JP2598593B2 - Carbonated water heater - Google Patents
Carbonated water heaterInfo
- Publication number
- JP2598593B2 JP2598593B2 JP4279614A JP27961492A JP2598593B2 JP 2598593 B2 JP2598593 B2 JP 2598593B2 JP 4279614 A JP4279614 A JP 4279614A JP 27961492 A JP27961492 A JP 27961492A JP 2598593 B2 JP2598593 B2 JP 2598593B2
- Authority
- JP
- Japan
- Prior art keywords
- hot water
- water supply
- amount
- water
- supply
- 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)
- Devices For Medical Bathing And Washing (AREA)
Description
【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION
【0001】[0001]
【産業上の利用分野】本発明は、給湯バーナの排気路が
気水接触部を通過するように形成され、前記給湯バーナ
への燃料供給量が大なるほど前記給湯バーナに対する送
風手段による燃焼用空気の送風量を大に制御する送風制
御手段が設けられ、水または湯を前記気水接触部を通過
させて給湯する炭酸給湯状態と、前記気水接触部を通過
させずに給湯する一般給湯状態とに切り換える切り換え
手段が設けられた炭酸給湯装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a hot water supply burner in which an exhaust passage is formed so as to pass through a gas-water contact portion. As the amount of fuel supplied to the hot water supply burner increases, combustion air is blown to the hot water supply burner by a blowing means. A blower control means for largely controlling the amount of blown air is provided, and a carbonated hot water supply state in which water or hot water is supplied by passing through the air / water contact section and a general hot water supply state in which hot water is supplied without passing through the air / water contact section. The present invention relates to a carbonated water heater provided with switching means for switching between the two.
【0002】[0002]
【従来の技術】かかる炭酸給湯装置は、水または湯を気
水接触部を通過させることにより、その水または湯に給
湯バーナの排気中の炭酸ガスを溶解させ、その炭酸ガス
が溶解された水または湯を浴槽等に供給するようにした
ものであり、切り換え手段にて、このように気水接触部
を通過させて給湯する炭酸給湯状態と、気水接触部を通
過させずに給湯する一般給湯状態とに切り換えることが
できるようにしてある。2. Description of the Related Art In such a carbonated water heater, water or hot water is passed through a gas-water contact portion to dissolve carbon dioxide gas in the exhaust gas of a hot water supply burner into the water or hot water, and the water in which the carbon dioxide gas is dissolved is dissolved. Alternatively, hot water is supplied to a bathtub or the like, and the switching means uses a carbon dioxide hot water supply state in which hot water is supplied by passing through the air / water contact portion, and a general hot water supply without passing through the air / water contact portion. It can be switched to the hot water supply state.
【0003】かかる炭酸給湯装置において、従来は、送
風制御手段を、給湯バーナへの燃料供給量が大なるほど
給湯バーナに対する燃焼用空気の送風量を大に制御する
状態で、同じ値の燃料供給量に対する送風手段による燃
焼用空気の送風量を炭酸給湯状態と一般給湯状態のいず
れにおいても同じ値に制御するように構成して、炭酸給
湯状態と一般給湯状態のいずれにおいても燃料供給量に
適した燃焼用空気の量を送風するようにしていた。[0003] In such a carbonated water heater, conventionally, the air supply control means controls the air supply amount of the combustion air to the hot water supply burner to be larger as the fuel supply amount to the hot water supply burner is larger. Is configured to control the amount of combustion air blown by the blowing means to the same value in both the carbonated hot water supply state and the general hot water supply state, and is suitable for the fuel supply amount in both the carbonated hot water supply state and the general hot water supply state. The amount of combustion air was blown.
【0004】[0004]
【発明が解決しようとする課題】従って、上記従来技術
では、排気中の炭酸ガスの濃度は、燃料供給量の大小に
かかわらずほぼ一定であり、水または湯に対する排気中
の炭酸ガスの溶解度も、燃料供給量の大小にかかわらず
ほぼ一定である。ところで、給湯バーナへの燃料供給量
が小となると、炭酸ガスの発生量が少なくなる。従っ
て、上記従来技術では、燃料供給量が小のときは、炭酸
ガスの量が少ない分、炭酸給湯状態においては水または
湯に溶解する炭酸ガスの量が少ないので、浴槽等に供給
する水または湯の炭酸濃度が小さいという問題があっ
た。Therefore, in the above prior art, the concentration of carbon dioxide in the exhaust gas is substantially constant regardless of the amount of fuel supply, and the solubility of the carbon dioxide gas in the exhaust gas with respect to water or hot water is also high. , And is substantially constant regardless of the amount of fuel supply. By the way, when the amount of fuel supply to the hot water supply burner is small, the amount of generated carbon dioxide is small. Therefore, in the above-described conventional technology, when the fuel supply amount is small, the amount of carbon dioxide gas is small, and the amount of carbon dioxide gas dissolved in water or hot water is small in the carbonic acid hot water supply state. There was a problem that the carbonic acid concentration of the hot water was low.
【0005】本発明は、かかる実情に鑑みてなされたも
のであり、その目的は、上記従来技術における問題を解
消する点にある。[0005] The present invention has been made in view of such circumstances, and an object thereof is to solve the above-mentioned problems in the prior art.
【0006】[0006]
【課題を解決するための手段】本発明による炭酸給湯装
置の特徴構成は、前記送風制御手段が、同じ値の前記燃
料供給量に対する前記送風量を前記炭酸給湯状態におい
ては前記一般給湯状態よりも小に制御するように構成さ
れている点にある。The characteristic structure of the carbonic water heater according to the present invention is that the blower control means sets the blower amount for the same fuel supply amount as the carbonated hot water supply state more than the general hot water supply state. The point is that it is configured to be controlled to small.
【0007】[0007]
【作用】上記特徴構成によれば、同じ値の燃料供給量に
対する送風量は、炭酸給湯状態においては一般給湯状態
よりも小となるので、炭酸給湯状態においては、同じ値
の燃料供給量における排気中の炭酸ガスの濃度を、従来
技術に比して大きくすることができる。従って、燃料供
給量が小のときでも、従来技術に比して、排気中の炭酸
ガスの濃度が大きくなって、水または湯に対する排気中
の炭酸ガスの溶解度も大きくすることができるので、水
または湯に溶解する炭酸ガスの量を増大することができ
る。According to the above-mentioned characteristic configuration, the amount of air blown for the same amount of fuel supply is smaller in the carbonated hot water supply state than in the general hot water supply state. The concentration of the carbon dioxide gas therein can be increased as compared with the prior art. Therefore, even when the fuel supply amount is small, the concentration of carbon dioxide in the exhaust gas becomes higher than in the conventional technology, and the solubility of the carbon dioxide gas in the exhaust gas with respect to water or hot water can be increased. Alternatively, the amount of carbon dioxide dissolved in hot water can be increased.
【0008】ちなみに、一般給湯状態においても、前述
の炭酸給湯状態におけるのと同様に、送風量を小に制御
することが想定される。しかしながら、燃料供給量が小
のときに、送風量を燃料供給量に適した量よりも小とす
ると、排気中の水蒸気の濃度が大きくなって熱交換器等
に結露が発生し易くなり、熱交換器等の耐久性が低下す
るという問題がある。従って、この問題を回避するため
に、排気中の炭酸ガスの濃度を大きくする必要がない一
般給湯状態においては、熱交換器等への結露の発生を確
実に防止できるように十分な安全係数を加味してある燃
料供給量に適した送風量に制御する。By the way, in the general hot water supply state, it is supposed that the blowing amount is controlled to be small as in the above-mentioned carbonic acid hot water supply state. However, if the air supply amount is smaller than the amount suitable for the fuel supply amount when the fuel supply amount is small, the concentration of water vapor in the exhaust gas becomes large, and dew condensation easily occurs in a heat exchanger and the like. There is a problem that the durability of the exchanger and the like is reduced. Therefore, in order to avoid this problem, in a general hot water supply state in which it is not necessary to increase the concentration of carbon dioxide gas in the exhaust gas, a sufficient safety factor is set so that the occurrence of dew condensation on the heat exchanger or the like can be reliably prevented. The air flow is controlled to be suitable for the added fuel supply amount.
【0009】尚、炭酸給湯状態においては、前記安全係
数を小さくすることにより、同じ値の燃料供給量に対す
る送風量を一般給湯状態よりも小とするが、その送風量
を一般給湯状態よりも小とする範囲は、熱交換器等の耐
久性に問題が生じない程度の範囲とする。In the carbonated hot water supply state, by reducing the safety coefficient, the amount of air blown for the same fuel supply amount is made smaller than that of the ordinary hot water supply state, but the amount of air blown is made smaller than that of the general hot water supply state. Should be within a range that does not cause a problem in durability of the heat exchanger and the like.
【0010】[0010]
【発明の効果】その結果、炭酸給湯状態において、燃料
供給量が小のときでも、従来技術に比して、水または湯
に溶解する炭酸ガスの量を増大することができるので、
浴槽等に供給する水または湯の炭酸濃度が小さいといっ
た上記従来技術における問題を解消することができるよ
うになった。As a result, even when the fuel supply amount is small in the carbonated hot water supply state, the amount of carbon dioxide dissolved in water or hot water can be increased as compared with the prior art.
It has become possible to solve the above-described problem in the prior art in which the concentration of carbon dioxide in water or hot water supplied to a bathtub or the like is low.
【0011】[0011]
【実施例】以下、本発明の実施例を図面に基づいて説明
する。先ず、図1に基づいて、炭酸給湯装置の全体構成
について説明する。Embodiments of the present invention will be described below with reference to the drawings. First, the overall configuration of the carbonic water heater will be described with reference to FIG.
【0012】浴槽2と、その浴槽2に湯水を供給する給
湯部Aと、浴槽水を加熱する追焚部Bと、制御部Cと、
その制御部Cに対して指令を与えるリモートコントロー
ラRと、気水接触部1と、一般給湯栓8とが設けられて
いる。気水接触部1は、給湯部Aから浴槽2に対する湯
水の供給を中継する。給湯部Aには、給湯用熱交換器3
と給湯バーナ4が、追焚部Bには追焚用熱交換器5と追
焚バーナ6が夫々備えられている。A bathtub 2, a hot water supply unit A for supplying hot and cold water to the bathtub 2, a reheating unit B for heating the bathtub water, and a control unit C;
A remote controller R for giving commands to the control unit C, the air / water contact unit 1, and a general hot water tap 8 are provided. The air / water contact unit 1 relays the supply of hot water from the hot water supply unit A to the bathtub 2. The hot water supply unit A has a heat exchanger 3 for hot water supply.
And a hot water supply burner 4, and a reheating unit B is provided with a reheating heat exchanger 5 and a reheating burner 6, respectively.
【0013】給湯用熱交換器3に水を供給する給水路W
1と、給湯用熱交換器3の出口側から気水接触部1に湯
を供給する浴槽用給湯路W2が設けられている。浴槽用
給湯路W2から一般給湯栓8に湯を供給する一般用給湯
路W3が分岐接続されている。又、浴槽2と追焚用熱交
換器5との間で浴槽水を循環させる循環路W4が設けら
れている。Water supply channel W for supplying water to hot water supply heat exchanger 3
1 and a bath water supply passage W2 for supplying hot water from the outlet side of the heat exchanger 3 for hot water supply to the air / water contact portion 1. A general hot water supply passage W3 for supplying hot water from the bathtub hot water supply passage W2 to the general hot water tap 8 is branched and connected. A circulation path W4 for circulating bath water is provided between the bath 2 and the additional heat exchanger 5.
【0014】給水路W1には、浴槽2と給湯用熱交換器
3とに対する給水量を検出する水量センサS1と給水温
度を検出する水温サーミスタS2が、浴槽用給湯路W2
には、給湯用熱交換器3の出湯温度を検出する出湯温サ
ーミスタS3と気水接触室1に対して水を供給する供給
状態と供給しない非供給状態とを切り換える電磁弁7
が、一般用給湯路W3には、一般給湯栓8の開栓を検出
する水流スイッチS4が、循環路W4には、循環ポンプ
9と浴槽水温度Txを検出する浴槽温サーミスタS5と
浴槽水位を検出する水位センサS6が夫々介装されてい
る。In the water supply passage W1, a water amount sensor S1 for detecting the amount of water supplied to the bathtub 2 and the heat exchanger 3 for hot water supply and a water temperature thermistor S2 for detecting the supply water temperature are provided.
A hot water temperature thermistor S3 for detecting the hot water temperature of the hot water supply heat exchanger 3 and a solenoid valve 7 for switching between a supply state in which water is supplied to the air / water contact chamber 1 and a non-supply state in which water is not supplied.
In the general hot water supply channel W3, a water flow switch S4 for detecting opening of the general hot water tap 8 is provided. Water level sensors S6 to be detected are provided respectively.
【0015】両バーナ4,6には、夫々ガス供給を断続
するガス弁41,61と、ガス供給量を調節するガス比
例弁42,62と、燃焼用空気を送風する送風手段とし
てのファン43,63とが備えられている。The burners 4 and 6 have gas valves 41 and 61 for intermitting gas supply, gas proportional valves 42 and 62 for adjusting gas supply, and a fan 43 as a blower for blowing air for combustion. , 63 are provided.
【0016】次に、図1に基づいて、気水接触部1につ
いて説明を加える。Next, the air / water contact portion 1 will be described with reference to FIG.
【0017】金属ケーシング11内に、湯を噴霧する噴
霧ノズル12と、充填層13とが装着されている。噴霧
ノズル12は、浴槽用給湯路W2に接続されている。充
填層13は、ステンレス線を立体格子状に編組形成した
ものである。充填層13の側方には、給湯部Aの排気路
Hと連通する排気供給口14が形成されている。この排
気供給口14から供給された高温の排気は、充填層13
を加熱してから上方の排気吐出口15から排出される。
つまり、排気路Hが気水接触部1を通過するように形成
されている。噴霧された湯滴は、充填層13で熱を奪わ
れた排気と接触して、排気中の炭酸ガスを溶解すると共
に、充填層13から熱を奪う。A spray nozzle 12 for spraying hot water and a packed layer 13 are mounted in a metal casing 11. Spray nozzle 12 is connected to bathtub hot water supply passage W2. The filling layer 13 is formed by braiding a stainless wire into a three-dimensional lattice. An exhaust supply port 14 communicating with the exhaust passage H of the hot water supply unit A is formed on the side of the packed layer 13. The high-temperature exhaust gas supplied from the exhaust gas supply port 14
Is heated and then discharged from the upper exhaust discharge port 15.
That is, the exhaust passage H is formed so as to pass through the water / water contact portion 1. The sprayed droplets come into contact with the exhaust gas whose heat has been taken away by the packed bed 13, dissolve carbon dioxide in the exhaust gas, and take away heat from the packed bed 13.
【0018】リモートコントローラRには、運転スイッ
チ20、湯張スイッチ21、浴槽水の目標温度Tsを設
定する湯張温度設定スイッチ22、浴槽2の目標水位を
設定する水位設定スイッチ23、及び一般給湯の目標温
度Tsを設定する一般温度設定スイッチ24の夫々が設
けられている。The remote controller R includes an operation switch 20, a hot water switch 21, a hot water temperature setting switch 22 for setting a target temperature Ts of bath water, a water level setting switch 23 for setting a target water level of the bathtub 2, and a general hot water supply. Each of the general temperature setting switches 24 for setting the target temperature Ts is provided.
【0019】制御部Cには、水量センサS1、水温サー
ミスタS2、出湯温サーミスタS3、水流スイッチS
4、浴槽温サーミスタS5、水位センサS6及びリモー
トコントローラRの夫々が接続されている。そして、制
御部Cは、予め設定記憶された情報及び各種の入力情報
に基づいて、電磁弁7、ガス弁41、61、ガス比例弁
42,62、ファン43,63の作動を制御して、給湯
バーナ4への燃料供給量Gpが大なるほど給湯バーナ4
に対するファン43による燃焼用空気の送風量を大にす
るように、ファン43の回転数Nsを大に制御すると共
に、湯を気水接触部1を通過させて浴槽2に給湯する炭
酸給湯状態と、気水接触部1を通過させずに一般給湯栓
20に給湯する一般給湯状態とに切り換える。つまり、
制御部Cを利用して、送風制御手段101と切り換え手
段102とが構成されている。The control section C includes a water amount sensor S1, a water temperature thermistor S2, a tap water temperature thermistor S3, and a water flow switch S.
4. Each of the bathtub temperature thermistor S5, the water level sensor S6, and the remote controller R is connected. Then, the control unit C controls the operations of the solenoid valve 7, the gas valves 41 and 61, the gas proportional valves 42 and 62, and the fans 43 and 63 based on the information set and stored in advance and various input information. As the fuel supply amount Gp to the hot water supply burner 4 increases, the hot water supply
The number of revolutions Ns of the fan 43 is controlled to be large so as to increase the amount of combustion air blown by the fan 43 with respect to the temperature, and the hot water is supplied to the bathtub 2 by passing hot water through the air / water contact portion 1. The state is switched to a general hot water supply state in which hot water is supplied to the general hot water tap 20 without passing through the air / water contact portion 1. That is,
Utilizing the control unit C, an air blowing control unit 101 and a switching unit 102 are configured.
【0020】図4に基づいて、ファン43の回転数Ns
の制御について説明する。ファン43の回転数Nsと、
給湯バーナ4への燃料供給量Gpとは、図4に示す関係
がある。図4中の実線(イ)は一般給湯状態の場合(A
モード)、図4中の破線(ロ)は炭酸給湯状態の場合
(Bモード)を示す。図中G1は最小燃料供給量、G2
は最大燃料供給量、N1は最小燃料供給量G1に対する
回転数、N2は最大燃料供給量G2に対する回転数であ
る。つまり、同じ値の燃料供給量Gpに対する回転数N
sを炭酸給湯状態においては一般給湯状態よりも小にす
るようにしてあり、もって、同じ値の燃料供給量Gpに
対する送風量を炭酸給湯状態においては一般給湯状態よ
りも小に制御するようにしてある。Referring to FIG. 4, the rotation speed Ns of the fan 43
Will be described. The rotation speed Ns of the fan 43,
The fuel supply amount Gp to the hot water supply burner 4 has a relationship shown in FIG. The solid line (A) in FIG. 4 indicates the case of the general hot water supply state (A
Mode), and the broken line (b) in FIG. 4 shows the case of the carbonated hot water supply state (B mode). In the figure, G1 is the minimum fuel supply amount, G2
Is the maximum fuel supply amount, N1 is the rotation speed for the minimum fuel supply amount G1, and N2 is the rotation speed for the maximum fuel supply amount G2. That is, the rotation speed N for the same value of the fuel supply amount Gp
In the carbonated hot water supply state, s is set to be smaller than that in the general hot water supply state, so that the air blowing rate for the same fuel supply amount Gp is controlled to be smaller in the carbonated hot water supply state than in the general hot water supply state. is there.
【0021】尚、図4中の(ハ)は、給湯用熱交換器3
の表面等に結露が発生する結露限界を示している。そし
て、一般給湯状態の場合は、給湯用熱交換器3への結露
の発生を確実に防止できる送風量になるように、前記結
露限界に対して十分な安全係数を加味した回転数Nsに
なるようにしてある。又、炭酸給湯状態の場合において
は、給湯用熱交換器3の耐久性に問題が生じない程度の
範囲で前記安全係数を小さくすることにより、同じ値の
燃料供給量Gpに対する回転数Nsを一般給湯状態より
も小にするようにしてある。(C) in FIG. 4 is a heat exchanger 3 for hot water supply.
Indicates the dew condensation limit at which dew condensation occurs on the surface and the like. In the case of the general hot water supply state, the rotation speed Ns takes into account a sufficient safety coefficient with respect to the dew condensation limit so that the amount of air to be blown can be reliably prevented from being generated on the heat exchanger 3 for hot water supply. It is like that. Further, in the case of the carbonated hot water supply state, the rotation speed Ns for the fuel supply amount Gp of the same value is generally reduced by reducing the safety coefficient to such an extent that the durability of the hot water supply heat exchanger 3 does not cause a problem. It is set to be smaller than the hot water supply state.
【0022】燃料供給量Gpは、給湯用熱交換器3に対
する給水量と、給水温度、及び、目標温度Ts等に基づ
いて決定される。燃料供給量Gpを求めた後は、一般給
湯状態では図4中の(イ)に、炭酸給湯状態では図4中
の(ロ)に夫々示す関係からファン43の回転数Nsを
求める。The fuel supply amount Gp is determined based on a water supply amount to the hot water supply heat exchanger 3, a water supply temperature, a target temperature Ts, and the like. After the fuel supply amount Gp is obtained, the rotational speed Ns of the fan 43 is obtained from the relationship shown in FIG. 4A in the general hot water supply state, and from the relationship shown in FIG.
【0023】一般給湯状態と炭酸給湯状態との切り換え
について説明する。湯張スイッチ21がONされると炭
酸給湯状態となる。一般給湯栓8が開栓されて水流スイ
ッチS4がONすると、一般給湯状態となる。但し、一
般給湯状態の方が優先される。つまり、炭酸給湯状態に
おいて、一般給湯栓8が開栓されると、割り込み信号が
発生して炭酸給湯状態を一旦中止して一般給湯状態とな
る。そして、一般給湯栓8が閉栓されると、炭酸給湯状
態に復帰する。Switching between the general hot water supply state and the carbonated hot water supply state will be described. When the hot water switch 21 is turned on, a carbonated hot water supply state is set. When the general hot water tap 8 is opened and the water flow switch S4 is turned on, a general hot water supply state is set. However, the general hot water supply state has priority. In other words, when the general hot water tap 8 is opened in the carbonated hot water supply state, an interrupt signal is generated, the carbonated hot water supply state is temporarily stopped, and the general hot water supply state is set. When the general hot water tap 8 is closed, the hot water supply state is restored.
【0024】次に、図2に示すフローチャートに基づい
て、浴槽2への給湯(炭酸給湯状態)における制御部C
の動作を説明する。Next, based on the flowchart shown in FIG. 2, the control unit C in hot water supply to the bathtub 2 (carbonated hot water supply state).
Will be described.
【0025】運転スイッチ20をONにした状態におい
て湯張スイッチ21をON操作すると、先ず、水位セン
サS6の検出情報に基づいて、浴槽水位が設定水位に達
しているか否か判別する。浴槽水位が設定水位に達して
いないときには、制御部Cに浴槽2への給湯指令が与え
られる。尚、浴槽水位が設定水位に達しているときにつ
いては後述する。When the hot water switch 21 is turned on while the operation switch 20 is turned on, first, it is determined whether or not the bathtub water level has reached the set water level based on the detection information of the water level sensor S6. When the bathtub water level has not reached the set water level, the controller C is given a hot water supply command to the bathtub 2. The case where the bathtub water level has reached the set water level will be described later.
【0026】給湯指令が与えられると、先ず、電磁弁7
を開にする。このときの給水量、給水温度、湯張温度設
定スイッチ22で設定された目標温度Ts等に基づい
て、燃料供給量Gpを求める。それから、図4中の
(ロ)に示す関係からファン43の目標回転数Nsを求
める。求められた燃料供給量Gp及び目標回転数Nsに
なるように出力を制御する(Bモード)。When a hot water supply command is given, first, the solenoid valve 7
Open. At this time, the fuel supply amount Gp is obtained based on the water supply amount, the water supply temperature, the target temperature Ts set by the hot water temperature setting switch 22, and the like. Then, the target rotation speed Ns of the fan 43 is obtained from the relationship shown in (b) in FIG. The output is controlled so as to achieve the obtained fuel supply amount Gp and target rotation speed Ns (B mode).
【0027】浴槽水位が設定水位に達すると浴槽2への
給湯を停止する。給湯停止後及び前述の浴槽水位が設定
水位に達しているときには、循環ポンプ9を作動させ
て、浴槽温サーミスタS5の検出情報に基づいて、浴槽
水温度Txが目標温度Tsを越えているか否かチェック
する。越えていないときは、浴槽水温度Txが目標温度
Tsに達するまで追焚する。越えているときは何もしな
い。以上の動作を湯張スイッチ21がOFFされるまで
実行する。When the bathtub water level reaches the set water level, hot water supply to the bathtub 2 is stopped. After stopping the hot water supply and when the bathtub water level has reached the set water level, the circulating pump 9 is operated to determine whether or not the bathtub water temperature Tx exceeds the target temperature Ts based on the detection information of the bathtub temperature thermistor S5. To check. If not, additional heating is performed until the bathtub water temperature Tx reaches the target temperature Ts. If it does, do nothing. The above operation is executed until the hot water switch 21 is turned off.
【0028】次に、図3に示すフローチャートに基づい
て、一般給湯栓8への給湯(一般給湯状態)における制
御部Cの動作を説明する。Next, the operation of the control section C in hot water supply to the general hot water tap 8 (general hot water supply state) will be described with reference to the flowchart shown in FIG.
【0029】一般給湯栓8が開栓されて水流スイッチS
4がONすると、割込処理を実行する。先ず、炭酸給湯
状態であるか等のステイタスをメモリに格納する。尚、
炭酸給湯状態であれば、電磁弁7を閉じて浴槽2への給
湯を一旦停止する。The general hot water tap 8 is opened and the water flow switch S
When 4 is turned on, an interrupt process is executed. First, the status such as the state of the carbonated hot water supply state is stored in the memory. still,
If it is in the carbonated hot water supply state, the electromagnetic valve 7 is closed and the hot water supply to the bathtub 2 is temporarily stopped.
【0030】次に、給水量、給水温度、一般温度設定ス
イッチ24で設定された目標温度Ts等に基づいて、燃
料供給量Gpを求める。それから、図4中の(イ)に示
す関係からファン43の目標回転数Nsを求める。求め
られた燃料供給量Gp及び目標回転数Nsになるように
出力を制御する(Aモード)。以上の動作を一般給湯栓
8が閉栓されるまで継続する。尚、割込処理を終了する
ときには、格納されたステイタスを読み出す。Next, the fuel supply amount Gp is determined based on the water supply amount, the water supply temperature, the target temperature Ts set by the general temperature setting switch 24, and the like. Then, the target rotation speed Ns of the fan 43 is obtained from the relationship shown in FIG. The output is controlled so that the fuel supply amount Gp and the target rotation speed Ns are obtained (A mode). The above operation is continued until the general hot water tap 8 is closed. When the interrupt processing is completed, the stored status is read.
【0031】〔別実施例〕上記実施例では、送風手段4
3による燃焼用空気の送風量を制御するに、送風制御手
段101が送風手段43の回転数を制御するようにして
いたが、送風手段43の駆動電力を制御するようにして
もよい。[Another Embodiment] In the above embodiment, the blowing means 4
Although the blowing control means 101 controls the rotation speed of the blowing means 43 to control the amount of combustion air blown by 3, the driving power of the blowing means 43 may be controlled.
【0032】上記実施例では、湯を給湯部Aの給湯バー
ナ4の排気と接触させていたが、水を接触させても良
い。又、湯又は水を追焚部Bの追焚バーナ6の排気と接
触させてもよい。In the above embodiment, the hot water is brought into contact with the exhaust gas of the hot water supply burner 4 of the hot water supply section A, but it may be brought into contact with water. In addition, hot water or water may be brought into contact with the exhaust gas from the reheating burner 6 of the reheating unit B.
【0033】尚、特許請求の範囲の項に図面との対照を
便利にするために符号を記すが、該記入により本発明は
添付図面の構成に限定されるものではない。Incidentally, reference numerals are written in the claims for convenience of comparison with the drawings, but the present invention is not limited to the configuration of the attached drawings by the entry.
【図1】本発明の実施例にかかる炭酸給湯装置の全体構
成のブロック図FIG. 1 is a block diagram of the overall configuration of a carbonic water heater according to an embodiment of the present invention.
【図2】炭酸給湯装置の制御作動のフローチャートを示
す図FIG. 2 is a diagram showing a flowchart of a control operation of the carbonated water heater.
【図3】炭酸給湯装置の制御作動のフローチャートを示
す図FIG. 3 is a view showing a flowchart of a control operation of the carbonated water heater.
【図4】給湯バーナへの燃料供給量と送風手段による燃
焼用空気の送風量との関係を示す図FIG. 4 is a diagram showing the relationship between the amount of fuel supplied to a hot water supply burner and the amount of combustion air blown by a blowing means.
1 気水接触部 4 給湯バーナ 43 送風手段 101 送風制御手段 102 切り換え手段 H 排気路 Gp 燃料供給量 DESCRIPTION OF SYMBOLS 1 Air-water contact part 4 Hot-water supply burner 43 Blowing means 101 Blowing control means 102 Switching means H Exhaust path Gp Fuel supply amount
Claims (1)
接触部(1)を通過するように形成され、前記給湯バー
ナ(4)への燃料供給量(Gp)が大なるほど前記給湯
バーナ(4)に対する送風手段(43)による燃焼用空
気の送風量を大に制御する送風制御手段(101)が設
けられ、水または湯を前記気水接触部(1)を通過させ
て給湯する炭酸給湯状態と、前記気水接触部(1)を通
過させずに給湯する一般給湯状態とに切り換える切り換
え手段(102)が設けられた炭酸給湯装置であって、 前記送風制御手段(101)が、同じ値の前記燃料供給
量(Gp)に対する前記送風量を前記炭酸給湯状態にお
いては前記一般給湯状態よりも小に制御するように構成
されている炭酸給湯装置。1. An exhaust passage (H) of a hot water supply burner (4) is formed so as to pass through a water / water contact portion (1), and the larger the amount of fuel supply (Gp) to the hot water supply burner (4), the more the above-mentioned. Air supply control means (101) for controlling the amount of combustion air blown by the air supply means (43) to the hot water supply burner (4) is provided, and water or hot water is passed through the air / water contact section (1) to supply hot water. A hot-water supply apparatus provided with switching means (102) for switching between a hot-water supply state in which the hot water is supplied and a general hot-water supply state in which hot water is supplied without passing through the air / water contact portion (1); However, the carbon dioxide hot water supply device is configured to control the blowing amount for the fuel supply amount (Gp) of the same value to be smaller in the carbonated hot water supply state than in the general hot water supply state.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4279614A JP2598593B2 (en) | 1992-10-19 | 1992-10-19 | Carbonated water heater |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4279614A JP2598593B2 (en) | 1992-10-19 | 1992-10-19 | Carbonated water heater |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH06129708A JPH06129708A (en) | 1994-05-13 |
JP2598593B2 true JP2598593B2 (en) | 1997-04-09 |
Family
ID=17613441
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4279614A Expired - Fee Related JP2598593B2 (en) | 1992-10-19 | 1992-10-19 | Carbonated water heater |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2598593B2 (en) |
-
1992
- 1992-10-19 JP JP4279614A patent/JP2598593B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH06129708A (en) | 1994-05-13 |
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