JPH1094786A - Control method for regenerating softening device - Google Patents

Control method for regenerating softening device

Info

Publication number
JPH1094786A
JPH1094786A JP8274158A JP27415896A JPH1094786A JP H1094786 A JPH1094786 A JP H1094786A JP 8274158 A JP8274158 A JP 8274158A JP 27415896 A JP27415896 A JP 27415896A JP H1094786 A JPH1094786 A JP H1094786A
Authority
JP
Japan
Prior art keywords
raw water
pressure
exchange resin
ion exchange
time
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP8274158A
Other languages
Japanese (ja)
Inventor
Nobuyuki Kobayashi
伸行 小林
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SAMSON CO Ltd
Original Assignee
SAMSON CO Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by SAMSON CO Ltd filed Critical SAMSON CO Ltd
Priority to JP8274158A priority Critical patent/JPH1094786A/en
Publication of JPH1094786A publication Critical patent/JPH1094786A/en
Pending legal-status Critical Current

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  • Treatment Of Water By Ion Exchange (AREA)

Abstract

PROBLEM TO BE SOLVED: To prevent a softening device from being incompletely regenerated by providing a raw water pressure detector for detecting the pressure of a raw water in a raw water supply line and outputting it to a controller, and prolonging the time for a reproducing process when the raw water pressure detected in the raw water pressure detector is lower than a prescribed pressure in the reproduction process. SOLUTION: In the reproduction process of this softening device, the raw water is introduced into a resin column 7 at first and the ion exchange resin is back washed while being stirred. Next, a chemical supplying and pushing-out process is performed by introducing a salt water produced in a salt water vessel 9 into the resin column 7 and ion-exchanging with the ion exchange resin. Finally the salt water in the resin column 7 is discharged and washed. In such a case, when the raw water pressure detected by the raw water pressure detecting device 4 is lower than the setted pressure for the chemical supply and pushing-out process or the setted pressure for washing process in the chemical supply and pushing-out process or the washing process, the control device stops the operation of a timer device 1 for a fixed time and the time for the chemical supply and pushing-out device or the washing process is prolonged by the stopping time of the timer device 1.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明はイオン交換樹脂によって
水の軟化処理を行う軟化装置の再生制御方法に関するも
のである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a regeneration control method for a softening device for softening water with an ion exchange resin.

【0002】[0002]

【従来の技術】給水ライン途中に、イオン交換樹脂を用
いて硬度成分を除去する軟化装置を設置することで、ボ
イラなどの水管中にスケールが付着するのを防止するこ
とが行われている。軟化装置は原水をイオン交換樹脂層
に通水し、原水とイオン交換樹脂の間でイオン交換する
ことにより、原水中の硬度成分を樹脂層内へ取り込むも
のであるため、一定量採水するごとに樹脂の再生を行う
必要がある。
2. Description of the Related Art A softening device for removing a hardness component using an ion exchange resin is installed in a water supply line to prevent scale from adhering to a water pipe of a boiler or the like. The softening device is to pass the raw water through the ion-exchange resin layer and ion-exchange between the raw water and the ion-exchange resin to take in the hardness component in the raw water into the resin layer. It is necessary to regenerate the resin.

【0003】再生の時期は軟水の採水量によって定ま
り、流量計や軟水使用装置の稼働時間などから採水量を
算出し、算出した採水量が設定量に達するごとに再生が
行われる。イオン交換樹脂の再生は、イオン交換樹脂を
攪拌する逆洗工程、イオン交換樹脂層へ塩水を送り、イ
オン交換を行うことでイオン交換樹脂が取り込んでいた
硬度成分を取り出す通薬・押出工程、イオン交換を行っ
た塩水を排出する洗浄工程で行われ、各工程では経過時
間をタイマー装置にて検出しており、経過時間が設定時
間に達すると工程を終了して次の工程に移る。
[0003] The time of regeneration is determined by the amount of water taken out of the soft water, the amount of water taken out is calculated from the operating time of the flow meter or the apparatus using the soft water, and the regeneration is performed every time the calculated amount of water taken out reaches the set amount. Regeneration of the ion-exchange resin consists of a backwashing step in which the ion-exchange resin is agitated, a salt-feeding process that sends salt water to the ion-exchange resin layer, and conducts ion exchange to remove the hardness component that the ion-exchange resin has taken up. This is performed in a washing step of discharging the replaced salt water. In each step, an elapsed time is detected by a timer device, and when the elapsed time reaches a set time, the step ends and the next step is performed.

【0004】再生時、通薬・押出工程は、塩水槽で生成
した塩水を樹脂塔へ送るものであり、通常、原水を駆動
流体としたエゼクタを使用して塩水を塩水槽より吸引
し、樹脂塔内へ注入する。通薬・押出工程時間内に塩水
とイオン交換樹脂の接触を完了させるためには、原水圧
力が所定圧力以上必要である。また、洗浄工程の場合
も、原水の圧力を利用してイオン交換樹脂層内の塩水を
排出するものであるため、原水圧力は高くなければなら
ない。そのため、再生時に原水圧力が低下して原水圧力
が所定の圧力よりも低くなると、通薬工程においてはエ
ゼクタの塩水吸引速度が低下し、押出工程において、樹
脂塔内に注入された塩水が全てのイオン交換樹脂と接触
しきらないうちに洗浄工程に移行して塩水が流し出され
てしまうので、イオン交換樹脂の再生が不完全となり、
硬度成分の含まれた水が取り出される硬度リークを発生
することとなる。また、通薬・押出工程中にイオン交換
樹脂の再生が行われた場合であっても、洗浄工程中に原
水圧力が低下すれば、軟化処理再開時に洗浄しきれなか
った塩水が処理水にリークし、同時に微量の硬度成分も
処理水中にリークする。原水圧力が低下するのは希な現
象であっても、硬度リークを防止するためには原水圧力
が低下することを見越した設定を行っておく必要があ
り、工程時間や使用水量を多く設定しなければならなか
った。
At the time of regeneration, the drug passing / extrusion step is to send the salt water generated in the salt water tank to the resin tower. Usually, the salt water is sucked from the salt water tank using an ejector using raw water as a driving fluid, and the resin is pumped. Inject into the tower. In order to complete the contact between the salt water and the ion exchange resin within the time of the drug passing / extrusion process, the raw water pressure needs to be equal to or higher than a predetermined pressure. Also, in the case of the washing step, since the salt water in the ion exchange resin layer is discharged using the pressure of the raw water, the pressure of the raw water must be high. Therefore, when the raw water pressure decreases during regeneration and the raw water pressure becomes lower than a predetermined pressure, the salt water suction speed of the ejector decreases in the drug passing step, and in the extrusion step, all the salt water injected into the resin tower is discharged. Before the ion-exchange resin is fully contacted, the process shifts to the washing process and the salt water flows out, so the regeneration of the ion-exchange resin becomes incomplete,
A water leak containing a hardness component is taken out, which causes a hardness leak. Also, even if the ion exchange resin is regenerated during the drug passing / extrusion process, if the raw water pressure drops during the washing process, the salt water that could not be completely washed when the softening process was restarted leaked into the treated water. At the same time, a small amount of hardness components also leak into the treated water. Even if it is a rare phenomenon that the raw water pressure decreases, it is necessary to make settings in anticipation that the raw water pressure will decrease in order to prevent hardness leaks. I had to.

【0005】[0005]

【発明が解決しようとする課題】本発明が解決しようと
する課題は、原水圧力が正常範囲にありながら再生工程
を必要以上に行ったり、原水圧力が低下することで再生
が不完全に終わることを防止することのできる軟化装置
の再生制御方法を提供することにある。
The problem to be solved by the present invention is that the regeneration step is performed more than necessary while the raw water pressure is in a normal range, or the regeneration is incompletely completed due to a decrease in the raw water pressure. It is an object of the present invention to provide a regeneration control method for a softening device, which can prevent the occurrence of swelling.

【0006】[0006]

【課題を解決するための手段】容器内にイオン交換樹脂
を充填した樹脂塔、塩水を生成する塩水槽、樹脂塔およ
び塩水槽への原水供給や処理水の取り出しを行うコント
ロールバルブ、コントロールバルブの制御を行う制御装
置をそれぞれ設け、原水給水ラインからコントロールバ
ルブへ送られた原水を樹脂塔内のイオン交換樹脂層へ通
水することによって軟化処理を行い、樹脂塔内のイオン
交換樹脂層へ定期的に塩水を供給することでイオン交換
樹脂の再生を行っており、再生の工程では制御装置に内
蔵したタイマー装置によって経過時間を検出し、経過時
間が設定時間に達すると再生の工程を終了させている軟
化装置において、原水給水ライン中の原水の圧力を検出
して制御装置へ出力する原水圧力検出装置を設けてお
き、再生工程時に原水圧力検出装置にて検出された原水
圧力が所定の圧力よりも低い場合、再生工程の時間を延
長することで再生を完全に行わせる。
Means for Solving the Problems A resin tower filled with ion exchange resin in a container, a salt water tank for generating salt water, a control valve for supplying raw water to the resin tower and the salt water tank and taking out treated water, and a control valve A control device is provided to perform control, and the raw water sent from the raw water supply line to the control valve is passed through the ion exchange resin layer in the resin tower to perform softening treatment, and is periodically sent to the ion exchange resin layer in the resin tower. The ion-exchange resin is regenerated by supplying salt water in an appropriate manner.In the regeneration process, the elapsed time is detected by a timer device built into the control device, and when the elapsed time reaches the set time, the regeneration process is terminated. In the softening device, a raw water pressure detecting device for detecting the pressure of the raw water in the raw water supply line and outputting the detected pressure to the control device is provided. If the detected raw water pressure at the pressure sensing device is lower than a predetermined pressure, thereby completely perform reproduction by extending the regeneration step time.

【0007】[0007]

【実施例】本発明の一実施例を図面を用いて説明する。
軟化装置はイオン交換樹脂の充填された樹脂塔7、各通
水を制御するコントロールバルブ8、塩水を生成する塩
水槽9、制御装置10からなる。原水給水ライン2の先
端はコントロールバルブ8に接続されており、制御装置
10によってコントロールバルブ8を制御することで、
原水給水ライン2を送られた原水はコントロールバルブ
8を通して樹脂塔7または塩水槽9へ送られる。原水給
水ライン2途中には原水の圧力を検出する原水圧力検出
装置4を設けておき、原水圧力検出装置4で検出した原
水圧力は制御装置10へ送られるようにしている。
An embodiment of the present invention will be described with reference to the drawings.
The softening device comprises a resin tower 7 filled with an ion exchange resin, a control valve 8 for controlling each water flow, a salt water tank 9 for producing salt water, and a control device 10. The tip of the raw water supply line 2 is connected to the control valve 8, and the control device 10 controls the control valve 8 to
The raw water sent through the raw water supply line 2 is sent to the resin tower 7 or the salt water tank 9 through the control valve 8. A raw water pressure detecting device 4 for detecting the pressure of raw water is provided in the raw water supply line 2, and the raw water pressure detected by the raw water pressure detecting device 4 is sent to the control device 10.

【0008】軟化処理を行う場合、制御装置10は原水
が樹脂塔7へ送られるようにコントロールバルブ8を調
節し、原水を樹脂塔7へ導入する。樹脂塔7内ではイオ
ン交換樹脂によって原水中の硬度成分が取り除かれ、処
理された軟水がコントロールバルブ8、処理水供給ライ
ン3を通って軟水タンク6へ送られる。処理水供給ライ
ン3途中には流量計5が設けられ、流量計5で検出した
流量は制御装置10へ送られる。制御装置10では流量
計5から得られる流量を積算し、積算された採水量が設
定値に達するとイオン交換樹脂の再生を行う。
When performing the softening treatment, the controller 10 adjusts the control valve 8 so that the raw water is sent to the resin tower 7, and introduces the raw water into the resin tower 7. In the resin tower 7, the hardness component in the raw water is removed by the ion exchange resin, and the treated soft water is sent to the soft water tank 6 through the control valve 8 and the treated water supply line 3. A flow meter 5 is provided in the middle of the treated water supply line 3, and the flow rate detected by the flow meter 5 is sent to the control device 10. The control device 10 integrates the flow rate obtained from the flow meter 5, and regenerates the ion exchange resin when the integrated water sampling amount reaches a set value.

【0009】軟化装置の再生工程では、まず原水を樹脂
塔7へ導入し、イオン交換樹脂を攪拌する逆洗が行われ
る。制御装置10では、逆洗工程の開始とともに、制御
装置10に内蔵しているタイマー装置1の作動を開始さ
せ経過時間を検出する。タイマー装置1にて検出してい
る経過時間が逆洗工程の設定時間に達すると逆洗工程を
終了する。
In the regeneration step of the softening device, first, raw water is introduced into the resin tower 7 and backwashing is performed in which the ion exchange resin is stirred. The control device 10 starts the operation of the timer device 1 incorporated in the control device 10 at the same time as the start of the backwashing process, and detects the elapsed time. When the elapsed time detected by the timer device 1 reaches the set time of the backwashing step, the backwashing step is ended.

【0010】逆洗工程が終了すると、制御装置10はコ
ントロールバルブ8の変更を行い、塩水槽9内で生成し
た塩水を樹脂塔7へ導入し、イオン交換樹脂との間でイ
オン交換を行わせる通薬・押出工程を行う。通薬・押出
工程時もタイマー装置1の作動を行わせて経過時間の検
出を行い、経過時間が通薬・押出工程の設定時間に達す
ると、通薬・押出工程を終了する。通薬・押出工程は原
水の圧力が重要であり、原水圧力検出装置4によって検
出された原水圧力によって通薬・押出工程時間が調整さ
れる。通薬・押出工程時に、検出している原水圧力が通
薬・押出工程用設定圧力を下回った場合、制御装置10
は一定時間タイマー装置1の作動を停止し、通薬・押出
工程の時間をタイマー装置停止時間分長くする。
When the backwashing step is completed, the control device 10 changes the control valve 8, introduces the salt water generated in the salt water tank 9 into the resin tower 7, and causes ion exchange with the ion exchange resin. Perform the drug delivery and extrusion process. At the time of the drug passing / extrusion step, the timer device 1 is operated to detect the elapsed time, and when the elapsed time reaches the set time of the drug passing / extrusion step, the drug passing / extrusion step is terminated. The pressure of raw water is important in the drug passing / extruding step, and the drug passing / extruding step time is adjusted by the raw water pressure detected by the raw water pressure detecting device 4. If the detected raw water pressure is lower than the set pressure for the drug-delivery / extrusion process during the drug-delivery / extrusion process, the control device 10
Stops the operation of the timer device 1 for a certain period of time, and prolongs the time of the drug delivery / extrusion process by the timer device stop time.

【0011】通薬・押出工程が終了すると、制御装置1
0はコントロールバルブ8の変更を行い、樹脂塔7内の
塩水を排出する洗浄工程を行う。洗浄工程時もタイマー
装置1の作動を行わせて経過時間の検出を行い、タイマ
ー装置1で検出している経過時間が洗浄工程の設定時間
に達すると、洗浄工程を終了する。また、洗浄工程時に
も原水圧力検出装置4によって原水圧力を検出してお
り、検出している原水圧力が洗浄工程用設定圧力を下回
った場合、制御装置10は一定時間タイマー装置の作動
を停止し、洗浄工程の時間をタイマー装置停止時間分長
くする。
[0011] When the drug delivery / extrusion process is completed, the control device 1
At 0, the control valve 8 is changed, and a washing step of discharging the salt water in the resin tower 7 is performed. During the cleaning process, the timer device 1 is operated to detect the elapsed time, and when the elapsed time detected by the timer device 1 reaches the set time of the cleaning process, the cleaning process ends. The raw water pressure is also detected by the raw water pressure detecting device 4 during the cleaning process, and when the detected raw water pressure falls below the set pressure for the cleaning process, the control device 10 stops the operation of the timer device for a certain period of time. In addition, the time of the cleaning process is lengthened by the stop time of the timer device.

【0012】なお、本実施例では、通薬・押出工程時ま
たは洗浄工程時に原水圧力が低下した時には該工程を一
定時間延長させるものであるが、原水圧力低下時間を検
出しておき、原水圧力低下時間から工程延長時間の換算
を行い、換算して求めた時間分工程時間を延長させるよ
うにしてもよい。
In this embodiment, when the pressure of the raw water drops during the drug passing / extrusion step or the washing step, the step is extended for a certain period of time. The process extension time may be converted from the decrease time, and the process time may be extended by the calculated time.

【0013】[0013]

【発明の効果】本発明を実施することによって、原水圧
力が正常範囲にある場合には、再生工程を必要以上に行
うことで必要以上の水を使用するといったことはなく、
原水圧力が低下した場合には再生工程の時間を延長する
ことで再生が不完全に終了することを防止することがで
きる。
According to the present invention, when the raw water pressure is within the normal range, the regeneration step is performed more than necessary, so that more water than necessary is not used.
When the pressure of the raw water drops, the time of the regeneration step is extended to prevent incomplete regeneration.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の一実施例を実施した軟化装置の概要図 1 タイマー装置 2 原水給水ライン 3 処理水供給ライン 4 原水圧力検出装置 5 流量計 6 軟水タンク 7 樹脂塔 8 コントロールバルブ 9 塩水槽 10 制御装置FIG. 1 is a schematic diagram of a softening device embodying an embodiment of the present invention. 1 Timer device 2 Raw water supply line 3 Treated water supply line 4 Raw water pressure detection device 5 Flow meter 6 Soft water tank 7 Resin tower 8 Control valve 9 Salt water tank 10 Control device

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】容器内にイオン交換樹脂を充填した樹脂
塔、塩水を生成する塩水槽、樹脂塔および塩水槽への原
水供給や処理水の取り出しを行うコントロールバルブ、
コントロールバルブの制御を行う制御装置をそれぞれ設
け、原水給水ラインからコントロールバルブへ送られた
原水を樹脂塔内のイオン交換樹脂層へ通水することによ
って軟化処理を行い、樹脂塔内のイオン交換樹脂層へ定
期的に塩水を供給することでイオン交換樹脂の再生を行
っており、再生の工程では制御装置に内蔵したタイマー
装置によって経過時間を検出し、経過時間が設定時間に
達すると再生の工程を終了させている軟化装置におい
て、原水給水ライン中の原水の圧力を検出して制御装置
へ出力する原水圧力検出装置を設けておき、再生工程時
に原水圧力検出装置にて検出された原水圧力が所定の圧
力よりも低い場合、再生工程の時間を延長することを特
徴とする軟化装置の再生制御方法。
1. A resin tower filled with an ion exchange resin in a container, a salt water tank for generating salt water, a control valve for supplying raw water to the resin tower and the salt water tank and for taking out treated water,
A control device that controls the control valve is provided, and the raw water sent from the raw water supply line to the control valve is passed through the ion exchange resin layer in the resin tower to perform softening treatment, and the ion exchange resin in the resin tower is The ion exchange resin is regenerated by periodically supplying salt water to the bed. In the regeneration process, the elapsed time is detected by a timer device built in the control device, and when the elapsed time reaches the set time, the regeneration process is performed. In the softening device, the raw water pressure detecting device that detects the pressure of the raw water in the raw water supply line and outputs it to the control device is provided, and the raw water pressure detected by the raw water pressure detecting device during the regeneration process is A regeneration control method for a softening device, wherein the regeneration step is extended when the pressure is lower than a predetermined pressure.
JP8274158A 1996-09-24 1996-09-24 Control method for regenerating softening device Pending JPH1094786A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8274158A JPH1094786A (en) 1996-09-24 1996-09-24 Control method for regenerating softening device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8274158A JPH1094786A (en) 1996-09-24 1996-09-24 Control method for regenerating softening device

Publications (1)

Publication Number Publication Date
JPH1094786A true JPH1094786A (en) 1998-04-14

Family

ID=17537848

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8274158A Pending JPH1094786A (en) 1996-09-24 1996-09-24 Control method for regenerating softening device

Country Status (1)

Country Link
JP (1) JPH1094786A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2497750A1 (en) 2011-03-11 2012-09-12 HUSTY M. Styczen, J. Hupert Spolka Jawna Water treatment system, a method of its automatic regeneration and a controller for the water treatment system
CN109879370A (en) * 2018-12-28 2019-06-14 中国环境科学研究院 Efficiently softening water treatment facilities

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2497750A1 (en) 2011-03-11 2012-09-12 HUSTY M. Styczen, J. Hupert Spolka Jawna Water treatment system, a method of its automatic regeneration and a controller for the water treatment system
CN109879370A (en) * 2018-12-28 2019-06-14 中国环境科学研究院 Efficiently softening water treatment facilities

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