JP3084853B2 - Carbonated spring production equipment - Google Patents
Carbonated spring production equipmentInfo
- Publication number
- JP3084853B2 JP3084853B2 JP03308768A JP30876891A JP3084853B2 JP 3084853 B2 JP3084853 B2 JP 3084853B2 JP 03308768 A JP03308768 A JP 03308768A JP 30876891 A JP30876891 A JP 30876891A JP 3084853 B2 JP3084853 B2 JP 3084853B2
- Authority
- JP
- Japan
- Prior art keywords
- combustion gas
- hot water
- water supply
- carbon dioxide
- concentration
- 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.)
- Expired - Fee Related
Links
Landscapes
- Bathtub Accessories (AREA)
- Treating Waste Gases (AREA)
- Gas Separation By Absorption (AREA)
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、炭酸ガスを含む燃焼ガ
スを溶解させて炭酸ガスを含んだ湯または水を得る炭酸
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 manufacturing apparatus for dissolving a combustion gas containing carbon dioxide gas to obtain hot water or water containing carbon dioxide gas.
【0002】[0002]
【従来の技術】従来この種の炭酸泉製造給湯装置には、
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、波線は燃焼ガスの流れ方向を示している。2. Description of the Related Art Conventionally, this type of carbonated spring manufacturing and hot water supply apparatus includes:
There was one as shown in FIG. In the figure, solid arrows indicate the flow direction of hot water and dashed lines indicate the flow direction of combustion gas.
【0003】鉛直方向上方の一端を大気解放した燃焼室
1と、燃焼室1の側面に設けられ水平方向に火炎fを形
成する燃焼手段2と、この燃焼手段2より下方の燃焼室
1に連接した湯を貯めておく貯湯室3と、燃焼室1内の
上方より下方に水を供給する給水路4と、貯湯室3に貯
った湯を所定の場所に供給するため貯湯室3に接続され
た給湯路5と、給湯路5の途中に設けた搬送装置6から
構成されている。そして水は給水路4を通って燃焼室1
内部に吐出され、燃焼手段2で形成された火炎fと直接
接触して熱交換されるとともに燃焼ガス中の二酸化炭素
が溶解した湯となる。湯は鉛直下方に落下し貯湯室3に
貯った後、搬送装置6により給湯路5を介して所定の場
所に供給されるようになっていた。[0003] A combustion chamber 1 whose upper end in the vertical direction is open to the atmosphere, a combustion means 2 provided on a side surface of the combustion chamber 1 for forming a flame f in a horizontal direction, and a combustion chamber 1 below the combustion means 2 are connected. A hot water storage chamber 3 for storing hot water, a water supply passage 4 for supplying water downward from above in the combustion chamber 1, and a hot water storage chamber 3 for supplying hot water stored in the hot water storage chamber 3 to a predetermined location. A hot water supply path 5 is provided, and a transport device 6 provided in the middle of the hot water supply path 5. And the water passes through the water supply channel 4 and the combustion chamber 1
It is discharged into the inside, and is brought into direct contact with the flame f formed by the combustion means 2 to exchange heat and become hot water in which carbon dioxide in the combustion gas is dissolved. The hot water falls vertically downward and is stored in the hot water storage chamber 3, and then supplied to a predetermined location by the transport device 6 via the hot water supply path 5.
【0004】[0004]
【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、貯湯室3を有するとともに、貯湯室3
に貯った湯を搬送するための搬送装置6が必要となり非
常に機器容積が大きくなる。また水道と縁切りをしてい
るため2階等への給湯の際には流量が不足し、それを補
うために大流量の搬送装置6が必要であった。また燃焼
室1に水を噴霧し熱交換を行なっているので燃焼が非常
に不安定となる。また燃焼室1内の大気圧下で燃焼ガス
中の二酸化炭素を水に溶解させているので、溶解効率が
低く溶存炭酸濃度も低くなる。さらに供給される水の流
量に応じて湯中の炭酸ガス濃度が変化するという課題が
あった。However, in the above configuration, the hot water storage room 3 is provided and the hot water storage room 3 is provided.
A transport device 6 for transporting the hot water stored in the apparatus is required, and the equipment volume becomes very large. In addition, the flow rate is insufficient at the time of hot water supply to the second floor or the like because it is cut off from the water supply, and a large flow rate transfer device 6 is required to compensate for the shortage. Further, since water is sprayed into the combustion chamber 1 to perform heat exchange, combustion becomes extremely unstable. Further, since carbon dioxide in the combustion gas is dissolved in water under the atmospheric pressure in the combustion chamber 1, the dissolving efficiency is low and the dissolved carbon dioxide concentration is low. Further, there is a problem that the concentration of carbon dioxide in the hot water changes according to the flow rate of the supplied water.
【0005】本発明は、かかる従来の課題を解消するも
ので、コンパクトかつ安価で、しかも湯または水中の溶
存炭酸濃度を高くし医学的な効果である血流増加作用を
もたらす高濃度の炭酸泉を作るとともに、湯または水中
の溶存炭酸ガスの濃度を一定に保つことを目的としてい
る。SUMMARY OF THE INVENTION The present invention solves the above-mentioned conventional problems, and provides a high-concentration carbonated spring which is compact and inexpensive and has a high dissolved carbonic acid concentration in hot water or water and has a medical effect of increasing blood flow. The purpose is to keep the concentration of dissolved carbon dioxide in hot water or water constant.
【0006】[0006]
【課題を解決するための手段】上記課題を解決するため
に、本発明の炭酸泉製造装置の第1手段は、湯または水
が通る給水給湯路と、二酸化炭素を含む燃焼ガスが通る
燃焼ガス導入路と、燃焼ガス導入路から供給された燃焼
ガスを給水給湯路内に導入し燃焼ガス中の二酸化炭素を
溶解する給水給湯路に設けた燃焼ガス導入手段と、湯ま
たは水と湯または水に溶解しなかった残留燃焼ガスを分
離する燃焼ガス導入手段の給水給湯路下流側に設けた気
液分離手段と、気液分離手段において分離した残留燃焼
ガスを気液分離手段から排出する排出路と、燃焼ガス導
入路内を流れる燃焼ガスを強制的に搬送する燃焼ガス導
入路に設けた燃焼ガス搬送手段と、燃焼ガス搬送手段を
制御する制御手段とを備えたものである。Means for Solving the Problems In order to solve the above problems, the first means of the carbonated spring manufacturing apparatus according to the present invention comprises a hot water supply passage through which hot water or water flows, and a combustion gas introduction through which a combustion gas containing carbon dioxide passes. And a combustion gas introduction means provided in a hot water supply path for introducing the combustion gas supplied from the combustion gas introduction path into the hot water supply path and dissolving carbon dioxide in the combustion gas, and supplying hot water or water and hot water or water. Gas-liquid separation means provided downstream of the water supply hot water supply path of the combustion gas introduction means for separating undissolved residual combustion gas, and a discharge path for discharging the residual combustion gas separated by the gas-liquid separation means from the gas-liquid separation means. A combustion gas conveying means provided in the combustion gas introduction path for forcibly conveying the combustion gas flowing in the combustion gas introduction path, and a control means for controlling the combustion gas conveying means.
【0007】本発明の炭酸泉製造装置の第2手段は、本
発明の炭酸泉製造装置の第1手段において、給水給湯路
内を流れる湯または水の流量を検知する水量検知手段を
設け、制御手段は水量検知手段からの情報に応じて燃焼
ガス搬送手段を制御するようにしたものである。The second means of the carbonated spring manufacturing apparatus of the present invention is the same as the first means of the carbonated spring manufacturing apparatus of the present invention, wherein water control means for detecting the flow rate of hot water or water flowing in the water supply hot water supply channel is provided. The combustion gas conveying means is controlled according to information from the water amount detecting means.
【0008】本発明の炭酸泉製造装置の第3手段は、本
発明の第1の炭酸泉製造装置において、燃焼ガス導入路
中を流れる燃焼ガス中の二酸化炭素の濃度検知する燃焼
ガス濃度検知手段を設け、制御手段は燃焼ガス濃度検知
手段からの情報に応じて燃焼ガス搬送手段を制御するよ
うにしたものである。The third means of the carbonated spring manufacturing apparatus according to the present invention, in the first carbonated spring manufacturing apparatus according to the present invention, further comprises a combustion gas concentration detecting means for detecting the concentration of carbon dioxide in the combustion gas flowing through the combustion gas introduction passage. The control means controls the combustion gas conveying means in accordance with information from the combustion gas concentration detecting means.
【0009】本発明の炭酸泉製造装置の第4手段は、本
発明の炭酸泉製造装置の第1手段において、給水給湯路
内を流れる湯または水に含まれる炭酸ガス濃度を検知す
る溶存炭酸ガス濃度検知手段を気液分離手段の下流側の
給水給湯路に設け、制御手段は前記溶存炭酸ガス濃度検
知手段からの情報に応じて燃焼ガス搬送手段を制御する
ようにしたものである。A fourth aspect of the carbonated spring manufacturing apparatus according to the present invention is the first aspect of the carbonated spring manufacturing apparatus according to the first aspect of the present invention, wherein the concentration of dissolved carbon dioxide is detected for detecting the concentration of carbon dioxide contained in hot water or water flowing in the water supply hot water supply passage. The means is provided in the hot water supply channel downstream of the gas-liquid separation means, and the control means controls the combustion gas conveying means in accordance with information from the dissolved carbon dioxide concentration detecting means.
【0010】[0010]
【作用】本発明は、上記の第1の手段により、二酸化炭
素を含んだ燃焼ガスは、燃焼ガス搬送手段によって、燃
焼ガス導入路から燃焼ガス導入手段に大量に搬送され
る。一方、湯または水は給水給湯路を介して燃焼ガス導
入手段に供給される。燃焼ガス導入手段において湯また
は水と燃焼ガスが混合し、熱交換するとともに、燃焼ガ
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、気液分離手段において溶
解しなかった残留燃焼ガスと炭酸ガスが溶解した湯また
は水は分離され、残留燃焼ガスは排出路を介して気液分
離手段から排出される。炭酸ガスが含まれる湯または水
は気液分離手段から出て給水給湯路を介してシャワーや
風呂等の所定の場所に供給される。制御手段は、供給す
る湯水中の溶存炭酸ガス濃度が所定の濃度になるように
燃焼ガス搬送手段を制御する。According to the first aspect of the present invention, a large amount of the combustion gas containing carbon dioxide is conveyed from the combustion gas introduction path to the combustion gas introduction means by the combustion gas conveyance means. On the other hand, hot water or water is supplied to the combustion gas introducing means via a hot water supply channel. Hot water or water is mixed with the combustion gas in the combustion gas introducing means, and heat exchange is performed. At the same time, highly water-soluble carbon dioxide in the combustion gas is dissolved to obtain hot water or water containing carbon dioxide gas. Thereafter, the residual combustion gas not dissolved and the hot water or water in which the carbon dioxide gas is dissolved are separated by the gas-liquid separation means, and the residual combustion gas is discharged from the gas-liquid separation means via the discharge path. Hot water or water containing carbon dioxide gas exits from the gas-liquid separation means and is supplied to a predetermined location such as a shower or a bath via a hot water supply channel. The control means controls the combustion gas conveying means so that the concentration of dissolved carbon dioxide in the supplied hot water becomes a predetermined concentration.
【0011】また本発明の第2の手段においては、給水
給湯路内を流れる湯または水の流量を水量検知手段で検
知し、湯または水の流量が所定の流量より多くなった場
合には、燃焼ガス導入路内を流れる燃焼ガスの流量が多
くなるように燃焼ガス搬送手段を制御し、逆に給水給湯
路内を流れる湯または水の流量が所定の流量より少なく
なった場合には、燃焼ガス導入路内を流れる燃焼ガスの
流量が少なくなるように燃焼ガス搬送手段を制御し、所
定の溶存炭酸ガス濃度の湯または水を供給する。Further, in the second means of the present invention, the flow rate of hot water or water flowing in the water supply hot water supply passage is detected by the water amount detecting means, and when the flow rate of hot water or water exceeds a predetermined flow rate, The combustion gas conveying means is controlled so that the flow rate of the combustion gas flowing in the combustion gas introduction passage increases, and conversely, if the flow rate of hot water or water flowing in the water supply hot water supply passage becomes smaller than a predetermined flow rate, the combustion The combustion gas conveying means is controlled so that the flow rate of the combustion gas flowing in the gas introduction path is reduced, and hot water or water having a predetermined dissolved carbon dioxide concentration is supplied.
【0012】また本発明の第3の手段においては、燃焼
ガス導入路内を流れる燃焼ガス中の二酸化炭素の濃度を
燃焼ガス濃度検知手段で検知し、燃焼ガス中の二酸化炭
素の濃度が所定の濃度よりも高くなった場合には、燃焼
ガス導入路内を流れる燃焼ガスの流量が少なくなるよう
に燃焼ガス搬送手段を制御し、逆に燃焼ガス中の二酸化
炭素の濃度が所定の濃度よりも低くなった場合には、燃
焼ガス導入路内を流れる燃焼ガスの流量が多くなるよう
に燃焼ガス搬送手段を制御し、所定の溶存炭酸ガス濃度
の湯または水を供給する。Further, in the third means of the present invention, the concentration of carbon dioxide in the combustion gas flowing in the combustion gas introduction path is detected by the combustion gas concentration detecting means, and the concentration of carbon dioxide in the combustion gas is determined by a predetermined value. When the concentration becomes higher than the concentration, the combustion gas conveying means is controlled so that the flow rate of the combustion gas flowing in the combustion gas introduction passage is reduced, and conversely, the concentration of the carbon dioxide in the combustion gas is lower than the predetermined concentration. When the temperature becomes low, the combustion gas conveying means is controlled so as to increase the flow rate of the combustion gas flowing in the combustion gas introduction path, and hot water or water having a predetermined dissolved carbon dioxide gas concentration is supplied.
【0013】また本発明の第4の手段においては、気液
分離手段の下流側の給水給湯路内を流れる湯または水の
溶存炭酸ガス濃度を溶存炭酸ガス濃度検知手段で検知
し、湯または水の溶存炭酸ガス濃度が所定の濃度よりも
高くなった場合には、燃焼ガス導入路内を流れる燃焼ガ
スの流量が少なくなるように燃焼ガス搬送手段を制御
し、逆に湯または水の溶存炭酸ガス濃度が所定の濃度よ
りも低くなった場合には、燃焼ガス導入路内を流れる燃
焼ガスの流量が多くなるように燃焼ガス搬送手段を制御
し、所定の溶存炭酸ガス濃度の湯また水を供給する。In a fourth aspect of the present invention, the dissolved carbon dioxide concentration detecting means detects the dissolved carbon dioxide concentration of the hot water or water flowing in the water supply hot water supply passage downstream of the gas-liquid separating means. When the concentration of dissolved carbon dioxide in the combustion gas becomes higher than a predetermined concentration, the combustion gas conveying means is controlled so that the flow rate of the combustion gas flowing in the combustion gas introduction passage is reduced, and conversely, the dissolved carbon dioxide in the hot water or water is controlled. When the gas concentration becomes lower than the predetermined concentration, the combustion gas conveying means is controlled so that the flow rate of the combustion gas flowing in the combustion gas introduction passage is increased, and hot water or water having a predetermined dissolved carbon dioxide gas concentration is supplied. Supply.
【0014】[0014]
【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、波
線矢印は燃焼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. In the drawing, solid arrows indicate the flow direction of hot and cold water, dashed arrows indicate the flow direction of combustion gas, and dashed lines indicate signal lines. The same components are denoted by the same reference numerals.
【0015】図1は、本発明の炭酸泉製造装置の第1手
段を給湯機に応用した場合の一実施例の要部切断の概略
構成図である。7は燃焼用空気を供給する燃焼ファン8
によって供給された空気と燃料搬送管9によって供給さ
れた燃料を混合し燃焼させる燃焼手段である。燃焼手段
7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。1
3は湯水が流れる給水給湯路であり、給水給湯路13の
途中に熱交換器11が設けられている。給水給湯路13
によって供給された水は熱交換器11で熱交換されて湯
となり熱交換器11から出湯される。また排気路12の
途中には、燃焼ガスの一部が流れるように燃焼ガス導入
路14が排気路12から分岐して設けられている。給水
給湯路13の熱交換器11下流側には直圧型縁切り器1
5が設けられ、給水給湯路13内を湯水が逆流する場合
は逆流を阻止し、逆流のない場合には直圧型縁切り器1
5の上流の供給圧のまま湯水を流すようにしている。直
圧型縁切り器15の下流側には燃焼ガス導入路14を介
して排気路12から燃焼ガスを導入して湯中に混入する
燃焼ガス導入手段16が設けられ、さらに燃焼ガス導入
手段16の下流側には燃焼ガスと湯を分離する気液分離
手段17が設けられている。気液分離手段17と排気路
12とは排出路18で連通されている。また燃焼ガス導
入路14の途中には燃焼ガス導入路14内を流れる燃焼
ガスを大量に燃焼ガス導入手段16に強制的に搬送する
燃焼ガス搬送手段19が設けられている。20は制御手
段であり、燃焼ガス搬送手段19を制御する。FIG. 1 is a schematic configuration diagram of a main part of one embodiment in which the first means of the carbonated spring manufacturing apparatus of the present invention is applied to a water heater. 7 is a combustion fan for supplying combustion air 8
Is a combustion means for mixing and burning the air supplied by the fuel and the fuel supplied by the fuel transfer pipe 9. A combustion chamber 10, a heat exchanger 11, and an exhaust path 12 are sequentially provided downstream from the combustion means 7 in the flow direction of the combustion gas. 1
Reference numeral 3 denotes a hot water supply channel through which hot water flows, and a heat exchanger 11 is provided in the middle of the hot water supply channel 13. Water supply hot water supply channel 13
The water supplied by the heat exchanger 11 is subjected to heat exchange in the heat exchanger 11 to become hot water, and is discharged from the heat exchanger 11. In the middle of the exhaust passage 12, a combustion gas introduction passage 14 is provided branching from the exhaust passage 12 so that a part of the combustion gas flows. The direct pressure type edger 1 is located downstream of the heat exchanger 11 in the water supply hot water supply path 13.
5 is provided to prevent backflow when hot water flows backward in the water supply / hot water supply path 13, and to prevent direct backflow when there is no backflow.
The hot and cold water is allowed to flow with the supply pressure upstream of 5. Downstream of the direct pressure type edger 15, there is provided combustion gas introduction means 16 for introducing combustion gas from the exhaust path 12 through the combustion gas introduction path 14 and mixing it into the hot water, and further downstream of the combustion gas introduction means 16. Gas-liquid separation means 17 for separating combustion gas and hot water is provided on the side. The gas-liquid separating means 17 and the exhaust path 12 are communicated by a discharge path 18. In the middle of the combustion gas introduction passage 14, there is provided a combustion gas conveying means 19 for forcibly conveying a large amount of combustion gas flowing in the combustion gas introduction passage 14 to the combustion gas introduction means 16. Reference numeral 20 denotes a control unit, which controls the combustion gas conveying unit 19.
【0016】図2において燃焼ガス導入手段14の一例
を示す。21は給湯入口で直圧型縁切り器15に連接し
ている。22は給湯出口で気液分離手段17に連接して
いる。23はノズル、24はベンチュリー、25は燃焼
ガス入口で燃焼ガス導入路14に連接している。FIG. 2 shows an example of the combustion gas introducing means 14. Reference numeral 21 denotes a hot water supply inlet which is connected to the direct pressure type edger 15. A hot water supply outlet 22 is connected to the gas-liquid separation means 17. Reference numeral 23 denotes a nozzle, 24 denotes a venturi, and 25 denotes a combustion gas inlet which is connected to the combustion gas introduction passage 14.
【0017】上記構成において、燃焼ファン8によって
供給された空気と燃料搬送管9によって供給された燃料
は燃焼手段7によって混合され燃焼室10内に火炎fを
形成する。火炎fによって生成された燃焼ガスは熱交換
器11で給水給湯路13から供給された水と熱交換が行
なわれ、燃焼ガスは冷却されて低温となり排気路12よ
り排気される。燃焼ガスの一部は燃焼ガス搬送手段19
により排気路12の途中から分岐して設けた燃焼ガス導
入路14を介して燃焼ガス導入手段16へと導かれる。
燃焼ガス導入路14内の燃焼ガスは、燃焼ガス搬送手段
19によって流量を調節されつつかつ大量に燃焼ガス導
入手段16に搬送される。In the above configuration, the air supplied by the combustion fan 8 and the fuel supplied by the fuel transfer pipe 9 are mixed by the combustion means 7 to form a flame f in the combustion chamber 10. The combustion gas generated by the flame f exchanges heat with the water supplied from the hot water supply path 13 in the heat exchanger 11, and the combustion gas is cooled to a low temperature and exhausted from the exhaust path 12. A part of the combustion gas is supplied to the combustion gas conveying means 19.
As a result, the fuel gas is guided to the combustion gas introduction means 16 via a combustion gas introduction path 14 provided in a branch from the middle of the exhaust path 12.
The combustion gas in the combustion gas introduction path 14 is conveyed in a large amount to the combustion gas introduction means 16 while the flow rate is adjusted by the combustion gas conveyance means 19.
【0018】一方熱交換器11に供給された水は湯とな
り直圧型縁切り器15に入る。直圧型縁切り器15にお
いて、給水給湯路13内を湯が逆流する場合には、逆流
が防止され、逆流のない場合には、供給された圧力を保
ちつつ給水給湯路13内を湯が流れる。その後湯は直圧
型縁切り器15の給水給湯路13下流側に設けられた燃
焼ガス導入手段16に送られる。燃焼ガス搬送手段19
によって大量に搬送された燃焼ガスは、燃焼ガス導入路
14を介して燃焼ガス導入手段16の燃焼ガス入口25
から入り、ノズル23周囲に滞留する。燃焼ガス導入手
段16では湯の供給圧によりノズル23から高速で湯が
噴出し、ベンチュリー24に入る。この際にベンチュリ
ー24はエゼクタ効果により負圧となりノズル23の周
囲の燃焼ガスがベンチュリー24に吸引される。燃焼ガ
ス搬送手段16によって強制的に燃焼ガス導入手段16
に搬送された高圧の燃焼ガスと、ノズル23とベンチュ
リー24のもたらすエゼクタ効果の2つの相乗効果によ
り、大量の燃焼ガスが給水給湯路13内の湯水に混入さ
れる。ベンチュリー24内に入った湯と燃焼ガスは、ベ
ンチュリー24内および気液分離手段17に至るまでの
給水給湯路13内で湯と直接的に接触し燃焼ガス中の水
溶性の高い二酸化炭素が湯に溶解するとともに燃焼ガス
と熱交換が行なわれる。湯に溶解しなかった燃焼ガスの
残りである残留燃焼ガスは気液分離手段17に入り湯と
分離され、気液分離手段17内の上方に滞留し、排出路
18を介して排気路12に戻る。一方、二酸化炭素が溶
解し温度の上昇した湯は気液分離手段17を出て給水給
湯路13を介してシャワーや浴槽に供給される。制御手
段20は、燃焼ガス搬送手段19を制御する。On the other hand, the water supplied to the heat exchanger 11 becomes hot water and enters the direct pressure type edger 15. In the direct pressure type edger 15, when hot water flows backward in the hot water supply channel 13, backflow is prevented. When there is no reverse flow, hot water flows in the hot water supply channel 13 while maintaining the supplied pressure. Thereafter, the hot water is sent to combustion gas introduction means 16 provided on the downstream side of the hot water supply channel 13 of the direct pressure type edger 15. Combustion gas conveying means 19
The combustion gas conveyed in a large amount by the combustion gas inlet 25 of the combustion gas introduction means 16 through the combustion gas introduction passage 14
And stays around the nozzle 23. In the combustion gas introducing means 16, the hot water is spouted from the nozzle 23 at high speed by the hot water supply pressure, and enters the venturi 24. At this time, the venturi 24 becomes negative pressure due to the ejector effect, and the combustion gas around the nozzle 23 is sucked into the venturi 24. Combustion gas introduction means 16
A large amount of combustion gas is mixed into the hot and cold water in the hot and cold water supply passage 13 due to the two synergistic effects of the high-pressure combustion gas conveyed to the nozzle and the ejector effect provided by the nozzle 23 and the venturi 24. The hot water and the combustion gas that have entered the venturi 24 come into direct contact with the hot water in the venturi 24 and in the water supply hot water supply passage 13 leading to the gas-liquid separation means 17, and the highly water-soluble carbon dioxide in the combustion gas is converted into the hot water. And heat exchange with the combustion gas is performed. Residual combustion gas, which is the remainder of the combustion gas not dissolved in the hot water, enters the gas-liquid separation means 17 and is separated from the hot water, stays in the gas-liquid separation means 17 and stays in the exhaust path 12 via the discharge path 18. Return. On the other hand, the hot water whose temperature has risen due to the dissolution of the carbon dioxide exits the gas-liquid separation means 17 and is supplied to the shower or bathtub through the water supply hot water supply path 13. The control means 20 controls the combustion gas conveying means 19.
【0019】このような構成により水道供給圧を利用し
て燃焼ガスを導入するので、従来のような搬送手段6や
貯湯室3が不要となるため、機器をコンパクトにするこ
とが出来る。また高圧の水道供給圧の下で直接燃焼ガス
を溶解するため、効率よく二酸化炭素を溶解することが
出来る。With such a configuration, the combustion gas is introduced using the water supply pressure, so that the conventional transport means 6 and hot water storage chamber 3 are not required, and the equipment can be made compact. Further, since the combustion gas is directly dissolved under a high water supply pressure, carbon dioxide can be efficiently dissolved.
【0020】また燃焼ガス導入路14を流れる燃焼ガス
の流量を燃焼ガス搬送手段19によって調節するととも
に、大量に燃焼ガスを燃焼ガス導入手段16に搬送する
ので、湯水中の溶存炭酸ガス濃度を所定の濃度に一定に
保て、かつ溶存炭酸ガス濃度を高濃度にすることが出来
る。Since the flow rate of the combustion gas flowing through the combustion gas introduction passage 14 is adjusted by the combustion gas conveying means 19 and the combustion gas is conveyed to the combustion gas introduction means 16 in large quantities, the concentration of dissolved carbon dioxide in the hot water can be adjusted to a predetermined value. , And the concentration of dissolved carbon dioxide can be increased.
【0021】得られた炭酸ガスが溶解した湯は風呂やシ
ャワーに供給され、人体に対して血流増加作用によって
保温効果、疲労回復効果、血圧安定化効果、傷治癒効果
を発揮する。さらに燃焼ガスと湯が直接接触するため、
燃焼ガス中の水蒸気の潜熱をも回収し高効率にすること
が出来る。また燃焼ガス中の二酸化炭素が溶解するた
め、地球温暖化の原因である二酸化炭素の排出を抑制す
ることが出来る。The hot water in which the carbon dioxide gas is dissolved is supplied to a bath or shower, and exerts a heat retaining effect, a fatigue recovery effect, a blood pressure stabilizing effect, and a wound healing effect on the human body by an action of increasing blood flow. Furthermore, since the combustion gas and hot water come into direct contact,
The latent heat of water vapor in the combustion gas can also be recovered and the efficiency can be increased. Further, since carbon dioxide in the combustion gas is dissolved, the emission of carbon dioxide, which causes global warming, can be suppressed.
【0022】図3は本発明の炭酸泉製造装置の第2手段
を給湯機に応用した場合の一実施例を示すもので、上記
第1の手段の実施例と異なる点は、給水給湯路13の途
中に給水給湯路13内を流れる湯水の流量を検知する水
量検知手段26を設け、水量検知手段26からの情報に
基づいて制御手段20が燃焼ガス搬送手段19を制御す
るようにしたことである。そしてこれ以外の構成は上記
第1の手段の実施例と同じである。FIG. 3 shows an embodiment in which the second 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 means is that the water supply hot water supply path 13 is provided. Water amount detection means 26 for detecting the flow rate of hot water flowing in the hot water supply path 13 is provided on the way, and the control means 20 controls the combustion gas transport means 19 based on information from the water amount detection means 26. . The other structure is the same as that of the first embodiment.
【0023】上記構成において、水量検知手段26によ
って検知された湯水の流量が所定の流量より多い場合に
は、制御手段20は、所定の流量と水量検知手段26に
よって検知された流量との差に応じて、燃焼ガス導入路
14内を流れる燃焼ガスの流量が多くなるように燃焼ガ
ス搬送手段19を制御する。逆に水量検知手段26によ
って検知された湯水の流量が所定の流量より少ない場合
には、制御手段20は、所定の流量と水量検知手段26
によって検知された流量との差に応じて、燃焼ガス導入
路14内を流れる燃焼ガスの流量が少なくなるように燃
焼ガス搬送手段19を制御する。In the above configuration, when the flow rate of hot water detected by the water amount detecting means 26 is larger than the predetermined flow rate, the control means 20 determines the difference between the predetermined flow rate and the flow rate detected by the water amount detecting means 26. Accordingly, the combustion gas conveying means 19 is controlled so that the flow rate of the combustion gas flowing in the combustion gas introduction passage 14 increases. Conversely, when the flow rate of the hot water detected by the water amount detecting means 26 is smaller than the predetermined flow rate, the control means 20 sets the predetermined flow rate and the water amount detecting means 26
The combustion gas conveying means 19 is controlled so that the flow rate of the combustion gas flowing in the combustion gas introduction path 14 decreases in accordance with the difference from the flow rate detected by the above.
【0024】このような構成により、給水給湯路13の
途中に設けた水量検知手段26によって得られた情報に
応じて燃焼ガス導入手段16の搬送する燃焼ガスの流量
を燃焼ガス搬送手段19によって調節するので、給水給
湯路13内を流れる湯水の溶存炭酸ガス濃度を所定の濃
度にすることが出来る。With such a configuration, the flow rate of the combustion gas carried by the combustion gas introduction means 16 is adjusted by the combustion gas conveyance means 19 according to the information obtained by the water amount detection means 26 provided in the middle of the water supply hot water supply passage 13. Therefore, the concentration of dissolved carbon dioxide gas in the hot and cold water flowing in the hot and cold water supply passage 13 can be set to a predetermined concentration.
【0025】図4は本発明の炭酸泉製造装置の第3手段
を給湯機に応用した場合の一実施例を示すもので、上記
第1の手段の実施例と異なる点は、燃焼ガス導入路14
の途中に燃焼ガス導入路14内を流れる燃焼ガス中の二
酸化炭素の濃度を検知する燃焼ガス濃度検知手段27を
設け、燃焼ガス濃度検知手段27からの情報に基づいて
制御手段20が燃焼ガス搬送手段19を制御するように
したことである。そしてこれ以外の構成は上記第1の手
段の実施例と同じである。FIG. 4 shows an embodiment in which the third means of the carbonated spring manufacturing apparatus of the present invention is applied to a water heater. The difference from the first embodiment is that the combustion gas introduction path 14 is different from the first embodiment.
A combustion gas concentration detecting means 27 for detecting the concentration of carbon dioxide in the combustion gas flowing through the combustion gas introduction passage 14 is provided in the middle of the process, and the control means 20 controls the combustion gas conveyance based on information from the combustion gas concentration detecting means 27. That is, the means 19 is controlled. The other structure is the same as that of the first embodiment.
【0026】上記構成において、燃焼ガス濃度検知手段
27によって検知された燃焼ガス導入路14内を流れる
燃焼ガス中の二酸化炭素の濃度が所定の濃度より少ない
場合には、制御手段20は、所定の二酸化炭素の濃度と
燃焼ガス濃度検知手段27によって検知された二酸化炭
素の濃度との差に応じて、燃焼ガス導入路14内を流れ
る燃焼ガスの流量が多くなるように燃焼ガス搬送手段1
9を制御する。逆に燃焼ガス濃度検知手段27によって
検知された燃焼ガス導入路14内を流れる燃焼ガス中の
二酸化炭素の濃度が所定の濃度より多い場合には、制御
手段20は、所定の二酸化炭素の濃度と燃焼ガス濃度検
知手段27によって検知された二酸化炭素の濃度との差
に応じて、燃焼ガス導入路14内を流れる燃焼ガスの流
量が少なくなるように燃焼ガス搬送手段19を制御す
る。In the above configuration, when the concentration of carbon dioxide in the combustion gas flowing through the combustion gas introduction path 14 detected by the combustion gas concentration detection means 27 is lower than the predetermined concentration, the control means 20 sets the predetermined concentration. In accordance with the difference between the concentration of carbon dioxide and the concentration of carbon dioxide detected by the combustion gas concentration detecting means 27, the combustion gas conveying means 1 increases the flow rate of the combustion gas flowing in the combustion gas introduction passage 14.
9 is controlled. Conversely, when the concentration of carbon dioxide in the combustion gas flowing through the combustion gas introduction passage 14 detected by the combustion gas concentration detection unit 27 is higher than the predetermined concentration, the control unit 20 sets the predetermined carbon dioxide concentration to The combustion gas conveying means 19 is controlled so that the flow rate of the combustion gas flowing in the combustion gas introduction passage 14 is reduced according to the difference from the concentration of carbon dioxide detected by the combustion gas concentration detection means 27.
【0027】このような構成により、燃焼ガス導入路1
4の途中に設けた燃焼ガス濃度検知手段27によって得
られた情報に応じて燃焼ガス導入手段16に搬送する燃
焼ガスの流量を燃焼ガス搬送手段19によって調節する
ので、給水給湯路13内を流れる湯水の溶存炭酸ガス濃
度を所定の濃度にすることが出来る。With such a configuration, the combustion gas introduction path 1
Since the flow rate of the combustion gas to be conveyed to the combustion gas introduction means 16 is adjusted by the combustion gas conveyance means 19 according to the information obtained by the combustion gas concentration detection means 27 provided in the middle of 4, the combustion gas flows through the water supply hot water supply passage 13. The dissolved carbon dioxide concentration of the hot water can be set to a predetermined concentration.
【0028】図5は本発明の炭酸泉製造装置の第4手段
を給湯機に応用した場合の一実施例を示すもので、上記
第1の手段の実施例と異なる点は、給水給湯路13内を
流れる湯水に含まれる炭酸ガスの濃度を検知する溶存炭
酸ガス濃度検知手段28を気液分離手段17の下流側の
給水給湯路13に設け、溶存炭酸ガス濃度検知手段28
からの情報に基づいて制御手段20が燃焼ガス搬送手段
19を制御するようにしたことである。そしてこれ以外
の構成は上記第1の手段の実施例と同じである。FIG. 5 shows an embodiment in which the fourth means of the carbonated spring manufacturing apparatus of the present invention is applied to a water heater. The difference from the first embodiment is that A dissolved carbon dioxide concentration detecting means 28 for detecting the concentration of carbon dioxide contained in the hot and cold water flowing in the water is provided in the hot water supply channel 13 downstream of the gas-liquid separating means 17.
The control means 20 controls the combustion gas conveying means 19 based on the information from. The other structure is the same as that of the first embodiment.
【0029】上記構成において、溶存炭酸ガス濃度検知
手段28によって検知された給水給湯路13内を流れる
湯水中の溶存炭酸ガス濃度が所定の濃度より低い場合に
は、制御手段20は、所定の溶存炭酸ガス濃度と溶存炭
酸ガス濃度検知手段28によって検知された溶存炭酸ガ
ス濃度との差に応じて、燃焼ガス導入路14内を流れる
燃焼ガスの流量が多くなるように燃焼ガス搬送手段19
を制御する。逆に溶存炭酸ガス濃度検知手段28によっ
て検知された給水給湯路13内を流れる湯水中の溶存炭
酸ガス濃度が所定の濃度より高い場合には、制御手段2
0は、所定の溶存炭酸ガス濃度と溶存炭酸ガス濃度検知
手段28によって検知された溶存炭酸ガス濃度との差に
応じて、燃焼ガス導入路14内を流れる燃焼ガスの流量
が少なくなるように燃焼ガス搬送手段19を制御する。In the above configuration, if the concentration of dissolved carbon dioxide in the hot water flowing through the water supply / water supply passage 13 detected by the dissolved carbon dioxide concentration detecting means 28 is lower than the predetermined concentration, the control means 20 sets the predetermined dissolved concentration. According to the difference between the concentration of carbon dioxide and the concentration of dissolved carbon dioxide detected by the concentration of dissolved carbon dioxide, the combustion gas transporting means 19 increases the flow rate of the combustion gas flowing in the combustion gas introduction passage 14.
Control. Conversely, if the dissolved carbon dioxide concentration in the hot water flowing through the water supply / water supply path 13 detected by the dissolved carbon dioxide concentration detecting means 28 is higher than a predetermined concentration, the control means 2
0 is set so that the flow rate of the combustion gas flowing through the combustion gas introduction passage 14 is reduced in accordance with the difference between the predetermined dissolved carbon dioxide concentration and the dissolved carbon dioxide concentration detected by the dissolved carbon dioxide concentration detecting means 28. It controls the gas transport means 19.
【0030】このような構成により、気液分離手段17
の下流側の給水給湯路13に設けた溶存炭酸ガス濃度検
知手段28によって得られた情報に応じて燃焼ガス導入
手段16に搬送する燃焼ガスの流量を、燃焼ガス搬送手
段19によって調節するので、給水給湯路13内を流れ
る湯水の溶存炭酸ガス濃度を所定の濃度にすることが出
来る。なお、上記各実施例では湯中に二酸化炭素を混合
する場合について説明したが、水中に二酸化炭素を混合
する場合にも応用できるもので、この時は図1における
バーナ7は熱交換器11を加熱しないような構造にする
必要がある。With such a configuration, the gas-liquid separation means 17
Since the flow rate of the combustion gas to be conveyed to the combustion gas introduction means 16 is adjusted by the combustion gas conveyance means 19 according to the information obtained by the dissolved carbon dioxide concentration detection means 28 provided in the water supply hot water supply path 13 on the downstream side of The dissolved carbon dioxide concentration of the hot water flowing in the hot water supply path 13 can be set to a predetermined concentration. In each of the above embodiments, the case of mixing carbon dioxide in hot water has been described. However, the present invention is also applicable to the case of mixing carbon dioxide in water. At this time, the burner 7 in FIG. The structure must not be heated.
【0031】[0031]
【発明の効果】以上のように本発明の炭酸泉製造装置に
おいては、次のような効果が得られる。 (1)給水給湯路を流れる湯または水中に直接、燃焼ガ
スを導入して二酸化炭素を溶解するため、従来の技術で
必要な貯湯室や搬送手段が不要となり、機器を非常にコ
ンパクトにすることが出来る。また湯または水の供給圧
を直接利用して湯または水を搬送出来るため搬送手段な
しで二階等への搬送が出来る。また高圧の水道供給圧の
下で直接燃焼ガスを溶解するため、効率よく二酸化炭素
を溶解することが出来る。 (2)また燃焼ガス導入路を流れる燃焼ガスの流量を燃
焼ガス搬送手段によって調節するとともに、大量に燃焼
ガスを燃焼ガス導入手段に搬送することが出来るので、
湯または水中の溶存炭酸ガス濃度を所定の濃度に一定に
保って、かつ溶存炭酸ガス濃度を高濃度にすることが出
来る。 (3)また炭酸ガスを含む湯は風呂やシャワーに供給さ
れ、湯を浴びることによって人体に対して保温効果、疲
労回復効果、血圧安定化効果、傷治癒効果を発揮する。
燃焼ガス中の二酸化炭素が溶解するため、地球温暖化の
原因である二酸化炭素の排出を削減することが出来る。
湯または水と燃焼ガスが直接接触するため、燃焼ガス中
の水蒸気の潜熱をも回収することができ高効率にするこ
とが出来る。As described above, in the carbonated spring manufacturing apparatus of the present invention, the following effects can be obtained. (1) Since the combustion gas is introduced directly into the hot water or water flowing through the hot water supply channel to dissolve the carbon dioxide, the hot water storage room and transport means required by the conventional technology become unnecessary, and the equipment is made very compact. Can be done. Also, since hot water or water can be transported directly using hot water or water supply pressure, the hot water or water can be transported to the second floor or the like without transport means. Further, since the combustion gas is directly dissolved under a high water supply pressure, carbon dioxide can be efficiently dissolved. (2) Since the flow rate of the combustion gas flowing through the combustion gas introduction path is adjusted by the combustion gas conveyance means, and the combustion gas can be conveyed to the combustion gas introduction means in a large amount,
The concentration of dissolved carbon dioxide in hot water or water can be kept constant at a predetermined concentration, and the concentration of dissolved carbon dioxide can be increased. (3) In addition, hot water containing carbon dioxide gas is supplied to a bath or shower, and by taking the hot water, the human body exerts a heat retaining effect, a fatigue recovery effect, a blood pressure stabilizing effect, and a wound healing effect.
Since the carbon dioxide in the combustion gas is dissolved, the emission of carbon dioxide, which causes global warming, can be reduced.
Since the hot water or the water and the combustion gas are in direct contact with each other, the latent heat of water vapor in the combustion gas can also be recovered, and high efficiency can be achieved.
【図1】本発明の炭酸泉製造装置を給湯機に応用した時
の一実施例の要部切断の概略構成図FIG. 1 is a schematic configuration diagram of a main part cut of an embodiment when a carbonated spring manufacturing apparatus of the present invention is applied to a water heater.
【図2】同実施例における燃焼ガス導入手段の断面図FIG. 2 is a cross-sectional view of a combustion gas introduction unit in the embodiment.
【図3】同装置の他の実施例において給水給湯路に水量
検知手段を設けた場合の要部切断の概略構成図FIG. 3 is a schematic configuration diagram of a main part cut when a water amount detecting means is provided in a water supply hot water supply channel in another embodiment of the same device.
【図4】同装置の他の実施例において燃焼ガス導入路に
燃焼ガス濃度検知手段を設けた場合の要部切断の概略構
成図FIG. 4 is a schematic configuration diagram of a main part cut when a combustion gas concentration detecting means is provided in a combustion gas introduction path in another embodiment of the same device.
【図5】同装置の他の実施例において気液分離手段の下
流側の給水給湯路に溶存炭酸ガス濃度検知手段を設けた
場合の要部切断の概略構成図FIG. 5 is a schematic configuration diagram of a main part cut in a case where a dissolved carbon dioxide concentration detecting unit is provided in a water supply hot water supply path downstream of a gas-liquid separating unit in another embodiment of the apparatus.
【図6】従来例における炭酸泉製造装置の要部切断の概
略構成図FIG. 6 is a schematic configuration diagram of cutting a main part of a carbonated spring manufacturing apparatus in a conventional example.
13 給水給湯路 14 燃焼ガス導入路 16 燃焼ガス導入手段 17 気液分離手段 18 排出路 19 燃焼ガス搬送手段 20 制御手段 26 水量検知手段 27 燃焼ガス濃度検知手段 28 溶存炭酸ガス濃度検知手段 DESCRIPTION OF SYMBOLS 13 Water supply hot water supply path 14 Combustion gas introduction path 16 Combustion gas introduction means 17 Gas-liquid separation means 18 Discharge path 19 Combustion gas conveyance means 20 Control means 26 Water amount detection means 27 Combustion gas concentration detection means 28 Dissolved carbon dioxide concentration detection means
フロントページの続き (56)参考文献 特開 昭63−242258(JP,A) 特開 昭63−242257(JP,A) 特開 平3−154616(JP,A) 特公 昭43−19814(JP,B1) 実公 昭50−20018(JP,Y1) (58)調査した分野(Int.Cl.7,DB名) B01F 1/00,3/04 Continuation of the front page (56) References JP-A-63-242258 (JP, A) JP-A-63-242257 (JP, A) JP-A-3-154616 (JP, A) JP-B-43-19814 (JP, A) , B1) Jikken 50-20018 (JP, Y1) (58) Fields studied (Int. Cl. 7 , DB name) B01F 1/00, 3/04
Claims (4)
素を含む燃焼ガスが通る燃焼ガス導入路と、前記燃焼ガ
ス導入路から供給された燃焼ガスを前記給水給湯路内に
導入し燃焼ガス中の二酸化炭素を溶解する前記給水給湯
路に設けた燃焼ガス導入手段と、湯または水と湯または
水に溶解しなかった残留燃焼ガスを分離する前記燃焼ガ
ス導入手段の前記給水給湯路下流側に設けた気液分離手
段と、前記気液分離手段において分離した残留燃焼ガス
を前記気液分離手段から排出する排出路と、前記燃焼ガ
ス導入路内を流れる燃焼ガスを強制的に前記燃焼ガス導
入手段に搬送する前記燃焼ガス導入路に設けた燃焼ガス
搬送手段と、前記燃焼ガス搬送手段を制御する制御手段
からなる炭酸泉製造装置。1. A hot water supply path through which hot water or water passes, a combustion gas introduction path through which a combustion gas containing carbon dioxide passes, and a combustion gas supplied from the combustion gas introduction path is introduced into the hot water supply path to perform combustion. Combustion gas introduction means provided in the water supply hot water supply path for dissolving carbon dioxide in gas; and hot water or water and downstream combustion combustion gas introduction means for separating residual combustion gas not dissolved in the hot water or water. Gas-liquid separation means provided on the side, a discharge passage for discharging the residual combustion gas separated by the gas-liquid separation means from the gas-liquid separation means, and a combustion gas forcibly flowing through the combustion gas introduction passage. A carbonated spring manufacturing apparatus comprising: a combustion gas conveying means provided in the combustion gas introduction path for conveying the gas to the gas introducing means; and a control means for controlling the combustion gas conveying means.
検知する水量検知手段を設け、制御手段は前記水量検知
手段からの情報に応じて燃焼ガス搬送手段を制御するよ
うにした請求項1記載の炭酸泉製造装置。2. A water supply means for detecting the flow rate of hot water or water flowing in a hot water supply channel, wherein the control means controls the combustion gas conveying means in accordance with information from the water quantity detection means. 2. The carbonated spring manufacturing apparatus according to 1.
酸化炭素の濃度を検知する燃焼ガス濃度検知手段を設
け、制御手段は前記燃焼ガス濃度検知手段からの情報に
応じて燃焼ガス搬送手段を制御するようにした請求項1
記載の炭酸泉製造装置。3. A combustion gas concentration detecting means for detecting the concentration of carbon dioxide in the combustion gas flowing in the combustion gas introduction passage, wherein the control means controls the combustion gas conveying means in accordance with information from the combustion gas concentration detecting means. 2. The method according to claim 1, wherein
The described carbonated spring manufacturing apparatus.
る炭酸ガス濃度を検知する溶存炭酸ガス濃度検知手段を
気液分離手段の下流側の給水給湯路に設け、制御手段は
前記溶存炭酸ガス濃度検知手段からの情報に応じて燃焼
ガス搬送手段を制御するようにした請求項1記載の炭酸
泉製造装置。4. A dissolved carbon dioxide concentration detecting means for detecting the concentration of carbon dioxide contained in the hot water or water flowing in the hot water supply water supply passage is provided in the water supply hot water supply passage downstream of the gas-liquid separation means. 2. The carbonated spring manufacturing apparatus according to claim 1, wherein the combustion gas conveying unit is controlled according to information from the gas concentration detecting unit.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP03308768A JP3084853B2 (en) | 1991-11-25 | 1991-11-25 | Carbonated spring production equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP03308768A JP3084853B2 (en) | 1991-11-25 | 1991-11-25 | Carbonated spring production equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH05137986A JPH05137986A (en) | 1993-06-01 |
JP3084853B2 true JP3084853B2 (en) | 2000-09-04 |
Family
ID=17985069
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP03308768A Expired - Fee Related JP3084853B2 (en) | 1991-11-25 | 1991-11-25 | Carbonated spring production equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3084853B2 (en) |
-
1991
- 1991-11-25 JP JP03308768A patent/JP3084853B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH05137986A (en) | 1993-06-01 |
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