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    • 11. 发明专利
    • METHOD FOR WASHING PACKING MATERIAL IN BIOLOGICAL FILTER APPARATUS
    • JPH0347596A
    • 1991-02-28
    • JP18261189
    • 1989-07-17
    • KURITA WATER IND LTD
    • MURAKAMI TAKAFUMI
    • C02F3/08
    • PURPOSE:To make the release effect of a biological membrane and the separation effect of caught SS(suspended solid) sufficient by simultaneously performing the drain of water from the bottom part of a treatment tank and the supply of washing air to the bottom part of said tank and disturbing the liquid level gradually falling in the tank by said washing air. CONSTITUTION:Air is supplied to the bottom part of a treatment tank 1 from an air source 5 such as a blower or an air compressor to be uniformly diffused into the water in the tank 1. Raw water to be treated is supplied to the treatment tank 1 from above from a storage tank 7 by a pump P and BOD or the like is treated with the bacteria of the biological membrane bonded to a packing material when the raw water passes through the packed bed 2 in the tank 1 as downward flow and SS mixed in the raw water is simultaneously collected and removed by the packed bed 2 while treated water is drained to the outside from the bottom part of the treatment tank. By this method, washing can be performed only by air without using washing water and excellent washing effect is obtained.
    • 13. 发明专利
    • Treatment of waste water of waste gas desulfurization
    • 废气处理废水废水
    • JPS5778988A
    • 1982-05-17
    • JP15531280
    • 1980-11-05
    • Kurita Water Ind Ltd
    • ETOU YOSHIHIROTAKADOI TADASHIMURAKAMI TAKAFUMI
    • C02F1/58
    • PURPOSE: To treat waste water in good efficiency by a method wherein a water soluble carbonate or the like is added to waste water from waste gas desulfurization treatment of which a pH is adjusted to 9.5 or more by adding an alkali agent to adjust a pH to 8 or more and, after solid-liqud separation is carried out, the treated water is incinerated.
      CONSTITUTION: To waste water from waste gas desulfrization treatment, an alkali agent comprising an ammonium compound and/or a calcium compound is added to adjust a pH thereof to 9.5 or more and, thereby, a metal ion such as Mg, Ni, Fe or the like in the waste water is precipitated. Further, a water soluble carbonate or a carbon dioxide gas is added to the effluent water to adjust a pH thereof to 8 or more to precipitate Ca in said water as an insoluble precipitate and, thereafter, solid- liquid separation is carried out in a solid-liquid separation apparatus. Subsequently, the discharged treated water is introduced into an incinerating process and incinerated by heating the same to 400°C or more. As the ammonium compound, there is ammonium hydroxide or the like and, as the water soluble carbonate, there is ammonium carbonate or the like.
      COPYRIGHT: (C)1982,JPO&Japio
    • 目的:通过添加碱剂以将pH调节至pH为9.5以上的废气脱硫处理中将水溶性碳酸盐等添加到废水中的方法,以高效率处理废水, 8以上,在进行固液分离后,对处理后的水进行焚烧。 构成:为了从废气脱硫处理中排出水,加入包含铵化合物和/或钙化合物的碱剂以将其pH调节至9.5以上,从而将金属离子如Mg,Ni,Fe或 废水中的类似物沉淀。 此外,将水溶性碳酸盐或二氧化碳气体加入到流出水中以将其pH调节至8以上,以将沉淀在所述水中的Ca作为不溶性沉淀物沉淀,然后在固体中进行固液分离 液体分离装置 随后,排出的处理水被引入焚烧过程中,并通过将其加热至400℃以上进行焚烧。 作为铵化合物,存在氢氧化铵等,作为水溶性碳酸酯,存在碳酸铵等。
    • 14. 发明专利
    • Coal gasification wastewater treatment method and apparatus
    • 煤气化废水处理方法和装置
    • JP2007289841A
    • 2007-11-08
    • JP2006119622
    • 2006-04-24
    • Kurita Water Ind Ltd栗田工業株式会社
    • TANITSU YOSHIKAZUMURAKAMI TAKAFUMINAKAHARA TOSHIJI
    • C02F1/02C02F1/58C02F1/74C10K1/10
    • PROBLEM TO BE SOLVED: To provide a coal gasification wastewater treatment method and apparatus which can efficiently remove cyanogen, metals, and COD components contained in gas washing wastewater generated in a coal gasification process to obtain treated water of good quality.
      SOLUTION: In the coal gasification wastewater treatment method, coal gasification wastewater is heated to 101-210°C under an alkaline condition, and generated suspended metals are removed to be subjected to wet catalytic oxidation. The coal gasification wastewater treatment apparatus comprises a heat hydrolysis reactor retaining the coal gasification wastewater under a pressure keeping the liquid phase of the wastewater at 101-210°C, a suspended metal remover, and a wet catalytic oxidation reactor.
      COPYRIGHT: (C)2008,JPO&INPIT
    • 要解决的问题:提供一种能够有效去除在煤气化过程中产生的气体洗涤废水中含有的氰,金属和COD成分的煤气化废水处理方法和装置,以获得质量好的处理水。

      解决方案:在煤气化废水处理方法中,煤气化废水在碱性条件下加热至101-210℃,除去生成的悬浮金属进行湿式催化氧化。 煤气化废水处理装置包括在保持101-210℃的废水液相的压力,悬浮金属去除剂和湿式催化氧化反应器的同时保持煤气化废水的热水反应器。 版权所有(C)2008,JPO&INPIT

    • 19. 发明专利
    • Method for treatment of waste water
    • 废水处理方法
    • JPS5727198A
    • 1982-02-13
    • JP10125780
    • 1980-07-25
    • Kurita Water Ind Ltd
    • FUKASE TETSUROUMURAKAMI TAKAFUMI
    • C02F3/30
    • PURPOSE: To effectively treat waste water and easily perform solid-liquid separation, by performing an anaerobic treatment on a part of waste water discharged from exhaust gas desulfurizing equipment, then, performing an aerobic treatment after mixing the treated waste water and the remaining waste water.
      CONSTITUTION: A part of the waste water from an exhaust gas desulfurizing process 5 containing dithionic acid is introduced into an anaerobic tank 1 together with returning sludge 6, methanol, peptone, and a BOD source, such as obsolete molasses, etc., and an anaerobic treatment is performed on them. Then, the mixed liquid in the anaerobic tank 1 is taken out little by little and separated into solid and liquid in a sedimentation tank 2. The solid material is returned to the anaerobic tank 1. The supernatant liquid is introduced into an aeration tank 3 and aerated by air 9 together with a part of the waste water 5 and the returned sludge 8. The mixed liquid in the aeration tank 3 is taken out and separated into solid and liquid in another sedimentation tank 4. The solid material is returned to the aeration tank 3 as returning sludge, and the supernatant liquid is discharged as the treated water 11.
      COPYRIGHT: (C)1982,JPO&Japio
    • 目的:为了有效地处理废水,容易进行固液分离,对废气脱硫设备排出的一部分废水进行厌氧处理,然后在处理废水与剩余废水混合后进行好氧处理 。 构成:将含有二硫酸的废气脱硫工序5的一部分废水与返回的污泥6,甲醇,胨,BOD源(如过时的糖蜜等)一起导入厌氧池1, 对他们进行厌氧处理。 然后,一点一点地取出厌氧槽1中的混合液,在沉淀池2中分离成固体和液体。将固体物质返回到厌氧池1.将上清液引入曝气池3中, 通过空气9与一部分废水5和返回的污泥8一起充气。曝气池3中的混合液体被取出并在另一个沉淀池4中分离成固体和液体。将固体材料返回到曝气 罐3作为返回污泥,作为处理水排出上清液。
    • 20. 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。