JPH06331211A - Carbonated water processing device - Google Patents

Carbonated water processing device

Info

Publication number
JPH06331211A
JPH06331211A JP5118191A JP11819193A JPH06331211A JP H06331211 A JPH06331211 A JP H06331211A JP 5118191 A JP5118191 A JP 5118191A JP 11819193 A JP11819193 A JP 11819193A JP H06331211 A JPH06331211 A JP H06331211A
Authority
JP
Japan
Prior art keywords
hot water
flow rate
separator
circulation circuit
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
JP5118191A
Other languages
Japanese (ja)
Other versions
JP3237301B2 (en
Inventor
Toshiya Watanabe
俊哉 渡邊
Yukinori Ozaki
行則 尾崎
Yuko Kubota
勇幸 久保田
Yukiro Komai
幸郎 古米
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 JP11819193A priority Critical patent/JP3237301B2/en
Publication of JPH06331211A publication Critical patent/JPH06331211A/en
Application granted granted Critical
Publication of JP3237301B2 publication Critical patent/JP3237301B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE:To increase the concentration of carbonic acid being dissolved in hot water, obtain a high blood circulation improving effect, and at the same time, making the device hard to receive effects of the hot water discharging flow rate or concentration due to the installation condition, and improve safety in the application of the device by increasing the flow rate of a gas to be introduced per a unit flow rate. CONSTITUTION:A circulation circuit 22 which circulates hot water in a separator 19 is provided, and a mixer 24 is provided in the middle of the circulation circuit 22. At the same time, the flow rate of a gas which is introduced for each unit flow rate of hot water to be discharged is drastically increased by circulating the gas at a high pressure by a carrying means 23. Also, a hot water discharging pipe is provided by branching from the downstream side of the carrying means 23 of the circulation circuit 22, and by carrying hot water at a high pressure, and effects of a pressure loss on the downstream side becomes hard to be received. Also, a control means 27 to stabilize the water surface of hot water stored in the separator 19 is provided so that the hot water in the separator 19 may not overflow or generate air biting.

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、二酸化炭素を含むガス
を湯に溶解させ、炭酸を含有した湯を作る炭酸泉製造装
置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a carbonated spring producing apparatus for dissolving carbon dioxide-containing gas in hot water to produce hot water containing carbonic acid.

【0002】[0002]

【従来の技術】従来この種の炭酸泉製造装置には、図6
に示すようなものがあった。図中の実線矢印は湯水の流
れ方向、破線矢印は燃焼ガスの流れ方向を示している。
2. Description of the Related Art Conventionally, a carbonated spring manufacturing apparatus of this type has a structure shown in FIG.
There was something like that. In the figure, the solid line arrow indicates the flow direction of hot water, and the broken line arrow indicates the flow direction of combustion gas.

【0003】湯または水が通る給水給湯路1と、二酸化
炭素を含むガスが通る導入路2と、導入路2から供給さ
れたガスを給水給湯路1内に導入し、ガス中に含まれる
二酸化炭素を湯または水に溶解する給水給湯路1の途中
に設けた混合器3と、湯または水と湯または水に溶解し
なかった未溶解ガスを分離する混合器3の給水給湯路1
下流側に設けた分離器4と、分離器4において分離した
未溶解ガスを分離器4から排出するエアベント5から構
成されていた。
A water supply hot water supply passage 1 through which hot water or water passes, an introduction passage 2 through which a gas containing carbon dioxide passes, and a gas supplied from the introduction passage 2 is introduced into the water supply hot water supply passage 1, and the carbon dioxide contained in the gas is introduced. Mixer 3 provided in the middle of water supply hot water supply passage 1 for dissolving carbon in hot water or water, and water supply hot water supply passage 1 for mixer 3 for separating hot water or water and undissolved gas not dissolved in hot water or water
It was composed of a separator 4 provided on the downstream side and an air vent 5 for discharging the undissolved gas separated in the separator 4 from the separator 4.

【0004】上記構成により、二酸化炭素を含んだガス
は、導入路2から混合器3に導かれる。一方湯または水
は給水給湯路1を介して混合器3に供給される。混合器
3において湯または水とガスが混合し、ガス中の水溶性
の高い二酸化炭素が溶解して炭酸ガスを含む湯または水
となる。その後分離器4において溶解しなかった未溶解
ガスと二酸化炭素が溶解した湯または水は分離され、未
溶解ガスはエアベント5を介して分離器4から排出され
る。また二酸化炭素が溶解した湯または水は分離器4を
出た後、給水給湯路1を介して所定の場所に供給される
ようにようになっていた。
With the above structure, the gas containing carbon dioxide is introduced into the mixer 3 from the introduction path 2. On the other hand, hot water or water is supplied to the mixer 3 via the hot water supply channel 1. Hot water or water is mixed with gas in the mixer 3, and carbon dioxide having high water solubility in the gas is dissolved to become hot water or water containing carbon dioxide gas. After that, the undissolved gas that has not been dissolved and the hot water or water in which carbon dioxide is dissolved are separated in the separator 4, and the undissolved gas is discharged from the separator 4 via the air vent 5. Further, the hot water or water in which carbon dioxide is dissolved is supplied to a predetermined place via the water supply hot water supply passage 1 after leaving the separator 4.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、上記の
ような構成では、混合器3において導入出来るガスの流
量は給水給湯路1を流れる湯または水の流量に比例する
ため、一般的な水道の供給水圧では流量が少なく、また
エアベント5から排出出来るガスの流量が少ないため、
導入出来るガスの流量が少なくなる。従って湯または水
に溶解された二酸化炭素の濃度も低くなってしまってい
た。さらに、設置状況によって給水給湯路1の下流側の
圧損が増えた場合、出湯流量が低下するとともに、混合
器3の背圧が増加し、混合器におけるガスの吸込流量が
減少し、濃度が著しく下がることがあった。
However, in the above configuration, the flow rate of the gas that can be introduced in the mixer 3 is proportional to the flow rate of the hot water or the water flowing through the hot water supply hot water supply passage 1, and therefore the supply of general water supply is not possible. Since the flow rate is small under water pressure and the flow rate of gas that can be discharged from the air vent 5 is small,
The flow rate of gas that can be introduced decreases. Therefore, the concentration of hot water or carbon dioxide dissolved in water was also low. Further, when the pressure loss on the downstream side of the hot water supply channel 1 increases depending on the installation situation, the hot water outlet flow rate decreases, the back pressure of the mixer 3 increases, the gas suction flow rate in the mixer decreases, and the concentration is significantly increased. There were times when it dropped.

【0006】また、分離器4内の湯面が下がった場合に
は、分離器4内のガスが給水給湯路1内に侵入し、湯を
使用する給水給湯路1の出口からガスが一緒に噴出する
ことがあった。また給水給湯路1を公共の水道などに直
結させた場合、万一水道側が負圧になると、二酸化炭素
ガスを含んだ湯が水道側に逆流する場合があるという課
題があった。
[0006] When the level of the hot water in the separator 4 drops, the gas in the separator 4 enters the hot water supply channel 1 and the gas flows together from the outlet of the hot water supply channel 1 that uses hot water. There was a gush. Further, when the hot water supply channel 1 is directly connected to a public water supply or the like, if there is a negative pressure on the water supply side, the hot water containing carbon dioxide gas may flow back to the water supply side.

【0007】次に、上記構成における炭酸濃度について
数式を用いて説明する。給水給湯路1を流れる湯の流量
をQw、導入されるガスの流量Qgとすると、湯中の炭
酸の濃度Cは、次式に示すようなガス流量と湯の流量の
比に比例した関数として表わすことが出来る。
Next, the carbon dioxide concentration in the above structure will be described using mathematical expressions. Assuming that the flow rate of the hot water flowing through the hot water supply channel 1 is Qw and the flow rate of the introduced gas is Qg, the carbon dioxide concentration C in the hot water is a function proportional to the ratio of the gas flow rate and the hot water flow rate as shown in the following equation. Can be represented.

【0008】C=F(Qg/Qw) ところが、QgはQwにほぼ比例した関係を持つため、
QgとQwの比例定数を仮にAとすると、次式のように
なる。
C = F (Qg / Qw) However, since Qg has a relationship almost proportional to Qw,
Assuming that the proportional constant of Qg and Qw is A, the following equation is obtained.

【0009】Qg=A・Qw この式を濃度の式に代入すると、 C=F(Qw・A/Qw)=F(A)=const. となり、濃度はQwに関係無しに、ほぼ一定値をとるこ
とになる。従って、この構成では高濃度化することが困
難であることが推測される。
Qg = AQw When this equation is substituted into the concentration equation, C = F (QwA / Qw) = F (A) = const. Therefore, the concentration takes a substantially constant value regardless of Qw. Therefore, it is presumed that it is difficult to increase the concentration with this configuration.

【0010】本発明の炭酸泉製造装置は、このような従
来の課題を解決するもので、単位出湯流量当りに導入す
るガスの流量を増加させ、湯中の炭酸濃度を高め、炭酸
により得られる血流増加作用等の医学的効果を高めるこ
と、並びに分離器を大気開放型にし、上水道側と縁切り
した構成をとることによって、上水道に炭酸が溶解した
湯が逆流することを防止し、上水道の衛生上の安全性を
確保することを第1の目的としている。
The carbonated spring producing apparatus of the present invention solves such a conventional problem, and increases the flow rate of the gas introduced per unit discharge flow rate to increase the carbonic acid concentration in the hot water to obtain blood obtained by carbonic acid. By increasing the medical effects such as the flow increasing action and by making the separator open to the atmosphere and taking a structure that is cut off from the water supply side, it is possible to prevent the hot water in which carbonic acid is dissolved from flowing back into the water supply and to improve the sanitation of the water supply. The first purpose is to ensure the above safety.

【0011】本発明の第2の目的は、単位出湯流量当り
に導入するガスの流量を増加させ、湯中の炭酸濃度を高
め、炭酸により得られる血流増加作用等の医学的効果を
高めること。分離器を大気開放型にし、上水道側と縁切
りした構成をとることによって、上水道に炭酸ガスが溶
解した湯が逆流することを防止し、上水道の衛生上の安
全性を確保すること、並びにポンプ等の搬送手段によっ
て湯を搬送することにより、下流側の圧損に関係なく炭
酸濃度の高い湯を供給すること、また装置の設置条件や
装置下流側の圧損が変化した場合でも、安定した流量の
湯を出湯することにある。
A second object of the present invention is to increase the flow rate of gas introduced per unit flow rate of hot water, increase the carbonic acid concentration in hot water, and enhance the medical effects such as blood flow increasing action obtained by carbonic acid. . By making the separator open to the atmosphere and taking a structure that is cut off from the water supply side, it is possible to prevent the hot water in which carbon dioxide gas is dissolved from flowing back into the water supply, and to ensure the sanitary safety of the water supply, as well as pumps, etc. The hot water having a high carbon dioxide concentration is supplied regardless of the pressure loss on the downstream side by transporting the hot water by the transporting means, and even if the installation condition of the device or the pressure loss on the downstream side of the device changes, the hot water has a stable flow rate. Is to take out hot water.

【0012】本発明の第3の目的は、分離器に入ってく
る湯の流量と、分離器から出ていく湯の流量を検知し
て、例えば、分離器に入ってくる流量と分離器から出て
いく流量が同じになるように、出湯流量を調節すること
により、流量変動を無くすこと、並びに炭酸濃度の安定
化を図ることにある。
A third object of the present invention is to detect the flow rate of hot water entering the separator and the flow rate of hot water exiting the separator, and for example, to detect the flow rate entering the separator and the separator. By adjusting the flow rate of tapping hot water so that the flow rate is the same, the flow rate fluctuation is eliminated and the carbon dioxide concentration is stabilized.

【0013】本発明の第4の目的は、分離器内に貯った
湯の水位を検知し、その水位に応じて分離器から出てい
く湯の流量を調節することにより、例えば低水圧の地域
などにおいて、分離器に供給される湯の流量が少ない場
合でも、分離器内の水位が下がってガスが出湯路中に侵
入して使用場所からガスが噴出することを防止し、装置
の使用上の安全性を高めることにある。
A fourth object of the present invention is to detect the water level of the hot water stored in the separator and adjust the flow rate of the hot water flowing out of the separator according to the water level. Even if the flow rate of hot water supplied to the separator is low in areas such as the area, the water level inside the separator is prevented from lowering and gas intrudes into the hot water discharge passage to prevent the gas from spouting from the place of use and using the device. It is to improve the safety above.

【0014】本発明の第5の目的は、分離器内に貯った
湯の水位を検知し、その水位に応じて分離器に入ってく
る湯の流量を調節することにより、例えば高水圧の地域
などにおいて、分離器に供給される湯の流量が多い場合
でも、分離器内の水位が上がって湯が分離器から溢れ出
ることを防止し、装置の使用上の安全性を高めることに
ある。
A fifth object of the present invention is to detect the water level of the hot water stored in the separator and adjust the flow rate of the hot water entering the separator in accordance with the water level, for example, to obtain a high water pressure. This is to prevent the hot water from overflowing from the separator by raising the water level in the separator even when the flow rate of the hot water supplied to the separator is high in the area, etc., and to enhance the safety in use of the device. .

【0015】[0015]

【課題を解決するための手段】上記第1の目的を達成す
るために、本発明の炭酸泉製造装置の第1の技術手段
は、湯を供給する給湯路と、二酸化炭素が含まれたガス
を供給する導入路と、給湯路に接続された、湯とガスを
分離する分離器と、分離器内の湯を循環させる循環回路
と、循環回路の途中に設けられた、循環回路内の湯を搬
送する搬送手段と、循環回路の搬送手段の下流側に設け
られ、導入路から供給されたガスを循環回路中に導入し
溶解させる混合器と、分離器から湯を出湯する出湯路
と、分離器から分離したガスを排出する排出路とを備え
たものである。
In order to achieve the above first object, the first technical means of the carbonated spring manufacturing apparatus of the present invention comprises a hot water supply passage for supplying hot water and a gas containing carbon dioxide. A supply line for supplying water, a separator connected to the hot water supply line for separating hot water and gas, a circulation circuit for circulating the hot water in the separator, and a hot water in the circulation circuit provided in the middle of the circulation circuit. A conveying means for conveying, a mixer provided on the downstream side of the conveying means of the circulation circuit, for introducing the gas supplied from the introduction passage into the circulation circuit and dissolving it, and a tapping passage for discharging hot water from the separator, And a discharge path for discharging the gas separated from the container.

【0016】また第2の目的を達成するために、本発明
の炭酸泉製造装置の第2の技術手段は、湯を供給する給
湯路と、二酸化炭素が含まれたガスを供給する導入路
と、給湯路に接続された、湯とガスを分離する分離器
と、分離器内の湯を循環させる循環回路と、循環回路の
途中に設けられ循環回路内の湯を搬送する搬送手段と、
循環回路の搬送手段の下流側に設けられ、導入路から供
給されたガスを循環回路中に導入し溶解させる混合器
と、搬送手段と混合器の間の循環回路から分岐し、循環
回路から湯を出湯する出湯路と、分離器から分離したガ
スを排出する排出路を備えたものである。
In order to achieve the second object, the second technical means of the carbonated spring manufacturing apparatus of the present invention comprises a hot water supply passage for supplying hot water, and an introduction passage for supplying a gas containing carbon dioxide. A separator connected to the hot water supply passage, for separating hot water and gas, a circulation circuit for circulating the hot water in the separator, and a conveying means provided in the middle of the circulation circuit for conveying the hot water in the circulation circuit,
A mixer provided on the downstream side of the conveying means of the circulation circuit for introducing and dissolving the gas supplied from the introduction path into the circulation circuit, and a circulation circuit between the conveying means and the mixer are branched, and hot water is circulated from the circulation circuit. It is provided with a hot water discharge path for discharging hot water and a discharge path for discharging the gas separated from the separator.

【0017】また第3の目的を達成するために、本発明
の炭酸泉製造装置の第3の技術手段は、本発明の炭酸泉
製造装置の第1の技術手段並びに第2の技術手段におい
て、給湯路の途中に、湯の流量を検知する入側流量検知
手段を設け、出湯路の途中に、湯の流量を検知する出側
流量検知手段を設け、出湯路の途中に、湯の流量を調節
する流量調節手段を設け、入側流量検知手段並びに出側
流量検知手段からの信号に応じて流量調節手段を制御す
る制御手段を備えたものである。
In order to achieve the third object, the third technical means of the carbonated spring producing apparatus of the present invention is the first technical means and the second technical means of the carbonated spring producing apparatus of the present invention. An inlet side flow rate detecting means for detecting the flow rate of the hot water is provided in the middle of the hot water, an outlet side flow rate detecting means for detecting the flow rate of the hot water is provided in the middle of the hot water discharge path, and the hot water flow rate is adjusted in the middle of the hot water path. A flow rate adjusting means is provided, and a control means for controlling the flow rate adjusting means according to signals from the inlet side flow rate detecting means and the outlet side flow rate detecting means is provided.

【0018】また第4の目的を達成するために、本発明
の炭酸泉製造装置の第4の技術手段は、本発明の炭酸泉
製造装置の第1の技術手段並びに第2の技術手段におい
て、分離器内に、分離器の内部に貯った湯の水位を検知
する水位検知手段を設け、出湯路の途中に、湯の流量を
調節する流量調節手段を設け、水位検知手段からの信号
に応じて流量調節手段を制御する制御手段を備えたもの
である。
In order to achieve the fourth object, the fourth technical means of the carbonated spring producing apparatus of the present invention is the separator in the first technical means and the second technical means of the carbonated spring producing apparatus of the present invention. Inside, a water level detecting means for detecting the water level of the hot water stored inside the separator is provided, and a flow rate adjusting means for adjusting the flow rate of the hot water is provided in the middle of the hot water outlet, and in response to a signal from the water level detecting means. The control means for controlling the flow rate adjusting means is provided.

【0019】また第5の目的を達成するために、本発明
の炭酸泉製造装置の第5の技術手段は、本発明の炭酸泉
製造装置の第1の技術手段並びに第2の技術手段におい
て、分離器内に、分離器の内部に貯った湯の水位を検知
する水位検知手段を設け、給湯路の途中に、湯の流量を
調節する流量調節手段を設け、水位検知手段からの信号
に応じて流量調節手段を制御する制御手段を備えたもの
である。
In order to achieve the fifth object, the fifth technical means of the carbonated spring producing apparatus of the present invention is the separator according to the first technical means and the second technical means of the carbonated spring producing apparatus of the present invention. Inside, a water level detecting means for detecting the water level of the hot water stored inside the separator is provided, and in the middle of the hot water supply passage, a flow rate adjusting means for adjusting the flow rate of the hot water is provided, and in response to a signal from the water level detecting means. The control means for controlling the flow rate adjusting means is provided.

【0020】[0020]

【作用】本発明は、上記の第1の技術手段により、湯は
給湯路から分離器に供給される。分離器内に貯った湯
は、搬送手段によって循環回路内を流れ混合器を介して
分離器に戻る。混合器において導入路から供給された二
酸化炭素を含むガスが循環回路内に導入され、湯とガス
が混合される。ガス中の水溶性の高い二酸化炭素は湯中
に溶解され、湯は炭酸を含んだ湯となる。湯に溶解しな
かった未溶解のガスと湯は分離器において分離され、未
溶解のガスは排出路を介して排出され、炭酸を含んだ湯
のみが出湯路を介して所定の場所に供給される。
According to the present invention, hot water is supplied from the hot water supply passage to the separator by the above-mentioned first technical means. The hot water stored in the separator flows in the circulation circuit by the conveying means and returns to the separator via the mixer. In the mixer, the gas containing carbon dioxide supplied from the introduction path is introduced into the circulation circuit, and the hot water and the gas are mixed. Highly water-soluble carbon dioxide in the gas is dissolved in hot water, and the hot water contains carbonic acid. The undissolved gas that was not dissolved in the hot water and the hot water are separated in the separator, the undissolved gas is discharged through the discharge passage, and only the carbon dioxide-containing hot water is supplied to the prescribed place through the discharge passage. .

【0021】混合器が、湯を供給する給湯路または出湯
路に直結されていない別設の循環回路に設けられている
ため、導入されるガスの流量は給湯路または出湯路を流
れる湯の流量に関係せず、循環回路を流れる循環流量に
比例する。循環流量は設けた搬送手段の能力により決定
されるため、搬送手段の能力を上げれば上げるほど導入
されるガスの流量は増え、高濃度にすることが出来る。
また分離器は排気路を介して大気開放になっているた
め、給湯路を上水道と直結させた場合でも給湯路は分離
器内に貯った湯と縁切りされており、給湯路が万一負圧
になっても分離器内に貯った炭酸を含んだ湯が給湯路に
逆流することは無い。
Since the mixer is provided in a separate circulation circuit which is not directly connected to the hot water supply passage or hot water supply passage for supplying hot water, the flow rate of the gas introduced is the flow rate of hot water flowing through the hot water supply passage or the hot water discharge passage. It is proportional to the circulation flow rate flowing through the circulation circuit regardless of. Since the circulation flow rate is determined by the capacity of the transfer means provided, the higher the capacity of the transfer means, the higher the flow rate of the introduced gas and the higher the concentration.
In addition, since the separator is open to the atmosphere via the exhaust passage, even if the hot water supply passage is directly connected to the water supply, the hot water supply passage is separated from the hot water stored in the separator, and the hot water supply passage is negative. Even if pressure is applied, the hot water containing carbonic acid stored in the separator does not flow back into the hot water supply passage.

【0022】ここで、湯中の炭酸濃度について数式を用
いて説明する。給湯路および出湯路内を流れる湯の流量
をQw、循環回路内を流れる湯の流量(循環流量)をQ
j、導入されるガスの流量Qgとすると、湯中の炭酸の
濃度Cは、次式に示すようなガス流量と湯の流量の比に
比例した関数として表わすことが出来る。
Here, the carbonic acid concentration in the hot water will be described using mathematical expressions. Qw is the flow rate of the hot water flowing in the hot water supply passage and the hot water discharge passage, and Q is the flow rate of the hot water flowing in the circulation circuit (circulation flow rate).
j and the flow rate Qg of the introduced gas, the carbon dioxide concentration C in the hot water can be expressed as a function proportional to the ratio of the gas flow rate to the hot water flow rate as shown in the following equation.

【0023】C=F(Qg/Qw) ところが、QgはQjにほぼ比例した関係を持つため、
QgとQwの比例定数を仮にAとすると、次式のように
なる。
C = F (Qg / Qw) However, since Qg has a relationship almost proportional to Qj,
Assuming that the proportional constant of Qg and Qw is A, the following equation is obtained.

【0024】Qg=Qj・A この式を濃度の式に代入すると、 C=F(A・Qj/Qw) となり、濃度はQj/Qwに比例する。従って、循環流
量を増やせば増やすほど高濃度化にすることが出来る。
Qg = Qj · A When this formula is substituted into the formula of concentration, C = F (A · Qj / Qw), and the concentration is proportional to Qj / Qw. Therefore, the higher the circulation flow rate, the higher the concentration.

【0025】一般的に循環流量Qjは供給される湯の流
量Qwの3〜4倍にすることが出来るので濃度も従来の
3〜4倍にすることが出来る。
Generally, the circulation flow rate Qj can be set to 3 to 4 times the flow rate Qw of the hot water supplied, so that the concentration can also be set to 3 to 4 times the conventional concentration.

【0026】また本発明の第2の技術手段においては、
第1の技術手段と同様に湯は給湯路から分離器に供給さ
れる。分離器内に貯った湯は、搬送手段によって循環回
路内を流れ混合器を介して分離器に戻る。混合器におい
て導入路から供給された二酸化炭素を含むガスが循環回
路内に導入され、湯とガスが混合される。ガス中の水溶
性の高い二酸化炭素は湯中に溶解され、湯は炭酸を含ん
だ湯となる。湯に溶解しなかった未溶解のガスと湯は分
離器において分離され、未溶解のガスは排出路を介して
排出され、炭酸を含んだ湯のみが出湯路を介して所定の
場所に供給される。分離器内に貯った湯は循環回路に分
岐して設けた出湯路から搬送手段によって高圧で出湯さ
れる。
Further, in the second technical means of the present invention,
Hot water is supplied to the separator from the hot water supply channel as in the first technical means. The hot water stored in the separator flows in the circulation circuit by the conveying means and returns to the separator via the mixer. In the mixer, the gas containing carbon dioxide supplied from the introduction path is introduced into the circulation circuit, and the hot water and the gas are mixed. Highly water-soluble carbon dioxide in the gas is dissolved in hot water, and the hot water contains carbonic acid. The undissolved gas that was not dissolved in the hot water and the hot water are separated in the separator, the undissolved gas is discharged through the discharge passage, and only the carbon dioxide-containing hot water is supplied to the prescribed place through the discharge passage. . The hot water stored in the separator is discharged at a high pressure from the hot water passage provided by branching into the circulation circuit by the conveying means.

【0027】混合器が、湯を供給する給湯路または出湯
路に直結されていない別設の循環回路に設けられている
ため、導入されるガスの流量は給湯路または出湯路を流
れる湯の流量に関係せず、循環回路を流れる循環流量に
比例する。循環流量は設けた搬送手段の能力により決定
されるため、搬送手段の能力を上げれば上げるほど導入
されるガスの流量は増え、高濃度にすることが出来る。
また分離器は排気路を介して大気開放になっているた
め、給湯路を上水道と直結させた場合でも給湯路は分離
器内に貯った湯と縁切りされており、給湯路が万一負圧
になっても分離器内に貯った炭酸を含んだ湯が給湯路に
逆流することは無い。さらに搬送手段の下流側の循環回
路から分岐して出湯路を設けたことによって、湯を強制
的に所定の場所に供給するため、設置条件等により出湯
路の下流側で圧損が大きくなっても、安定した流量を確
保することが出来る。
Since the mixer is provided in a separate circulation circuit which is not directly connected to the hot water supply passage or hot water discharge passage for supplying hot water, the flow rate of the introduced gas is the flow rate of hot water flowing through the hot water supply passage or the hot water discharge passage. It is proportional to the circulation flow rate flowing through the circulation circuit regardless of. Since the circulation flow rate is determined by the capacity of the transfer means provided, the higher the capacity of the transfer means, the higher the flow rate of the introduced gas and the higher the concentration.
In addition, since the separator is open to the atmosphere via the exhaust passage, even if the hot water supply passage is directly connected to the water supply, the hot water supply passage is separated from the hot water stored in the separator, and the hot water supply passage is negative. Even if pressure is applied, the hot water containing carbonic acid stored in the separator does not flow back into the hot water supply passage. Further, since the hot water supply path is provided by branching from the circulation circuit on the downstream side of the conveying means, the hot water is forcibly supplied to a predetermined location, so even if the pressure loss becomes large on the downstream side of the hot water supply path due to installation conditions and the like. It is possible to secure a stable flow rate.

【0028】また本発明の第3の技術手段においては、
入側流量検知手段から得られた流量と出側流量検知手段
から得られた情報に応じて出湯路途中に設けた流量調節
手段で出湯路内を流れる湯の流量を制御する。例えば、
給湯路を介して分離器に入ってくる湯の流量と、出湯路
を介して分離器から出ていく湯の流量が同じになるよう
に出湯路に設けた流量調節手段を制御することにより、
分離器内の水面を一定に保つとともに、出湯される流量
の変動を無くし、循環回路内を流れる流量を安定にさせ
ることにより、混合器に導入されるガスの流量を安定化
させて湯中の炭酸濃度を安定させることが出来る。
In the third technical means of the present invention,
The flow rate of the hot water flowing in the hot water outlet is controlled by the flow rate adjusting means provided in the hot water outlet according to the flow rate obtained from the inlet flow rate detecting means and the information obtained from the outlet flow rate detecting means. For example,
By controlling the flow rate adjusting means provided in the hot water outlet so that the flow rate of hot water entering the separator via the hot water supply passage and the flow rate of hot water leaving the separator via the hot water supply passage are the same,
By keeping the water level in the separator constant, eliminating fluctuations in the flow rate of hot water discharged, and stabilizing the flow rate in the circulation circuit, the flow rate of gas introduced into the mixer is stabilized and The carbon dioxide concentration can be stabilized.

【0029】また本発明の第4の技術手段においては、
分離器内の湯の水位を検知する水位検知手段から得られ
た情報に応じて出湯路途中に設けた流量調節手段で出湯
路内を流れる湯の流量を制御する。例えば、低水圧地域
などでは分離器に供給される湯の流量が少ないため分離
器内の水位が下がり、循環路や出湯路にガスが混入する
ことがある。しかし、分離器内の水位が所定の値より下
がったことを水位検知手段で検知した場合には、出湯路
から流れ出る湯の流量を少なくするように流量調節手段
を制御することにより、水位が所定値より下がることを
抑え、循環路や出湯路にガスが混入することが防止出
来、装置使用上の安全性を確保することが出来る。
In the fourth technical means of the present invention,
According to the information obtained from the water level detecting means for detecting the water level of the hot water in the separator, the flow rate adjusting means provided in the hot water outlet controls the flow rate of the hot water flowing in the hot water outlet. For example, in a low water pressure area or the like, since the flow rate of hot water supplied to the separator is small, the water level in the separator may drop, and gas may be mixed into the circulation path or the hot water exit path. However, when the water level detecting means detects that the water level in the separator has dropped below a predetermined value, the flow level adjusting means is controlled so as to reduce the flow rate of the hot water flowing out of the hot water outlet passage, thereby controlling the water level to a predetermined level. It is possible to suppress falling below the value, prevent gas from mixing in the circulation path or the hot water supply path, and ensure safety in using the device.

【0030】また本発明の第5の技術手段においては、
分離器内の湯の水位を検知する水位検知手段から得られ
た情報に応じて給湯路途中に設けた流量調節手段で給湯
路内を流れる湯の流量を制御する。例えば、高水圧地域
などでは分離器に供給される湯の流量が多いため分離器
内の水位が上がり、排出路を介して炭酸を含んだ湯が溢
れ出てしまうことがある。しかし、分離器内の水位が所
定の値より上がったことを水位検知手段で検知した場合
には、給湯路から分離器に供給される湯の流量を少なく
するように流量調節手段を制御することにより、水位が
所定値より上がることを抑え、排出路を介して湯が溢れ
出ることが防止出来、装置使用上の安全性を確保するこ
とが出来る。
Further, in the fifth technical means of the present invention,
According to the information obtained from the water level detecting means for detecting the water level of the hot water in the separator, the flow rate adjusting means provided in the hot water supply path controls the flow rate of the hot water flowing in the hot water supply path. For example, in a high water pressure area or the like, the flow rate of hot water supplied to the separator is high, so that the water level in the separator rises, and hot water containing carbonic acid may overflow through the discharge passage. However, when the water level detecting means detects that the water level in the separator rises above a predetermined value, the flow rate adjusting means should be controlled so as to reduce the flow rate of hot water supplied from the hot water supply passage to the separator. Thus, it is possible to prevent the water level from rising above a predetermined value, prevent the hot water from overflowing through the discharge path, and ensure the safety in using the device.

【0031】[0031]

【実施例】以下本発明の実施例を添付図面にもとづいて
説明する。図中の実線矢印は湯水の流れ方向を示し、破
線矢印は排気ガスの流れ方向を示し、破線は信号線を示
している。また同一の構成要素には同一の符号を付けて
いる。
Embodiments of the present invention will be described below with reference to the accompanying drawings. Solid arrows in the figure indicate the flow direction of hot and cold water, broken line arrows indicate the flow direction of exhaust gas, and broken lines indicate signal lines. Further, the same components are designated by the same reference numerals.

【0032】図1は、本発明の炭酸泉製造装置の第1の
技術手段を給湯機に応用した場合の第1の実施例の要部
切断の概略構成図である。
FIG. 1 is a schematic block diagram of the main part cutting of the first embodiment when the first technical means of the carbonated spring manufacturing apparatus of the present invention is applied to a water heater.

【0033】6は燃焼用空気を供給する燃焼ファン7に
よって供給された空気と燃料供給路8の途中に設けられ
た燃料調節手段9によって流量調節された燃料を混合し
燃焼させる燃焼手段である。燃焼手段6から燃焼ガスの
流れ方向下流側に順に燃焼室10と熱交換器11と排気
路12が連接して設けられている。排気路12の途中に
は、燃焼ガスの一部が流れるように導入路13が排気路
12から分岐して設けられている。14は熱交換器11
に水を供給する給水路である。また給水路14の途中に
は給水路14内を流れる水の流量を検知する入側水流量
検知手段15と水の温度を検知する入水温検知手段16
が設けられている。給水路14から供給された水は熱交
換器11で熱交換されて湯となり給湯路17に入る。湯
は給湯路17の途中に設けられた出湯温検知手段18に
おいて温度を検知された後、分離器19に至る。分離器
19において湯とガスが分離され、湯のみが分離器19
から出湯路20を介して浴槽21等の所定の場所に供給
される。分離器19には、分離器19の底部と上部に接
続口を持ち、分離器19内の湯を循環させる循環回路2
2が備えられており、循環回路22の途中には湯を搬送
する搬送手段23が設けられている。また循環回路22
の搬送手段23の下流側には、導入路13から供給され
た燃焼ガスを循環回路22内に導入する混合器24が設
けられている。分離器19には分離したガスを大気中に
排出する排出路25が設けられている。
Reference numeral 6 is a combustion means for mixing and burning the air supplied by the combustion fan 7 for supplying combustion air and the fuel whose flow rate is adjusted by the fuel adjusting means 9 provided in the middle of the fuel supply passage 8. A combustion chamber 10, a heat exchanger 11, and an exhaust passage 12 are provided in this order from the combustion means 6 downstream in the flow direction of combustion gas. In the middle of the exhaust passage 12, an introduction passage 13 is provided so as to branch from the exhaust passage 12 so that a part of the combustion gas flows. 14 is a heat exchanger 11
It is a water supply channel that supplies water to. In the middle of the water supply passage 14, an inlet side water flow rate detecting means 15 for detecting the flow rate of water flowing in the water supply passage 14 and an inlet water temperature detecting means 16 for detecting the temperature of the water.
Is provided. The water supplied from the water supply passage 14 is heat-exchanged by the heat exchanger 11 to become hot water and enters the hot water supply passage 17. The hot water reaches the separator 19 after the temperature is detected by the hot water temperature detecting means 18 provided in the hot water supply path 17. The hot water and the gas are separated in the separator 19, and only the hot water is separated in the separator 19.
Is supplied to a predetermined place such as a bathtub 21 via the tap passage 20. The separator 19 has a connection port at the bottom and the top of the separator 19 and circulates the hot water in the separator 19.
2 is provided, and a transport means 23 for transporting hot water is provided in the circulation circuit 22. The circulation circuit 22
A mixer 24 for introducing the combustion gas supplied from the introduction passage 13 into the circulation circuit 22 is provided on the downstream side of the conveying means 23. The separator 19 is provided with an exhaust passage 25 for exhausting the separated gas into the atmosphere.

【0034】また26は出湯する湯の温度を設定する温
度設定手段である。27は装置全体を制御する制御手段
であり、燃焼ファン7、燃料調節手段9、入側流量検知
手段15、入水温検知手段16、出湯温検知手段18、
搬送手段23、温度設定手段26と図に示すように結線
されている。
Numeral 26 is a temperature setting means for setting the temperature of the hot water discharged. Reference numeral 27 is a control means for controlling the entire apparatus, including a combustion fan 7, a fuel adjusting means 9, an inlet side flow rate detecting means 15, an incoming water temperature detecting means 16, a hot water temperature detecting means 18,
The conveying means 23 and the temperature setting means 26 are connected as shown in the figure.

【0035】上記構成において、空気は燃焼ファン7に
よって燃焼手段6に供給され、燃料は燃料調節手段9で
流量調節され燃料供給路8から燃焼手段6に供給され
る。燃焼手段6では供給された空気と燃料が混合され、
燃焼室10内で燃焼を行う。燃焼によって生成された燃
焼ガスは熱交換器11で給水路14から供給された水と
熱交換を行い、燃焼ガスは排気路12より排気される。
燃焼ガスの一部は排気路12の途中から分岐して設けた
導入路13を介して混合器24へ導かれる。一方、熱交
換器11に給水路14から供給された水は熱交換されて
湯となり給湯路17を介して分離器19に至る。分離器
19に入った湯は搬送手段23によって循環回路22に
入り、循環回路22の途中に設けた混合器24において
導入路13から供給された燃焼ガスと混合し、分離器1
9に戻る。途中燃焼ガス中の水溶性の高い二酸化炭素ガ
スは湯中に溶解し炭酸の含んだ湯となる。分離器19に
は炭酸を含んだ湯と湯に溶解しなかった未溶解のガスが
混ざって排出される。分離器19において湯と未溶解の
ガスが分離され、未溶解のガスは排出路25から排出さ
れ、炭酸を含んだ湯が出湯路20から所定の場所に供給
される。
In the above structure, the air is supplied to the combustion means 6 by the combustion fan 7, the flow rate of the fuel is adjusted by the fuel adjustment means 9, and the fuel is supplied to the combustion means 6 from the fuel supply passage 8. In the combustion means 6, the supplied air and fuel are mixed,
Combustion is performed in the combustion chamber 10. The combustion gas generated by combustion exchanges heat with the water supplied from the water supply passage 14 in the heat exchanger 11, and the combustion gas is exhausted from the exhaust passage 12.
A part of the combustion gas is guided to the mixer 24 via the introduction path 13 that is branched from the middle of the exhaust path 12. On the other hand, the water supplied from the water supply passage 14 to the heat exchanger 11 is heat-exchanged into hot water and reaches the separator 19 via the hot water supply passage 17. The hot water that has entered the separator 19 enters the circulation circuit 22 by the conveying means 23, and is mixed with the combustion gas supplied from the introduction passage 13 in the mixer 24 provided in the middle of the circulation circuit 22, and the separator 1
Return to 9. Highly water-soluble carbon dioxide gas in the combustion gas on the way is dissolved in hot water to form hot water containing carbonic acid. Hot water containing carbonic acid and undissolved gas not dissolved in the hot water are mixed and discharged to the separator 19. The hot water and the undissolved gas are separated in the separator 19, the undissolved gas is discharged from the discharge passage 25, and the hot water containing carbonic acid is supplied from the hot water discharge passage 20 to a predetermined place.

【0036】制御手段27は、温度設定手段26で設定
された温度の湯を出湯するように、入側水流量検知手段
15で得られた流量と、入水温検知手段16で得られた
水温、並びに出湯温検知手段18で得られた湯温の情報
に基づいて、燃焼手段6で燃焼する燃焼量を決定し、決
定した燃焼量になるように燃料調節手段9を制御し、同
燃焼量で安定した燃焼が行えるように、燃焼ファン7の
能力を制御する。また搬送手段23を制御する。
The control means 27 outputs the hot water having the temperature set by the temperature setting means 26, the flow rate obtained by the incoming side water flow rate detecting means 15, the water temperature obtained by the incoming water temperature detecting means 16, In addition, based on the hot water temperature information obtained by the hot water temperature detection means 18, the combustion amount burned by the combustion means 6 is determined, and the fuel adjustment means 9 is controlled so that the determined combustion amount is achieved. The capability of the combustion fan 7 is controlled so that stable combustion can be performed. It also controls the transport means 23.

【0037】このような構成により、搬送手段23を用
いて分離器19内の湯を大量に循環させることにより、
循環回路22中に大量の燃焼ガスを導入することが出
来、出湯路20から出湯する湯中の炭酸濃度を高めるこ
とが出来る。また分離器19は排出路25と連通されて
大気開放になっているため、給湯路17は分離器19内
に貯った湯と縁切りされており、給湯路17が万一負圧
になっても分離器19内に貯った炭酸を含んだ湯が給湯
路17に逆流することは無い。
With this structure, a large amount of hot water in the separator 19 is circulated by using the conveying means 23,
A large amount of combustion gas can be introduced into the circulation circuit 22, and the concentration of carbon dioxide in the hot water discharged from the hot water passage 20 can be increased. Further, since the separator 19 is in communication with the discharge passage 25 and is open to the atmosphere, the hot water supply passage 17 is cut off from the hot water stored in the separator 19, and the hot water supply passage 17 becomes negative pressure by any chance. However, the hot water containing carbonic acid stored in the separator 19 does not flow back into the hot water supply passage 17.

【0038】図2は本発明の炭酸泉製造装置の第2の技
術手段を給湯機に応用した場合の第2の実施例であり、
上記第1の技術手段の実施例と異なる点は、出湯路20
を搬送手段23と混合器24の間の循環回路22に分岐
して設けたことである。そしてこれ以外の構成は上記第
1の技術手段の実施例と同じであり、同一符号を付け詳
細な説明を省略する。
FIG. 2 shows a second embodiment in which the second technical means of the carbonated spring manufacturing apparatus of the present invention is applied to a water heater.
The difference from the embodiment of the first technical means is that the hot water outlet 20
Is branched and provided in the circulation circuit 22 between the conveying means 23 and the mixer 24. The rest of the configuration is the same as that of the first embodiment of the technical means described above, and the same reference numerals are given to omit detailed description.

【0039】上記構成において、炭酸が溶解した湯は循
環回路22内を循環し、搬送手段23の下流側から一部
が出湯路20を介して所定の場所に圧送される。出湯路
20から出湯する湯は搬送手段23により高圧で送られ
るため、浴槽21と装置の位置関係や出湯路20の配管
長さ等の設置状況による圧損が多少変化しても、分離器
19へ湯が逆流したり、供給する湯の流量が著しく変化
することが無く、安定した湯の供給が出来る。また搬送
手段23を用いて分離器19内の湯を大量に循環させる
ことにより、循環回路22中に大量の燃焼ガスを導入す
ることが出来、出湯路20から出湯する湯中の炭酸濃度
を高めることが出来る。また分離器19は排出路25と
連通されて大気開放になっているため、給湯路17は分
離器19内に貯った湯と縁切りされており、給湯路17
が万一負圧になっても分離器19内に貯った炭酸を含ん
だ湯が給湯路17に逆流することは無い。
In the above-mentioned structure, the hot water in which carbonic acid is dissolved circulates in the circulation circuit 22, and a part of the hot water is conveyed from the downstream side of the conveying means 23 to the predetermined location via the hot water discharge passage 20. Since the hot water discharged from the hot water outlet 20 is sent at a high pressure by the transport means 23, even if the pressure loss due to the positional relationship between the bath 21 and the device or the installation condition such as the pipe length of the hot water outlet 20 changes to the separator 19, The hot water does not flow backward and the flow rate of the hot water to be supplied does not change remarkably, so that the hot water can be stably supplied. Further, by circulating a large amount of hot water in the separator 19 using the transporting means 23, a large amount of combustion gas can be introduced into the circulation circuit 22, and the carbon dioxide concentration in the hot water discharged from the hot water outlet 20 is increased. You can Further, since the separator 19 is connected to the discharge passage 25 and is open to the atmosphere, the hot water supply passage 17 is cut off from the hot water stored in the separator 19, and the hot water supply passage 17 is cut off.
Even if the pressure becomes negative, the hot water containing carbonic acid stored in the separator 19 does not flow back into the hot water supply passage 17.

【0040】図3は本発明の炭酸泉製造装置の第3の技
術手段を給湯機に応用した場合の第3の実施例であり、
上記第1および第2の技術手段と異なる点は、給湯路1
7の上流の給水路14に湯の流量を検知する入側流量検
知手段15を設け、出湯路20に湯の流量を検知する出
側流量検知手段28を設け、出湯路20に湯の流量を調
節する流量調節手段29を設け、入側流量検知手段15
と出側流量検知手段28で得られた情報に基づいて流量
調節手段29を制御する制御手段27を設けたことであ
る。そしてこれ以外の構成は上記第1の技術手段および
第2の技術手段と同じであり、同一の符号を付して詳細
な説明を省略する。
FIG. 3 shows a third embodiment in which the third technical means of the carbonated spring manufacturing apparatus of the present invention is applied to a water heater.
The difference from the first and second technical means is that the hot water supply passage 1
7 is provided with an inlet side flow rate detecting means 15 for detecting the flow rate of hot water, an outlet side flow rate detecting means 28 for detecting the flow rate of hot water is provided in the hot water outlet path 20, and a hot water flow rate is provided in the hot water outlet path 20. Flow rate adjusting means 29 for adjusting is provided, and the inlet side flow rate detecting means 15
And the control means 27 for controlling the flow rate adjusting means 29 based on the information obtained by the outlet side flow rate detecting means 28. The other configurations are the same as those of the first technical means and the second technical means, and the same reference numerals are given and detailed description thereof will be omitted.

【0041】上記構成において、例えば、制御手段27
は、入側流量検知手段15から得られた流量と出側流量
検知手段28から得られた流量が同じになるように、流
量調節手段29を制御する。これにより、給水路14並
びに給湯路17から分離器19に供給される流量と、分
離器19から出湯路20を介して出湯する流量を同じに
することにより、分離器19内の水面を一定に保つとと
もに、出湯流量の変動を無くし、安定した出湯を行なう
ことが出来る。さらに循環回路22内を流れる流量を安
定にさせることにより、混合器24に導入されるガスの
流量を安定化させて湯中の炭酸濃度を安定させることが
出来る。
In the above configuration, for example, the control means 27
Controls the flow rate adjusting means 29 so that the flow rate obtained from the inlet side flow rate detecting means 15 and the flow rate obtained from the outlet side flow rate detecting means 28 become the same. As a result, the flow rate of water supplied from the water supply passage 14 and the hot water supply passage 17 to the separator 19 is made equal to that of the hot water discharged from the separator 19 via the hot water discharge passage 20, so that the water surface in the separator 19 is kept constant. It is possible to keep the temperature stable and to eliminate the fluctuation of the flow rate of the hot water, and to perform the stable hot water discharge. Further, by stabilizing the flow rate in the circulation circuit 22, the flow rate of the gas introduced into the mixer 24 can be stabilized and the carbon dioxide concentration in the hot water can be stabilized.

【0042】図4は本発明の炭酸泉製造装置の第4の技
術手段を給湯機に応用した場合の第4実施例であり、上
記第1および第2の技術手段と異なる点は、分離器19
に分離器19内に貯った湯の水位を検知する水位検知手
段30を設け、出湯路20に湯の流量を調節する流量調
節手段29を設け、水位検知手段30から得られた情報
に基づいて流量調節手段29を制御する制御手段27を
設けたことである。そしてこれ以外の構成は上記第1の
技術手段および第2の技術手段と同じであり、同一の符
号を付して詳細な説明を省略する。
FIG. 4 shows a fourth embodiment in which the fourth technical means of the carbonated spring producing apparatus of the present invention is applied to a water heater, and the difference from the first and second technical means is that the separator 19 is used.
Is provided with a water level detecting means 30 for detecting the water level of the hot water stored in the separator 19, and a flow rate adjusting means 29 for adjusting the flow rate of the hot water is provided in the hot water outlet passage 20, based on the information obtained from the water level detecting means 30. That is, the control means 27 for controlling the flow rate adjusting means 29 is provided. The other configurations are the same as those of the first technical means and the second technical means, and the same reference numerals are given and detailed description thereof will be omitted.

【0043】上記構成において、制御手段27は、水位
検知手段30で得られた水位が所定の範囲内に治まるよ
うに、流量調節手段29を制御する。例えば水位が上が
り過ぎれば、流量調節手段29の開度を増して、出湯路
20を介して分離器19から出る湯の流量を増加させ、
分離器19内の湯の水位が下がるように調節する。また
水位が下がり過ぎれば、流量調節手段29の開度を減ら
して、出湯路20を介して分離器19から出る湯の流量
を減少させ、分離器19内の湯の水位が上がるように調
節する。例えば、低水圧地域などでは分離器19に供給
される湯の流量が少ないため分離器19内の水位が下が
り、循環回路22や出湯路20にガスが混入することが
ある。しかし、分離器19内の水位が所定の値より下が
ったことを水位検知手段30で検知した場合には、出湯
路20から流れ出る湯の流量を少なくするように流量調
節手段29を制御することにより、水位が所定値より下
がることを抑え、循環回路22や出湯路20にガスが混
入することが防止出来、装置使用上の安全性を確保する
ことが出来る。
In the above structure, the control means 27 controls the flow rate adjusting means 29 so that the water level obtained by the water level detecting means 30 falls within a predetermined range. For example, if the water level rises too much, the opening degree of the flow rate adjusting means 29 is increased to increase the flow rate of hot water discharged from the separator 19 via the hot water discharge passage 20,
The water level of the hot water in the separator 19 is adjusted to lower. If the water level drops too much, the opening degree of the flow rate adjusting means 29 is reduced to decrease the flow rate of the hot water discharged from the separator 19 via the hot water outlet passage 20, and the hot water level in the separator 19 is adjusted to rise. . For example, in a low water pressure area or the like, since the flow rate of the hot water supplied to the separator 19 is low, the water level in the separator 19 may drop, and the circulation circuit 22 and the hot water outlet 20 may be mixed with gas. However, when the water level detecting means 30 detects that the water level in the separator 19 has dropped below a predetermined value, the flow rate adjusting means 29 is controlled so as to reduce the flow rate of the hot water flowing out of the hot water outlet passage 20. Further, it is possible to prevent the water level from falling below a predetermined value, prevent the gas from being mixed in the circulation circuit 22 and the hot water passage 20, and ensure the safety in using the device.

【0044】図5は本発明の炭酸泉製造装置の第5の技
術手段を給湯機に応用した場合の第5の実施例であり、
上記第1および第2の技術手段と異なる点は、分離器1
9に分離器19内に貯った湯の水位を検知する水位検知
手段30を設け、給湯路17に湯の流量を調節する流量
調節手段29を設け、水位検知手段30から得られた情
報に基づいて流量調節手段29を制御する制御手段27
を設けたことである。そしてこれ以外の構成は上記第1
の技術手段および第2の技術手段と同じであり、同一の
符号を付して詳細な説明を省略する。
FIG. 5 is a fifth embodiment in which the fifth technical means of the carbonated spring producing apparatus of the present invention is applied to a water heater.
The difference from the first and second technical means is that the separator 1
9 is provided with a water level detecting means 30 for detecting the water level of the hot water stored in the separator 19, and a flow rate adjusting means 29 for adjusting the flow rate of the hot water is provided in the hot water supply passage 17, and the information obtained from the water level detecting means 30 is used. Control means 27 for controlling the flow rate adjusting means 29 based on
Is provided. And other configurations are the same as those of the first
This is the same as the technical means and the second technical means, and the same reference numerals are given and detailed description thereof will be omitted.

【0045】上記構成において、制御手段27は、水位
検知手段30で得られた水位が所定の範囲内に治まるよ
うに、流量調節手段29を制御する。例えば水位が上が
り過ぎれば、流量調節手段29の開度を減少させて、給
湯路17を介して分離器19に入る湯の流量を減少さ
せ、分離器19内の湯の水位が下がるように調節する。
また水位が下がり過ぎれば、流量調節手段29の開度を
増加させて、給湯路17から分離器19に入る湯の流量
を増加させ、分離器19内の湯の水位が上がるように調
節する。例えば、高水圧地域などでは分離器19に供給
される湯の流量が多いため分離器19内の水位が上が
り、排出路25を介して炭酸を含んだ湯が溢れ出てしま
うことがある。しかし、分離器19内の水位が所定の値
より上がったことを水位検知手段30で検知した場合に
は、給湯路17から分離器19に供給される湯の流量を
少なくするように流量調節手段29を制御することによ
り、水位が所定値より上がることを抑え、排出路25を
介して湯が溢れ出ることが防止出来、装置使用上の安全
性を確保することが出来る。
In the above structure, the control means 27 controls the flow rate adjusting means 29 so that the water level obtained by the water level detecting means 30 falls within a predetermined range. For example, if the water level rises too much, the opening degree of the flow rate adjusting means 29 is decreased to decrease the flow rate of the hot water entering the separator 19 via the hot water supply passage 17, and the hot water level in the separator 19 is adjusted to be lowered. To do.
If the water level falls too low, the opening degree of the flow rate adjusting means 29 is increased to increase the flow rate of the hot water entering the separator 19 from the hot water supply passage 17 and the hot water level in the separator 19 is adjusted to rise. For example, in a high water pressure area or the like, since the flow rate of hot water supplied to the separator 19 is large, the water level in the separator 19 may rise, and hot water containing carbonic acid may overflow via the discharge path 25. However, when the water level detecting means 30 detects that the water level in the separator 19 has risen above a predetermined value, the flow rate adjusting means reduces the flow rate of hot water supplied from the hot water supply passage 17 to the separator 19. By controlling 29, it is possible to prevent the water level from rising above a predetermined value, prevent hot water from overflowing through the discharge passage 25, and ensure safety in using the device.

【0046】[0046]

【発明の効果】以上のように本発明の炭酸泉製造装置に
よれば、次のような効果が得られる。
As described above, according to the carbonated spring producing apparatus of the present invention, the following effects can be obtained.

【0047】請求項1記載の発明によれば、搬送手段を
用いて分離器内の湯を大量に循環させることにより、循
環回路中に大量の燃焼ガスを導入することが出来、出湯
路から出湯する湯中の炭酸濃度を高めることが出来、入
浴等により高い血流増加作用を得ることが出来る。また
分離器を排出路を介して大気開放し、給湯路と分離器を
縁切りした構成をとることにより、給湯路に炭酸を含ん
だ湯が逆流することを防止し、衛生上の安全性を確保す
ることが出来る。
According to the first aspect of the present invention, a large amount of combustion gas can be introduced into the circulation circuit by circulating a large amount of hot water in the separator using the conveying means, and the hot water is discharged from the hot water discharge passage. The concentration of carbon dioxide in hot water can be increased, and a high blood flow increasing action can be obtained by taking a bath or the like. In addition, by opening the separator to the atmosphere through the discharge path and separating the hot water supply path from the separator, it is possible to prevent backflow of hot water containing carbonic acid into the hot water supply path, ensuring hygienic safety. You can do it.

【0048】請求項2記載の発明によれば、搬送手段を
用いて分離器内の湯を大量に循環させることにより、循
環回路中に大量の燃焼ガスを導入することが出来、出湯
路から出湯する湯中の炭酸濃度を高めることが出来、入
浴等により高い血流増加作用を得ることが出来る。また
分離器を排出路を介して大気開放し、給湯路と分離器を
縁切りした構成をとることにより、給湯路に炭酸を含ん
だ湯が逆流することを防止し、衛生上の安全性を確保す
ることが出来る。さらに出湯路から出湯する湯は搬送手
段により高圧で送られるため、浴槽と装置の位置関係や
出湯路の配管長さ等の設置状況による圧損が多少変化し
ても、分離器へ湯が逆流したり、供給する湯の流量が著
しく変化することが無く、安定した湯の供給が出来る。
According to the second aspect of the invention, a large amount of combustion gas can be introduced into the circulation circuit by circulating a large amount of hot water in the separator by using the conveying means, and the hot water is discharged from the hot water discharge passage. The concentration of carbon dioxide in hot water can be increased, and a high blood flow increasing action can be obtained by taking a bath or the like. In addition, by opening the separator to the atmosphere through the discharge path and separating the hot water supply path from the separator, it is possible to prevent backflow of hot water containing carbonic acid into the hot water supply path, ensuring hygienic safety. You can do it. Furthermore, since the hot water discharged from the hot water outlet is sent at a high pressure by the transport means, even if the pressure loss due to the positional relationship between the bathtub and the device and the installation conditions such as the length of the hot water outlet pipe changes, the hot water will flow back to the separator. In addition, the flow rate of hot water to be supplied does not change significantly, and stable hot water supply can be achieved.

【0049】請求項3記載の発明によれば、例えば、給
湯路を介して分離器に入ってくる湯の流量と、出湯路を
介して分離器から出ていく湯の流量が同じになるように
出湯路に設けた流量調節手段を制御することにより、分
離器内の水面を一定に保つとともに、出湯される流量の
変動を無くし、循環回路内を流れる流量を安定にさせる
ことにより、混合器に導入されるガスの流量を安定化さ
せて湯中の炭酸濃度を安定させることが出来る。
According to the third aspect of the invention, for example, the flow rate of the hot water entering the separator via the hot water supply passage and the flow rate of the hot water exiting from the separator via the hot water discharge passage are the same. By controlling the flow rate adjusting means provided in the hot water outlet in the mixer, the water level in the separator is kept constant, fluctuations in the flow rate of hot water discharged are eliminated, and the flow rate in the circulation circuit is stabilized, thereby stabilizing the mixer. The concentration of carbon dioxide in the hot water can be stabilized by stabilizing the flow rate of the gas introduced into.

【0050】請求項4記載の発明によれば、例えば、低
水圧地域などでは分離器に供給される湯の流量が少ない
ため分離器内の水位が下がり、循環路や出湯路にガスが
混入することが考えられる。しかし、分離器内の水位が
所定の値より下がったことを水位検知手段で検知した場
合には、出湯路から流れ出る湯の流量を少なくするよう
に流量調節手段を制御することにより、水位が所定値よ
り下がることを抑え、循環路や出湯路にガスが混入する
ことが防止出来、装置使用上の安全性を確保することが
出来る。
According to the fourth aspect of the invention, for example, in a low water pressure area or the like, since the flow rate of the hot water supplied to the separator is small, the water level in the separator is lowered and gas is mixed in the circulation path and the hot water exit path. It is possible. However, when the water level detecting means detects that the water level in the separator has dropped below a predetermined value, the flow level adjusting means is controlled so as to reduce the flow rate of the hot water flowing out of the hot water outlet passage, thereby controlling the water level to a predetermined level. It is possible to suppress falling below the value, prevent gas from mixing in the circulation path or the hot water supply path, and ensure safety in using the device.

【0051】請求項5記載の発明によれば、例えば、高
水圧地域などでは分離器に供給される湯の流量が多いた
め分離器内の水位が上がり、排出路を介して炭酸を含ん
だ湯が溢れ出てしまうことが考えられる。しかし、分離
器内の水位が所定の値より上がったことを水位検知手段
で検知した場合には、給湯路から分離器に供給される湯
の流量を少なくするように流量調節手段を制御すること
により、水位が所定値より上がることを抑え、排出路を
介して湯が溢れ出ることが防止出来、装置使用上の安全
性を確保することが出来る。
According to the fifth aspect of the invention, for example, in a high water pressure area or the like, since the flow rate of the hot water supplied to the separator is large, the water level in the separator rises and the hot water containing carbonic acid is discharged through the discharge passage. Is likely to overflow. However, when the water level detecting means detects that the water level in the separator rises above a predetermined value, the flow rate adjusting means should be controlled so as to reduce the flow rate of hot water supplied from the hot water supply passage to the separator. Thus, it is possible to prevent the water level from rising above a predetermined value, prevent the hot water from overflowing through the discharge path, and ensure the safety in using the device.

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

【図1】本発明の炭酸泉製造装置を給湯機に応用した場
合の第1の実施例の要部構成図
FIG. 1 is a configuration diagram of essential parts of a first embodiment when a carbonated spring manufacturing apparatus of the present invention is applied to a water heater.

【図2】本発明の炭酸泉製造装置を給湯機に応用した場
合の第2の実施例の要部構成図
FIG. 2 is a configuration diagram of essential parts of a second embodiment when the carbonated spring manufacturing apparatus of the present invention is applied to a water heater.

【図3】本発明の炭酸泉製造装置を給湯機に応用した場
合の第3の実施例の要部構成図
FIG. 3 is a configuration diagram of essential parts of a third embodiment in which the carbonated spring manufacturing apparatus of the present invention is applied to a water heater.

【図4】本発明の炭酸泉製造装置を給湯機に応用した場
合の第4の実施例の要部構成図
FIG. 4 is a configuration diagram of essential parts of a fourth embodiment when the carbonated spring manufacturing apparatus of the present invention is applied to a water heater.

【図5】本発明の炭酸泉製造装置を給湯機に応用した場
合の第5の実施例の要部構成図
FIG. 5 is a configuration diagram of essential parts of a fifth embodiment in which the carbonated spring manufacturing apparatus of the present invention is applied to a water heater.

【図6】従来の炭酸泉製造装置の要部構成図FIG. 6 is a configuration diagram of main parts of a conventional carbonated spring manufacturing device.

【符号の説明】[Explanation of symbols]

13 導入路 15 入側流量検知手段 17 給湯路 19 分離器 20 出湯路 22 循環回路 23 搬送手段 24 混合器 25 排出路 27 制御手段 28 出側流量検知手段 29 流量調節手段 30 水位検知手段 13 introduction path 15 inlet side flow rate detecting means 17 hot water supply channel 19 separator 20 hot water channel 22 circulation circuit 23 conveying means 24 mixer 25 discharge channel 27 control means 28 outlet side flow rate detecting means 29 flow rate adjusting means 30 water level detecting means

───────────────────────────────────────────────────── フロントページの続き (72)発明者 古米 幸郎 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Yukio Furumai 1006 Kadoma, Kadoma City, Osaka Prefecture Matsushita Electric Industrial Co., Ltd.

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】湯を供給する給湯路と、二酸化炭素が含ま
れたガスを供給する導入路と、前記給湯路に接続され
た、湯とガスを分離する分離器と、前記分離器内の湯を
循環させる循環回路と、前記循環回路の途中に設けられ
前記循環回路内の湯を搬送する搬送手段と、前記循環回
路の前記搬送手段の下流側に設けられ、前記導入路から
供給されたガスを前記循環回路中に導入し溶解させる混
合器と、前記分離器から湯を出湯する出湯路と、前記分
離器から分離したガスを排出する排出路とを備えた炭酸
泉製造装置。
1. A hot water supply passage for supplying hot water, an introduction passage for supplying a gas containing carbon dioxide, a separator connected to the hot water supply passage for separating hot water and gas, and the inside of the separator. A circulation circuit for circulating hot water, a conveying means provided in the middle of the circulation circuit for conveying the hot water in the circulation circuit, a circulation circuit provided downstream of the conveyance means of the circulation circuit, and supplied from the introduction path. A carbonated spring manufacturing apparatus comprising: a mixer for introducing gas into the circulation circuit to dissolve it; a hot water outlet for discharging hot water from the separator; and a discharge passage for discharging the gas separated from the separator.
【請求項2】湯を供給する給湯路と、二酸化炭素が含ま
れたガスを供給する導入路と、前記給湯路に接続され
た、湯とガスを分離する分離器と、前記分離器内の湯を
循環させる循環回路と、前記循環回路の途中に設けられ
前記循環回路内の湯を搬送する搬送手段と、前記循環回
路の前記搬送手段の下流側に設けられ、前記導入路から
供給されたガスを前記循環回路中に導入し溶解させる混
合器と、前記搬送手段と前記混合器の間の前記循環回路
から分岐し、前記循環回路から湯を出湯する出湯路と、
前記分離器から分離したガスを排出する排出路とを備え
た炭酸泉製造装置。
2. A hot water supply passage for supplying hot water, an introduction passage for supplying a gas containing carbon dioxide, a separator connected to the hot water supply passage for separating hot water and gas, and the inside of the separator. A circulation circuit for circulating hot water, a conveying means provided in the middle of the circulation circuit for conveying the hot water in the circulation circuit, a circulation circuit provided downstream of the conveyance means of the circulation circuit, and supplied from the introduction path. A mixer that introduces gas into the circulation circuit and dissolves it, and a tapping channel that branches from the circulation circuit between the conveying means and the mixer, and taps hot water from the circulation circuit.
An apparatus for producing carbonated spring, comprising a discharge passage for discharging the gas separated from the separator.
【請求項3】給湯路の途中に、湯の流量を検知する入側
流量検知手段を設け、出湯路の途中に、湯の流量を検知
する出側流量検知手段を設け、出湯路の途中に、湯の流
量を調節する流量調節手段を設け、前記入側流量検知手
段並びに前記出側流量検知手段からの信号に応じて前記
流量調節手段を制御する制御手段を設けた請求項1また
は請求項2記載の炭酸泉製造装置。
3. An inlet flow rate detecting means for detecting the flow rate of hot water is provided in the hot water supply path, an outlet flow rate detecting means for detecting the flow rate of hot water is provided in the hot water supply path, and an outlet flow rate detecting means is provided in the hot water supply path. 3. The method according to claim 1, further comprising flow rate adjusting means for adjusting the flow rate of the hot water, and control means for controlling the flow rate adjusting means according to signals from the inlet side flow rate detecting means and the outlet side flow rate detecting means. Carbonated spring production device described in 2.
【請求項4】分離器の内部に貯った湯の水位を検知する
水位検知手段を設け、出湯路の途中に、湯の流量を調節
する流量調節手段を設け、前記水位検知手段からの信号
に応じて前記流量調節手段を制御する制御手段を設けた
請求項1または請求項2記載の炭酸泉製造装置。
4. A water level detecting means for detecting the water level of the hot water stored in the separator is provided, and a flow rate adjusting means for adjusting the flow rate of the hot water is provided in the middle of the hot water discharge passage, and a signal from the water level detecting means is provided. The carbonated spring manufacturing apparatus according to claim 1 or 2, further comprising control means for controlling the flow rate adjusting means in accordance with the above.
【請求項5】分離器の内部に貯った湯の水位を検知する
水位検知手段を設け、給湯路の途中に、湯の流量を調節
する流量調節手段を設け、前記水位検知手段からの信号
に応じて前記流量調節手段を制御する制御手段を設けた
請求項1または請求項2記載の炭酸泉製造装置。
5. A water level detecting means for detecting the water level of the hot water stored inside the separator is provided, and a flow rate adjusting means for adjusting the flow rate of the hot water is provided in the middle of the hot water supply passage, and a signal from the water level detecting means is provided. The carbonated spring manufacturing apparatus according to claim 1 or 2, further comprising control means for controlling the flow rate adjusting means in accordance with the above.
JP11819193A 1993-05-20 1993-05-20 Carbonated spring production equipment Expired - Fee Related JP3237301B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11819193A JP3237301B2 (en) 1993-05-20 1993-05-20 Carbonated spring production equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11819193A JP3237301B2 (en) 1993-05-20 1993-05-20 Carbonated spring production equipment

Publications (2)

Publication Number Publication Date
JPH06331211A true JPH06331211A (en) 1994-11-29
JP3237301B2 JP3237301B2 (en) 2001-12-10

Family

ID=14730416

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11819193A Expired - Fee Related JP3237301B2 (en) 1993-05-20 1993-05-20 Carbonated spring production equipment

Country Status (1)

Country Link
JP (1) JP3237301B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2021182391A1 (en) * 2020-03-09 2021-09-16 株式会社マツバラ Device for producing sterile water, and method for producing sterile water

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2021182391A1 (en) * 2020-03-09 2021-09-16 株式会社マツバラ Device for producing sterile water, and method for producing sterile water

Also Published As

Publication number Publication date
JP3237301B2 (en) 2001-12-10

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