JP6535532B2 - Method of regenerating ion exchange resin - Google Patents

Method of regenerating ion exchange resin Download PDF

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JP6535532B2
JP6535532B2 JP2015144557A JP2015144557A JP6535532B2 JP 6535532 B2 JP6535532 B2 JP 6535532B2 JP 2015144557 A JP2015144557 A JP 2015144557A JP 2015144557 A JP2015144557 A JP 2015144557A JP 6535532 B2 JP6535532 B2 JP 6535532B2
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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供給径路を介して再生液を供給し、再生処理タンクの出口から廃液径路を介して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 method for regenerating this ion exchange resin, the regenerating solution is supplied from the regenerating solution tank containing the regenerating solution to the regenerating treatment tank containing the ion exchange resin having a reduced ion exchange capacity through the regenerating solution supply path, There has been one in which the regenerating solution which has passed through the ion exchange resin from the outlet of the tank through the waste liquid passage is 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、イオン交換樹脂の再生が終了した際に、再生処理タンクに残留した再生液は、廃液径路を介して廃液槽に送られ、無駄に廃棄されていた。   However, in the thing of the above-mentioned patent document 1, when reproduction | regeneration of ion exchange resin was complete | finished, the reproduction | regeneration liquid which remained in the reproduction | regeneration processing tank was sent to the waste-liquid tank via the waste-liquid path, and was wasted wastefully.

そこで本発明は、イオン交換樹脂の再生が終了した際に、再生処理タンクに残留した再生液を再生液タンクに戻し、無駄を無くす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。   Therefore, the present invention aims to provide a regeneration method of ion exchange resin that can return the regeneration solution remaining in the regeneration processing tank to the regeneration solution tank and eliminate waste when regeneration of ion exchange resin is completed. There is.

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して前記イオン交換樹脂を再生する再生工程と、前記イオン交換樹脂を再生後の前記再生液を排出する再生液排出工程と、再生液排出工程で排出された前記再生液の状態をセンサでモニターし、前記イオン交換樹脂の再生が終了したことを検知した際に、前記再生液の排出を停止すると共に、前記再生処理タンク内に残留した前記再生液を前記再生処理タンクの中間部に設けられた再生液戻し経路を介して前記再生液タンクに戻す再生液戻し工程と、該再生液戻し工程終了後に、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 regeneration step of supplying the regeneration solution from the regeneration solution tank to the regeneration treatment tank after the first rinsing step, and regenerating the ion exchange resin; and regenerating the ion exchange resin. The state of the regenerating solution discharged in the regenerating solution discharging step of discharging the solution and the regenerating solution discharging step is monitored by a sensor to detect that the regeneration of the ion exchange resin is completed. When, playback stops the discharge of the regenerant, returning the regenerated liquid remaining in the regeneration process tank to the regenerant tank via a regenerant return path provided in the intermediate portion of the regeneration process tank After the completion of the liquid return step and the regenerated liquid return step, washing water is supplied to the regeneration treatment tank, the ion exchange resin is washed with water, and then the ion exchange resin is washed with water. And a process.

本発明のイオン交換樹脂の再生方法によれば、再生液排出工程で排出された前記再生液の状態をセンサによってモニターし、イオン交換樹脂の再生が終了したことを検知した際に、再生液の排出を停止すると共に、再生処理タンク内に残留した再生液を再生液戻し径路を介して再生液タンクに戻す再生液戻し工程を備えていることにより、再生液を無駄にすることなく有効に利用することができ、コストの削減を図ることができる。   According to the method for regenerating an ion exchange resin of the present invention, when the state of the regenerating solution discharged in the regenerating solution discharging step is monitored by a sensor and it is detected that the regeneration of the ion exchange resin is completed, By stopping the discharge and providing the regenerating solution return step of returning the regenerating solution remaining in the regenerating processing tank to the regenerating solution tank through the regenerating solution return path, the regenerating solution is effectively used without wasting it. The cost can be reduced.

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 supplies the reproduction | regeneration liquid to the reproduction | regeneration processing tank at the reproduction | regeneration process. 再生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 | emitting the reproduction | regeneration liquid from the reproduction | regeneration processing tank at the reproduction | regeneration process. 再生液戻し工程で再生処理タンクから再生液タンクに再生液を戻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 returned the reproduction | regeneration liquid from the reproduction | regeneration processing tank to the reproduction | regeneration liquid tank by the reproduction | regeneration liquid return 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、再生処理タンク13からの廃液の状態をモニターするセンサ17とを備えている。   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, a waste liquid tank 16 for storing waste liquid from the regeneration processing tank 13, and a sensor 17 for monitoring the state of waste liquid from the regeneration processing tank 13 are provided.

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1を導出する導出径路13bとが設けられている。再生処理タンク13と給水タンク15との間には給水径路18が設けられ、給水径路18には給水弁19が設けられている。再生処理タンク13と廃液槽16との間には、排水径路20が設けられ、排水径路20の再生処理タンク13側には前記センサ17が設けられるとともに、センサ17よりも下流側に、出口弁21と引抜きポンプ22と廃液排出弁23とが順に設けられている。再生液タンク14の下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24が設けられ、再生液供給径路24には、再生液タンク14側に供給弁25が、再生処理タンク13側に再生液注入弁26がそれぞれ設けられ、供給弁25と再生液注入弁26との間に再生液ポンプ27が配置されている。さらに、再生液タンク14の上部と再生処理タンク13の中間部との間には、再生処理タンク13から再生液を再生液タンク14に戻す再生液戻し径路28が設けられ、再生液戻し径路28には、再生処理タンク13側に余剰再生液排出弁29が、再生液タンク14側に再生液戻し弁30がそれぞれ設けられ、余剰再生液排出弁29と再生液戻し弁30との間に前記再生液ポンプ27が配置されている。また、再生液供給径路24と再生液戻し径路28とは、一部に共通の配管が用いられている。   The regeneration treatment tank 13 is provided with an introduction path 13 a for introducing the ion exchange resin 12 and a lead-out path 13 b for leading the ion exchange resin 1. A water supply passage 18 is provided between the regeneration processing tank 13 and the water supply tank 15, and a water supply valve 19 is provided in the water supply passage 18. A drainage path 20 is provided between the regeneration processing tank 13 and the waste liquid tank 16, and the sensor 17 is provided on the regeneration processing tank 13 side of the drainage path 20, and an outlet valve downstream of the sensor 17 21, a withdrawal pump 22 and a waste liquid discharge valve 23 are provided in order. Between the lower portion of the regenerating solution tank 14 and the upper portion of the regenerating treatment tank 13, a regenerating solution supply path 24 for supplying the regenerating solution is provided. However, the regeneration solution injection valve 26 is provided on the regeneration processing tank 13 side, and the regeneration solution pump 27 is disposed between the supply valve 25 and the regeneration solution injection valve 26. Further, a regeneration liquid return path 28 for returning the regeneration liquid from the regeneration processing tank 13 to the regeneration liquid tank 14 is provided between the upper portion of the regeneration liquid tank 14 and the middle portion of the regeneration processing tank 13. The surplus regeneration liquid discharge valve 29 is provided on the regeneration processing tank 13 side, and the regeneration liquid return valve 30 is provided on the regeneration liquid tank 14 side, and between the surplus regeneration liquid discharge valve 29 and the regeneration liquid return valve 30 A regenerating fluid pump 27 is disposed. In addition, common pipes are used in part for the regeneration liquid supply path 24 and the regeneration liquid return path 28.

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19を開き、給水タンク15から給水径路18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19を閉じて、出口弁21と廃液排出弁23とを開き、引抜きポンプ22を作動させて排水径路20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 19 is opened and washing water is supplied from the water supply tank 15 to the regeneration processing tank 13 via the water supply path 18, as shown in FIG. The water supply valve 19 is closed, the outlet valve 21 and the waste liquid discharge valve 23 are opened, the drawing pump 22 is operated, and the waste water having the ion exchange resin 12 washed is sent to the waste liquid tank 16 via the drainage passage 20.

第1水洗工程終了後、再生工程が行われる。再生工程では、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21と廃液排出弁23とを閉じ、供給弁25と再生液注入弁26とを開き、再生液ポンプ27を作動させて再生液供給径路24を介して再生液を再生処理タンク13に送り、イオン交換樹脂12を再生させる。   After the completion of the first washing step, the regeneration step is performed. In the regeneration step, as shown in FIG. 4, the drawing pump 22 is stopped and the outlet valve 21 and the waste solution discharge valve 23 are closed, the supply valve 25 and the regeneration solution injection valve 26 are opened, and the regeneration solution pump 27 is operated. Then, the regeneration solution is sent to the regeneration processing tank 13 through the regeneration solution supply path 24 to regenerate the ion exchange resin 12.

次いで、図5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、再生液ポンプ27を停止するとともに供給弁25と再生液注入弁26とを閉じ、出口弁21と廃液排出弁23とを開き、引抜きポンプ22を作動させて、排水径路20を介してイオン交換樹脂12を通過した再生液を廃液槽16に送る。   Next, as shown in FIG. 5, a regeneration solution discharging step is performed. In the regenerating solution discharging step, the regenerating solution pump 27 is stopped, the supply valve 25 and the regenerating solution inlet valve 26 are closed, the outlet valve 21 and the waste solution discharging valve 23 are opened, the drawing pump 22 is operated, and the drainage path 20 The regenerated solution that has passed through the ion exchange resin 12 is sent to the waste liquid tank 16 via the

再生処理タンク13から排出されるイオン交換樹脂12を通過した再生液は、排水径路20に設けられたセンサ17によってモニターされ、イオン交換樹脂12の再生が終了したことを検知した際には、再生液戻し工程が行われる。再生液戻し工程は、図6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21と廃液排出弁23とを閉じ、余剰再生液排出弁29と再生液戻し弁30とを開き、再生液ポンプ27を作動させ、再生処理タンク13内に残留した再生液を再生液戻し径路28を介して再生液タンク14に戻す。   The regeneration solution that has passed through the ion exchange resin 12 discharged from the regeneration treatment tank 13 is monitored by the sensor 17 provided in the drainage path 20, and when it is detected that regeneration of the ion exchange resin 12 is completed, regeneration is performed. A liquid return step is performed. In the regenerating solution returning step, as shown in FIG. 6, the drawing pump 22 is stopped, the outlet valve 21 and the waste solution discharging valve 23 are closed, and the excess regenerating solution discharging valve 29 and the regenerating solution return valve 30 are opened. The liquid pump 27 is operated to return the regenerated liquid remaining in the regeneration processing tank 13 to the regenerated liquid tank 14 via the regenerated liquid return path 28.

再生液戻し工程終了後、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、再生液ポンプ27を停止するとともに余剰再生液排出弁29と再生液戻し弁30とを閉じ、第1水洗工程と同様に、給水弁19を開き給水タンク15から給水径路18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19を閉じ、出口弁21と廃液排出弁23とを開き、引抜きポンプ22を作動させて排水径路20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 completion of the regenerating solution returning step, the second water washing step is performed. In the second washing step, as shown in FIG. 7, the regeneration solution pump 27 is stopped, the surplus regeneration solution discharge valve 29 and the regeneration solution return valve 30 are closed, and the water supply valve 19 is After the cleaning water is supplied from the open water supply tank 15 to the regeneration processing tank 13 through the water supply path 18, as shown in FIG. 8, the water supply valve 19 is closed, the outlet valve 21 and the waste liquid discharge valve 23 are opened, The pump 22 is operated to drain the ion exchange resin 12 washed through the drainage passage 20 to the drainage tank 16, and the regenerated ion exchange resin 12 is led out through the lead passage 13b.

本形態例は、上述のように、排水径路20に設けたセンサ17によって、イオン交換樹脂12を通過した再生液の状態をモニターし、イオン交換樹脂12の再生が終了したことを検知した際に、排水径路20を遮断すると共に、再生処理タンク13内に残留した再生液を再生液戻し径路28を介して再生液タンク14に戻す再生液戻し工程を備えていることにより、再生液を無駄にすることなく有効に利用することができ、コストの削減を図ることができる。   In this embodiment, as described above, the state of the regeneration solution having passed through the ion exchange resin 12 is monitored by the sensor 17 provided in the drainage path 20, and it is detected that the regeneration of the ion exchange resin 12 is completed. The waste fluid path 20 is shut off, and the regenerating fluid returning step for returning the regenerating fluid remaining in the regenerating treatment tank 13 to the regenerating fluid tank 14 via the regenerating fluid return route 28 wastes the regenerating fluid. It can be used effectively without doing so, and the cost can be reduced.

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、再生液やセンサは、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 regeneration solution and the sensor 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…イオン交換樹脂生成装置、12…イオン交換樹脂、13…再生処理タンク、13a…導入経路、13b…導出径路、14…再生液タンク、15…給水タンク、16…廃液槽、17…センサ、18…給水径路、19…給水弁、20…排水径路、21…出口弁、22…引抜きポンプ、23…廃液排出弁、24…再生液供給径路、25…供給弁、26…再生液注入弁、27…再生液ポンプ、28…再生液戻し径路、29…余剰再生液排出弁、30…再生液戻し弁 11: Ion exchange resin generator, 12: Ion exchange resin, 13: Regeneration treatment tank, 13a: Introduction path, 13b: Derivation route, 14: Regeneration solution tank, 15: Water supply tank, 16: Waste tank, 17: Sensor, 18 ... water supply path, 19 ... water supply valve, 20 ... drainage path, 21 ... outlet valve, 22 ... withdrawal pump, 23 ... waste liquid discharge valve, 24 ... regeneration liquid supply path, 25 ... supply valve, 26 ... regeneration liquid injection valve, 27: Regeneration fluid pump, 28: Regeneration fluid return path, 29: Excess regeneration fluid discharge valve, 30: Regeneration fluid return 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して前記イオン交換樹脂を再生する再生工程と、
前記イオン交換樹脂を再生後の前記再生液を排出する再生液排出工程と、
再生液排出工程で排出された前記再生液の状態をセンサでモニターし、前記イオン交換樹脂の再生が終了したことを検知した際に、前記再生液の排出を停止すると共に、前記再生処理タンク内に残留した前記再生液を前記再生処理タンクの中間部に設けられた再生液戻し経路を介して前記再生液タンクに戻す再生液戻し工程と、
該再生液戻し工程終了後に、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;
After the completion of the first washing step, a regeneration step of supplying the regeneration solution from the regeneration solution tank to the regeneration treatment tank to regenerate the ion exchange resin;
A regenerating solution discharging step of discharging the regenerating solution after regenerating the ion exchange resin;
The state of the regenerating solution discharged in the regenerating solution discharging step is monitored by a sensor, and when it is detected that the regeneration of the ion exchange resin is completed, the discharging of the regenerating solution is stopped, and A regenerating solution returning step of returning the regenerating solution remaining in the regenerating solution tank to the regenerating solution tank through a regenerating solution return path provided in an intermediate portion of the regenerating treatment tank ;
After the completion of the regenerating solution returning 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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