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    • 3. 发明专利
    • VIBRATION ELIMINATING DEVICE
    • JPH05126205A
    • 1993-05-21
    • JP14390491
    • 1991-05-20
    • EBARA CORP
    • WATANABE KAZUHIDEKANEMITSU YOICHIIKEDA YUKIO
    • B23Q11/00E04H9/02F16F15/02G01H1/00G01H17/00H01L21/027H01L21/30
    • PURPOSE:To provide a vibration eliminating device which can avoid the state that would affect yield of products or accuracy of measurement and observation by monitoring vibration on a floor plate all the time with a vibration sensor mounted on the floor plate of a vibration eliminating table, judging whether the vibration is within a permitted value of mounted machinery and by putting out a machinery operative signal when the vibration is within the permitted value. CONSTITUTION:A vibration eliminating device suspends a floor plate of a vibration eliminating table 1 and has a spring action for eliminating microvibration from the installed floor of the vibration eliminating table or an exciting force from machinery 2 itself on the vibration eliminating table floor plate. A vibration detector S for detecting vibration on the floor plate is provided at the vibration eliminating table 1, and a vibration monitor device 4 is provided for judging whether the vibration detected by the vibration detector S is within a permitted value of the machinery 2 mounted on the floor plate of the vibration eliminating table 1 and for putting out a machinery operative signal only when the vibration is within the permitted value.
    • 4. 发明专利
    • DEVICE FOR REMOVAL OF HARMFUL SUBSTANCE FROM EXHAUST GAS
    • JPH0259001A
    • 1990-02-28
    • JP20805088
    • 1988-08-24
    • EBARA CORP
    • TSUJIMURA MANABUIKEDA YUKIO
    • B01D53/46B01D5/00B01D7/02B01D8/00B01D53/34B01D53/68B01D53/70H01L21/302H01L21/3065
    • PURPOSE:To remove harmful substance from exhaust gases by installing an addition- reaction tank, wherein gases, which are able to be liquefied or sublimated under atmospheric temperature and pressure, a selectively condensed or sublimated, on the upstream side of an exhaust-gas reaction tank to prevent blocking of the exhaust-gas reaction tank. CONSTITUTION:When a group of gases A, which are easily liquefied or sublimated under atmospheric temperature and pressure, and a group of gases B in gaseous state, being mixed together, flow into an addition-reaction tank 12, a majority of the group of gases A is liquefied or sublimated since the temperature of the tank 12 is located slightly lower than that of an exhaust-gas reaction tank 5 situated downstream, while the group of gases B remain in gaseous state, whereby the group of gases B which haven't been condensed or sublimated and a part of the group A flow into the tank 5, while, since the temperature in the tank 5 is higher than that of the tank 12, the gases having flowed into the tank 5 are subjected to an adsorption reaction in gaseous state, without being liquefied or sublimated. Consequently, blocking of the interior of the tank 5 is avoided and harmful substances are removed from the exhaust gases without fail.
    • 8. 发明专利
    • Mixed bed filtering and demineralizing method
    • 混合床过滤和分解方法
    • JPS59147690A
    • 1984-08-24
    • JP2203483
    • 1983-02-15
    • Ebara Corp
    • HAGIWARA MASAHIROISAYAMA YASUSHIIKEDA YUKIOINO TAKAO
    • C02F1/42B01J47/04
    • PURPOSE:To separate easily anion and cation exchange resins by specifying the mode value, geometric standard deviation and the particle size range to be separated from the population of the anion and cation exchange resins to increase the ion exchange velocity and clad separating capacity. CONSTITUTION:In the titled method using anion and cation resins having particle size forming a logarithmic normal distribution, 1) the mode value of the anion and cation exchange resins are regulated respectively to 420-600mu and 500- 700mu so that the mode value of the former may be lower than that of the latter, 2) one of the geometric standard deviations of the anion and cation exchange resins is regulated to
    • 目的:通过指定阴离子交换树脂和阳离子交换树脂的离子交换速度和包层分离能力,分离容易的阴离子和阳离子交换树脂,分离模式值,几何标准偏差和粒度范围。 构成:在使用具有对数正态分布的粒径的阴离子和阳离子树脂的标题方法中,1)将阴离子和阳离子交换树脂的模式值分别调节为420-600mu和500-700mu,使得模式值 前者可能低于后者,2)阴离子和阳离子交换树脂的几何标准偏差之一调节为<= 1.30,3)符合先前指定的粒度范围的颗粒与相应的 阴离子和阳离子交换树脂。 将两种树脂在水中的终端速度通过使用上述三种方法中的任意一种使彼此相等的阴离子和阳离子交换树脂的比例被调节到规定的范围。 比例或更少的树脂与总树脂的比例。