JPS59213412A - Apparatus for removing carbon dioxide in water - Google Patents

Apparatus for removing carbon dioxide in water

Info

Publication number
JPS59213412A
JPS59213412A JP8638883A JP8638883A JPS59213412A JP S59213412 A JPS59213412 A JP S59213412A JP 8638883 A JP8638883 A JP 8638883A JP 8638883 A JP8638883 A JP 8638883A JP S59213412 A JPS59213412 A JP S59213412A
Authority
JP
Japan
Prior art keywords
water
air
chamber
carbon dioxide
gas
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.)
Granted
Application number
JP8638883A
Other languages
Japanese (ja)
Other versions
JPH0331481B2 (en
Inventor
Tatsuo Okazaki
龍夫 岡崎
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP8638883A priority Critical patent/JPS59213412A/en
Publication of JPS59213412A publication Critical patent/JPS59213412A/en
Publication of JPH0331481B2 publication Critical patent/JPH0331481B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Degasification And Air Bubble Elimination (AREA)
  • Physical Water Treatments (AREA)

Abstract

PURPOSE:To remove efficiently gaseous carbon dioxide in a short time by dispersing compressed air, which is atomized through a porous partition wall, into water to bring the air into close contact with water. CONSTITUTION:By driving a blower 5 and opening a valve 10, the compressed air is introduced into a bubbling chamber 2, and atomized through a partition wall 4 to bubble the water flowing down to the surface of the chamber. The bubbles are pressed and moved in the bubbling chamber 2 in the flowing direction of the air current to the side of an overflow wall 11. The bubbles, overflowed from the overflow wall, are separated into the air contg. gaseous carbon dioxide and the water in a gas-liquid separation chamber 12. The sending pressure of the air to be supplied is set strong enough, and the amt. of air is set to be enormous as compared with the water supply to a water spouting tube 8. A port is provided to the ceiling of the gas-liquid separation chamber 12 to discharge the separated air to the outside. The water after treatment is discharged from a discharge port 14 to a water storage tank 13.

Description

【発明の詳細な説明】 本発明は、主として、上水を電気分解、電気滲透作用に
より、飲用に供する適性の水に変換する場合などの目的
において、例えば前処理として実行される水の炭酸除去
装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention is primarily concerned with the removal of carbonation from water, which is carried out as a pre-treatment, for example, for the purpose of converting tap water into drinkable water by electrolysis or electroosmosis. It is related to the device.

一般に、地下水、河川の水には遊離炭酸という炭酸が多
く含壕れている。この炭酸の起源は、はとんど、雨水に
溶けている炭酸ガスであるが、また、土壌中で生物の呼
吸作用、バクテリアの分解作用で発生する炭酸ガスでも
ある。そして炭酸ガスの溶解と解離の関係は、 ”02  + H20二H,C05(炭酸)H,CO3
: H+ + Hco;− HCo、  : H+ −1−COこ である。
Generally, groundwater and river water contain a large amount of carbonic acid called free carbonate. The origin of this carbonic acid is usually carbon dioxide gas dissolved in rainwater, but it is also carbon dioxide gas generated in the soil by the respiration of living organisms and the decomposition of bacteria. And the relationship between dissolution and dissociation of carbon dioxide gas is ``02 + H202H, C05 (carbonic acid) H, CO3
: H+ + Hco; - HCo, : H+ -1-CO.

したがって、電解作用によって、陰極室側の水に水酸基
を多量に発生しても、H+とHCO,−あるいはH+と
COvに分かれた状態で、 OH−+ H+→H,0 となシ、水酸基を消耗してしまうので、電解効率が著し
く低下することになる。
Therefore, even if a large amount of hydroxyl groups are generated in the water on the cathode chamber side by electrolytic action, the hydroxyl groups will be separated into H+ and HCO,- or H+ and COv, and the hydroxyl groups will become OH-+ H+→H,0. Since it is consumed, the electrolytic efficiency will be significantly reduced.

また、電解作用を与えた時、陰極室側には有用々カルシ
ウムイオンなどが集まるが、上記の炭酸は、 H2CO,−1−Ca −+ H,−1−CaC0゜の
反応を示し、炭酸カルシウムとなって、沈澱し、もしく
は、電極表面にスケールとして付着し、通電率を低下さ
せるのこのため、Ca−を消耗してしまう欠点もある。
In addition, when electrolysis is applied, useful calcium ions gather on the cathode chamber side, but the above carbonic acid shows a reaction of H2CO, -1-Ca - + H, -1-CaC0°, and becomes calcium carbonate. As a result, it precipitates or adheres to the electrode surface as a scale, lowering the current conduction rate, which also has the disadvantage of consuming Ca.

そこで、水中に空気を吹き込むことにより、泡立てを行
ない、炭酸ガスの除去を行なう方式が採用された。こ\
では、水のガス溶存度が条件(気圧・温度)で一定であ
ることを利用し、炭酸ガスと空気との置換で、実質的に
炭酸ガヌ溶存量を低下させるのである。この具体的方式
としては、水槽底部に多数の孔を穿った板を介して空気
を供給し、水槽中の水を通って気泡状態で上昇する空気
を、その泡の表面で水と接触し、水中の炭酸ガスとの置
換を達成するものがある。しかし、この方式では、水量
に対する空気の供給量が少なく、また、気泡が大^く、
充分外気液の接触表面積が得られないので、予期したよ
うな炭酸除去が達成されない状況にある。
Therefore, a method was adopted in which air was blown into the water to create foam and remove carbon dioxide gas. child\
This takes advantage of the fact that the degree of gas solubility in water is constant depending on the conditions (atmospheric pressure and temperature), and by substituting carbon dioxide gas with air, the amount of dissolved GANO carbonate is substantially reduced. In this specific method, air is supplied through a plate with many holes at the bottom of the aquarium, and the air rises in the form of bubbles through the water in the aquarium, and is brought into contact with the water on the surface of the bubbles. There are some that achieve replacement of carbon dioxide gas in water. However, with this method, the amount of air supplied relative to the amount of water is small, and the air bubbles are large.
Since a sufficient surface area for contact with the outside air and liquid is not obtained, the expected carbon dioxide removal cannot be achieved.

本発明は、上記事情にもとづいてなされたもので、ポー
ラスな隔壁を介して細分化した圧力空気を噴出している
状況のもとで、この隔壁に沿って水を拡散し、全ての水
を泡立たせて、高度の空気接触状態を実現し、これによ
って短時間で効果的な炭酸ガス除去を行なえるようにし
た水の炭酸除去装置を提供しようとするものである。
The present invention was made based on the above circumstances, and in a situation where fragmented pressurized air is ejected through a porous partition wall, water is diffused along the partition wall and all the water is removed. It is an object of the present invention to provide a device for removing carbon dioxide from water, which achieves a high degree of air contact by foaming the water, thereby effectively removing carbon dioxide gas in a short period of time.

以下、本発明の一実施例を図面を参照して具体的に説明
する。図において、符号lは、内形の装置本体であり、
その中央には泡立て室2が、捷だ、一端側には圧力空気
供給室3が設けられている。
Hereinafter, one embodiment of the present invention will be specifically described with reference to the drawings. In the figure, the symbol l is an internal device main body,
A foaming chamber 2 is provided in the center, and a pressurized air supply chamber 3 is provided at one end.

そして、上記泡立て室2の一端側には、上記圧力空気供
給室3とを仕切るように、素焼や、合成樹脂細粒を半溶
集結して作る、例えば商品名「ノ<ルコン」などの通気
多孔質板、その他、気孔を有するポーラスな隔壁4が設
けてあって、上記隔壁4を介して、上記圧力空気供給室
3より上記泡立て室2内へ細分化された圧力空気を供給
するのである。そして、上記圧力空気供給室3はブロア
5に接続されており、また、ブロア5と圧力空気供給室
3との間の連通何処6には電熱などのヒータ7が設けら
れている。
One end side of the foaming chamber 2 is provided with a ventilator, such as the product name "Norucon" made by unglazed or semi-molten aggregate of fine particles of synthetic resin, so as to separate it from the pressurized air supply chamber 3. A porous partition wall 4 having pores such as a porous plate or the like is provided, and finely divided pressurized air is supplied from the pressurized air supply chamber 3 into the bubbling chamber 2 through the partition wall 4. . The pressurized air supply chamber 3 is connected to a blower 5, and a heater 7 such as an electric heater is provided at a communication point 6 between the blower 5 and the pressurized air supply chamber 3.

一方、上記泡立て室2の一端側上方には、泡立て室2の
横幅に対応して噴水用管8が配設してあり、上記噴水用
管8の長手方向に並設したノズル9を介して上記隔壁4
に向は水が拡散放出される。
On the other hand, above one end side of the whisking chamber 2, a fountain pipe 8 is arranged corresponding to the width of the whisking chamber 2, and a fountain pipe 8 is provided through nozzles 9 arranged in parallel in the longitudinal direction of the fountain pipe 8. The partition wall 4
In the opposite direction, water is diffused and released.

蛾 上記噴水用管8は、電磁弁lOを介して水道水(図示せ
ず)に接続されている。また、」二記噴水用管8から離
間して、例えば、泡立て室2の反対側には、溢流壁11
を介して気液分離室12が連設されており、上記気液分
離室12の底部には、貯水槽13への排出口14が開口
されている。
The fountain pipe 8 is connected to tap water (not shown) via a solenoid valve lO. In addition, an overflow wall 11 is provided at a distance from the fountain pipe 8, for example, on the opposite side of the whisking chamber 2.
A gas-liquid separation chamber 12 is connected to the gas-liquid separation chamber 12 via a gas-liquid separation chamber 12, and a discharge port 14 to a water storage tank 13 is opened at the bottom of the gas-liquid separation chamber 12.

このような構成においては、ブロア5を駆動し、電磁弁
10を開放することで(これは手動でもよいが、貯水槽
13に設けたレベル検出器からの信号などで自動的に動
作してもよい)、圧力空気が隔壁4を介して細分化(2
て泡立て室2に入る時、その表面に流下する水を泡立て
る。この泡立ては、泡立て室2を気流の流れる方向へと
抑圧移動され、溢流壁ll側へと押される。そして、溢
流壁を越えた位置で、気液分離室12で、炭酸ガスを含
んだ空気と、含有炭酸ガスを除去された水とが分けられ
る。
In such a configuration, by driving the blower 5 and opening the solenoid valve 10 (this can be done manually, but it can also be done automatically by a signal from a level detector installed in the water tank 13, etc.). (good), the pressurized air is subdivided (2
When entering the foaming chamber 2, the water flowing down onto its surface is foamed. This foaming is suppressed and moved in the direction of air flow in the foaming chamber 2, and is pushed toward the overflow wall ll side. Then, at a position beyond the overflow wall, air containing carbon dioxide gas and water from which carbon dioxide gas is removed are separated in a gas-liquid separation chamber 12.

そして、上記供給空気の圧送力は、たとえ、泡立て室2
内に水が残留しても、隔壁6から気液分離室12へと流
れる水泡がその水によって妨げられることがないほどに
強力に設定され、噴水用管8への水供給量に関して、厖
大な空気量になるように設定される。
And, even if the pumping force of the above-mentioned supply air is
Even if water remains inside, the water bubbles flowing from the partition wall 6 to the gas-liquid separation chamber 12 are set so strongly that they are not obstructed by the water, and the amount of water supplied to the fountain pipe 8 is The air volume is set to match the amount of air.

なお、この実施例では、気液分離室+2tj:、天井に
開口があって、分離された空気を外部に放出する。
In this embodiment, there is an opening in the ceiling of the gas-liquid separation chamber +2tj, and the separated air is discharged to the outside.

処理後の水は、排出口14より貯水槽13へと放出され
るのである。
The treated water is discharged from the outlet 14 into the water storage tank 13.

なお、この実施例では、上水について説明したが、下水
の処理にも適用できること勿論である。
Although this embodiment has been described with respect to tap water, it goes without saying that it can also be applied to sewage treatment.

本発明は以上詳述したようになり、一端側にポーラスな
隔壁を設けた泡立て室と、上記隔壁に沿って供給水を拡
散する手段と、上記隔壁を介して上記泡立て室に空気を
圧送する手段と、水の分散によって形成される水泡を上
記泡立て室で成長させた後、導出し、気液を分離する手
段とを具備したので、水は隔壁上で細分化した空気流で
強制的に細かに泡立てられ、順次、送られて、水泡を拡
大し、最後に放出され、気液の分離がなされる。
The present invention has been described in detail above, and includes a whisking chamber provided with a porous partition wall on one end side, a means for diffusing supply water along the partition wall, and a means for pumping air into the whisking chamber through the partition wall. and a means for extracting water bubbles formed by dispersion of water after growing in the bubbling chamber and separating gas and liquid. The foam is finely whipped, sent sequentially to enlarge the bubbles, and finally released to separate the gas and liquid.

このため、水中に空気を吹き込む方式と異カリ、面積当
りの空気接触量を厖大なものとし、その水に含まれてい
る炭酸ガスは空気中に取出され、空気と置換し、炭酸ガ
ス排出を著しくすることができる。
For this reason, unlike the method of blowing air into water, the amount of air contact per area is enormous, and the carbon dioxide contained in the water is taken out into the air and replaced with air, reducing carbon dioxide emissions. Can be done significantly.

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

第1図は本発明の一実施例を示す縦断側面図、第2図は
同横断平面図である。 l・・・装置本体、2・・・泡立て室、3・・・圧力空
気供給室、4・・・隔壁、5・・・ブロア、6・・・連
通部、7・・・ヒータ、8・・・噴水用管、9・・・ノ
ズル、11・・・溢流壁。 出願人     岡 崎 龍 夫 手 lk  補 止 替(方式) 1.め件の表示 昭和58年特許お+6486388号 2 発す1の名称 !のに証諒“* df! 3、補正をする渚 4件との関係 %許田U人 住 73T  埼玉県上福岡市西2丁目7番18号4、
補正命令の日付 昭4158年8月30日(発シ1日) & 補正の対象 上式ぺ)
FIG. 1 is a vertical cross-sectional side view showing one embodiment of the present invention, and FIG. 2 is a cross-sectional plan view thereof. 1... Apparatus body, 2... Foaming chamber, 3... Pressure air supply chamber, 4... Partition wall, 5... Blower, 6... Communication portion, 7... Heater, 8... ... Fountain pipe, 9... Nozzle, 11... Overflow wall. Applicant Ryu Okazaki Supplemental Replacement (Method) 1. Display of the matter 1988 patent O+6486388 2 Name of issue 1! 3.Relationship with 4 cases of Nagisa to be corrected %Kyoda U residence 73T 2-7-18-4 Nishi, Kamifukuoka City, Saitama Prefecture
Date of amendment order: August 30, 1982 (Issuance 1st day) & Subject of amendment above)

Claims (1)

【特許請求の範囲】[Claims] 一端側にポーラスな隔壁を設けた泡立て室と、上記隔壁
に沿って供給水を拡散する手段と、上記隔壁を介して上
記泡立て室に空気を圧送する手段と、水の分散によって
形成された水泡を上記泡立て室で成長させた後、導出し
気液を分離する手段とを具備したことを特徴とする水の
炭酸除去装置。
a whisking chamber having a porous partition on one end; means for dispersing supplied water along the partition; means for pumping air into the whisking chamber through the partition; and bubbles formed by dispersion of water. An apparatus for removing carbonic acid from water, characterized in that the device comprises means for growing the water in the bubbling chamber and then extracting it to separate gas and liquid.
JP8638883A 1983-05-17 1983-05-17 Apparatus for removing carbon dioxide in water Granted JPS59213412A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8638883A JPS59213412A (en) 1983-05-17 1983-05-17 Apparatus for removing carbon dioxide in water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8638883A JPS59213412A (en) 1983-05-17 1983-05-17 Apparatus for removing carbon dioxide in water

Publications (2)

Publication Number Publication Date
JPS59213412A true JPS59213412A (en) 1984-12-03
JPH0331481B2 JPH0331481B2 (en) 1991-05-07

Family

ID=13885487

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8638883A Granted JPS59213412A (en) 1983-05-17 1983-05-17 Apparatus for removing carbon dioxide in water

Country Status (1)

Country Link
JP (1) JPS59213412A (en)

Also Published As

Publication number Publication date
JPH0331481B2 (en) 1991-05-07

Similar Documents

Publication Publication Date Title
US1526179A (en) Method of aerating or agitating liquids
US3054602A (en) Apparatus for treatment of sewage
US2872415A (en) Domestic water treatment process
US5554280A (en) Filter system
JP4426596B2 (en) Air diffuser
JP2003220398A (en) Aerobic sludge digester
KR20010033596A (en) Vapor/liquid mixer and polluted water purification apparatus using the mixer
US2811258A (en) Domestic water-treatment apparatus
JPS59213412A (en) Apparatus for removing carbon dioxide in water
JPH0716671B2 (en) Water circulation purification device
JPS59213411A (en) Apparatus for removing carbon dioxide in water
US5980613A (en) Pressurized radon stripper
JPH0244878Y2 (en)
JP4172287B2 (en) Method and apparatus for aerobic digestion treatment of sludge
JPS6323995Y2 (en)
JPS59213410A (en) Apparatus for removing carbon dioxide in water
JPH07204682A (en) Anaerobic water treatment apparatus
JP2000512545A (en) Reaction tank for purification of polluted wastewater
CN220723874U (en) Sewage treatment system
JP2000005768A (en) Water treating equipment
JPS63166493A (en) Apparatus for making ozone dissolved water
SU874098A1 (en) Degassing device
JPH10165792A (en) Gas-liquid mixing device and waste water purifying device using the same
RU203069U1 (en) GAS SEPARATOR FOR OBTAINING MICROBIAL PROTEIN MASS
JP4252189B2 (en) Methane fermentation treatment equipment