JP3042067B2 - Water heater - Google Patents
Water heaterInfo
- Publication number
- JP3042067B2 JP3042067B2 JP3225873A JP22587391A JP3042067B2 JP 3042067 B2 JP3042067 B2 JP 3042067B2 JP 3225873 A JP3225873 A JP 3225873A JP 22587391 A JP22587391 A JP 22587391A JP 3042067 B2 JP3042067 B2 JP 3042067B2
- Authority
- JP
- Japan
- Prior art keywords
- hot water
- exhaust
- water supply
- combustion gas
- 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.)
- Expired - Fee Related
Links
Landscapes
- Control For Baths (AREA)
- Instantaneous Water Boilers, Portable Hot-Water Supply Apparatuses, And Control Of Portable Hot-Water Supply Apparatuses (AREA)
- Devices For Medical Bathing And Washing (AREA)
Description
【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を得る給湯装置に関
するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a hot water supply apparatus for dissolving combustion gas containing carbon dioxide gas to obtain hot water containing carbon dioxide gas.
【0002】[0002]
【従来の技術】従来この種の給湯装置には、図5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に示している。2. Description of the Related Art Conventionally, this type of hot water supply apparatus is as shown in FIG. The solid line arrows in the figure indicate the flow direction of hot water, and the wavy 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を有するため機器が非常に大
きくなり、貯湯室3に貯った湯を搬送するための搬送装
置6が必要となる。また燃焼ガスと水が接触する燃焼室
1内は大気圧であり、二酸化炭素の溶解度が低く湯中の
炭酸ガス濃度が低い。However, in the above configuration, since the hot water storage chamber 3 is provided, the equipment becomes very large, and the transport device 6 for transporting the hot water stored in the hot water storage chamber 3 is required. Become. The inside of the combustion chamber 1 where the combustion gas and water come into contact is at atmospheric pressure, the solubility of carbon dioxide is low, and the concentration of carbon dioxide in the hot water is low.
【0005】また供給される水の水圧が異なれば、給水
路4から供給される水の量が異なるので燃焼ガスから回
収する熱量が異なり出湯温度が変化する。また供給され
る燃料が異なれば、燃焼ガスの温度が異なるとともに燃
焼ガス中の二酸化炭素濃度が異なるので、燃焼ガスから
回収する熱量が異なるとともに供給する湯に含まれた炭
酸ガス濃度も異なってくる。If the pressure of the supplied water is different, the amount of heat recovered from the combustion gas is different because the amount of water supplied from the water supply passage 4 is different, and the tapping temperature is changed. If the supplied fuel is different, the temperature of the combustion gas is different and the concentration of carbon dioxide in the combustion gas is different. Therefore, the amount of heat recovered from the combustion gas is different and the concentration of carbon dioxide contained in the supplied hot water is also different. .
【0006】また個人の好みに応じて湯に含まれる炭酸
ガス濃度を変更したくても変更することが出来ないとい
う課題があった。Another problem is that the concentration of carbon dioxide contained in hot water cannot be changed according to personal preference, even if it is desired.
【0007】本発明は、かかる従来の課題を解消するも
ので、湯に導入する燃焼ガス量を変更することによって
湯の温度が変化しても常に使用者が望む温度の湯を安定
して供給することを第1の目的としている。The present invention has been made to solve the above-mentioned conventional problems. By changing the amount of combustion gas introduced into the hot water, even if the temperature of the hot water changes, the hot water at a temperature desired by the user is always supplied stably. The first purpose is to do so.
【0008】本発明の第2の目的は、湯に含まれる炭酸
ガス濃度を検知することにより、常に使用者が望む炭酸
ガス濃度の湯を安定して供給することである。A second object of the present invention is to stably supply hot water having a carbon dioxide gas concentration desired by a user by detecting the concentration of carbon dioxide gas contained in the hot water.
【0009】[0009]
【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、本発明の第1の給湯装置は、二酸化炭素を含
む燃焼ガスを生成する燃料を用いる燃焼手段と、燃焼手
段から排出される燃焼ガスが通る排気路と、燃焼ガスと
水を熱交換する熱交換器と、熱交換器に水を供給する給
水路と、熱交換器から湯を所定の場所に供給する給湯路
と、給湯路内に燃焼ガスを導入する排気導入手段と、排
気路から排気導入手段に燃焼ガスを供給する排気導入路
と、給湯路に導入する燃焼ガスの量を調節するため排気
導入路途中に設けた導入量調節手段と、排気導入手段の
給湯路下流側に設けた湯と燃焼ガスを分離する気液分離
手段と、気液分離手段で分離した燃焼ガスのみを吐出す
る排気吐出器と、排気吐出器から排気路に分離した燃焼
ガスを戻す排気返却路と、給水路若しくは給湯路の途中
に設けた水量を調節する水量調節手段と、気液分離手段
の給湯路下流側に設けた出湯温度を検知する出湯温度検
知手段と、出湯温度を設定する出湯温度設定手段と、温
度設定手段と出湯温度検知手段からの信号に基づいて燃
焼手段と水量調節手段と導入量調節手段とを制御する制
御手段を備えたものである。In order to achieve the first object, a first hot water supply apparatus according to the present invention comprises a combustion means using a fuel for producing a combustion gas containing carbon dioxide, and an exhaust gas from the combustion means. An exhaust path through which the combustion gas passes, a heat exchanger that exchanges heat between the combustion gas and water, a water supply path that supplies water to the heat exchanger, and a hot water supply path that supplies hot water from the heat exchanger to a predetermined location. An exhaust introduction means for introducing combustion gas into the hot water supply path, an exhaust introduction path for supplying combustion gas from the exhaust path to the exhaust introduction means, and an exhaust introduction path for adjusting the amount of combustion gas introduced into the hot water supply path. Introducing amount adjusting means provided, gas-liquid separating means for separating hot gas and combustion gas provided on the downstream side of the hot water supply path of exhaust introducing means, and an exhaust discharger for discharging only the combustion gas separated by the gas-liquid separating means, Exhaust return that returns combustion gas separated from the exhaust discharger to the exhaust path A water path adjusting means provided in the middle of the water supply path or the hot water supply path for adjusting the amount of water; a hot water temperature detecting means provided downstream of the hot water supply path of the gas-liquid separation means for detecting a hot water temperature; and setting the hot water temperature. The apparatus includes a tapping temperature setting unit, and a control unit that controls the combustion unit, the water amount adjusting unit, and the introduction amount adjusting unit based on signals from the temperature setting unit and the tapping temperature detecting unit.
【0010】また第2の目的を達成するために、本発明
の第2の給湯装置は、二酸化炭素を含む燃焼ガスを生成
する燃料を用いる燃焼手段と、燃焼手段から排出される
燃焼ガスが通る排気路と、燃焼ガスと水を熱交換する熱
交換器と、熱交換器に水を供給する給水路と、熱交換器
から湯を所定の場所に供給する給湯路と、給湯路内に燃
焼ガスを導入する排気導入手段と、排気路から排気導入
手段に燃焼ガスを供給する排気導入路と、給湯路に導入
する燃焼ガスの量を調節するため排気導入路途中に設け
た導入量調節手段と、排気導入手段の給湯路下流側に設
けた湯と燃焼ガスを分離する気液分離手段と、気液分離
手段で分離した燃焼ガスのみを吐出する排気吐出器と、
排気吐出器から排気路に分離した燃焼ガスを戻す排気返
却路と、給水路若しくは給湯路の途中に設けた水量を調
節する水量調節手段と、気液分離手段の給湯路下流側に
設けた給湯路を流れる湯に含まれる炭酸ガス濃度を検知
する炭酸濃度検知手段と、出湯する湯に含まれる炭酸ガ
ス濃度を設定する炭酸濃度設定手段と、炭酸濃度設定手
段と炭酸濃度検知手段からの信号に基づいて燃焼手段と
水量調節手段と導入量調節手段とを制御する制御手段を
備えたものである。In order to achieve the second object, a second hot water supply apparatus according to the present invention includes a combustion unit that uses a fuel that generates a combustion gas containing carbon dioxide, and a combustion gas that is discharged from the combustion unit. An exhaust passage, a heat exchanger for exchanging heat between combustion gas and water, a water supply passage for supplying water to the heat exchanger, a hot water supply passage for supplying hot water from the heat exchanger to a predetermined location, and a combustion in the hot water supply passage. Exhaust introducing means for introducing gas, an exhaust introducing path for supplying combustion gas from the exhaust path to the exhaust introducing means, and an introduction amount adjusting means provided in the exhaust introducing path for adjusting the amount of combustion gas introduced to the hot water supply path. Gas-liquid separating means for separating hot gas and combustion gas provided on the downstream side of the hot water supply path of the exhaust introducing means, and an exhaust discharger for discharging only the combustion gas separated by the gas-liquid separating means,
An exhaust return path for returning the combustion gas separated from the exhaust discharger to the exhaust path, a water amount adjusting means provided in the middle of the water supply path or the hot water supply path, and a hot water supply provided downstream of the gas-liquid separation means on the hot water supply path. Carbon dioxide concentration detecting means for detecting the concentration of carbon dioxide contained in the hot water flowing through the road, carbon dioxide concentration setting means for setting the carbon dioxide concentration contained in the hot water to be discharged, and signals from the carbon dioxide concentration setting means and the carbon dioxide concentration detecting means. It is provided with control means for controlling the combustion means, the water amount adjusting means and the introduction amount adjusting means based on the combustion means.
【0011】[0011]
【作用】本発明は、上記の第1の手段により、燃焼手段
によって二酸化炭素を含んだ燃焼ガスが生成される。燃
焼ガスは熱交換器において熱交換されて低温となって排
気路を通って排出される。途中導入量調節手段によって
流量調節された燃焼ガスの一部が排気導入路を介して排
気導入手段に導かれる。According to the present invention, the first means produces a combustion gas containing carbon dioxide by the combustion means. The combustion gas is heat-exchanged in the heat exchanger and becomes low temperature and is discharged through the exhaust passage. Part of the combustion gas whose flow rate has been adjusted by the introduction amount adjusting means on the way is guided to the exhaust introduction means via the exhaust introduction path.
【0012】一方水量調節手段によって流量を調節され
た水が、給水路を介して熱交換器に供給され、燃焼ガス
と熱交換して湯となり給湯路に入る。熱交換した湯は給
湯路途中に設けた排気導入手段によって導いた燃焼ガス
と混合し更に燃焼ガスと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
湯となる。その後気液分離手段において溶解しなかった
燃焼ガスと湯が分離され、燃焼ガスは排気吐出器から吐
出し排気返却路を介して排気路に返される。炭酸ガスが
含まれる湯は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。On the other hand, the water whose flow rate has been adjusted by the water amount adjusting means is supplied to the heat exchanger through the water supply passage, exchanges heat with the combustion gas and becomes hot water and enters the hot water supply passage. The heat-exchanged hot water is mixed with the combustion gas introduced by the exhaust gas introduction means provided in the middle of the hot water supply path, and further heat-exchanges with the combustion gas. Becomes Thereafter, the undissolved combustion gas and hot water are separated by the gas-liquid separation means, and the combustion gas is discharged from the exhaust discharger and returned to the exhaust path via the exhaust return path. Hot water containing carbon dioxide gas is supplied to a predetermined place such as a shower or a bath via a hot water supply path.
【0013】供給する湯の温度は、気液分離手段の供給
路下流側に設けた出湯温度検知手段によって検知する。
出湯温度検知手段によって検知される湯温が温度設定手
段によって設定された湯温になるように、燃焼手段、水
量調節手段、導入量調節手段を制御手段が制御する。The temperature of the hot water to be supplied is detected by a tapping temperature detecting means provided on the downstream side of the supply path of the gas-liquid separating means.
The control means controls the combustion means, the water amount adjusting means, and the introduction amount adjusting means such that the hot water temperature detected by the hot water temperature detecting means becomes the hot water temperature set by the temperature setting means.
【0014】また本発明の第2の手段においては、供給
する湯に含まれる炭酸濃度は、気液分離手段の給湯路下
流側に設けた炭酸濃度検知手段によって検知する。炭酸
濃度検知手段によって検知される濃度が濃度設定手段に
よって設定された濃度になるように、燃焼手段、水量調
節手段、導入量調節手段を制御手段が制御する。In the second means of the present invention, the concentration of carbon dioxide contained in the supplied hot water is detected by a carbon dioxide concentration detecting means provided on the downstream side of the hot water supply path of the gas-liquid separation means. The control unit controls the combustion unit, the water amount adjusting unit, and the introduction amount adjusting unit such that the concentration detected by the carbon dioxide concentration detecting unit becomes the concentration set by the concentration setting unit.
【0015】[0015]
【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. In the drawing, solid arrows indicate the flow direction of hot water, dashed arrows indicate the flow direction of exhaust gas, and dashed lines indicate signal lines. The same components are denoted by the same reference numerals.
【0016】図1は、本発明の給湯装置における一実施
例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から順番に燃焼室10と熱交換器11と排気
路12が連接して設けられている。熱交換器11には水
を供給する給水路13と熱交換器11で熱交換した湯を
所定の場所に供給する給湯路14が接続されている。給
水路13の途中には給水路13を流れる水の流量を調節
する水量調節手段15が設けられている。また燃焼ガス
の一部が流れるように排気導入路16が排気路12の途
中から分岐して設けられている。給湯路14の途中には
給水路13への逆流を阻止するとともに給水路13の供
給圧を利用出来る直圧型縁切り器17が設けられ、直圧
型縁切り器17の下流側には排気導入路16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排気導
入手段18が設けられ、さらに排気導入手段18の下流
側には燃焼ガスと湯を分離する気液分離手段19が設け
られている。気液分離手段19には残留燃焼ガスのみを
吐出する排気吐出器20が設けられ、排気吐出器20と
排気路12とは排気返却路21で連通されている。気液
分離手段19の給湯路14の下流側には給湯路14を流
れる湯の温度を検知する出湯温度検知手段22が設けら
れている。また排気導入路16の途中には排気導入手段
18に導く燃焼ガスの流量を調節する導入量調節手段2
3が設けられている。24は出湯温度を使用者が設定す
る出湯温度設定手段である。25は出湯温度設定手段2
4において設定された温度に出湯温度検知手段22で得
られる温度がなるように、燃焼手段7や水量調節手段1
5や導入量調節手段23を制御する制御手段である。FIG. 1 is a schematic configuration diagram of one embodiment of the hot water supply apparatus of the present invention. Reference numeral 7 denotes combustion means for mixing and supplying air supplied by a combustion fan 8 for supplying air for combustion and fuel supplied by a fuel transfer pipe 9.
A combustion chamber 10, a heat exchanger 11, and an exhaust passage 12 are provided in order from the combustion means 7 in order. The heat exchanger 11 is connected to a water supply path 13 for supplying water and a hot water supply path 14 for supplying hot water heat-exchanged by the heat exchanger 11 to a predetermined location. In the middle of the water supply passage 13, a water amount adjusting means 15 for adjusting the flow rate of the water flowing through the water supply passage 13 is provided. Further, an exhaust introduction path 16 is provided branching from the middle of the exhaust path 12 so that a part of the combustion gas flows. In the middle of the hot water supply path 14, a direct pressure type edging device 17 that can prevent the backflow to the water supply channel 13 and use the supply pressure of the water supply channel 13 is provided, and an exhaust introduction path 16 is provided downstream of the direct pressure type edging device 17. Exhaust gas introducing means 18 for introducing the combustion gas from the exhaust passage 12 through the exhaust passage 12 and mixing into the hot water is provided. Further, a gas-liquid separating means 19 for separating the combustion gas and the hot water is provided downstream of the exhaust gas introducing means 18. ing. The gas-liquid separation means 19 is provided with an exhaust discharger 20 for discharging only residual combustion gas, and the exhaust discharger 20 and the exhaust path 12 are connected by an exhaust return path 21. On the downstream side of the hot water supply path 14 of the gas-liquid separation means 19, there is provided a tapping temperature detecting means 22 for detecting the temperature of hot water flowing through the hot water supply path 14. In the middle of the exhaust gas introduction path 16, an introduction amount adjusting means 2 for adjusting the flow rate of the combustion gas guided to the exhaust introduction means 18.
3 are provided. Reference numeral 24 denotes tapping temperature setting means for setting tapping temperature by a user. 25 is tap water temperature setting means 2
4 so that the temperature obtained by the tapping water temperature detecting means 22 becomes the temperature set in 4.
5 and control means for controlling the introduction amount adjusting means 23.
【0017】図2において排気導入手段18の詳細を示
す。26は給湯入口で、直圧型縁切り器17に連接して
いる。27は給湯出口で、気液分離手段19に連接して
いる。28はノズル、29はベンチュリー、30は排気
入口で排気導入路16に接続している。FIG. 2 shows details of the exhaust introducing means 18. Reference numeral 26 denotes a hot water supply inlet, which is connected to the direct pressure type edger 17. 27 is a hot water supply outlet, which is connected to the gas-liquid separation means 19. Reference numeral 28 denotes a nozzle, 29 denotes a venturi, and 30 denotes an exhaust inlet connected to the exhaust introduction path 16.
【0018】図3において気液分離手段19および排気
吐出器20の詳細を示す。31はフロート、32は排気
出口で、排気返却路21に連接している。また33は排
気導入手段18の給湯出口27に連通した入口、34は
給湯路14に連接する出口である。FIG. 3 shows the details of the gas-liquid separating means 19 and the exhaust / discharge device 20. 31 is a float, 32 is an exhaust outlet, which is connected to the exhaust return path 21. Reference numeral 33 denotes an inlet connected to the hot water supply outlet 27 of the exhaust gas introducing means 18, and reference numeral 34 denotes an outlet connected to the hot water supply passage 14.
【0019】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。一方給水路13から供給された水は湯となり
給湯路14に入る。湯は途中、直圧型縁切り器17で逆
流を防止されつつ給湯路14途中に設けられた排気導入
手段18に送られる。排気導入手段18は図2に示すよ
うに、給湯入口26に連接したノズル28と、給湯出口
27に連接した給湯圧力を低下するためのベンチュリー
29からなり、ノズル28からの湯の噴出圧により導入
量調節手段23で調節された燃焼ガスの一部を排気路1
2から排気導入路16を介して導入し、ベンチュリー2
9および給湯路14内で湯と直接的に接触し燃焼ガス中
の二酸化炭素が溶解するとともに燃焼ガスと熱交換が行
なわれる。その後、湯は図3に示す気液分離手段19に
入り湯と残留燃焼ガスとに分離され、残留燃焼ガスが存
在する場合は排気吐出器20内のフロート31が下降
し、残留燃焼ガスは排気出口32より排気返却路21を
介して排気路12に返され、湯が存在する場合はフロー
ト31が上昇し排気出口32を閉塞する。二酸化炭素が
溶解し温度の上昇した湯は気液分離手段19下流に設け
られた出湯温度検知手段22によって最終的な温度の確
認が行なわれた後、給湯路14を介してシャワーや浴槽
に供給される。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 water supply passage 13 in the heat exchanger 11, and the combustion gas is cooled to a low temperature and exhausted from the exhaust passage 12. On the other hand, the water supplied from the water supply channel 13 becomes hot water and enters the hot water supply channel 14. The hot water is sent to the exhaust introducing means 18 provided in the middle of the hot water supply path 14 while the backflow is prevented by the direct pressure type edger 17 on the way. As shown in FIG. 2, the exhaust gas introducing means 18 comprises a nozzle 28 connected to a hot water supply inlet 26 and a venturi 29 connected to a hot water supply outlet 27 for reducing hot water supply pressure. A part of the combustion gas adjusted by the amount adjusting means 23 is supplied to the exhaust passage 1
2 through the exhaust introduction passage 16 and venturi 2
In the hot water supply passage 9 and the hot water supply passage 14, the carbon dioxide in the combustion gas is dissolved directly and heat exchange is performed with the combustion gas. Thereafter, the hot water enters the gas-liquid separation means 19 shown in FIG. 3 and is separated into hot water and residual combustion gas. When residual combustion gas exists, the float 31 in the exhaust discharger 20 descends, and the residual combustion gas is exhausted. The water is returned from the outlet 32 to the exhaust path 12 via the exhaust return path 21, and when hot water exists, the float 31 rises and closes the exhaust outlet 32. Hot water whose temperature has risen due to the dissolution of carbon dioxide is supplied to a shower or bathtub through a hot water supply path 14 after the final temperature is confirmed by a tapping temperature detecting means 22 provided downstream of the gas-liquid separating means 19. Is done.
【0020】出湯する湯の温度は、出湯温度設定手段2
4において使用者が設定し、出湯温度検知手段22で検
知される温度が出湯温度設定手段24において設定され
た温度になるように、燃焼手段7、燃焼ファン8、水量
調節手段15、導入量調節手段23を制御手段25が制
御する。The temperature of the hot water to be discharged is determined by a hot water temperature setting means 2
4, the combustion means 7, the combustion fan 8, the water amount adjusting means 15, the introduction amount adjustment so that the temperature detected by the tapping temperature detecting means 22 is set by the user at the tapping temperature setting means 24. The control means 25 controls the means 23.
【0021】このような構成により従来の貯湯室が不要
となるため、機器がコンパクトとなり、かつ水道圧によ
り搬送器なしで給湯できる。また高圧である水道圧下で
直接燃焼ガスを溶解するため、大気圧下より効率よく二
酸化炭素を溶解することが出来る。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
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となる。ま
た燃焼ガス中の二酸化炭素やNOxが溶解するため、地
球温暖化の原因である二酸化炭素や有害なNOxの排出
を抑制することが出来る。さらに気液分離手段の下流側
の湯の温度を検知し、使用者が設定した温度になるよう
に制御するので、出湯量、燃焼量、燃焼ガスの導入量が
変化しても安定した温度の湯を供給出来るとともに、使
用上安全性を確保することが出来る。With such a configuration, a conventional hot water storage room is not required, so that the equipment is compact and hot water can be supplied by tap water without a transporter. Further, since the combustion gas is directly dissolved under high water pressure, carbon dioxide can be dissolved more efficiently than under atmospheric pressure. The obtained 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. Furthermore, since the combustion gas and hot water come into direct contact,
The latent heat of water vapor in the combustion gas is also recovered, resulting in high efficiency. Further, since carbon dioxide and NOx in the combustion gas are dissolved, emission of carbon dioxide and harmful NOx, which cause global warming, can be suppressed. Furthermore, since the temperature of the hot water downstream of the gas-liquid separation means is detected and controlled so as to be the temperature set by the user, even if the amount of hot water discharged, the amount of combustion, and the amount of introduced combustion gas change, a stable temperature can be obtained. Hot water can be supplied and safety in use can be ensured.
【0022】図4は本発明の他の実施例を示したもの
で、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から順番
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。熱交換器11には水を供給する給水路1
3と熱交換器11で熱交換した湯を所定の場所に供給す
る給湯路14が接続されている。給水路13の途中には
給水路13を流れる水の流量を調節する水量調節手段1
5が設けられている。また燃焼ガスの一部が流れるよう
に排気導入路16が排気路12の途中から分岐して設け
られている。給湯路14の途中には給水路13への逆流
を阻止するとともに給水路13の供給圧を利用出来る直
圧型縁切り器17が設けられ、直圧型縁切り器17の下
流側には排気導入路16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排気導入手段18が設けら
れ、さらに排気導入手段18の下流側には気液分離手段
19が設けられている。気液分離手段19には残留燃焼
ガスのみを吐出する排気吐出器20が設けられ、排気吐
出器20と排気路12とは排気返却路21で連通されて
いる。気液分離手段19の給湯路14の下流側には給湯
路14を流れる湯に含まれる二酸化炭素の濃度を検知す
る炭酸濃度検知手段35が設けられている。また排気導
入路16の途中には排気導入手段18に導く燃焼ガスの
流量を調節する導入量調節手段23が設けられている。
36は出湯する湯に含まれる二酸化炭素の濃度を使用者
が設定する炭酸濃度設定手段である。25は炭酸濃度検
知手段35で得られる濃度が炭酸濃度設定手段36にお
いて設定された濃度になるように、燃焼手段7や水量調
節手段15や導入量調節手段23を制御する制御手段で
ある。FIG. 4 shows another embodiment of the present invention. Reference numeral 7 denotes a mixture of air supplied by a combustion fan 8 for supplying combustion air and fuel supplied by a fuel transfer pipe 9 for combustion. It is a combustion means. A combustion chamber 10, a heat exchanger 11, and an exhaust passage 12 are provided in order from the combustion means 7 in order. Water supply channel 1 for supplying water to heat exchanger 11
A hot water supply path 14 for supplying hot water heat-exchanged by the heat exchanger 3 and the heat exchanger 11 to a predetermined place is connected. In the middle of the water supply channel 13, a water amount adjusting means 1 for adjusting the flow rate of water flowing through the water supply channel 13.
5 are provided. Further, an exhaust introduction path 16 is provided branching from the middle of the exhaust path 12 so that a part of the combustion gas flows. In the middle of the hot water supply path 14, a direct pressure type edging device 17 that can prevent the backflow to the water supply channel 13 and use the supply pressure of the water supply channel 13 is provided, and an exhaust introduction path 16 is provided downstream of the direct pressure type edging device 17. Exhaust introducing means 18 is provided for introducing the combustion gas from the exhaust passage 12 through the exhaust passage 12 and mixing it into the hot water. Further, a gas-liquid separating means 19 is provided downstream of the exhaust introducing means 18. The gas-liquid separation means 19 is provided with an exhaust discharger 20 for discharging only residual combustion gas, and the exhaust discharger 20 and the exhaust path 12 are connected by an exhaust return path 21. On the downstream side of the hot water supply path 14 of the gas-liquid separation means 19, a carbon dioxide concentration detecting means 35 for detecting the concentration of carbon dioxide contained in the hot water flowing through the hot water supply path 14 is provided. Further, an introduction amount adjusting means 23 for adjusting the flow rate of the combustion gas guided to the exhaust introduction means 18 is provided in the exhaust introduction path 16.
Reference numeral 36 denotes a carbon dioxide concentration setting means for setting the concentration of carbon dioxide contained in the hot water to be supplied by the user. Reference numeral 25 denotes control means for controlling the combustion means 7, the water amount adjusting means 15, and the introduction amount adjusting means 23 so that the concentration obtained by the carbonic acid concentration detecting means 35 becomes the concentration set by the carbonic acid concentration setting means 36.
【0023】図2において排気導入手段18の詳細を示
す。26は給湯入口で、直圧型縁切り器17に連接して
いる。27は給湯出口で気液分離手段19に連接してい
る。28はノズル、29はベンチュリー、30は排気入
口で排気導入路16に接続している。FIG. 2 shows the details of the exhaust introducing means 18. Reference numeral 26 denotes a hot water supply inlet, which is connected to the direct pressure type edger 17. 27 is a hot water supply outlet connected to the gas-liquid separation means 19. Reference numeral 28 denotes a nozzle, 29 denotes a venturi, and 30 denotes an exhaust inlet connected to the exhaust introduction path 16.
【0024】図3において気液分離手段19および排気
吐出器20の詳細を示す。31はフロート、32は排気
出口で排気返却路21に連接している。また33は排気
導入手段18の給湯出口27に連通した入口、34は給
湯路14に連接する出口である。FIG. 3 shows details of the gas-liquid separation means 19 and the exhaust / discharge device 20. 31 is a float, and 32 is an exhaust outlet which is connected to the exhaust return path 21. Reference numeral 33 denotes an inlet connected to the hot water supply outlet 27 of the exhaust gas introducing means 18, and reference numeral 34 denotes an outlet connected to the hot water supply passage 14.
【0025】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。一方、給水路13から供給された水は湯とな
り給湯路14に入る。湯は途中、直圧型縁切り器17で
逆流を防止されつつ給湯路14途中に設けられた排気導
入手段18に送られる。排気導入手段18は図2に示す
ように、給湯入口26に連接したノズル28と、給湯出
口27に連接した給湯圧力を低下するためのベンチュリ
ー29からなり、ノズル28からの湯の噴出圧により導
入量調節手段23で調節された燃焼ガスの一部を排気路
12から排気導入路16を介して導入し、ベンチュリー
29および給湯路14内で湯と直接的に接触し燃焼ガス
中の二酸化炭素が溶解するとともに燃焼ガスと熱交換が
行なわれる。その後、湯は図3に示す気液分離手段19
に入り湯と残留燃焼ガスとに分離され、残留燃焼ガスが
存在する場合は排気吐出器20内のフロート31が下降
し、残留燃焼ガスは排気出口32より排気返却路21を
介して排気路12に返され、湯が存在する場合はフロー
ト31が上昇し排気出口32を閉塞する。二酸化炭素が
溶解し温度の上昇した湯は気液分離手段19下流に設け
られた炭酸濃度検知手段35によって湯に含まれる二酸
化炭素の濃度の確認が行なわれた後、給湯路14を介し
てシャワーや浴槽に供給される。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 water supply passage 13 in the heat exchanger 11, and the combustion gas is cooled to a low temperature and exhausted from the exhaust passage 12. On the other hand, the water supplied from the water supply channel 13 becomes hot water and enters the hot water supply channel 14. The hot water is sent to the exhaust introducing means 18 provided in the middle of the hot water supply path 14 while the backflow is prevented by the direct pressure type edger 17 on the way. As shown in FIG. 2, the exhaust gas introducing means 18 comprises a nozzle 28 connected to a hot water supply inlet 26 and a venturi 29 connected to a hot water supply outlet 27 for reducing hot water supply pressure. A part of the combustion gas adjusted by the amount adjusting means 23 is introduced from the exhaust path 12 through the exhaust introduction path 16, and comes into direct contact with hot water in the venturi 29 and the hot water supply path 14, and carbon dioxide in the combustion gas is removed. Dissolution and heat exchange with the combustion gas take place. Thereafter, the hot water is supplied to the gas-liquid separation means 19 shown in FIG.
The hot water and the residual combustion gas are separated into each other, and when the residual combustion gas exists, the float 31 in the exhaust discharger 20 descends, and the residual combustion gas is discharged from the exhaust outlet 32 through the exhaust return passage 21 through the exhaust passage 12. When there is hot water, the float 31 rises and closes the exhaust outlet 32. The temperature of the hot water in which the carbon dioxide is dissolved is raised after the concentration of carbon dioxide contained in the hot water is confirmed by the carbon dioxide concentration detecting means 35 provided downstream of the gas-liquid separation means 19, and then showered through the hot water supply path 14. And supplied to the bathtub.
【0026】出湯する湯に含まれる二酸化炭素の濃度
は、炭酸濃度設定手段36において使用者が設定し、炭
酸濃度検知手段35で検知される濃度が、炭酸濃度設定
手段36において設定された濃度になるように、燃焼手
段7、燃焼ファン8、水量調節手段15、導入量調節手
段23を制御手段25が制御する。The concentration of carbon dioxide contained in the hot water is set by the user in the carbonic acid concentration setting means 36, and the concentration detected by the carbonic acid concentration detecting means 35 is adjusted to the concentration set by the carbonic acid concentration setting means 36. The control means 25 controls the combustion means 7, the combustion fan 8, the water amount adjustment means 15, and the introduction amount adjustment means 23 so as to be as follows.
【0027】このような構成により従来の貯湯室が不要
となるため、機器がコンパクトとなり、かつ水道圧によ
り搬送器なしで給湯できる。また高圧である水道圧下で
直接燃焼ガスを溶解するため、大気圧下より効率よく二
酸化炭素を溶解することが出来る。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
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となる。ま
た燃焼ガス中の二酸化炭素やNOxが溶解するため、地
球温暖化の原因である二酸化炭素や有害なNOxの排出
を抑制することが出来る。さらに気液分離手段の下流側
の湯に含まれる二酸化炭素の濃度を検知し、使用者が設
定した濃度になるように制御するので、出湯量、燃焼
量、燃焼ガスの導入量が変化しても安定した濃度の湯を
供給出来るとともに、使用上安全性を確保することが出
来る。With such a configuration, a conventional hot water storage room is not required, so that the equipment is compact and hot water can be supplied without a transporter by tap water pressure. Further, since the combustion gas is directly dissolved under high water pressure, carbon dioxide can be dissolved more efficiently than under atmospheric pressure. The obtained 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. Furthermore, since the combustion gas and hot water come into direct contact,
The latent heat of water vapor in the combustion gas is also recovered, resulting in high efficiency. Further, since carbon dioxide and NOx in the combustion gas are dissolved, emission of carbon dioxide and harmful NOx, which cause global warming, can be suppressed. Furthermore, since the concentration of carbon dioxide contained in the hot water downstream of the gas-liquid separation means is detected and controlled so as to be the concentration set by the user, the amount of hot water discharged, the amount of combustion, and the amount of combustion gas introduced change. Can supply hot water with a stable concentration, and can secure safety in use.
【0028】[0028]
【発明の効果】以上のように、本発明の給湯装置におい
ては、次のような効果が得られる。 (1)請求項1記載の発明によれば、給湯路を流れる湯
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、従来の技術でいる貯湯器がいらず機器が非常にコン
パクトにすることが出来る。また水道圧を利用して搬送
出来るため搬送器なしで二階等への搬送が出来る。水道
圧がかかった高圧下で二酸化炭素を溶解できるため、効
率の高い溶解が出来る。また湯は風呂やシャワーに供給
され、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
素やNOxが溶解するため、地球温暖化の原因である二
酸化炭素や有害なNOxの排出を削減することが出来
る。導入量調節手段により溶解する二酸化炭素の濃度を
変化させることが出来る。湯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。さらに気液分離手段の下
流側給湯路に出湯温度検知手段を設けているので、燃焼
ガスの導入量を導入量調節手段によって変化させること
で潜熱回収量が変わっても常に使用者が欲する温度の湯
を提供することが出来る。 (2)請求項2記載の発明によれば、給湯路を流れる湯
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、従来の技術でいる貯湯器がいらず機器が非常にコン
パクトにすることが出来る。また水道圧を利用して搬送
出来るため搬送器なしで二階等への搬送が出来る。水道
圧がかかった高圧下で二酸化炭素を溶解できるため、効
率の高い溶解が出来る。また湯は風呂やシャワーに供給
され、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
素やNOxが溶解するため、地球温暖化の原因である二
酸化炭素や有害なNOxの排出を削減することが出来
る。導入量調節手段により溶解する二酸化炭素の濃度を
変化させることが出来る。湯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。さらに気液分離手段の下
流側給湯路に炭酸濃度検知手段を設けているので、水の
流量を変化させることで燃焼ガスの導入量が変化して湯
中の二酸化炭素濃度が変わっても常に使用者が欲する濃
度の湯を提供することが出来る。As described above, the hot water supply apparatus of the present invention has the following effects. (1) According to the first aspect of the present invention, since the combustion gas is introduced directly into the hot water flowing through the hot water supply path to dissolve the carbon dioxide, the equipment is very compact without the need for a hot water storage device according to the prior art. It can be. In addition, since it can be transported using tap water pressure, it can be transported to the second floor or the like without a transporter. Since carbon dioxide can be dissolved under high water pressure, high efficiency dissolution can be achieved. Hot water is supplied to baths and showers and exerts a heat retaining effect, a fatigue recovery effect, a blood pressure stabilizing effect, and a wound healing effect on the human body. Since carbon dioxide and NOx in the combustion gas are dissolved, emissions of carbon dioxide and harmful NOx, which cause global warming, can be reduced. The concentration of dissolved carbon dioxide can be changed by the introduction amount adjusting means. Since the hot water and the combustion gas are in direct contact, the latent heat of water vapor in the combustion gas can also be recovered, and high efficiency can be achieved. Furthermore, since the tap water temperature detection means is provided in the downstream hot water supply path of the gas-liquid separation means, the amount of combustion gas introduced is changed by the introduction amount adjustment means, so that even if the latent heat recovery amount changes, the temperature desired by the user is always maintained. Hot water can be provided. (2) According to the second aspect of the present invention, since the combustion gas is introduced directly into the hot water flowing through the hot water supply path to dissolve the carbon dioxide, the equipment is very compact without the need for a hot water storage device according to the prior art. It can be. In addition, since it can be transported using tap water pressure, it can be transported to the second floor or the like without a transporter. Since carbon dioxide can be dissolved under high water pressure, high efficiency dissolution can be achieved. Hot water is supplied to baths and showers and exerts a heat retaining effect, a fatigue recovery effect, a blood pressure stabilizing effect, and a wound healing effect on the human body. Since carbon dioxide and NOx in the combustion gas are dissolved, emissions of carbon dioxide and harmful NOx, which cause global warming, can be reduced. The concentration of dissolved carbon dioxide can be changed by the introduction amount adjusting means. Since the hot water and the combustion gas are in direct contact, the latent heat of water vapor in the combustion gas can also be recovered, and high efficiency can be achieved. Furthermore, since the carbon dioxide concentration detection means is provided in the hot water supply path downstream of the gas-liquid separation means, it is always used even if the flow rate of water changes the introduction amount of combustion gas and the carbon dioxide concentration in the hot water changes. Can provide hot water of the concentration desired by the person.
【図1】本発明の一実施例における給湯装置の要部欠載
の概略構成図FIG. 1 is a schematic configuration diagram of a main part of a hot water supply device according to an embodiment of the present invention;
【図2】同実施例における排気導入手段の断面図FIG. 2 is a cross-sectional view of the exhaust gas introducing means in the embodiment.
【図3】同実施例における気液分離手段および排気吐出
器の断面図FIG. 3 is a cross-sectional view of a gas-liquid separation unit and an exhaust discharger in the same embodiment.
【図4】本発明の他の実施例における給湯装置の要部欠
載の概略構成図FIG. 4 is a schematic configuration diagram of a main part of a hot water supply device according to another embodiment of the present invention, which is omitted
【図5】従来例における給湯装置の要部欠載の概略構成
図FIG. 5 is a schematic configuration diagram of a main part of a hot water supply device in a conventional example, which is not mounted.
7 燃焼手段 11 熱交換器 12 排気路 13 給水路 14 給湯路 15 水量調節手段 16 排気導入路 18 排気導入手段 19 気液分離手段 20 排気吐出器 21 排気返却路 22 出湯温度検知手段 23 導入量調節手段 24 出湯温度設定手段 25 制御手段 35 炭酸濃度検知手段 36 炭酸濃度設定手段 Reference Signs List 7 Combustion means 11 Heat exchanger 12 Exhaust path 13 Water supply path 14 Hot water supply path 15 Water volume adjustment means 16 Exhaust introduction path 18 Exhaust introduction means 19 Gas-liquid separation means 20 Exhaust discharger 21 Exhaust return path 22 Outlet hot water temperature detection means 23 Introduction amount adjustment Means 24 Hot water temperature setting means 25 Control means 35 Carbon dioxide concentration detecting means 36 Carbon dioxide concentration setting means
───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) F24H 1/10 301 F24H 1/14 ──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int.Cl. 7 , DB name) F24H 1/10 301 F24H 1/14
Claims (2)
を用いる燃焼手段と、前記燃焼手段から排出される燃焼
ガスが通る排気路と、燃焼ガスと水を熱交換する熱交換
器と、前記熱交換器に水を供給する給水路と、前記熱交
換器から湯を所定の場所に供給する給湯路と、前記給湯
路内に燃焼ガスを導入する排気導入手段と、前記排気路
から前記排気導入手段に燃焼ガスを供給する排気導入路
と、前記給湯路に導入する燃焼ガスの量を調節する前記
排気導入路の途中に設けた導入量調節手段と、前記排気
導入手段の前記給湯路下流側に設け、湯と燃焼ガスを分
離する気液分離手段と、前記気液分離手段で分離した燃
焼ガスのみを吐出する排気吐出器と、前記排気吐出器か
ら前記排気路に分離した燃焼ガスを戻す排気返却路と、
前記給水路若しくは前記給湯路の途中に設けた水量を調
節する水量調節手段と、前記気液分離手段の前記給湯路
下流側に設けた出湯温度を検知する出湯温度検知手段
と、出湯温度を設定する出湯温度設定手段と、前記出湯
温度設定手段と前記出湯温度検知手段からの信号に基づ
いて前記燃焼手段と前記水量調節手段と前記導入量調節
手段とを制御する制御手段からなる給湯装置。A combustion unit that uses a fuel that generates a combustion gas containing carbon dioxide; an exhaust passage through which the combustion gas discharged from the combustion unit passes; a heat exchanger that exchanges heat between the combustion gas and water; A water supply path for supplying water to the heat exchanger; a water supply path for supplying hot water from the heat exchanger to a predetermined location; exhaust introduction means for introducing combustion gas into the hot water supply path; An exhaust gas introduction path for supplying combustion gas to the introduction means, an introduction amount adjustment means provided in the middle of the exhaust gas introduction path for adjusting the amount of combustion gas introduced to the hot water supply path, and the hot water supply path downstream of the exhaust gas introduction means. A gas-liquid separating means for separating hot water and combustion gas, an exhaust discharger for discharging only the combustion gas separated by the gas-liquid separation means, and a combustion gas separated from the exhaust discharger to the exhaust passage. Return exhaust return path,
A water amount adjusting means for adjusting an amount of water provided in the middle of the water supply path or the hot water supply path; a tapping temperature detecting means for detecting a tapping temperature provided on the downstream side of the hot water path of the gas-liquid separation means; and setting a tapping temperature. A hot water supply apparatus comprising: a hot water temperature setting means for controlling the combustion means, the water amount adjusting means and the introduction amount adjusting means based on signals from the hot water temperature setting means and the hot water temperature detecting means.
を用いる燃焼手段と、前記燃焼手段から排出される燃焼
ガスが通る排気路と、燃焼ガスと水を熱交換する熱交換
器と、前記熱交換器に水を供給する給水路と、前記熱交
換器から湯を所定の場所に供給する給湯路と、前記給湯
路内に燃焼ガスを導入する排気導入手段と、前記排気路
から前記排気導入手段に燃焼ガスを供給する排気導入路
と、前記給湯路に導入する燃焼ガスの量を調節する前記
排気導入路の途中に設けた導入量調節手段と、前記排気
導入手段の前記給湯路下流側に設け、湯と燃焼ガスを分
離する気液分離手段と、前記気液分離手段で分離した燃
焼ガスのみを吐出する排気吐出器と、前記排気吐出器か
ら前記排気路に分離した燃焼ガスを戻す排気返却路と、
前記給水路若しくは前記給湯路の途中に設けた水量を調
節する水量調節手段と、前記気液分離手段の前記給湯路
下流側に設けた前記給湯路を流れる湯に含まれる炭酸ガ
ス濃度を検知する炭酸濃度検知手段と、出湯する湯に含
まれる炭酸ガス濃度を設定する炭酸濃度設定手段と、前
記炭酸濃度設定手段と前記炭酸濃度検知手段からの信号
に基づいて前記燃焼手段と前記水量調節手段と前記導入
量調節手段とを制御する制御手段からなる給湯装置。2. A combustion means using a fuel for producing a combustion gas containing carbon dioxide, an exhaust passage through which the combustion gas discharged from the combustion means passes, a heat exchanger for exchanging heat between the combustion gas and water, A water supply path for supplying water to the heat exchanger; a water supply path for supplying hot water from the heat exchanger to a predetermined location; exhaust introduction means for introducing combustion gas into the hot water supply path; An exhaust gas introduction path for supplying combustion gas to the introduction means, an introduction amount adjustment means provided in the middle of the exhaust gas introduction path for adjusting the amount of combustion gas introduced to the hot water supply path, and the hot water supply path downstream of the exhaust gas introduction means. A gas-liquid separating means for separating hot water and combustion gas, an exhaust discharger for discharging only the combustion gas separated by the gas-liquid separation means, and a combustion gas separated from the exhaust discharger to the exhaust passage. Return exhaust return path,
A water amount adjusting means for adjusting an amount of water provided in the water supply path or the hot water supply path; and detecting a concentration of carbon dioxide contained in hot water flowing through the hot water supply path provided on the downstream side of the hot water supply path of the gas-liquid separation means. Carbonic acid concentration detecting means, carbonic acid concentration setting means for setting the concentration of carbon dioxide contained in hot water to be discharged, the burning means and the water amount adjusting means based on signals from the carbonic acid concentration setting means and the carbonic acid concentration detecting means. A hot water supply apparatus comprising control means for controlling the introduction amount adjusting means.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3225873A JP3042067B2 (en) | 1991-09-05 | 1991-09-05 | Water heater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3225873A JP3042067B2 (en) | 1991-09-05 | 1991-09-05 | Water heater |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0566059A JPH0566059A (en) | 1993-03-19 |
| JP3042067B2 true JP3042067B2 (en) | 2000-05-15 |
Family
ID=16836195
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3225873A Expired - Fee Related JP3042067B2 (en) | 1991-09-05 | 1991-09-05 | Water heater |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3042067B2 (en) |
-
1991
- 1991-09-05 JP JP3225873A patent/JP3042067B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0566059A (en) | 1993-03-19 |
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