TW202019830A - water softener - Google Patents

water softener Download PDF

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Publication number
TW202019830A
TW202019830A TW108132146A TW108132146A TW202019830A TW 202019830 A TW202019830 A TW 202019830A TW 108132146 A TW108132146 A TW 108132146A TW 108132146 A TW108132146 A TW 108132146A TW 202019830 A TW202019830 A TW 202019830A
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Taiwan
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water
exchange resin
ion exchange
tank
brine
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TW108132146A
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Chinese (zh)
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高島孝輔
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日商東麗股份有限公司
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Priority claimed from JP2018166656A external-priority patent/JP2020039992A/en
Priority claimed from JP2018170399A external-priority patent/JP2020040028A/en
Application filed by 日商東麗股份有限公司 filed Critical 日商東麗股份有限公司
Publication of TW202019830A publication Critical patent/TW202019830A/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J49/00Regeneration or reactivation of ion-exchangers; Apparatus therefor
    • B01J49/05Regeneration or reactivation of ion-exchangers; Apparatus therefor of fixed beds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J49/00Regeneration or reactivation of ion-exchangers; Apparatus therefor
    • B01J49/50Regeneration or reactivation of ion-exchangers; Apparatus therefor characterised by the regeneration reagents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J49/00Regeneration or reactivation of ion-exchangers; Apparatus therefor
    • B01J49/75Regeneration or reactivation of ion-exchangers; Apparatus therefor of water softeners
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J49/00Regeneration or reactivation of ion-exchangers; Apparatus therefor
    • B01J49/80Automatic regeneration
    • B01J49/85Controlling or regulating devices therefor
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/42Treatment of water, waste water, or sewage by ion-exchange

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Treatment Of Water By Ion Exchange (AREA)

Abstract

The present invention is a water softener (1) for softening water by passing to-be-treated water through an ion-exchange resin (9), the water softener comprising: an ion-exchange resin-filled tank (2) filled with the ion-exchange resin (9); a saltwater tank (4) for storing saltwater (14) for regenerating the ion-exchange resin (9); and a controller (13) for switching between a water softening operation in which water is softened by passing the to-be-treated water through the ion-exchange resin (9) in the ion-exchange resin-filled tank (2), a washing operation in which the interior of the ion-exchange resin-filled tank (2) is washed, a regenerating operation in which the saltwater (14) in the saltwater tank (4) is passed through the ion-exchange resin (9) in the ion-exchange resin-filled tank (2) to regenerate the ion-exchange resin (9), and a water-supplying operation in which water is supplied to the interior of the saltwater tank (4).

Description

軟水器water softener

本發明係關於使被處理水通水於已填充離子交換樹脂的離子交換樹脂填充槽中,施行軟水化處理的軟水器。The present invention relates to a water softener for passing water to be treated in an ion exchange resin filled tank filled with ion exchange resin, and performing a water softening treatment.

使用離子交換樹脂的軟水器中,作為防止在停電恢復後朝藥液槽之逆流等不需要的水流入之手段,係構成為在開始進行流路控制閥的位置初始化處理之前,判斷藥液閥是否關閉,在藥液閥呈開啟狀態時,係於最初施行藥液閥的位置初始化處理後才施行關閉藥液閥的控制,在藥液閥呈關閉狀態時,則在藥液閥的位置初始化處理之前,先行進行旁通閥、入水閥及採水閥的位置初始化處理(參照專利文獻1)。另外,專利文獻1的軟水器雖可防止藥液閥逆流等,但有若在離子交換樹脂填充槽內有殘留藥液狀態進行通水,則藥液被出水的問題。又,使用藥液時,有再生處理時所需要的藥液量不足而離子交換樹脂之再生不足的問題。In the water softener using ion exchange resin, as a means to prevent the inflow of unnecessary water such as backflow to the chemical liquid tank after the power failure is restored, it is configured to determine the chemical liquid valve before starting the position initialization process of the flow path control valve Whether to close, when the chemical liquid valve is in the open state, the control of closing the chemical liquid valve is implemented after the initial processing of the initial position of the chemical liquid valve is performed, and when the chemical liquid valve is closed, the position of the chemical liquid valve is initialized Before the processing, the position initialization processing of the bypass valve, the water inlet valve, and the water collection valve is performed (refer to Patent Document 1). In addition, although the water softener of Patent Document 1 can prevent backflow of the chemical solution valve, etc., there is a problem that if the residual chemical solution is passed through the ion-exchange resin filling tank, the chemical solution is discharged. In addition, when the chemical solution is used, there is a problem that the amount of the chemical solution required for the regeneration process is insufficient and the regeneration of the ion exchange resin is insufficient.

另一方面,使用離子交換樹脂的軟水器,若未通水而使被處理水長時間持續滯留於離子交換樹脂填充槽內,則有機物等從離子交換樹脂溶出至離子交換樹脂填充槽內的被處理水內,因該等有機物等而被處理水遭著色。所以,有提案:若離子交換樹脂填充槽未通水狀態(以下稱「非通水狀態」)持續一定時間,則自動施行離子交換樹脂填充槽內之洗淨運轉的軟水器(參照專利文獻2)。 [先前技術文獻] [專利文獻]On the other hand, in a water softener using ion exchange resin, if the water to be treated is left in the ion exchange resin filled tank for a long period of time, organic substances and the like are eluted from the ion exchange resin into the ion exchange resin filled tank. In the treated water, the treated water is colored due to such organic substances. Therefore, there is a proposal that if the ion-exchange resin filling tank is not in a water-passing state (hereinafter referred to as "non-water-passing state") for a certain period of time, a water softener that automatically performs the washing operation in the ion-exchange resin filling tank (see Patent Document 2 ). [Prior Technical Literature] [Patent Literature]

專利文獻1:日本專利特開2010-247103號公報 專利文獻2:日本專利特開2001-246376號公報Patent Document 1: Japanese Patent Laid-Open No. 2010-247103 Patent Document 2: Japanese Patent Laid-Open No. 2001-246376

(發明所欲解決之問題)(Problems to be solved by the invention)

然而,專利文獻2所提案的軟水器,因為在非通水狀態持續一定時間後才進行洗淨運轉,故視非通水狀態開始時刻不同而每次開始進行洗淨運轉的時段亦各不同。例如有時在通水頻率較高的晚間時段開始進行洗淨運轉。若在洗淨運轉中進行通水,則有從原水入口管進入的被處理水直接流出至軟水出口管的問題。 (解決問題之技術手段)However, the water softener proposed in Patent Document 2 performs the washing operation after the non-watering state continues for a certain period of time, so the time period for starting the washing operation differs depending on the starting time of the non-watering state. For example, the washing operation may be started in the evening period when the frequency of passing water is high. If water is passed during the washing operation, there is a problem that the treated water entering from the raw water inlet pipe directly flows out to the soft water outlet pipe. (Technical means to solve problems)

(1)解決上述課題的本發明一實施態樣之軟水器,係使被處理水通水於離子交換樹脂而施行軟水化處理的軟水器,具備有: 離子交換樹脂填充槽,其係填充著離子交換樹脂; 鹽水槽,其係用於儲存著對離子交換樹脂進行再生的鹽水;以及 控制部,其切換下述運轉:軟水化運轉,係使被處理水通水於上述離子交換樹脂填充槽內的上述離子交換樹脂,而進行軟水化;洗淨運轉,係將上述離子交換樹脂填充槽的內部洗淨;再生運轉,係使上述鹽水槽內的上述鹽水通水於上述離子交換樹脂填充槽內的上述離子交換樹脂,而進行離子交換樹脂的再生;及給水運轉,係將水供應至上述鹽水槽內部; 上述控制部係以在既定時刻施行上述洗淨運轉之方式進行控制。 (2)本發明一實施態樣的軟水器,較佳係上述既定時刻為在上午0點至上午6點之期間。 (3)本發明一實施態樣的軟水器,上述既定時刻亦可每日為相同時刻。 (4)本發明一實施態樣的軟水器,係使被處理水通水於離子交換樹脂而施行軟水化處理的軟水器,具備有: 離子交換樹脂填充槽,其係填充著離子交換樹脂; 鹽水槽,其係用於儲存對離子交換樹脂進行再生的鹽水;以及 控制部,其切換下述運轉:軟水化運轉,係使被處理水通水於上述離子交換樹脂填充槽內的上述離子交換樹脂,而進行軟水化;洗淨運轉,係將上述離子交換樹脂填充槽的內部洗淨;再生運轉,係使上述鹽水槽內的上述鹽水通水於上述離子交換樹脂填充槽內的上述離子交換樹脂,而進行離子交換樹脂的再生;及給水運轉,係將水供應至上述鹽水槽內部; 上述控制部係以在剛對該控制部供應電氣後,進行上述洗淨運轉與上述給水運轉之方式進行控制。 (對照先前技術之功效)(1) A water softener according to an embodiment of the present invention that solves the above-mentioned problems is a water softener that allows water to be treated to pass through an ion exchange resin to perform a water softening treatment, and includes: Ion exchange resin filled tank, which is filled with ion exchange resin; Brine tank, which is used to store brine for regeneration of ion exchange resin; and The control unit switches the following operations: the dehydration operation is to pass the water to be treated through the ion exchange resin in the ion exchange resin filling tank to perform dehydration; the washing operation is to fill the ion exchange resin The inside of the tank is cleaned; the regeneration operation is to allow the brine in the brine tank to pass water to the ion exchange resin in the ion exchange resin filling tank to regenerate the ion exchange resin; and the water supply operation is to supply water To the inside of the above brine tank; The control unit performs control so as to execute the cleaning operation at a predetermined time. (2) The water softener according to an embodiment of the present invention is preferably the above-mentioned predetermined time from 0am to 6am. (3) In the water softener according to an embodiment of the present invention, the predetermined time may be the same time every day. (4) A water softener according to an embodiment of the present invention is a water softener that allows water to be treated to pass through an ion exchange resin to perform water softening treatment, and includes: Ion exchange resin filled tank, which is filled with ion exchange resin; Brine tank, which is used to store brine for regeneration of ion exchange resin; and The control unit switches the following operations: a dehydration operation, in which the water to be treated is passed through the ion exchange resin in the ion exchange resin filling tank to perform dehydration; a washing operation, in which the ion exchange resin is filled The inside of the tank is washed; the regeneration operation is to allow the brine in the brine tank to pass water to the ion exchange resin in the ion exchange resin filling tank to regenerate the ion exchange resin; and the water supply operation is to supply water To the inside of the above brine tank; The control unit performs control such that the washing operation and the water supply operation are performed immediately after the control unit is supplied with electricity. (Comparing the efficacy of the previous technology)

本發明的軟水器可設定成在每日的既定時刻實施離子交換樹脂填充槽內之洗淨運轉。所以,若在洗淨運轉中進行通水,雖導致從原水入口管流入的被處理水流出至軟水出口管,但藉由將既定時刻設定在未施行通水的時段,可防止此種不良情況發生。The water softener of the present invention can be set to perform the washing operation in the ion exchange resin filling tank at a predetermined time every day. Therefore, if the water is passed during the washing operation, the treated water flowing from the raw water inlet pipe will flow out to the soft water outlet pipe, but by setting the predetermined time at the time when the water is not implemented, this kind of bad situation can be prevented occur.

[軟水器之構成] 針對本發明的軟水器一實施形態,根據圖式進行說明。參照圖1。軟水器1係具備有:收納著離子交換樹脂9的離子交換樹脂填充槽2、在離子交換樹脂填充槽2上面切換原水等之通水方向的控制閥3、控制著控制閥3的控制部13、及用於儲存對離子交換樹脂進行再生之鹽水14的鹽水槽4。於控制閥3分別連接設置:供應原水的原水入口管5、供應軟水的軟水出口管6、以及排水出口管7。鹽水槽4與離子交換樹脂填充槽2係經由控制閥3且利用鹽水管12連接設置。[Composition of water softener] An embodiment of the water softener of the present invention will be described based on the drawings. Refer to Figure 1. The water softener 1 is provided with an ion exchange resin filled tank 2 containing ion exchange resin 9, a control valve 3 that switches the direction of passage of raw water or the like on the ion exchange resin filled tank 2, and a control unit 13 that controls the control valve 3 And a brine tank 4 for storing brine 14 that regenerates the ion exchange resin. Connected to the control valve 3 are: a raw water inlet pipe 5 for supplying raw water, a soft water outlet pipe 6 for supplying soft water, and a drain outlet pipe 7. The brine tank 4 and the ion-exchange resin filled tank 2 are connected and installed via a control valve 3 and a brine pipe 12.

離子交換樹脂填充槽2係內部填充著既定量之離子交換樹脂9的有底筒形容器。從原水入口管5供應的原水成為被處理水,經由控制閥3與上過濾器10流入於離子交換樹脂填充槽2內。然後,藉由被處理水通過離子交換樹脂填充槽2內、被施行軟水化處理而成為軟水。軟水係從下過濾器11進入至集水管8,通過集水管8,經由控制閥3從軟水出口管6流出。The ion exchange resin filling tank 2 is a bottomed cylindrical container filled with a predetermined amount of ion exchange resin 9. The raw water supplied from the raw water inlet pipe 5 becomes treated water, and flows into the ion exchange resin filling tank 2 via the control valve 3 and the upper filter 10. Then, the treated water passes through the ion-exchange resin filling tank 2 and is subjected to softening treatment to become softened water. The soft water system enters the water collecting pipe 8 from the lower filter 11, passes through the water collecting pipe 8, and flows out of the soft water outlet pipe 6 via the control valve 3.

上過濾器10係具有離子交換樹脂9不致漏出、使被處理水通過的過濾器機能。所以,在上過濾器10所形成開口的大小係小於離子交換樹脂9的粒徑。又,為了降低通水時的壓力損失,上過濾器10的開口率最好在強度容許範圍內越大越好。同樣地,下過濾器11亦具有具有離子交換樹脂9不致漏出、使被處理水通過的過濾器機能。所以,在下過濾器11所形成開口的大小係小於離子交換樹脂9的粒徑。又,為了降低通水時的壓力損失,下過濾器11的開口率最好在強度容許範圍內越大越好。The upper filter 10 has a filter function that allows the ion-exchange resin 9 not to leak and to pass the water to be treated. Therefore, the size of the opening formed in the upper filter 10 is smaller than the particle size of the ion exchange resin 9. In addition, in order to reduce the pressure loss when passing water, the opening ratio of the upper filter 10 is preferably as large as possible within the allowable range of strength. Similarly, the lower filter 11 has a filter function that allows the ion-exchange resin 9 not to leak out and allows the water to be treated to pass through. Therefore, the size of the opening formed in the lower filter 11 is smaller than the particle size of the ion exchange resin 9. In addition, in order to reduce the pressure loss when passing water, the opening ratio of the lower filter 11 is preferably as large as possible within the allowable range of strength.

控制部13係由具備有控制軟水器各部位之微電腦的控制基板所構成。控制部13具備有:用於判斷是否開始進行後述離子交換樹脂9之再生運轉、洗淨運轉之作為計時手段的計時器A、計數朝離子交換樹脂填充槽2的累計通水量之計數器、以及計數朝離子交換樹脂填充槽2的總通水量之計數器。The control unit 13 is composed of a control board equipped with a microcomputer that controls various parts of the water softener. The control unit 13 includes a timer A as a timing means for judging whether to start the regeneration operation and cleaning operation of the ion exchange resin 9 described later, a counter that counts the cumulative water flow rate toward the ion exchange resin filling tank 2, and a count A counter of the total water flow rate of the tank 2 filled with ion exchange resin.

[軟水器動作] 其次,針對依此構成的軟水器1之動作進行說明。軟水器1係除進行供應軟水的軟水化運轉之外,尚進行逆洗淨運轉、再生運轉、正洗淨運轉、給水運轉等各種運轉。利用軟水器1所具備控制部13的控制,自動地適時進行離子交換樹脂9之再生運轉、逆洗淨運轉。另外,本案合併將逆洗淨運轉與正洗淨運轉稱為「洗淨運轉」。[Water softener action] Next, the operation of the water softener 1 configured as above will be described. In addition to the softening operation for supplying soft water, the water softener 1 also performs various operations such as reverse cleaning operation, regeneration operation, forward cleaning operation, and water supply operation. Under the control of the control unit 13 included in the water softener 1, the regeneration operation and the reverse cleaning operation of the ion exchange resin 9 are automatically performed in a timely manner. In addition, in this case, the reverse cleaning operation and the forward cleaning operation are called "cleaning operation".

[軟水化運轉] 針對軟水化運轉使用圖2進行說明。軟水化運轉係將屬於被處理水的原水施行軟水化之步驟。使從原水入口管5供應的被處理水經由控制閥3流入於上過濾器10中,再從上過濾器10朝下流入於離子交換樹脂填充槽2內。然後,利用離子交換樹脂9的作用,將屬於硬水的被處理水形成為軟水。然後,使軟水流入於下過濾器11,通過集水管8,經由控制閥3流出於軟水出口管6。[Softening operation] The softening operation will be described using FIG. 2. The softening operation is a step of softening the raw water belonging to the treated water. The water to be treated supplied from the raw water inlet pipe 5 flows into the upper filter 10 via the control valve 3, and then flows into the ion exchange resin filling tank 2 downward from the upper filter 10. Then, by the action of the ion exchange resin 9, the water to be treated that belongs to hard water is formed into soft water. Then, soft water flows into the lower filter 11, passes through the water collecting pipe 8, and flows out through the control valve 3 into the soft water outlet pipe 6.

[逆洗淨運轉] 針對逆洗淨運轉使用圖3進行說明。逆洗淨運轉係對離子交換樹脂填充槽2施行與軟水化運轉呈反方向的通水,而將離子交換樹脂9所附著之異物排出的步驟。利用控制部13切換控制閥3的流路,使來自原水入口管5的原水,經由控制閥3通過集水管8流入於下過濾器11。然後,原水在離子交換樹脂填充槽2的內部從下側朝上側流動,再流入於上過濾器10。最後,將含異物的原水經由控制閥3從排水出口管7排出。[Reverse cleaning operation] The reverse cleaning operation will be described using FIG. 3. The reverse cleaning operation is a step of discharging water to the ion-exchange resin filling tank 2 in the opposite direction to the dehydration operation, and discharging the foreign matter adhering to the ion-exchange resin 9. The control unit 13 switches the flow path of the control valve 3 so that the raw water from the raw water inlet pipe 5 flows into the lower filter 11 through the water collecting pipe 8 through the control valve 3. Then, the raw water flows from the lower side to the upper side in the ion exchange resin filling tank 2, and then flows into the upper filter 10. Finally, the raw water containing foreign matter is discharged from the drain outlet pipe 7 via the control valve 3.

[再生運轉] 針對再生運轉使用圖4進行說明。再生運轉係使鹽水流入於離子交換樹脂填充槽2內的離子交換樹脂9,而施行離子交換樹脂9之再生處理的步驟。利用控制部13切換控制閥3的流路,使鹽水槽4內的鹽水14通過鹽水管12,經由控制閥3流入於上過濾器10。然後,使鹽水從上過濾器10在離子交換樹脂填充槽2內朝下流動,而施行離子交換樹脂9的再生。使離子交換樹脂9之再生處理時所使用的鹽水,流入於下過濾器11,再通過集水管8,經由控制閥3從排水出口管7排出。[Regeneration operation] The regeneration operation will be described using FIG. 4. The regeneration operation is a step of causing brine to flow into the ion exchange resin 9 in the ion exchange resin filling tank 2 and performing the regeneration process of the ion exchange resin 9. The control unit 13 switches the flow path of the control valve 3, and the brine 14 in the brine tank 4 passes through the brine pipe 12 and flows into the upper filter 10 via the control valve 3. Then, the salt water flows downward from the upper filter 10 in the ion exchange resin filling tank 2 to perform regeneration of the ion exchange resin 9. The brine used in the regeneration process of the ion exchange resin 9 flows into the lower filter 11, passes through the water collection pipe 8, and is discharged from the drain outlet pipe 7 via the control valve 3.

[正洗淨運轉] 針對正洗淨運轉使用圖5進行說明。正洗淨運轉係對離子交換樹脂填充槽2施行與軟水化運轉同方向之通水,而將配管內殘留的鹽水等洗淨並排出的步驟。利用控制部13切換控制閥3的流路,使來自原水入口管5的原水,經由控制閥3流入於上過濾器10。然後,原水從上過濾器10在離子交換樹脂填充槽2內朝下流動,並流入於下過濾器11中,再通過集水管8,經由控制閥3從排水出口管7排出。[Washing operation] The positive cleaning operation will be described using FIG. 5. The positive washing operation is a step of applying water to the ion exchange resin filling tank 2 in the same direction as the dehydration operation, and washing and discharging the brine remaining in the piping. The control unit 13 switches the flow path of the control valve 3 so that the raw water from the raw water inlet pipe 5 flows into the upper filter 10 via the control valve 3. Then, the raw water flows downward from the upper filter 10 in the ion-exchange resin filling tank 2, flows into the lower filter 11, passes through the water collecting pipe 8, and is discharged from the drain outlet pipe 7 via the control valve 3.

[給水運轉] 針對給水運轉使用圖6進行說明。給水運轉係用於在離子交換樹脂9之再生運轉前,生成鹽水14的步驟。利用控制部13切換控制閥3的流路,將來自原水入口管5的原水,經由控制閥3通過鹽水管12,將剛好既定分量供水至鹽水槽4。 [實施例][Water supply operation] The water supply operation will be described using FIG. 6. The water supply operation is a step for generating brine 14 before the regeneration operation of the ion exchange resin 9. The control unit 13 switches the flow path of the control valve 3 and feeds the raw water from the raw water inlet pipe 5 through the brine pipe 12 through the control valve 3 to supply just a predetermined amount of water to the brine tank 4. [Example]

針對本發明的軟水器實際運轉之順序進行說明。另外,以下說明係例示本發明之較佳實施形態,惟本發明並不侷限於該等,在本發明範圍內亦可實施其他實施形態。The actual operation sequence of the water softener of the present invention will be described. In addition, the following description exemplifies preferred embodiments of the present invention, but the present invention is not limited to these, and other embodiments can be implemented within the scope of the present invention.

<實施形態1> 圖7所示係實施形態1的軟水器1之各種運轉的實施時序的流程圖。在剛對軟水器1的控制部13供應電氣後,由控制閥3切換流路,依序施行離子交換樹脂9的逆洗淨運轉、正洗淨運轉及給水運轉(步驟W1)。以下將步驟W1的運轉稱為「洗淨給水運轉」。洗淨給水運轉中,係將用於除去離子交換樹脂9所附著的異物、以及將配管內所殘留鹽水排出用的必要份量之原水,供應給離子交換樹脂填充槽2,再將既定量原水供應給鹽水槽4。<Embodiment 1> FIG. 7 is a flowchart showing the execution sequence of various operations of the water softener 1 according to the first embodiment. Immediately after the electric supply to the control unit 13 of the water softener 1, the flow path is switched by the control valve 3, and the reverse cleaning operation, the forward cleaning operation, and the water supply operation of the ion exchange resin 9 are sequentially performed (step W1 ). Hereinafter, the operation of step W1 is referred to as "washing and water supply operation". During the washing and water supply operation, the necessary amount of raw water for removing the foreign materials adhering to the ion exchange resin 9 and discharging the residual salt water in the piping is supplied to the ion exchange resin filling tank 2, and then a given amount of raw water is supplied Give brine tank 4.

所以,即使在給水運轉途中發生停電、在鹽水槽4內未被供應鹽水14狀態下放置時,因為在停電後剛對控制部13供應電氣後即施行洗淨給水運轉,因而可防止在後續實施再生運轉時發生鹽水不足而再生不足的情形。Therefore, even if a power outage occurs during the water supply operation and is placed in the state where the brine 14 is not supplied in the brine tank 4, the washing and water supply operation is performed immediately after the power is supplied to the control unit 13 after the power outage, which prevents subsequent implementation In the regeneration operation, there is insufficient salt water and insufficient regeneration.

若完成洗淨給水運轉,控制部13便開始監視從洗淨給水運轉結束後起之經過時間的計時器A之計時計數、以及監視從洗淨給水運轉結束後起的通水量之累計值的累計量計數器之計數(步驟S1)。When the washing and water supply operation is completed, the control unit 13 starts to monitor the count of the timer A that has elapsed since the washing and water supply operation ends, and monitors the accumulation of the cumulative value of the water flow rate after the washing and water supply operation ends. The count of the quantity counter (step S1).

本實施形態,將開始再生運轉或洗淨運轉的時刻設為「設定時刻」。本實施形態中,將再生運轉或洗淨運轉設定成在使用頻率較少的上午0點至上午6點期間內、較佳係上午3點實施。控制部13判斷目前時刻是否為設定時刻(步驟S2)。若目前時刻為設定時刻(步驟S2的判斷為「YES」),則前進至步驟S3。圖7係將「設定時刻」設為上午3點。In this embodiment, the time at which the regeneration operation or the cleaning operation is started is set as the "set time". In this embodiment, the regeneration operation or the washing operation is set to be carried out during the period from 0 am to 6 am, which is less frequently used, preferably at 3 am. The control unit 13 determines whether the current time is the set time (step S2). If the current time is the set time (the determination in step S2 is "YES"), the process proceeds to step S3. Figure 7 sets the "set time" to 3 am.

另外,步驟S2的設定時刻係可配合軟水器的使用頻率等再行適當變更。例如當因夜班等導致上午3點的使用頻率較高之情況,亦可設定成在下午3點實施再生運轉、洗淨運轉。In addition, the setting time of step S2 can be changed appropriately according to the frequency of use of the water softener and the like. For example, when the frequency of use at 3 am is high due to night shifts, etc., it may be set to perform the regeneration operation and the washing operation at 3 pm.

計時器A與累計量計數器係決定進行離子交換樹脂9之再生運轉的時序。本實施形態中,再生運轉係設定為每隔9天實施、或累計通水量每達1.9噸時實施。控制部13係首先判斷計時器A的計數值是否未滿9天(步驟S3)。若計時器A的計數未滿9天(步驟S3為「YES」),接著判斷累計通水量的計數值是否未滿1.9噸(步驟S4)。The timer A and the cumulative amount counter determine the timing of the regeneration operation of the ion exchange resin 9. In this embodiment, the regeneration operation system is set to be implemented every 9 days or when the cumulative water flow reaches 1.9 tons. The control unit 13 first determines whether the count value of the timer A is less than 9 days (step S3). If the count of the timer A is less than 9 days ("YES" in step S3), then it is determined whether the count value of the accumulated water flow is less than 1.9 tons (step S4).

步驟S4的設定累計量可配合被處理水的硬度適當變更。例如當被處理水的硬度較高時,因為被處理水的處理量變少,因而亦可設定為每1.5噸等較短間隔施行再生運轉。The set cumulative amount in step S4 can be appropriately changed in accordance with the hardness of the water to be treated. For example, when the hardness of the water to be treated is high, since the amount of water to be treated is reduced, it can also be set to perform the regeneration operation at shorter intervals such as 1.5 tons.

控制部13係在計時器A的計數達9天以上(步驟S3的判斷為「NO」)時,切換控制閥3的流路,施行離子交換樹脂9的再生運轉(步驟S6)。本實施形態中,在再生運轉之前先進行逆洗淨運轉,於再生運轉之後依序施行正洗淨運轉與給水運轉。將此依序進行逆洗淨運轉、再生運轉、正洗淨運轉及給水運轉的一連串運轉稱為「洗淨再生給水運轉」。然後,在離子交換樹脂9的洗淨再生給水運轉結束時,控制部13重置計時器A的計數與累計量計數器的計數(步驟S7)。計時器A與累計量計數器再度開始計數(步驟S1),測定離子交換樹脂9在再生運轉後的經過時間與累計通水量。The control unit 13 switches the flow path of the control valve 3 and performs the regeneration operation of the ion exchange resin 9 when the count of the timer A reaches 9 days or more (the determination in step S3 is "NO") (step S6). In this embodiment, the reverse cleaning operation is performed before the regeneration operation, and the normal cleaning operation and the water supply operation are sequentially performed after the regeneration operation. This series of operations in which the reverse cleaning operation, the regeneration operation, the forward cleaning operation, and the water supply operation are performed in this order is called "washing and regeneration water supply operation". Then, when the washing regeneration water supply operation of the ion exchange resin 9 is completed, the control unit 13 resets the count of the timer A and the count of the accumulated amount counter (step S7). The timer A and the cumulative amount counter start counting again (step S1), and measure the elapsed time and the cumulative water flow rate of the ion exchange resin 9 after the regeneration operation.

再者,控制部13係即使計時器A的計數未滿9天(步驟S3的判斷為「YES」),但若累計通水量達1.9噸以上(步驟S4的判斷為「NO」),則如同上述,切換控制閥3的流路,進行離子交換樹脂9的洗淨再生給水運轉(步驟S6)。Furthermore, even if the count of the timer A is less than 9 days (the judgment of step S3 is "YES"), if the cumulative water flow exceeds 1.9 tons (the judgment of step S4 is "NO"), it is the same as As described above, the flow path of the control valve 3 is switched, and the ion exchange resin 9 is washed to regenerate the water supply operation (step S6).

另一方面,若經過天數未滿9天(步驟S3的判斷為「YES」)、累計通水量未滿1.9噸(步驟S4的判斷為「YES」)、且軟水器1中沒有通水的情況,則離子交換樹脂填充槽2內的被處理水成為滯留在離子交換樹脂填充槽2內的狀態。若長時間持續此種狀態,則因從離子交換樹脂9滲出的有機物等導致被處理水著色,因而離子交換樹脂填充槽2內必需清洗。所以,本實施形態的軟水器1,係即使經過天數未滿9天(步驟S3的判斷為「YES」)、累計通水量未滿1.9噸(步驟S4的判斷為「YES」),但若已達設定時刻,則進行離子交換樹脂填充槽2內的洗淨運轉(逆洗淨運轉與正洗淨運轉)。藉由進行既定時間之洗淨運轉,離子交換樹脂9所附著之異物被除去,且對離子交換樹脂填充槽2供應用於將配管內所殘留鹽水排出時必要份量的原水。On the other hand, if the elapsed days are less than 9 days (the judgment in step S3 is "YES"), the cumulative water flow is less than 1.9 tons (the judgment in step S4 is "YES"), and there is no water flow in the water softener 1 , The water to be treated in the ion exchange resin filled tank 2 is in a state of staying in the ion exchange resin filled tank 2. If this state continues for a long period of time, the water to be treated will become colored due to organic matter oozing out of the ion exchange resin 9, and therefore the ion exchange resin filled tank 2 must be cleaned. Therefore, the water softener 1 of the present embodiment is that even if the number of days elapsed is less than 9 days (the judgment in step S3 is "YES"), the cumulative water flow is less than 1.9 tons (the judgment in step S4 is "YES"), but if At the set time, the cleaning operation (reverse cleaning operation and forward cleaning operation) in the ion exchange resin filling tank 2 is performed. By performing the washing operation for a predetermined time, the foreign materials adhering to the ion exchange resin 9 are removed, and the ion exchange resin filling tank 2 is supplied with the necessary amount of raw water for discharging the brine remaining in the piping.

本實施形態1中,即使在再生途中發生停電,離子交換樹脂填充槽2中有殘留鹽水的情況,但因為在剛對控制部13供應電氣後即施行洗淨運轉,故可防止離子交換樹脂填充槽2內的鹽水從軟水出口管6流出。又,因為在剛對控制部13供應電氣後即施行給水運轉,因而可防止在下一次再生運轉時鹽水14不足而再生不足之情形。In the first embodiment, even if there is a power outage in the middle of regeneration, there may be residual brine in the ion exchange resin filling tank 2. However, since the washing operation is performed immediately after the control unit 13 is supplied with electricity, the ion exchange resin filling can be prevented The brine in the tank 2 flows out from the soft water outlet pipe 6. In addition, since the water supply operation is performed immediately after the control unit 13 is supplied with electricity, it is possible to prevent the situation where the salt water 14 is insufficient and the regeneration is insufficient during the next regeneration operation.

<參考實施形態1> 作為軟水器1之運轉參考例,針對參考實施形態1進行說明。圖8所示係參考實施形態1的實施時序的流程圖。該參考實施形態1與上述實施形態1的差異處在於:參考實施形態1係在進行洗淨給水運轉之前,追加利用總通水量值判斷是否進行洗淨給水運轉的處理。除了該追加的處理之外,其餘均與實施形態1共通,故相關共通的部分加註相同元件符號並省略說明。<Reference Embodiment 1> As a reference example of the operation of the water softener 1, the reference embodiment 1 will be described. FIG. 8 is a flowchart showing the implementation sequence of the first embodiment. The difference between the reference embodiment 1 and the above-mentioned embodiment 1 is that the reference embodiment 1 adds a process of determining whether to perform the washing water supply operation using the total water flow value before performing the washing water supply operation. Except for this additional processing, the rest are common to the first embodiment. Therefore, the common parts are denoted by the same component symbols and their description is omitted.

如圖8所示,參考實施形態1係在剛對軟水器1的控制部13供應電氣後,控制部13即開始監視通水量累計值之總通水量計數器的計數(步驟W1)。As shown in FIG. 8, according to the first embodiment, immediately after power is supplied to the control unit 13 of the water softener 1, the control unit 13 starts monitoring the count of the total water flow counter of the accumulated water flow rate (step W1 ).

該總通水量計數器係在未重置對軟水器1所通水的水量之下持續累計,再決定進行洗淨給水運轉的時序。參考實施形態1係假設普通家庭剛安裝了軟水器1後,於實施洗淨運轉時所使用的水量,將總通水量設定為100L以上。控制部13判斷總通水量的計數值是否達100L以上(步驟W2)。若總通水量的計數器未滿100L(步驟W2的判斷為「NO」),則跳過步驟W3,前往至步驟S1。若總通水量的計數器達100L以上(步驟W2的判斷為「YES」),則前進至步驟W3,接著前往至步驟S1。在步驟W3時,由控制閥3切換流路,實施洗淨給水運轉。依此,在剛對控制部13供應電氣後,配合通水量的累計值,選擇是否進行步驟W3之洗淨給水運轉的理由如下。The total water flow counter is continuously accumulated under the amount of water passed to the water softener 1 without resetting, and then the timing of the washing and water supply operation is determined. In the first embodiment, it is assumed that the water flow rate used in the washing operation immediately after the water softener 1 is installed in an ordinary household is set to 100 L or more. The control unit 13 judges whether or not the count value of the total water flow rate exceeds 100 L (step W2). If the total water flow counter is less than 100L (the determination in step W2 is "NO"), step W3 is skipped and the process proceeds to step S1. If the total water flow counter reaches 100L or more (the determination in step W2 is "YES"), the process proceeds to step W3, and then proceeds to step S1. At step W3, the flow path is switched by the control valve 3, and the washing water supply operation is performed. Accordingly, the reason for selecting whether to perform the washing and water supply operation in step W3 in accordance with the cumulative value of the water flow immediately after the power supply to the control unit 13 is as follows.

首先,軟水器1係在安裝於普通家庭前,對軟水器1所組裝的組裝線供應電氣施行通電檢查。若在進行該通電檢查的期間內實施洗淨給水運轉,則通電檢查必須等待洗淨給水運轉完成前的期間,導致檢查效率變差。所以,觀察由總通水量計數器所累計的通水量,使軟水器1在普通家庭安裝軟水器1前的總通水量較少期間內不要施行洗淨給水運轉,可效率佳地進行通電檢查。First, before the water softener 1 is installed in an ordinary home, the assembly line of the water softener 1 is supplied with electricity to perform a power-on inspection. If the cleaning and water supply operation is performed during the period of conducting the power-on inspection, the power-on inspection must wait for the period before the cleaning and water supply operation is completed, resulting in poor inspection efficiency. Therefore, by observing the water flux accumulated by the total water flux counter, the water softener 1 should not be subjected to the washing and water supply operation during the period when the total water flux of the ordinary household before the water softener 1 is installed is small, and the power supply inspection can be performed efficiently.

另一方面,軟水器1安裝於普通家庭,由使用者開始使用後,必需在剛對控制部13供應電氣後即實施洗淨給水運轉。所以,將剛安裝於普通家庭後馬上實施的洗淨運轉時所使用水量設為指標,若總通水量達該指標值以上,則在對控制部13供應電氣後即馬上實施洗淨給水運轉。本參考形態1中,將該指標量設定為「100L」。依此,若剛安裝後所實施的洗淨運轉結束,由使用者開始使用後,則在剛對控制部13供應電氣後馬上實施洗淨給水運轉。On the other hand, the water softener 1 is installed in an ordinary home, and after the user starts to use it, it is necessary to perform the washing and water supply operation immediately after the control unit 13 is supplied with electricity. Therefore, the amount of water used in the washing operation immediately after installation in an ordinary home is set as an index, and if the total water flow rate exceeds the index value, the washing and water supply operation is performed immediately after power is supplied to the control unit 13. In this reference form 1, the index amount is set to "100L". Accordingly, when the washing operation performed immediately after the installation is completed and the user starts to use it, the washing and water supply operation is performed immediately after power is supplied to the control unit 13.

另外,步驟W2的總通水量係可配合軟水器1剛施工後所實施之洗淨運轉的通水量等適當變更。例如因為離子交換樹脂填充槽2內的離子交換樹脂9之量較少等而可減少洗淨運轉的通水量時,亦可將總通水量設定為50L。In addition, the total water flow rate in step W2 can be appropriately changed in accordance with the water flow rate of the washing operation performed immediately after the construction of the water softener 1 and the like. For example, when the amount of ion exchange resin 9 in the ion exchange resin filling tank 2 is small and the water flow rate in the washing operation can be reduced, the total water flow rate may be set to 50 L.

<實施形態2> 圖9所示係實施形態2的軟水器1之各種運轉實施時序的流程圖。另外,相關與實施形態1的流程圖及內容屬共通部分不再贅述。<Embodiment 2> FIG. 9 is a flowchart showing the sequence of various operations of the water softener 1 according to the second embodiment. In addition, the flow charts and contents related to Embodiment 1 are common, and are not repeated here.

剛對軟水器1的控制部13供應電氣後,由控制部13開始監視從洗淨給水運轉結束後起之經過時間的計時器A之計時、以及監視從洗淨給水運轉結束後起的通水量之累計值的累計量計數器之計數(步驟S1)。步驟S2係同實施形態1。另外,若一星期內的各天使用頻率不同時,亦可依照一星期內的各天改變設定時刻。亦可例如星期一設定為上午4時,星期二設定為上午5點等。相關以下的各步驟均同實施形態1。Immediately after supplying electric power to the control unit 13 of the water softener 1, the control unit 13 starts monitoring the elapsed time of the timer A since the end of the washing water supply operation, and monitors the amount of water passing after the end of the washing water supply operation The accumulated value of the accumulated value counter is counted (step S1). Step S2 is the same as the first embodiment. In addition, if the frequency of use is different for each day of the week, the set time can also be changed according to each day of the week. For example, Monday may be set at 4 am, Tuesday may be set at 5 am, etc. The following steps are the same as in the first embodiment.

因為本實施形態2係依如上述進行動作,故若到達每日設定時刻(步驟S2的判斷為「YES」),前進至步驟S5或步驟S6,進行逆洗淨運轉與正洗淨運轉、亦即洗淨運轉。Since the second embodiment operates as described above, if the daily set time is reached (the judgment in step S2 is "YES"), proceed to step S5 or step S6 to perform the reverse cleaning operation and the forward cleaning operation. That is washing operation.

<水質測定> 為了確認是否每24小時施行洗淨運轉便已足夠,測定離子交換樹脂填充槽2內之滯留水的水質。所測定之水質的項目係濁度、色度及化學需氧量。濁度與色度係使用日本電色工業股份有限公司製WATER ANALYZER WA6000測定。化學需氧量(以下稱「COD」)係根據JIS K 0102-17滴定法,利用滴定CODMn值進行測定。<Water quality measurement> In order to confirm whether it is sufficient to perform the washing operation every 24 hours, the water quality of the stagnation water in the ion exchange resin filled tank 2 was measured. The measured water quality items are turbidity, color and chemical oxygen demand. The turbidity and chromaticity were measured using WATER ANALYZER WA6000 manufactured by Nippon Denshoku Industries Co., Ltd. The chemical oxygen demand (hereinafter referred to as "COD") is measured by titration of CODMn value according to JIS K 0102-17 titration method.

原水係使用pH7.5±0.5的RO水,在離子交換樹脂填充槽2中裝滿RO水,於鹽水槽4中裝滿鹽水14。接著,將上述實施形態2的洗淨再生給水運轉設為1循環,施行2循環。然後,從原水入口管2將2L的RO水流入於離子交換樹脂填充槽2,再採集從軟水出口管6流出的水。將該水設為浸漬液原水,測定浸漬液原水的水質。The original water system uses RO water with a pH of 7.5±0.5, fills the ion exchange resin filled tank 2 with RO water, and fills the brine tank 4 with brine 14. Next, the washing regeneration water supply operation of the second embodiment described above is set to one cycle, and two cycles are performed. Then, 2 L of RO water was flowed into the ion exchange resin filling tank 2 from the raw water inlet pipe 2, and then the water flowing out of the soft water outlet pipe 6 was collected. This water was used as the raw water of the immersion liquid, and the water quality of the raw water of the immersion liquid was measured.

另外,相關色度、濁度及CODMn的增加量,基準係依各國家有所不同,例如亦有將色度增加量在5.0度以下、濁度增加量在0.5度以下、CODMn增加量在2.0mg/L以下作為基準的國家。In addition, the relative chromaticity, turbidity, and CODMn increase are based on different countries. For example, the chroma increase is less than 5.0 degrees, the turbidity increase is less than 0.5 degrees, and the CODMn increase is 2.0. Countries with mg/L or less as benchmarks.

(實驗1) 施行洗淨再生給水運轉計2循環,直接放置24小時。經24小時後,為採集離子交換樹脂填充槽2內的滯留水,從原水入口管2將2L的RO水流入於離子交換樹脂填充槽2之後,再採集從軟水出口管6流出的水。測定該水的水質,將經24小時後的水之水質、與浸漬液原水的水質進行比對,測定色度、濁度及CODMn的增加量。色度、濁度、CODMn的增加量均屬非常小的值。色度、濁度、CODMn的增加量整合於表1。滿足上述基準。(Experiment 1) Perform 2 cycles of washing and regenerating water supply operation, and leave it for 24 hours. After 24 hours, in order to collect the stagnation water in the ion exchange resin filling tank 2, 2L of RO water was flowed into the ion exchange resin filling tank 2 from the raw water inlet pipe 2, and then the water flowing out of the soft water outlet pipe 6 was collected. The water quality of this water was measured, the water quality after 24 hours was compared with the water quality of the raw water of the immersion liquid, and the increase in color, turbidity, and CODMn was measured. The increase in color, turbidity, and CODMn are all very small values. The increase in color, turbidity, and CODMn are summarized in Table 1. Meet the above criteria.

(實驗2) 除了放置72小時外,其餘均與實驗1同樣地測定色度、濁度及CODMn的增加量。色度、濁度、CODMn的增加量均大於經24小時後的結果。色度、濁度、CODMn的增加量整合於表1。未滿足上述基準。 [表1]

Figure 108132146-A0304-0001
(Experiment 2) The chromaticity, turbidity, and increase in CODMn were measured in the same manner as in Experiment 1, except for 72 hours. The increase in color, turbidity, and CODMn are all greater than the result after 24 hours. The increase in color, turbidity, and CODMn are summarized in Table 1. The above criteria are not met. [Table 1]
Figure 108132146-A0304-0001

針對本發明參照詳細的特定實施態樣進行了說明,惟在不脫逸本發明精神與範疇前提下,亦可追加各種變更與修正,此係熟習此技術者可輕易思及。The present invention has been described with reference to detailed specific implementations, but various changes and modifications can be added without departing from the spirit and scope of the present invention, which can be easily considered by those skilled in the art.

本申請案係以2018年9月6日所提出申請的日本專利申請案(特願2018-166656)、2018年9月12日所提出申請的日本專利申請案(特願2018-170399)為基礎,參照其內容並援引於本案中。 (產業上之可利用性)This application is based on the Japanese patent application filed on September 6, 2018 (Japanese Patent Application 2018-166656) and the Japanese patent application filed on September 12, 2018 (Japanese Patent Application 2018-170399). , Referring to its content and citing in this case. (Industry availability)

根據本發明,因為可設定為每日在既定時刻實施離子交換樹脂填充槽內的洗淨運轉,在洗淨運轉中施行通水時雖從原水入口管流入的被處理水流出至軟水出口管,但藉由將既定時刻設定為不進行通水的時段,可發揮提供能防止此種不良情況之軟水器的效果。發揮此項效果的本發明,可有效使用作為相關於使被處理水通水於已填充著離子交換樹脂的離子交換樹脂填充槽而施行軟水化處理的軟水器。According to the present invention, it can be set that the washing operation in the ion-exchange resin filling tank is carried out at a predetermined time every day. Although the water to be treated flowing from the raw water inlet pipe flows out to the soft water outlet pipe when water is passed during the washing operation, However, by setting the predetermined time to a time period during which water is not passed, it is possible to exert the effect of providing a water softener that can prevent such a bad situation. The present invention that exerts this effect can be effectively used as a water softener that allows water to be treated to pass through an ion-exchange resin-filled tank filled with an ion-exchange resin and to perform a water-softening treatment.

1:軟水器 2:離子交換樹脂填充槽 3:控制閥 4:鹽水槽 5:原水入口管 6:軟水出口管 7:排水出口管 8:集水管 9:離子交換樹脂 10:上過濾器 11:下過濾器 12:鹽水管 13:控制部 14:鹽水1: Water softener 2: Ion exchange resin filled tank 3: Control valve 4: brine tank 5: Raw water inlet pipe 6: Soft water outlet pipe 7: Drain outlet pipe 8: Water collecting pipe 9: ion exchange resin 10: Upper filter 11: Lower filter 12: brine tube 13: Control Department 14: brine

圖1係表示本發明的軟水器一實施形態之概略構成圖; 圖2係表示圖1之軟水器在軟水化運轉時的水流動的概略圖; 圖3係表示圖1之軟水器在逆洗淨運轉時的水流動的概略圖; 圖4係表示圖1之軟水器在再生運轉時的水流動的概略圖; 圖5係表示圖1之軟水器在正洗淨運轉時的水流動的概略圖; 圖6係表示圖1之軟水器在給水運轉時的水流動的概略圖; 圖7係表示實施形態1的洗淨給水運轉、洗淨再生給水運轉及洗淨運轉之實施時序的流程圖; 圖8係表示參考實施形態1的洗淨給水運轉、洗淨再生給水運轉及洗淨運轉之實施時序的流程圖;及 圖9係表示實施形態2在洗淨再生給水運轉及洗淨運轉之實施時序的流程圖。1 is a schematic configuration diagram showing an embodiment of the water softener of the present invention; FIG. 2 is a schematic diagram showing the flow of water during the softening operation of the water softener of FIG. 1; Figure 3 is a schematic diagram showing the flow of water during the reverse cleaning operation of the water softener of Figure 1; 4 is a schematic diagram showing the flow of water during the regeneration operation of the water softener of FIG. 1; FIG. 5 is a schematic diagram showing the flow of water during the washing operation of the water softener of FIG. 1; 6 is a schematic diagram showing the water flow of the water softener of FIG. 1 during water supply operation; 7 is a flowchart showing the implementation sequence of the washing water supply operation, washing regeneration water supply operation, and washing operation in Embodiment 1; 8 is a flowchart showing the implementation timing of the cleaning water supply operation, cleaning regeneration water supply operation, and cleaning operation with reference to Embodiment 1; and FIG. 9 is a flowchart showing the implementation sequence of the washing regeneration water supply operation and the washing operation in the second embodiment.

Claims (4)

一種軟水器,係使被處理水通水於離子交換樹脂而施行軟水化處理的軟水器,具備有: 離子交換樹脂填充槽,其係填充著離子交換樹脂; 鹽水槽,其係用於儲存供離子交換樹脂再生用的鹽水;以及 控制部,其係切換下述運轉:軟水化運轉,係使被處理水通水於上述離子交換樹脂填充槽內的上述離子交換樹脂,而進行軟水化;洗淨運轉,係將上述離子交換樹脂填充槽的內部洗淨;再生運轉,係使上述鹽水槽內的上述鹽水通水於上述離子交換樹脂填充槽內的上述離子交換樹脂,而進行離子交換樹脂的再生;及給水運轉,係將水供應至上述鹽水槽內部; 上述控制部係以在既定時刻施行上述洗淨運轉之方式進行控制。A water softener is a water softener that allows treated water to pass through ion exchange resin to perform water softening treatment, and includes: Ion exchange resin filled tank, which is filled with ion exchange resin; Brine tank, which is used to store brine for ion exchange resin regeneration; and The control unit switches the following operations: the dehydration operation, which allows the water to be treated to pass through the ion exchange resin in the ion exchange resin filling tank, to perform dehydration; the washing operation, which converts the ion exchange resin The inside of the filling tank is washed; the regeneration operation is to allow the brine in the brine tank to pass water to the ion exchange resin in the ion exchange resin filling tank to regenerate the ion exchange resin; and the water supply operation is to replace the water Supply to the inside of the above brine tank; The control unit performs control so as to execute the cleaning operation at a predetermined time. 如請求項1之軟水器,其中,上述既定時刻係上午0點至上午6點之期間。For example, the water softener according to claim 1, wherein the above-mentioned predetermined time is a period from 0am to 6am. 如請求項1或2之軟水器,其中,上述既定時刻係每日均為相同時刻。For example, the water softener according to claim 1 or 2, wherein the predetermined time is the same time every day. 一種軟水器,係使被處理水通水於離子交換樹脂而施行軟水化處理的軟水器,具備有: 離子交換樹脂填充槽,其係填充著離子交換樹脂; 鹽水槽,其係用於儲存供離子交換樹脂再生用的鹽水;以及 控制部,其係切換下述運轉:軟水化運轉,係使被處理水通水於上述離子交換樹脂填充槽內的上述離子交換樹脂,而進行軟水化;洗淨運轉,係將上述離子交換樹脂填充槽的內部洗淨;再生運轉,係使上述鹽水槽內的上述鹽水通水於上述離子交換樹脂填充槽內的上述離子交換樹脂,而進行離子交換樹脂的再生;及給水運轉,係將水供應至上述鹽水槽內部; 上述控制部係以在剛對該控制部供應電氣之後,即進行上述洗淨運轉與上述給水運轉之方式進行控制。A water softener is a water softener that allows treated water to pass through ion exchange resin to perform water softening treatment, and includes: Ion exchange resin filled tank, which is filled with ion exchange resin; Brine tank, which is used to store brine for ion exchange resin regeneration; and The control unit switches the following operations: the dehydration operation, which allows the water to be treated to pass through the ion exchange resin in the ion exchange resin filling tank, to perform dehydration; the washing operation, which converts the ion exchange resin The inside of the filling tank is washed; the regeneration operation is to allow the brine in the brine tank to pass water to the ion exchange resin in the ion exchange resin filling tank to regenerate the ion exchange resin; and the water supply operation is to replace the water Supply to the inside of the above brine tank; The control unit performs control in such a manner that the washing operation and the water supply operation are performed immediately after power is supplied to the control unit.
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