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JP6535538B2 - Method of regenerating ion exchange resin - Google Patents
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JP6535538B2 - Method of regenerating ion exchange resin - Google Patents

Method of regenerating ion exchange resin Download PDF

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JP6535538B2
JP6535538B2 JP2015151743A JP2015151743A JP6535538B2 JP 6535538 B2 JP6535538 B2 JP 6535538B2 JP 2015151743 A JP2015151743 A JP 2015151743A JP 2015151743 A JP2015151743 A JP 2015151743A JP 6535538 B2 JP6535538 B2 JP 6535538B2
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尚友 赤澤
尚友 赤澤
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Maezawa Industries Inc
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Description

本発明は、イオン交換樹脂の再生方法に関し、詳しくは、イオン交換能力の低下したイオン交換樹脂を収容した再生処理タンクに、再生液を供給してイオン交換樹脂を再生するイオン交換樹脂の再生方法に関する。   The present invention relates to a method of regenerating an ion exchange resin, and more specifically, a method of regenerating an ion exchange resin in which a regeneration solution is supplied to a regeneration processing tank containing an ion exchange resin having a reduced ion exchange capacity. About.

従来、溶液中に含まれた各イオンを分離するために、イオン交換樹脂が用いられているが、このイオン交換樹脂は、一定量のイオン交換を行うとイオン交換能力を失うことから、元の交換イオンを含む再生液に浸漬させて再生させている。このイオン交換樹脂の再生方法として、イオン交換能力の低下したイオン交換樹脂を収容した再生処理タンクに、再生液を収容した再生液タンクから再生液を供給し、イオン交換樹脂を通過した再生液を廃液槽に送るものがあった(例えば、特許文献1参照。)。   Conventionally, an ion exchange resin is used to separate the ions contained in the solution, but this ion exchange resin loses its ion exchange capacity when a certain amount of ion exchange is carried out. Regeneration is performed by immersing in a regeneration solution containing exchange ions. As a regeneration method of this ion exchange resin, the regeneration solution is supplied from a regeneration solution tank containing a regeneration solution to a regeneration treatment tank containing an ion exchange resin having a reduced ion exchange capacity, and the regeneration solution passing through the ion exchange resin is There was one to be sent to the waste liquid tank (see, for example, Patent Document 1).

特開平7−270214号JP-A-7-270214

しかし、上述の特許文献1のものでは、イオン交換能力の低下したイオン交換樹脂を収容した再生処理タンクに再生液を供給した後、一定時間静置させてイオン交換樹脂を再生させているが、静置時間が長くなることがあった。   However, in the thing of the above-mentioned patent document 1, after supplying a regeneration liquid to the regeneration processing tank which accommodated the ion exchange resin with which ion exchange capacity fell, it is made to stand still for a fixed time, and the ion exchange resin is regenerated. The standing time may be long.

そこで本発明は、イオン交換樹脂の再生時間の短縮を図ることができるイオン交換樹脂の再生方法を提供することを目的としている。   Then, an object of this invention is to provide the reproduction | regeneration method of the ion exchange resin which can aim at shortening of the reproduction | regeneration time of ion exchange resin.

上記目的を達成するため、本発明のイオン交換樹脂の再生方法は、イオン交換能力の低下したイオン交換樹脂を収容した再生処理タンクに、再生液を供給して前記イオン交換樹脂を再生するイオン交換樹脂の再生方法において、前記再生処理タンクにイオン交換能力の低下した前記イオン交換樹脂を収容して洗浄水を供給し、前記イオン交換樹脂を水洗し、イオン交換樹脂洗浄後の洗浄水を排出する第1水洗工程と、第1水洗工程終了後、再生液タンクから前記再生液を前記再生処理タンクに供給する再生液供給工程と、前記再生処理タンクに供給された前記再生液を循環させて前記イオン交換樹脂を再生する再生工程と、前記再生工程が所定時間経過した後に、前記再生液の循環を停止して一定時間静置させる静置工程と、 前記静置工程終了後の前記再生処理タンク内の前記再生液を排出する再生液排出工程と、該再生液排出工程終了後に、前記再生処理タンクに洗浄水を供給し、前記イオン交換樹脂を水洗し、次いで、前記イオン交換樹脂を洗浄後の洗浄水を排出する第2水洗工程とを有することを特徴としている。 In order to achieve the above object, according to the ion exchange resin regeneration method of the present invention, an ion exchange resin is supplied to a regeneration treatment tank containing an ion exchange resin with reduced ion exchange capacity to regenerate the ion exchange resin. In the resin regeneration method, the ion exchange resin with reduced ion exchange capacity is accommodated in the regeneration treatment tank to supply washing water, the ion exchange resin is washed with water, and the washing water after ion exchange resin washing is discharged. A first washing step; and a regenerating solution supply step of supplying the regenerating solution from the regenerating solution tank to the regenerating treatment tank after completion of the first rinsing step; circulating the regenerating solution supplied to the regenerating treatment tank; A regeneration step of regenerating the ion exchange resin, a stationary step of stopping the circulation of the regenerating solution after a lapse of a predetermined time, and allowing the solution to stand for a predetermined time; A regeneration liquid discharging step of discharging the regenerant of the reproduction processing tanks After the completion, after regeneration fluid discharge step is completed, to supply cleaning water to the reproduction processing tank, washed with water said ion exchange resin and then, And a second water-washing step of discharging the washing water after washing the ion exchange resin.

本発明のイオン交換樹脂の再生方法によれば、再生液を再生処理タンクに供給する再生液供給工程の後に、再生処理タンクに供給された再生液を循環させてイオン交換樹脂を再生する再生工程を設けたことにより、イオン交換樹脂の再生効率を高めることができ、再生時間の短縮を図ることができる。   According to the regeneration method of the ion exchange resin of the present invention, the regeneration step of circulating the regeneration solution supplied to the regeneration treatment tank to regenerate the ion exchange resin after the regeneration solution supply step of supplying the regeneration solution to the regeneration treatment tank As a result, the regeneration efficiency of the ion exchange resin can be enhanced, and the regeneration time can be shortened.

本発明の一形態例を示すイオン交換樹脂再生装置の系統図である。It is a systematic diagram of the ion exchange resin regeneration device which shows one embodiment of the present invention. 第1水洗工程で再生処理タンクに洗浄水を供給しているイオン交換樹脂再生装置の説明図である。It is explanatory drawing of the ion exchange resin reproduction | regeneration apparatus which supplies the wash water to the reproduction | regeneration processing tank by a 1st water washing process. 第1水洗工程で再生処理タンクから洗浄水を排出しているイオン交換樹脂再生装置の説明図である。It is explanatory drawing of the ion exchange resin reproduction | regeneration apparatus which is discharging | emitting wash water from the reproduction | regeneration processing tank by the 1st water washing process. 再生液供給工程で再生処理タンクに再生液を供給しているイオン交換樹脂再生装置の説明図である。It is explanatory drawing of the ion exchange resin reproduction | regeneration apparatus which is supplying the reproduction | regeneration liquid to the reproduction | regeneration processing tank at a reproduction | regeneration liquid supply process. 再生工程で再生液を循環させているイオン交換樹脂再生装置の説明図である。It is explanatory drawing of the ion exchange resin reproduction | regeneration apparatus which circulates the reproduction | regeneration liquid at the reproduction | regeneration process. 再生液排出工程で再生処理タンクから再生液を排出しているイオン交換樹脂再生装置の説明図である。It is explanatory drawing of the ion exchange resin reproduction | regeneration apparatus which is discharging | generating the reproduction | regeneration liquid from the reproduction | regeneration processing tank at a reproduction | regeneration liquid discharge process. 第2水洗工程で再生処理タンクに洗浄水を供給しているイオン交換樹脂再生装置の説明図である。It is explanatory drawing of the ion exchange resin reproduction | regeneration apparatus which supplies the wash water to the reproduction | regeneration processing tank by a 2nd water washing process. 第2水洗工程で再生処理タンクから洗浄水を排出しているイオン交換樹脂再生装置の説明図である。It is explanatory drawing of the ion exchange resin reproduction | regeneration apparatus which has discharged | emitted the wash water from the reproduction | regeneration processing tank by the 2nd water washing process.

図1は、イオン交換樹脂再生装置11の一形態例を示すもので、イオン交換能力の低下したイオン交換樹脂12を収容する再生処理タンク13と、再生液を貯留する再生液タンク14と、洗浄水を貯留する給水タンク15と、再生処理タンク13からの廃液を貯留する廃液槽16とを備え、再生処理タンク13には、イオン交換樹脂12を導入する導入経路13aと、イオン交換樹脂12を導出する導出径路13bとが設けられている。   FIG. 1 shows an embodiment of the ion exchange resin regeneration apparatus 11, which includes a regeneration treatment tank 13 containing an ion exchange resin 12 having a reduced ion exchange capacity, a regeneration solution tank 14 storing a regeneration solution, and washing. A water supply tank 15 for storing water, and a waste liquid tank 16 for holding waste liquid from the regeneration processing tank 13. The regeneration processing tank 13 includes an introduction path 13a for introducing the ion exchange resin 12 and the ion exchange resin 12. A lead-out path 13b for lead-out is provided.

再生処理タンク13と給水タンク15との間には給水径路17が設けられ、給水径路17には給水弁18が設けられている。再生処理タンク13の下部と廃液槽16との間には、排水径路19が設けられ、排水径路19には、再生処理タンク13側に出口弁20が、廃液槽16側に廃液排出弁21がそれぞれ設けられ、出口弁20と廃液排出弁21との間に引抜きポンプ22が配置されている。再生液タンク14の上部と再生処理タンク13の上部との間には、再生液を供給する再生液供給径路23が設けられ、再生液供給径路23には供給弁24が設けられ、供給弁24と再生液タンク14との間に再生液ポンプ25が配置されている。さらに、再生処理タンク13の上部と下部との間には、配管の一部が前記排水径路19と共通すると共に、出口弁20と引抜きポンプ22とが共通する循環径路26が設けられ、循環径路26の再生処理タンク13の上部側には入口弁27が設けられている。   A water supply passage 17 is provided between the regeneration processing tank 13 and the water supply tank 15, and a water supply valve 18 is provided in the water supply passage 17. A drainage path 19 is provided between the lower part of the regeneration processing tank 13 and the waste liquid tank 16, and the drainage path 19 has an outlet valve 20 on the regeneration processing tank 13 side and a waste liquid discharge valve 21 on the waste tank 16 side. Each is provided, and a drawing pump 22 is disposed between the outlet valve 20 and the waste liquid discharge valve 21. A regeneration solution supply path 23 for supplying regeneration solution is provided between the upper portion of the regeneration solution tank 14 and the upper portion of the regeneration processing tank 13, and a supply valve 24 is provided in the regeneration solution supply path 23. The regenerating solution pump 25 is disposed between the regenerating solution tank 14 and the regenerating solution tank 14. Furthermore, between the upper part and the lower part of the regeneration processing tank 13, a circulation path 26 is provided, in which a part of the pipe is common to the drainage path 19, and the outlet valve 20 and the withdrawal pump 22 are common. An inlet valve 27 is provided on the upper side of the regeneration processing tank 13 of 26.

上述のイオン交換樹脂再生装置11でイオン交換能力の低下したイオン交換樹脂12を再生させる際には、導入経路13aを介してイオン交換能力の低下したイオン交換樹脂12を再生処理タンク13に導入した後、まず、第1水洗工程が行われる。第1水洗工程では、図2に示されるように、給水弁18を開き、給水タンク15から給水径路17を介して再生処理タンク13に洗浄水を供給した後、図3に示されるように、給水弁18を閉じて、出口弁20と廃液排出弁21とを開き、引抜きポンプ22を作動させて排水径路19を介して、イオン交換樹脂12を洗浄した排水を廃液槽16に送る。   When the ion exchange resin 12 whose ion exchange capacity has been reduced is regenerated by the ion exchange resin regeneration apparatus 11 described above, the ion exchange resin 12 whose ion exchange capacity has decreased is introduced into the regeneration treatment tank 13 via the introduction path 13a. After that, first, the first water washing step is performed. In the first washing step, as shown in FIG. 2, after the water supply valve 18 is opened and washing water is supplied from the water supply tank 15 to the regeneration processing tank 13 via the water supply path 17, as shown in FIG. The water supply valve 18 is closed, the outlet valve 20 and the waste liquid discharge valve 21 are opened, the drawing pump 22 is operated, and the drained water having the ion exchange resin 12 washed is sent to the waste liquid tank 16 via the drainage path 19.

第1水洗工程終了後、再生液供給工程が行われる。再生液供給工程では、図4に示されるように、引抜きポンプ22を停止するとともに出口弁20と廃液排出弁21とを閉じ、供給弁24を開き、再生液ポンプ25を作動させて再生液供給径路23を介して再生液を再生処理タンク13に送る。また、この時、必要に応じて給水弁18を開いて給水して再生液を希釈する。   After completion of the first water washing step, a regenerating solution supply step is performed. In the regenerating solution supplying step, as shown in FIG. 4, the drawing pump 22 is stopped, the outlet valve 20 and the waste solution discharging valve 21 are closed, the supply valve 24 is opened, and the regenerating solution pump 25 is operated to supply the regenerating solution. The regeneration solution is sent to the regeneration processing tank 13 via the path 23. Also, at this time, the water supply valve 18 is opened as necessary to supply water to dilute the regenerating solution.

次いで、図5に示されるように、再生工程が行われる。再生工程では、再生液ポンプ25を停止するとともに供給弁24及び給水弁18を閉じ、出口弁20と入口弁27とを開き、引抜きポンプ22を作動させて循環径路26を介して、再生処理タンク13の底部から引き抜いた再生液を再生処理タンク13の上部から再度供給し、循環する再生液によりイオン交換樹脂12を再生させる。また、所定時間が経過した後に、引抜きポンプ22を停止して必要に応じて一定時間静置させる。   Then, as shown in FIG. 5, a regeneration step is performed. In the regeneration process, the regeneration solution pump 25 is stopped, the supply valve 24 and the water supply valve 18 are closed, the outlet valve 20 and the inlet valve 27 are opened, the withdrawal pump 22 is operated, and the regeneration process tank 26 is operated. The regeneration solution withdrawn from the bottom of the tank 13 is again supplied from the top of the regeneration processing tank 13, and the ion exchange resin 12 is regenerated by the circulating regeneration solution. In addition, after the predetermined time has elapsed, the drawing pump 22 is stopped and allowed to stand for a predetermined time as needed.

イオン交換樹脂12の再生が終了すると、図6に示されるように、再生液排出工程が行われる。再生液排出工程では入口弁27を閉じ、出口弁20と廃液排出弁21とを開き、引抜きポンプ22を作動させて、排水径路19を介してイオン交換樹脂12を循環した再生液を廃液槽16に送る。   When regeneration of the ion exchange resin 12 is completed, as shown in FIG. 6, a regeneration solution discharging step is performed. In the regenerating solution discharging step, the inlet valve 27 is closed, the outlet valve 20 and the waste solution discharging valve 21 are opened, the drawing pump 22 is operated, and the regenerating solution in which the ion exchange resin 12 is circulated through the drainage path 19 is drained. Send to

再生液排出工程後、第2水洗工程が行われる。第2水洗工程は、図7に示されるように、引抜きポンプ22を停止するとともに出口弁20と廃液排出弁21とを閉じ、第1水洗工程と同様に、給水弁18を開き給水タンク15から給水径路17を介して再生処理タンク13に洗浄水を供給した後、図8に示されるように、給水弁18を閉じ、出口弁20と廃液排出弁21とを開き、引抜きポンプ22を作動させて排水径路19を介してイオン交換樹脂12を洗浄した排水を廃液槽16に送液し、導出径路13bを介して再生されたイオン交換樹脂12を導出する。   After the regenerating solution discharging step, the second water washing step is performed. In the second washing step, as shown in FIG. 7, the withdrawal pump 22 is stopped and the outlet valve 20 and the waste liquid discharge valve 21 are closed, and the water supply valve 18 is opened and the water supply tank 15 is opened similarly to the first washing step. After washing water is supplied to the regeneration processing tank 13 via the water supply path 17, as shown in FIG. 8, the water supply valve 18 is closed, the outlet valve 20 and the waste liquid discharge valve 21 are opened, and the drawing pump 22 is operated. The waste water obtained by cleaning the ion exchange resin 12 through the drainage path 19 is sent to the waste liquid tank 16, and the regenerated ion exchange resin 12 is drawn out through the lead path 13b.

本形態例は、上述のように、再生液タンク14から再生液を再生処理タンク13に供給する再生液供給工程の後に、再生処理タンク13に供給された再生液を循環させてイオン交換樹脂12を再生する再生工程を設けたことにより、イオン交換樹脂12の再生効率を高めることができ、再生時間の短縮を図ることができる。   In the present embodiment, as described above, after the regenerating solution supply step of supplying the regenerating solution from the regenerating solution tank 14 to the regeneration processing tank 13, the regeneration solution supplied to the regeneration processing tank 13 is circulated to circulate the ion exchange resin 12 By providing the regeneration step of regenerating the ion exchange resin 12, the regeneration efficiency of the ion exchange resin 12 can be enhanced, and the regeneration time can be shortened.

なお、本発明のイオン交換樹脂は限定されるものではなく、また、再生液はイオン交換樹脂に応じて適宜選択すればよい。さらに、再生処理タンクと再生液タンクとの間に高低差があれば、再生液ポンプを省略することができる。   The ion exchange resin of the present invention is not limited, and the regenerating solution may be appropriately selected according to the ion exchange resin. Furthermore, if there is a difference in height between the regeneration processing tank and the regeneration solution tank, the regeneration solution pump can be omitted.

11…イオン交換樹脂再生装置、12…イオン交換樹脂、13…再生処理タンク、14…再生液タンク、15…給水タンク、16…廃液槽、17…給水径路、18…給水弁、19…排水径路、20…出口弁、21…廃液排出弁、22…引抜きポンプ、23…再生液供給径路、24…供給弁、25…再生液ポンプ、26…循環径路、27…入口弁 DESCRIPTION OF SYMBOLS 11 ... Ion exchange resin regeneration apparatus, 12 ... Ion exchange resin, 13 ... Regeneration processing tank, 14 ... Regeneration liquid tank, 15 ... Water supply tank, 16 ... Waste liquid tank, 17 ... Water supply path, 18 ... Water supply valve, 19 ... Drainage path , 20: outlet valve, 21: waste liquid discharge valve, 22: withdrawal pump, 23: regeneration liquid supply path, 24: supply valve, 25: regeneration liquid pump, 26: circulation path, 27: inlet valve

Claims (1)

イオン交換能力の低下したイオン交換樹脂を収容した再生処理タンクに、再生液を供給して前記イオン交換樹脂を再生するイオン交換樹脂の再生方法において、
前記再生処理タンクにイオン交換能力の低下した前記イオン交換樹脂を収容して洗浄水を供給し、前記イオン交換樹脂を水洗し、イオン交換樹脂洗浄後の洗浄水を排出する第1水洗工程と、
第1水洗工程終了後、再生液タンクから前記再生液を前記再生処理タンクに供給する再生液供給工程と、
前記再生処理タンクに供給された前記再生液を循環させて前記イオン交換樹脂を再生する再生工程と、
前記再生工程が所定時間経過した後に、前記再生液の循環を停止して一定時間静置させる静置工程と、
前記静置工程終了後の前記再生処理タンク内の前記再生液を排出する再生液排出工程と、
該再生液排出工程終了後に、前記再生処理タンクに洗浄水を供給し、前記イオン交換樹脂を水洗し、次いで、前記イオン交換樹脂を洗浄後の洗浄水を排出する第2水洗工程とを有することを特徴とするイオン交換樹脂の再生方法。
In a regeneration method of an ion exchange resin, a regeneration solution is supplied to a regeneration treatment tank containing an ion exchange resin having a reduced ion exchange capacity to regenerate the ion exchange resin,
A first washing step of storing the ion exchange resin having reduced ion exchange capacity in the regeneration treatment tank to supply washing water, washing the ion exchange resin with water, and discharging washing water after washing of the ion exchange resin;
Supplying a regenerating solution from the regenerating solution tank to the regenerating treatment tank after the first washing step;
A regeneration step of recirculating the regeneration solution supplied to the regeneration treatment tank to regenerate the ion exchange resin;
A stationary step of stopping the circulation of the regenerating solution and allowing it to stand for a predetermined time after a predetermined time has elapsed from the regenerating step;
A regenerating solution discharging step of discharging the regenerating solution in the regenerating processing tank after completion of the stationary step;
After completion of the regenerating solution discharging step, the method further comprises the steps of: supplying washing water to the regeneration treatment tank, washing the ion exchange resin with water, and discharging the washing water after washing the ion exchange resin. A method of regenerating an ion exchange resin characterized by
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JP2014133196A (en) * 2013-01-09 2014-07-24 Kobelco Eco-Solutions Co Ltd Phosphoric acid recovery method from sewage sludge incineration ash or steel-making slag

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