Electric blower assembly
    3.
    发明授权
    Electric blower assembly 失效
    电动鼓风机总成

    公开(公告)号:US4057370A

    公开(公告)日:1977-11-08

    申请号:US646593

    申请日:1976-01-05

    CPC classification number: F04D29/441 F04D25/082

    Abstract: Electric blower assembly wherein air expelled by centrifugal force from impellers passes through volute chambers disposed peripherally with respect to said impellers and each defining a space which is increasingly larger as the distance from the impellers increases, whereby smooth air flow is produced in the volute chambers since the speed of air flow therethrough is lessened and pressure therein becomes static pressure. From the volute chambers air passes along inclined channels and then around a drive motor, whereby the drive motor is cooled. In entering at least part of each volute chamber air from the impellers comes into contact with a volute chamber wall extension which becomes gradually lower in a direction opposing that of impeller rotation whereby noise due to contact of a volute chamber wall by all portions of the air from the impeller does not occur simultaneously and a quieter blower assembly is provided.

    Abstract translation: 电动鼓风机组件,其中通过离心力从叶轮排出的空气通过相对于所述叶轮周向设置的蜗壳室,并且每个限定了随着与叶轮的距离增加而越来越大的空间,由此在蜗壳室中产生平滑的气流,因为 减少其中流过的空气的速度,并且其中的压力变成静压。 从蜗壳室中,空气沿着倾斜的通道流过,然后围绕驱动马达,由此驱动马达被冷却。 在进入每个蜗壳室的至少一部分时,来自叶轮的至少一部分空气与涡流室壁延伸部接触,蜗壳室壁延伸部在与叶轮旋转相反的方向上逐渐降低,由此由于蜗壳室壁与空气的所有部分接触而产生噪音 从叶轮不同时发生,并且提供更安静的鼓风机组件。

    Process for producing anthracene diether
    4.
    发明申请
    Process for producing anthracene diether 有权
    制备蒽二醚的方法

    公开(公告)号:US20060079721A1

    公开(公告)日:2006-04-13

    申请号:US10539807

    申请日:2002-12-19

    CPC classification number: C07C41/16 C07C2603/24 C07C43/2055

    Abstract: An industrially advantageous process is presented whereby a high purity anthracene diether can be produced in good yield. An aqueous medium containing an alkali salt of 9,10-anthracenediol is added to an organic solvent containing an etherifying agent in the presence or absence of a quaternary ammonium compound or a quaternary phosphonium compound, to carry out the etherifying reaction to produce the anthracene diether.

    Abstract translation: 提出了一种工业上有利的方法,其中可以以良好的产率制备高纯度的蒽二醚。 在有或没有季铵化合物或季鏻化合物的情况下,将含有9,10-蒽二醇的碱金属盐的水性介质加入到含有醚化剂的有机溶剂中,进行醚化反应,生成蒽二醚 。

    Method for the treatment of waste water
    5.
    发明授权
    Method for the treatment of waste water 失效
    废水处理方法

    公开(公告)号:US5702615A

    公开(公告)日:1997-12-30

    申请号:US670786

    申请日:1996-06-24

    Abstract: A method for the treatment of waste water, which comprises treating waste water containing at least a sulfide-type malodorous substance, in the presence of a transition metal compound and hydrogen peroxide or a hydrogen peroxide-forming compound, wherein at least an iron family element compound and a vanadium family element compound are used as the transition metal compound.

    Abstract translation: 一种处理废水的方法,其包括在过渡金属化合物和过氧化氢或形成过氧化氢的化合物的存在下处理含有至少硫化物型恶臭物质的废水,其中至少一种铁族元素 化合物和钒族元素化合物用作过渡金属化合物。

    Process for producing anthracene diether
    7.
    发明授权
    Process for producing anthracene diether 有权
    制备蒽二醚的方法

    公开(公告)号:US07279607B2

    公开(公告)日:2007-10-09

    申请号:US10539807

    申请日:2002-12-19

    CPC classification number: C07C41/16 C07C2603/24 C07C43/2055

    Abstract: An industrially advantageous process is presented whereby a high purity anthracene diether can be produced in good yield.An aqueous medium containing an alkali salt of 9,10-anthracenediol is added to an organic solvent containing an etherifying agent in the presence or absence of a quaternary ammonium compound or a quaternary phosphonium compound, to carry out the etherifying reaction to produce the anthracene diether.

    Abstract translation: 提出了一种工业上有利的方法,其中可以以良好的产率制备高纯度的蒽二醚。 在有或没有季铵化合物或季鏻化合物的情况下,将含有9,10-蒽二醇的碱金属盐的水性介质加入到含有醚化剂的有机溶剂中,进行醚化反应,生成蒽二醚 。

    Method for electrolyzing cerous sulfate
    8.
    发明授权
    Method for electrolyzing cerous sulfate 失效
    电解硫酸铈的方法

    公开(公告)号:US4530745A

    公开(公告)日:1985-07-23

    申请号:US620095

    申请日:1984-06-13

    CPC classification number: C07C45/28 C07C46/04 C25B1/00

    Abstract: A method for electrolyzing cerous sulfate in the electrolytic oxidation of cerous sulfate to ceric sulfate in an aqueous sulfuric acid solution, characterized in that the concentration of the cerous sulfate in the electrolyte to be supplied to the electrolytic cell is maintained, by the presence of ceric sulfate, at a level of at least the saturated concentration of cerous sulfate in the aqueous sulfuric acid solution (exclusive of the cerous sulfate and ceric sulfate) at the initial sulfuric acid concentration and at the temperature of electrolysis, and at most the saturated concentration of cerous sulfate in the presence of the ceric sulfate in the aqueous sulfuric acid solution at the initial sulfuric acid concentration and at the temperature of electrolysis, and the concentration of the ceric sulfate in the electrolyte is maintained at a level of at most the saturated concentration of ceric sulfate in the aqueous sulfuric acid solution at the initial sulfuric acid concentration and at the temperature of electrolysis.

    Abstract translation: 在硫酸水溶液中将硫酸铈电解氧化成硫酸铈的硫酸铈电解方法,其特征在于,通过存在铈离子保持供给到电解槽的电解质中的硫酸铈浓度 硫酸盐,在初始硫酸浓度和电解温度下,至少在硫酸水溶液(不包括硫酸铈和硫酸铈)中的硫酸铈饱和浓度至少达到饱和浓度 硫酸铈在硫酸水溶液存在下,在初始硫酸浓度和电解温度下,电解液中硫酸铈的浓度保持在最高饱和浓度 硫酸铈在硫酸水溶液中的初始硫酸浓度和 在电解温度下。

    Oxidizing an organic compound
    9.
    发明授权
    Oxidizing an organic compound 失效
    氧化有机化合物

    公开(公告)号:US4632782A

    公开(公告)日:1986-12-30

    申请号:US603790

    申请日:1984-04-25

    CPC classification number: C07C46/04 C07C50/12

    Abstract: A process for oxidizing an organic compound by ceric sulfate dissolved in an aqueous sulfuric acid solution, wherein the organic compound is oxidized (1) by means of a ceric sulfate-aqueous sulfuric acid solution or a cerous sulfate-containing ceric sulfate-aqueous sulfuric acid solution in which the molar concentration (mol/liter) of ceric sulfate is at least the molar concentration of cerium (ions) contained in the molecules of cerous sulfate at the maximum solubility of cerous sulfate in an aqueous sulfuric acid solution at the final sulfuric acid concentration (exclusive of ceric sulfate and cerous sulfate) and at the temperature under the oxidation reaction conditions and at most the saturated molar concentration of ceric sulfate in said aqueous sulfuric acid solution, (2) under a condition such that at the end of the oxidation reaction, the concentration of ceric sulfate is maintained at a level capable of dissolving cerous sulfate which is present at a concentration of at least the maximum solubility of cerous sulfate in said aqueous sulfuric acid solution.

    Abstract translation: 溶解在硫酸水溶液中的硫酸铈氧化有机化合物的方法,其中有机化合物通过硫酸铈 - 硫酸水溶液或含硫酸铈的硫酸铈 - 硫酸水溶液氧化(1) 其中硫酸铈的摩尔浓度(mol / l)至少为硫酸铈分子中硫酸铈分子的最大溶解度在最终硫酸的硫酸水溶液中的摩尔浓度(摩尔/升) 浓度(不包括硫酸铈和硫酸铈),并且在氧化反应条件下的温度和至多在所述硫酸水溶液中的硫酸铈的饱和摩尔浓度,(2)在氧化结束的条件下 反应中,将硫酸铈的浓度维持在能够溶解至少浓度的硫酸铈的水平 硫酸铈在所述硫酸水溶液中的最大溶解度。

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