JP3047592B2 - Carbonated spring production equipment - Google Patents
Carbonated spring production equipmentInfo
- Publication number
- JP3047592B2 JP3047592B2 JP4022401A JP2240192A JP3047592B2 JP 3047592 B2 JP3047592 B2 JP 3047592B2 JP 4022401 A JP4022401 A JP 4022401A JP 2240192 A JP2240192 A JP 2240192A JP 3047592 B2 JP3047592 B2 JP 3047592B2
- Authority
- JP
- Japan
- Prior art keywords
- combustion gas
- hot water
- carbon dioxide
- water supply
- water
- 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
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/32—Direct CO2 mitigation
Landscapes
- Chimneys And Flues (AREA)
- Control For Baths (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8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開放した燃焼室
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で形成された火災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, 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 interior, and is brought into direct contact with the fire 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、給水路4から供給された水と接触する
燃焼ガス中の二酸化炭素の濃度は、安定した燃焼を保持
するため一定値(5〜8%)に決まっており、高濃度化
が困難であった。However, in the above configuration, the concentration of carbon dioxide in the combustion gas coming into contact with the water supplied from the water supply passage 4 has a constant value (5) in order to maintain stable combustion. 88%), and it was difficult to increase the concentration.
【0005】また燃焼手段2の故障により一酸化炭素が
多く生成された場合には燃焼ガス中の二酸化炭素の濃度
が低くなってしまい、燃焼ガスと水を接触させて燃焼ガ
ス中の二酸化炭素を溶解させても高濃度にすることが出
来なかった。When a large amount of carbon monoxide is generated due to the failure of the combustion means 2, the concentration of carbon dioxide in the combustion gas decreases, and the carbon dioxide in the combustion gas is brought into contact with the combustion gas and water. High concentrations could not be obtained even after dissolution.
【0006】さらに、一酸化炭素を含む燃焼ガスが給湯
路5から湯とともに供給された場合には出湯箇所におい
て一酸化炭素の濃度が上がり衛生的に良くなかった。さ
らに燃焼ガス中に含まれる二酸化窒素等の窒素酸化物が
湯中に入り、湯中の硝酸イオン濃度が上がるため衛生上
好ましくないという課題があった。Further, when the combustion gas containing carbon monoxide is supplied together with hot water from the hot water supply channel 5, the concentration of carbon monoxide at the hot water outlet increases, which is not hygienic. Furthermore, there is a problem that nitrogen oxides such as nitrogen dioxide contained in the combustion gas enter the hot water and increase the concentration of nitrate ions in the hot water, which is not preferable for sanitation.
【0007】本発明は、かかる従来の課題を解消するも
ので、燃焼を安定に保ちながら、一酸化炭素を二酸化炭
素に変換し、燃焼ガスの中の二酸化炭素の濃度を高めた
燃焼ガスと湯または水を接触させることにより、湯また
は水に溶解する二酸化炭素の溶解効率を高め、湯または
水に含まれる溶存炭酸ガス濃度を上げるとともに万一燃
焼ガスが湯または水と共に供給されても出湯箇所におけ
る空気中の一酸化炭素濃度が上がらないようにすること
を第1の目的としている。SUMMARY OF THE INVENTION The present invention solves the above-mentioned conventional problems. A combustion gas and a hot water in which carbon monoxide is converted into carbon dioxide and the concentration of carbon dioxide in the combustion gas is increased while maintaining stable combustion. Or, by bringing water into contact, the dissolving efficiency of carbon dioxide dissolved in hot water or water is increased, the concentration of dissolved carbon dioxide contained in the hot water or water is increased, and even if combustion gas is supplied together with hot water or water, the tapping point The first object is to prevent the concentration of carbon monoxide in the air from increasing.
【0008】本発明の第2の目的は、燃焼ガス中に含ま
れる二酸化窒素等の窒素酸化物を除去し、燃焼ガス中の
二酸化炭素の濃度を高めた燃焼ガスと湯また水と接触さ
せることにより、湯または水に溶解する二酸化炭素の溶
解効率を高め、湯または水に含まれる溶存炭酸ガス濃度
を上げるとともに湯または水に燃焼ガス中の窒素酸化物
が溶解するのを防止することである。A second object of the present invention is to remove nitrogen oxides such as nitrogen dioxide contained in a combustion gas and bring the combustion gas having an increased concentration of carbon dioxide in the combustion gas into contact with hot water or water. Is to increase the dissolving efficiency of carbon dioxide dissolved in hot water or water, to increase the concentration of dissolved carbon dioxide contained in hot water or water, and to prevent nitrogen oxides in the combustion gas from being dissolved in the hot water or water. .
【0009】本発明の第3の目的は、燃焼ガス中に含ま
れる窒素酸化物を除去し、燃焼ガス中の二酸化炭素及び
一酸化炭素の濃度を高めた燃焼ガス中に含まれる一酸化
炭素を二酸化炭素に変換することによって、より二酸化
炭素の濃度の高い燃焼ガスを得、そしてこの燃焼ガスと
接触させた湯または水に溶解する二酸化炭素の溶解効率
を高めて湯または水に含まれる溶存炭酸ガス濃度を高め
るとともに燃焼ガスが湯または水と共に供給されても出
湯箇所における空気中の一酸化炭素濃度が上がらないよ
うにせしめ、かつ湯または水に燃焼ガス中の窒素酸化物
が溶解するのを防止する。A third object of the present invention is to remove nitrogen oxides contained in the combustion gas and remove the carbon monoxide contained in the combustion gas in which the concentrations of carbon dioxide and carbon monoxide in the combustion gas are increased. By converting it to carbon dioxide, a combustion gas with a higher concentration of carbon dioxide is obtained, and the dissolved carbon dioxide contained in the hot water or water is increased by increasing the dissolving efficiency of carbon dioxide dissolved in the hot water or water brought into contact with the combustion gas. Increases the gas concentration and prevents the concentration of carbon monoxide in the air at the tapping point from rising even when the combustion gas is supplied together with the hot water or water, and prevents the nitrogen oxides in the combustion gas from being dissolved in the hot water or water. To prevent.
【0010】[0010]
【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の手段は、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、湯または水に溶解する給水給湯路に設けた燃焼ガス
導入手段と、湯または水とこの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、燃焼ガス導入路に設けた酸化触媒を備えたも
のである。In order to solve the above-mentioned 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 passes, and a combustion gas through which a combustion gas containing carbon dioxide passes. An introduction path, 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 in 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 water and residual combustion gas not dissolved in the hot water or water, and gas-liquid separation of the residual combustion gas separated by the gas-liquid separation means It has a discharge path for discharging from the means and an oxidation catalyst provided in the combustion gas introduction path.
【0011】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、湯ま
たは水に溶解する給水給湯路に設けた燃焼ガス導入手段
と、湯または水とこの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、燃焼ガス導入路に設けた脱硝触媒を備えたものであ
る。In order to achieve the second object, the second means of the carbonated spring manufacturing apparatus according to the present invention comprises a hot water supply passage through which hot water or water passes, and a combustion gas introduction passage through which a combustion gas containing carbon dioxide passes. The combustion gas supplied from the combustion gas introduction path is introduced into the hot water supply path, and the carbon dioxide in the combustion gas is dissolved in the hot water or water. Gas-liquid separation means provided downstream of the hot water supply path of the combustion gas introduction means for separating the residual combustion gas not dissolved in the hot water or water, and the residual combustion gas separated in the gas-liquid separation means from the gas-liquid separation means. It has a discharge path for discharging and a denitration catalyst provided in a combustion gas introduction path.
【0012】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、湯また
は水に溶解する給水給湯路に設けた燃焼ガス導入手段
と、湯または水とこの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、燃焼ガス導入路に設けた脱硝触媒と、脱硝触媒の下
流側の燃焼ガス導入路に設けた酸化触媒を備えたもので
ある。In order to achieve the third object, a third means of the carbonated spring manufacturing apparatus according to the present invention comprises a hot water supply passage through which hot water or water passes, and a combustion gas introduction passage through which a combustion gas containing carbon dioxide passes. Means for introducing combustion gas supplied from the combustion gas introduction path into the hot water supply path and dissolving carbon dioxide in the combustion gas in the hot water or water; Gas-liquid separation means provided downstream of the hot water supply channel of the combustion gas introduction means for separating residual combustion gas not dissolved in hot water or water, and residual combustion gas separated in the gas-liquid separation means is discharged from the gas-liquid separation means. A denitration catalyst provided in the combustion gas introduction passage, and an oxidation catalyst provided in the combustion gas introduction passage downstream of the denitration catalyst.
【0013】[0013]
【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。二
酸化炭素を含んだ燃焼ガスは、燃焼ガス導入路から燃焼
ガス導入手段に導かれる。燃焼ガス導入路の途中に設け
た酸化触媒により、燃焼ガス中に含まれる一酸化炭素は
二酸化炭素に変換され、燃焼ガス中の二酸化炭素の濃度
が高められる。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
て湯または水と二酸化炭素の濃度の高まった燃焼ガスが
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。尚酸
化触媒により一酸化炭素が無くなったので湯または水に
一酸化炭素が混合されることが無くなる。また燃焼ガス
中の二酸化炭素の濃度が高められるため二酸化炭素の湯
または水への溶解効率が高まる。According to the present invention, the first means produces a combustion gas containing carbon dioxide by the combustion means. The combustion gas containing carbon dioxide is guided from the combustion gas introduction path to the combustion gas introduction means. By the oxidation catalyst provided in the middle of the combustion gas introduction path, carbon monoxide contained in the combustion gas is converted into carbon dioxide, and the concentration of carbon dioxide in the combustion gas is increased. On the other hand, hot water or water is supplied to the combustion gas introducing means via a hot water supply channel. In the combustion gas introducing means, hot water or water and a combustion gas having an increased concentration of carbon dioxide are mixed and heat exchanged, and at the same time, highly water-soluble carbon dioxide in the combustion gas dissolves to become hot water containing carbon dioxide gas. Thereafter, the residual combustion gas not dissolved and the hot and cold 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 containing carbon dioxide gas comes out of the gas-liquid separation means and is supplied to a predetermined place such as a shower or a bath via a hot water supply channel. Since carbon monoxide is eliminated by the oxidation catalyst, carbon monoxide is not mixed with hot water or water. Further, since the concentration of carbon dioxide in the combustion gas is increased, the efficiency of dissolving carbon dioxide in hot water or water is increased.
【0014】また本発明の第2の手段においては、燃焼
ガス導入路の途中に設けた脱硝触媒に燃焼ガス中に含ま
れる二酸化窒素等の窒素酸化物が吸着され、窒素酸化物
の湯または水への溶解が無くなる。また窒素酸化物が無
くなった分だけ燃焼ガス中の二酸化炭素の濃度が高めら
れ湯または水への二酸化炭素の溶解効率が高まる。[0014] In the second means of the present invention, nitrogen oxides such as nitrogen dioxide contained in the combustion gas are adsorbed by a denitration catalyst provided in the middle of the combustion gas introduction path, and the nitrogen oxide hot water or water Dissolution in the water is eliminated. In addition, the concentration of carbon dioxide in the combustion gas is increased by an amount corresponding to the disappearance of the nitrogen oxides, and the efficiency of dissolving carbon dioxide in hot water or water is increased.
【0015】また本発明の第3の手段においては、燃焼
ガス導入路の途中に設けた脱硝触媒に燃焼ガス中に含ま
れる二酸化窒素等の窒素酸化物が吸着され、窒素酸化物
が無くなった分だけ燃焼ガス中の二酸化炭素および一酸
化炭素の濃度が高まる。[0015] In the third means of the present invention, nitrogen oxides such as nitrogen dioxide contained in the combustion gas are adsorbed by the denitration catalyst provided in the middle of the combustion gas introduction path, and the nitrogen oxide is removed. Only the concentration of carbon dioxide and carbon monoxide in the combustion gas increases.
【0016】窒素酸化物が無くなった燃焼ガスは次に酸
化触媒を通過することにより、一酸化炭素が二酸化炭素
に変換される。脱硝触媒で窒素酸化物を取り除いた後酸
化触媒を通ることにより、酸化触媒では一酸化窒素を二
酸化窒素に変換する必要が無くなり、その分だけ効率良
く一酸化炭素を二酸化炭素に変換される。窒素酸化物が
無くなった分と一酸化炭素を変換した分だけ燃焼ガス中
の二酸化炭素の濃度が高められ、より一層二酸化炭素の
湯または水への溶解効率が高まる。また湯または水への
窒素酸化物および一酸化炭素の混合や溶解がなくなる。The combustion gas free of nitrogen oxides is then passed through an oxidation catalyst to convert carbon monoxide to carbon dioxide. By passing the oxidation catalyst after removing the nitrogen oxides with the denitration catalyst, the oxidation catalyst does not need to convert nitrogen monoxide to nitrogen dioxide, and carbon monoxide can be efficiently converted to carbon dioxide by that much. The concentration of carbon dioxide in the combustion gas is increased by the amount that the nitrogen oxides have disappeared and the amount that the carbon monoxide has been converted, and the dissolving efficiency of carbon dioxide in hot water or water is further increased. Also, mixing and dissolving of nitrogen oxides and carbon monoxide in hot water or water are eliminated.
【0017】[0017]
【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.
【0018】図1は、本発明の炭酸泉製造装置の第1の
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の途中に設け
られた燃料調節手段10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7から燃焼
ガスの流れ方向下流側に順番に燃焼室11と熱交換器1
2と排気路13が連接して設けられている。FIG. 1 is a schematic configuration diagram of a main part of an embodiment in which the first means of the carbonated spring manufacturing apparatus of the present invention is applied to a water heater. Reference numeral 7 denotes combustion means for mixing and supplying air supplied by a combustion fan 8 for supplying combustion air and fuel whose flow rate has been adjusted by a fuel adjustment means 10 provided in the fuel transfer pipe 9. The combustion chamber 11 and the heat exchanger 1 are sequentially arranged downstream from the combustion means 7 in the flow direction of the combustion gas.
2 and an exhaust path 13 are provided in series.
【0019】14は湯または水が流れる給水給湯路であ
り、給水給湯路14の途中に熱交換器12が設けられて
いる。熱交換器12の給水給湯路14の上流側には給水
給湯路14内を流れる水の流量を検知する水量検知手段
15が設けられている。給水給湯路14によって供給さ
れた水は熱交換器12で熱交換されて湯となり熱交換器
12から出湯される。また排気路13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16が排気路
13から分岐して設けられている。給水給湯路14の熱
交換器12下流側には直圧型縁切り器17が設けられ、
給水給湯路14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17の上流の供
給圧のまま湯水を流すようにしている。Reference numeral 14 denotes a hot water supply or hot water supply passage through which water flows. The heat exchanger 12 is provided in the middle of the hot or cold water supply water supply passage 14. On the upstream side of the water supply / hot water supply path 14 of the heat exchanger 12, a water amount detection means 15 for detecting the flow rate of water flowing in the water supply / water supply path 14 is provided. The water supplied by the hot water supply path 14 is heat-exchanged in the heat exchanger 12 to become hot water, and is discharged from the heat exchanger 12. In the middle of the exhaust passage 13, a combustion gas introduction passage 16 is provided branching from the exhaust passage 13 so that a part of the combustion gas flows. On the downstream side of the heat exchanger 12 in the water supply / hot water supply path 14, a direct pressure type edger 17 is provided.
When hot water flows backward in the hot water supply channel 14, the hot water is prevented from flowing backward, and when there is no reverse flow, hot water flows with the supply pressure upstream of the direct pressure type border cutting device 17.
【0020】直圧型縁切り器17の下流側には燃焼ガス
導入路16を介して排気路13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18が設けられ、さら
に燃焼ガス導入手段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と排気路13とは排出路20で連通されている。
また排出路20の途中には排出路20内を流れる残留燃
焼ガスの流量を調節する排出量調節手段21が設けられ
ている。Downstream of the direct pressure type edger 17, there is provided a combustion gas introducing means 18 for introducing a combustion gas from an exhaust path 13 through a combustion gas introduction path 16 and mixing it into hot water. A gas-liquid separation unit 19 for separating combustion gas and hot water is provided downstream of 18. The gas-liquid separation means 19 and the exhaust path 13 are connected by a discharge path 20.
In the middle of the discharge passage 20, there is provided a discharge amount adjusting means 21 for adjusting the flow rate of the residual combustion gas flowing in the discharge passage 20.
【0021】燃焼ガス導入路16の途中には触媒部22
が設けられており、触媒部22の下流側の燃焼ガス導入
路16には燃焼ガス導入手段18からの水または湯の逆
流を防止する逆止弁23が設けられている。In the middle of the combustion gas introduction passage 16, a catalyst portion 22 is provided.
A check valve 23 for preventing backflow of water or hot water from the combustion gas introduction means 18 is provided in the combustion gas introduction passage 16 on the downstream side of the catalyst section 22.
【0022】24は制御手段であり、水量検知手段15
から湯の使用流量を検知すると、温度設定手段25から
設定温度を読み取り、給水給湯路14の途中に設けた出
湯温度検知手段26で検知される湯温が設定温度になる
ように燃料調節手段10、燃焼ファン8を制御する。ま
た気液分離手段19から湯が排出路20内に逆流しない
ように排出量調節手段21を制御するとともに、触媒部
22に設けた加熱ヒーター27の制御を行なう。Reference numeral 24 denotes a control means, and the water amount detecting means 15
When the flow rate of the hot water is detected from the water, the set temperature is read from the temperature setting means 25, and the fuel adjusting means 10 is set so that the hot water temperature detected by the tap water temperature detecting means 26 provided in the middle of the hot water supply path 14 becomes the set temperature. , The combustion fan 8 is controlled. In addition, the controller controls the discharge amount adjusting means 21 so that hot water does not flow backward from the gas-liquid separating means 19 into the discharge path 20, and controls the heater 27 provided in the catalyst part 22.
【0023】図2において燃焼ガス導入手段18の一例
を示す。28は給湯入口で、直圧型縁切り器17に連接
している。29は給湯出口で、気液分離手段19に連接
している。30はノズル、31はベンチュリー、32は
燃焼ガス入口で、燃焼ガス導入路16に連接している。FIG. 2 shows an example of the combustion gas introducing means 18. Reference numeral 28 denotes a hot water supply inlet, which is connected to the direct pressure type edger 17. Reference numeral 29 denotes a hot water supply outlet, which is connected to the gas-liquid separation means 19. Reference numeral 30 denotes a nozzle, 31 denotes a venturi, and 32 denotes a combustion gas inlet, which is connected to the combustion gas introduction passage 16.
【0024】図3において触媒部22の一例を示す。燃
焼ガス導入路16の途中に触媒部22が設けられてお
り、内部には酸化触媒33が設けられている。酸化触媒
33に接して酸化触媒33を加熱する加熱ヒーター27
が設けられている。FIG. 3 shows an example of the catalyst section 22. A catalyst section 22 is provided in the middle of the combustion gas introduction path 16, and an oxidation catalyst 33 is provided inside. Heater 27 that contacts oxidation catalyst 33 and heats oxidation catalyst 33
Is provided.
【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調節手段10によって調節された
後燃料搬送管9から供給された燃料は燃焼手段7によっ
て混合され燃焼室11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12で給水給湯路
14から供給された水と熱交換が行われ、燃焼ガスは冷
却されて低温となり排気路13より排気される。In the above configuration, the air supplied by the combustion fan 8 and the fuel supplied from the fuel transfer pipe 9 after being adjusted by the fuel adjusting means 10 are mixed by the combustion means 7 to form a flame f in the combustion chamber 11. I do. The combustion gas generated by the flame f exchanges heat with the water supplied from the hot water supply path 14 in the heat exchanger 12, and the combustion gas is cooled to a low temperature and exhausted from the exhaust path 13.
【0026】一方、燃焼ガスの一部は排気路13の途中
から分岐して設けた燃焼ガス導入路16を介して燃焼ガ
ス導入手段18へと導かれる。燃焼ガス導入路16の途
中の触媒部22において燃焼ガス中の一酸化炭素は酸化
されて二酸化炭素に変換され、二酸化炭素の濃度が高め
られる。On the other hand, a part of the combustion gas is guided to the combustion gas introduction means 18 through the combustion gas introduction path 16 which is provided by branching from the middle of the exhaust path 13. The carbon monoxide in the combustion gas is oxidized and converted into carbon dioxide in the catalyst section 22 on the way of the combustion gas introduction passage 16, and the concentration of carbon dioxide is increased.
【0027】一方、熱交換器12に供給された水は湯と
なり直圧型縁切り器17に入る。直圧型縁切り器15に
おいて、給水給湯路14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14内を湯が流れる。その後、湯は
直圧型縁切り器17の給水給湯路14下流側に設けられ
た燃焼ガス導入手段18に送られる。On the other hand, the water supplied to the heat exchanger 12 becomes hot water and enters the direct pressure type edger 17. In the direct pressure type edger 15, when the hot water flows backward in the hot water supply channel 14, the reverse flow is prevented, and when there is no reverse flow, the hot water flows in the hot water supply channel 14 while maintaining the supplied pressure. Thereafter, the hot water is sent to the combustion gas introducing means 18 provided on the downstream side of the hot water supply path 14 of the direct pressure type edger 17.
【0028】燃焼ガスは燃焼ガス導入路16を介して燃
焼ガス導入手段18の燃焼ガス入口32から入り、ノズ
ル30周囲に滞留する。燃焼ガス導入手段18では湯の
供給圧によりノズル30から高速で湯が噴出し、ベンチ
ュリー31に入る。この際にベンチュリー31はエゼク
タ効果により負圧となりノズル30の周囲の燃焼ガスが
ベンチュリー31に吸引される。ベンチュリー31内に
入った湯と燃焼ガスは、ベンチュリー31内および気液
分離手段19に至るまでの給水給湯路14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19に入り湯と分離され、気液分離手段19
内の上方に滞留し、排出路20を介して排気路13に戻
る。排気路13に戻る残留燃焼ガスの流量は、排出路2
0の途中に設けた排出量調節手段21によって調節され
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19を出て給水給湯路14を介してシャワーや
浴槽に供給される。The combustion gas enters from the combustion gas inlet 32 of the combustion gas introduction means 18 through the combustion gas introduction passage 16 and stays around the nozzle 30. In the combustion gas introducing means 18, the hot water is spouted from the nozzle 30 at a high speed by the hot water supply pressure, and enters the venturi 31. At this time, the venturi 31 becomes negative pressure due to the ejector effect, and the combustion gas around the nozzle 30 is sucked into the venturi 31. The hot water and the combustion gas that have entered the venturi 31 come into direct contact with the hot water in the venturi 31 and the water supply hot water supply path 14 leading to the gas-liquid separation means 19, 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 19 and is separated from the hot water.
And stays in the upper part, returns to the exhaust path 13 via the discharge path 20. The flow rate of the residual combustion gas returning to the exhaust path 13
It is adjusted by the discharge amount adjusting means 21 provided in the middle of 0. On the other hand, the hot water whose temperature has risen due to the dissolution of carbon dioxide exits the gas-liquid separation means 19 and is supplied to a shower or a bathtub through the hot water supply path 14.
【0029】制御手段24は、水量検知手段15におい
て湯の使用流量を検知すると、温度設定手段25から設
定温度を読み取り、給水給湯路14の途中に設けた出湯
温度検知手段26で検知される湯温が設定温度になるよ
うに燃料調節手段10、燃焼ファン8を制御する。また
気液分離手段19から湯が排出路20内に逆流しないよ
うに排出量調節手段21を制御するとともに、触媒部2
2に設けた加熱ヒーター27の制御を行なう。When the water amount detection means 15 detects the flow rate of the hot water, the control means 24 reads the set temperature from the temperature setting means 25 and detects the hot water detected by the tap water temperature detection means 26 provided in the middle of the water supply hot water supply passage 14. The fuel control means 10 and the combustion fan 8 are controlled so that the temperature becomes the set temperature. Also, while controlling the discharge amount adjusting means 21 so that hot water does not flow backward from the gas-liquid separation means 19 into the discharge path 20, the catalyst unit 2
2 is controlled.
【0030】このような構成により燃焼ガス中の一酸化
炭素を酸化触媒33により酸化させ二酸化炭素に変換す
ることで、燃焼ガス中の二酸化炭素の濃度(分圧)が高
くなり、二酸化炭素の湯への溶解効率を高くすることが
出来、結果として湯中の溶存炭酸ガス濃度を高くするこ
とが出来る。With such a configuration, carbon monoxide in the combustion gas is oxidized by the oxidation catalyst 33 and converted into carbon dioxide, so that the concentration (partial pressure) of the carbon dioxide in the combustion gas increases, and The efficiency of dissolution in water can be increased, and as a result, the concentration of dissolved carbon dioxide in the hot water can be increased.
【0031】得られた溶存炭酸ガスが溶解した湯に入浴
することによって、血流増加作用による保温効果、疲労
回復効果、血圧安定化効果、傷治癒効果を発揮するが、
高濃度化することにより、さらに高い効果を得ることが
出来る。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。By bathing in the hot water in which the dissolved carbon dioxide gas is dissolved, a warming effect by blood flow increasing effect, a fatigue recovery effect, a blood pressure stabilizing effect, and a wound healing effect are exhibited.
By increasing the concentration, a higher effect can be obtained. Furthermore, since the combustion gas and the hot water are in direct contact, the latent heat of the water vapor in the combustion gas can 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.
【0032】また気液分離手段19における燃焼ガスと
湯との分離が不十分で湯とともに燃焼ガスが混入して出
湯口から供給された場合でも、有害な一酸化炭素が室内
に噴出することが無く、使用上の安全および室内環境衛
生を保つことが出来る。Even when the gas-liquid separation means 19 does not sufficiently separate the combustion gas from the hot water and the combustion gas is mixed with the hot water and supplied from the tap, harmful carbon monoxide may be blown into the room. Therefore, safety in use and indoor environmental hygiene can be maintained.
【0033】図4は本発明の炭酸泉製造装置の第2の手
段を給湯機に応用した場合の一実施例であり、図5は触
媒部22の一例を示している。上記第1の手段の実施例
と異なる点は、触媒部22の内部に脱硝触媒34を設け
たことである。そしてこれ以外の構成は上記第1の手段
の実施例と同じで、同一符号を付してある。FIG. 4 shows an embodiment in which the second means of the carbonated spring manufacturing apparatus of the present invention is applied to a water heater, and FIG. 5 shows an example of the catalyst section 22. The difference from the first embodiment is that a denitration catalyst 34 is provided inside the catalyst section 22. The other configuration is the same as that of the first embodiment, and the same reference numerals are given.
【0034】上記構成において、燃焼ガス導入路16内
を流れる燃焼ガス中の窒素酸化物は脱硝触媒34に吸着
される。In the above configuration, nitrogen oxides in the combustion gas flowing in the combustion gas introduction passage 16 are adsorbed by the denitration catalyst 34.
【0035】このような構成により燃焼ガス中の二酸化
窒素等の窒素酸化物を脱硝触媒により吸着することで、
燃焼ガス中の二酸化炭素の濃度(分圧)が高くなり、二
酸化炭素の湯への溶解効率を高くすることが出来、結果
として湯中の溶存炭酸ガス濃度を高くすることが出来
る。With this configuration, nitrogen oxides such as nitrogen dioxide in the combustion gas are adsorbed by the denitration catalyst,
The concentration (partial pressure) of carbon dioxide in the combustion gas increases, so that the efficiency of dissolving carbon dioxide in hot water can be increased, and as a result, the concentration of dissolved carbon dioxide in the hot water can be increased.
【0036】得られた溶存炭酸ガスが溶解した湯に入浴
することによって、血流増加作用による保温効果、疲労
回復効果、血圧安定化効果、傷治癒効果を発揮するが、
高濃度化することにより、さらに高い効果を得ることが
出来る。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に、
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。By bathing in the hot water in which the dissolved carbon dioxide gas is dissolved, a warming effect due to a blood flow increasing effect, a fatigue recovery effect, a blood pressure stabilizing effect, and a wound healing effect are exhibited.
By increasing the concentration, a higher effect can be obtained. Furthermore, since the combustion gas and the hot water are in direct contact, the latent heat of the water vapor in the combustion gas can be recovered and the efficiency can be increased. Also, because the carbon dioxide in the combustion gas dissolves,
The emission of carbon dioxide, which causes global warming, can be suppressed.
【0037】また有害な二酸化窒素が湯と反応して硝酸
イオンになることが無いので、湯の使用上の安全を保つ
ことが出来る。Further, since harmful nitrogen dioxide does not react with hot water to form nitrate ions, safety in use of hot water can be maintained.
【0038】図6は本発明の炭酸泉製造装置の第3の手
段を給湯機に応用した場合の一実施例であり、図7は触
媒部22の一例を示している。上記第1の手段の実施例
と異なる点は、触媒部22の内部に上流側から順に脱硝
触媒34、加熱ヒーター27、酸化触媒33を設けたこ
とである。そしてこれ以外の構成は上記第1の手段の実
施例と同じ、同一符号を付してある。FIG. 6 shows an embodiment in which the third means of the carbonated spring manufacturing apparatus according to the present invention is applied to a water heater, and FIG. 7 shows an example of the catalyst section 22. The difference from the first embodiment is that a denitration catalyst 34, a heater 27, and an oxidation catalyst 33 are provided inside the catalyst unit 22 in this order from the upstream side. The other components are denoted by the same reference numerals as those in the first embodiment.
【0039】上記構成において、燃焼ガス導入路16内
を流れる燃焼ガスはまず脱硝触媒34により成分中の窒
素酸化物が吸着され、窒素酸化物が無くなった状態で燃
焼ガスは酸化触媒33で酸化される。酸化触媒33にお
いては、窒素酸化物を酸化する必要が無くなった分だ
け、一酸化炭素を酸化する効率が良くなり、二酸化炭素
への変換率が良くなる。In the above configuration, the combustion gas flowing in the combustion gas introduction passage 16 is first adsorbed by the denitration catalyst 34 with nitrogen oxides contained therein, and the combustion gas is oxidized by the oxidation catalyst 33 with the nitrogen oxides removed. You. In the oxidation catalyst 33, the efficiency of oxidizing carbon monoxide is improved and the conversion rate to carbon dioxide is improved by the amount of eliminating the need to oxidize nitrogen oxides.
【0040】このような構成により燃焼ガス中の二酸化
窒素等の窒素酸化物を吸着することで、燃焼ガス中の二
酸化炭素および一酸化炭素の濃度(分圧)が高くなり、
その後の一酸化炭素から二酸化炭素への変換効率も高く
することが出来る。結果として二酸化炭素の湯への溶解
効率を高くすることが出来、結果として湯中の溶存炭酸
ガス濃度を高くすることが出来る。By adsorbing nitrogen oxides such as nitrogen dioxide in the combustion gas by such a configuration, the concentration (partial pressure) of carbon dioxide and carbon monoxide in the combustion gas increases,
Subsequent conversion efficiency from carbon monoxide to carbon dioxide can also be increased. As a result, the efficiency of dissolving carbon dioxide in hot water can be increased, and as a result, the concentration of dissolved carbon dioxide in the hot water can be increased.
【0041】得られた溶存炭酸ガスが溶解した湯に入浴
することによって、血流増加作用による保温効果、疲労
回復効果、血圧安定化効果、傷治癒効果を発揮するが、
高濃度化することにより、さらに高い効果を得ることが
出来る。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。By bathing in the hot water in which the dissolved carbon dioxide gas is dissolved, a warming effect, a fatigue recovery effect, a blood pressure stabilizing effect, and a wound healing effect by blood flow increasing effect are exhibited.
By increasing the concentration, a higher effect can be obtained. Furthermore, since the combustion gas and the hot water are in direct contact, the latent heat of the water vapor in the combustion gas can 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.
【0042】また気液分離手段19における燃焼ガスと
湯との分離が不十分で湯とともに燃焼ガスが混入して出
湯口から供給された場合でも、有害な一酸化炭素が室内
に噴出することが無く、また二酸化窒素が湯と反応して
硝酸イオンとなることが無く湯の使用上の安全および室
内環境衛生を保つことが出来る。Even if the gas-liquid separation means 19 does not sufficiently separate the combustion gas from the hot water and the combustion gas is mixed with the hot water and supplied from the tap, harmful carbon monoxide may be blown into the room. There is no nitrogen dioxide reacting with the hot water to form nitrate ions, so that the safety in using the hot water and the indoor environmental hygiene can be maintained.
【0043】[0043]
【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。As described above, in the carbonated spring manufacturing apparatus of the present invention, the following effects can be obtained.
【0044】請求項1記載の発明によれば、燃焼ガス中
の一酸化炭素を酸化させ二酸化炭素に変換することで、
燃焼ガス中の二酸化炭素の濃度(分圧)が高くなり、二
酸化炭素の湯への溶解効率を高くすることが出来、結果
として湯中の溶存炭酸ガス濃度を高くすることが出来
る。得られた溶存炭酸ガスが溶解した湯に入浴すること
によって、血流増加作用による保温効果、疲労回復効
果、血圧安定化効果、傷治癒効果を発揮するが、高濃度
化することにより、さらに高い効果を得ることが出来
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。また気液分離手段19における燃焼ガスと湯と
の分離が不十分で湯とともに燃焼ガスが混入して出湯口
から供給された場合でも、有害な一酸化炭素が室内に噴
出することが無く、使用上の安全および室内環境衛生を
保つことが出来る。According to the first aspect of the present invention, by oxidizing carbon monoxide in the combustion gas and converting it into carbon dioxide,
The concentration (partial pressure) of carbon dioxide in the combustion gas increases, so that the efficiency of dissolving carbon dioxide in hot water can be increased, and as a result, the concentration of dissolved carbon dioxide in the hot water can be increased. By bathing in the hot water in which the dissolved carbon dioxide gas is dissolved, it exhibits a heat retention effect, a fatigue recovery effect, a blood pressure stabilizing effect, and a wound healing effect due to a blood flow increasing effect. The effect can be obtained. Furthermore, since the combustion gas and the hot water are in direct contact, the latent heat of the water vapor in the combustion gas can 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. Further, even when the gas-liquid separation means 19 does not sufficiently separate the combustion gas and the hot water and the combustion gas is mixed with the hot water and supplied from the tap, the harmful carbon monoxide does not blow out into the room and is not used. The above safety and indoor environmental hygiene can be maintained.
【0045】請求項2記載の発明によれば、燃焼ガス中
の二酸化窒素等の窒素酸化物を吸着することで、燃焼ガ
ス中の二酸化炭素の濃度(分圧)が高くなり、二酸化炭
素の湯への溶解効率を高くすることが出来、結果として
湯中の溶存炭酸ガス濃度を高くすることが出来る。得ら
れた溶存炭酸ガスが溶解した湯に入浴することによっ
て、血流増加作用による保温効果、疲労回復効果、血圧
安定化効果、傷治癒効果を発揮するが、高濃度化するこ
とにより、さらに高い効果を得ることが出来る。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。また
有害な二酸化窒素が湯と反応して硝酸イオンになること
が無いので、湯の使用上の安全を保つことが出来る。According to the second aspect of the present invention, by adsorbing nitrogen oxides such as nitrogen dioxide in the combustion gas, the concentration (partial pressure) of carbon dioxide in the combustion gas increases, and the carbon dioxide The efficiency of dissolution in water can be increased, and as a result, the concentration of dissolved carbon dioxide in the hot water can be increased. By bathing in the hot water in which the dissolved carbon dioxide gas is dissolved, it exhibits a heat retention effect, a fatigue recovery effect, a blood pressure stabilizing effect, and a wound healing effect due to a blood flow increasing effect. The effect can be obtained. Furthermore, since the combustion gas and the hot water are in direct contact, the latent heat of the water vapor in the combustion gas can 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. In addition, since harmful nitrogen dioxide does not react with hot water to form nitrate ions, safety in using hot water can be maintained.
【0046】請求項3記載の発明によれば、燃焼ガス中
の二酸化窒素等の窒素酸化物を吸着することで、燃焼ガ
ス中の二酸化炭素および一酸化炭素の濃度(分圧)が高
くなり、その後の一酸化炭素から二酸化炭素への変換効
率も高くすることが出来る。結果として二酸化炭素の湯
への溶解効率を高くすることが出来、結果として湯中の
溶存炭酸ガス濃度を高くすることが出来る。得られた溶
存炭酸ガスが溶解した湯に入浴することによって、血流
増加作用による保温効果、疲労回復効果、血圧安定化効
果、傷治癒効果を発揮するが、高濃度化することによ
り、さらに高い効果を得ることが出来る。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。また燃焼ガ
スと湯との分離が不十分で湯とともに燃焼ガスが混入し
て出湯口から供給された場合でも、有害な一酸化炭素が
室内に噴出することが無く、また二酸化窒素が湯と反応
して硝酸イオンとなることが無く湯の使用上の安全およ
び室内環境衛生を保つことが出来る。According to the third aspect of the invention, by adsorbing nitrogen oxides such as nitrogen dioxide in the combustion gas, the concentrations (partial pressure) of carbon dioxide and carbon monoxide in the combustion gas are increased, Subsequent conversion efficiency from carbon monoxide to carbon dioxide can also be increased. As a result, the efficiency of dissolving carbon dioxide in hot water can be increased, and as a result, the concentration of dissolved carbon dioxide in the hot water can be increased. By bathing in the hot water in which the dissolved carbon dioxide gas is dissolved, it exhibits a heat retention effect, a fatigue recovery effect, a blood pressure stabilizing effect, and a wound healing effect due to a blood flow increasing effect. The effect can be obtained. Furthermore, since the combustion gas and the hot water are in direct contact, the latent heat of the water vapor in the combustion gas can 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. Also, even when the combustion gas and hot water are not sufficiently separated and the combustion gas is mixed with the hot water and supplied from the tap, no harmful carbon monoxide is emitted into the room, and nitrogen dioxide reacts with the hot water. As a result, it does not become nitrate ions and the safety in using hot water and the indoor environmental hygiene can be maintained.
【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】同装置の実施例における燃焼ガス導入手段の断
面図FIG. 2 is a sectional view of a combustion gas introducing means in the embodiment of the apparatus.
【図3】同装置の実施例における触媒部の断面図FIG. 3 is a sectional view of a catalyst unit in the embodiment of the apparatus.
【図4】本発明の他の実施例における給湯装置の要部切
断の概略構成図FIG. 4 is a schematic configuration diagram of a main part cut of a hot water supply apparatus according to another embodiment of the present invention.
【図5】同装置の実施例における触媒部の断面図FIG. 5 is a sectional view of a catalyst section in the embodiment of the apparatus.
【図6】本発明の他の実施例における給湯装置の要部切
断の概略構成図FIG. 6 is a schematic configuration diagram of a main part cut of a hot water supply apparatus according to another embodiment of the present invention.
【図7】同装置の実施例における触媒部の断面図FIG. 7 is a sectional view of a catalyst unit in the embodiment of the apparatus.
【図8】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. 8 is a schematic configuration diagram of a main part of a carbonated spring manufacturing apparatus according to a conventional example.
14 給水給湯路 16 燃焼ガス導入路 18 燃焼ガス導入手段 19 気液分離手段 20 排出路 33 酸化触媒 34 脱硝触媒 14 hot water supply path 16 combustion gas introduction path 18 combustion gas introduction means 19 gas-liquid separation means 20 discharge path 33 oxidation catalyst 34 denitration catalyst
───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) A61H 33/02 F23J 15/00 ──────────────────────────────────────────────────続 き Continued on front page (58) Field surveyed (Int. Cl. 7 , DB name) A61H 33/02 F23J 15/00
Claims (3)
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湯または水に溶解す
る前記給水給湯路に設けた燃焼ガス導入手段と、湯また
は水とこの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に設けた酸化触媒からなる
炭酸泉製造装置。1. A hot water supply passage through which hot water or water passes, a combustion gas introduction passage through which combustion gas containing carbon dioxide passes, and a combustion gas supplied from the combustion gas introduction passage are introduced into the hot water supply passage. Combustion gas introduction means provided in the water supply hot water supply path for dissolving carbon dioxide in combustion gas in hot water or water; and combustion gas introduction means for separating hot water or water from residual combustion gas not dissolved in the hot water or water A gas-liquid separation means provided downstream of the water supply hot water supply path, a discharge path for discharging the residual combustion gas separated by the gas-liquid separation means from the gas-liquid separation means, and an oxidation catalyst provided in the combustion gas introduction path. Carbonated spring manufacturing equipment.
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湯または水に溶解す
る前記給水給湯路に設けた燃焼ガス導入手段と、湯また
は水とこの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に設けた脱硝触媒からなる
炭酸泉製造装置。2. A hot water supply passage through which hot water or water passes, a combustion gas introduction passage through which combustion gas containing carbon dioxide passes, and a combustion gas supplied from the combustion gas introduction passage are introduced into the hot water supply passage. Combustion gas introduction means provided in the water supply hot water supply path for dissolving carbon dioxide in combustion gas in hot water or water; and combustion gas introduction means for separating hot water or water from residual combustion gas not dissolved in the hot water or water A gas-liquid separating means provided downstream of the water supply hot water supply path, a discharge path for discharging the residual combustion gas separated by the gas-liquid separating means from the gas-liquid separating means, and a denitration catalyst provided in the combustion gas introduction path. Carbonated spring manufacturing equipment.
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湯または水に溶解す
る前記給水給湯路に設けた燃焼ガス導入手段と、湯また
は水とこの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に設けた脱硝触媒と、前記
脱硝触媒の下流側の前記燃焼ガス導入路に設けた酸化触
媒からなる炭酸泉製造装置。3. A hot water supply passage through which hot water or water passes, a combustion gas introduction passage through which combustion gas containing carbon dioxide passes, and a combustion gas supplied from the combustion gas introduction passage are introduced into the hot water supply passage. Combustion gas introduction means provided in the water supply hot water supply path for dissolving carbon dioxide in combustion gas in hot water or water; and combustion gas introduction means for separating hot water or water from residual combustion gas not dissolved in the hot water or water A gas-liquid separating means provided downstream of the water supply hot water supply path, a discharge path for discharging the residual combustion gas separated by the gas-liquid separating means from the gas-liquid separating means, and a denitration catalyst provided in the combustion gas introduction path. And an oxidation catalyst provided in the combustion gas introduction passage downstream of the denitration catalyst.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4022401A JP3047592B2 (en) | 1992-02-07 | 1992-02-07 | Carbonated spring production equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4022401A JP3047592B2 (en) | 1992-02-07 | 1992-02-07 | Carbonated spring production equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH05212086A JPH05212086A (en) | 1993-08-24 |
| JP3047592B2 true JP3047592B2 (en) | 2000-05-29 |
Family
ID=12081646
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4022401A Expired - Fee Related JP3047592B2 (en) | 1992-02-07 | 1992-02-07 | Carbonated spring production equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3047592B2 (en) |
-
1992
- 1992-02-07 JP JP4022401A patent/JP3047592B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH05212086A (en) | 1993-08-24 |
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