JP2518541B2 - Ion-exchange resin regeneration method for water softening equipment - Google Patents

Ion-exchange resin regeneration method for water softening equipment

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Publication number
JP2518541B2
JP2518541B2 JP5326322A JP32632293A JP2518541B2 JP 2518541 B2 JP2518541 B2 JP 2518541B2 JP 5326322 A JP5326322 A JP 5326322A JP 32632293 A JP32632293 A JP 32632293A JP 2518541 B2 JP2518541 B2 JP 2518541B2
Authority
JP
Japan
Prior art keywords
salt
water
exchange resin
ion exchange
ion
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 - Lifetime
Application number
JP5326322A
Other languages
Japanese (ja)
Other versions
JPH07132235A (en
Inventor
明美 川人
俊一 渡
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.)
Miura Co Ltd
Original Assignee
Miura Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Miura Co Ltd filed Critical Miura Co Ltd
Priority to JP5326322A priority Critical patent/JP2518541B2/en
Publication of JPH07132235A publication Critical patent/JPH07132235A/en
Application granted granted Critical
Publication of JP2518541B2 publication Critical patent/JP2518541B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Treatment Of Water By Ion Exchange (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は、硬水軟化装置におい
てイオン交換樹脂の再生方法に係るものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for regenerating an ion exchange resin in a water softening device.

【0002】[0002]

【従来の技術】ボイラー水や食品工業水等に使用される
水道水や井戸水は、見た目にはきれいで透明であるが、
その中には種々の不純物(例えばカルシウム・マグネシ
ウム等の硬度成分)が含まれている。この水道水や井戸
水をそのまま使用するとスケールの付着や腐食の原因と
なる。そこで、これら不純物のうち硬度分を除去するた
めに硬水軟化装置が使用される。この硬水軟化装置で
は、一般に、Na型の強酸性陽イオン交換樹脂を使用
し、原水中の不純物(例えばCa2+,Mg2+など)をN
+ に置換するようになっている。
2. Description of the Related Art Tap water and well water used for boiler water, food industry water, etc. are clean and transparent in appearance,
Among them, various impurities (hardness components such as calcium and magnesium) are included. If this tap water or well water is used as it is, it may cause scale adhesion or corrosion. Therefore, a water softening device is used to remove hardness of these impurities. In this water softening device, generally, a Na-type strongly acidic cation exchange resin is used to remove impurities (such as Ca 2+ and Mg 2+ ) in the raw water from N.
It is designed to be replaced with a + .

【0003】ところで、この硬水軟化装置を長時間使用
すると、イオン交換樹脂が順次Na型からCa型に変換
され、ついには全てのイオン交換樹脂がCa型に変換さ
れる。そうなると、原水中の硬度分を除去しきれなくな
るので、硬水軟化装置のコントロール装置により、適
宜、イオン交換樹脂の再生操作を行う必要がある。硬水
軟化装置では、これらの硬水の軟化とイオン交換樹脂の
再生とが交互に行われ、硬水の軟化が確実に行われるよ
うに構成されている。
By the way, when the water softening device is used for a long time, the ion exchange resin is sequentially converted from Na type to Ca type, and finally all the ion exchange resins are converted to Ca type. If this happens, the hardness component in the raw water cannot be completely removed, so it is necessary to appropriately regenerate the ion exchange resin by the control device of the water softening device. In the water softening device, the softening of the hard water and the regeneration of the ion-exchange resin are alternately performed to surely soften the hard water.

【0004】このイオン交換樹脂の再生には一般に塩水
が使用される。従来、塩水は、専売公社から発売される
粉状の並塩を用いて図1に示すような塩水装置にて生成
していた。図1について説明すると、図中の1は塩水タ
ンクで、この塩水タンク内を水平に仕切るネット2が設
けられてあり、ネットの上に粉状の並塩3が投入されて
いる。水は、塩水タンク下部に設けた塩水バルブ4を通
って、ネット上の湿潤部5の上部ラインまで供給され
る。湿潤部の塩は水に溶解し、所定の濃度の塩水が得ら
れるとともに、前記湿潤部には溶解した体積分だけ上部
の塩が自重で落下し、塩が補給される。
Salt water is generally used to regenerate the ion exchange resin. Conventionally, salt water has been produced by a salt water apparatus as shown in FIG. 1 using powdery normal salt sold by a monopoly company. Referring to FIG. 1, reference numeral 1 in the figure is a salt water tank, which is provided with a net 2 for horizontally partitioning the inside of the salt water tank, and a powdery normal salt 3 is put on the net. Water is supplied to the upper line of the moisturizing section 5 on the net through the salt water valve 4 provided at the lower portion of the salt water tank. The salt in the wet portion is dissolved in water to obtain a salt water having a predetermined concentration, and the salt in the upper portion falls by its own volume by the dissolved volume to the wet portion to replenish the salt.

【0005】この塩水装置の塩水は、硬水軟化装置のコ
ントロール装置(図示せず)の働きにより、塩水バルブ
4から吸引されてイオン交換樹脂の再生に利用される。
再生動作が終了すると、水が塩水バルブを通って塩水タ
ンク内に補給される。
The salt water of this salt water device is sucked from the salt water valve 4 and used for regeneration of the ion exchange resin by the function of a control device (not shown) of the water softening device.
When the regeneration operation is completed, water is replenished into the salt water tank through the salt water valve.

【0006】[0006]

【発明が解決しようとする課題】以上のような作用にお
いて、しばしば並塩が固まり湿潤部上部に塩橋を形成
し、塩が湿潤部に落下、供給されず、所定の塩水濃度が
得られないという問題があった。又、粉状の並塩では水
の浸透性が悪く、水と塩との接触が不十分で飽和溶解度
に達するのに長時間を要していた。又、硬水の軟化時に
イオン交換樹脂表面に付着した鉄分やマンガンは、塩水
のみでは再生時に十分に除去することができず、イオン
交換樹脂の早期劣化の原因となっていた。本発明はこれ
らの問題点を解決すると共に装置の大型化及びコストア
ップを招くこと無くキレート剤の塩水中に於ける濃度を
容易に所定値に調整でき鉄分やマンガン分の除去を効率
良く行えるようにすることを目的とする。
In the above operation, the normal salt often solidifies to form a salt bridge in the upper part of the wet part, and the salt does not drop into the wet part and is not supplied, so that a predetermined salt water concentration cannot be obtained. There was a problem. Further, the powdery normal salt had poor water permeability, and the contact between water and the salt was insufficient, and it took a long time to reach the saturated solubility. Further, iron and manganese adhering to the surface of the ion exchange resin during softening of hard water cannot be sufficiently removed during regeneration with only salt water, which is a cause of early deterioration of the ion exchange resin. The present invention solves these problems and makes it possible to easily adjust the concentration of the chelating agent in the salt water to a predetermined value without increasing the size and cost of the apparatus, and to efficiently remove iron and manganese. The purpose is to

【0007】[0007]

【課題を解決するための手段】この発明は、上記の目的
を達成するためになされたものであって、塩水タンク内
で水に固形塩を溶解させて、塩水を生成し、この塩水を
用いてイオン交換樹脂を再生する硬水軟化装置のイオン
交換樹脂再生方法において、前記固形塩として粉状の塩
にキレート剤を添加し、これをペレット状に成形したも
のを用いたことを特徴とするものである。
The present invention has been made in order to achieve the above-mentioned object, and a solid salt is dissolved in water in a salt water tank to produce salt water, and this salt water is used. In a method of regenerating an ion exchange resin in a water softening device for regenerating an ion exchange resin, a chelating agent is added to a powdery salt as the solid salt, and the chelate agent is molded into pellets. Is.

【0008】[0008]

【作用】上記手段によれば、固形塩間の空隙部が非常に
大きく、且つ固形塩間の接触部の面積が少ないため、塩
橋の発生を確実に防止されるとともに、水の浸透性が良
好で塩の溶解が容易となり、短時間で所定の飽和溶解度
(濃度)の塩水となる。同時に、固形塩に含まれるキレ
ート剤も塩の溶解と共に溶解し、飽和溶解度の塩水とな
ったときにはキレート剤の濃度も所定値に保たれる。
又、塩水中にキレート剤が含まれることになるので、再
生時に、イオン交換樹脂に付着した鉄分やマンガンがキ
レート剤でマスキングされ、容易に溶解除去される。
According to the above means, since the voids between the solid salts are very large and the contact area between the solid salts is small, the formation of salt bridges can be reliably prevented and the water permeability can be improved. Good and easy to dissolve the salt, and the salt water has a predetermined saturated solubility (concentration) in a short time. At the same time, the chelating agent contained in the solid salt also dissolves as the salt dissolves, and when the salt water becomes saturated in solubility, the concentration of the chelating agent is also maintained at a predetermined value.
Further, since the chelating agent is contained in the salt water, the iron and manganese adhering to the ion exchange resin are masked by the chelating agent during the regeneration, and easily dissolved and removed.

【0009】[0009]

【実施例】この発明の再生方法に用いる固形塩は、粉状
の塩に活性剤として作用するキレート剤を添加混合し、
これを例えばプレス等にて、図2に示すような球状
(イ)、円筒状(ロ)、楕円状(ハ)あるいは多角柱状
(ニ)等のペレット状に成形したものである。
EXAMPLE A solid salt used in the regenerating method of the present invention is prepared by adding a chelating agent acting as an activator to a powdery salt and mixing it.
This is molded into a pellet shape such as a spherical shape (a), a cylindrical shape (b), an elliptical shape (c) or a polygonal columnar shape (d) by a press or the like, for example.

【0010】イオン交換樹脂の再生を行うべくこの発明
の固形塩を塩水装置に使用すると、固形塩間の空隙部が
非常に大きく、且つ固形塩間の接触部の面積が少ないた
め、塩橋の発生を確実に防止することができるととも
に、水の浸透性が良好で塩の溶解が容易となり、短時間
で所定の飽和溶解度(濃度)の塩水を得ることができ
る。さらにこの発明によれば、塩水中にキレート剤が含
まれることになるので、再生時に、イオン交換樹脂に付
着した鉄分やマンガンがキレート剤でマスキングされ、
容易に溶解除去される。従って、イオン交換樹脂の再生
が確実となる。
When the solid salt of the present invention is used in a salt water apparatus to regenerate the ion-exchange resin, the voids between the solid salts are very large and the contact area between the solid salts is small. It is possible to reliably prevent the generation of the salt water, the water permeability is good, the salt is easily dissolved, and the salt water having a predetermined saturated solubility (concentration) can be obtained in a short time. Further, according to the present invention, since the chelating agent will be contained in the salt water, at the time of regeneration, iron and manganese attached to the ion exchange resin are masked by the chelating agent,
Easily dissolved and removed. Therefore, the regeneration of the ion exchange resin becomes reliable.

【0011】[0011]

【発明の効果】この発明は、以上のような構成であるの
で、次のような効果を奏する。 塩橋の発生を確実に防止することができ、水の浸透
性が良好で塩の溶解が容易となり、短時間で所定の飽和
溶解度(濃度)の塩水を得ることができるので、硬水軟
化装置の性能の向上を図ることができる。 塩水中に含まれるキレート剤の作用により、イオン
交換樹脂に付着した鉄分やマンガンをマスキングして、
容易に溶解除去することができ、イオン交換樹脂の早期
劣化を防止することができ(イオン交換樹脂のイオン交
換能力を常に高い値に維持することができる)、イオン
交換樹脂の長寿命化を図ることができる。 固形塩が塩とキレート剤を固体状の結合状態に、一
定の割合で含んでいる為に、塩が溶解した分だけキレー
ト剤を水に溶解することができ、キレート剤の濃度を一
定の適正濃度に容易に調整でき、鉄分やマンガン分の除
去を効率よく行える。 軟水装置において、キレート剤の自動投入機構やキ
レート剤の濃度を所定の値に調整する為の自動濃度調整
機構等を必要とせず、軟水装置の大型化及びコストアッ
プを招くこと無く、キレート剤の投入及び濃度調整を行
うことができる。
Since the present invention is constructed as described above, it has the following effects. The generation of salt bridges can be reliably prevented, the water permeability is good, salt dissolution is easy, and salt water with a predetermined saturation solubility (concentration) can be obtained in a short time. The performance can be improved. By the action of the chelating agent contained in salt water, it masks iron and manganese attached to the ion exchange resin,
It can be easily dissolved and removed, premature deterioration of the ion exchange resin can be prevented (the ion exchange capacity of the ion exchange resin can always be maintained at a high value), and the life of the ion exchange resin can be extended. be able to. Since the solid salt contains the salt and the chelating agent in a solid state in a fixed ratio, the chelating agent can be dissolved in water as much as the salt is dissolved, and the concentration of the chelating agent can be adjusted to a certain level. The concentration can be easily adjusted and iron and manganese can be removed efficiently. In the water softener, there is no need for an automatic feeding mechanism of the chelating agent or an automatic concentration adjusting mechanism for adjusting the concentration of the chelating agent to a predetermined value, without increasing the size and cost of the water softening device. Dosing and concentration adjustment can be performed.

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

【図1】図は従来の塩水装置の縦断面図である。FIG. 1 is a vertical sectional view of a conventional salt water device.

【図2】図はこの発明における固形塩のペレット形状例
を示す斜視図である。
FIG. 2 is a perspective view showing an example of a solid salt pellet shape in the present invention.

【符号の説明】[Explanation of symbols]

1…塩水タンク 2…ネット 3…塩 4…塩水バルブ 5…湿潤部 6…塩橋 1 ... salt water tank 2 ... net 3 ... salt 4 ... salt water valve 5 ... wetting part 6 ... salt bridge

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】塩水タンク内で水に固形塩を溶解させて、
塩水を生成し、この塩水を用いてイオン交換樹脂を再生
する硬水軟化装置のイオン交換樹脂再生方法において、
前記固形塩として粉状の塩にキレート剤を添加し、これ
をペレット状に成形したものを用いたことを特徴とする
硬水軟化装置のイオン交換樹脂再生方法。
1. A solid salt is dissolved in water in a salt water tank,
In an ion exchange resin regeneration method of a water softening device that produces salt water and regenerates an ion exchange resin using this salt water,
A method for regenerating an ion-exchange resin in a water softening device, characterized in that a chelating agent is added to a powdery salt as the solid salt, and the chelating agent is molded into pellets.
JP5326322A 1993-11-29 1993-11-29 Ion-exchange resin regeneration method for water softening equipment Expired - Lifetime JP2518541B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5326322A JP2518541B2 (en) 1993-11-29 1993-11-29 Ion-exchange resin regeneration method for water softening equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5326322A JP2518541B2 (en) 1993-11-29 1993-11-29 Ion-exchange resin regeneration method for water softening equipment

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP59008695A Division JPS60150841A (en) 1984-01-20 1984-01-20 Solid salt for hard water softening apparatus

Publications (2)

Publication Number Publication Date
JPH07132235A JPH07132235A (en) 1995-05-23
JP2518541B2 true JP2518541B2 (en) 1996-07-24

Family

ID=18186480

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5326322A Expired - Lifetime JP2518541B2 (en) 1993-11-29 1993-11-29 Ion-exchange resin regeneration method for water softening equipment

Country Status (1)

Country Link
JP (1) JP2518541B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100446444B1 (en) * 2002-03-21 2004-08-30 웅진코웨이주식회사 Regenerating Agents and Methods for Regenerating Ion-Exchange Resin in Soft Water Generator
JP5007831B2 (en) * 2008-05-29 2012-08-22 株式会社ノーリツ Water softening system and hot water supply system
JP5556046B2 (en) * 2009-03-31 2014-07-23 栗田工業株式会社 Treatment liquid for purification of crude ion exchange resin

Also Published As

Publication number Publication date
JPH07132235A (en) 1995-05-23

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