JPH04114789A - Drinking water preparation apparatus - Google Patents

Drinking water preparation apparatus

Info

Publication number
JPH04114789A
JPH04114789A JP23506390A JP23506390A JPH04114789A JP H04114789 A JPH04114789 A JP H04114789A JP 23506390 A JP23506390 A JP 23506390A JP 23506390 A JP23506390 A JP 23506390A JP H04114789 A JPH04114789 A JP H04114789A
Authority
JP
Japan
Prior art keywords
water
hydrogencarbonate
carbonic acid
tower
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
JP23506390A
Other languages
Japanese (ja)
Inventor
Akikazu Yamamoto
明和 山本
Tomonori Yamamoto
友紀 山本
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 JP23506390A priority Critical patent/JPH04114789A/en
Publication of JPH04114789A publication Critical patent/JPH04114789A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To supply hydrogencarbonate-containing water with excellent taste by installing a tower filled with a carbonate-containing substance, a water supplying means to supply water to the tower, a carbonic acid gas supplying means, and a taking out means to take out water containing hydrogencarbonate. CONSTITUTION:When tap water is supplied to a pressure container 20 through a pipeline 14 and brought into contact with a carbonate-containing substance and at the same time carbonic acid gas is supplied from a carbonic acid gas bomb 24 under pressure, hydrogencarbonate salt components are dissolved in water and hydrogencarbonate-concentrated hard water is prepared. This hydrogencarbonate-concentrated water is diluted with tap water to the hardness of the water 300ppm by an ejector 30 and then sent to a carbonic acid removing tower 34. After the dissolved carbonic acid gas is removed by aeration by air from an air filter 38 in the carbonic acid removing tower 34, the water is filtered by a silver carrying activated carbon and a hollow fiber separation membrane in a filter unit 46 and slight malodorous taste is removed. Next, sterilization by a ultraviolet-ray sterilizing unit 58 is carried out. The obtained water containing hydrogencarbonate is mineral water with smooth and good taste.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は飲用水製造装置に係り、詳しくは重炭酸塩ミネ
ラル分の多い美味な飲用水の製造装置に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to an apparatus for producing drinking water, and more particularly to an apparatus for producing delicious drinking water with a high bicarbonate mineral content.

[従来の技術] 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遊離
塩素や懸濁物を除去する浄水器が市販されている。
[Prior Art] In order to provide delicious drinking water, water purifiers are commercially available that use tap water as raw water and use activated carbon or hollow fiber membranes to remove free chlorine and suspended solids from tap water. .

[発明が解決しようとする課題] これらの浄水器は、原水が決まれば水質はほぼ一定水質
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。また、ミネラル
水、アルカリイオン水の製造装置も存在するが、特定の
味の水しか製造できない。
[Problems to be Solved by the Invention] In these water purifiers, once the raw water is determined, the water quality is almost constant, and therefore the taste is only constant. That is, these water purifiers can only remove free chlorine, trace amounts of organic matter, iron, suspended solids, etc. from tap water, but cannot change dissolved ions in raw water. Therefore, changes in taste due to changes in dissolved ions cannot be expected. There are also equipment for producing mineral water and alkaline ionized water, but they can only produce water with a specific taste.

[課題を解決するための手段] 本発明の飲用水製造装置は、炭酸塩含有物質を充填した
塔と、該塔に水を供給する手段と、炭酸ガスを加圧下に
供給する手段と、重炭酸塩硬度成分含有水の取出手段と
を備えてなることを特徴とするものである。
[Means for Solving the Problems] The drinking water production apparatus of the present invention comprises a tower filled with a carbonate-containing substance, a means for supplying water to the tower, a means for supplying carbon dioxide gas under pressure, and a The present invention is characterized by comprising a means for taking out water containing a carbonate hardness component.

[作用] 本発明の飲用水製造装置からは、きわめて「おいしい」
と感じられる重炭酸塩硬度成分含有水が供給される。
[Function] The drinking water production device of the present invention produces extremely delicious water.
Water containing bicarbonate hardness components is supplied.

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看目し、同
様の反応を機減的に行なわせる実験をした。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
ラル分のうち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。
The inventors investigated famous waters around the world and found that most of the water that tastes good comes from underground. We conducted an experiment in which the reaction was performed in a controlled manner. the result,
The important component that makes water taste delicious is the bicarbonate hardness component among minerals, and it has been found that it is important that this is present in appropriate amounts in water.

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。
However, this bicarbonate hardness component exists only in low concentrations in nature. That is, when the concentration of the bicarbonate hardness component increases, the bicarbonate hardness component is in a gas-liquid equilibrium relationship in which it is decomposed into carbonate and carbon dioxide gas as shown in the reaction formula below.

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。
Therefore, high concentrations of bicarbonate hardness components are not present at atmospheric pressure.

Ca (HCO3)2  :l:  CaCO3+H2
0+CO3Mg (HCO3)2  :  MgCO3
+H20+CO3本発明の飲用水製造装置は、この反応
を簡単にかつ速やかに行なわせ、重炭酸塩硬度成分を高
濃度に含んだ水をつくるものである。
Ca(HCO3)2 :l: CaCO3+H2
0+CO3Mg (HCO3)2: MgCO3
+H20+CO3 The drinking water production device of the present invention allows this reaction to occur simply and quickly, and produces water containing a high concentration of bicarbonate hardness components.

重炭酸塩硬度成分を高圧炭酸ガスと水との共存下で溶出
する物質として、炭酸塩硬度成分を含む鉱物が挙げられ
る。これらの鉱物にはいろいろあり、例えば、石灰石、
大埋石等が挙げられる。また、鉱物とは別に、珊瑚骨格
や貝殻のような生物による炭酸塩成分を主体にした物質
が挙げられる。(これらの生物由来炭酸塩含有物質の場
合、鉱物よりも上記条件下で速やかに高濃度の重炭酸塩
硬度成分を溶出させることが可能である。これは、炭酸
塩と水との接触面積の違いによるものと思われる。つま
り、これらの物質は多孔質になっているためと考えられ
る。)これらの炭酸塩含有物質と水とを圧力容器に充填
し、炭酸ガス圧をかけると重炭酸塩硬度成分が溶出する
Examples of substances that elute bicarbonate hardness components in the coexistence of high-pressure carbon dioxide gas and water include minerals containing carbonate hardness components. There are many types of these minerals, such as limestone,
Examples include large buried stones. In addition to minerals, there are also substances mainly composed of carbonate components produced by living organisms such as coral skeletons and shells. (In the case of these biological carbonate-containing substances, it is possible to elute bicarbonate hardness components at higher concentrations more quickly under the above conditions than with minerals. This is because the contact area between carbonate and water is (In other words, it is thought that this is because these substances are porous.) When these carbonate-containing substances and water are filled in a pressure vessel and carbon dioxide pressure is applied, bicarbonate is formed. Hardness components are eluted.

なお、上記手法により溶出した重炭酸塩溶解水には、そ
れぞれの物質特有の異臭味が存在する。
Note that the bicarbonate-dissolved water eluted by the above method has an unusual odor and taste peculiar to each substance.

これを除去するための方法として、吸着剤による吸着が
有効である。有効な吸着剤として活性炭がある。ただ、
溶解水中には多量の遊離炭酸ガスが含まれており、これ
が存在すると大気圧下では効果的な吸着ができない。こ
れの解決策として、重炭酸塩硬度成分を溶出させる条件
下で同時に吸着させるか、また、−旦遊離炭酸ガスを脱
気させてから吸着させる方法が有効である。
Adsorption using an adsorbent is an effective method for removing this. Activated carbon is an effective adsorbent. just,
Dissolved water contains a large amount of free carbon dioxide, and its presence does not allow effective adsorption under atmospheric pressure. As a solution to this problem, it is effective to simultaneously adsorb the bicarbonate hardness component under conditions that elute it, or to first degas free carbon dioxide gas and then adsorb it.

上記手法により得られた重炭酸塩硬度成分は、人の好み
により適度な濃度に希釈する必要がある。希釈方法には
いろいろあるが、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
いて好みの味として飲用することができる。
The bicarbonate hardness component obtained by the above method needs to be diluted to an appropriate concentration depending on the person's preference. There are various dilution methods, such as purified water that is treated with a water purifier that combines activated carbon and hollow fiber membranes, purified water that is further treated with a reverse osmosis membrane, and carbonated water that is made by dissolving carbon dioxide gas in purified water. You can drink it to taste as you like.

[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] Hereinafter, the present invention will be described in more detail based on Examples.

1J1図は本発明の飲用水製造装置の全体フローである
Figure 1J1 shows the overall flow of the drinking water production apparatus of the present invention.

第1図に示す飲用水製造装置の原料となる水道水は配管
10、バルブ12を介して供給される。
Tap water, which is a raw material for the drinking water production apparatus shown in FIG. 1, is supplied through a pipe 10 and a valve 12.

配管10は、配管14.16に分岐している。Line 10 branches into line 14.16.

配管14はミネラル水発生塔1Bに接続されている。ミ
ネラル水発生塔18は、圧力容器20内に石灰石や貝殻
等の炭酸塩含有物質22が充填されており、配管14か
ら水道水が導入されると共に、ガスボンベ24から炭酸
ガスが所定圧力にて導入される。炭酸塩含有物質22に
埋設されるようにして銀担持活性炭が充填された集水器
26が設置されており、重炭酸塩を含む水がこの集水器
26及び配管28で取り出される。なお、本実施例では
活性炭の取替を容易にするため%集水器に充填している
が、圧力容器内に炭酸塩含有物質と同様に充填しても良
い。配管28はエジェクタ30、配管32を介して脱炭
酸塔34に接続されている。なお、エジェクタ30には
前記水道配管10から分岐した配管16が接続されてお
り、配管28からの炭酸塩含有水と水道水とが混合され
て脱炭酸塔34の頂部の散水器36に導入される。
Piping 14 is connected to mineral water generation tower 1B. In the mineral water generation tower 18, a pressure vessel 20 is filled with carbonate-containing substances 22 such as limestone and shells, and tap water is introduced from a pipe 14, and carbon dioxide gas is introduced at a predetermined pressure from a gas cylinder 24. be done. A water collector 26 filled with silver-supported activated carbon is installed so as to be buried in the carbonate-containing material 22, and water containing bicarbonate is taken out through the water collector 26 and piping 28. In this example, the activated carbon is filled in a water collector in order to facilitate its replacement, but it may be filled in the pressure vessel in the same manner as the carbonate-containing substance. The pipe 28 is connected to a decarboxylation tower 34 via an ejector 30 and a pipe 32. A pipe 16 branched from the water pipe 10 is connected to the ejector 30, and the carbonate-containing water from the pipe 28 and tap water are mixed and introduced into a water sprinkler 36 at the top of the decarbonation tower 34. Ru.

なお、エジェクタ30において重炭酸塩含有水と水道水
とを混合するのは、重炭酸塩を過剰に含む水を水道水で
希釈し、炭酸カルシウムの沈・殴殺の析出を防止すると
共に硬度が300ppm程度の飲用に適する硬度にまで
希釈するためである。
The reason for mixing the bicarbonate-containing water and tap water in the ejector 30 is to dilute the water containing excessive bicarbonate with tap water to prevent precipitation of calcium carbonate and to reduce the hardness to 300 ppm. This is to dilute it to a degree of hardness suitable for drinking.

脱炭酸塔34には、ラシヒリング等の充填材が充填され
ておりエアフィルタ38、エアポンプ40及び配管42
を介して空気が吹き込まれることにより、溶存した炭酸
ガスの放出が行なわれる。脱炭酸された水は配管44に
より濾過ユニット46へ送られる。この濾過ユニット4
6は、銀担持活性炭の濾過層46aと、中空糸分離膜の
濾過層46bとを備えている。
The decarboxylation tower 34 is filled with a filler such as a Raschig ring, and is equipped with an air filter 38, an air pump 40, and piping 42.
Dissolved carbon dioxide gas is released by blowing air through it. The decarboxylated water is sent via piping 44 to a filtration unit 46 . This filtration unit 4
6 includes a filtration layer 46a made of silver-supported activated carbon and a filtration layer 46b made of a hollow fiber separation membrane.

なお、脱炭酸塔34には洗浄水の供給配管48が接続さ
れると共に、洗浄排水用の配管5o及び脱炭酸処理時の
オーバーフロー水の排出用配管52が設けられている。
The decarboxylation tower 34 is connected to a washing water supply pipe 48, and is also provided with a washing water pipe 5o and a pipe 52 for discharging overflow water during the decarboxylation process.

さらに、脱炭酸塔34には、水面が低下する際に導入さ
れる空気中の菌を除外するためのエアフィルタ54が接
続されている。
Furthermore, an air filter 54 is connected to the decarboxylation tower 34 for removing bacteria in the air that is introduced when the water level decreases.

前記濾過ユニット46は配管56、紫外線滅菌ユニット
58を経て製品飲用水として取り出される。
The filtration unit 46 passes through a pipe 56 and an ultraviolet sterilization unit 58 and is taken out as product drinking water.

この実施例装置においては、配管14で水道水を圧力容
器20内に供給し、炭酸塩含有物質と接触させると共に
、炭酸ガスボンベ24から炭酸ガスを2〜10気圧の範
囲で供給する。そうすると、重炭酸塩成分が水に溶出し
、濃厚な重炭酸塩硬度の水がつくられる。この濃厚重炭
酸塩水溶液は、エジェクタ30により水道水で硬度30
0ppm程度に希釈された後、脱炭酸塔34に送られる
。そして、該脱炭酸塔34でエアフィルタ38からの空
気により気曝することにより溶存炭酸ガスを除去した後
、濾過ユニット46において銀担持活性炭と中空糸分離
膜で濾過処理し、微量の異臭味を除去する。次いで、紫
外線滅菌ユニット58で滅菌する。
In this embodiment, tap water is supplied into the pressure vessel 20 through a pipe 14 and brought into contact with a carbonate-containing substance, and carbon dioxide gas is supplied from a carbon dioxide gas cylinder 24 at a pressure in the range of 2 to 10 atmospheres. The bicarbonate component then dissolves into the water, creating water with a thick bicarbonate hardness. This concentrated bicarbonate aqueous solution is mixed with tap water using an ejector 30 and has a hardness of 30.
After being diluted to about 0 ppm, it is sent to the decarboxylation tower 34. Then, dissolved carbon dioxide gas is removed by aeration with air from the air filter 38 in the decarboxylation tower 34, and then filtered with silver-supported activated carbon and a hollow fiber separation membrane in the filtration unit 46 to eliminate trace amounts of off-odor taste. Remove. Next, it is sterilized using an ultraviolet sterilization unit 58.

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、まろやかな美味なハイミネラルウォータである。
The water containing the bicarbonate hardness component thus produced is a mellow and delicious high mineral water.

[効果] 以上の通り、本発明の飲用水製造装置によると、きわめ
て美味な重炭酸塩含有水を容易に供給することができる
[Effects] As described above, according to the drinking water production apparatus of the present invention, extremely delicious bicarbonate-containing water can be easily supplied.

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

第1図は本発明の実施例装置の系統図である。 18・・・ミネラル水発生塔、 34・・・脱炭酸塔。 FIG. 1 is a system diagram of an embodiment of the present invention. 18... Mineral water generation tower, 34...Decarboxylation tower.

Claims (1)

【特許請求の範囲】[Claims] 炭酸塩含有物質を充填した塔と、該塔に水を供給する手
段と、炭酸ガスを加圧下に供給する手段と、重炭酸塩硬
度成分含有水の取出手段とを備えてなることを特徴とす
る飲用水製造装置。
It is characterized by comprising a column filled with a carbonate-containing substance, a means for supplying water to the column, a means for supplying carbon dioxide gas under pressure, and a means for taking out water containing a bicarbonate hardness component. Drinking water production equipment.
JP23506390A 1990-09-05 1990-09-05 Drinking water preparation apparatus Pending JPH04114789A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23506390A JPH04114789A (en) 1990-09-05 1990-09-05 Drinking water preparation apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23506390A JPH04114789A (en) 1990-09-05 1990-09-05 Drinking water preparation apparatus

Publications (1)

Publication Number Publication Date
JPH04114789A true JPH04114789A (en) 1992-04-15

Family

ID=16980528

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23506390A Pending JPH04114789A (en) 1990-09-05 1990-09-05 Drinking water preparation apparatus

Country Status (1)

Country Link
JP (1) JPH04114789A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105016549A (en) * 2015-07-28 2015-11-04 江苏奇星流体设备有限公司 Natural mineral water production device and method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105016549A (en) * 2015-07-28 2015-11-04 江苏奇星流体设备有限公司 Natural mineral water production device and method

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