JPH0768255A - Water softener for steam generator - Google Patents
Water softener for steam generatorInfo
- Publication number
- JPH0768255A JPH0768255A JP5221072A JP22107293A JPH0768255A JP H0768255 A JPH0768255 A JP H0768255A JP 5221072 A JP5221072 A JP 5221072A JP 22107293 A JP22107293 A JP 22107293A JP H0768255 A JPH0768255 A JP H0768255A
- Authority
- JP
- Japan
- Prior art keywords
- water
- electrolyzer
- exchange resin
- steam generator
- cation exchange
- 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
Links
Landscapes
- Treatment Of Water By Ion Exchange (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
(57)【要約】
【目的】 薬品の供給を不要化し連続的に軟水を供給す
る。
【構成】 蒸気発生装置17に水を供給する水路に、流
路切り換え弁8、9、14と、電気分解装置2と、陽イ
オン交換樹脂12を充填した軟水化装置13を設け、採
水時には電気分解装置2に水が流れないよう弁8、9を
切り換え、イオン交換樹脂の再生時には、電気分解装置
2の両電極間に直流電圧を印加し、陽極室5で得られる
酸性水を陽イオン交換樹脂12を再生する再生水として
軟水化装置13に供給する。これによって、樹脂再生用
の、薬品供給が不要となり連続的に軟水が供給される。
(57) [Summary] [Purpose] Supplying soft water continuously without chemical supply. [Structure] A water passage for supplying water to a steam generator 17 is provided with flow path switching valves 8, 9, 14 and an electrolyzer 2 and a water softener 13 filled with a cation exchange resin 12 for collecting water. The valves 8 and 9 are switched so that water does not flow to the electrolyzer 2, and at the time of regeneration of the ion exchange resin, a DC voltage is applied between both electrodes of the electrolyzer 2 so that the acidic water obtained in the anode chamber 5 is converted into cations. It is supplied to the water softening device 13 as regenerated water for regenerating the exchange resin 12. As a result, the supply of chemicals for resin regeneration becomes unnecessary, and soft water is continuously supplied.
Description
【0001】[0001]
【産業上の利用分野】本発明は、家庭用蒸気発生装置、
加湿器、食器洗い器、洗濯機などに用いる軟水器に関す
るものである。BACKGROUND OF THE INVENTION The present invention relates to a household steam generator,
The present invention relates to a water softener used in a humidifier, a dishwasher, a washing machine, and the like.
【0002】[0002]
【従来の技術】一般に、水道水、井戸水はカルシウム、
マグネシウムイオン等の硬度成分を含んでおり、このよ
うな水を蒸気発生装置に用いると、缶体内にスケールが
付着し、伝熱状態が不良になる。これらの問題を改善す
る目的で従来より提案されている軟水器を、図4に基づ
いて説明する。2. Description of the Related Art Generally, tap water and well water are calcium,
It contains hardness components such as magnesium ions, and if such water is used in a steam generator, the scale adheres to the inside of the can, resulting in poor heat transfer. A water softener conventionally proposed for the purpose of improving these problems will be described with reference to FIG.
【0003】図4において、水は原水供給パイプ1を通
り、ポーラスな隔壁、例えば素焼きの隔壁7によって、
陽極室5、陰極室6を分離形成し、各極室には電極3お
よび4が吊設されている電気分解装置2に入る。イオン
交換時には、陰極水出口パイプ11に接続されている排
水弁21は閉じられており、水は陽極室5、陽極水出口
パイプ10を通って、陽イオン交換樹脂12の充填して
ある軟水化装置13に入る。陽イオン交換樹脂12によ
り、水中のカルシウム、マグネシウム等の陽イオンは、
水素イオンと置換され、軟化された水が蒸気発生装置1
7に供給される。 イオン交換樹脂再生時には、電気分
解装置2の電極3および4に直流電圧を印加し、得られ
た酸性水を軟水化装置13に軟水化装置上部から供給
し、樹脂を水素型に再生する。In FIG. 4, water passes through the raw water supply pipe 1 and is supplied by a porous partition wall, for example, a unglazed partition wall 7.
The anode chamber 5 and the cathode chamber 6 are separately formed, and the electrodes 3 and 4 enter the electrolyzer 2 in which the electrodes 3 and 4 are suspended. At the time of ion exchange, the drain valve 21 connected to the cathode water outlet pipe 11 is closed, and the water passes through the anode chamber 5 and the anode water outlet pipe 10 to soften the water filled with the cation exchange resin 12. Enter device 13. With the cation exchange resin 12, cations such as calcium and magnesium in water are
The water that has been replaced with hydrogen ions and softened is the steam generator 1
7 is supplied. At the time of regenerating the ion exchange resin, a direct current voltage is applied to the electrodes 3 and 4 of the electrolyzer 2, and the obtained acidic water is supplied to the water softening device 13 from above the water softening device to regenerate the resin into a hydrogen type.
【0004】[0004]
【発明が解決しようとする課題】しかしながら従来の軟
水器では、電気分解装置の陰極にステンレスを用いると
電極間非通電時電圧にはステンレス電極の腐食が起こ
り、陰極に貴金属電極を用いるとコストが高くなるとい
う課題があった。However, in the conventional water softener, when stainless steel is used for the cathode of the electrolyzer, corrosion of the stainless electrode occurs in the voltage when the electrodes are not energized, and when a noble metal electrode is used for the cathode, the cost is reduced. There was a problem of becoming higher.
【0005】また、イオン交換樹脂による軟水化が水温
に大きく影響され、水温の低い所では大容量の樹脂が必
要とされるという課題があり、再生時に水の電気分解で
得られる酸性水を用いるため装置が複雑化するという課
題もあった。Further, there is a problem that the softening of water by the ion exchange resin is greatly affected by the water temperature, and a large volume of resin is required at a place where the water temperature is low. Therefore, acid water obtained by electrolysis of water during regeneration is used. Therefore, there is a problem that the device becomes complicated.
【0006】本発明は上記課題を解決するもので、第1
の目的として、水中の硬度成分を効率的に除去し、蒸気
発生装置缶体へのスケール付着を防止することであり、
第2の目的としては、軟水化装置のコストを下げるこ
と、第3の目的としては、装置を単純化することにあ
る。The present invention is intended to solve the above-mentioned problems.
The purpose of this is to efficiently remove hardness components in water and prevent scale adhesion to the steam generator can body.
The second purpose is to reduce the cost of the water softening device, and the third purpose is to simplify the device.
【0007】[0007]
【課題を解決するための手段】本発明は上記目的を達成
するため、第1の手段として、蒸気発生装置に水を供給
する水路に陰極室を隔膜で仕切り陽極室と陰極室を多槽
分離形成し、これら極室にそれぞれ電極を配設し、樹脂
再生時には両電極間に直流電圧を印加し、陽極室で得ら
れる酸性水を陽イオン交換樹脂を再生する再生水として
軟水化装置に供給する電気分解装置と陽イオン交換樹脂
を充填した軟水化装置と採水時と再生時で水路を切り換
える弁とを設け、電極間非通電時には電気分解装置に水
が流れないようにする構成としたものである。In order to achieve the above object, the present invention provides, as a first means, a cathode chamber is partitioned by a diaphragm in a water passage for supplying water to a steam generator, and the anode chamber and the cathode chamber are separated into multiple tanks. Electrodes are provided in these electrode chambers, and a DC voltage is applied between both electrodes during resin regeneration, and the acidic water obtained in the anode chamber is supplied to the water softener as regeneration water for regenerating the cation exchange resin. An electrolysis device and a water softening device filled with cation exchange resin, and a valve that switches the water channel between water collection and regeneration so that water does not flow to the electrolysis device when the electrodes are not energized Is.
【0008】また、第2の手段として、陽イオン交換樹
脂を充填し、採水時には軟水化装置を加熱ヒーターで加
熱保温し、再生時には、軟水化装置の加熱を止め、温度
差により陽イオン交換樹脂を再生する軟水化装置を蒸気
発生装置の供給水路に配置する構成としたものである。As a second means, a cation exchange resin is filled, the water softening device is heated and kept warm by a heater when water is collected, the heating of the water softening device is stopped at the time of regeneration, and cation exchange is performed due to a temperature difference. The water softening device for regenerating the resin is arranged in the supply water passage of the steam generator.
【0009】[0009]
【作用】本発明第1の手段による蒸気発生装置用の軟水
器は、採水時には電気分解装置に通水しないため、非通
電時でもステンレス電極の腐食の恐れがなくなり、陰極
にステンレス電極を用いることができ、電極コストを下
げることができる。In the water softener for the steam generator according to the first means of the present invention, since water is not passed through the electrolyzer during water sampling, there is no fear of corrosion of the stainless electrode even when the power is not supplied, and the stainless electrode is used as the cathode. Therefore, the electrode cost can be reduced.
【0010】本発明第2の手段による蒸気発生装置用の
軟水器は、採水時には軟水化装置を加熱ヒーターで加熱
保温し、水中のカルシウム、マグネシウムイオンを水素
イオンで置換し、軟化水を蒸気発生装置に供給すること
が出来る。また、樹脂の再生時には、軟水化装置の加熱
を止め、温度差による樹脂の再生を行うため、水電気分
解装置等が不要となり装置を単純化することができる。In the water softener for a steam generator according to the second means of the present invention, the water softener is heated and kept warm by a heater at the time of water sampling, the calcium and magnesium ions in the water are replaced with hydrogen ions, and the softened water is steamed. It can be supplied to the generator. Further, when the resin is regenerated, the heating of the water softening device is stopped and the resin is regenerated due to the temperature difference. Therefore, a water electrolysis device or the like is not required and the device can be simplified.
【0011】[0011]
(実施例1)本発明の第1の手段の実施例を図1に基づ
いて説明する。(Embodiment 1) An embodiment of the first means of the present invention will be described with reference to FIG.
【0012】図において、1は原水供給パイプ、2は原
水供給パイプ1を通して下方から水が供給される電気分
解装置であり、ポーラスな隔壁、例えば素焼きの隔壁7
によって陰極室6と陽極室5とに分離形成しており、陽
極室壁面を陽極3とし、陰極室6には陰極4を吊設して
いる。この電気分解装置2の陰極室6の上部には排水パ
イプ11が連通され、陽極室5の上部には軟水化装置1
3の上方に連通するパイプ10が接続されている。軟水
化装置13には陽イオン交換樹脂12が収納され、この
軟水化装置13の下部にはパイプ16を介して蒸気発生
装置17が連通している。なお、原水供給パイプ1から
電気分解装置2または軟水化装置13への水を供給する
水路には水路を切り換える弁8、9が設けられ、また軟
水化装置13から蒸気発生装置17または排水パイプ1
5への水路には水路を切り換える弁14が設けられてい
る。In the figure, 1 is a raw water supply pipe, 2 is an electrolyzer to which water is supplied from below through the raw water supply pipe 1, and is a porous partition wall, for example, unglazed partition wall 7.
The cathode chamber 6 and the anode chamber 5 are separately formed by using the anode chamber wall surface as the anode 3, and the cathode 4 is suspended in the cathode chamber 6. A drain pipe 11 is connected to the upper part of the cathode chamber 6 of the electrolyzer 2 and the water softener 1 is connected to the upper part of the anode chamber 5.
A pipe 10 communicating with the upper part of 3 is connected. A cation exchange resin 12 is housed in the water softening device 13, and a steam generator 17 communicates with a lower portion of the water softening device 13 via a pipe 16. It should be noted that valves 8 and 9 for switching water channels are provided in a water channel for supplying water from the raw water supply pipe 1 to the electrolyzer 2 or the water softener 13, and the water softener 13 to the steam generator 17 or the drain pipe 1 is provided.
The waterway to 5 is provided with a valve 14 for switching the waterway.
【0013】以上の構成において、水は原水供給パイプ
1を通り、採水時には水が、電気分解装置2に流れない
よう、弁8及び9を切り換え、水は陽イオン交換樹脂1
2の充填してある軟水化装置13に上方向から入り、陽
イオン交換樹脂12により、水中のカルシウム、マグネ
シウム等の陽イオンは、水素イオンと置換され、軟化さ
れた水がパイプ16を通って、蒸気発生装置17に供給
される。In the above structure, the water passes through the raw water supply pipe 1, and the valves 8 and 9 are switched so that the water does not flow to the electrolyzer 2 at the time of water sampling.
2 is entered from above into the water softening device 13 filled with cations, and cations such as calcium and magnesium in the water are replaced with hydrogen ions by the cation exchange resin 12, and the softened water passes through the pipe 16. , To the steam generator 17.
【0014】イオン交換樹脂再生時には、水が電気分解
装置2を介して軟水化装置13に流れるように弁8及び
9を切り換え、電気分解装置2の両電極間に直流電圧を
印加し、陽極室5で得られた酸性水を軟水化装置13に
軟水化装置上部から供給し、樹脂を水素型に再生する。
再生時には、弁14は蒸気発生装置17に水を供給しな
いように切り換え、軟水化装置13からの水は、排水パ
イプ15を通って排水される。水電気分解装置2の陰極
室6内のアルカリ水は排水パイプ11を通って排水され
る。During regeneration of the ion-exchange resin, the valves 8 and 9 are switched so that water flows through the electrolyzer 2 to the water softener 13, and a DC voltage is applied between both electrodes of the electrolyzer 2 so that the anode chamber The acidic water obtained in 5 is supplied to the water softening device 13 from the upper part of the water softening device to regenerate the resin into a hydrogen form.
During regeneration, the valve 14 is switched so as not to supply water to the steam generator 17, and the water from the water softening device 13 is drained through the drain pipe 15. The alkaline water in the cathode chamber 6 of the water electrolyzer 2 is drained through the drain pipe 11.
【0015】電気分解装置2は陽極3に、チタン−白金
メッキ電極等のチタン−貴金属不溶性電極、陰極4にス
テンレス電極を用い、通電時には、水を下方向から上方
向に電極面に沿って通水するため、水の電気分解で発生
した気泡が電極面から離脱しやすくなり、電気分解装置
2内にガスがたまることがなくなり、これによって槽電
圧の上昇を防止できる。また採水時、停止時等の電極間
非通電時には、電気分解装置2に水を通水しない構成の
ため、陰極4のステンレス電極の腐食を防止することが
できる。The electrolyzer 2 uses a titanium-precious metal insoluble electrode such as a titanium-platinum-plated electrode for the anode 3, and a stainless steel electrode for the cathode 4. When electricity is applied, water is passed from the lower side to the upper side along the electrode surface. Since water is supplied, bubbles generated by electrolysis of water are easily separated from the electrode surface, and gas is not accumulated in the electrolyzer 2. This makes it possible to prevent increase in cell voltage. In addition, since water is not passed through the electrolyzer 2 when the electrodes are not energized, such as when collecting water or when stopping, corrosion of the stainless steel electrode of the cathode 4 can be prevented.
【0016】以上のように本実施例1では、陽イオン交
換樹脂12で水中のカルシウム、マグネシウムイオン等
の硬度成分を除去し、蒸気発生装置17の缶体へのスケ
ールの付着を防止出来、水の電気分解で得られた酸性水
でイオン交換樹脂の再生を行うことで、連続的に軟水を
蒸気発生装置17に供給することができる。As described above, in the first embodiment, the cation exchange resin 12 can remove hardness components such as calcium and magnesium ions in the water to prevent the scale from adhering to the can of the steam generator 17, and The soft water can be continuously supplied to the steam generator 17 by regenerating the ion exchange resin with the acidic water obtained by the electrolysis.
【0017】また、電気分解装置2の壁面を電極とする
ことで、装置を薄型化でき、槽電圧の上昇も防止でき、
採水時、停止時等の電極間非通電時には、電気分解装置
2に水を通水しないため、ステンレス電極の腐食を防止
し、陰極材料としてステンレスを用いることが出来、電
極コストを下げることができる。Further, by using the wall surface of the electrolyzer 2 as an electrode, the device can be made thin and the rise of the cell voltage can be prevented,
Since water does not pass through the electrolyzer 2 when the electrodes are not energized, such as when collecting water or when stopping, the corrosion of the stainless electrodes can be prevented, and stainless steel can be used as the cathode material, reducing the electrode cost. it can.
【0018】(実施例2)本発明の第1の手段の第2の
実施例を図2に基づいて説明する。(Embodiment 2) A second embodiment of the first means of the present invention will be described with reference to FIG.
【0019】図2において、水は原水供給パイプ1を通
り、採水時には水が、電気分解装置2に流れないよう、
弁8を切り換え、水は陽イオン交換樹脂12の充填して
ある軟水化装置13に上方向から入り、陽イオン交換樹
脂12により、水中のカルシウム、マグネシウム等の陽
イオンは、水素イオンと置換され、軟化された水がパイ
プ16を通って蒸気発生装置17に供給される。In FIG. 2, the water passes through the raw water supply pipe 1 so that the water does not flow to the electrolyzer 2 at the time of water sampling.
The valve 8 is switched, and water enters the water softening device 13 filled with the cation exchange resin 12 from above, and the cation exchange resin 12 replaces cations such as calcium and magnesium in the water with hydrogen ions. The softened water is supplied to the steam generator 17 through the pipe 16.
【0020】イオン交換樹脂再生時には、電気分解装置
2に水が流れるように弁8を切り換えるので、水はパイ
プ18を通り、電気分解装置2に下部から供給され、電
気分解装置2の両電極間に直流電圧を印加し、陽極室5
で得られた酸性水を再生水パイプ10を通って、軟水化
装置13に軟水化装置下部から供給し、樹脂を水素型に
再生し、排水弁19を切り換えてパイプ20から排水さ
れる。陰極室6で得られるアルカリ水は排水弁21を開
き排水する。再生時には、排水弁14は水を軟水化装置
13に通水する方向に切り換え、蒸気発生装置17に水
を供給しないようにする。During regeneration of the ion exchange resin, the valve 8 is switched so that water flows to the electrolyzer 2, so that water is supplied from below to the electrolyzer 2 through the pipe 18 and between the electrodes of the electrolyzer 2. DC voltage is applied to the anode chamber 5
The acidic water obtained in 1 is supplied to the water softening device 13 from the lower part of the water softening device through the reclaimed water pipe 10, the resin is regenerated into the hydrogen type, and the drain valve 19 is switched to be drained from the pipe 20. The alkaline water obtained in the cathode chamber 6 is drained by opening the drain valve 21. At the time of regeneration, the drain valve 14 switches the water to the direction in which the water is passed to the water softening device 13 so that the water is not supplied to the steam generator 17.
【0021】停止時には排水弁14を切り換え、電気分
解装置2、軟水化装置13の水をすべて排水し、水抜き
をする。When stopped, the drain valve 14 is switched to drain all the water from the electrolyzer 2 and the water softener 13, and drain the water.
【0022】電気分解装置2は陽極3に、チタン−白金
メッキ電極等のチタン−貴金属不溶性電極、陰極4にス
テンレス電極を用い、通電時には、水を下方向から上方
向に電極面に沿って通水するため、水の電気分解で発生
した気泡が電極面から離脱しやすくなり、電気分解装置
2内にガスがたまることがなくなり、これによって槽電
圧の上昇を防止できる。また採水時、停止時等の電極間
非通電時には、電気分解装置2に水を通水しない構成の
ため、陰極4のステンレス電極の腐食を防止することが
できる。The electrolyzer 2 uses a titanium-precious metal insoluble electrode such as a titanium-platinum-plated electrode for the anode 3, and a stainless steel electrode for the cathode 4. When electricity is applied, water is passed from the lower side to the upper side along the electrode surface. Since water is supplied, bubbles generated by electrolysis of water are easily separated from the electrode surface, and gas is not accumulated in the electrolyzer 2. This makes it possible to prevent increase in cell voltage. In addition, since water is not passed through the electrolyzer 2 when the electrodes are not energized, such as when collecting water or when stopping, corrosion of the stainless steel electrode of the cathode 4 can be prevented.
【0023】樹脂逆洗時には、陰極室6の排水弁21を
閉じ、水を軟水化装置13の下部から供給し、陽イオン
交換樹脂12を洗浄して、排水パイプ20を通って排水
される。At the time of backwashing the resin, the drain valve 21 of the cathode chamber 6 is closed, water is supplied from the lower part of the water softener 13, the cation exchange resin 12 is washed, and the water is drained through the drain pipe 20.
【0024】以上のように本実施例2では、陽イオン交
換樹脂で水中のカルシウム、マグネシウムイオン等の硬
度成分を除去し、蒸気発生装置の缶体へのスケールの付
着を防止出来、水の電気分解で得られた酸性水でイオン
交換樹脂の再生を行うことで、連続的に軟水を蒸気発生
装置に供給することができる。As described above, in the second embodiment, hardness components such as calcium and magnesium ions in the water can be removed by the cation exchange resin to prevent the scale from adhering to the can of the steam generator, and the water electricity can be prevented. By regenerating the ion exchange resin with the acidic water obtained by the decomposition, soft water can be continuously supplied to the steam generator.
【0025】また、電気分解装置壁面を電極とすること
で、装置を薄型化でき、槽電圧の上昇も防止でき、採水
時、停止時等の電極間非通電時には、水電気分解装置に
水を通水しないため、ステンレス電極の腐食を防止し、
陰極材料としてステンレスを用いることが出来、電極コ
ストを下げることができる。Further, by using the electrode on the wall surface of the electrolyzer, the device can be made thin and the rise of the cell voltage can be prevented. Since it does not pass water, it prevents corrosion of the stainless steel electrode,
Stainless steel can be used as the cathode material, and the electrode cost can be reduced.
【0026】また、逆洗を行うことで、懸濁物の蓄積を
防ぎ樹脂層の目詰まりを防止できる。 (実施例3)本
発明の第2の手段の実施例を図3に基づいて説明する。By performing backwashing, it is possible to prevent accumulation of suspensions and prevent clogging of the resin layer. (Embodiment 3) An embodiment of the second means of the present invention will be described with reference to FIG.
【0027】図3において、水は原水供給パイプ1を通
り、加熱ヒーター22によって加熱保温され、陽イオン
交換樹脂12が充填してある軟水化装置13に入る。イ
オン交換時には、排水パイプ15に接続されている排水
弁14は閉じられており、軟水化装置13に入った水は
陽イオン交換樹脂12により、水中のカルシウム、マグ
ネシウム等の陽イオンが、水素イオンと置換され、軟水
化された水がパイプ16を通って、蒸気発生装置17に
供給される。In FIG. 3, water passes through the raw water supply pipe 1, is heated and kept warm by the heater 22, and enters the water softener 13 filled with the cation exchange resin 12. At the time of ion exchange, the drain valve 14 connected to the drain pipe 15 is closed, and the water entering the water softening device 13 is converted into cations such as calcium and magnesium in the water by the cation exchange resin 12. The water that has been replaced with water and has been softened is supplied to the steam generator 17 through the pipe 16.
【0028】イオン交換樹脂再生時には、加熱ヒーター
22による加熱保温を停止し、温度差により陽イオン交
換樹脂の再生を行う。再生時には排水弁14を開け、排
水パイプ15から排水を行い、蒸気発生装置17に水を
供給しないようにする。At the time of regenerating the ion exchange resin, the heat retention by the heater 22 is stopped and the cation exchange resin is regenerated by the temperature difference. At the time of regeneration, the drain valve 14 is opened to drain water from the drain pipe 15 so that the steam generator 17 is not supplied with water.
【0029】以上のように本実施例3では、加熱ヒータ
ーで水温を上昇させ、陽イオン交換樹脂で水中のカルシ
ウム、マグネシウムイオン等の硬度成分を効率良く除去
し、蒸気発生装置の缶体へのスケールの付着を防止出来
る。また、樹脂の再生時には、軟水化装置の加熱を止
め、温度差による樹脂の再生を行うため、水電気分解装
置等が不要となり装置を単純化することができる。As described above, in the third embodiment, the water temperature is raised by the heater and the hardness components such as calcium and magnesium ions in the water are efficiently removed by the cation exchange resin, so that the can body of the steam generator can be treated. Prevents scale from adhering. Further, when the resin is regenerated, the heating of the water softening device is stopped and the resin is regenerated due to the temperature difference. Therefore, a water electrolysis device or the like is not required and the device can be simplified.
【0030】[0030]
【発明の効果】以上の説明から明らかなように、本発明
の第1の手段による蒸気発生装置用の軟水器を用いる
と、陽イオン交換樹脂で水中のカルシウム、マグネシウ
ムイオン等の硬度成分を除去し、蒸気発生装置の缶体へ
のスケールの付着を防止出来、水の電気分解で得られた
酸性水でイオン交換樹脂の再生を行うことで、連続的に
軟水を蒸気発生装置に供給することができる。As is clear from the above description, when the water softener for a steam generator according to the first means of the present invention is used, hardness components such as calcium and magnesium ions in water are removed by a cation exchange resin. However, it is possible to prevent the scale from sticking to the can body of the steam generator, and to regenerate the ion-exchange resin with acidic water obtained by electrolysis of water to continuously supply soft water to the steam generator. You can
【0031】また、電気分解装置壁面を電極とすること
で、装置を薄型化でき、槽電圧の上昇も防止でき、採水
時、停止時等の電極間非通電時には、水電気分解装置に
水を通水しないため、ステンレス電極の腐食を防止し、
陰極材料としてステンレスを用いることが出来、電極コ
ストを下げることができる。By using the walls of the electrolyzer as electrodes, the device can be made thinner, the rise of the cell voltage can be prevented, and when water is not supplied between the electrodes such as when water is drawn or stopped, water is put into the water electrolyzer. Since it does not pass water, it prevents corrosion of the stainless steel electrode,
Stainless steel can be used as the cathode material, and the electrode cost can be reduced.
【0032】第2の手段による蒸気発生用の軟水器を用
いると、加熱ヒーターで水温を上昇させ、陽イオン交換
樹脂で水中のカルシウム、マグネシウムイオン等の硬度
成分を効率良く除去し、蒸気発生装置の缶体へのスケー
ルの付着を防止出来る。また、樹脂の再生時には、軟水
化装置の加熱を止め、温度差による樹脂の再生を行うた
め、水電気分解装置等が不要となり装置を単純化するこ
とができる。When the water softener for steam generation by the second means is used, the water temperature is raised by the heater and the cation exchange resin is used to efficiently remove hardness components such as calcium and magnesium ions in the water. It is possible to prevent the scale from sticking to the can body. Further, when the resin is regenerated, the heating of the water softening device is stopped and the resin is regenerated due to the temperature difference. Therefore, a water electrolysis device or the like is not required and the device can be simplified.
【図1】本発明の実施例1における蒸気発生装置用の軟
水器の構成を示す断面図FIG. 1 is a cross-sectional view showing a configuration of a water softener for a steam generator according to a first embodiment of the present invention.
【図2】本発明の実施例2における蒸気発生装置用の軟
水器の構成を示す断面図FIG. 2 is a cross-sectional view showing the structure of a water softener for a steam generator according to a second embodiment of the present invention.
【図3】本発明の実施例3における蒸気発生装置用の軟
水器の構成を示す断面図FIG. 3 is a cross-sectional view showing the configuration of a water softener for a steam generator according to a third embodiment of the present invention.
【図4】従来の軟水器の構成を示す断面図FIG. 4 is a sectional view showing a configuration of a conventional water softener.
1 原水供給パイプ 2 電気分解装置 5 陽極室 6 陰極室 7 隔壁 12 イオン交換樹脂 13 軟水化装置 17 蒸気発生装置 1 Raw Water Supply Pipe 2 Electrolyzer 5 Anode Chamber 6 Cathode Chamber 7 Partition 12 Ion Exchange Resin 13 Water Softener 17 Steam Generator
Claims (3)
室を隔膜で仕切り陽極室と陰極室を多槽分離形成し、こ
れら極室にそれぞれ電極を配設した電気分解装置と、陽
イオン交換樹脂を充填した軟水化装置と、前記電気分解
装置を介して、または前記電気分解装置を介さずに直接
に前記軟水化装置に通水するように水の供給水路を切り
換える弁とを設け、採水時には前記電気分解装置に水が
流れないよう弁を切り換え、水を軟水化装置上方向から
通水し、陽イオン交換樹脂の再生時には、弁を切り替
え、電気分解装置に水を下方向から通水し、電気分解装
置の両電極間に直流電圧を印加し、陽極室で得られる酸
性水を前記陽イオン交換樹脂を再生する再生水として前
記軟水化装置に供給する蒸気発生装置用の軟水器。1. An electrolyzer in which a cathode chamber is partitioned by a diaphragm and an anode chamber and a cathode chamber are separated into multiple tanks in a water channel for supplying water to a steam generator, and electrodes are respectively arranged in these polar chambers, A water softening device filled with an ion exchange resin, and a valve for switching a water supply channel so as to pass water through the electrolyzer or directly without passing through the electrolyzer , Switch the valve so that water does not flow to the electrolyzer during water collection, pass water from above the water softener, and switch the valve when regenerating the cation exchange resin, and move water downward to the electrolyzer. Water from the electrolyzer, a DC voltage is applied between the electrodes of the electrolyzer, and the acidic water obtained in the anode chamber is supplied to the water softener as regenerated water for regenerating the cation exchange resin. vessel.
キ電極、チタン貴金属焼結電極より選択した貴金属電
極、陰極にステンレス電極を用いた、請求項1記載の蒸
気発生装置用の軟水器。2. The water softener for a steam generator according to claim 1, wherein the electrolyzer uses a titanium noble metal plating electrode for the anode, a noble metal electrode selected from titanium noble metal sintered electrodes, and a stainless steel electrode for the cathode.
オン交換樹脂を充填した軟水化装置を設け、イオン交換
時には軟水化装置を加熱ヒーターで加熱保温し、陽イオ
ン交換樹脂の再生時には、軟水化装置の加熱を止め、温
度差により陽イオン交換樹脂を再生する蒸気発生装置用
の軟水器。3. A water supply for supplying water to a steam generator is provided with a water softening device filled with a cation exchange resin, the water softening device is heated and kept warm by a heater during ion exchange, and when the cation exchange resin is regenerated. , A water softener for a steam generator that stops heating the water softener and regenerates the cation exchange resin due to the temperature difference.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5221072A JPH0768255A (en) | 1993-09-06 | 1993-09-06 | Water softener for steam generator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5221072A JPH0768255A (en) | 1993-09-06 | 1993-09-06 | Water softener for steam generator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0768255A true JPH0768255A (en) | 1995-03-14 |
Family
ID=16761053
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5221072A Pending JPH0768255A (en) | 1993-09-06 | 1993-09-06 | Water softener for steam generator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0768255A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101227856B1 (en) * | 2007-06-13 | 2013-01-31 | 삼성전자주식회사 | Steam Cleaner |
-
1993
- 1993-09-06 JP JP5221072A patent/JPH0768255A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101227856B1 (en) * | 2007-06-13 | 2013-01-31 | 삼성전자주식회사 | Steam Cleaner |
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