the oligosilane from the reactor. The reaction step satisfies all of the following conditions (i) to (iii): (i) a temperature of the hydrosilane-containing fluid at an inlet of the catalyst layer is higher than a temperature of the oligosilane-containing fluid at an outlet of the catalyst layer; (ii) the temperature of the hydrosilane-containing fluid at the inlet of the catalyst layer is from 200 to 400° C.; and (iii) the temperature of the oligosilane-containing fluid at the outlet of the catalyst layer is from 50 to 300° C.

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