JP2853210B2 - Soft water production equipment - Google Patents
Soft water production equipmentInfo
- Publication number
- JP2853210B2 JP2853210B2 JP28405389A JP28405389A JP2853210B2 JP 2853210 B2 JP2853210 B2 JP 2853210B2 JP 28405389 A JP28405389 A JP 28405389A JP 28405389 A JP28405389 A JP 28405389A JP 2853210 B2 JP2853210 B2 JP 2853210B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- soft water
- boiler
- chamber
- blow
- 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.)
- Expired - Fee Related
Links
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- Separation Using Semi-Permeable Membranes (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明はイオン交換膜を用いた軟水給水ボイラ用の軟
水製造装置、特にドナン膜透析装置を用いた軟水製造装
置に関する。Description: TECHNICAL FIELD The present invention relates to a soft water producing apparatus for a soft water feed water boiler using an ion exchange membrane, and more particularly to a soft water producing apparatus using a Donan membrane dialysis apparatus.
従来、軟水給水ボイラ用の軟水製造装置として、Na形
カチオン交換樹脂により原水中のCa2+やMg2+などの硬度
成分を捕捉して軟水化する軟水製造装置が使用されてい
る。2. Description of the Related Art Conventionally, as a soft water producing device for a soft water feed water boiler, a soft water producing device that captures hardness components such as Ca 2+ and Mg 2+ in raw water with a Na-type cation exchange resin and softens the water has been used.
このような軟水製造装置は、Na形カチオン交換樹脂中
のNa+と原水中のCa2+やMg2+をイオン交換して軟水を製
造しているため、カチオン交換樹脂がCa2+やMg2+で飽和
すると、軟化を一時中断して、例えばNaCl溶液などの再
生剤を供給して、カチオン交換樹脂をNa形に再生する作
業が必要である。Such a soft water producing apparatus ion-exchanges Na + in the Na type cation exchange resin with Ca 2+ or Mg 2+ in the raw water to produce soft water, so that the cation exchange resin is Ca 2+ or Mg When saturated with 2+, it is necessary to temporarily suspend softening and supply a regenerant such as a NaCl solution to regenerate the cation exchange resin into the Na form.
この再生作業は手間がかかり、自動再生を行う場合で
も再生剤の補給が必要であり、再生剤の入れ忘れなどに
よるトラブルも発生する可能性がある。また再生作業に
より軟化工程が中断するため、連続して軟水を製造でき
ず、ボイラに連続して軟水を供給するためには、再生作
業の間に供給するための軟水を貯留しておくタンクが必
要となる。さらに再生剤として特別の薬剤が必要であ
る。This regenerating operation is troublesome, requires replenishment of the regenerating agent even when performing automatic regenerating, and there is a possibility that a trouble such as forgetting to insert the regenerating agent may occur. In addition, since the softening process is interrupted by the regeneration operation, soft water cannot be produced continuously.To continuously supply soft water to the boiler, a tank for storing soft water to be supplied during the regeneration operation is required. Required. Further, a special agent is required as a regenerating agent.
本発明の目的は、上記問題点を解決するもので、軟水
を連続的に製造でき、軟化工程を中断して行う特別の再
生工程、ならびに特別の再生薬剤が不要で、製造コスト
を低減できる軟水製造装置を提供することを目的とす
る。An object of the present invention is to solve the above-mentioned problems, a soft water can be continuously produced, a special regeneration step performed by interrupting the softening step, and a soft water that can reduce the production cost without requiring a special regeneration agent. An object is to provide a manufacturing apparatus.
本発明は、カチオン交換膜により仕切られた被処理液
室および再生剤室と、原水を前記被処理液室に導く流路
と、被処理液室から軟化水をボイラに給水する流路と、
ボイラからブロー水を前記再生剤室に導く流路とを有し
ていることを特徴とする軟水製造装置である。The present invention provides a liquid chamber to be treated and a regenerating agent chamber partitioned by a cation exchange membrane, a flow path for guiding raw water to the liquid processing chamber, and a flow path for supplying softened water from the liquid processing chamber to the boiler,
A soft water producing apparatus having a flow path for guiding blow water from a boiler to the regenerating agent chamber.
本発明で使用する原水としては、硬度成分を含む水道
水、工業用水、河川水、井戸水など、一般にボイラに供
給されている硬度成分を含む水が使用できる。As the raw water used in the present invention, water containing a hardness component generally supplied to a boiler, such as tap water, industrial water, river water, and well water containing a hardness component, can be used.
本発明で使用する再生剤は、ボイラ水の濃度を一定に
保つためにボイラ稼動中にブローされるブロー水であ
る。このブロー水はブロー率によって異なるが、通常、
原水の20倍程度のアルカリ金属イオン濃度を有してい
る。本発明では、ブロー水のアルカリ金属イオンと原水
中の硬度成分が、カチオン交換膜を介してドナン膜透析
できるような濃度勾配を有するブロー水を使用するが、
下記(1)式を満たすものが好ましい。The regenerant used in the present invention is blow water blown during operation of the boiler to keep the concentration of the boiler water constant. This blow water depends on the blow rate, but usually
It has an alkali metal ion concentration about 20 times that of raw water. In the present invention, blow water having a concentration gradient such that the alkali metal ions of the blow water and the hardness component in the raw water can be dialyzed through a cation exchange membrane using a Donan membrane,
Those satisfying the following expression (1) are preferable.
〔作 用〕 本発明の軟水製造装置では、Ca2+やMg2+などの硬度成
分を含む原水を被処理液室に供給し、アルカリ金属イオ
ンを高濃度で含むボイラのブロー水を再生剤室に供給
し、被処理液室と再生剤室を仕切るカチオン交換膜を介
して、ドナン膜透析を行う。このとき原水中の硬度成分
は再生剤室側に、またブロー水中のアルカリ金属イオン
は被処理液室側に透析され、原水が軟化される。そして
軟化水を供給としてボイラに供給し、その濃縮されてア
ルカリ金属イオン濃度が増しているブロー水を軟水製造
装置の再生剤に導き、再生剤として使用する。 [Operation] In the soft water producing apparatus of the present invention, raw water containing a hardness component such as Ca 2+ or Mg 2+ is supplied to the liquid chamber to be treated, and blow water of a boiler containing alkali metal ions at a high concentration is used as a regenerating agent. The solution is supplied to the chamber, and the Donane membrane dialysis is performed through a cation exchange membrane that separates the liquid chamber to be treated and the regenerant chamber. At this time, the hardness component in the raw water is dialyzed toward the regenerating agent chamber, and the alkali metal ions in the blow water are dialyzed toward the liquid chamber to be treated, so that the raw water is softened. Then, the softened water is supplied to the boiler as a supply, and the blown water, which has been concentrated and has an increased alkali metal ion concentration, is led to a regenerating agent of a softening water producing apparatus and used as a regenerating agent.
以下、本発明の実施例を図面により説明する。 Hereinafter, embodiments of the present invention will be described with reference to the drawings.
第1図は実施例の軟水製造装置の系統図、第2図は軟
水製造装置の分解斜視図である。FIG. 1 is a system diagram of a soft water producing apparatus according to an embodiment, and FIG. 2 is an exploded perspective view of the soft water producing apparatus.
図において、1は軟水製造装置、2はボイラである。
軟水製造装置1は被処理液室3と再生剤室4がカチオン
交換膜5により仕切られている。この被処理液室3およ
び再生剤室4はスペーサ5a、5bによって形成され、両端
部に端板6a、6bを配置してボルト7およびナット8によ
り締結されている。第1図および第2図では理解しやす
いように、被処理液室3と再生剤室4のユニットが1個
だけ図示されているが、実際はこれらの複数のユニット
が多数並べて積層されている。In the figure, 1 is a soft water production device, and 2 is a boiler.
In the soft water producing apparatus 1, the liquid chamber 3 to be treated and the regenerating agent chamber 4 are separated by a cation exchange membrane 5. The liquid chamber 3 and the regenerating agent chamber 4 are formed by spacers 5a and 5b, and end plates 6a and 6b are arranged at both ends and fastened by bolts 7 and nuts 8. In FIGS. 1 and 2, only one unit of the liquid chamber 3 and the regenerating agent chamber 4 is shown for easy understanding, but in reality, many of these units are stacked side by side.
各スペーサ5a、5bには流入孔9a、9bおよび流出孔10
a、10bが設けられている。被処理液室3の流入孔9aは原
水管11に連絡し、被処理液室3の流出孔10aは給水管12
によりボイラ2に連絡している。また再生剤室4の流入
孔9bはブロー水管13によりボイラ2に連絡し、再生剤室
4の流出孔10bは排水管14に連絡している。被処理液室
3と再生剤室4は併流式となっているが、向流式あるい
は交差流式でもよい。Each spacer 5a, 5b has an inflow hole 9a, 9b and an outflow hole 10
a and 10b are provided. The inflow hole 9a of the liquid chamber 3 to be treated communicates with the raw water pipe 11, and the outflow hole 10a of the liquid chamber 3 to be treated is connected to the water supply pipe 12.
To boiler 2. The inflow hole 9b of the regenerating agent chamber 4 is connected to the boiler 2 by a blow water pipe 13, and the outflow hole 10b of the regenerating agent chamber 4 is connected to a drain pipe 14. The liquid chamber 3 and the regenerating agent chamber 4 are of a co-current type, but may be of a counter-current type or a cross-current type.
ボイラ2は給水管12から軟水が供給され、蒸気管15か
ら蒸気が取出され、その一部は負荷16から復水として、
復水管17を経て給水管12の軟水とともにボイラ2に循環
するようになっている。またボイラ2内の水の濃度を一
定に保つために、ボイラ水の一部がブロー水として取出
され、ブロー水管13から軟水製造装置1の再生剤室4に
再生剤として供給されるようになっている。In the boiler 2, soft water is supplied from a water supply pipe 12, and steam is taken out from a steam pipe 15, and a part of the steam is condensed from a load 16,
The water is circulated to the boiler 2 through the condensing pipe 17 together with the soft water of the water supply pipe 12. Also, in order to keep the concentration of water in the boiler 2 constant, a part of the boiler water is taken out as blow water and supplied from the blow water pipe 13 to the regenerant chamber 4 of the soft water producing apparatus 1 as a regenerant. ing.
このような軟水製造装置では、原水管11より被処理液
室3にCa2+やMg2+などの硬度成分を含む原水を供給し、
ブロー水管13より再生剤室4にアルカリ金属イオンを多
く含むボイラ2のブロー水を供給して軟化を行う。この
ときブロー水のアルカリ金属イオン濃度が高いため、カ
チオン交換膜はアルカリ金属イオン(Na)型になるが、
原水中の硬度成分の方が選択性が高いため、イオン交換
が行われる。そして硬度成分を交換したカチオン交換膜
が、ブロー水で再生されてアルカリ金属イオン型にな
り、結果的に各イオンの濃度勾配をドライビングフォー
スとしてドナン膜透析が行われる。このため原水中の硬
度成分は再生剤室4側に、またブロー水中のアルカリ金
属イオンは被処理液室3側にそれぞれ透析され、その結
果原水が軟化される。そして軟水が給水管12からボイラ
2に供給されて蒸気となり、ボイラ2のブロー水はブロ
ー水管13から再生剤室4に供給され、再生剤として使用
され、排水管14から排出される。In such a soft water producing apparatus, raw water containing a hardness component such as Ca 2+ and Mg 2+ is supplied from the raw water pipe 11 to the liquid chamber 3 to be treated,
The blow water of the boiler 2 containing a large amount of alkali metal ions is supplied from the blow water pipe 13 to the regenerating agent chamber 4 for softening. At this time, since the alkali metal ion concentration of the blow water is high, the cation exchange membrane becomes an alkali metal ion (Na) type,
Since the hardness component in the raw water has higher selectivity, ion exchange is performed. Then, the cation exchange membrane whose hardness components have been exchanged is regenerated with blow water to be of an alkali metal ion type. As a result, Donan membrane dialysis is performed using the concentration gradient of each ion as a driving force. For this reason, the hardness component in the raw water is dialyzed toward the regenerating agent chamber 4 and the alkali metal ions in the blow water are dialyzed toward the liquid chamber 3 to be treated. As a result, the raw water is softened. Then, the soft water is supplied from the water supply pipe 12 to the boiler 2 and becomes steam, and the blow water of the boiler 2 is supplied from the blow water pipe 13 to the regenerating agent chamber 4, used as a regenerant, and discharged from the drain pipe 14.
このような軟水製造装置1では、イオン交換(軟化)
と再生が並行して連続的に行われるため、連続して排出
されるボイラ2のブロー水が、連続して再生剤に利用で
き、再生のための軟化工程の中断や、軟水またはブロー
水貯留槽なども必要ではない。このため軟化工程を中断
して行う特別の再生工程や特別の再生薬剤が不要とな
り、軟水を連続的に低コストで製造することができる。In such a soft water producing apparatus 1, ion exchange (softening) is performed.
And regeneration are performed in parallel and continuously, so that the blow water of the boiler 2 discharged continuously can be continuously used as a regenerant, and the softening process for regeneration can be interrupted, or the soft water or blow water can be stored. No tank is required. This eliminates the need for a special regeneration step or a special regeneration agent that is performed by interrupting the softening step, and enables continuous production of soft water at low cost.
次に試験例について説明する。 Next, test examples will be described.
試験例 第1図および第2図に示すような軟水製造装置を用
い、カチオン交換膜に旭硝子(株)製の強酸性カチオン
交換膜セレミオンCMV(商標)を使用し、下記の条件で
運転して軟水を製造した。Test Example Using a soft water production apparatus as shown in FIGS. 1 and 2, a strong acid cation exchange membrane Selemion CMV (trade name) manufactured by Asahi Glass Co., Ltd. was used as the cation exchange membrane, and operated under the following conditions. Soft water was produced.
原 水…厚木市水(水質を表1に示す) ブロー水…Na濃度:0.027N(ブロー率約5%) 通液速度…原 水:1.4ml/min 軟化剤:0.07ml/min 通液方法…向流 膜面積…114cm2 得られた軟水のカチオン(Na、K、Mg、Ca)濃度を原
子吸光法にて測定した。なお軟水のサンプリングは、負
荷した原水中のCa2+、Mg2+の当量の総和がカチオン交換
膜の交換容量を上回った後に行った。Raw water: Atsugi city water (water quality is shown in Table 1) Blow water: Na concentration: 0.027N (blow rate: about 5%) Flow rate: Raw water: 1.4 ml / min Softener: 0.07 ml / min ··· Countercurrent membrane area · · 114 cm 2 The concentration of cations (Na, K, Mg, Ca) in the obtained soft water was measured by an atomic absorption method. The sampling of soft water was performed after the total equivalent of Ca 2+ and Mg 2+ in the loaded raw water exceeded the exchange capacity of the cation exchange membrane.
軟水の分析結果は表1のとおりであり、一般の軟水給
水ボイラの目標である硬度成分1mg/(CaCO3として)
を大きく下回る軟水が得られた。The analysis result of soft water is as shown in Table 1. Hardness component 1mg / (as CaCO 3 ) which is the target of general soft water feed water boiler
Was obtained.
〔発明の効果〕 本発明ではボイラのブロー水を再生剤として用いて原
水をドナン膜透析するので、軟水を連続的に製造でき、
軟化を中断して行う特別の再生工程や特別の再生薬剤が
不要で、製造コストが低減できる軟水製造装置が得られ
る。 [Effects of the Invention] In the present invention, raw water is subjected to Donan membrane dialysis using boiler blow water as a regenerant, so that soft water can be continuously produced,
Thus, a soft water producing apparatus which does not require a special regeneration step or a special regenerating agent for interrupting softening and can reduce the production cost can be obtained.
第1図は実施例の軟水製造装置の系統図、第2図はその
分解斜視図である。 各図中、同一符号は同一または相当部分を示し、1は軟
水製造装置、2はボイラ、3は被処理液室、4は再生剤
室、5はカチオン交換膜、11は原水管、12は給水管、13
はブロー水管である。FIG. 1 is a system diagram of a soft water producing apparatus according to an embodiment, and FIG. 2 is an exploded perspective view thereof. In each figure, the same reference numerals indicate the same or corresponding parts, 1 is a soft water producing apparatus, 2 is a boiler, 3 is a liquid chamber to be treated, 4 is a regenerant chamber, 5 is a cation exchange membrane, 11 is a raw water pipe, and 12 is a raw water pipe. Water pipe, 13
Is a blow water pipe.
Claims (1)
室および再生剤室と、原水を前記被処理液室に導く流路
と、被処理液室から軟化水をボイラに給水する流路と、
ボイラからブロー水を前記再生剤室に導く流路とを有し
ていることを特徴とする軟水製造装置。1. A liquid chamber to be treated and a regenerating agent chamber partitioned by a cation exchange membrane, a flow path for leading raw water to the liquid chamber, and a flow path for supplying softened water from the liquid chamber to the boiler. ,
A soft water producing apparatus having a flow path for guiding blow water from the boiler to the regenerating agent chamber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP28405389A JP2853210B2 (en) | 1989-10-31 | 1989-10-31 | Soft water production equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP28405389A JP2853210B2 (en) | 1989-10-31 | 1989-10-31 | Soft water production equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03146190A JPH03146190A (en) | 1991-06-21 |
| JP2853210B2 true JP2853210B2 (en) | 1999-02-03 |
Family
ID=17673681
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP28405389A Expired - Fee Related JP2853210B2 (en) | 1989-10-31 | 1989-10-31 | Soft water production equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2853210B2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105439317A (en) * | 2015-11-19 | 2016-03-30 | 四川省宜宾惠美线业有限责任公司 | Application method of cation bed failure outlet water |
| CN105347558A (en) * | 2015-11-19 | 2016-02-24 | 四川省宜宾惠美线业有限责任公司 | Application system for cation exchanger failure and water outlet |
| KR20220131387A (en) * | 2020-02-18 | 2022-09-27 | 가부시기가이샤에프.씨.씨 | Ion-exchange device |
-
1989
- 1989-10-31 JP JP28405389A patent/JP2853210B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03146190A (en) | 1991-06-21 |
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| LAPS | Cancellation because of no payment of annual fees |