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    • 2. 发明专利
    • セレン含有水の処理方法及び処理装置
    • 用于处理含硒水的方法和装置
    • JP2015039652A
    • 2015-03-02
    • JP2013170455
    • 2013-08-20
    • 栗田工業株式会社Kurita Water Ind Ltd
    • ASADA HIROYUKIMURAMATSU YUICHITANITSU YOSHIKAZU
    • C02F1/70B01D53/14C02F1/58C02F1/78
    • 【課題】セレン含有水を金属チタンとそれよりも卑な金属との混合物又は合金と接触させ、該卑な金属の一部を溶出させることによりセレンを還元するセレン含有排水の処理方法及び装置において、セレン含有水が亜硫酸イオン、チオ硫酸イオン、亜硝酸イオンなどを含んでいてもセレンを効率よく処理することができるようにする。【解決手段】セレン含有水を、金属チタンとチタンより卑な金属との混合物の充填層7Aと接触させて、前記卑な金属の単体の一部を溶出させることにより、該セレン含有水中のセレンを還元処理するセレン含有水の処理方法及び装置において、該還元処理に先立ち、前記セレン含有水をオゾン酸化槽1で酸化処理する。【選択図】図1
    • 要解决的问题:提供一种处理含硒水的方法和设备,其中每个含硒水与含有金属钛和金属碱的混合物或合金与钛接触以洗脱 贱金属的一部分并且还原硒,并且其中的每一个构成为使得即使含硒的水含有亚硫酸根离子,硫代硫酸根离子,亚硝酸根离子等也能够有效地处理含硒水。 解决方案:在含硒水处理方法和装置中,含硒水与钛金属混合物的混合物与钛的混合物的填充层7A与钛接触,以洗脱一部分 在含硒水中还原硒,并且含硒水在臭氧氧化槽1中被氧化,在含硒水被还原之前。
    • 3. 发明专利
    • EXTRACTION METHOD
    • JP2000176438A
    • 2000-06-27
    • JP36108898
    • 1998-12-18
    • ELECTRIC POWER DEV COKANSAI ELECTRIC POWER COKURITA WATER IND LTD
    • NOGUCHI YOSHIKAZUMUTO KENICHITOYAMA KOJIYAMASHITA NAOYUKIASADA HIROYUKIETO YOSHIHIRO
    • C02F1/26B01D11/04
    • PROBLEM TO BE SOLVED: To stably and effectively perform a series of treatments from extraction to crystallizing recovery in by response to a variation in object concentration in water to be treated by adjusting a pH value of stripping agent before stripping based on a pH value after stripping. SOLUTION: A pipeline for feeding stripping agent in which boron has been back extracted in a stripping 3 to a crystallizer 4 is provided with a pH meter 4A to measure pH. And pH of the stripping agent before backward extraction is determined so that pH of stripping agent after backward extraction becomes a predetermined pH value. Based on this result, the operation of a chemical injection pump P2 is controlled. When pH of the stripping agent after stripping for adjusting the added quantity of alkali to a pH adjusting tank 2 is lower than a predetermined pH value, the fed quantity of alkali to the pH adjusting tank 2 is increased so that pH of the stripping agent is raised, and on the contrary, when pH of the stripping agent after backward extraction is higher than the predetermined pH value, the fed quantity of alkali to the pH adjusting tank 2 is reduced so that pH of the stripping agent is lowered. In this way, by increasing or decreasing the fed quantity of alkali, pH of the stripping agent before stripping is adjusted.
    • 4. 发明专利
    • TREATMENT OF SELENIUM-CONTAINING WATER
    • JP2000167571A
    • 2000-06-20
    • JP34429898
    • 1998-12-03
    • KURITA WATER IND LTD
    • ETO YOSHIHIROASADA HIROYUKIMURAKAMI TAKAFUMI
    • C02F1/58C02F1/70
    • PROBLEM TO BE SOLVED: To reduce the addition amt. of a chemical agent and the generation amt. of sludge and to recover water to reutilize the same by evaporating selenium-containing water to concentrate the same and treating conc. water at specific temp. or higher by the contact with metal iron or the addition of an iron (II) salt. SOLUTION: When selenium-containing water such as exhaust gas desulfurization waste water of a lime steam power plant or waste water of petroleum refining factory is treated, selenium-containing water is evaporated to be conc. and conc. water is treated at 60 deg.C or higher by the contact with metal iron or the addition of an iron (II) salt. At this time, pref., the conc.. water is adjusted to pH 3-6 to be brought into contact with metal iron. As metal iron to be used, there is no special limit and, for example, pure iron, alloyed steel, other iron alloy or the like can be designated but metal iron having a large surface area such as fine iron particles, an iron wire or granular iron is pref. Further, there is no special limit with respect to an iron (II) salt, for example, ferrous chloride, ferrous bromide or ferrous iodide can be designated.
    • 8. 发明专利
    • Boron recovery apparatus
    • BORON恢复装置
    • JP2008073639A
    • 2008-04-03
    • JP2006257470
    • 2006-09-22
    • Kurita Water Ind Ltd栗田工業株式会社
    • ASADA HIROYUKI
    • C02F1/28B01D9/02C01B35/12C02F1/04
    • PROBLEM TO BE SOLVED: To provide a boron recovery method by which boron can be recovered as borax or orthoboric acid having a high utility value from boron-containing water.
      SOLUTION: The boron recovery apparatus is provided with: an adsorption tower 1 for adsorbing boron in boron-containing water; a regenerant storage tank 2 for storing alkali for desorbing boron; an evaporator 3 for evaporating and concentrating a desorbing liquid; a cooling tank 4 for precipitating the crystals of metaborate from an evaporated and concentrated liquid; a filter 5 for separating the crystals; a dissolution tank 6 for dissolving the crystals into water; a neutralization tank 7 for neutralizing the dissolved liquid with acid and precipitating the crystals of tetraborate; a filter 8 for separating the crystals of tetraborate and a supernatant liquor; and a returning passage 9 for returning the supernatant liquor into the adsorption tower.
      COPYRIGHT: (C)2008,JPO&INPIT
    • 待解决的问题:提供一种硼回收方法,通过硼回收方法可以从含硼水中回收硼酸或具有高效用价值的原硼酸。 解决方案:硼回收装置设有:用于在含硼水中吸附硼的吸附塔1; 用于储存用于解吸硼的碱的再生剂储存罐2; 用于蒸发和浓缩解吸液体的蒸发器3; 用于从蒸发和浓缩的液体中沉淀偏硼酸晶体的冷却槽4; 用于分离晶体的过滤器5; 用于将晶体溶解在水中的溶解槽6; 中和罐7,用于用酸中和溶解的液体并沉淀四硼酸盐的晶体; 用于分离四硼酸盐晶体和上清液的过滤器8; 以及用于将上清液返回到吸附塔中的返回通道9。 版权所有(C)2008,JPO&INPIT
    • 10. 发明专利
    • Method for treating boron-containing water
    • 用于处理含硼水的方法
    • JP2003080269A
    • 2003-03-18
    • JP2001271428
    • 2001-09-07
    • Kurita Water Ind LtdTohoku Electric Power Co Inc東北電力株式会社栗田工業株式会社
    • HAYASAKA TAKAOYAMAURA TSUGUAKISATO TAKESHIETO YOSHIHIROASADA HIROYUKI
    • C02F1/52C02F1/42C02F1/58
    • PROBLEM TO BE SOLVED: To provide a method for treating boron-containing water by which the amount of chemicals used and the regeneration frequency of an ion exchange resin are reduced and boron can be efficiently removed by flocculation precipitation and/or ion exchange.
      SOLUTION: (1) In the method for treating boron-containing water by flocculation precipitation, the concentration of boron in the boron-containing water is automatically analyzed and the amount of a flocculant added is automatically controlled. (2) When the boron-containing water is treated by an ion exchange method, the concentration of boron is automatically analyzed and time appropriate to the regeneration of an ion exchange resin is automatically controlled. (3) When the boron-containing water is treated by the ion exchange method after treatment by flocculation precipitation, the concentration of boron is automatically analyzed and the amount of a flocculant added is automatically controlled.
      COPYRIGHT: (C)2003,JPO
    • 要解决的问题:提供一种处理含硼水的方法,通过该方法可以减少使用的化学品的使用量和离子交换树脂的再生频率,并且可以通过絮凝沉淀和/或离子交换有效地除去硼。 解决方案:(1)在通过絮凝沉淀处理含硼水的方法中,自动分析含硼水中硼的浓度,并自动控制添加的絮凝剂的量。 (2)当通过离子交换法处理含硼水时,自动分析硼的浓度,自动控制适合离子交换树脂再生的时间。 (3)当通过絮凝沉淀处理后,通过离子交换法处理含硼水时,自动分析硼的浓度,并自动控制添加的絮凝剂的量。