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    • 6. 发明申请
    • PROCESS AND APPARATUS FOR PURIFICATION OF CONTAMINATED ACIDS
    • 用于净化污染酸的方法和装置
    • WO1996022153A1
    • 1996-07-25
    • PCT/CA1996000022
    • 1996-01-15
    • ECO-TEC LIMITED
    • ECO-TEC LIMITEDBROWN, Craig, J.
    • B01D61/04
    • B01D61/027B01D61/04B01D61/243B01D61/58B01D2311/04B01J41/05C01B17/902C02F1/442C23G1/36B01D2311/18B01D2311/25
    • Acids contaminated with multi-valent metal salts are purified by a process which involves treatment in an acid sorption unit (ASU) and a nanofiltration unit (NFU). The feed solution can first be delivered to the ASU, which produces two solutions, one high in acid concentration and the other high in metal salt concentration. The high acid concentration solution can be treated in the NFU to produce an acid end product and a reject metal salt solution which can be recirculated to the feed of the NFU. Alternatively, the high metal salt solution can be treated in the NFU, and its permeate recirculated to the ASU as eluate. In an alternative configuration, the feed is delivered first to the NFU. In all cases, the membrane reject solution from the NFU is recirculated to increase the metal salt concentration. A second NFU can be used to process the solution from the ASU which contains a high metal salt concentration.
    • 被多价金属盐污染的酸通过涉及在酸吸附单元(ASU)和纳滤单元(NFU)中处理的方法进行纯化。 饲料溶液可以先送到ASU,产生两种溶液,酸浓度高,金属盐浓度高。 可以在NFU中处理高酸浓度溶液,以产生可以再循环到NFU进料的酸终产物和废弃金属盐溶液。 或者,高金属盐溶液可以在NFU中处理,并且其渗透物作为洗脱液再循环到ASU中。 在另一种配置中,饲料首先送到NFU。 在所有情况下,来自NFU的膜拒绝溶液被再循环以增加金属盐浓度。 第二个NFU可用于处理含有高金属盐浓度的ASU溶液。
    • 8. 发明申请
    • TREATMENT OF CHLORINE DIOXIDE GENERATOR EFFLUENT AND FEED STREAMS WITH FIXED-RESIN BED
    • 二氧化氯发生器液体和固定树脂进料流的处理
    • WO1998016462A1
    • 1998-04-23
    • PCT/CA1997000750
    • 1997-10-09
    • PULP AND PAPER RESEARCH INSTITUTE OF CANADAECO-TEC LIMITEDPALEOLOGOU, MichaelTHOMPSON, RokhsarehBROWN, Craig, J.SHEEDY, Michael
    • PULP AND PAPER RESEARCH INSTITUTE OF CANADAECO-TEC LIMITED
    • C01B11/02
    • C01B17/904C01B11/023C01D5/16Y10S423/14
    • A process employing a fixed-resin bed Acid Retardation Unit (ARU) to separate spent acid from chlorine dioxide generators into a de-acidified sodium sulfate component and a purified sulfuric acid component. The de-acidified sodium sulfate produced is returned to the chemical recovery cycle of the kraft mill in place of acidic chlorine dioxide generator effluent thereby avoiding the destruction of alkalinity in pulp mill liquors. In addition, sulfuric acid is purified providing an opportunity for reuse in various mill applications, and/or concentrated and recycled to the generator. Alternatively, to avoid high evaporation costs, the purified acid can be used to regenerate a cation-exchange unit (CEU) used in the conversion of sodium chlorate to a sodium chlorate/chloric acid mixture which is fed to the generator in place of sodium chlorate and sulfuric acid. Using this approach, the sulfuric acid requirement of chlorine dioxide generators and, in turn, the amount of acidic generator effluent can be reduced. The process is applicable to both atmospheric and subatmospheric chlorine dioxide generators. In the latter case, the concentration of the purified sulfuric acid from the ARU or any other acid separation system can be increased by using a portion of it to dissolve the sodium sesquisulfate by-product from such generators.
    • 一种使用固定树脂床酸延迟单元(ARU)将废酸从二氧化氯发生器分离成脱酸的硫酸钠组分和纯化的硫酸组分的方法。 所产生的脱酸硫酸钠返回到牛皮纸磨机的化学回收循环,代替酸性二氧化氯发生器流出物,从而避免纸浆厂液中碱度的破坏。 此外,纯化硫酸提供了在各种研磨应用中再利用的机会,和/或浓缩并再循环到发生器中。 或者,为了避免高的蒸发成本,可以使用纯化的酸来再生用于将氯酸钠转化成氯酸钠/氯酸混合物的阳离子交换单元(CEU),该氯酸钠/氯酸混合物被供给发生器代替氯酸钠 和硫酸。 使用这种方法,可以减少二氧化氯发生器的硫酸需求,进而降低酸性发生器流出物的量。 该方法适用于大气和低气压的二氧化氯发生器。 在后一种情况下,来自ARU或任何其它酸分离系统的纯化硫酸的浓度可以通过使用其一部分来从这种发生器中溶解倍半硫酸钠副产物而增加。