Dielectric-Fluid Quality Control Apparatus and Electrical-Discharge Machining Apparatus
    23.
    发明申请
    Dielectric-Fluid Quality Control Apparatus and Electrical-Discharge Machining Apparatus 有权
    电介质质量控制装置和放电加工装置

    公开(公告)号:US20070289925A1

    公开(公告)日:2007-12-20

    申请号:US11665610

    申请日:2005-05-23

    IPC分类号: C02F1/42 B23H1/10

    摘要: A water purifying unit generates pure water by eliminating impurity ions from dielectric fluid. A corrosion-protection-ion generating unit generates corrosion protection ions, substitutes predetermined cations for impurity cations contained in the dielectric fluid, and substitutes the corrosion protection ions for impurity anions contained in the dielectric fluid. A switching unit switches a supply of the dielectric fluid between the water purifying unit and the corrosion-protection-ion generating unit. A switching control unit controls the switching unit based on a conductivity of the dielectric fluid measured by a conductivity measuring unit.

    摘要翻译: 净水单元通过从介质流体中除去杂质离子来产生纯净水。 腐蚀保护离子产生单元产生腐蚀保护离子,将预定的阳离子替代包含在介电流体中的杂质阳离子,并将腐蚀保护离子替代为包含在介电流体中的杂质阴离子。 开关单元在水净化单元和防腐蚀离子产生单元之间切换电介质流体供应。 开关控制单元基于由电导率测量单元测量的介电流体的电导率来控制开关单元。

    [Air and Water Conditioning System and Filter Media]
    25.
    发明申请
    [Air and Water Conditioning System and Filter Media] 审中-公开
    [空气和水调节系统和过滤介质]

    公开(公告)号:US20050274663A1

    公开(公告)日:2005-12-15

    申请号:US10709694

    申请日:2004-05-24

    申请人: Lipa Roitman

    发明人: Lipa Roitman

    摘要: Disclosed is an air-water-catalyst-UV light contacting, air heating and cooling, humidifying and dehumidifying CHAMBER, which receives water that continuously recirculates through the water filtering, heating and cooling, (and deionizing) loop, which gets fresh outdoors air through the energy-efficient heat exchanger, which generates water from the atmospheric moisture, which stores and recirculates pure water through potable water holding tank, and to which is connected a novel design energy-efficient self-regulating steam distillation apparatus. Also, a water filtration system utilizing zwitterionic polymers as ion exchange and salt-absorbing and filtration media. Also disclosed are novel ionic and zwitterionic polymers, derived from cellulose.

    摘要翻译: 公开了一种空气 - 水催化剂 - 紫外线接触,空气加热和冷却,加湿和除湿CHAMBER,其接收连续循环通过水过滤,加热和冷却(和去离子)循环的水,其获得新鲜的室外空气通过 节能换热器,其从大气湿气中产生水,其通过饮用水储存罐储存和再循环纯水,并且连接有新颖的设计节能的自动调节蒸汽蒸馏装置。 另外,利用两性离子聚合物作为离子交换和盐吸收和过滤介质的水过滤系统。 还公开了衍生自纤维素的新型离子和两性离子聚合物。

    Method for preparation of strong acid cation exchange resins
    28.
    发明授权
    Method for preparation of strong acid cation exchange resins 有权
    强酸阳离子交换树脂的制备方法

    公开(公告)号:US06784213B2

    公开(公告)日:2004-08-31

    申请号:US10158664

    申请日:2002-05-30

    IPC分类号: C08F834

    摘要: An improved process for preparing strong acid cation exchange resins by sulfonation of wet crosslinked copolymer in the absence of organic swelling solvents is disclosed. This process involves dewatering a crosslinked poly(vinylaromatic) copolymer to selected residual moisture levels of 3 to 35%, followed by non-solvent sulfonation, to provide strong acid cation exchange resins having enhanced physical stability and that are free of chlorinated-solvent contaminants.

    摘要翻译: 公开了通过在不存在有机溶胀溶剂的情况下磺化湿交联共聚物制备强酸阳离子交换树脂的改进方法。 该方法包括将交联的聚(乙烯基芳族化合物)共聚物脱水至3至35%的选定残余水分含量,然后进行非溶剂磺化,以提供具有增强的物理稳定性且不含氯化溶剂污染物的强酸阳离子交换树脂。

    Electrodeionization module
    29.
    发明授权
    Electrodeionization module 有权
    电离模块

    公开(公告)号:US06596145B2

    公开(公告)日:2003-07-22

    申请号:US09824275

    申请日:2001-04-02

    IPC分类号: C02F140

    摘要: An electrodeionization (EDI) module is formed from an anode spaced apart from a cathode, one or more waste channels formed between the electrodes and a product channel located inward of the waste channel(s). Ion permeable membranes form the boundary between the product channel and the waste channel(s). The product channel and waste channels are filled with a mixture of anionic and cationic ion exchange materials. At least the waste channel(s) and preferably the product channel as well, use either an anion bead having a relatively low affinity for the selected anion specie(s) to be retained (e.g. Type II) or it is a blend with Type I materials. Preferably, the membranes contain an ion exchange material to speed the transfer of ions across them. More preferably, the anionic membrane contains anion materials that have a relatively low affinity for the selected specie or species for retention.

    摘要翻译: 从阴极间隔开的阳极形成电去离子(EDI)模块,在电极之间形成的一个或多个废物通道和位于废物通道内侧的产品通道。 离子渗透膜形成产品通道和废物通道之间的边界。 产品通道和废物通道充满阴离子和阳离子交换材料的混合物。 至少废物通道,优选产物通道也使用对所选择的阴离子物质具有相对低亲和力的阴离子珠粒(例如II型),或者是与I型的共混物 材料 优选地,膜含有离子交换材料以加速离子通过它们的转移。 更优选地,阴离子膜包含对所选择的物种或物质具有相对低亲和力的阴离子材料用于保留。

    Electrodeionization apparatus
    30.
    发明申请
    Electrodeionization apparatus 审中-公开
    电离电离装置

    公开(公告)号:US20030079993A1

    公开(公告)日:2003-05-01

    申请号:US10283061

    申请日:2002-10-30

    IPC分类号: C02F001/469 B01D061/48

    摘要: An electrodeionization apparatus in which enough electric current flows even when a low voltage is applied, so that it can made sufficient deionizing treatment is provided. A cation exchange membrane 3 and an anion exchange membrane 4 are arranged between a cathode 1 and an anode 2, a cathode-concentration compartment 5 is formed between the cathode 1 and the cation exchange membrane 3, an anode-concentration compartment 6 is formed between the anode 2 and the anion exchange membrane, and a desalting compartment 7 is formed between the cation exchange membrane 3 and the anion exchange membrane 4. The cathode-concentration compartment 5 and the anode-concentration compartment 6 each of which is used also as a concentrating compartment are filled with a cation exchange resin 8. The desalting compartment 7 is filled with a mixture of the cation exchange membrane 8 and an anion exchange membrane 9. Raw water is fed into the desalting compartment 7 and taken out as deionized water. Electrode water was fed into the compartments 5 and 6, respectively.

    摘要翻译: 提供即使在施加低电压时也有足够的电流流动的电去电离装置,从而可以进行充分的去离子处理。 阳极交换膜3和阴离子交换膜4设置在阴极1和阳极2之间,在阴极1和阳离子交换膜3之间形成阴极浓缩室5,阳极浓缩室6 阳极2和阴离子交换膜以及脱盐室7形成在阳离子交换膜3和阴离子交换膜4之间。阴极浓缩室5和阳极浓度室6也用作 浓缩室填充有阳离子交换树脂8.脱盐室7填充有阳离子交换膜8和阴离子交换膜9的混合物。原水进料到脱盐室7中,并以去离子水取出。 电极水分别进入隔室5和6。