JPS6230598A - Neutralization apparatus for supplying water and hot water - Google Patents

Neutralization apparatus for supplying water and hot water

Info

Publication number
JPS6230598A
JPS6230598A JP17001585A JP17001585A JPS6230598A JP S6230598 A JPS6230598 A JP S6230598A JP 17001585 A JP17001585 A JP 17001585A JP 17001585 A JP17001585 A JP 17001585A JP S6230598 A JPS6230598 A JP S6230598A
Authority
JP
Japan
Prior art keywords
water
water supply
hot water
inlet
neutralization
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
JP17001585A
Other languages
Japanese (ja)
Inventor
Kunihiro Tsuruta
邦弘 鶴田
Ikuo Kobayashi
郁夫 小林
Mitsuyo Nomura
野村 充代
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP17001585A priority Critical patent/JPS6230598A/en
Publication of JPS6230598A publication Critical patent/JPS6230598A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To effectively perform corrosion-proof treatment, by forming a zigzag water flow passage in a treatment tank and arranging a granular basic substance in the water flow passage. CONSTITUTION:A granular basic substance 5 comprising a magnesium alloy and a granular basic substance 5' comprising sodium silicate are stored in a treatment tank 1. An upper lid 2 has an inflow port 6 and an outflow port 7 and nets 8a, 8b respectively arranged to said ports 6, 7. A bottom lid 3 has a freely detachable plug 9 and both lids 2, 3 are fixed in a freely detachable manner by using screw 10a-10d and holding rods 11a-11d and formed of a material wherein nickel or chromium plating is applied to brass while the side surface body 4 of the tank is formed of an acrylic resin. By this method, the elution of the metal of piping is suppressed and neutralizing capacity is also enhanced.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は銅や亜鉛メッキ鋼配管を用いた給水給湯設備機
器に用いる防蝕用中和装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a corrosion-preventing neutralization device for use in water and hot water supply equipment using copper or galvanized steel piping.

従来の技術 従来、給水給湯配管として銅配管や亜鉛メッキ鋼管が用
いられているが%PHの低い水質地区でこれらを用いる
と銅イオンや亜鉛イオンの溶出によるトラブルが時折発
生していた。すなわち、銅配管における青水や亜鉛メッ
キ鋼管における赤水である。青水は溶出した銅イオンと
セッケンの脂肪酸とが反応して生成した青色不溶性化合
物(脂肪酸鋼)を原因とするタオルおよび浴槽の青着色
であり、赤水は亜鉛メッキ層消失による鉄さび発生を原
因とする水の赤着色である。
BACKGROUND OF THE INVENTION Conventionally, copper piping and galvanized steel pipes have been used as water supply piping, but when these are used in areas with low %PH water quality, problems sometimes occur due to the elution of copper ions and zinc ions. That is, blue water in copper piping and red water in galvanized steel pipes. Blue water is the blue coloration of towels and bathtubs caused by a blue insoluble compound (fatty acid steel) produced by the reaction between eluted copper ions and fatty acids in soap, and red water is caused by iron rust caused by the disappearance of the galvanized layer. It is the red coloring of water.

発明が解決しようとする問題点 これらの水質障害を防止する防錆剤として、液体又は固
体のポリりん酸塩、液体の珪酸塩がある。
Problems to be Solved by the Invention Liquid or solid polyphosphates and liquid silicates are available as rust preventive agents for preventing these water quality problems.

これら防錆剤は金属表面に保1博皮膜を形成して防蝕を
行う働きであるが、ポリりん酸塩は温水中では分解して
逆に障害を促進する問題点があり、珪酸塩は保護波1漢
を形成するまでに長期間かかり抑制効果がすぐに表われ
ないという問題点があった。
These rust inhibitors work to prevent corrosion by forming a protective film on the metal surface, but polyphosphates have the problem of decomposing in hot water and promoting damage, while silicates are The problem was that it took a long time to form a wave, and the suppressive effect was not immediately apparent.

一方、これらの添加剤を配管内に注入する装置として、
液体品をポンプにて連続注入するものがあるが、補給水
の流量に比例して液体を注入できる制′gfJ機f11
が必要であり、取扱いが繁雑である欠点がある。
On the other hand, as a device for injecting these additives into pipes,
There is a pump that continuously injects liquid products, but there is a control machine that can inject liquid in proportion to the flow rate of make-up water.
The disadvantage is that it requires complicated handling.

問題点を解決するだめの手段 この問題点を解決するために本発明は、流入口および流
出口を有する処理槽内に、ジグザグ状の水流動路を形成
し、この水流動路に下記(I)(IQの群より選択した
多数の粒状塩基性物質を配置するとともに、前記粒状塩
基性物質と前記流入口および前記流出口との間に網を配
置した構成の給水給湯用中和装置とした。
Means for Solving the Problem In order to solve this problem, the present invention forms a zigzag-shaped water flow path in a treatment tank having an inlet and an outlet, and the following (I) is formed in this water flow path. ) (A neutralization device for water supply, in which a large number of granular basic substances selected from the group of IQ are arranged, and a net is arranged between the granular basic substances and the inlet and the outlet. .

CI)  マダイ・シウムもしくはマグネシウム合金0
 珪酸ナトリウムもしくは珪酸カリウム作   用 このfjl成により、弱酸性の水は中性から弱アルカリ
性の水となり配管金属の腐食が抑制される。
CI) Red sea bream, sium or magnesium alloy 0
Sodium silicate or potassium silicate action Due to this fjl formation, weakly acidic water becomes neutral to weakly alkaline water, and corrosion of pipe metals is suppressed.

また、網により粒状塩基性物質が中和装置運搬時に誤っ
て処理槽の外へこぼれ落ちたり、流水時に流出すること
を防止できるとともに、網の整流作用により中和性能が
向上する作用が生じる。
In addition, the net prevents particulate basic substances from accidentally spilling out of the treatment tank during transportation of the neutralization device or from flowing out during running water, and the rectifying action of the net improves neutralization performance.

また、塩基性物質も溶解度が小さいので寿命が長い。In addition, basic substances also have a long life because they have low solubility.

実施例 以下、本発明の実施例を図面を用いて説明する。Example Embodiments of the present invention will be described below with reference to the drawings.

第1図、第2図に示す一実施例において、処理槽1は上
蓋2と底蓋3と側面体4とから成シ、処理槽1の内には
マグネシウム合金(Mg96%、A13%、Zn1%)
からなる粒状塩基性物質5と、珪酸ナトリウム(st○
275%−N a 2025%)からなる粒状塩基性物
質5′が格納されている。上蓋2は流入口6と流出ロア
を有してお9゜それぞれの流路内には網8aと網8bが
配置されている。底蓋3は着脱自在の栓9を有し、上蓋
2とネジ体10a・10b・1oc・1odと保持ta
<11a・11b・11c・11dを用いて着脱自在に
固定している。
In one embodiment shown in FIGS. 1 and 2, the processing tank 1 consists of a top cover 2, a bottom cover 3, and a side body 4, and the inside of the processing tank 1 contains magnesium alloy (96% Mg, 13% A, 1 %)
granular basic substance 5 consisting of sodium silicate (st○
275% - Na 2025%) is stored. The upper lid 2 has an inlet 6 and an outlet lower, and a net 8a and a net 8b are arranged in each of the flow passages. The bottom cover 3 has a removable stopper 9, and the top cover 2, screw bodies 10a, 10b, 1oc, 1od and a retainer ta.
<11a, 11b, 11c, and 11d are used to removably fix it.

上蓋2と底蓋3は黄銅にニッケル・クロムメッキを施し
たものであり、側面体4はアクリル樹脂から成る。網8
a・8bはステンレスを用いており、必要により着脱自
在の構成や配置しない構成も可能である。
The top cover 2 and bottom cover 3 are made of brass plated with nickel and chrome, and the side body 4 is made of acrylic resin. Net 8
Stainless steel is used for a and 8b, and if necessary, a structure in which they can be attached and detached or a structure in which they are not arranged is also possible.

第3図は他の実施例であシ、マグネシウム合金粒5と珪
酸ナトリウム粒5′を流通性のある分離体12にて分離
し、上部にマグネシウム合金粒5、下部に珪酸ナトリウ
ム粒5′を各4配置行している。
FIG. 3 shows another embodiment in which magnesium alloy grains 5 and sodium silicate grains 5' are separated by a flowable separator 12, with magnesium alloy grains 5 in the upper part and sodium silicate grains 5' in the lower part. There are 4 rows each.

なお、容器構成は第1図と同じである。Note that the container configuration is the same as in FIG. 1.

第4図は他の実施例そあり、マグネシウム合金からなる
粒状塩基性物質5を配置している。なお。
FIG. 4 shows another embodiment, in which granular basic material 5 made of a magnesium alloy is arranged. In addition.

容器構成は第1図と同じである。The container configuration is the same as in FIG.

第5図は曲の実施例である。処理槽1は、上蓋2′と底
蓋3′と側面体4とから成り、処理槽1の内には珪酸ナ
トリウムからなる粒状塩基性物質5′が格納されている
。底蓋3′は、流入口6と流出ロアを有しており、それ
ぞれの流路内には網8aと網8bが配置されている。上
蓋2′は着脱自在の栓9を有し、底蓋3′とネジ体10
a・10b・10cm10dおよび保持棒11a・11
b・11cm11dを用いて着脱自在に固定されている
FIG. 5 is an example of a song. The processing tank 1 consists of a top cover 2', a bottom cover 3', and a side body 4, and a granular basic substance 5' made of sodium silicate is stored inside the processing tank 1. The bottom cover 3' has an inlet 6 and an outlet lower, and a net 8a and a net 8b are arranged in each flow path. The top lid 2' has a removable stopper 9, and the bottom lid 3' has a screw body 10.
a, 10b, 10cm10d and holding rods 11a, 11
It is removably fixed using b.11cm11d.

第6図は他の実施例である。流入口6および流81□1
、□。1よ7ヤ、ゎ13□い    :てジグザグ状の
水流動路を形成し、珪酸ナトリウ”からなる粒状塩基性
物質5′を網8′)なか′充填       :□ し1処理槽1内に格納しひる・中和装置は・″    
   1テンレスを用いた箱体14と蓋体15とからな
る。
FIG. 6 shows another embodiment. Inlet 6 and flow 81□1
, □. 1 to 7, ゎ13□: Form a zigzag-shaped water flow path, and fill the net 8' with granular basic substance 5' made of sodium silicate: □ and store it in 1 treatment tank 1 Shihiru/neutralization device is...
It consists of a box body 14 and a lid body 15 made of stainless steel.

箱体14は流入口6と流出ロアを両側面にもち、底部に
は着脱自在な栓9を設けている。一方、蓋体15はしき
り板13との間に隙間16を設け、バイパス流路として
活用できるようにした。なお、箱体14と蓋体15はパ
ツキン17を介してネジ       ;1日で固定し
ている。
The box body 14 has an inlet 6 and an outlet lower on both sides, and a removable stopper 9 is provided at the bottom. On the other hand, a gap 16 is provided between the lid body 15 and the partition plate 13 so that the lid body 15 can be used as a bypass flow path. In addition, the box body 14 and the lid body 15 were fixed with screws through a gasket 17 in one day.

中和のメカニズムは次のように考えられる。The mechanism of neutralization is thought to be as follows.

マグネシウムが水のなかの水素イオンと反応してマグネ
シウムイオンとして溶出するとともに、水酸化イオンが
増大してpHが上昇する。反応式%式% 珪酸ナトリウムは、水のなかの水素イオンと珪酸ナトリ
ウム中のナトリウムイオンがイオン交換してナトリウム
イオンが水中に溶出するととひに。
Magnesium reacts with hydrogen ions in water and is eluted as magnesium ions, and at the same time, hydroxide ions increase and the pH rises. Reaction Formula % Formula % Sodium silicate reacts when hydrogen ions in water and sodium ions in sodium silicate undergo ion exchange and sodium ions are eluted into water.

水酸化イオンが増大してpHが上昇する。珪酸は残〉L
として大部分は残る。反応式は次の通りである。
Hydroxide ions increase and the pH increases. Silicic acid remains〉L
The majority remains. The reaction formula is as follows.

Na25i○3+2H20−+ H2S i O3+2
N a++20H−珪酸カリウムも同様である。
Na25i○3+2H20-+ H2S i O3+2
The same applies to Na++20H-potassium silicate.

本発明の実施例の効果を第7図に示すごとき給湯機器に
て判定した。第7図において、給水給湯用中和装置1゛
は、3001の貯湯能力を持つ貯湯タンク19と水側銅
製熱交換器2oを結ぶ流路(送り側)21に設置してい
る。動作について説明する。集熱板22にて太陽熱を授
受して低温低圧のガスとなった搬送冷媒は圧縮機23に
て高温高圧ガスとなり、冷媒11111 S!交換器に
て放熱して水側銅製熱交換器20の水を温めて湯とする
。ここで搬送冷媒は中温高圧の液となって集熱fi、2
2へ移動し膨張弁24によって減圧し低温低圧液に変わ
る。一方、水側銅製熱交換器20にて温水となった水は
流路(戻り側)24を経由して貯湯タンク19へ移動し
、再び流路(送υ側)21を経由して給水給湯用中和装
置1′へ流入する。この給水給湯用中和装置1′におい
ては流入口6より流入しマグネシウム合金からなる固形
塩基性物質5と接触して流出ロアよシ流出する。なお、
水は循環ポンプ25を経由して水側銅製熱交換器20へ
流入する。また水側銅製熱交換器とは二重壁管式であシ
鉛メッキにて一体化している。
The effects of the embodiments of the present invention were evaluated using a water heater as shown in FIG. In FIG. 7, a water supply neutralization device 1'' is installed in a flow path (sending side) 21 connecting a hot water storage tank 19 having a hot water storage capacity of 3001 and a water side copper heat exchanger 2o. The operation will be explained. The conveyed refrigerant, which has become a low-temperature, low-pressure gas by receiving and receiving solar heat on the heat collecting plate 22, becomes a high-temperature, high-pressure gas in the compressor 23, and the refrigerant 11111 S! The exchanger radiates heat to warm the water in the water-side copper heat exchanger 20 and turn it into hot water. Here, the conveyed refrigerant becomes a medium-temperature, high-pressure liquid and collects heat fi, 2
2, the pressure is reduced by the expansion valve 24, and the liquid turns into a low-temperature, low-pressure liquid. On the other hand, the water heated by the copper heat exchanger 20 on the water side moves to the hot water storage tank 19 via the flow path (return side) 24, and then passes through the flow path (transmission side) 21 again for water supply and hot water supply. flow into the neutralization device 1'. In this water supply neutralization device 1', water flows in through the inlet 6, comes into contact with the solid basic substance 5 made of magnesium alloy, and flows out through the outflow lower. In addition,
Water flows into the water side copper heat exchanger 20 via the circulation pump 25. In addition, the water side copper heat exchanger is a double wall tube type and is integrated with lead plating.

給水給湯用中和装置1は、内容積1000 ccの処理
槽を内部にもつ。
The neutralization device 1 for water supply and hot water supply has a treatment tank with an internal volume of 1000 cc inside.

この給湯機器の貯湯タンクに3004の市水(15°C
)を入れ、5〜717m1nの流量で循環させながら2
4時間運転して53°Cの温水を得て効果を判定した。
3004 city water (15°C) is stored in the hot water storage tank of this hot water supply equipment.
) and circulate it at a flow rate of 5 to 717 m1n.
The effectiveness was evaluated after 4 hours of operation to obtain hot water at 53°C.

く実験1〉 第1図、第3図、第4図、第5図の構成を有する給水給
湯用中和装置に、M、!796%、A13%。
Experiment 1〉 M,! 796%, A13%.

Zn1%)、珪酸ナトリウム(N a 2025%、5
i0275%)、珪酸カリウム(K2025%、Si0
275%)の粒(4〜15xmの大豆状)を格納し、第
7図の給湯機器にてその効果を確かめた。その結果を第
1表に示す。
Zn1%), sodium silicate (N a 2025%, 5
i0275%), potassium silicate (K2025%, Si0
275%) grains (4-15xm soybean-like) were stored, and their effectiveness was confirmed using the water heater shown in Figure 7. The results are shown in Table 1.

実験はpH6,3の市水を用いており、運転初期の水と
24時間後の水の水質分析結果よりその効果特性を表わ
した。中和することにより銅イオンの溶出が抑制されて
いることがわかる。
The experiment used city water with a pH of 6.3, and the effectiveness characteristics were expressed from the results of water quality analysis of the water at the beginning of operation and after 24 hours. It can be seen that the elution of copper ions is suppressed by neutralization.

以下余白 第  1  表 く実験2〉 第4図の構成を有する給水給湯用中和装置に、M 、j
99合金J99a%−A13%−Zn1%)、珪酸ナト
リウム(Na2025%−Si0275%)を格納し、
第7図の給湯機器にて網の有無の効果確認を行った。そ
の結果を第2表に示す。
The following is a blank space: 1 Experiment 2〉 In the water supply neutralization device having the configuration shown in Fig. 4, M, j
99 alloy J99a%-A13%-Zn1%), sodium silicate (Na2025%-Si0275%),
We confirmed the effectiveness of the presence or absence of a screen using the hot water supply equipment shown in Figure 7. The results are shown in Table 2.

網の存在によってpHが上昇し銅イオンも減少してくる
ことがわかる。
It can be seen that the presence of the net increases the pH and decreases copper ions.

第2表 く実験3〉 第6図に示す給水給湯用中和装置に粒状塩基性物質を配
置し、給水の中和処理を行った。この水を第7図の給湯
機器(但し、同図における給水給湯用中和装置1′は搭
載せず)の貯湯タンク19に流入し、24時間運転の沸
きあげ試験を行った。
Experiment 3 shown in Table 2> A granular basic substance was placed in the water supply neutralization device shown in FIG. 6, and the supply water was neutralized. This water was flowed into the hot water storage tank 19 of the hot water supply equipment shown in FIG. 7 (however, the neutralization device 1' for water supply and hot water supply in the same figure was not installed), and a 24-hour boiling test was conducted.

その結果を第3表に示す。The results are shown in Table 3.

給水の中和処理によって嗣イオンの溶出が抑制されてい
ることがわかる。
It can be seen that the elution of Tsugu ions is suppressed by the neutralization treatment of the water supply.

以下余白 第3表 く実験4〉 第7図の給湯機器の流路(戻シ側)24に亜鉛メッキ鋼
配管を取り付けた。pH6,3の試験水を用いると、給
水給湯用中和装置がない場合はZn”0.05 ppm
のM、9合金を用いた同装置を取りつけるとpH80で
Zn2+0.01 ppmと亜鉛イオンの溶出が抑制さ
れてだ。
Experiment 4, shown in Table 3 in the margin below> Galvanized steel piping was attached to the flow path (return side) 24 of the hot water supply equipment shown in FIG. When using test water with a pH of 6.3, Zn"0.05 ppm if there is no neutralization device for water supply.
When the same equipment using the M9 alloy was installed, the elution of zinc ions was suppressed to Zn2+0.01 ppm at pH 80.

く実験5〉 第7図の給湯機器から得られた温水を用いてタオルのセ
ッケンによる青着色実験を行なった。従来の給湯機器(
給水給湯用中和装置なし)がら得られた温水(p H5
,8、Cu ” 1.55 ppm、Mg”     
   ’3ppm)い。、5%。ヤ7ヶ、蔽い浸しえ白
い、オ        ニルを浸したところ15回繰り
返しでタオルが青く        1□ なった。一方、本発明の給水給湯用中和装置を用   
    ■いた給湯機器(マグネシウム粒を格納した第
 図       1の構成)から得られた温水(p 
H7,3、C・2+11゜ 0、O8ppm、 My2+10ppm)に0.5%の
セラ□・ケン液に浸した白いタオルを侵しても30回繰
り返しでもタオルは青くならなかった。これは、木発明
を用いると銅イオンが減少することによる脂肪酸銅(青
色化合物)生成量の減少とマグネシウムイオンが増加す
ることによる脂肪酸マグネシウム(白色化合物)生成量
の増加のためである。
Experiment 5> Using hot water obtained from the water heater shown in Figure 7, an experiment was conducted to color a towel blue with soap. Conventional hot water equipment (
Hot water (pH 5
,8, Cu" 1.55 ppm, Mg"
'3ppm) Yes. , 5%. After 7 months, I soaked the towel in white, and after 15 repetitions, the towel turned blue. On the other hand, using the neutralization device for water supply and hot water supply of the present invention,
■Hot water (p
Even when a white towel soaked in 0.5% Sera□/Ken solution was stained with H7.3, C・2+11°0, O8ppm, My2+10ppm), the towel did not turn blue even after 30 repetitions. This is because when using the wood invention, the production amount of fatty acid copper (blue compound) decreases due to a decrease in copper ions, and the production amount of fatty acid magnesium (white compound) increases due to an increase in magnesium ions.

発明の効果 以上のように本発明によれば、流入口および流出口を有
する処理槽内に、ジグザグ状の水流動路を形成し、該水
流動路内に下記の(I)(II)の群より選択した多数
の粒状塩基性物質を配置するとともに。
Effects of the Invention As described above, according to the present invention, a zigzag water flow path is formed in a treatment tank having an inlet and an outlet, and the following (I) and (II) are formed in the water flow path. Along with placing a large number of particulate basic substances selected from the group.

前記粒状塩基性物質と前記流入口および前記流出口との
間に網を配置しているので、 (I)  マグネシウムもくくはマグネシウム合金(I
I)  !酸ナトリウムもしくは珪酸カリウム次の効果
が得られる。
Since the net is arranged between the particulate basic substance and the inlet and outlet, (I) magnesium or magnesium alloy (I
I)! Sodium acid or potassium silicate The following effects can be obtained.

(1)弱酸性の水が中性から弱アルカリ性になシ、配管
金属の溶出が抑制される。
(1) Slightly acidic water becomes neutral to weakly alkaline, and elution of pipe metals is suppressed.

(2)網により粒状塩基性物質が中和装置運搬時に誤っ
て処理槽の外へこぼれ落ちたシ、流水時に流出すること
を防止できるとともに、網の整流作用により中和性能が
向上する。
(2) The net prevents particulate basic substances from accidentally spilling out of the treatment tank during transport of the neutralization device or from flowing out during running water, and the rectifying action of the net improves neutralization performance.

(3)塩基性物質も溶解度が小さいので寿命が長い。(3) Basic substances also have a long life because they have low solubility.

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

第1図は本発明の一実施例の給水給湯用中和装置の断面
図、第2図は第1図のA−A′線断面図、第3図は同他
の実施例の断面図、第4図は同他の実施例の断面図、第
5図は同他の実施例の断面図、第6図は同他実施例の断
面図、第7図は本発明の効果判定に用いた給湯修器の概
略図である。 1・・・・・処理槽、5・5′・・・・・粒状塩基性物
質、6・・・・−流入口、7・・・・・・流出口、8・
8a・8b・・・・・・網。 代理人の氏名 弁理士 中 尾 敏 男 ほか1名第2
図 S   ffc 第3図 第4図 第5図 第6図
FIG. 1 is a cross-sectional view of a neutralizing device for water supply and hot water according to an embodiment of the present invention, FIG. 2 is a cross-sectional view taken along line A-A' in FIG. 1, and FIG. 3 is a cross-sectional view of another embodiment of the present invention. FIG. 4 is a cross-sectional view of another example, FIG. 5 is a cross-sectional view of another example, FIG. 6 is a cross-sectional view of another example, and FIG. 7 is a cross-sectional view of another example. It is a schematic diagram of a water heater repair device. 1... Processing tank, 5, 5'... Granular basic substance, 6... - inlet, 7... outlet, 8...
8a, 8b...net. Name of agent: Patent attorney Toshio Nakao and 1 other person 2nd
Figure S ffc Figure 3 Figure 4 Figure 5 Figure 6

Claims (1)

【特許請求の範囲】 (1)流入口および流出口を有する処理槽内に、ジグザ
グ状の水流動路を形成し、この水流動路内に下記( I
)(II)の群より選択した多数の粒状塩基性物質を配置
するとともに、前記粒状塩基性物質と前記流入口および
前記流出口との間に網を配置した給水給湯用中和装置。 (I)マグネシウムもしくはマグネシウム合金(II)珪
酸ナトリウムもしくは珪酸カリウム(2)流入口および
流出口が粒状塩基性物質より上部にある特許請求の範囲
第1項記載の給水給湯用中和装置。 (3)処理槽が流入口および流出口を有する上蓋と、底
蓋と、前記上蓋と底蓋との間に位置する側面体とからな
る特許請求の範囲第1項記載の給水給湯用中和装置。 (4)上蓋と底蓋をネジを用いて着脱自在に固定した特
許請求の範囲第1項記載の給水給湯用中和装置。 (5)底蓋に着脱自在な栓を設けた特許請求の範囲第1
項記載の給水給湯用中和装置。
[Claims] (1) A zigzag water flow path is formed in a treatment tank having an inlet and an outlet, and the following (I) is formed in this water flow path.
) A neutralizing device for water and hot water supply, wherein a large number of granular basic substances selected from the group (II) are arranged, and a net is arranged between the granular basic substances and the inlet and the outlet. (I) Magnesium or magnesium alloy (II) Sodium silicate or potassium silicate (2) The neutralization device for water supply and hot water supply according to claim 1, wherein the inlet and outlet are located above the particulate basic material. (3) Neutralization for water and hot water supply according to claim 1, wherein the treatment tank comprises a top cover having an inlet and an outlet, a bottom cover, and a side body located between the top cover and the bottom cover. Device. (4) The neutralizing device for water supply and hot water supply according to claim 1, wherein the top cover and the bottom cover are detachably fixed using screws. (5) Claim 1 in which a removable stopper is provided on the bottom cover.
Neutralization device for water supply and hot water supply as described in section.
JP17001585A 1985-08-01 1985-08-01 Neutralization apparatus for supplying water and hot water Pending JPS6230598A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17001585A JPS6230598A (en) 1985-08-01 1985-08-01 Neutralization apparatus for supplying water and hot water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17001585A JPS6230598A (en) 1985-08-01 1985-08-01 Neutralization apparatus for supplying water and hot water

Publications (1)

Publication Number Publication Date
JPS6230598A true JPS6230598A (en) 1987-02-09

Family

ID=15897013

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17001585A Pending JPS6230598A (en) 1985-08-01 1985-08-01 Neutralization apparatus for supplying water and hot water

Country Status (1)

Country Link
JP (1) JPS6230598A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009131825A (en) * 2007-11-01 2009-06-18 Security:Kk Reduced-water making catalyst and reduced-water making container

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0324279A (en) * 1989-06-20 1991-02-01 Toshiba Corp Production of metal oxide film

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0324279A (en) * 1989-06-20 1991-02-01 Toshiba Corp Production of metal oxide film

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009131825A (en) * 2007-11-01 2009-06-18 Security:Kk Reduced-water making catalyst and reduced-water making container

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