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    • 21. 发明专利
    • OZONE TREATMENT METHOD AND APPARATUS
    • JPH04197491A
    • 1992-07-17
    • JP32742990
    • 1990-11-28
    • KURITA WATER IND LTDMUNAKATA CHIKU SUIDOU KIGIYOUD
    • SATO SHINGOTO YUKIOTAKADOI TADASHITODOROKI KAZUMAABE YOSHITERU
    • C02F1/50C02F1/78
    • PURPOSE:To rapidly control the proper injection amount of ozone even when the quality of a solution to be treated is changed by calculating the pseudo- primary reaction speed constant K1 of the solution to be treated and controlling the injection amount of ozone on the basis of the calibration curve formed at every constant K1. CONSTITUTION:In an ozone reaction tower 1 where ozone-containing gas is brought into contact with a solution to be treated, the solution to be treated is supplied to a liquid supply passage 2 and discharged from a drain passage 3. Ozone-containing gas is supplied to the reaction tower 1 from an ozone generator 4 by an ozone injection pipe 5 and exhaust gas is discharged from the reaction tower 1 from an exhaust passage 6. Further, the concn. of ozone dissolved in the treated solution or the concn. of ozone in the exhaust gas is measured by ozone densitometers 9, 10, 13. Furthermore, a pseudo-primary reaction speed constant K is operated from the measured value by an operation apparatus 14. A control apparatus 17 controls the injection amount of ozone on the basis of the calibration curve showing the relation between the injection amount of ozone and the concn. of dissolved ozone or the concn. of exhaust ozone prepared at every constant K1.
    • 24. 发明专利
    • Treatment of waste water of stack gas scrubbing in refuse incineration plant
    • 垃圾焚烧厂垃圾处理废水处理
    • JPS5929082A
    • 1984-02-16
    • JP13834882
    • 1982-08-09
    • Kurita Water Ind Ltd
    • ITOU MASAOETOU YOSHIHIROTAKADOI TADASHI
    • C02F1/62
    • PURPOSE: To remove effectively mercury and other heavy metals by adding an S compd. and an Fe compd. at the vicinity of neutrality to the waste water of stack gas scrubbing in a refuse incineration plant to cause reaction then adding an alkali agent to the water to adjust the same basic and subjecting the water to a solid-liquid sepn.
      CONSTITUTION: An S compd. (e.g.; Na
      2 S) and an Fe compd. (e.g.; FeCl
      3 ) are added under 6W8pH conditions to the above-described waste water of stack gas scrubbing to cause reaction. The S compd. in this case is added for the purpose of removing mercury and other heavy metals, and the Fe compd. for the purpose of removing unreacted S ions. An alkali agent such as slaked lime is added to the waste water of stack gas scrubbing subjected to the above-described treatment to adjust the pH thereof to 9W11 and the water is subjected to a solid- liquid sepn. with heavy metals except mercury as insoluble hydroxides. If it is desired to remove F as well, a Ca compd. such as CaCl
      2 or the like is added to the water in the fore stage (6W8pH) and a good result is obtd. if Ca(OH)
      2 is used as the alkali agent in the post stage.
      COPYRIGHT: (C)1984,JPO&Japio
    • 目的:通过添加S化合物有效去除汞和其他重金属。 和一个Fe compd 在与垃圾焚烧厂中的堆垛气体的废水中立的中性附近引起反应,然后向水中加入碱剂以调节相同的碱性并使水经受固体液体分离。 宪法: (例如,Na 2 S)和Fe化合物。 (例如FeCl 3)在6-8pH条件下加入到上述废气中,以进行反应。 S compd。 在这种情况下,为了除去汞和其他重金属,以及Fe化合物。 以除去未反应的S离子。 向经过上述处理的层叠气体洗涤废水中加入熟石灰等碱剂,将其pH调节至9〜11,并对水进行固液分离。 除汞以外的重金属是不溶性氢氧化物。 如果需要除去F也可以使用Ca compd。 例如CaCl2等添加到前级(6-8pH)的水中,得到良好的结果。 如果在后期使用Ca(OH)2作为碱剂。
    • 27. 发明专利
    • Method for treating water containing fluoride ion
    • 用于处理含氟氟离子的方法
    • JPS5727191A
    • 1982-02-13
    • JP10241680
    • 1980-07-28
    • Kurita Water Ind Ltd
    • ETOU YOSHIHIROTAKADOI TADASHIMURAKAMI TAKAFUMI
    • C02F1/58
    • PURPOSE: To effectively and highly treat water containing a fluoride ion, by producing sediments under the presence of a magnesium ion and by separating the sediments.
      CONSTITUTION: At the first process, a crude water is introdiced to the first reaction tank 1 from a crude water pipe 5, and pH of the crude water is adjusted to 5W8.5 under a condition where calcium ions and/or aluminium ions exist. When pH of the crude water is adjusted, sediments are prodiced. The reacted liquid in the first reaction tank 1 is separated into a solid and a liquid in a precipitation tank 2. The sediment thus obtained is discharged to the outside of the process line through a sludge discharging pipe 8, and the supernatant liquid is introduced into the second reaction tank 3. At the second process, pH of the liquid introdiced from the first process is adjusted to ≥9.5 under the presence of magnesium ions and sediments are produced. The reacted liquid in the second reaction tank 2 is separated into a solid and a liquid in a precipitation tank 4. The supernatant liquid is discharged to the outside of the system through a treat water pipe 11 and a neutralization treatment is performed on the liquid if necessary. The sediments are returned to the first reaction tank 1 through a returning pipe 12 in the third process.
      COPYRIGHT: (C)1982,JPO&Japio
    • 目的:有效和高效地处理含有氟离子的水,通过在镁离子的存在下产生沉淀物并分离沉淀物。 构成:在第一工序中,将粗水从原水管5引入第一反应槽1,在存在钙离子和/或铝离子的条件下将粗水的pH调节至5-8.5。 当调整原水的pH值时,产生沉淀物。 第一反应槽1中的反应液体在析出槽2中分离成固体和液体。由此获得的沉淀物通过污泥排放管8排出到生产线外部,并将上清液引入 第二反应罐3.在第二过程中,在镁离子的存在下将从第一工艺引入的液体的pH调节至> = 9.5,并产生沉淀物。 将第二反应槽2中的反应液体分离成析出槽4中的固体和液体。上清液通过处理水管道11排出到系统外部,并对液体进行中和处理,如果 必要。 沉淀物在第三工序中通过回流管12返回到第一反应槽1。
    • 29. 发明专利
    • COAGULATING FILTRATION METHOD AND SYSTEM
    • JP2003170174A
    • 2003-06-17
    • JP2001371614
    • 2001-12-05
    • KURITA WATER IND LTD
    • TAKADOI TADASHI
    • C02F1/44B01D21/01C02F1/56
    • PROBLEM TO BE SOLVED: To reduce the frequency of chemical cleaning of a membrane solid- liquid separation device by stabilizing the flux of a membrane after adding coagulants in raw water such as river water, ground water, lake water, industrial water or various wastewater and carrying out a coagulation reaction in a coagulation tank and forcedly supplying water after coagulation to a re- coagulation tank with a pump for subjecting it to coagulation again. SOLUTION: Coagulation treatment of the raw water is carried out in the coagulation tank 1, water after coagulation is force-fed with the pump 3 in the re-coagulation tank 4. The organic high molecular coagulant is added, and flocks crushed by the pump 3 are re-coagulated, then the solid-liquid separation is carried out by the membrane separation device 5. The differential pressure of the membrane separation device 5 is measured with the differential pressure measuring device 8. Re-coagulation is properly carried out by controlling the addition of the organic high molecular coagulant by a chemical-feeding amount control device 10 so that the rise value of the differential pressure in a water flow process leading to back washing is within a predetermined allowable range. COPYRIGHT: (C)2003,JPO