JPS5973092A - Apparatus for manufacture of demineralized water - Google Patents

Apparatus for manufacture of demineralized water

Info

Publication number
JPS5973092A
JPS5973092A JP18177582A JP18177582A JPS5973092A JP S5973092 A JPS5973092 A JP S5973092A JP 18177582 A JP18177582 A JP 18177582A JP 18177582 A JP18177582 A JP 18177582A JP S5973092 A JPS5973092 A JP S5973092A
Authority
JP
Japan
Prior art keywords
water
pure water
demineralized water
unit
output
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
JP18177582A
Other languages
Japanese (ja)
Inventor
Hideo Goto
後藤 日出雄
Tomoaki Hayashi
友明 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.)
Yamato Scientific Co Ltd
Yamato Kagaku KK
Original Assignee
Yamato Scientific Co Ltd
Yamato Kagaku KK
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 Yamato Scientific Co Ltd, Yamato Kagaku KK filed Critical Yamato Scientific Co Ltd
Priority to JP18177582A priority Critical patent/JPS5973092A/en
Priority to US06/529,598 priority patent/US4563272A/en
Priority to DE3337169A priority patent/DE3337169C2/en
Priority to GB08327606A priority patent/GB2128176B/en
Publication of JPS5973092A publication Critical patent/JPS5973092A/en
Pending legal-status Critical Current

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  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)

Abstract

PURPOSE:To manufacture demineralized water of desired purity with excellent reliability, by providing a means for measuring the purity of each output water from each unit for manufacturing demineralized water, a means for returning said output water to an outputted unit for manufacturing demineralized water, etc. CONSTITUTION:From raw water (a) supplied by the operation of a supply pump 19, demineralized water is obtained by three-stage treatment with the first, second and third units 3, 5, 7 for manufacturing demineralized water. That is, a microcomputer 9 compares the result of purity measured by the first, second and third conductometers 11, 13, 15 provided in the passageways of output water from each unit 3, 5, 7 for manufacturing demineralized water with predetermined purity preset by a setting instrument 17, and controls a pump 19 for supplying demineralized water, the first electromagnetic valve 21 for switching the drainage (b) of output water from the first unit 3 for manufacturing demineralized water, the second electromagnetic valve 23 for controlling the circulating current of treated water to the third unit 7 for manufacturing demineralized water, a reflux motor 25 and an alarm device 27 for abnormality.

Description

【発明の詳細な説明】[Detailed description of the invention]

この発明は、製造されIこ純水の信頼性を向上した純水
製造装置に関り−る。 一般に、純水を得る方法としては人別して蒸留法、イA
ン交換法、逆浸透法がある。蒸留法とは、原水を加熱し
て沸騰さU、発生した然気を冷)Jl。 凝縮して純水を11する方法である。イオン交換法とは
、原水をイオン交換樹脂中を通過させて溶存イΔン物質
を除去して):10水を1″14万沈(ある3、1、た
、逆浸透法とは、特殊’cI゛l′−J△11114 
(・〕4川しC原水を分子レベルC濾過して純水を11
7る方法゛Cある。、?、E東の純水製’IL %置は
、上述した3方法のうらいり゛れかの方法にJ、り原水
を処理づる」、)に()11成さl′tた純水製j聞ユ
ニツ1〜を処理水にI+j、(;(二通宜に複数引合わ
けて使用し、純水を11?るにζ置で((する、。 しかし4賃がら、従来の純水製ノ?、装置(こtBいて
は、最終的に製造された純水の純度だ(ノを電気伝導度
によって判定し、判定結末が−jコめ定めた練磨、J、
り低い場合には、当該純水を廃ノ’q、’ I、Cいた
1、弓4イわノ)、原水の処理過程(ごおい乙、戦損(
1するいは使1[1限度を越えた純水製造ユニツ]−が
ル)るJSA合(二は、これを検知りる手段がないlJ
め、I:+l:L(な置−ソ1へ交換の対策をとること
がでさり゛、廃棄しく; tJ’ :t’Lはならない
争口水の’!IJ ’r’jiをイ1オニ続し−(:’
 l、 ;l、)こととイ1うて、結果的に所望の純度
を荀りる純水が1H7られる信頼性を向−1−(jるこ
とが(゛さイ1い。。 この発明は上記に鑑みてなされたしので、−この1]的
としては、所望の糾葭を(T (fイλ純水か116れ
る1、1す・fi l’l /!:向−1シI′、しt
l[j水うソ造装置を提供すること(、−ある1゜ 1記目的を達成
The present invention relates to a pure water production apparatus that improves the reliability of produced pure water. In general, the methods for obtaining pure water differ depending on the person: distillation,
There are two methods: ion exchange method and reverse osmosis method. The distillation method involves heating raw water to bring it to a boil, and then cooling the generated air. This is a method of condensing pure water to 11%. The ion exchange method involves passing raw water through an ion exchange resin to remove dissolved ions. 'cI゛l'-J△11114
(・) 4 rivers C raw water is filtered at molecular level C to make pure water 11
There is a method ゛C. ,? , E East's pure water manufacturer 'IL % The pure water manufacturer's IL % location is the method of processing the raw water by one of the three methods mentioned above. I + j, (; ?, equipment (this is the purity of the finally produced pure water) is judged by electrical conductivity, and the result of the judgment is -J.
If the amount of water is low, the pure water should be used as waste water (waste 1, 1, bow 4), raw water treatment process (good, war damage).
1 or use 1 [a pure water production unit that exceeds the limit] - JSA case (2) there is no way to detect this
Therefore, I:+l:L (instead, it is possible to take measures to replace it with So1, so please discard it; Continued - (:'
As a result, it is possible to improve the reliability of pure water with the desired purity.This invention was made in view of the above, therefore, - this 1] target is the desired test (T (f i λ pure water? I', then
l[j To provide a water burying device (,-Achieving the purpose of 1゜1)

【Jるために、この発明は、原水を少9
シの純水製造−1−ツトて゛処理して純水を製造りるに
1賀(3二おい(、各純水製造ユニツl−/J+ +う
の各/(の出力水の純度測定装置と、純度測定結果が所
定iiQを越え−Cいる状態Ci’fij記出力水を処
理出力した純水製)’QHJニットに当該出力水を還流
する循環)−置と、当該出ツノ水の還流が一定時間11
J:続したことで純水製造を停止する駆動制御装置とを
設(づ、各純水装j青−Lニツ]・の破損を適確に検出
し、且つ当該各コニッ1−の処理出力水の純度を浦償づ
るよ−うにしたことを要旨どする。 1ス下、図面を用いてこの発明の詳細な説明jJ−る4 第1図は、この発明の一実施例を承りものである。1は
純水製造器を示しており、該純水製造器1は、蒸留法、
イΔン交換法、逆浸透法のう1ついずれかの方法で原水
処理を行なうように構成され゛(いる第1.第2.第3
の純水製造ユニツj−3゜5.7にJ、る7段処理で供
給ボンf]9)の駆動により給水ざl’j /、:原水
から純水を製造りるしの−(゛、マーイクL’l−Iン
ビノータ9にJ、ンc′I′i該製;Δ’I−稈h’制
御される(14成である。す41わら、−′イク「ド−
」ンピl−タ9は、各純水製)貴コニツト、’31.7
の出ツノ水路に設()られた第1.第2.第3の電気1
ノ、)9瓜泪11,13.15にJ、ろ紳1:坦の測定
結果を予め設定装置17によっ−C定め/j紳純度比較
し、当該比較結果に基づき原水の供給ボンゾ19.第1
の純水製mユニツ1へ3の出/J水の排水切換のための
第1の電磁弁21.鴇埋4くの第3の練水製造ユニツ1
−7へのjヱ流制御を行なう第2の電磁弁23 it3
.J:び還流七−夕2り、異常芳報艮装27を制御する
。 次に、本実施倒にお()る純水11″°1造I稈すJ 
fIを第2図に承り如く、−ノイクロ」ノビ1−タ(→
の中央処理装置ff1(CPU)の処理フl−,1−1
−11,′、−)さ説明りる。 一般に、原水としく゛は、例え(、[水道が”) fj
tEされるが、給水開始直後にJフいて(,1当該水道
管中の各種不純物か原水1.二!Ie人しCいる場合が
あり、そのJ、うな原水から所定の純f9を右りる純水
を!′l造りるとは不i″i丁能である。そのため、C
PUはまず「分クイーンを・リレット後(ステップ10
0)に、第1の純水装J貨コニツ1−3による1jξ給
ポンプ19によ−)で給水された原水についでの処理水
の純度を第′1の電気1云Mj I良:+ 1−1から
読み込み(ステップ110)、ス′jツブ120で測定
結果(Ul)を予め設定した純度(Ux )と比較して
、01 ン℃】χてあれば次の処理を行なうへくスフ−
ツブ165に、−C51゛: U y、 (あれば純水
製造が不可能と判断して当該処理水を111承りへくス
テップ130に進む。 ステップ130は、第′1の電磁弁21を1)1水側に
切(■え(スlツ1140に進む。ここで、前述した、
J、うに、水道1′8中の不純水が混入した原水として
II給水聞胎1l−IF2のしのC′あるため、いつま
でもIJL /J〔かij’cLわれる場合には、第1
の純水製造ユニット3の破10等か考えられる。ステッ
プ140・−,1601ま当該破損あるいは処理能力低
下を検出覆るための7+」−−(ある、、〈1な1.〕
ハ、(’11N1す(、;、排水開始と共にT分(例え
ば5か)フィンを駆動開始さげ、JJI水が−F分間紺
;続し/、=こと4−検7.11 L、 <、+1給ポ
ンプ19を骨止づるど共に第1の純水製造Iニットの交
換の必要性を警報装置27(、より報知して純水製造器
1の駆動部を淳止刀る(スノノ−f280)。 一方、CI)IJは、?J +  てUXか成\7tノ
で第1の電磁弁21を送水側に切換えた後、第2の純水
製造]、ユニット!5に供給され処理された出力水につ
いての糸屯度02を第2の電気1云)9度lll 13
から5売み取って第2の純水製造ユニット5にJ、る■
埋前の純度U1 ど比較して相ス・j的な純1(シの向
」−麿((]2、・′01 )を求める(ステップ10
5・IF〕0)。 ソシテ、c p u +、、t、当該向−11,q (
?、) 2  ””(J +  ) ’a予め設定した
1偵U rと比較し−(、((ソ2−01 )゛・Ul
・(あれば第2の純水製造−J−ソト5が破損あるいは
処理能力低下と判断し【スノッゾ200に進み、当該ユ
ニツ1−5の交換の必要性を報知りべく警報装置27を
駆動さ[!(純水製造ぽ:1の駆動を停止」する(ステ
ップ280)。 CP Uは、ステップ205〜230において、第3の
純水製造−1ニツ1へ7の交換の必要性を萌述したステ
ップ180〜200ど同様に当該ユニット7の込狸にJ
、る相対的な純度の向上度(U3.”02)の比較によ
って行ない、(U3/U2)>設定舶U/(・あれば次
の処理を行なうべくステップ240に進み、(Ua /
−(J2 ) ・、Uzであれば警報装置27を駆動さ
せて純水製造器1の駆動を停止する(ステップ2ε30
>。 さら(こ、CP Uは、ステップ205て゛8売み込ん
だ第3の純水j%I 造ユニット7からの出力水の純度
03を予め設定した所望純度’(J Hと比較して、U
3>Ul−1であれば所望の純度を右りる純水が製造で
さたと判断し−C第2の電磁弁23を採水可能(ステッ
プ270)とすべくセラl−1,、U3>UHであれば
再磨第3の純水製造■ニラ1〜7で処理づべく第2の電
磁弁23を循環路側にセラ1〜すると其に循環ポンプ2
5を駆動ざける(ステップ260)。 なお、本実前例〇は、16水を3個の純水製)己1ニッ
1へで処理して純水を111るJ、うにしたが、必゛用
に応じて適宜増減してbJ、いことは菖う31、(シ<
fい。 また、ホ実IJ^例では循環路は1じ柊[υの純水製j
ろユニット部にのみ設(プたが、各純水t!llj造二
Iニット部に設けることにJ、7)−(は、当該g−i
ニットの出力水の純度が当該各コニツ1へごとに設定さ
れた1111どなることを保証Cき、ひいCは最終的に
背られた純水の純度を高めることが(−0)ろ1゜以上
説明したようにこの発明にJ、、 Itは、 、fil
i zJ・:製j聞装置に設()られた複数の純水1契
造コーツi・からの各出力水の純度を測定し、必娶があ
れば当該出力水の前段の純水″rA造コニツ1〜に循環
さUるJ、・)にしたので、各純水!!A8コーツ1−
の破1i)’:・、“か適(1(rに検出でき・、且つ
所望の純■を右づる純水が1qられる信頼性4−向上り
ること/心でさる
[In order to reduce the amount of raw water, this invention
Purity production of pure water - 1 - Processing and manufacturing of pure water (32 units (, each pure water production unit l-/J+ + each unit/() purity measuring device When the purity measurement result exceeds a predetermined value, the purified water produced by processing the output water is returned to the QHJ knit, and the output water is refluxed. is a certain period of time 11
J: A drive control device is installed to stop the production of pure water due to continuous operation. The following is a summary of how the purity of water is determined. Below is a detailed explanation of this invention using drawings. Figure 1 shows an embodiment of this invention. 1 indicates a pure water production device, and the pure water production device 1 is a distillation method,
The system is configured to treat raw water using one of the following methods: ∆an exchange method or reverse osmosis method.
Pure water production unit j-3゜5.7J, water supply tank f]9) is driven by water supply tank f]9): Pure water is produced from raw water Rirshino-(゛, Mark L'l-I Invinota 9 J, nc'I'i made; Δ'I-culm h' is controlled (14 formations.
''Pita 9 is manufactured by each pure water manufacturer, '31.7
The first waterway was built on the Nodetsuno Channel. Second. third electricity 1
ノ,)9瓜泪11, 13.15J、 ro 1: The measurement results of the 19. 1st
First solenoid valve 21 for switching the output/J water to the pure water m unit 1 3. Tokubu 4th 3rd rensui production unit 1
The second solenoid valve 23 it3 controls the flow to -7.
.. J: controls the abnormality notification device 27. Next, the pure water 11"°1 I culm J
As shown in Fig. 2, the fI is shown in Figure 2.
Processing steps of the central processing unit ff1 (CPU) l-, 1-1
-11,',-) is explained. In general, raw water and water are used as analogies (, [water supply is”) fj
However, immediately after the start of water supply, there may be various impurities in the water pipe or raw water. It is impossible to produce pure water.Therefore, C
PU first performs ``minute queen after relet (step 10)''.
0), the purity of the treated water supplied by the 1jξ supply pump 19 by the first pure water unit 1-3 is determined by the purity of the treated water from the 1st electric 1 mj I quality: + 1-1 (step 110), compare the measurement result (Ul) with the preset purity (Ux) in the step 120, and if it is 01 °C]χ, proceed to the next step. −
-C51゛: U y, (If there is, it is determined that it is impossible to produce pure water and the process proceeds to step 130 where the treated water is accepted by 111. In step 130, the '1st solenoid valve 21 is ) 1 Cut to the water side (■ E (Proceed to Sluts 1140.
J, sea urchin, as the raw water mixed with impure water in the water supply 1'8 is C' of II water supply stage 1l-IF2, if IJL /J[or ij'cL is used, the
It is thought that the pure water production unit 3 was damaged. Step 140.
Ha, ('11N1 (, ;, When the water starts draining, start driving the fins for T minutes (for example, 5), and the JJI water is dark blue for -F minutes; continued/, = thing 4-test 7.11 L, <, In addition to stopping the +1 supply pump 19, the alarm device 27 notifies the necessity of replacing the first pure water production unit 1 and stops the driving part of the pure water production device 1 (Sunono-F280 ).On the other hand, CI)IJ switches the first solenoid valve 21 to the water supply side at ?J+ and UX conversion, and then is supplied to the second pure water production unit !5 for processing. The thread thickness of the output water is 02 and the second electricity is 1 yen) 9 degrees lll 13
5 and sell it to the second pure water production unit 5.
Purity before burial U1 is compared to find the relative purity 1 (Shinomukai' - Maro ((]2, ·'01) (Step 10
5・IF〕0). Sosite, c p u +,, t, the direction -11, q (
? , ) 2 "" (J + ) 'a Compare with the preset first reconnaissance U r -(, ((So2-01)゛・Ul
・(If there is, it is determined that the second pure water production J-Soto 5 is damaged or the processing capacity has decreased. [Proceed to Sunozzo 200 and activate the alarm device 27 to notify the need to replace the unit 1-5.) [!(Stops driving of pure water production port 1) (step 280). In steps 205 to 230, the CPU explains the necessity of exchanging the third pure water production port 1 to 7. In steps 180 to 200, J
This is done by comparing the relative improvement in purity (U3."02), and if (U3/U2)>setting vessel U/(.
-(J2) ・, If it is Uz, the alarm device 27 is activated and the deionizer 1 is stopped (step 2ε30
>. Furthermore, the CPU compares the purity of the output water from the third pure water sold in step 205 with the purity of the output water from the production unit 7 to the preset desired purity (J).
If 3>Ul-1, it is determined that pure water with the desired purity has been produced, and the second electromagnetic valve 23 is activated to enable water sampling (step 270). >If it is UH, re-polishing and producing third pure water.
5 is turned off (step 260). In addition, in this practical example 0, 16 water was treated with 3 pure water products per 1 day to make pure water 111J, but the amount can be increased or decreased as needed to make bJ, Ikoto is iris 31, (shi<
F. In addition, in the Hoji IJ^ example, the circulation path is made of pure water made of 1ji holly [υ]
It is installed only in the filtration unit part (but it is installed in each pure water t!llj construction 2 I knit part)
Ensure that the purity of the output water of the unit is 1111 set for each concerned unit 1, and that the purity of the ultimately rejected pure water is increased by (-0) 1° or more. As explained in this invention, J,, It is, , fil
i zJ・: Measure the purity of each output water from multiple pure water units installed in the manufacturing equipment (), and if necessary, add the pure water “rA” in the previous stage of the output water Since I made it to be circulated to Zukonetsu 1~, each pure water!! A8 Coates 1-
Break 1i)':・, "Kasuit(1(r)・and the desired purity ■ is 1q of pure water

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

第1図はこの発明の実施例、:i’、 21シ1は第i
 r*]に示した実施例にJ5りる処理フ[−1−ヂr
−−L−図(ある、。 (図面のL要4ふ部分を表わづ荀翼の、31明)3・・
・第1の純水製造コニ・・ノ)・5− ff! 2 ノ
I+Ii水:F! 7古、、I −” ツh7・・・第
3の純水:IA造コニツト 9・・・マイク1−1]ンビ−?−タ ′11・・・第′1の電気1人々Nh[13・・・第2
の電気伝導度語 15・・・第3の電気1人心度h1 23・・・第2の電磁’5125・・・循j莫ポンプ特
 δ′1  出願人  )・L仙−手・l学+λ、式会
社5
FIG. 1 shows an embodiment of the present invention: i', 21 1 is the i-th
r*] J5 processing filter [-1-dir
--L-Diagram (There is. (Represents the L main part of the drawing, 31 marks of Xun's wing) 3...
・First pure water production process...ノ)・5-ff! 2 No I + Ii water: F! 7 old,, I-" tsuh7...Third pure water: IA construction unit 9...Mike 1-1] Nb-?-ta'11...'1st electricity 1 person Nh[13 ...Second
Electrical conductivity word 15...Third electricity 1 degree of conductivity h1 23...Second electromagnetic '5125...Circulation j Mo pump special δ'1 Applicant)・L Sen-te・L science+λ , Shikisha 5

Claims (1)

【特許請求の範囲】[Claims] 1京水を複数の純水製造−lニツ1−〇゛処理して純水
を製造する装置(こd5いて、各純水製造ユニツ1へか
らの各々の出力水の紳度測光装首と、純度測定結束が所
定値を越えている状態で前記出力水を処理出力した純水
製j責ユニツ1−に当該出力水を還流する循環装置と、
当該出力水の還流が一定時間絹゛続したことで純水製造
を停止覆る駆動制御装置とを設りたことを17)徴とり
る純水1契迄装置。
A device for producing pure water by processing 1 quintillion water in multiple pure water production units 1-〇゛ (this d5 is equipped with a light metering device for each output water from each pure water production unit 1). , a circulation device that returns the output water to the pure water responsible unit 1- which processed and output the output water in a state where the purity measurement band exceeds a predetermined value;
17) A deionized water supply system that detects the installation of a drive control device that stops deionized water production when the output water reflux continues for a certain period of time.
JP18177582A 1982-10-16 1982-10-16 Apparatus for manufacture of demineralized water Pending JPS5973092A (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP18177582A JPS5973092A (en) 1982-10-16 1982-10-16 Apparatus for manufacture of demineralized water
US06/529,598 US4563272A (en) 1982-10-16 1983-09-06 Demineralizer
DE3337169A DE3337169C2 (en) 1982-10-16 1983-10-12 Process for demineralizing water and demineralizer for carrying out the process
GB08327606A GB2128176B (en) 1982-10-16 1983-10-14 A demineralizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18177582A JPS5973092A (en) 1982-10-16 1982-10-16 Apparatus for manufacture of demineralized water

Publications (1)

Publication Number Publication Date
JPS5973092A true JPS5973092A (en) 1984-04-25

Family

ID=16106662

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18177582A Pending JPS5973092A (en) 1982-10-16 1982-10-16 Apparatus for manufacture of demineralized water

Country Status (1)

Country Link
JP (1) JPS5973092A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61110056A (en) * 1984-11-05 1986-05-28 Hitachi Ltd Liquid refining method and apparatus

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50147153A (en) * 1974-05-20 1975-11-26
JPS54146073A (en) * 1978-05-08 1979-11-14 Toukiyouto Screw-system sand-sediment drawing device operation method

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50147153A (en) * 1974-05-20 1975-11-26
JPS54146073A (en) * 1978-05-08 1979-11-14 Toukiyouto Screw-system sand-sediment drawing device operation method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61110056A (en) * 1984-11-05 1986-05-28 Hitachi Ltd Liquid refining method and apparatus

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