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    • 51. 发明专利
    • METHOD FOR REGENERATING ION EXCHANGE RESIN FOR DESALTING CONDENSED WATER
    • JPH11216373A
    • 1999-08-10
    • JP2208098
    • 1998-02-03
    • KURITA WATER IND LTD
    • TSURUMI TAKESHIMISUMI YOSHITERU
    • C02F1/42B01J49/00
    • PROBLEM TO BE SOLVED: To prevent the generation of eluted substances from ion exchange resins by setting the temperature of water contacting the resins at a specified value when condensed water is desalted to regenerate the resins which caught hydrazine. SOLUTION: The regeneration of ion exchange resins (condensed water ion desalting exchange resins) which caught hydrazine by desalting condensed water is implemented in a procedure consisting of the first transfer process (transfer of ion exchange resins from a desalting column to a separation-regeneration column), a backwash-separation process (backwash of the resins in a separation- regeneration column and separation of anion and cation exchange resins), the second transfer process, a regeneration process (regeneration of each resin in a regeneration column and a separation-regeneration column), a water-washing process (extrusion-washing of a regenerating agent), and other in this order. Each process is implemented at a water temperature of at the highest 15 deg.C. The generation of oxidative substances generated by the reaction between solvent oxygen in water and hydrazine is controlled, reducing the generation of resinous eluted substances composed mainly of a sulfonate.
    • 52. 发明专利
    • METHOD FOR REGENERATING ANION EXCHANGE RESIN
    • JPH10337485A
    • 1998-12-22
    • JP15129797
    • 1997-06-09
    • KURITA WATER IND LTD
    • TSURUMI TAKESHIOBATA KASHU
    • B01J49/00
    • PROBLEM TO BE SOLVED: To regenerate anion exchange resin in a short time and at a low cost and to recover ion exchange performance by allowing a regenerant of specific concentration to flow through the anion exchange resin at a specific space velocity in the state heated at a specific temp., and bringing the regenerant, into contact with the anion exchange resin. SOLUTION: In the state that an anion exchange resin layer is heated at 40-60 deg.C, preferably at 40 - about 50 deg.C, the regenerant of low concentration is allowed to flow at high speed to regenerate it. As a heating method of the anion exchange layer, any optional method such as heating with electric heating or heating with infrared radiation, can be used, and heating with hot water is preferred. A water flow quantity of hot water is desired to be >= about one time in a volume ratio of the anion exchange resin, preferably about 1-3 times. The water flow speed is desired to be 15-40 hr at the space velocity(SV), preferably about 20-35 hr . An alkali aqueous liquid such as an ammonia aqueous liquid and a sodium hydroxide aqueous liquid can be used as the regenerant. The concentration is 1-3.5 wt.%, preferably about 2-3 wt.%.
    • 53. 发明专利
    • REGENERATION OF CONDENSED WATER DESALTING APPARATUS
    • JPH10230171A
    • 1998-09-02
    • JP3383197
    • 1997-02-18
    • KURITA WATER IND LTD
    • TSURUMI TAKESHINOMURA MAKOTO
    • G21F9/12B01J49/00
    • PROBLEM TO BE SOLVED: To efficiently regenerate an anion exchange resin, even in such a case that condensed water of a system wherein amines low in volatility are added to a steam generator is treated, by eluting a decomposition product of amines adsorbed on the anion exchange resin, especially, fatty acid having a relatively high mol.wt. such as glycolic acid in a high elution ratio. SOLUTION: In a method for regenerating a condensed water desalting apparatus passing condensed water through a mixed bed of an anion exchange resin and a cation exchange resin to perform desalting, the mixed bed is separated into the anion exchange resin bed and the cation exchange resin bed and the anion exchange resin bed is brought into contact with alkali (bi)carbonate and subsequently brought into contact with alkali hydroxide to be regenerated while the cation exchange resin is brought into contact with an acid to be generated. Herein, the regeneration waste soln. of the anion exchange resin containing alkali (bi)carbonate and the regeneration waste soln. of the cation exchange resin containing the acid are mixed and a soln. obtained by absorbing generated carbon dioxide by alkali hydroxide is used as alkali (bi)carbonate in the next regeneration.
    • 54. 发明专利
    • METHOD FOR REGENERATION OF ION EXCHANGE RESIN
    • JPH10230170A
    • 1998-09-02
    • JP3533197
    • 1997-02-19
    • KURITA WATER IND LTD
    • TSURUMI TAKESHIOBATA KASHU
    • B01J49/00
    • PROBLEM TO BE SOLVED: To regenerate ion exchange resin within a short time at a low cost and miniaturize an apparatus by passing a regenerating agent in a specified concentration with a flow rate at specified spatial velocity and bringing the agent into contact with the ion exchange resin. SOLUTION: At the time when cation or anion exchange resin used for a pure water producing apparatus is regenerated, as a regenerating agent, an aqueous acidic solution such as hydrochloric acid, aqueous acidic solutions, etc., is used for cation exchange resin and an aqueous alkaline solution such as an aqueous ammonia solution, an aqueous sodium hydroxide solution, etc., is used for anion exchange resin. The concentration of the regenerating agent is controlled to be 1-3.5wt.%, preferably 2-3wt.% and regeneration is carried out by passing the regenerating agent through ion exchange resin layers. In this case, the spatial velocity of the regenerating agent is controlled to be 15-40/hr , preferably 20-35/hr, for both cation and anion exchange resin. The agent liquid passing direction may be both upward flow and downward flow and upward flow is preferable.
    • 55. 发明专利
    • WASHING OF CONDENSED WATER DESALTING APPARATUS
    • JPH09308881A
    • 1997-12-02
    • JP12480896
    • 1996-05-20
    • KURITA WATER IND LTD
    • TSURUMI TAKESHINOMURA MAKOTO
    • C02F1/42B01J49/00
    • PROBLEM TO BE SOLVED: To wash a condensed water desalting apparatus within a short washing time by reducing the load of a suspension of a metal oxide leaked at the initial period of the passage of water after the regeneration of a desalting tower to an ion exchange resin bed. SOLUTION: In a condensed water treatment system wherein condensed is filtered by a filter 1 and filtered condensed water and unfiltered condensed water are parallelly passed through a plurality of desalting columns 2a, 2b... of a condensed water desalting apparatus 2 to be desalted, the anion and cation exchange resins of the mixed bed 7a of the desalting column 2a lowered in its desalting capacity are backward washed and separated to be regenerated and washed, and the washed resins are mixed in the desalting column 2a to form the mixed bed 7a to perform washing at the initial stage of water passage. At this time, the washing waste waster of the desalting column 2a is circulated to the filter 1 to be filtered before introduced into the desalting column 2a to perform circulating washing.
    • 57. 发明专利
    • FILTER
    • JPH0824524A
    • 1996-01-30
    • JP18194994
    • 1994-07-12
    • KURITA WATER IND LTD
    • TSURUMI TAKESHI
    • B01D24/00B01D24/38B01D29/62B01D29/66B01D29/88
    • PURPOSE:To directly or indirectly give impact to a filter medium to strip SS that has been captured by providing a collision member on which a fibrous block filter medium collides when a filter bed is backward washed on the upper surface of the filter bed. CONSTITUTION:A filter bed 3 consisting of a fibrous block filter medium is formed on a lower water collecting plate 2 of a tank filter 1. A collision member 9 on which the fibrous block filter medium collides when the filter bed 3 is backward washed is attached. The collision member 9 may have an arbitrary form, but it occupies such a position that the filter medium collides with it properly and the flow thereof is not prevented. Then, on backward washing by air and washing water, the filter medium collides with the collision member 9 and also the filter medium come into collision is reoriented and collides with the other filter medium, allowing a lot of SS captured to be effectively stripped. Therefore, good washing effect is obtained, and the filter medium is used for a long period of time.
    • 59. 发明专利
    • TREATMENT OF FLUORIDE-CONTAINING WATER
    • JPH0747371A
    • 1995-02-21
    • JP19350993
    • 1993-08-04
    • KURITA WATER IND LTD
    • TSURUMI TAKESHISATO TAKESHI
    • C02F1/28B01D65/02C02F1/58C02F9/00
    • PURPOSE:To efficiently wash the membrane of an incorporated membrane separation device by bringing a fluoride ion adsorption material into contact with alkali, adding acid to a recovered waste liq. to produce fluoric acid, then reusing the waste liq. for washing a separation membrane. CONSTITUTION:The flow part high in fluorine concn. of the recovered waste liq. obtained in the case of the recovering treatment by bringing the fluoride ion adsorption material in a fluorine adsorption tower 7 into contact with the alkali such as NaOH is recovered into a storage tank 8 through a pipe 26. Then, when the performance of the separation membrane 3A of the membrane separation device 3 deteriorates, the operation of a treating system is stopped, and the recovered waste liq. in the storage tank 8 and the acid soln. in a storage tank 9 are mixed by the pipe 26 provided with a pump 35 and the pipe 27 provided with a pump 36, respectively to produce fluoric acid, and introduced to the separation device 3 through a pipe 28 and washed by dipping for a prescribed time. Then, after washing, the alkali soln. in a storage tank 10 is introduced to the separation device 3 through the pipe 29 and 28 provided with a pump 37 and washed by dipping for a prescribed time, then washed.
    • 60. 发明专利
    • TREATMENT OF EXHAUST GAS-DESULFURIZATION WASTEWATER
    • JPH0716564A
    • 1995-01-20
    • JP14615293
    • 1993-06-17
    • KURITA WATER IND LTD
    • MURAKAMI TAKESHITSURUMI TAKESHI
    • B01D53/34B01D53/50B01D53/77C02F1/42
    • PURPOSE:To obtain treated water of high quality by effectively removing heavy metal ions contained in the exhaust gas-desulfurization wastewater from a power plant by bringing the exhaust gas-desulfurization wastewater into contact with a chelate resin under a neutral pH condition. CONSTITUTION:The exhaust gas-desulfurization wastewater discharged from a power plant is supplied to a mixing tank 1 from a pipe 11 along with the return sludge from a sedimentation tank 2 and mixed with slaked lime supplied from a pipe 12, and the resulting mixture is supplied to the sedimentation tank 2 from a pipe 13 and subjected to solid-liquid separation. That is, fluorine in the wastewater is reacted with slaked lime and sedimented as CaF2 to be removed. A part of sedimented sludge based on CaF2 is returned to the mixing tank 1 to be reutilized while the supernatant water of the sedimentation tank 2 is supplied to a filter 5 by a pipe 16 and subjected to filtering treatment and the filtered water is sent to a resin tower 7 by a pipe 17 and passed through a chelate resin to adsorb and remove heavy metal ions of Zn, Ni or the like contained in the wastewater.