JP2002130830A - Hot water supply apparatus - Google Patents
Hot water supply apparatusInfo
- Publication number
- JP2002130830A JP2002130830A JP2000319065A JP2000319065A JP2002130830A JP 2002130830 A JP2002130830 A JP 2002130830A JP 2000319065 A JP2000319065 A JP 2000319065A JP 2000319065 A JP2000319065 A JP 2000319065A JP 2002130830 A JP2002130830 A JP 2002130830A
- Authority
- JP
- Japan
- Prior art keywords
- neutralizer
- water
- neutralizing agent
- heat exchanger
- detecting
- 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.)
- Withdrawn
Links
Landscapes
- Instantaneous Water Boilers, Portable Hot-Water Supply Apparatuses, And Control Of Portable Hot-Water Supply Apparatuses (AREA)
- Details Of Fluid Heaters (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、燃焼排気ガスと熱
交換して温水を得る給湯器に関し、詳しくは燃焼排気ガ
スの排気潜熱までも回収するようにした給湯器に関する
ものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water heater for obtaining hot water by exchanging heat with combustion exhaust gas, and more particularly to a water heater for recovering even the latent heat of exhaust gas from combustion exhaust gas.
【0002】[0002]
【従来の技術】一般に潜熱まで回収する給湯器は図1に
示すように構成されている。燃焼室1にはガス等の燃料
を燃焼させる燃焼バーナ2と、燃焼バーナ2の燃焼排気
ガスと熱交換する熱交換器3とを配置してある。熱交換
器3は燃焼排気ガスの流れ方向の上流側に位置する主熱
交換器部3aと、この燃焼排気ガスの流れ方向の下流側
に位置する副熱交換器3bとを有している。熱交換器3
の副熱交換器部3bには加熱される水を供給するための
給水流路4を接続してあり、熱交換器3の主熱交換器部
3aには熱交換器3で加熱された水を出湯するための出
湯流路5を接続してある。燃焼室1には副熱交換部3a
で発生した凝縮水を受け止めるドレンパン6を配置して
あり、ドレンパン6で受けた凝縮水を排出するドレン排
出流路7をドレンパン6に接続してある。ドレン排水流
路7の途中には中和器8を配置してあり、中和器8には
CaCO3のような中和剤を装填してある。2. Description of the Related Art In general, a water heater for recovering latent heat is configured as shown in FIG. A combustion burner 2 for burning fuel such as gas and a heat exchanger 3 for exchanging heat with the combustion exhaust gas of the combustion burner 2 are arranged in the combustion chamber 1. The heat exchanger 3 has a main heat exchanger section 3a located on the upstream side in the flow direction of the combustion exhaust gas, and a sub heat exchanger 3b located on the downstream side in the flow direction of the combustion exhaust gas. Heat exchanger 3
A water supply flow path 4 for supplying water to be heated is connected to the sub-heat exchanger section 3b, and the water heated by the heat exchanger 3 is connected to the main heat exchanger section 3a of the heat exchanger 3. Is connected to a tapping channel 5 for tapping. The combustion chamber 1 has a sub heat exchange section 3a
A drain pan 6 for receiving the condensed water generated by the drain pan 6 is disposed, and a drain discharge channel 7 for discharging the condensed water received by the drain pan 6 is connected to the drain pan 6. A neutralizer 8 is arranged in the middle of the drain drain passage 7, and the neutralizer 8 is loaded with a neutralizing agent such as CaCO 3 .
【0003】かかる給湯器では燃焼バーナ2で燃料を燃
焼させると共に給水流路4から給水すると、水が熱交換
器3を通るとき燃焼排気ガスの熱と熱交換されて水が加
熱され、加熱された水が出湯流路5から供給される。熱
交換器3で熱交換するとき主熱交換器部3aでは主に顕
熱交換されるが、副熱交換器部3bでは顕熱交換以外に
潜熱交換される。このように副熱交換器部3bで潜熱も
回収するようにすることで熱効率を向上することができ
る。このとき、副熱交換器部3bで潜熱も回収するため
に副熱交換器部3bで燃焼排気ガスが過冷却されるため
に凝縮水が発生し、凝縮水がドレンパン6に受けられ、
ドレンパン6からドレン排出流路7を経て排出される。
そして燃焼排気ガスが過冷却されることで発生する凝縮
水は強酸性であるため、そのまま排出することができな
く、中和器8に通すことで中和させてから排出される。In such a water heater, when fuel is burned by the combustion burner 2 and water is supplied from the water supply passage 4, when the water passes through the heat exchanger 3, the heat is exchanged with the heat of the combustion exhaust gas to heat the water. The hot water is supplied from the hot water flow path 5. When heat is exchanged in the heat exchanger 3, sensible heat is mainly exchanged in the main heat exchanger 3a, but latent heat is exchanged in the sub heat exchanger 3b in addition to sensible heat exchange. As described above, latent heat is recovered by the sub heat exchanger section 3b, so that thermal efficiency can be improved. At this time, condensed water is generated because the combustion exhaust gas is supercooled in the sub heat exchanger 3b to recover latent heat in the sub heat exchanger 3b, and the condensed water is received by the drain pan 6,
It is discharged from a drain pan 6 through a drain discharge channel 7.
The condensed water generated by supercooling the combustion exhaust gas cannot be discharged as it is because it is strongly acidic, and is discharged after passing through the neutralizer 8 to be neutralized.
【0004】[0004]
【発明が解決しようとする課題】ところで、中和器8は
内部に装填した中和剤で凝縮水を中和するものであり、
中和剤が消耗するものであるために消耗したときに中和
剤を交換しなけばならない。ところが従来は中和器8の
中和剤がどれくらい消耗しているか的確な検知ができ
ず、適切な中和剤の交換ができないという問題がある。
つまり、従来は中和剤の消耗量を実験的に確認し、給湯
器の運転時間によりその消耗量を予測的に判断し、中和
剤の交換時期を決めているので実際とは異なる中和剤の
消耗量で交換してしまうという問題がある。中和剤の消
耗量は給湯器の運転時間により一義的に決められるもの
でなく、給湯器の運転モードや気象条件等で大きく変動
するものである。このため中和剤がさほど消耗していな
いのに中和剤を交換してしまう無駄を生じたり、中和剤
の処理能力が低下しているのに拘わらず運転してしまう
という弊害が生じるという問題がある。The neutralizer 8 neutralizes condensed water with a neutralizing agent charged therein.
Since the neutralizing agent is exhausted, the neutralizing agent must be replaced when exhausted. However, conventionally, there is a problem that it is not possible to accurately detect how much the neutralizing agent in the neutralizer 8 has been consumed, and it is not possible to appropriately replace the neutralizing agent.
In other words, in the past, the amount of consumption of the neutralizing agent was experimentally confirmed, the amount of consumption was predictively determined based on the operation time of the water heater, and the time for replacing the neutralizing agent was determined. There is a problem that the agent is replaced by the consumed amount of the agent. The amount of consumption of the neutralizing agent is not uniquely determined by the operation time of the water heater, but greatly varies depending on the operation mode of the water heater, weather conditions, and the like. For this reason, there is a waste that the neutralizing agent is replaced when the neutralizing agent is not consumed so much, or a problem that the operation is performed even though the processing capacity of the neutralizing agent is reduced occurs. There's a problem.
【0005】本発明は叙述の点に鑑みてなされたもので
あって、中和剤の消耗度合いを的確に検出して適切な時
期に中和剤の交換ができる給湯器を提供することを課題
とする。The present invention has been made in view of the above description, and has as its object to provide a water heater capable of accurately detecting the degree of consumption of a neutralizing agent and replacing the neutralizing agent at an appropriate time. And
【0006】[0006]
【課題を解決するための手段】上記課題を解決するため
本発明の給湯器は、燃焼室1に配置された燃焼バーナ2
と、前記燃焼バーナ2の燃焼排気ガスの熱と熱交換して
水を加熱する熱交換器3と、前記熱交換器3に加熱され
る水を供給する給水流路4と、前記熱交換器3にて加熱
された水を出湯する出湯流路5とを具備する給湯器であ
って、前記熱交換器3は、燃焼排気ガスの流れの上流側
に位置する主熱交換器部3aとこの燃焼排気ガスの流れ
の下流側に位置する副熱交換器部3bとを有し、前記燃
焼室1には前記副熱交換器部3bにて発生した凝縮水を
受け止めるためのドレンパン6を配設し、前記ドレンパ
ン6の凝縮水を排水するためのドレン排水流路7を前記
ドレンパン6に連結すると共に前記ドレン排水流路7に
て排水される凝縮水を中和する中和器8を前記ドレン排
水流路7に配設し、前記中和器8の質量変化を検出する
ことにより前記中和器8内の中和剤の消耗度合いを検出
する検出手段を設けて成ることを特徴とする。In order to solve the above-mentioned problems, a water heater according to the present invention comprises a combustion burner 2 disposed in a combustion chamber 1.
A heat exchanger 3 for exchanging heat with the heat of the combustion exhaust gas of the combustion burner 2 to heat water; a water supply passage 4 for supplying water to be heated to the heat exchanger 3; A hot water supply path 5 for discharging the water heated in 3, wherein the heat exchanger 3 includes a main heat exchanger section 3a located upstream of the flow of the combustion exhaust gas and a main heat exchanger section 3a. A sub-heat exchanger section 3b positioned downstream of the flow of the combustion exhaust gas, and a drain pan 6 for receiving condensed water generated in the sub-heat exchanger section 3b is provided in the combustion chamber 1. Then, a drain drain passage 7 for draining condensed water of the drain pan 6 is connected to the drain pan 6 and a neutralizer 8 for neutralizing condensed water discharged in the drain drain passage 7 is connected to the drain. It is disposed in the drainage channel 7 and detects the change in the mass of the neutralizer 8 to detect Characterized in that it comprises providing a detecting means for detecting the exhaustion degree of the neutralizing agent in the vessel 8.
【0007】上記のように中和器8の質量変化を検出す
ることにより中和器8内の中和剤の消耗度合いを検出す
る検出手段を設けたため、中和器8内に存在する中和剤
の質量を定量的に検出して中和剤の消耗度合いを検知で
き、中和剤の消耗度合いを正確に検知できて適切な時期
に中和剤の交換ができる。As described above, since the detecting means for detecting the degree of consumption of the neutralizing agent in the neutralizer 8 by detecting the change in the mass of the neutralizer 8 is provided, the neutralization existing in the neutralizer 8 is provided. It is possible to detect the degree of consumption of the neutralizing agent by quantitatively detecting the mass of the agent, to accurately detect the degree of consumption of the neutralizing agent, and to replace the neutralizing agent at an appropriate time.
【0008】また前記中和器8は、上記凝縮水が流入口
10から流入すると共に前記中和器8内の中和剤で中和
した処理水を流出口11からオーバーフローにて流出さ
せるようにして常に一定水位に保たれる構造とし、前記
検出手段は、前記中和器8の質量変化を検出することに
より中和剤と水の比重の差により中和剤の消耗度合いを
検出することを特徴とすることも好ましい。この場合、
中和剤と水が入った状態で中和器8の質量の変化を検出
するものでも、中和剤と水との比重差により中和剤の消
耗度合いを正確に検知できる。また中和器8内の水の水
位を一定に保った状態で検出するために何時でも精度高
く中和剤の消耗度合いを検知できて一層適切な時期に中
和剤の交換ができ、また中和剤の消耗度合いを検知する
制御も容易にできる。The neutralizer 8 allows the condensed water to flow in from the inlet 10 and causes the treated water neutralized by the neutralizing agent in the neutralizer 8 to flow out from the outlet 11 by overflow. And the detecting means detects the change in the mass of the neutralizer 8 to detect the degree of consumption of the neutralizer by the difference in the specific gravity of the neutralizer and water. It is also preferable to have a feature. in this case,
Even when the change in the mass of the neutralizer 8 is detected in a state where the neutralizing agent and water are contained, the degree of consumption of the neutralizing agent can be accurately detected based on the specific gravity difference between the neutralizing agent and water. In addition, since the water level in the neutralizer 8 is detected with the water level kept constant, the degree of consumption of the neutralizer can be detected with high accuracy at any time, and the neutralizer can be replaced at a more appropriate time. Control for detecting the degree of consumption of the waving agent can also be easily performed.
【0009】また前記中和器8は、その質量変化にて前
記中和器8が位置変化するようにスプリング12等の弾
性体にて支持され、前記検出手段は、前記中和器8の位
置変化を検出することにより前記中和器8の質量変化を
検出することを特徴とすることも好ましい。この場合、
中和器8が中和器8の質量変化で上下等に位置変化する
ときの位置を検出することで中和剤の消耗を検出できて
簡単な構造で正確に中和剤の消耗を検知できる。The neutralizer 8 is supported by an elastic body such as a spring 12 so that the neutralizer 8 changes its position due to a change in its mass. It is also preferable to detect a change in mass of the neutralizer 8 by detecting a change. in this case,
By detecting the position of the neutralizer 8 when the neutralizer 8 changes its position vertically due to a change in the mass of the neutralizer 8, the neutralizer consumption can be detected, and the neutralizer consumption can be accurately detected with a simple structure. .
【0010】また前記検出手段は、圧力センサー13等
の圧力変化を電気的変化に置き換える手段で前記中和器
8の質量変化を検出することを特徴とすることも好まし
い。この場合、中和器8の質量変化を正確に電気的変化
として取り出すことができて制御が容易にできる。It is also preferable that the detecting means detects a change in the mass of the neutralizer 8 by means for replacing a change in pressure of the pressure sensor 13 or the like with an electric change. In this case, the change in mass of the neutralizer 8 can be accurately taken out as an electric change, and control can be easily performed.
【0011】また前記中和器8を設置部14に一点支持
にて上下に回動自在になるように設置したことを特徴と
することも好ましい。この場合、中和器8を上下動可能
に設置するものでも所定の位置で所定の方向に上下動可
能にでき、中和器8の質量変化を一層正確に検出でき
る。It is also preferable that the neutralizer 8 is installed on the installation portion 14 so as to be rotatable up and down with one point support. In this case, even if the neutralizer 8 is installed to be able to move up and down, the neutralizer 8 can be made to move up and down at a predetermined position in a predetermined direction, and the change in mass of the neutralizer 8 can be detected more accurately.
【0012】また中和剤の消耗度合いが所定値以上にな
ったのを検出してから一定時間を経た後も検出している
ときに中和剤が所定の消耗状態になったと判定するよう
にしたことを特徴とすることも好ましい。つまり、中和
剤の消耗度合いが所定値以上になったのを検出してから
一定時間を経ても継続してそれを検出している場合や、
中和剤の消耗度合いが所定値以上になったのを検出して
から一定時間を経たときに再度測定してもそれが検出さ
れた場合中和剤が所定の消耗状態になったと判定するよ
うになっている。これにより地震やポンプの振動等で中
和器8の質量の検出の誤動作が発生する場合があるが、
上記のようにすることでこのような誤動作をなくすこと
ができる。Further, it is determined that the neutralizing agent has reached a predetermined consumption state when the neutralizing agent has reached a predetermined value or more after detecting that the degree of consumption of the neutralizing agent has exceeded a predetermined value. It is also preferable to be characterized by the following. In other words, if the degree of consumption of the neutralizing agent is continuously detected even after a certain period of time after detecting that the degree of consumption of the neutralizing agent has exceeded a predetermined value,
Even if it is measured again after a certain period of time after detecting that the degree of consumption of the neutralizing agent has reached a predetermined value or more, if it is detected again, it is determined that the neutralizing agent has reached the predetermined consumption state. It has become. This may cause a malfunction in detecting the mass of the neutralizer 8 due to an earthquake, vibration of a pump, or the like.
By doing as described above, such a malfunction can be eliminated.
【0013】[0013]
【発明の実施の形態】給湯器全体の構造は従来の技術で
説明したものと同じであるために詳しい説明は省略し、
要部である中和器8の部分だけを説明する。従来は中和
器8はドレン排水流路7の途中に固定的に設置してあっ
たが、本発明では中和器8が上下動可能に設置してあ
り、ドレン排水流路7と中和器8とはフレキシブルな管
路で接続してある。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The overall structure of a water heater is the same as that described in the prior art, so a detailed description is omitted.
Only the part of the neutralizer 8 which is the main part will be described. Conventionally, the neutralizer 8 is fixedly installed in the middle of the drain drain passage 7, but in the present invention, the neutralizer 8 is installed so as to be movable up and down, and The vessel 8 is connected by a flexible conduit.
【0014】図2の例の場合、中和器8を上下動自在に
配置してあり、中和器8と設置部14との間に弾性体を
介装して中和器8を上下動自在に支持してある。本例の
場合、上記弾性体としてスプリング12を介装してあ
る。中和器8の側方には中和器8の上下する量を検出す
る変位検出部15を配置してあり、変位検出部15を制
御基板16に接続してある。しかして中和器8の質量が
大きいと中和器8が下がり、中和器8の質量が小さいと
中和器8が上がり、変位検出部15で中和器8の質量が
検出される。In the example of FIG. 2, the neutralizer 8 is arranged to be vertically movable, and an elastic body is interposed between the neutralizer 8 and the installation portion 14 to move the neutralizer 8 vertically. It is freely supported. In the case of this example, a spring 12 is interposed as the elastic body. Displacement detector 15 for detecting the amount of rise and fall of neutralizer 8 is arranged on the side of neutralizer 8, and displacement detector 15 is connected to control board 16. When the mass of the neutralizer 8 is large, the neutralizer 8 is lowered, and when the mass of the neutralizer 8 is small, the neutralizer 8 is raised, and the displacement detector 15 detects the mass of the neutralizer 8.
【0015】また中和器8には図3に示すように凝縮水
が流入する流入口10と中和処理した処理水が流出する
流出口11とを設けてある。そして図3の例のものでは
流出口11から処理水がオーバーフローにて流出するよ
うになっており、中和器8内が一定の水位に保たれるよ
うになっている。ところで、中和器8に装填される中和
剤はCaCO3等であり、中和剤は水より比重の重いも
のである。このために中和器8内の水の水位を一定にし
た状態では水と中和剤との比重差にて中和剤8の量によ
り中和器8の質量が変わる。これにより中和器8の質量
が判ると中和剤の消耗量が判る。従って中和器8の質量
により中和器8が上下する位置を変位検出部15で検出
して中和器8内の中和剤の消耗量が所定になったことが
検出される。このとき中和器8内の水位を一定にした状
態で中和器8の質量を測定して中和剤の消耗量を検出す
るために中和剤の消耗量を定量的に検出できると共に何
時検出しても正確に検出することができる。As shown in FIG. 3, the neutralizer 8 is provided with an inlet 10 through which condensed water flows and an outlet 11 through which neutralized treated water flows out. In the example of FIG. 3, the treated water flows out of the outlet 11 by overflow, and the inside of the neutralizer 8 is maintained at a constant water level. Incidentally, the neutralizing agent loaded into the neutralizer 8 is CaCO 3 or the like, and the neutralizing agent has a higher specific gravity than water. For this reason, when the water level in the neutralizer 8 is kept constant, the mass of the neutralizer 8 changes depending on the amount of the neutralizer 8 due to the specific gravity difference between the water and the neutralizer. Thus, when the mass of the neutralizer 8 is known, the consumed amount of the neutralizing agent can be known. Therefore, the displacement detector 15 detects the position where the neutralizer 8 moves up and down based on the mass of the neutralizer 8 and detects that the consumption amount of the neutralizing agent in the neutralizer 8 has become predetermined. At this time, with the water level in the neutralizer 8 kept constant, the mass of the neutralizer 8 is measured to detect the consumption of the neutralizing agent. Even if it is detected, it can be accurately detected.
【0016】図4の例でも中和器8は流入口10から凝
縮水が流入して処理水が流出口11から流出するように
なっているが、本例の場合、流出口11からオーバーフ
ローすることにより水位を一定に保つようになっている
のでなく、運転しているとき流出口11から所定量づつ
水を流出させて中和器8内の水位を所定の変動範囲Δh
内で略一定に保つようにしてある。このようにしてある
場合も、中和器8の質量を検出することで中和剤の消耗
量を検出することができる。In the example shown in FIG. 4 as well, the condensed water flows into the neutralizer 8 from the inlet 10 and the treated water flows out from the outlet 11. In the present embodiment, the neutralized water overflows from the outlet 11. In this way, the water level is not kept constant, but during operation, water is flowed out of the outlet 11 by a predetermined amount at a time, and the water level in the neutralizer 8 is changed within a predetermined fluctuation range Δh.
It is kept almost constant within. Also in this case, the consumption of the neutralizing agent can be detected by detecting the mass of the neutralizer 8.
【0017】また中和器8は中和器8内の所定の水位ま
で水を溜めて中和処理し、中和器8内の水を一度に排出
するタイプものであってもよい。この場合、中和器8内
に所定の水位まで水を溜めたとき、または中和器8の水
を全て抜いたとき中和器8の質量を検出するようにする
と、中和剤の消耗量を正確に検出することができる。The neutralizer 8 may be of a type in which water is collected to a predetermined water level in the neutralizer 8 for neutralization, and the water in the neutralizer 8 is discharged at a time. In this case, if the mass of the neutralizer 8 is detected when water is collected up to a predetermined water level in the neutralizer 8 or when all the water in the neutralizer 8 is drained, the consumption amount of the neutralizer is reduced. Can be accurately detected.
【0018】また上記中和器8内の中和剤の消耗量が所
定量以上になると中和剤が交換されるようになってい
る。つまり、中和剤が消耗すると中和剤が補充するので
なく(中和剤を補充するようにすると補充するとき不純
物が入るおそれがある。)、中和剤を装填した部分がカ
セットとして交換される。例えば、図5に示すように中
和器8の器台8aに容器8bを着脱自在に装着してあ
り、容器8bに予め中和剤を装填してある。このように
してあると、容器8bをカセットとして交換できる。ま
た中和器8の容器8b内に図5に示すように邪魔板17
を設けてラビリンス構造にしてあると、凝縮水のショー
トパスがなくなって中和処理が確実に行われる。When the consumption of the neutralizing agent in the neutralizer 8 becomes equal to or more than a predetermined amount, the neutralizing agent is replaced. That is, when the neutralizing agent is consumed, the neutralizing agent is not replenished (if the neutralizing agent is replenished, impurities may enter the replenishing agent), and the part loaded with the neutralizing agent is replaced as a cassette. You. For example, as shown in FIG. 5, a container 8b is detachably mounted on a base 8a of the neutralizer 8, and a neutralizing agent is previously loaded in the container 8b. With this configuration, the container 8b can be replaced as a cassette. Also, as shown in FIG.
Is provided, and the labyrinth structure is used, the short path of the condensed water is eliminated, and the neutralization treatment is reliably performed.
【0019】また図6は中和器8の質量を検出する他の
例を示すものであり、圧力変化を電気的変化に置き換え
る手段で中和器8の質量変化を検出するようにしてあ
る。本例の場合、圧力変化を電気的変化に置き換える手
段として圧力センサー13を用いており、中和器8が圧
力センサー13を介して支持してあり、圧力センサー1
3を制御基板16に接続してある。この場合も圧力セン
サー13にて中和器8の質量変化を検出することにより
中和剤の消耗量を検出することができる。FIG. 6 shows another example of detecting the mass of the neutralizer 8, in which a change in pressure of the neutralizer 8 is detected by means for replacing a change in pressure with an electrical change. In the case of this example, the pressure sensor 13 is used as a means for replacing a pressure change with an electrical change, and the neutralizer 8 is supported via the pressure sensor 13.
3 is connected to the control board 16. Also in this case, the amount of consumption of the neutralizing agent can be detected by detecting a change in the mass of the neutralizer 8 with the pressure sensor 13.
【0020】また図7は中和器8の質量を検出する他の
例を示すものである。中和器8は設置部14の上に配置
してあるが、中和器8の底部の一端を支点18にて回動
自在に支持することで中和器8を設置部14に一点支持
してあり、中和器8の他端側が上下動自在になってい
る。中和器8の底部の他端と設置部14との間には弾性
体としてスプリング12を介装してあり、中和器8の側
方には中和器8の上下する量を検出する変位検出部15
を配置してあり、変位検出部15を制御基板16に接続
してある。この場合も、変位検出部15で中和器8の上
下位置を検出することで中和器8の質量を検出でき、中
和器8の内の中和剤の消耗量を検出できる。この場合、
中和器8を上下動可能に設置するものでも所定の位置で
所定の方向に上下動可能にでき、中和器8の質量変化を
一層正確に検出できる。かかる例のスプリング12や変
位検出部15に代えて、圧力センサー13等の圧力変化
を電気的変化に置き換える手段を用いてもよい。FIG. 7 shows another example of detecting the mass of the neutralizer 8. The neutralizer 8 is arranged on the installation part 14. One end of the bottom of the neutralizer 8 is rotatably supported at a fulcrum 18 to support the neutralizer 8 at one point on the installation part 14. The other end of the neutralizer 8 is vertically movable. A spring 12 is provided as an elastic body between the other end of the bottom of the neutralizer 8 and the installation part 14, and the amount of movement of the neutralizer 8 is detected on the side of the neutralizer 8. Displacement detector 15
Are arranged, and the displacement detection unit 15 is connected to the control board 16. In this case as well, the mass of the neutralizer 8 can be detected by detecting the upper and lower positions of the neutralizer 8 by the displacement detection unit 15, and the consumption amount of the neutralizing agent in the neutralizer 8 can be detected. in this case,
Even if the neutralizer 8 is installed to be vertically movable, the neutralizer 8 can be vertically moved at a predetermined position in a predetermined direction, and the change in the mass of the neutralizer 8 can be detected more accurately. In place of the spring 12 and the displacement detection unit 15 in such an example, a unit for replacing a pressure change of the pressure sensor 13 or the like with an electrical change may be used.
【0021】本発明では中和器8の質量を検出すること
で中和器8内の中和剤の消耗量が検知されるが、例え
ば、中和剤の消耗量が所定量になったことが検知された
とき、ランプ等で表示されて中和剤が消耗したことが報
知されて中和剤の交換が促され、この報知後も運転を続
けてさらに中和剤が消耗したのが検知されたとき、ブザ
ー等で中和剤が消耗したことが報知されて中和剤の交換
が促され、この報知後も運転を続けて中和剤が消耗した
のが検知されたとき、運転が強制的に止められて中和剤
を交換しないと運転を再開できないようにされる。この
ように段階的に報知し、最終的に運転を停止すると、中
和剤の交換が確実に行われると共に中和処理されない水
が排出されるおそれがなくなる。In the present invention, the amount of the neutralizer consumed in the neutralizer 8 is detected by detecting the mass of the neutralizer 8, for example, when the consumed amount of the neutralizer reaches a predetermined amount. Is detected, a message such as a lamp is displayed to inform the user that the neutralizing agent has been exhausted, prompting the user to replace the neutralizing agent, and continuing the operation after this notification to detect that the neutralizing agent has been further consumed. When the neutralizing agent has been exhausted by a buzzer or the like, the replacement of the neutralizing agent is prompted, and after the notification, the operation is continued and it is detected that the neutralizing agent has been exhausted. The operation is not restarted unless the neutralizing agent is replaced by being forcibly stopped. When the notification is given in a stepwise manner and the operation is finally stopped, the neutralizing agent is reliably exchanged and the water that is not subjected to the neutralization treatment is not discharged.
【0022】また本発明で中和剤の消耗量が所定量以下
になったと検知したとき上記のように報知されるが、こ
の検知から一定時間を経てもこの検知がされたとき中和
剤の消耗量が所定量となったと判定されて報知するよう
に制御される。つまり、地震やポンプの振動等で中和器
8の質量の検出に誤動作を生じるおそれがあるが、一定
時間を経るようにすると、このような誤動作がなくな
り、中和剤の消耗量が所定値になったとき正確に報知さ
れる。In the present invention, when it is detected that the consumption amount of the neutralizing agent has become less than the predetermined amount, the above-mentioned notification is made. It is controlled to determine that the consumption amount has reached the predetermined amount and to notify the user. In other words, there is a possibility that an erroneous operation may occur in the detection of the mass of the neutralizer 8 due to an earthquake, a vibration of a pump, or the like. You will be notified exactly when it becomes.
【0023】[0023]
【発明の効果】本発明の請求項1の発明は、叙述の如く
中和器の質量変化を検出することにより前記中和器内の
中和剤の消耗度合いを検出する検出手段を設けているの
で、中和器内に存在する中和剤の質量を定量的に検出し
て中和剤の消耗度合いを検知でき、中和剤の消耗度合い
を正確に検知できて適切な時期に中和剤の交換ができる
ものである。According to the first aspect of the present invention, the detecting means for detecting the degree of consumption of the neutralizing agent in the neutralizer by detecting a change in the mass of the neutralizer as described above is provided. Therefore, the mass of the neutralizing agent present in the neutralizer can be quantitatively detected to detect the degree of neutralizing agent consumption, and the degree of neutralizing agent consumption can be accurately detected, and the neutralizing agent can be detected at an appropriate time. Can be exchanged.
【0024】また本発明の請求項2の発明は、請求項1
において、前記中和器は、凝縮水が流入口から流入する
と共に前記中和器の中和剤で中和した処理水を流出口か
らオーバーフローにて流出させるようにして常に一定水
位に保たれる構造とし、前記検出手段は、前記中和器の
質量変化を検出することにより中和剤と水の比重の差に
より中和剤の消耗度合いを検出するので、中和剤と水が
入った状態で中和器の質量の変化を検出するものでも、
中和剤と水との比重差により中和剤の消耗度合いを正確
に検知できるものであり、しかも中和器内の水の水位を
一定に保った状態で検出するために何時でも精度高く中
和剤の消耗度合いを検知できて一層適切な時期に中和剤
の交換ができ、また中和剤の消耗度合いを検知する制御
も容易にできるものである。Further, the invention of claim 2 of the present invention is directed to claim 1
In the above, the neutralizer is always kept at a constant water level so that the condensed water flows in from the inlet and the treated water neutralized by the neutralizing agent of the neutralizer flows out from the outlet by overflow. And the detecting means detects the degree of consumption of the neutralizing agent by the difference in the specific gravity of the neutralizing agent and water by detecting a change in the mass of the neutralizing device. To detect changes in the neutralizer mass with
It can accurately detect the degree of consumption of the neutralizing agent based on the difference in specific gravity between the neutralizing agent and water.In addition, the water level in the neutralizer can be detected while maintaining a constant water level. The neutralizing agent can be replaced at a more appropriate time by detecting the degree of consumption of the waving agent, and control for detecting the degree of neutralizing agent consumption can be easily performed.
【0025】また本発明の請求項3の発明は、請求項1
または請求項2において、前記中和器は、その質量変化
にて前記中和器が位置変化するようにスプリング等の弾
性体にて支持され、前記検出手段は、前記中和器の位置
変化を検出することにより前記中和器の質量変化を検出
するので、中和器が中和器の質量変化で上下等に位置変
化するときの位置を検出することで中和剤の消耗を検出
できて簡単な構造で正確に中和剤の消耗を検知できるも
のである。Further, the invention of claim 3 of the present invention is directed to claim 1
Alternatively, in claim 2, the neutralizer is supported by an elastic body such as a spring so that the neutralizer changes its position due to a change in mass thereof, and the detecting unit detects a change in the position of the neutralizer. Since the mass change of the neutralizer is detected by detecting, the consumption of the neutralizer can be detected by detecting the position when the neutralizer changes its position vertically or the like due to the mass change of the neutralizer. With a simple structure, the consumption of the neutralizing agent can be accurately detected.
【0026】また本発明の請求項4の発明は、請求項1
または請求項2において、前記検出手段は、圧力センサ
ー等の圧力変化を電気的変化に置き換える手段で前記中
和器の質量変化を検出するので、中和器の質量変化を正
確に電気的変化として取り出すことができて制御が容易
にできるものである。The invention of claim 4 of the present invention provides the method of claim 1
Alternatively, in claim 2, since the detecting means detects the mass change of the neutralizer by means of replacing a pressure change of a pressure sensor or the like with an electric change, the mass change of the neutralizer is accurately regarded as an electric change. It can be taken out and controlled easily.
【0027】また本発明の請求項5の発明は、請求項1
乃至請求項4において、前記中和器を設置部に一点支持
にて上下に回動自在になるように設置したので、中和器
を上下動可能に設置するものでも所定の位置で所定の方
向に上下動可能にでき、中和器の質量変化を一層正確に
検出できるものである。Further, the invention of claim 5 of the present invention is directed to claim 1
In Claim 4, since the neutralizer is installed on the installation part so as to be rotatable up and down by one point support, even if the neutralizer is installed so as to be movable up and down in a predetermined direction at a predetermined position. The change in the mass of the neutralizer can be detected more accurately.
【0028】また本発明の請求項6の発明は、請求項1
乃至請求項5において、中和剤の消耗度合いが所定値以
上になったのを検出してから一定時間を経た後も検出し
ているときに中和剤が所定の消耗状態になったと判定す
るようにしたので、地震やポンプの振動等による中和器
の質量の検出の誤動作による影響を排除できて中和剤の
消耗度合いを正確に判定できるものである。The invention of claim 6 of the present invention provides the method of claim 1
In Claim 5 or Claim 5, it is determined that the neutralizing agent has reached the predetermined consumption state when the degree of consumption of the neutralizing agent has been detected after a certain period of time after the fact that the degree of consumption of the neutralizing agent has reached a predetermined value or more. With this configuration, it is possible to eliminate the influence of a malfunction in detecting the mass of the neutralizer due to an earthquake, vibration of a pump, or the like, and to accurately determine the degree of consumption of the neutralizer.
【図1】給湯器の全体的な構造を示す概略断面図であ
る。FIG. 1 is a schematic sectional view showing the overall structure of a water heater.
【図2】本発明の実施の形態の一例の中和器の質量を検
出する構造を示す概略正面図である。FIG. 2 is a schematic front view showing a structure for detecting the mass of a neutralizer according to an example of the embodiment of the present invention.
【図3】同上の中和器の構造を示す概略断面図である。FIG. 3 is a schematic sectional view showing the structure of a neutralizer according to the first embodiment.
【図4】同上の中和器の他の例の構造を示す概略断面図
である。FIG. 4 is a schematic sectional view showing the structure of another example of the neutralizer according to the embodiment.
【図5】(a)(b)は中和器の他の例の構造を示す概
略断面図である。FIGS. 5A and 5B are schematic cross-sectional views showing the structure of another example of the neutralizer.
【図6】同上の中和器の質量を検出する構造の他の例の
概略正面図である。FIG. 6 is a schematic front view of another example of the structure for detecting the mass of the neutralizer of the above.
【図7】同上の中和器の質量を検出する構造の他の例の
概略正面図である。FIG. 7 is a schematic front view of another example of the structure for detecting the mass of the neutralizer of the above.
1 燃焼室 2 燃焼バーナ 3 熱交換器 3a 主熱交換器部 3b 副熱交換器部 4 給水流路 5 出湯流路 6 ドレンパン 7 ドレン排水流路 8 中和器 10 流入口 11 流出口 13 圧力サンサー 14 設置部 DESCRIPTION OF SYMBOLS 1 Combustion chamber 2 Combustion burner 3 Heat exchanger 3a Main heat exchanger part 3b Sub heat exchanger part 4 Water supply channel 5 Hot water supply channel 6 Drain pan 7 Drain drainage channel 8 Neutralizer 10 Inlet 11 Outlet 13 Pressure sensor 14 Installation section
Claims (6)
燃焼バーナの燃焼排気ガスの熱と熱交換して水を加熱す
る熱交換器と、前記熱交換器に加熱される水を供給する
給水流路と、前記熱交換器にて加熱された水を出湯する
出湯流路とを具備する給湯器であって、前記熱交換器
は、燃焼排気ガスの流れの上流側に位置する主熱交換器
部とこの燃焼排気ガスの流れの下流側に位置する副熱交
換器部とを有し、前記燃焼室には前記副熱交換器部にて
発生した凝縮水を受け止めるためのドレンパンを配設
し、前記ドレンパンの凝縮水を排水するためのドレン排
水流路を前記ドレンパンに連結すると共に前記ドレン排
水流路にて排水される凝縮水を中和する中和器を前記ド
レン排水流路に配設し、前記中和器の質量変化を検出す
ることにより中和器内の中和剤の消耗度合いを検出する
検出手段を設けて成ることを特徴とする給湯器。1. A combustion burner disposed in a combustion chamber, a heat exchanger for exchanging heat with heat of combustion exhaust gas of the combustion burner to heat water, and supplying water to be heated to the heat exchanger. A water heater comprising a water supply flow path and a hot water supply path for discharging hot water heated by the heat exchanger, wherein the heat exchanger includes a main heat source located upstream of a flow of combustion exhaust gas. An exchange unit and a sub heat exchanger unit located downstream of the flow of the combustion exhaust gas, and a drain pan for receiving condensed water generated in the sub heat exchanger unit is provided in the combustion chamber. A drain outlet for draining the condensed water of the drain pan is connected to the drain pan, and a neutralizer for neutralizing the condensed water drained in the drain drain passage is provided in the drain drain passage. Arranged in the neutralizer by detecting a change in the mass of the neutralizer. A water heater comprising a detecting means for detecting a degree of consumption of the neutralizing agent.
流入すると共に前記中和器内の中和剤で中和した処理水
を流出口からオーバーフローにて流出させるようにして
常に一定水位に保たれる構造とし、前記検出手段は、前
記中和器の質量変化を検出することにより中和剤と水の
比重の差により中和剤の消耗度合いを検出することを特
徴とする請求項1記載の給湯器。2. The neutralizer according to claim 1, wherein the condensed water flows in from an inlet, and the treated water neutralized by a neutralizing agent in the neutralizer flows out from an outlet through an overflow. The water level is maintained, and the detecting means detects a degree of consumption of the neutralizer by detecting a change in the mass of the neutralizer and a difference in specific gravity of the neutralizer and water. Item 2. The water heater according to item 1.
和器が位置変化するようにスプリング等の弾性体にて支
持され、前記検出手段は、前記中和器の位置変化を検出
することにより前記中和器の質量変化を検出することを
特徴とする請求項1または請求項2記載の給湯器。3. The neutralizer is supported by an elastic body such as a spring so that the position of the neutralizer changes according to a change in mass of the neutralizer. The detecting unit detects a change in the position of the neutralizer. The water heater according to claim 1 or 2, wherein a change in mass of the neutralizer is detected by performing the operation.
変化を電気的変化に置き換える手段で前記中和器の質量
変化を検出することを特徴とする請求項1または請求項
2記載の給湯器。4. The water heater according to claim 1, wherein said detecting means detects a change in mass of said neutralizer by means for replacing a change in pressure with an electric change such as a pressure sensor. .
に回動自在になるように設置したことを特徴とする請求
項1乃至請求項4のいずれかに記載の給湯器。5. The water heater according to claim 1, wherein the neutralizer is installed on the installation portion so as to be rotatable up and down by one point support.
たのを検出してから一定時間を経た後も検出していると
きに中和剤が所定の消耗状態になったと判定するように
したことを特徴とする請求項1乃至請求項5のいずれか
に記載の給湯器。6. A method for determining that the neutralizing agent has reached a predetermined consumable state when the neutralizing agent has reached a predetermined value or more after detecting that the degree of consumption of the neutralizing agent has exceeded a predetermined value. The water heater according to any one of claims 1 to 5, wherein:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2000319065A JP2002130830A (en) | 2000-10-19 | 2000-10-19 | Hot water supply apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2000319065A JP2002130830A (en) | 2000-10-19 | 2000-10-19 | Hot water supply apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2002130830A true JP2002130830A (en) | 2002-05-09 |
Family
ID=18797586
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2000319065A Withdrawn JP2002130830A (en) | 2000-10-19 | 2000-10-19 | Hot water supply apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2002130830A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009264708A (en) * | 2008-04-30 | 2009-11-12 | Osaka Gas Co Ltd | Water heater |
JP2013113566A (en) * | 2011-11-30 | 2013-06-10 | Noritz Corp | Structure for fixing neutralizer and heat source apparatus |
JP2017106662A (en) * | 2015-12-09 | 2017-06-15 | 株式会社パロマ | Hot water supply system |
-
2000
- 2000-10-19 JP JP2000319065A patent/JP2002130830A/en not_active Withdrawn
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009264708A (en) * | 2008-04-30 | 2009-11-12 | Osaka Gas Co Ltd | Water heater |
JP2013113566A (en) * | 2011-11-30 | 2013-06-10 | Noritz Corp | Structure for fixing neutralizer and heat source apparatus |
JP2017106662A (en) * | 2015-12-09 | 2017-06-15 | 株式会社パロマ | Hot water supply system |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US10682589B2 (en) | Condensate neutralizer system including condensate device health monitoring | |
US10480822B2 (en) | Condensate neutralizer device | |
CN101091015A (en) | Measures for keeping a degree of contamination of a steam generator including its contents below a predetermined maximum | |
US10794792B2 (en) | Leak detection system | |
JP2011106761A (en) | Neutralization device and latent heat recovery type water heater including the same | |
CN209431654U (en) | Boiler and water heater | |
JP4937870B2 (en) | Water heater with drain neutralization tank | |
JP2002130830A (en) | Hot water supply apparatus | |
JP4815950B2 (en) | Condensate treatment apparatus and hot water supply apparatus provided with the same | |
JPH06323580A (en) | Humidifier | |
JP5778597B2 (en) | Neutralizer and hot water supply apparatus having the same | |
JPH0926284A (en) | Water leakage detector for heat exchanger | |
JP5323363B2 (en) | Neutralizing device, combustion device equipped with neutralizing device, and control method of neutralizing device | |
JP2015129601A (en) | heat source machine | |
JP5778614B2 (en) | Neutralizer and hot water supply apparatus having the same | |
JP3837112B2 (en) | Water heater | |
JP5598698B2 (en) | Bath equipment | |
JP2010249438A (en) | Latent heat recovery type water heater | |
JP5005398B2 (en) | Combustion equipment | |
JP2007326085A (en) | Drain neutralization device | |
JP3435296B2 (en) | Device for monitoring the life of the neutralizer for drainage | |
JP2008121981A (en) | Denitrifying device for water heater, and water heater | |
JP2004286395A (en) | Latent heat recovery type heat source machine | |
JP2004286394A (en) | Latent heat recovery type heat source machine | |
US11137316B2 (en) | Leak detection system |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A300 | Withdrawal of application because of no request for examination |
Free format text: JAPANESE INTERMEDIATE CODE: A300 Effective date: 20080108 |