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JPH07178389A - Drinking water production equipment and drinking water generator - Google Patents

Drinking water production equipment and drinking water generator

Info

Publication number
JPH07178389A
JPH07178389A JP32710593A JP32710593A JPH07178389A JP H07178389 A JPH07178389 A JP H07178389A JP 32710593 A JP32710593 A JP 32710593A JP 32710593 A JP32710593 A JP 32710593A JP H07178389 A JPH07178389 A JP H07178389A
Authority
JP
Japan
Prior art keywords
water
carbon dioxide
drinking water
concentration
carbonate
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
JP32710593A
Other languages
Japanese (ja)
Inventor
Akikazu Yamamoto
明和 山本
Yoshimasa Nakano
吉雅 中野
Mitsuru Nozue
満 野末
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.)
Kurita Water Industries Ltd
Original Assignee
Kurita Water Industries 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 Kurita Water Industries Ltd filed Critical Kurita Water Industries Ltd
Priority to JP32710593A priority Critical patent/JPH07178389A/en
Publication of JPH07178389A publication Critical patent/JPH07178389A/en
Pending legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)
  • Water Treatment By Sorption (AREA)

Abstract

(57)【要約】 【目的】 従来の飲用水製造装置の炭酸ガス溶解槽及び
希釈工程を不要とする。飲用水生成器の中空糸分離膜の
細菌汚染を防止する。 【構成】 炭酸塩含有物質充填塔50への給水配管10
に流量計12を設け、炭酸塩含有物質充填塔50への炭
酸ガス供給配管14に弁20を設け、制御装置30によ
り流量計12の測定値に基いて弁20の開閉を制御す
る。飲用水生成器50の中空糸分離膜64に水道水を供
給する洗浄水導入口と排水口を設ける。 【効果】 200ppm以下の低濃度炭酸水であれば、
配管ないし炭酸塩含有物質充填塔内上部の滞留部で十分
に得ることができる。給水量に応じて炭酸ガス量を調整
し、濃度調整した低濃度炭酸水を炭酸塩含有物質充填塔
に供給することにより、所望の重炭酸塩硬度成分濃度で
あって、炭酸ガス濃度の低い水を得ることができる。中
空糸分離膜を水道水で洗浄することにより、細菌による
汚染及び細菌の増殖に起因する臭気発生を有効に防止す
ることができる。
(57) [Summary] [Purpose] The carbon dioxide gas dissolution tank and dilution process of conventional drinking water production equipment are unnecessary. Prevents bacterial contamination of the hollow fiber separation membrane of the drinking water generator. [Constitution] Water supply pipe 10 to the carbonate-containing substance packed tower 50
A flow meter 12 is installed in the column, a valve 20 is installed in the carbon dioxide gas supply pipe 14 to the carbonate-containing substance packed tower 50, and the controller 30 controls the opening and closing of the valve 20 based on the measured value of the flow meter 12. The hollow fiber separation membrane 64 of the drinking water generator 50 is provided with a wash water inlet and a drain for supplying tap water. [Effect] If it is a low-concentration carbonated water of 200 ppm or less,
It can be sufficiently obtained in the pipe or the retention part in the upper part of the carbonate-containing substance packed tower. By adjusting the amount of carbon dioxide gas according to the amount of water supplied and supplying low-concentration carbonated water whose concentration has been adjusted to the carbonate-containing substance packed tower, water with a desired bicarbonate hardness component concentration and low carbon dioxide concentration is obtained. Can be obtained. By washing the hollow fiber separation membrane with tap water, it is possible to effectively prevent odor generation due to bacterial contamination and bacterial growth.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は飲用水製造装置及び飲用
水生成器に係り、詳しくは重炭酸塩ミネラル分の多い美
味な飲用水を製造するための飲用水製造装置及びこの飲
用水製造装置に好適な飲用水生成器に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a drinking water producing apparatus and a drinking water generator, and more particularly to a drinking water producing apparatus for producing delicious drinking water rich in bicarbonate minerals and the drinking water producing apparatus. To a suitable drinking water generator.

【0002】[0002]

【従来の技術】従来、美味な飲用水を提供しようとする
ものとして、水道水を原水として活性炭や中空糸膜を利
用して水道水中の有機物、遊離塩素や懸濁物を除去する
浄水器や浄水設備が市販されている。
2. Description of the Related Art Conventionally, water purifiers for removing organic substances, free chlorine and suspensions in tap water by using activated carbon and hollow fiber membranes with tap water as raw water have been used to provide delicious drinking water. Water purification equipment is commercially available.

【0003】これらの浄水器や浄水設備は、原水が決ま
れば水質はほぼ一定の水質であり、そのため一定の味に
しかならない。即ち、これら浄水器や浄水設備の場合、
水道水中の遊離塩素や微量有機物、鉄分、懸濁物等が除
去できるだけで原水中の溶存イオン類を変化させること
はできない。従って、この溶存イオンの変化による味の
変化は期待できない。
[0003] In these water purifiers and water purification equipment, the quality of water is almost constant once the raw water is determined, and therefore, it has only a certain taste. That is, in the case of these water purifiers and water purification equipment,
It can only remove free chlorine, trace organic substances, iron, suspensions, etc. in tap water, and cannot change dissolved ions in raw water. Therefore, a change in taste due to this change in dissolved ion cannot be expected.

【0004】一方、珊瑚や特定の鉱石を利用して微量の
ミネラル分を溶解させるミネラル水生成装置やアルカリ
イオン水の製造装置も市販されているが、これらによっ
ても特定の味の水しか製造できない。
On the other hand, although a mineral water producing device for dissolving a trace amount of minerals by using coral or a specific ore and a production device for alkaline ionized water are commercially available, they can produce only water having a specific taste. .

【0005】このような問題点を解決するために、本出
願人は、特開平5−212388号公報にて、炭酸塩含
有物質を充填した塔とこの塔に炭酸ガス溶解槽を通じて
低濃度炭酸水を給水する手段とを備える重炭酸塩硬度成
分含有の飲用水製造装置を提案した。
In order to solve such a problem, the applicant of the present invention has disclosed, in JP-A-5-212388, a tower filled with a carbonate-containing substance and a low-concentration carbonated water through a carbon dioxide gas dissolving tank in the tower. A drinking water producing apparatus containing a hardness component of bicarbonate was proposed.

【0006】即ち、本発明者らは、世界各地の銘水を調
査したところ、おいしいと感じられる水が地中から湧出
したものに多いことから、地下における水と地中成分と
の反応に着目し、同様の反応を機械的に行わせる実験を
した。その結果、おいしいと感じられる水の基になる重
要な成分は、ミネラル分の内でも重炭酸塩硬度成分で、
これが水の中に適当量存在することが重要であることが
判明した。
That is, the inventors of the present invention investigated the famous waters in various parts of the world, and found that the most delicious water came from the ground. Therefore, attention was paid to the reaction between underground water and underground components. Then, an experiment was conducted to mechanically carry out the same reaction. As a result, the important ingredient that is the basis of water that feels delicious is the bicarbonate hardness ingredient, even among minerals.
It has been found important that this be present in the water in the proper amount.

【0007】しかし、この重炭酸塩硬度成分は、自然界
では低濃度でしか存在しない。即ち、重炭酸塩硬度成分
は濃度が高くなると、下記反応式の通り炭酸塩と炭酸ガ
スに分解される気液平衡関係にある。従って、大気圧下
では高濃度の重炭酸塩硬度成分は存在しない。
However, this bicarbonate hardness component exists only in a low concentration in nature. That is, when the concentration of the bicarbonate hardness component increases, it has a gas-liquid equilibrium relationship in which it is decomposed into carbonate and carbon dioxide according to the following reaction formula. Therefore, there is no high concentration bicarbonate hardness component under atmospheric pressure.

【0008】 Ca(HCO32 =CaCO3 +H2 O+CO2 Mg(HCO32 =MgCO3 +H2 O+CO2 前記特開平5−212388号公報記載の飲用水製造装
置は、炭酸ガス溶解槽を用い、炭酸ガスの存在する槽に
水を注入することにより、水の炭酸ガスの吸収性を利用
して炭酸水を製造し、これを炭酸塩含有物質を充填した
塔に通水することにより高濃度の重炭酸塩硬度含有水を
得るものである。
Ca (HCO 3 ) 2 = CaCO 3 + H 2 O + CO 2 Mg (HCO 3 ) 2 = MgCO 3 + H 2 O + CO 2 The drinking water production apparatus described in JP-A-5-212388 has a carbon dioxide gas dissolving tank. By injecting water into the tank containing carbon dioxide, carbonated water is produced by utilizing the absorption of carbon dioxide in water, and the carbonated water is passed through the tower filled with the carbonate-containing substance to increase the concentration. It is intended to obtain water having a concentration of bicarbonate hardness.

【0009】なお、特開平5−212388号公報にお
いて、炭酸塩含有物質を充填した塔としては、具体的に
は、圧力容器内に炭酸塩含有物質が充填されると共に、
この炭酸塩含有物質に埋設されるように活性炭が充填さ
れた集水管が設置されており、重炭酸塩硬度含有水は、
この集水管から中空糸分離膜(UF(限外濾過)膜等)
を透過して取り出されるような構成の飲用水生成器とさ
れている。そして、飲用水生成器からの重炭酸塩硬度含
有水は、水道水で希釈された後、ディスペンサ(給水冷
却装置)から飲用水として給水される。
Incidentally, in JP-A-5-212388, as the column packed with the carbonate-containing substance, specifically, the carbonate-containing substance is packed in a pressure vessel, and
A water collection pipe filled with activated carbon is installed so as to be embedded in this carbonate-containing substance, and bicarbonate hardness-containing water is
From this water collection pipe to a hollow fiber separation membrane (UF (ultrafiltration) membrane, etc.)
The drinking water generator is configured so as to be taken out after passing through. The bicarbonate hardness-containing water from the drinking water generator is diluted with tap water and then supplied as drinking water from a dispenser (water cooling device).

【0010】[0010]

【発明が解決しようとする課題】特開平5−21238
8号公報記載の飲用水製造装置においては、炭酸水を製
造するために炭酸ガス溶解槽を必要とし、瞬時に大量の
炭酸水を必要とする場合に、温度低下、給水流量の低下
が生じるという不具合がある。
DISCLOSURE OF THE INVENTION Problems to be Solved by the Invention
In the drinking water production apparatus described in Japanese Patent Publication No. 8, a carbon dioxide gas dissolution tank is required to produce carbonated water, and when a large amount of carbonated water is instantly required, a temperature drop and a water supply flow rate drop occur. There is a defect.

【0011】また、炭酸ガス溶解槽の水温,給水量,炭
酸ガス圧力,給水中の溶存空気量等により得られる炭酸
水濃度の変動等があり、これが重炭酸塩硬度含有水の濃
度変動を引き起こすという不具合もあった。更に、この
重炭酸塩硬度含有水の濃度を調整するには、流量比例設
定器にて重炭酸塩硬度含有水と希釈水(水道水)との混
合水の水質を分析しながら、手動にて希釈割合を調整す
る必要があり、操作が煩雑であるという問題もあった。
Further, there are variations in the concentration of carbonated water obtained depending on the water temperature of the carbon dioxide gas dissolution tank, the amount of water supplied, the pressure of carbon dioxide, the amount of dissolved air in the water, etc., which causes variations in the concentration of water containing bicarbonate hardness There was also a problem. Furthermore, in order to adjust the concentration of this bicarbonate hardness-containing water, manually analyze the water quality of the mixed water of bicarbonate hardness-containing water and dilution water (tap water) with a flow rate proportional setting device. There is also a problem that the operation is complicated because it is necessary to adjust the dilution ratio.

【0012】また、このような問題とは別に、ディスペ
ンサーの給水口から細菌が飲用水生成器に逆流すること
による、飲用水生成器に設けられた中空系分離膜の二次
側(透過水側)膜面及び飲用水生成器からディスペンサ
ーへの配管の細菌汚染の問題もあった。
[0012] In addition to such a problem, the secondary side (permeate side) of the hollow separation membrane provided in the drinking water generator is caused by backflow of bacteria from the water supply port of the dispenser to the drinking water generator. ) There was also a problem of bacterial contamination of the membrane surface and piping from the drinking water generator to the dispenser.

【0013】特に、UF膜は、原水中に存在する有機質
懸濁物や細菌の死骸等を捕捉するものであるため、水の
滞留が続くと嫌気細菌等により硫化水素臭等の臭気が発
生するという問題もある。とりわけ、膜流入水が活性炭
で処理されたものであると、原水である水道水中の塩素
が活性炭で除去され、このため膜面にはより一層雑菌が
繁殖し易くなる。
Particularly, since the UF membrane captures organic suspensions and dead bodies of bacteria existing in raw water, odors such as hydrogen sulfide odor are generated by anaerobic bacteria when the water continues to stay. There is also a problem. In particular, when the membrane inflow water is treated with activated carbon, chlorine in tap water, which is raw water, is removed with activated carbon, so that bacteria are more likely to propagate on the membrane surface.

【0014】本発明は上記従来の問題点を解決し、炭酸
ガス溶解槽を必要とすることなく、連続的又は間欠的に
低濃度炭酸水の供給が行われれば、連続的にその炭酸ガ
ス濃度に対応した重炭酸塩硬度成分含有水を供給するこ
とができると共に、飲用の際の希釈工程を省略できる飲
用水製造装置、及び、内部の中空糸分離膜の細菌汚染を
有効に防止し得る飲用水生成器を提供することを目的と
する。
The present invention solves the above-mentioned conventional problems, and if the low-concentration carbonated water is supplied continuously or intermittently without the need for a carbon dioxide gas dissolving tank, the concentration of the carbon dioxide gas is continuously increased. A water supply device that can supply water containing a hardness component of bicarbonate and that can omit the dilution step when drinking, and a drinking water that can effectively prevent bacterial contamination of the hollow fiber separation membrane inside It is intended to provide a water generator.

【0015】[0015]

【課題を解決するための手段】請求項1の飲用水製造装
置は、炭酸塩含有物質を充填した塔と、該充填塔に水を
供給する流量計を有する配管と、該配管に連絡された炭
酸ガスを供給する弁を有する配管と、前記流量計の測定
結果に基いて前記弁の開閉を制御する制御装置とを備え
てなることを特徴とする。
The drinking water producing apparatus according to claim 1 is a column filled with a carbonate-containing substance, a pipe having a flow meter for supplying water to the column, and a pipe connected to the pipe. It is characterized by comprising a pipe having a valve for supplying carbon dioxide gas, and a control device for controlling opening / closing of the valve based on a measurement result of the flow meter.

【0016】請求項2の飲用水生成器は、内部に活性炭
充填層と該充填層の流出水が導入される中空糸分離膜モ
ジュールとを備えた飲用水生成器において、該中空糸分
離膜モジュールは、洗浄水の導入口及び排水口を有し、
前記導入口には水道水の供給手段が連絡されていること
を特徴とする。
The drinking water generator according to claim 2 is a drinking water generator comprising an activated carbon packed bed and a hollow fiber separation membrane module into which the outflow water of the packed bed is introduced, wherein the hollow fiber separation membrane module is provided. Has an inlet and an outlet for washing water,
A supply means of tap water is connected to the inlet.

【0017】即ち、本発明者らは、前記特開平5−21
2388号公報記載の飲用水製造装置に更に改良を加え
るべく種々の検討を重ねた結果、200ppm程度まで
希釈した低濃度の炭酸水であれば、炭酸塩含有物質充填
塔に到る配管ないし炭酸塩含有物質充填塔内上部の滞留
部において、水への炭酸ガスの溶解反応により十分に得
ることができ、従って、炭酸ガス溶解槽は不要であるこ
と、及び、炭酸ガス濃度を調整して得られた低濃度炭酸
水とすることにより、炭酸塩含有物質充填塔における反
応で、適度な濃度の重炭酸塩硬度成分の溶出が起こり、
また、残留炭酸ガス濃度も低く抑えることができ、この
ため飲用水とするための希釈工程を不要とすることがで
きること、更に、飲用水生成器の中空糸分離膜を水道水
で洗浄することにより、細菌汚染を防止できることを見
出し、本発明を完成させた。
That is, the inventors of the present invention have described the above-mentioned Japanese Patent Laid-Open No. 5-21
As a result of various studies to further improve the drinking water production apparatus described in Japanese Patent No. 2388, as long as it is a low-concentration carbonated water diluted to about 200 ppm, a pipe to reach a carbonate-containing substance packed tower or a carbonate salt It can be obtained sufficiently by the dissolution reaction of carbon dioxide gas in water in the retention part in the upper part of the column containing the substance to be contained, and therefore, the tank for dissolving carbon dioxide gas is not necessary, and it is obtained by adjusting the carbon dioxide concentration. By using low-concentration carbonated water, in the reaction in the carbonate-containing substance packed tower, elution of the bicarbonate hardness component of an appropriate concentration occurs,
In addition, the concentration of residual carbon dioxide can be suppressed to a low level, so that the dilution step for making drinking water is unnecessary, and further, the hollow fiber separation membrane of the drinking water generator is washed with tap water. The inventors have found that bacterial contamination can be prevented, and have completed the present invention.

【0018】[0018]

【作用】請求項1の飲用水製造装置においては、炭酸塩
含有物質充填塔に水及び炭酸ガスを供給する配管ないし
炭酸塩含有物質充填塔内上部の滞留部において炭酸ガス
を水に溶解させる。この炭酸ガス溶解量は、流量計によ
る炭酸ガス供給弁の制御で、炭酸塩含有物質充填塔への
給水量に応じた適当量に調整することができる。このた
め、例えば、200ppm以下の低濃度炭酸水であっ
て、その炭酸ガス濃度を調整した炭酸水とすることによ
り、得られる重炭酸塩硬度成分含有水の重炭酸塩硬度成
分濃度を所望の濃度に調整することができる。
In the drinking water producing apparatus according to the first aspect of the present invention, carbon dioxide is dissolved in water in a pipe for supplying water and carbon dioxide to the carbonate containing substance-filling tower or in a retention portion in an upper part of the carbonate containing substance-filling tower. The amount of dissolved carbon dioxide can be adjusted to an appropriate amount according to the amount of water supplied to the carbonate-containing substance packed tower by controlling the carbon dioxide supply valve with a flow meter. For this reason, for example, the low-concentration carbonated water of 200 ppm or less, and the carbonate hardness component-containing water obtained by adjusting the carbon dioxide gas concentration to obtain the bicarbonate hardness component concentration of the obtained bicarbonate hardness component-containing water has a desired concentration. Can be adjusted to.

【0019】即ち、低濃度炭酸水を化学的合成品以外の
食品添加物である貝殻未焼成カルシウムもしくはサンゴ
未焼成カルシウム等を充填した充填塔に通水すると、以
下の反応式により重炭酸塩硬度成分が溶出してくる。
That is, when low-concentration carbonated water is passed through a packed column filled with uncalcined shell calcium or uncalcined coral, which is a food additive other than a chemically synthesized product, bicarbonate hardness is calculated by the following reaction formula. The components are eluting.

【0020】 CaCO3 +H2 O+CO2 =Ca(HCO32 MgCO3 +H2 O+CO2 =Mg(HCO32 従って、この炭酸中のCO2 濃度を変化させることによ
り、得られる飲用水中の重炭酸塩硬度成分を変化させる
ことができる。
CaCO 3 + H 2 O + CO 2 = Ca (HCO 3 ) 2 MgCO 3 + H 2 O + CO 2 = Mg (HCO 3 ) 2 Therefore, by varying the CO 2 concentration in this carbonic acid, The bicarbonate hardness component can be varied.

【0021】しかも、この重炭酸塩硬度成分含有水は、
200ppm以下といった低濃度炭酸水から得ることに
より、炭酸水と炭酸塩との反応時間に係わらず未反応の
遊離炭酸濃度は200ppm以下となる。このため、得
られる重炭酸塩硬度成分含有水は、希釈を行うことなく
飲用水として給水することができる。
Moreover, the water containing the bicarbonate hardness component is
By obtaining from a low concentration carbonated water of 200 ppm or less, the unreacted free carbonic acid concentration becomes 200 ppm or less regardless of the reaction time of the carbonated water and the carbonate. Therefore, the obtained bicarbonate hardness component-containing water can be supplied as drinking water without dilution.

【0022】また、請求項2の飲用水生成器において
は、中空糸分離膜を水道水で洗浄することにより、細菌
による汚染及び細菌の増殖に起因する臭気発生を有効に
防止することができる。
In the drinking water generator of the second aspect, by washing the hollow fiber separation membrane with tap water, it is possible to effectively prevent odor generation due to contamination with bacteria and bacterial growth.

【0023】なお、本発明において、重炭酸塩硬度成分
を含む鉱物としては、珊瑚骨格や貝殻のような多孔質生
物による炭酸塩成分を主体にした物質が挙げられる。
In the present invention, examples of the mineral containing a bicarbonate hardness component include a substance mainly composed of a carbonate component by a porous organism such as a coral skeleton or a shell.

【0024】また、本発明により得られる重炭酸塩硬度
成分含有水は原水の硬度以下の水とすることはできな
い。このため、利用者の好みに応じて適度な濃度に希釈
しても良い。この場合、希釈方法には特に制限はない
が、希釈水としては、水道水を活性炭と中空糸膜を組み
合わせた浄水器で処理した浄水、浄水を更に逆浸透膜で
処理した純水、浄水に炭酸ガスを溶解させた炭酸水など
を用いることができる。
The bicarbonate hardness component-containing water obtained according to the present invention cannot be water having a hardness equal to or lower than the hardness of raw water. Therefore, it may be diluted to an appropriate concentration according to the preference of the user. In this case, the diluting method is not particularly limited, but as the diluting water, tap water treated with a water purifier combining activated carbon and a hollow fiber membrane, purified water further treated with a reverse osmosis membrane, and purified water can be used. Carbonated water in which carbon dioxide gas is dissolved can be used.

【0025】なお、飲用される際の水中の硬度成分濃度
(ppm as CaCO3 )は300ppm以下程度
である。
The hardness component concentration (ppm as CaCO 3 ) in water at the time of drinking is about 300 ppm or less.

【0026】[0026]

【実施例】以下、実施例をもとにして本発明についてさ
らに詳細に説明する。
EXAMPLES The present invention will be described in more detail below with reference to examples.

【0027】図1は本発明の飲用水製造装置の一実施例
を示す系統図、図2は図1の飲用水生成器の拡大図であ
る。
FIG. 1 is a system diagram showing an embodiment of the drinking water producing apparatus of the present invention, and FIG. 2 is an enlarged view of the drinking water generator of FIG.

【0028】図1に示す飲用水製造装置の原料となる水
道水は、パルス発信式流量計12が設けられた配管10
より、炭酸ガス供給配管14の混合点Aに供給される。
なお、この混合点Aは、配管のチーズでできており特別
な構造を必要としないが、炭酸ガス圧が水道水圧より低
い場合は、エジェクター等の吸引機能を有する配管部品
を必要とする場合もある。
The tap water used as the raw material for the drinking water production apparatus shown in FIG. 1 is a pipe 10 provided with a pulse transmission type flow meter 12.
Thus, the carbon dioxide gas is supplied to the mixing point A of the pipe 14.
The mixing point A is made of cheese for piping and does not require a special structure. However, when the carbon dioxide gas pressure is lower than the tap water pressure, a pipe part having a suction function such as an ejector may be required. is there.

【0029】一方、食品用炭酸ガスボンベ16からの炭
酸ガスが、減圧弁18にて数kg/cm2 (例えば、8
kg/cm2 )に減圧され、電磁弁20を有する配管1
4より供給され、混合点Aにおいて、水道水と混合され
る。なお、22,24は逆止弁である。
On the other hand, carbon dioxide gas from the carbon dioxide gas cylinder 16 for food is fed to the pressure reducing valve 18 at several kg / cm 2 (for example, 8
Pipe 1 that has a solenoid valve 20 and is depressurized to kg / cm 2 ).
4 and is mixed with tap water at the mixing point A. In addition, 22 and 24 are check valves.

【0030】混合点Aにおいて、炭酸ガスと水道水とが
混合されて得られた炭酸水は配管14により飲用水生成
器(ミネラル水発生塔)50の導入口50Aに供給され
る。
At the mixing point A, the carbonated water obtained by mixing the carbon dioxide gas and the tap water is supplied to the inlet 50A of the drinking water generator (mineral water generation tower) 50 through the pipe 14.

【0031】図2に示す如く、ミネラル水発生塔50
は、圧力容器52内に、炭酸ガスと水とが混合溶解する
ように旋回流を生み出す構造の流入部54と、空間滞留
部56及び珊瑚等の炭酸塩含有物質58と銀担持活性炭
60が、順次積層充填されており、この炭酸塩含有物質
58の層で炭酸水は炭酸塩含有物質58と反応して重炭
酸塩硬度成分と未反応の遊離炭酸の混合水が製造され
る。この混合水は、次いで、活性炭60で残留塩素や有
機物等が除去され、更に、集水管62の底部から集水さ
れる。集水された水(ミネラル水)は、中空糸膜モジュ
ール64のUF膜64Aにて懸濁物が除去された後、流
出部64B及び配管66を経て系外に取り出される。
As shown in FIG. 2, the mineral water generation tower 50
In the pressure vessel 52, an inflow part 54 having a structure that creates a swirling flow so that carbon dioxide gas and water are mixed and dissolved, a space retention part 56, a carbonate-containing substance 58 such as coral, and silver-supporting activated carbon 60, The layers of the carbonate-containing substance 58 are sequentially stacked and filled, and the carbonated water reacts with the carbonate-containing substance 58 to produce mixed water of the hardness component of bicarbonate and unreacted free carbonic acid. The mixed water is then subjected to activated carbon 60 to remove residual chlorine, organic matter and the like, and is further collected from the bottom of the water collecting pipe 62. The collected water (mineral water) is taken out of the system through the outflow portion 64B and the pipe 66 after the suspended matter is removed by the UF membrane 64A of the hollow fiber membrane module 64.

【0032】本実施例の飲用水製造装置においては、コ
ントローラ30に流量計12の測定値が入力され、この
測定値に基いて電磁弁20の開閉を制御することによ
り、所望の低濃度炭酸水をミネラル水発生器50に供給
する。このため、ミネラル水発生器からは所望の重炭酸
塩硬度成分濃度であって、炭酸ガス濃度が更に低い水を
得ることができることから、得られる重炭酸塩硬度成分
水は特に希釈することなく、直接飲用に供給することが
できる。
In the drinking water producing apparatus of this embodiment, the measured value of the flow meter 12 is input to the controller 30, and the opening / closing of the solenoid valve 20 is controlled based on this measured value to obtain a desired low concentration carbonated water. Is supplied to the mineral water generator 50. Therefore, from the mineral water generator, it is possible to obtain water having a desired bicarbonate hardness component concentration and a lower carbon dioxide concentration, so that the obtained bicarbonate hardness component water is not particularly diluted, Can be supplied directly for drinking.

【0033】このようにして製造された重炭酸塩硬度成
分を含有する水は、まろやかで美味なミネラルウォータ
ーである。
The water containing the bicarbonate hardness component produced in this manner is mellow and delicious mineral water.

【0034】ところで、原水の水道水中の残留塩素は、
ミネラル水発生器50の活性炭60にて除去されるた
め、集水管62で集水された水には、残留塩素は存在し
ない。従って、長期間放置されると雑菌類が繁殖し、こ
れは、中空糸分離膜64の一次側にて除去される。この
中空糸膜モジュール64のUF膜64Aで除去された雑
菌類や有機性懸濁物が嫌気状態になると、前述の如く、
臭気を発生するようになる。また、中空糸膜の二次側
は、配管66からの雑菌の逆流で配管も含めて雑菌汚染
が起きる。
By the way, residual chlorine in tap water of raw water is
Since it is removed by the activated carbon 60 of the mineral water generator 50, residual water does not exist in the water collected by the water collecting pipe 62. Therefore, if left unattended for a long period of time, various fungi propagate and are removed on the primary side of the hollow fiber separation membrane 64. When the bacteria and the organic suspension removed by the UF membrane 64A of the hollow fiber membrane module 64 become anaerobic, as described above,
It starts to emit odor. Also, on the secondary side of the hollow fiber membrane, contamination of various bacteria including the piping occurs due to the reverse flow of various bacteria from the piping 66.

【0035】このため、本実施例においては、ミネラル
水発生器50の中空糸膜モジュール64は、水道水で洗
浄可能に構成されている。
Therefore, in this embodiment, the hollow fiber membrane module 64 of the mineral water generator 50 is constructed so that it can be washed with tap water.

【0036】即ち、水道水の供給配管10には洗浄用電
磁弁32を有する洗浄配管34が分岐しており、この配
管34は中空糸膜モジュール64の洗浄水道入口64B
に接続されている。
That is, in the tap water supply pipe 10, a washing pipe 34 having a solenoid valve 32 for washing is branched, and this pipe 34 is a washing water inlet 64B of the hollow fiber membrane module 64.
It is connected to the.

【0037】従って、洗浄用電磁弁32を開けて、塩素
を含有する水道水を洗浄水導入口64Cより膜モジュー
ル64内に導入し、UF膜64A、流出部64B、流出
配管66を経て取り出すことにより、水道水中の残留塩
素が検出される程度まで洗浄する。そして、その後、電
磁弁32を閉じて次回使用するまでこの状態を保持する
と、系内の雑菌は殺菌され、無菌状態の水をいつでも取
り出せるようになる。
Therefore, the electromagnetic valve 32 for cleaning is opened, tap water containing chlorine is introduced into the membrane module 64 through the cleaning water inlet 64C, and taken out through the UF membrane 64A, the outflow portion 64B, and the outflow pipe 66. Clean the tap water to the extent that residual chlorine can be detected. Then, after that, if the electromagnetic valve 32 is closed and this state is maintained until the next use, germs in the system are sterilized, and aseptic water can be taken out at any time.

【0038】また、配管66に手動弁70Aを有する塩
素水導入管70Aを設けると共に、配管34に手動弁7
2Aを有する排出管72を設け、塩素洗浄用手動弁70
A及び72Aを開として、加圧状態で200ppm程度
の塩素水を配管70より注入して、配管72より取り出
すことにより、膜モジュール64の逆洗と殺菌を行なっ
て長期の使用が可能となる。
A chlorine water introducing pipe 70A having a manual valve 70A is provided in the pipe 66, and the manual valve 7 is provided in the pipe 34.
A discharge valve 72 having 2A is provided, and a chlorine cleaning manual valve 70 is provided.
By opening A and 72A and injecting about 200 ppm of chlorine water in a pressurized state from the pipe 70 and taking out from the pipe 72, backwashing and sterilization of the membrane module 64 can be performed, and long-term use becomes possible.

【0039】[0039]

【発明の効果】以上詳述した通り、請求項1の飲用水製
造装置によれば、炭酸ガス溶解槽及び飲用水とするため
の希釈工程を省略して、任意の重炭酸塩硬度成分濃度を
有する、極めて美味な重炭酸塩硬度成分含有水を制御装
置のパネル操作のみで容易に供給することができる。請
求項1の飲用水製造装置によれば、装置の小型、コンパ
クト化及び操作の簡易化が図れ、工業的に極めて有利で
ある。
As described in detail above, according to the drinking water production apparatus of claim 1, the concentration step of any bicarbonate hardness component can be eliminated by omitting the carbon dioxide gas dissolving tank and the dilution step for making drinking water. It is possible to easily supply the extremely delicious water containing the bicarbonate hardness component that is possessed only by operating the panel of the control device. According to the drinking water production apparatus of the first aspect, the apparatus can be made small and compact and the operation can be simplified, which is extremely advantageous industrially.

【0040】請求項2の飲用水生成器によれば、装置構
成が簡易な飲用水生成器であって、雑菌による汚染、臭
気の発生を有効に防止することができる飲用水生成器が
提供される。
According to the drinking water generator of the second aspect, a drinking water generator having a simple device configuration is provided, which is capable of effectively preventing contamination and odor generation due to various bacteria. It

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

【図1】本発明の飲用水製造装置の一実施例を示す系統
図である。
FIG. 1 is a system diagram showing an embodiment of a drinking water production apparatus of the present invention.

【図2】図1に用いられている飲用水生成器の拡大図で
ある。
2 is an enlarged view of the drinking water generator used in FIG. 1. FIG.

【符号の説明】[Explanation of symbols]

12 流量計 16 炭酸ガスボンベ 20,32 電磁弁 30 コントローラ 50 ミネラル水発生塔 58 重炭酸塩含有物質 60 活性炭 62 集水管 64 中空糸膜モジュール 64A UF膜 12 Flowmeter 16 Carbon dioxide cylinder 20, 32 Solenoid valve 30 Controller 50 Mineral water generation tower 58 Bicarbonate-containing substance 60 Activated carbon 62 Water collecting pipe 64 Hollow fiber membrane module 64A UF membrane

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C02F 1/68 540 A D ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Office reference number FI technical display location C02F 1/68 540 AD

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 炭酸塩含有物質を充填した塔と、該充填
塔に水を供給する流量計を有する配管と、該配管に連絡
された炭酸ガスを供給する弁を有する配管と、前記流量
計の測定結果に基いて前記弁の開閉を制御する制御装置
とを備えてなる飲用水製造装置。
1. A tower filled with a carbonate-containing substance, a pipe having a flow meter for supplying water to the packed tower, a pipe having a valve for supplying carbon dioxide gas connected to the pipe, and the flow meter. And a controller for controlling the opening and closing of the valve based on the measurement result of 1.
【請求項2】 内部に活性炭充填層と該充填層の流出水
が導入される中空糸分離膜モジュールとを備えた飲用水
生成器において、該中空糸分離膜モジュールは、洗浄水
の導入口及び排水口を有し、前記導入口には水道水の供
給手段が連絡されていることを特徴とする飲用水生成
器。
2. A drinking water generator comprising a packed bed of activated carbon and a hollow fiber separation membrane module into which the outflow water of the packed bed is introduced, wherein the hollow fiber separation membrane module comprises a washing water inlet and A drinking water generator having a drainage port, and tap water supply means is connected to the introduction port.
JP32710593A 1993-12-24 1993-12-24 Drinking water production equipment and drinking water generator Pending JPH07178389A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP32710593A JPH07178389A (en) 1993-12-24 1993-12-24 Drinking water production equipment and drinking water generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP32710593A JPH07178389A (en) 1993-12-24 1993-12-24 Drinking water production equipment and drinking water generator

Publications (1)

Publication Number Publication Date
JPH07178389A true JPH07178389A (en) 1995-07-18

Family

ID=18195351

Family Applications (1)

Application Number Title Priority Date Filing Date
JP32710593A Pending JPH07178389A (en) 1993-12-24 1993-12-24 Drinking water production equipment and drinking water generator

Country Status (1)

Country Link
JP (1) JPH07178389A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20020012941A (en) * 2000-08-09 2002-02-20 이태수 A water-supply apparatus improved the oxygen content of water
EP2248768A1 (en) 2009-05-05 2010-11-10 Sociedad Anónima Minera Catalano-Aragonesa Process for producing drinking water by coagulation -flocculation using a mineral product containing clays and mineral carbonates
JP2014237103A (en) * 2013-06-10 2014-12-18 タカラベルモント株式会社 Soda water discharge device
KR101655433B1 (en) * 2016-03-17 2016-09-07 앵스트롬스 주식회사 sparkling beverages manufacturing system using gas-liquid membrane contactor and it's method

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20020012941A (en) * 2000-08-09 2002-02-20 이태수 A water-supply apparatus improved the oxygen content of water
EP2248768A1 (en) 2009-05-05 2010-11-10 Sociedad Anónima Minera Catalano-Aragonesa Process for producing drinking water by coagulation -flocculation using a mineral product containing clays and mineral carbonates
JP2014237103A (en) * 2013-06-10 2014-12-18 タカラベルモント株式会社 Soda water discharge device
KR101655433B1 (en) * 2016-03-17 2016-09-07 앵스트롬스 주식회사 sparkling beverages manufacturing system using gas-liquid membrane contactor and it's method

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