JPH05123697A - Method for preventing scaling in equipment for dissolving inorganic bleaching powder - Google Patents

Method for preventing scaling in equipment for dissolving inorganic bleaching powder

Info

Publication number
JPH05123697A
JPH05123697A JP3040709A JP4070991A JPH05123697A JP H05123697 A JPH05123697 A JP H05123697A JP 3040709 A JP3040709 A JP 3040709A JP 4070991 A JP4070991 A JP 4070991A JP H05123697 A JPH05123697 A JP H05123697A
Authority
JP
Japan
Prior art keywords
bleaching powder
inorganic bleaching
dissolving
polyphosphoric acid
water
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
JP3040709A
Other languages
Japanese (ja)
Inventor
Nobuaki Miyakoshi
暢章 宮腰
Terumoto Fujishima
輝元 藤島
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.)
Nippon Soda Co Ltd
Original Assignee
Nippon Soda 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 Nippon Soda Co Ltd filed Critical Nippon Soda Co Ltd
Priority to JP3040709A priority Critical patent/JPH05123697A/en
Publication of JPH05123697A publication Critical patent/JPH05123697A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To prevent the formation of calcium scale in an equipment for dissolving inorg. bleaching powder attached to an equipment for treating water. CONSTITUTION:A polyphosphoric acid compd. is added to water in which inorg. bleaching powder is dissolved. By this addition, the formation of scale in an equipment for dissolving inorg. bleaching powder is prevented, scale removing work is considerably relieved and the maintenance and control of an equipment for treating water are facilitated.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、無機晒粉溶解設備のス
ケール防止方法に係り、さらに詳しくは、無機晒粉溶解
設備の無機晒粉溶解槽およびそれ以降の配管へのカルシ
ウムスケールの生成、付着を防止する方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a scale prevention method for an inorganic bleaching powder melting facility, and more specifically, for producing a calcium scale in an inorganic bleaching powder melting tank of an inorganic bleaching powder melting facility and a pipe thereafter. A method for preventing adhesion.

【0002】本発明は、無機晒粉を水に溶解した次亜塩
素酸カルシウム水溶液を用いる殺菌消毒設備、晒設備等
の無機晒粉溶解設備に好適に適用される。
The present invention is preferably applied to inorganic bleaching powder dissolving equipment such as sterilizing and disinfecting equipment and bleaching equipment using an aqueous solution of calcium hypochlorite in which inorganic bleaching powder is dissolved in water.

【0003】[0003]

【従来の技術】従来から、水道水、プール水、汚水処理
設備およびし尿処理設備の排水、機械装置の冷却水等の
殺菌消毒、スライムコントロールなどを目的とした水処
理に、塩素または次亜塩素酸塩の水溶液を注入する方法
が採用されており、その一方式として、無機晒粉溶解設
備を水処理設備に付設し、無機晒粉を水に溶解して次亜
塩素酸カルシウム水溶液を製造し、水処理設備に注入す
る方法が知られている。
2. Description of the Related Art Conventionally, chlorine or hypochlorite has been used for water treatment such as tap water, pool water, wastewater treatment facilities and human waste treatment facilities, sterilization of cooling water of machinery and slime control. A method of injecting an aqueous solution of an acid salt is adopted, and as one method, an inorganic bleaching powder dissolving equipment is attached to a water treatment equipment, and the inorganic bleaching powder is dissolved in water to produce an aqueous solution of calcium hypochlorite. , A method of injecting into a water treatment facility is known.

【0004】[0004]

【発明が解決すべき課題】前記無機晒粉溶解設備におい
ては、無機晒粉を水に溶解した次亜塩素酸カルシウム水
溶液中のカルシウム濃度が高濃度となることにより、溶
解槽内部や次亜塩素酸カルシウム水溶液の排出配管内
に、炭酸カルシウムを主成分とするカルシウムスケール
が生成、付着し、次亜塩素酸カルシウム水溶液の流れを
悪化し、甚だしくは配管を閉塞させるなどの障害を生じ
ていた。
In the above-mentioned inorganic bleaching powder dissolution equipment, the high concentration of calcium in the aqueous solution of calcium hypochlorite obtained by dissolving the inorganic bleaching powder in water causes the inside of the dissolution tank and the hypochlorite to become high. In the discharge pipe of the calcium acid aqueous solution, calcium scale containing calcium carbonate as a main component was generated and adhered, which deteriorated the flow of the calcium hypochlorite aqueous solution and seriously caused obstacles such as clogging of the pipe.

【0005】これらの障害対策として、通常塩酸を使用
して無機晒粉溶解槽内部や次亜塩素酸カルシウム水溶液
の排出配管内に生成したカルシウムスケールを定期的に
溶解除去する方法等が採用されているが、カルシウムス
ケール中に残存している次亜塩素酸カルシウムと塩酸と
の反応による毒性の強い塩素ガスの発生や、塩酸による
装置の腐蝕など解決すべき課題を有していた。
As a countermeasure against these obstacles, a method of regularly dissolving and removing the calcium scale generated in the inorganic bleaching powder dissolving tank or in the discharge pipe of the aqueous solution of calcium hypochlorite by using hydrochloric acid has been adopted. However, there are problems to be solved, such as generation of highly toxic chlorine gas due to the reaction between calcium hypochlorite remaining in the calcium scale and hydrochloric acid, and corrosion of the device by hydrochloric acid.

【0006】本発明は、無機晒粉溶解設備の前記の課題
を解決する手段として、カルシウムスケールの無機晒粉
溶解槽内部や次亜塩素酸カルシウム水溶液の排出配管内
への生成、付着を防止する方法を提供することを目的と
する。
The present invention, as a means for solving the above-mentioned problems of the apparatus for dissolving inorganic bleaching powder, prevents the generation and adhesion of calcium scale inside the tank for bleaching inorganic bleaching powder and the discharge pipe of calcium hypochlorite aqueous solution. The purpose is to provide a method.

【0007】[0007]

【課題を解決するための手段】本発明者等は、前記目的
を達成すべく鋭意研究した結果、無機晒粉をポリリン酸
化合物を含有する水で溶解することにより、カルシウム
スケールの生成が抑制され、また生成したカルシウムス
ケールが溶解槽、配管等にほとんど付着しないことを見
出し、本発明を完成した。
Means for Solving the Problems As a result of intensive studies to achieve the above-mentioned object, the present inventors have found that the dissolution of inorganic bleaching powder in water containing a polyphosphate compound suppresses the formation of calcium scale. Further, they have found that the produced calcium scale hardly adheres to the dissolution tank, piping, etc., and have completed the present invention.

【0008】本発明は、無機晒粉製剤を、ポリリン酸化
合物を含有する水を用いて溶解することを特徴とする無
機晒粉溶解設備のスケール防止方法である。
The present invention is a method for preventing scale in an inorganic bleaching powder dissolving facility, which comprises dissolving an inorganic bleaching powder preparation with water containing a polyphosphoric acid compound.

【0009】以下本発明を詳細に説明する。The present invention will be described in detail below.

【0010】本発明において、無機晒粉溶解設備は、内
部に無機晒粉製剤を充填し、水を導入して無機晒粉製剤
を溶解し、次亜塩素酸カルシウム水溶液を排出する無機
晒粉溶解槽を構成の中心とする設備であればよく、前記
溶解槽の詳細構造、溶解プロセス、本設備を付設する水
処理設備等には特に制限はない。
In the present invention, the equipment for dissolving inorganic bleaching powder is filled with an inorganic bleaching powder formulation inside, dissolving the inorganic bleaching powder formulation by introducing water, and discharging the aqueous solution of calcium hypochlorite. Any equipment may be used as long as it has a tank as the center of its constitution, and there are no particular restrictions on the detailed structure of the dissolution tank, the dissolution process, the water treatment equipment attached with this equipment, and the like.

【0011】(無機晒粉製剤)無機晒粉製剤は、次亜塩
素酸カルシウムを主成分とする組成物の錠剤、顆粒剤、
粉剤等任意の剤形の製剤である。通常、高度晒粉(次亜
塩素酸カルシウム・無水塩、2水塩、3水塩)、60%
高度晒粉およびそれらの配合組成物の各種剤形の製剤が
市販されており、その何れをも使用できる。また剤形の
異なる2種以上を併用してもよい。
(Inorganic Bleaching Powder Formulation) An inorganic bleaching powder formulation is a tablet, granule, or tablet of a composition containing calcium hypochlorite as a main component.
It is a preparation of any dosage form such as a powder. Normally, advanced bleaching powder (calcium hypochlorite / anhydrous salt, dihydrate, trihydrate), 60%
Various dosage forms of advanced bleaching powder and their blended compositions are commercially available, and any of them can be used. Further, two or more kinds having different dosage forms may be used in combination.

【0012】(ポリリン酸化合物)ポリリン酸化合物
は、トリポリリン酸、ヘキサメタリン酸、メタリン酸、
ピロリン酸、トリリン酸、トリメタリン酸、テトラメタ
リン酸等の金属塩、好ましくはナトリウム塩またはカリ
ウム塩である。ポリリン酸化合物を含有する水は、前記
ポリリン酸化合物の少なくとも1種を含有するものであ
り、前記ポリリン酸化合物の少なくとも1種を主成分と
する錠剤、顆粒剤、粉剤等任意の剤形のポリリン酸化合
物製剤を水に溶解したポリリン酸化合物水溶液を、無機
晒粉溶解槽の導入水に注入することにより得られる。
(Polyphosphoric acid compound) Polyphosphoric acid compounds include tripolyphosphoric acid, hexametaphosphoric acid, metaphosphoric acid,
Metal salts such as pyrophosphoric acid, triphosphoric acid, trimetaphosphoric acid and tetrametaphosphoric acid, preferably sodium salts or potassium salts. The water containing a polyphosphoric acid compound contains at least one kind of the polyphosphoric acid compound, and polyphosphoric acid having any dosage form such as tablets, granules and powders containing at least one kind of the polyphosphoric acid compound as a main component. It is obtained by injecting an aqueous solution of a polyphosphoric acid compound in which an acid compound preparation is dissolved in water into the water introduced into the tank for dissolving inorganic bleaching powder.

【0013】(ポリリン酸化合物製剤)前記ポリリン酸
化合物製剤として、ポリリン酸化合物の単独系またはポ
リリン酸化合物と溶解速度調整剤、結合剤、滑沢剤等の
賦形剤との混合物系が使用される。前記混合物系の製剤
の賦形剤である溶解速度調整剤として、ステアリン酸カ
ルシウム,ステアリン酸マグネシウム,ステアリン酸ナ
トリウム等のステアリン酸金属塩、ステアリン酸、ケイ
酸微粉末、ケイ酸カルシウム微粉末などが、結合剤とし
て、ポリエチレングリコール,ポリビニルピロリドン等
の水溶性高分子、カルボキシメチルセルロース、アルギ
ン酸ナトリウム、ホウ酸などが、また滑沢剤として、ス
テアリン酸カルシウム、ステアリン酸マグネシウム、タ
ルクなどが使用される。
(Polyphosphoric acid compound preparation) As the polyphosphoric acid compound preparation, a polyphosphoric acid compound alone or a mixture system of a polyphosphoric acid compound and an excipient such as a dissolution rate adjusting agent, a binder and a lubricant is used. It Examples of the dissolution rate adjusting agent that is an excipient of the mixture-based preparation include metal stearates such as calcium stearate, magnesium stearate, and sodium stearate, stearic acid, fine powder of silicic acid, and fine powder of calcium silicate. Water-soluble polymers such as polyethylene glycol and polyvinylpyrrolidone, carboxymethyl cellulose, sodium alginate, boric acid and the like are used as binders, and calcium stearate, magnesium stearate, talc and the like are used as lubricants.

【0014】ポリリン酸化合物製剤の水への溶解方法、
ポリリン酸化合物水溶液の無機晒粉溶解槽の導入水への
注入方法等には特に制限はなく、ポリリン酸化合物製剤
を充填した容器に水を導入して溶解し、得られたポリリ
ン酸化合物水溶液をポンプまたはヘッド差を利用して無
機晒粉溶解槽の導入水配管中に注入する、ごく一般的な
方法を採用することができる。
A method for dissolving a polyphosphate compound preparation in water,
There is no particular limitation on the method of injecting the polyphosphoric acid compound aqueous solution into the introduced water of the inorganic bleaching powder dissolving tank, and the water is introduced into the container filled with the polyphosphoric acid compound formulation to dissolve the resulting polyphosphoric acid compound aqueous solution. It is possible to employ a very general method of injecting into the introduction water pipe of the inorganic bleaching powder dissolving tank by utilizing a pump or a head difference.

【0015】ポリリン酸化合物の無機晒粉溶解槽への導
入量は、無機晒粉溶解槽で溶解する無機晒粉製剤 100重
量部に対して、 0.1〜20重量部、好ましくは 0.5〜10重
量部の範囲である。ポリリン酸化合物の無機晒粉溶解槽
への導入量が過少な場合、スケール防止効果が不十分と
なり、また過大な場合には、無機晒粉溶解槽への導入水
が酸性になり、また排水中のリン濃度が大きくなるので
好ましくない。
The amount of the polyphosphoric acid compound introduced into the inorganic bleaching powder dissolution tank is 0.1 to 20 parts by weight, preferably 0.5 to 10 parts by weight, relative to 100 parts by weight of the inorganic bleaching powder preparation dissolved in the inorganic bleaching powder dissolution tank. Is the range. If the amount of polyphosphoric acid compound introduced into the inorganic bleaching powder dissolution tank is too small, the scale prevention effect will be insufficient, and if it is too large, the water introduced into the inorganic bleaching powder dissolution tank will be acidic and in the wastewater. It is not preferable because the phosphorus concentration of is increased.

【0016】[0016]

【作 用】本発明の無機晒粉溶解設備のスケール防止
方法は、前記したように、無機晒粉製剤を水に溶解し次
亜塩素酸カルシウム水溶液を製造するに際し、無機晒粉
製剤を溶解するために無機晒粉溶解槽に導入する水中
に、ポリリン酸化合物を含有させることを特徴とする。
[Operation] As described above, the scale prevention method of the inorganic bleaching powder dissolution equipment of the present invention dissolves the inorganic bleaching powder preparation when the inorganic bleaching powder preparation is dissolved in water to produce a calcium hypochlorite aqueous solution. Therefore, the polyphosphoric acid compound is contained in the water introduced into the tank for dissolving the inorganic bleaching powder.

【0017】本発明において、ポリリン酸化合物を含有
する水を用いて無機晒粉製剤を溶解することにより、得
られる次亜塩素酸カルシウム水溶液中に存在するカルシ
ウム化合物の微粒子の表面電位が低下し、炭酸カルシウ
ム等のスケール生成の原因となるカルシウム化合物の、
無機晒粉製剤溶解槽およびそれ以降の次亜塩素酸カルシ
ウム水溶液排出配管への付着が防止される。
In the present invention, by dissolving the inorganic bleaching powder formulation with water containing a polyphosphoric acid compound, the surface potential of the calcium compound fine particles present in the obtained calcium hypochlorite aqueous solution is lowered, Of calcium compounds that cause scale formation such as calcium carbonate,
Adhesion to the inorganic bleaching powder solution dissolution tank and the subsequent calcium hypochlorite aqueous solution discharge pipe is prevented.

【0018】[0018]

【実 施 例】本発明を実施例および比較例により、さ
らに詳しく説明する。ただし、本発明の範囲は以下の実
施例により何等制限を受けるものではない。
[Examples] The present invention will be described in more detail with reference to Examples and Comparative Examples. However, the scope of the present invention is not limited by the following examples.

【0019】(1) 試験用無機晒粉溶解設備 実施例で用いた試験用無機晒粉溶解設備(添付図1およ
び図2参照)は、3リットルの塩化ビニル製無機晒粉溶
解槽:1、1リットルの塩化ビニル製ポリリン酸化合物
水溶液槽(図1)またはポリリン酸化合物製剤溶解槽
(図2):2、無機晒粉製剤溶解槽に水を導入するため
の注水管:3、無機晒粉製剤溶解槽から次亜塩素酸カル
シウム水溶液を排出するための流出管:4、前記溶解
槽:1内に製剤を保持するための孔空き仕切り板:5、
ポリリン酸化合物水溶液を注水管内に注入するための連
結管:6からなる。
(1) Test Inorganic Bleaching Powder Dissolving Equipment The test inorganic bleaching powder dissolving equipment used in the examples (see attached FIGS. 1 and 2) is a 3 liter vinyl chloride inorganic bleaching powder dissolving tank: 1 liter polyvinyl chloride aqueous solution tank of polyphosphoric acid compound (Fig. 1) or polyphosphoric acid compound preparation dissolving tank (Fig. 2): 2, water injection pipe for introducing water into inorganic bleaching agent dissolution tank: 3, inorganic bleaching powder Outflow pipe for discharging the calcium hypochlorite aqueous solution from the preparation dissolution tank: 4, a perforated partition plate for holding the preparation in the dissolution tank: 5,
It consists of a connecting pipe: 6 for injecting the polyphosphoric acid compound aqueous solution into the water injection pipe.

【0020】(2) 無機晒粉製剤試料:HC−1〜HC−3 実施例および比較例に下記の無機晒粉製剤を使用した。 HC−1:日曹ハイクロン 20g錠剤 (有効塩素濃度70%以上、日本曹達(株)製) HC−2:日曹ハイクロン 顆粒剤 (有効塩素濃度70%以上、日本曹達(株)製) HC−3:60%高度晒粉 粉 剤 (有効塩素濃度60%以上、日本曹達(株)製)(2) Samples of inorganic bleaching powder formulation: HC-1 to HC-3 The following inorganic bleaching powder formulations were used in Examples and Comparative Examples. HC-1: Nisso Hyklon 20g tablets (effective chlorine concentration 70% or more, manufactured by Nippon Soda Co., Ltd.) HC-2: Nisso Hyklon granules (effective chlorine concentration 70% or more, manufactured by Nippon Soda Co., Ltd.) HC- 3: 60% advanced bleaching powder (effective chlorine concentration of 60% or more, manufactured by Nippon Soda Co., Ltd.)

【0021】 (3) ポリリン酸化合物製剤試料:PP−1〜PP−5 実施例に下記のポリリン酸化合物製剤を使用した。 PP−1:ヘキサメタリン酸ナトリウム 100重量部とアル
ギン酸ナトリウム30重量部とからなる混合物を圧縮成形
した 20g錠剤 PP−2:トリポリリン酸ナトリウム 100重量部に10%ポ
リビニルピロリドン水溶液20重量部を加えて混練し、押
出し造粒、乾燥して得た顆粒を圧縮成形した 20g錠剤 PP−3:ヘキサメタリン酸ナトリウム40重量部、ホウ酸
58重量部およびステアリン酸カルシウム 2重量部からな
る混合物を圧縮成形した 20g錠剤 PP−4:ヘキサメタリン酸ナトリウム 顆粒剤 PP−5:トリポリリン酸ナトリウム 粉 剤
(3) Polyphosphoric acid compound preparation samples: PP-1 to PP-5 The following polyphosphoric acid compound preparations were used in the examples. PP-1: 20 g tablet obtained by compression-molding a mixture consisting of 100 parts by weight of sodium hexametaphosphate and 30 parts by weight of sodium alginate PP-2: 20 parts by weight of 10% polyvinylpyrrolidone aqueous solution was added to 100 parts by weight of sodium tripolyphosphate and kneaded. Granules obtained by extrusion granulation and drying were compression molded 20g Tablet PP-3: 40 parts by weight sodium hexametaphosphate, boric acid
20 g tablet obtained by compression-molding a mixture of 58 parts by weight and 2 parts by weight of calcium stearate PP-4: sodium hexametaphosphate granules PP-5: sodium tripolyphosphate powder

【0022】(4) 溶解試験 (a) 試験法−A 前記試験用無機晒粉溶解設備(図1)のポリリン酸化合
物水溶液槽:2にポリリン酸化合物製剤を水に溶解した
ポリリン酸化合物水溶液を、一方、無機晒粉溶解槽:1
に無機晒粉製剤を充填し、注水管:3に前記調製したポ
リリン酸化合物水溶液を連結管:6を通して注入しなが
ら注水して無機晒粉製剤を溶解し、次亜塩素酸カルシウ
ム水溶液を流出管:4を通して試験片:7上に連続的に
流下させた。 無機晒粉製剤溶解槽:1およびポリリン
酸化合物水溶液槽:2への製剤または水溶液の保持量が
1/2になった時点でそれぞれを初期値まで追加補充し
ながら、無機晒粉製剤を溶解した。また比較として、ポ
リリン酸化合物水溶液の注入を行わない以外には、同一
の条件で無機晒粉製剤を溶解した。6日間の連続試験
後、無機晒粉溶解槽:1ならびに流出管:4内部、およ
び試験片:7上面へのカルシウムスケールの付着状況を
目視観察した。試験条件および目視観察結果を表1に示
す。
(4) Dissolution test (a) Test method-A The polyphosphoric acid compound aqueous solution tank of the test inorganic bleaching powder dissolution equipment (FIG. 1): 2 was filled with a polyphosphoric acid compound aqueous solution prepared by dissolving the polyphosphoric acid compound preparation in water. On the other hand, inorganic bleaching powder dissolution tank: 1
To the inorganic bleaching powder formulation and injecting water into the water injection pipe: 3 while injecting the prepared polyphosphoric acid compound aqueous solution through the connecting pipe: 6 to dissolve the inorganic bleaching powder formulation and to discharge the calcium hypochlorite aqueous solution outflow pipe. : 4 over the test piece: 7 continuously. Inorganic bleaching powder preparation dissolution tank: 1 and polyphosphoric acid compound aqueous solution tank: When the holding amount of the preparation or the aqueous solution to 2 was halved, the inorganic bleaching powder preparation was dissolved while supplementing each to the initial value. .. In addition, as a comparison, the inorganic bleaching powder preparation was dissolved under the same conditions except that the injection of the polyphosphoric acid compound aqueous solution was not performed. After the continuous test for 6 days, the state of adhesion of calcium scale to the inorganic bleaching powder dissolving tank: 1 and the outflow tube: 4, and the upper surface of the test piece: 7 was visually observed. Table 1 shows the test conditions and the results of visual observation.

【0023】(b) 試験法−B 前記試験用無機晒粉溶解設備(図2)のポリリン酸化合
物製剤溶解槽:2にポリリン酸化合物製剤を充填し、水
を導入しながら溶解してポリリン酸化合物水溶液を連続
調製した。一方、無機晒粉溶解槽:1に無機晒粉製剤を
充填し、注水管:3に前記調製したポリリン酸化合物水
溶液を連結管:6を通して注入しながら注水して無機晒
粉製剤を溶解し、次亜塩素酸カルシウム水溶液を流出
管:4を通して試験片:7上に連続的に流下させた。4
8時間の連続試験後、無機晒粉溶解槽:1ならびに流出
管:4内部、および試験片:7上面へのカルシウムスケ
ールの付着状況を目視観察した。試験条件および観察結
果を表1に示す。
(B) Test Method-B The polyphosphoric acid compound preparation dissolution tank of the above-mentioned test inorganic bleaching dissolution equipment (FIG. 2): 2 is filled with the polyphosphoric acid compound preparation and dissolved while introducing water to obtain polyphosphoric acid. A compound aqueous solution was continuously prepared. On the other hand, the inorganic bleaching powder dissolving tank: 1 is filled with the inorganic bleaching powder formulation, and the water injection pipe: 3 is injected while injecting the prepared polyphosphoric acid compound aqueous solution through the connecting pipe: 6 to dissolve the inorganic bleaching powder formulation, An aqueous solution of calcium hypochlorite was continuously made to flow down on the test piece: 7 through the outflow tube: 4. Four
After the continuous test for 8 hours, the state of adhesion of the calcium scale to the inside of the inorganic bleaching powder dissolving tank: 1 and the outflow tube: 4, and the upper surface of the test piece: 7 was visually observed. Table 1 shows the test conditions and observation results.

【0024】[0024]

【表1】 [Table 1]

【0025】表1中、ポリリン酸化合物の供給速度は、
水溶液の供給速度からポリリン酸化合物純分の供給速度
を算出した値を示す。また、スケール付着状況は、下記
を表す。 ○:スケールがほとんど認められない。 △:スケールがわずかに認められるが、容易に剥離す
る。 ×:スケールが大量に固着しており、剥離が困難であ
る。
In Table 1, the feeding rate of the polyphosphate compound is
The value which calculated the supply rate of the polyphosphoric acid compound pure component from the supply rate of an aqueous solution is shown. In addition, the scale adhesion status indicates the following. ◯: Almost no scale is recognized. Δ: Slight peeling is observed, but peeling is easy. X: A large amount of scale is fixed, and peeling is difficult.

【0026】表1に示したように、ポリリン酸化合物を
含有する水で無機晒粉製剤を溶解した場合には、スケー
ルがほとんど認められず、またわずかに認められる場合
(実施例3,6および7参照)でも、生成したスケール
は沈積した状態であり、流水等で容易に除去できた。こ
れに対し、水のみを用いて無機晒粉を溶解した場合(比
較例参照)には、多量のスケールが生成し、かつ容器、
配管、試験片等に固着し、機械的な方法での剥離が困難
であった。
As shown in Table 1, when the inorganic bleaching powder preparation was dissolved in water containing a polyphosphoric acid compound, almost no scale was observed and a small scale was observed (Examples 3, 6 and 7), the generated scale was in a deposited state and could be easily removed with running water or the like. On the other hand, when the inorganic bleaching powder is dissolved using only water (see Comparative Example), a large amount of scale is produced, and the container,
It adhered to pipes, test pieces, etc., and was difficult to peel off by a mechanical method.

【0027】[0027]

【発明の効果】本発明において、前記詳述したように無
機晒粉製剤をポリリン酸化合物を含有する水を用いて溶
解することにより、無機晒粉製剤溶解設備のスケール付
着が防止される。すなわち、従来の無機晒粉製剤溶解設
備の、無機晒粉製剤溶解槽への注水管にポリリン酸化合
物を添加可能な設備を付加するだけで、頻繁に行ってい
たスケール除去作業が不必要となるか、または年1〜2
回程度に軽減される。したがって、水処理設備、晒設備
等、無機晒粉製剤溶解設備の付設される設備の維持管理
が極めて容易となる。
INDUSTRIAL APPLICABILITY In the present invention, as described in detail above, by dissolving an inorganic bleaching powder preparation with water containing a polyphosphoric acid compound, scale adhesion to the inorganic bleaching powder preparation dissolving equipment is prevented. That is, by simply adding a facility capable of adding a polyphosphoric acid compound to the water injection pipe of the conventional inorganic bleaching powder formulation dissolution tank to the inorganic bleaching powder formulation dissolution tank, the frequent scale removal work becomes unnecessary. Or 1-2 years
It is reduced to about once. Therefore, it becomes extremely easy to maintain and manage the facilities such as the water treatment facility and the bleaching facility, which are equipped with the facility for dissolving the inorganic bleached powder formulation.

【0028】本発明は、無機晒粉溶解設備の付設される
諸設備の維持管理を容易とする、無機晒粉溶解設備のス
ケール防止方法を提供するものであり、その産業的、特
に水処理分野における意義は極めて大きい。
The present invention provides a scale prevention method for an inorganic bleaching powder melting facility, which facilitates the maintenance of various facilities attached to the inorganic bleaching powder melting facility, and its industrial, particularly water treatment field. Is extremely significant.

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

【図1】実施例の試験方法−Aで用いた無機晒粉製剤溶
解設備の概念図
FIG. 1 is a conceptual diagram of the inorganic bleaching powder dissolution equipment used in the test method-A of the example.

【図2】実施例の試験方法−Bで用いた無機晒粉製剤溶
解設備の概念図
FIG. 2 is a conceptual diagram of an inorganic bleaching powder dissolution equipment used in the test method-B of the example.

【符号の説明】[Explanation of symbols]

1:無機晒粉製剤溶解槽、2:ポリリン酸化合物水溶液
槽またはポリリン酸化合物製剤溶解槽、3:注水管、
4:次亜塩素酸カルシウム水溶液の流出管、5:無機晒
粉製剤溶解槽内に設けた孔空き仕切り板、6:ポリリン
酸水溶液を注水管内に送り込むための連結管、7:試験
1: Inorganic bleaching powder preparation dissolving tank, 2: Polyphosphoric acid compound aqueous solution tank or polyphosphoric acid compound preparation dissolving tank, 3: Water injection pipe,
4: Outflow pipe of calcium hypochlorite aqueous solution, 5: Perforated partition plate provided in the tank for dissolving inorganic bleaching powder formulation, 6: Connection pipe for sending polyphosphoric acid aqueous solution into the water injection pipe, 7: Test piece

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】無機晒粉製剤を、ポリリン酸化合物含有水
を用いて溶解することを特徴とする無機晒粉溶解設備の
スケール防止方法
1. A method for preventing scale in an inorganic bleaching powder dissolution facility, which comprises dissolving an inorganic bleaching powder formulation with water containing a polyphosphate compound.
【請求項2】請求項1において、ポリリン酸化合物含有
水中のポリリン酸化合物の含有量が、無機晒粉製剤の溶
解量 100重量部に対し、 0.1〜20重量部である無機晒粉
溶解設備のスケール防止方法
2. The inorganic bleaching powder dissolving equipment according to claim 1, wherein the content of the polyphosphoric acid compound in the polyphosphoric acid compound-containing water is 0.1 to 20 parts by weight per 100 parts by weight of the dissolved amount of the inorganic bleaching powder preparation. Scale prevention method
【請求項3】請求項1において、無機晒粉製剤が、錠
剤、顆粒剤および/または粉剤である無機晒粉溶解設備
のスケール防止方法
3. The method for preventing scale of an inorganic bleaching powder dissolving facility according to claim 1, wherein the inorganic bleaching powder formulation is a tablet, a granule and / or a powder.
【請求項4】ポリリン酸化合物製剤を水に溶解し、無機
晒粉製剤溶解槽の導入水に添加する請求項1に記載の無
機晒粉溶解設備のスケール防止方法
4. The method for preventing scale of an inorganic bleaching powder dissolution facility according to claim 1, wherein the polyphosphoric acid compound formulation is dissolved in water and added to the water introduced into the inorganic bleaching powder formulation dissolution tank.
【請求項5】請求項4において、ポリリン酸化合物製剤
が、ポリリン酸化合物を主成分とする錠剤、顆粒剤およ
び/または粉剤である無機晒粉溶解設備のスケール防止
方法
5. The method of preventing scale of an inorganic bleaching-dissolving facility according to claim 4, wherein the polyphosphate compound preparation is a tablet, granule and / or powder containing a polyphosphate compound as a main component.
JP3040709A 1991-02-14 1991-02-14 Method for preventing scaling in equipment for dissolving inorganic bleaching powder Pending JPH05123697A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3040709A JPH05123697A (en) 1991-02-14 1991-02-14 Method for preventing scaling in equipment for dissolving inorganic bleaching powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3040709A JPH05123697A (en) 1991-02-14 1991-02-14 Method for preventing scaling in equipment for dissolving inorganic bleaching powder

Publications (1)

Publication Number Publication Date
JPH05123697A true JPH05123697A (en) 1993-05-21

Family

ID=12588109

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3040709A Pending JPH05123697A (en) 1991-02-14 1991-02-14 Method for preventing scaling in equipment for dissolving inorganic bleaching powder

Country Status (1)

Country Link
JP (1) JPH05123697A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5194223B1 (en) * 2012-03-05 2013-05-08 株式会社セイネン Chemical treatment agent
CN103787512A (en) * 2014-01-26 2014-05-14 南京超旭节能科技有限公司 Front water purification scale preventer

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS508757A (en) * 1973-05-29 1975-01-29
JPS61114720A (en) * 1984-11-10 1986-06-02 Nippon Soda Co Ltd Molded disinfectant dissolving device

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS508757A (en) * 1973-05-29 1975-01-29
JPS61114720A (en) * 1984-11-10 1986-06-02 Nippon Soda Co Ltd Molded disinfectant dissolving device

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5194223B1 (en) * 2012-03-05 2013-05-08 株式会社セイネン Chemical treatment agent
JP2013184983A (en) * 2012-03-05 2013-09-19 Seinen:Kk Chemical treatment agent
CN103787512A (en) * 2014-01-26 2014-05-14 南京超旭节能科技有限公司 Front water purification scale preventer
CN103787512B (en) * 2014-01-26 2015-10-07 南京超旭节能科技有限公司 Preposition water purification scale-proof apparatus

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