JPH0777327A - Soot clogging detection method for combustion device and co sensor trouble detection method for co sensor equipped combustion device based on the method - Google Patents

Soot clogging detection method for combustion device and co sensor trouble detection method for co sensor equipped combustion device based on the method

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Publication number
JPH0777327A
JPH0777327A JP24592293A JP24592293A JPH0777327A JP H0777327 A JPH0777327 A JP H0777327A JP 24592293 A JP24592293 A JP 24592293A JP 24592293 A JP24592293 A JP 24592293A JP H0777327 A JPH0777327 A JP H0777327A
Authority
JP
Japan
Prior art keywords
thermal efficiency
sensor
combustion
soot
heat exchanger
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.)
Granted
Application number
JP24592293A
Other languages
Japanese (ja)
Other versions
JP3312968B2 (en
Inventor
Yoshihiko Tanaka
良彦 田中
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Gastar Co Ltd
Original Assignee
Gastar Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Gastar Co Ltd filed Critical Gastar Co Ltd
Priority to JP24592293A priority Critical patent/JP3312968B2/en
Publication of JPH0777327A publication Critical patent/JPH0777327A/en
Application granted granted Critical
Publication of JP3312968B2 publication Critical patent/JP3312968B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Regulation And Control Of Combustion (AREA)
  • Control Of Combustion (AREA)
  • Feeding And Controlling Fuel (AREA)

Abstract

PURPOSE:To make it possible to detect soot clogging in automatic mode by monitoring arithmetic operations of thermal efficiency one after another based on temperature information of a heating medium on the input and output of a heat exchanger and a flow rate of a heating medium and the supply of fuel and determining that a combustion device is clogged with soot, if the computed value drops to a specified value or blow. CONSTITUTION:When operating hot water supply heater or the like, thermal efficiency during combustion operation of a burner 1 is determined from the following equation: Thermal efficiency=effective amount of heat/amount of supplied heat-lambdaX (outside temperature-input temperature) X flow rate/(alphaX fuel supply) based on information about input temperature, output temperature, supply and flow rate of fuel in terms of a thermal efficiency arithmetic operation unit 24 where lambda stands for a specific heat a heating medium, while alpha stands for amount of heat per unit volume. Then, a stabilization determinant unit 25 compares a preceding thermal efficiency with the latest thermal efficiency and when this difference between both values is small than an allowable range when the thermal efficiency is stabilized), an average thermal efficiency is determined by an average thermal efficiency computation unit 27. When this average thermal efficiency exceeds an allowable deviation value and drops below that, it is determined that the heat exchanger 2 is clogged with soot so that an annunciation unit 29 is operated.

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、給湯器や暖房器等の燃
焼装置の煤詰まり検知方法と、それを利用したCOセン
サ付燃焼装置のCOセンサ故障検知方法に関するもので
ある。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a soot clogging detection method for a combustion device such as a water heater or a heater, and a CO sensor failure detection method for a combustion device with a CO sensor using the method.

【0002】[0002]

【従来の技術】最近においては、ガスや石油を燃料とす
る給湯器、風呂釜、あるいは暖房器等の燃焼装置の小型
化を図るため、装置内に燃焼ファンを配設することによ
り、燃料量に見合った空気量をバーナに供給して強制燃
焼を行わせている。しかし、燃焼ファンにより燃料量に
見合った空気量がバーナに供給されなくなり、燃料量と
空気量のバランスが崩れると、部分不燃を起こしやす
く、一度部分不燃を起こすと熱交換器に煤が急速に付着
し、火災へとつながる虞があった。このような燃料量と
空気量のバランスの崩れに起因する部分不燃の発生例
が、図5と図6に示されている。
2. Description of the Related Art Recently, in order to miniaturize a combustion apparatus such as a water heater, a bath heater, or a heater that uses gas or oil as a fuel, a combustion fan is provided in the apparatus to reduce the amount of fuel. The combustor is forcedly burned by supplying the burner with an amount of air commensurate with. However, if the combustion fan does not supply the burner with an amount of air commensurate with the amount of fuel, and the balance between the amount of fuel and the amount of air is lost, partial incombustion easily occurs, and once partial incombustion occurs, soot rapidly increases in the heat exchanger. There is a risk that they will adhere and lead to a fire. An example of occurrence of partial incombustion due to the imbalance of the fuel amount and the air amount is shown in FIGS. 5 and 6.

【0003】図5には、燃焼ファン3が排気側に配設さ
れているタイプの給湯器が示されており、このような給
湯器を埃の多い地面等に設置した場合には、バーナ1の
空気口から埃が吸い込まれ、バーナ1の炎口1aの内側
に図示のように埃が溜まり、そのため、バーナ1に供給
される空気は均等ではなくなり、空気量と燃料量とのバ
ランスが崩れ、バーナ1の炎口に埃が付着した部分で部
分不燃を起こすこととなり、熱交換器2に急速に煤が付
着し、煤詰まりが発生することとなる。
FIG. 5 shows a water heater of the type in which the combustion fan 3 is arranged on the exhaust side. When such a water heater is installed on a dusty ground or the like, the burner 1 is used. The dust is sucked from the air port of the burner 1, and the dust is accumulated inside the flame port 1a of the burner 1 as shown in the figure. Therefore, the air supplied to the burner 1 is not uniform, and the balance between the air amount and the fuel amount is lost. Partial non-combustion occurs at a portion where dust is attached to the burner 1 burner 1, soot is rapidly attached to the heat exchanger 2, and soot clogging occurs.

【0004】図6には、燃焼ファン3が給気側に配設さ
れているタイプの給湯器が示されており、このような給
湯器では、燃焼ファン3とバーナ1との間にパンチング
メタル等の均圧板4を介設することによって、燃焼ファ
ン3からの空気が均等に分圧されてバーナ1の各部へ空
気が供給されるよう構成されている。この場合には、燃
焼ファン3の回転による吸い込み力が強く、給気口3a
から蚊や蛾等の虫が吸い込まれ、この虫が前記均圧板4
に引っ掛かり、バーナ1には均等に空気が供給されなく
なって部分不燃を起こすこととなり、前記同様に熱交換
器2に煤詰まりが生ずることとなる。
FIG. 6 shows a water heater of the type in which the combustion fan 3 is arranged on the air supply side. In such a water heater, punching metal is provided between the combustion fan 3 and the burner 1. By interposing the pressure equalizing plate 4 such as the above, the air from the combustion fan 3 is evenly divided and the air is supplied to each part of the burner 1. In this case, the suction force due to the rotation of the combustion fan 3 is strong and the intake port 3a
Insects such as mosquitoes and moths are sucked in from the pressure equalizing plate 4
As a result, air is not evenly supplied to the burner 1 to cause partial incombustion, and soot is clogged in the heat exchanger 2 as described above.

【0005】上記のように部分不燃が起き、熱交換器2
に煤詰まりが生じた場合に、従来はこれを検知する方法
がなく、燃焼装置の利用者が装置周辺の煤の汚れや燃焼
時の異臭に気付く等、人間の感覚に頼る他なかった。一
方、燃焼装置にCOセンサを配設して、このCOセンサ
が排ガス中のCOガスを検出し、CO検出濃度が予め与
えられている基準濃度に達したときに、警報器を動作さ
せる等のCO安全動作を行うCO安全装置が設けられて
いるCOセンサ付燃焼装置では、上記のように、部分不
燃が起こることによりCO検出濃度が基準濃度に達する
ので、COセンサによるCO安全動作が行われるが、C
Oセンサが故障するとCO安全動作が行われなくなるの
で、部分不燃が放置されたままとなり、災害へとつなが
る虞を生じ大変危険である。
Partial incombustion occurs as described above, and the heat exchanger 2
When soot clogging occurs, there is no conventional method for detecting this, and the user of the combustion device has no choice but to rely on human senses, such as notice of dirt on the soot around the device or a strange odor during combustion. On the other hand, a CO sensor is provided in the combustion device, the CO sensor detects the CO gas in the exhaust gas, and an alarm device is activated when the detected CO concentration reaches a predetermined reference concentration. In the combustion device with a CO sensor provided with the CO safety device for performing the CO safety operation, the CO detection concentration reaches the reference concentration due to the partial incombustibility as described above, and therefore the CO safety operation by the CO sensor is performed. But C
If the O sensor fails, CO safe operation cannot be performed, so that partial incombustibility is left unattended, which may lead to a disaster, which is very dangerous.

【0006】[0006]

【発明が解決しようとする課題】しかしながら、煤詰ま
りの判断を人間の感覚だけに頼るのは甚だ危険であり、
これを自動的に検知できる機能を有する燃焼装置が望ま
れている。
However, it is extremely dangerous to rely solely on the human sense to judge the soot clogging,
A combustion device having a function of automatically detecting this is desired.

【0007】また、COセンサ付燃焼装置においては、
熱交換器の煤詰まりを自動的に検知できるようにすれ
ば、煤詰まりが検知されても、COセンサによるCO安
全動作が行われないときには、COセンサの故障が検知
されることとなり、不完全燃焼による事故を未然に防ぐ
ことができる。
Further, in the combustion device with a CO sensor,
If the soot clogging of the heat exchanger can be detected automatically, even if the soot clogging is detected, if the CO safety operation by the CO sensor is not performed, the failure of the CO sensor will be detected, resulting in incompleteness. Accidents due to combustion can be prevented.

【0008】本発明は、上記課題を解決するためになさ
れたものであり、その目的は、熱交換器の煤詰まりを人
間の感覚に頼らずに、自動的に検知できる燃焼装置の煤
詰まり検知方法とそれを利用したCOセンサ付燃焼装置
のCOセンサ故障検知方法を提供することにある。
The present invention has been made to solve the above problems, and an object thereof is to detect soot clogging of a combustion device which can automatically detect soot clogging of a heat exchanger without relying on human senses. A method and a method for detecting a CO sensor failure in a combustion apparatus with a CO sensor using the method.

【0009】[0009]

【課題を解決するための手段】本発明は上記目的を達成
するために、次のように構成されている。すなわち、本
発明は、バーナに供給される燃料を、燃焼ファンの回転
によって取り込まれる空気を利用して燃焼し、この燃焼
火力でもって熱交換器を通る加熱媒体を加熱する燃焼装
置の煤詰まり検知方法であって、熱交換器の入側と出側
における加熱媒体の温度情報と、燃料供給量と、加熱媒
体の流量とを含む情報を取り込んで、バーナの燃焼運転
時に熱効率を逐次演算モニタし、予め与えられる基準熱
効率の値と比較し、熱効率の演算値が基準熱効率の値よ
りも所定の許容偏差を越えて低下したときに熱交換器の
煤詰まりが発生したと判断して煤詰まり検知信号を出力
することを特徴として構成されており、また、これを利
用した本発明のCOセンサ付燃焼装置のCOセンサ故障
検知方法は、前記燃焼装置に排気ガス中のCO濃度を検
出するCOセンサと、COセンサのCO検出濃度が予め
与えられる基準濃度に達したときにCO安全動作を行う
CO安全装置が設けられ、請求項1記載の方法で演算さ
れる熱効率の演算値が予め与えられる基準熱効率の値よ
りも所定の許容偏差を越えて低下したときにCOセンサ
の故障検知信号を出力することを特徴として構成されて
いる。
In order to achieve the above object, the present invention is constructed as follows. That is, the present invention burns the fuel supplied to the burner using the air taken in by the rotation of the combustion fan, and detects the soot clogging of the combustion device that heats the heating medium passing through the heat exchanger with this combustion thermal power. In this method, information including the temperature information of the heating medium on the inlet side and the outlet side of the heat exchanger, the fuel supply amount, and the flow rate of the heating medium is taken in, and the thermal efficiency is sequentially calculated and monitored during the burner combustion operation. , The soot clogging is detected by comparing with the value of the reference thermal efficiency given in advance and judging that the soot clogging of the heat exchanger has occurred when the calculated value of the thermal efficiency is lower than the value of the reference thermal efficiency by a predetermined allowable deviation. A method for detecting a CO sensor failure in a combustion apparatus with a CO sensor according to the present invention, which is configured to output a signal, detects the CO concentration in exhaust gas in the combustion apparatus. A CO sensor and a CO safety device that performs a CO safety operation when the CO detected concentration of the CO sensor reaches a predetermined reference concentration, and a calculated value of thermal efficiency calculated by the method according to claim 1 is given in advance. It is configured to output a failure detection signal of the CO sensor when the value is lower than a predetermined reference thermal efficiency value by a predetermined allowable deviation.

【0010】[0010]

【作用】熱交換器の入側と出側における加熱媒体の温度
情報と、燃料供給量と、加熱媒体の流量との情報から、
バーナ燃焼運転時の熱効率を逐次演算モニタし、この熱
効率の演算値が、例えば、煤詰まりがないときの熱効率
である基準熱効率の値よりも所定の許容偏差を越えて低
下したときに、燃焼装置に煤詰まりがあったものと判断
して、煤詰まり検知信号を出力する。
[Operation] From the information on the temperature of the heating medium on the inlet side and the outlet side of the heat exchanger, the fuel supply amount, and the information on the flow rate of the heating medium,
The thermal efficiency during burner combustion operation is sequentially monitored, and when the calculated value of this thermal efficiency falls below a predetermined allowable deviation from the value of the reference thermal efficiency which is the thermal efficiency when there is no soot clogging, the combustion device It is judged that there was soot clogging, and a soot clogging detection signal is output.

【0011】また、排ガス中のCO濃度が基準濃度に達
したときに、COセンサによるCO安全動作が行われる
COセンサ付燃焼装置では、上記のように煤詰まりが検
知されても、COセンサによるCO安全動作が行われて
いない場合には、COセンサの故障が検知される。
Further, in the combustion device with a CO sensor, in which the CO sensor performs a CO safe operation when the CO concentration in the exhaust gas reaches the reference concentration, even if soot clogging is detected as described above, the CO sensor detects When the CO safe operation is not performed, the failure of the CO sensor is detected.

【0012】[0012]

【実施例】以下、本発明の実施例を図面に基づいて説明
する。図1と図2には、本発明に係る燃焼装置の煤詰ま
り検知方法と、それを利用したCOセンサ付燃焼装置の
COセンサ故障検知方法を行う第1の実施例が示されて
いる。
Embodiments of the present invention will be described below with reference to the drawings. 1 and 2 show a first embodiment for carrying out a soot clogging detection method for a combustion apparatus according to the present invention and a CO sensor failure detection method for a combustion apparatus with a CO sensor using the method.

【0013】図2には、本実施例における燃焼装置とし
て、加熱媒体が水である給湯器のシステム構成が示され
ている。同図において、熱交換器2の入口側には給水管
6が接続されており、この給水管6には入水温度を検出
する入側サーミスタ8と、水の流量を検出する流量セン
サ9とが設けられている。熱交換器2の出口側には給湯
管7が接続され、この給湯管7には、出湯温度を検出す
る出側サーミスタ10が設けられており、給湯管7の出口
側には給湯栓(図示せず)が設けられている。
FIG. 2 shows a system configuration of a water heater in which the heating medium is water as the combustion apparatus in this embodiment. In the figure, a water supply pipe 6 is connected to the inlet side of the heat exchanger 2, and an inlet side thermistor 8 for detecting the water entrance temperature and a flow rate sensor 9 for detecting the water flow rate are connected to the water supply pipe 6. It is provided. A hot water supply pipe 7 is connected to the outlet side of the heat exchanger 2, and a hot water supply pipe 7 is provided with an outlet side thermistor 10 for detecting the hot water discharge temperature. (Not shown).

【0014】熱交換器2の下方にはバーナ1が配設され
ており、バーナ1へはガス管12から燃料としてのガスが
供給され、一方、バーナ1の下方にある燃焼ファン3の
回転によりバーナ1へ空気が供給され、このバーナ1で
のガスと空気の燃焼による燃焼火力により熱交換器2を
通る水が加熱される。また、ガス管12にはガス供給量を
開弁量によって制御するガス比例弁13と、管路の開閉を
行うガス電磁弁18が介設されている。
A burner 1 is disposed below the heat exchanger 2, and gas as a fuel is supplied to the burner 1 from a gas pipe 12, while the combustion fan 3 below the burner 1 is rotated. Air is supplied to the burner 1, and the combustion heat generated by the combustion of gas and air in the burner 1 heats the water passing through the heat exchanger 2. In addition, a gas proportional valve 13 that controls the gas supply amount by the valve opening amount and a gas solenoid valve 18 that opens and closes the pipeline are provided in the gas pipe 12.

【0015】この種の給湯器には制御装置11が備えられ
ており、この制御装置にはリモコン(図示せず)が接続
され、このリモコンには給湯温度を設定するボタンや設
定温度の表示部が設けられている。制御装置11は給湯器
の給湯動作を制御しており、給湯栓が開けられると流量
センサ9が水の流量を検出して、その流量がある一定の
流量以上になったときに、流量センサ9からの信号を受
けて制御装置は燃焼ファン3を回転させ、ガス電磁弁18
を開け、ガス比例弁13の開弁量を可変して、熱交換器2
から出る湯温の安定化制御を行っている。
This type of water heater is provided with a control device 11, and a remote control (not shown) is connected to this control device. The remote control has a button for setting the hot water temperature and a set temperature display section. Is provided. The controller 11 controls the hot water supply operation of the water heater, and when the hot water tap is opened, the flow rate sensor 9 detects the flow rate of water, and when the flow rate exceeds a certain flow rate, the flow rate sensor 9 The control device rotates the combustion fan 3 in response to the signal from the gas solenoid valve 18
Open and change the opening amount of the gas proportional valve 13 to change the heat exchanger 2
It controls the stabilization of the temperature of the hot water discharged from the hot water.

【0016】さらに、この給湯器は、排ガス中のCO濃
度を検出するCOセンサ19が排気側に配設されているC
Oセンサ付給湯器であり、COセンサ19は制御装置11内
に形成されているCO安全装置5に接続されており、C
O検出濃度が基準濃度に達したときに警報器40を動作さ
せたり、ガス電磁弁18を閉めて燃焼停止を行う等のCO
安全動作が行われるよう構成されている。
Further, in this water heater, a CO sensor 19 for detecting the CO concentration in the exhaust gas is arranged on the exhaust side.
It is a water heater with an O sensor, the CO sensor 19 is connected to the CO safety device 5 formed in the control device 11, and C
When the O detected concentration reaches the reference concentration, the alarm device 40 is operated, or the gas solenoid valve 18 is closed to stop combustion.
It is configured for safe operation.

【0017】本実施例は、上記構成のCOセンサ付給湯
器において、熱交換器2の煤詰まりによるバーナの燃焼
運転時の熱効率の低下を利用して、煤詰まりを検知する
ものである。
In the present embodiment, in the water heater with a CO sensor having the above-mentioned structure, soot clogging is detected by utilizing the decrease in thermal efficiency during combustion operation of the burner due to soot clogging of the heat exchanger 2.

【0018】図1には、本実施例の煤詰まり検知方法を
行う煤詰まり検知部17のブロック構成図が示されてい
る。煤詰まり検知部17は、前記制御装置11の内部に形成
されており、温度検出部20と、燃料供給量計測部21と、
流量検出部22と、熱効率演算部24と、安定判定部25と、
平均熱効率算出部27と、比較判定部28と、報知部29と、
データ格納部30と、メモリ31とを有して構成されてい
る。
FIG. 1 shows a block diagram of a soot clogging detection section 17 for carrying out the soot clogging detection method of this embodiment. The soot clogging detection unit 17, which is formed inside the control device 11, a temperature detection unit 20, a fuel supply amount measurement unit 21,
A flow rate detection unit 22, a thermal efficiency calculation unit 24, a stability determination unit 25,
An average thermal efficiency calculation unit 27, a comparison determination unit 28, an informing unit 29,
The data storage unit 30 and the memory 31 are provided.

【0019】データ格納部30には、基準熱効率と許容偏
差が記憶されている。基準熱効率は、熱交換器2に煤詰
まりがない場合のバーナの燃焼運転時の熱効率であり、
この熱効率は、図3の曲線Aに示すように、燃焼開始後
徐々に上昇して一定の値に安定するので、この安定した
ときの熱効率が、実験や演算等により予め求められて記
憶されている。一般に3〜16号の給湯器における基準熱
効率はほぼ79〜83%である。
The data storage unit 30 stores the reference thermal efficiency and the allowable deviation. The reference thermal efficiency is the thermal efficiency during burner combustion operation when there is no soot clogging in the heat exchanger 2,
This thermal efficiency gradually rises and stabilizes at a constant value after the start of combustion, as shown by the curve A in FIG. 3. Therefore, the thermal efficiency at this stable time is obtained in advance by experiments, calculations, etc. and stored. There is. Generally, the standard thermal efficiency of the water heaters of Nos. 3 to 16 is about 79 to 83%.

【0020】また、許容偏差は、熱交換器2に煤詰まり
が生じていないと判断するための、前記基準熱効率を基
準とした許容の範囲である。熱交換器2に煤詰まりがあ
ると、同図の曲線Bに示すように、その熱効率は前記熱
交換器2に煤詰まりがないときの基準熱効率の値よりも
低下しており、この実施例では、熱効率の値が基準熱効
率の値よりも許容偏差を越えて低下したときに、燃焼装
置の煤詰まり検知信号を出力するようにしている。
The permissible deviation is a permissible range based on the reference thermal efficiency for determining that the heat exchanger 2 is not clogged with soot. When the heat exchanger 2 has soot clogging, its thermal efficiency is lower than the reference thermal efficiency value when the heat exchanger 2 does not have soot clogging, as shown by a curve B in FIG. Then, when the thermal efficiency value is lower than the reference thermal efficiency value by more than the allowable deviation, the soot clogging detection signal of the combustion device is output.

【0021】CO安全装置5がCO安全動作を行うとき
の基準濃度は、煤詰まり検知信号が出力されるときのC
O検出濃度よりも十分低い値が設定されている。つま
り、バーナ燃焼運転時の熱効率が基準熱効率より許容偏
差を越えて低下して、燃焼装置の煤詰まり検知信号が出
力される以前に、CO検出濃度が基準濃度に達して、C
OセンサによるCO安全動作が行われるよう構成されて
いる。
The reference concentration when the CO safety device 5 performs the CO safety operation is C when the soot clogging detection signal is output.
A value sufficiently lower than the O detection concentration is set. That is, the CO detection concentration reaches the reference concentration before the soot clogging detection signal of the combustion device is output, when the thermal efficiency during burner combustion operation falls below the reference thermal efficiency by more than the allowable deviation, and C
It is configured to perform CO safe operation by the O sensor.

【0022】温度検出部20は、熱交換器2の入側と出側
における水の温度情報を、入側サーミスタ8と出側サー
ミスタ10により検出して、これらを入側温度および出側
温度として熱効率演算部24に加える。
The temperature detector 20 detects the temperature information of the water on the inlet side and the outlet side of the heat exchanger 2 by means of the inlet side thermistor 8 and the outlet side thermistor 10, and regards these as the inlet side temperature and the outlet side temperature. It is added to the thermal efficiency calculation unit 24.

【0023】燃料供給量計測部21は、バーナ1へ供給さ
れる燃料供給量を計測するもので、この燃料供給量は、
ガス比例弁13に流れる開弁駆動電流を計測することによ
って求められ、熱効率演算部24に加えられる。
The fuel supply amount measuring unit 21 measures the fuel supply amount supplied to the burner 1, and this fuel supply amount is
It is obtained by measuring the valve opening drive current flowing through the gas proportional valve 13 and added to the thermal efficiency calculation unit 24.

【0024】流量検出部23は、流量センサ9からの信号
を受けて給水管6に流入する水の流量を検出しており、
この検出した流量を熱効率演算部24に加える。
The flow rate detector 23 receives the signal from the flow rate sensor 9 and detects the flow rate of water flowing into the water supply pipe 6,
This detected flow rate is added to the thermal efficiency calculation unit 24.

【0025】熱効率演算部24では、前記した入側温度、
出側温度、燃料供給量、流量の情報から、バーナ1の燃
焼運転時の熱効率を、内蔵されている演算回路を用いて
逐次演算モニタする。熱効率の値は、熱効率=実効熱量
/供給熱量=λ・(出側温度−入側温度)・流量/(α
・燃料供給量)を計算することにより求められる。ここ
で、λは加熱媒体の比熱であり、水の場合は1となる。
また、αは燃料であるガスの単位体積当たりの熱量であ
る。このように求められた熱効率の演算値は、メモリ31
に逐次記憶される。
In the thermal efficiency calculation unit 24, the above-mentioned inlet temperature,
The thermal efficiency during combustion operation of the burner 1 is sequentially calculated and monitored from the information on the outlet side temperature, the fuel supply amount, and the flow rate by using a built-in calculation circuit. The value of thermal efficiency is thermal efficiency = effective heat amount / supply heat amount = λ · (outlet temperature − inlet temperature) · flow rate / (α
-Fuel supply amount) is calculated. Here, λ is the specific heat of the heating medium and is 1 in the case of water.
Further, α is the amount of heat per unit volume of gas that is fuel. The calculated value of the thermal efficiency thus obtained is stored in the memory 31
Are sequentially stored in.

【0026】安定判定部25は、メモリ31に記憶されてい
る熱効率の演算値を読み出し、直前の熱効率の値と最新
の熱効率の演算値とを比較して、この差が予め与えられ
ている許容範囲よりも小さくなったときに、熱効率が安
定したものと判断して、安定信号を平均熱効率算出部27
に加える。
The stability judgment unit 25 reads the calculated value of the thermal efficiency stored in the memory 31, compares the immediately preceding thermal efficiency value with the latest calculated value of the thermal efficiency, and this difference is given in advance. When it becomes smaller than the range, it is judged that the thermal efficiency is stable, and the stability signal is sent to the average thermal efficiency calculation unit 27.
Add to.

【0027】平均熱効率算出部27では、安定信号を受け
ると、安定信号が発せられた以降にメモリ31に記憶され
た最新およびその前、さらにその前の熱効率の演算値を
順に3つを読み出し、この3つの熱効率の演算値の平均
を、内蔵されている演算回路により演算して求め、これ
を平均熱効率として比較判定部28に加える。
When the average thermal efficiency calculation unit 27 receives the stability signal, it reads out the three latest and previous thermal efficiency calculation values stored in the memory 31 after the stability signal is issued, in sequence, The average of the three calculated values of thermal efficiency is calculated by the built-in arithmetic circuit, and this is added to the comparison and determination unit 28 as the average thermal efficiency.

【0028】比較判定部28には比較回路が形成されてお
り、平均熱効率の値を受けて、この値をデータ格納部30
に記憶されている基準熱効率の値と比較する。そして、
平均熱効率の値が基準熱効率の値よりもデータ格納部30
に記憶されている許容偏差を越えて低下したときに、熱
交換機2に煤詰まりが発生したと判断して、煤詰まり検
知信号を報知部29に加え、さらに、COセンサによるC
O安全動作が行われないときには、COセンサ故障検知
信号も報知部29に加える。
A comparison circuit is formed in the comparison / decision unit 28, which receives the value of the average thermal efficiency and uses this value as the data storage unit 30.
It is compared with the reference thermal efficiency value stored in. And
The value of the average thermal efficiency is higher than that of the reference thermal efficiency.
When it falls below the allowable deviation stored in the table, it is determined that soot clogging has occurred in the heat exchanger 2, a soot clogging detection signal is added to the notifying unit 29, and the CO sensor
When the O-safe operation is not performed, the CO sensor failure detection signal is also added to the notification unit 29.

【0029】報知部29では、煤詰まり検知信号やCOセ
ンサ故障検知信号を受けて、警報器40を鳴らしたり、あ
るいはリモコンの表示部に表示して、燃焼装置の煤詰ま
りやCOセンサ故障の報知を行う。さらに、ガス電磁弁
18を閉めて燃焼停止を行う等の安全動作を行う。
The notification unit 29 receives the soot clogging detection signal or the CO sensor failure detection signal and sounds the alarm 40 or displays it on the display unit of the remote controller to notify of the soot clogging of the combustion device or the CO sensor failure. I do. In addition, gas solenoid valve
Perform safety operation by closing 18 and stopping combustion.

【0030】本実施例によれば、バーナの燃焼運転時の
熱効率を逐次演算モニタし、熱効率の演算値が基準熱効
率の値よりも許容偏差を越えて低下したときに、燃焼装
置に煤詰まりがあると判断して煤詰まり検知信号を出力
しており、このように、人間の感覚に頼らずに煤詰まり
が自動的に検知されることになる。
According to the present embodiment, the thermal efficiency of the burner during combustion operation is sequentially monitored, and when the calculated thermal efficiency value falls below the reference thermal efficiency value by more than the allowable deviation, soot is blocked in the combustion device. The soot clogging detection signal is output when it is determined that the soot clogging is detected, and thus the soot clogging is automatically detected without depending on the human sense.

【0031】また、上記のように煤詰まりが検知されて
も、COセンサによるCO安全動作が行われないときに
は、COセンサの故障が検知される。
Even if soot clogging is detected as described above, if the CO safety operation by the CO sensor is not performed, a failure of the CO sensor is detected.

【0032】図4には、本発明を加熱媒体が空気である
FF型石油ファンヒータに適用した第2の実施例の構成
が示されている。部屋から入り込む冷たい空気の入口側
にはフィルタ16が設けられ、冷たい空気は送風ファン15
の回転により熱交換器2の方向へ送られている。入側サ
ーミスタ8は熱交換器2の入側の冷たい空気の温度を、
また、出側サーミスタ10は熱交換器2の出側の暖かい空
気の温度を検出する。また、バーナ1に供給される石油
の量は、電磁ポンプ14により制御されており、この電磁
ポンプ14は、前記給湯器のガス比例弁13と同じ機能を有
している。
FIG. 4 shows the configuration of a second embodiment in which the present invention is applied to an FF type oil fan heater in which the heating medium is air. A filter 16 is provided on the inlet side of the cold air coming from the room, and the cool air is blown by a fan 15
Is sent to the heat exchanger 2 by the rotation. The inlet side thermistor 8 measures the temperature of the cold air on the inlet side of the heat exchanger 2,
Further, the outlet thermistor 10 detects the temperature of warm air on the outlet side of the heat exchanger 2. The amount of oil supplied to the burner 1 is controlled by an electromagnetic pump 14, which has the same function as the gas proportional valve 13 of the water heater.

【0033】さらに、バーナ1に供給される空気は、燃
焼ファン3の回転により屋外より取り込まれている。こ
のバーナ1における空気と石油の燃焼による燃焼火力に
より、熱交換器2を通る空気が加熱されて、この暖かい
空気が部屋に放出される。また、排気側には、排ガス中
のCO濃度を検出するCOセンサ19が装備されており、
このCOセンサ19には、前記第1の実施例同様にCO安
全装置34が接続されており、CO安全装置34は、CO検
出濃度が基準濃度を越えたときCO安全動作が行われる
よう構成されている。
Further, the air supplied to the burner 1 is taken in from the outside by the rotation of the combustion fan 3. The combustion heat generated by the combustion of air and oil in the burner 1 heats the air passing through the heat exchanger 2 and discharges the warm air into the room. Further, the exhaust side is equipped with a CO sensor 19 for detecting the CO concentration in the exhaust gas,
A CO safety device 34 is connected to the CO sensor 19 as in the first embodiment, and the CO safety device 34 is configured to perform a CO safety operation when the detected CO concentration exceeds a reference concentration. ing.

【0034】このCOセンサ付FF型石油ファンヒータ
の場合にも、熱交換器2に煤詰まりがあれば、バーナ1
の燃焼運転時の熱効率を、前記第1の実施例同様に、逐
次演算モニタすることにより煤詰まりが検知される。た
だし、この場合、図1に示す第1の実施例における燃料
供給量計測部21では、ガス比例弁13の代わりに電磁ポン
プ14を用いて、その駆動電流により石油の燃料供給量を
計測しており、また、流量検出部22では、流量センサ9
の代わりに送風ファン15を用い、この消費電力から空気
の流量としての送風量を求めている。この送風量は、送
風ファン15の回転数によって求めることもできるが、こ
うすると、フィルタ16に目詰まりがあったり、もしく
は、熱交換器2の出側から逆風があって、排気抵抗が大
きくなると送風量と送風ファン15の回転数とが比例しな
くなり、送風ファン15の回転数から正確な送風量が得ら
れなくなる。
Also in the case of this FF type oil fan heater with a CO sensor, if there is soot clogging in the heat exchanger 2, the burner 1
The soot clogging can be detected by sequentially monitoring the thermal efficiency during the combustion operation in the same manner as in the first embodiment. However, in this case, in the fuel supply amount measuring unit 21 in the first embodiment shown in FIG. 1, the electromagnetic pump 14 is used instead of the gas proportional valve 13, and the fuel supply amount of oil is measured by the drive current thereof. In addition, in the flow rate detection unit 22, the flow rate sensor 9
The blower fan 15 is used instead of, and the amount of blown air as the flow rate of air is obtained from this power consumption. This amount of blown air can be obtained by the number of rotations of the blower fan 15, but if this is done, if the filter 16 is clogged or there is backwind from the outlet side of the heat exchanger 2, the exhaust resistance becomes large. The amount of blown air and the number of revolutions of the blower fan 15 are not proportional to each other, and an accurate amount of blown air cannot be obtained from the number of revolutions of the blower fan 15.

【0035】一方、上記のように排気抵抗が大きくなる
と、送風ファン15の吹き出し側の圧力が高まって、送風
ファン15は空転に近くなり、送風ファン15を駆動するモ
ニタ15aの負荷が小さくなるので、送風ファン15の消費
電力は小さくなる。また、排気抵抗が大きくなると送風
量も小さくなるため、送風量が小さくなると送風ファン
15の消費電力も小さくなる傾向となるが、消費電力と送
風量は必ずしも比例関係とはならないので、本実施例で
は、送風ファン15の回転数と消費電力の情報によって送
風量を正確に求めている。
On the other hand, when the exhaust resistance increases as described above, the pressure on the blow-out side of the blower fan 15 increases, the blower fan 15 becomes nearly idle, and the load on the monitor 15a that drives the blower fan 15 decreases. The power consumption of the blower fan 15 is small. Also, as the exhaust resistance increases, the air flow also decreases.
Although the power consumption of 15 also tends to be small, since the power consumption and the air flow rate are not necessarily in a proportional relationship, in the present embodiment, the air flow rate is accurately obtained from the information of the rotation speed of the air blower fan 15 and the power consumption. There is.

【0036】以上のように、送風ファン15の回転数と消
費電力より送風量が、入側サーミスタ8と出側サーミス
タ10より熱交換器2の入側と出側の温度情報が、また、
電磁ポンプ14の駆動電流により燃料供給量が求められ、
これらの情報に基づいて第1の実施例同様に熱効率が逐
次演算モニタされ、その安定したとき以降の熱効率の平
均値が基準熱効率と比較されることにより、煤詰まりの
検知が自動的に行われる。また、煤詰まりが検知されて
も、COセンサによるCO安全動作が行われないときに
は、COセンサの故障が検知されることとなり、前記第
1の実施例同様の効果を奏する。
As described above, the amount of air blown from the number of revolutions of the blower fan 15 and the power consumption, the temperature information of the inlet side and the outlet side of the heat exchanger 2 from the inlet side thermistor 8 and the outlet side thermistor 10, and
The fuel supply amount is obtained by the drive current of the electromagnetic pump 14,
As in the first embodiment, the thermal efficiency is sequentially calculated and monitored based on this information, and the average value of the thermal efficiencies after the stabilization is compared with the reference thermal efficiency, so that the soot clogging is automatically detected. . Further, even if soot clogging is detected, if the CO safety operation by the CO sensor is not performed, a failure of the CO sensor is detected, and the same effect as in the first embodiment is obtained.

【0037】なお、本発明は上記実施例に限定されるこ
とはなく、様々な実施の態様を採り得る。例えば、上記
各実施例では、煤詰まり検知信号を発生するときと、C
Oセンサの故障を検知するときのそれぞれの許容偏差を
同一の値に設定して、安定熱効率の値が、基準熱効率の
値よりも許容偏差を越えて低下して煤詰まりが検知され
ると、COセンサの故障も検知するように構成したが、
COセンサの故障の検知は、上記煤詰まりの検知よりも
早く、すなわち、許容偏差よりも小さな値を準許容偏差
として新たに設定して、平均熱効率の値が基準熱効率の
値よりもこの準許容偏差を越えて低下したときに、CO
センサの故障が検知されるようにしてもよい。
The present invention is not limited to the above-mentioned embodiment, and various embodiments can be adopted. For example, in each of the above-described embodiments, when the soot clogging detection signal is generated, and when C
When each allowable deviation when detecting a failure of the O sensor is set to the same value, and the value of stable thermal efficiency is lower than the value of the reference thermal efficiency by more than the allowable deviation, soot clogging is detected, Although it is configured to detect the CO sensor failure,
The detection of the CO sensor failure is faster than the detection of the soot clogging, that is, a value smaller than the allowable deviation is newly set as the quasi-permissible deviation, and the average thermal efficiency value is lower than the reference thermal efficiency value. When it falls below the deviation, CO
A sensor failure may be detected.

【0038】また、上記各実施例では、熱効率が安定し
た以降の平均熱効率の値を、メモリ31に記憶されている
最新のもの、その前のもの、さらにその前のものと、3
つの熱効率の平均値から求めたが、3つ以外の複数個の
熱効率の平均値から求めてもよい。さらに、平均熱効率
を求めることなく、熱効率が安定した以降のメモリ31に
記憶されている最新の熱効率の値だけを用いて、基準熱
効率の値と比較するようにしてもよい。
In each of the above-mentioned embodiments, the average thermal efficiency value after the thermal efficiency is stabilized is the latest one stored in the memory 31, the previous one, the previous one, and the previous one stored in the memory 31.
The average value of the three thermal efficiencies is used, but the average value of the plurality of thermal efficiencies other than three may be used. Furthermore, the average thermal efficiency may not be calculated, and only the latest thermal efficiency value stored in the memory 31 after the thermal efficiency becomes stable may be used for comparison with the reference thermal efficiency value.

【0039】さらに、上記実施例では、燃料供給量をガ
ス比例弁13や電磁ポンプ14に流れる駆動電流から求めた
が、ガス管や石油管等の燃料を供給する管に流量計を配
設して、直接燃料供給量を計測するようにしてもよい。
Further, in the above embodiment, the fuel supply amount was obtained from the drive current flowing through the gas proportional valve 13 and the electromagnetic pump 14. However, a flow meter is installed in a gas supply pipe such as a gas pipe or a petroleum pipe. Then, the fuel supply amount may be directly measured.

【0040】さらに、上記各実施例では、COセンサ付
の給湯器や石油ファンヒータを用いて説明したが、CO
センサが装備されていない燃焼装置においても、上記各
実施例の同様の方法によって燃焼装置の煤詰まりが検知
されることは当然である。
Further, in each of the above embodiments, the water heater with the CO sensor and the petroleum fan heater are used for explanation.
Even in a combustion apparatus not equipped with a sensor, it is natural that the soot clogging of the combustion apparatus can be detected by the same method as in the above-described embodiments.

【0041】さらに、上記第1の実施例では、煤詰まり
検知信号やCOセンサ故障検知信号が報知部29に加えら
れると、報知部29でガス電磁弁18を閉めてガス燃料路を
遮断し燃焼停止を行うようにしたが、報知部29では、前
記各検知信号が加えられると、CO安全装置5に遮断信
号を加えて、CO安全装置5を介して、前記同様にガス
燃料路を遮断して燃焼停止を行うようにしてもよい。さ
らには、警報を出したり、換気扇を回すようにしたり、
リモコンに表示したりする等してもよい。
Further, in the first embodiment, when the soot clogging detection signal or the CO sensor failure detection signal is applied to the notification section 29, the notification section 29 closes the gas solenoid valve 18 to shut off the gas fuel passage and burn. Although the stop is performed, in the notification unit 29, when each of the detection signals is added, a cutoff signal is added to the CO safety device 5 to cut off the gas fuel path through the CO safety device 5 in the same manner as described above. Alternatively, the combustion may be stopped. In addition, it gives an alarm, turns on a ventilation fan,
It may be displayed on a remote controller or the like.

【0042】さらに、上記実施例では、演算される熱効
率の最新の値とその直前の値との差が許容範囲よりも小
さくなったときに熱効率が安定したものと判断したが、
バーナの点火時から一定の時間を設定し、この時間が経
過したときに熱効率が安定したものと判断するようにし
てもよい。
Further, in the above embodiment, it was determined that the thermal efficiency was stable when the difference between the latest calculated thermal efficiency value and the immediately preceding value was smaller than the allowable range.
It is also possible to set a certain time from when the burner is ignited and to judge that the thermal efficiency is stable when this time has elapsed.

【0043】さらに、上記実施例では、熱効率の演算値
が安定した以降に熱効率演算値と基準熱効率とを比較し
て煤詰まりやCOセンサの故障を検知したが、熱効率の
演算値が安定したか否かは判断せず、例えば、バーナの
点火開始時からの時間と燃焼量に基づく基準熱効率のデ
ータを予め与えておき、点火時からの熱効率演算値をこ
の基準熱効率と比較して同様に煤詰まりやCOセンサの
故障を検知するようにしてもよい。この場合、出側サー
ミスタ10の測定温度は流量によりタイムラグが発生する
ので、流量に応じた補正を行うことにより、その温度を
正確に得ることができる。
Further, in the above embodiment, after the calculated value of the thermal efficiency is stable, the calculated value of the thermal efficiency is compared with the reference thermal efficiency to detect the soot clogging or the failure of the CO sensor. Is the calculated value of the thermal efficiency stable? It is not determined whether or not, for example, data of the reference thermal efficiency based on the time from the start of ignition of the burner and the amount of combustion is given in advance, and the thermal efficiency calculation value from the time of ignition is compared with this reference thermal efficiency. It is also possible to detect clogging or a CO sensor failure. In this case, since the measured temperature of the output side thermistor 10 causes a time lag depending on the flow rate, the temperature can be accurately obtained by performing correction according to the flow rate.

【0044】さらに、燃料供給量に応じて燃焼ファン3
の送風量を可変し、燃料供給量≒ファン送風量として燃
焼制御しているタイプの燃焼装置にあっては、ファン送
風量のデータを燃料供給量のデータとして用いてもよ
く、この場合、燃料供給量≒ファン送風量≒ファン回転
数として扱ってもよい。
Further, the combustion fan 3 is used depending on the fuel supply amount.
In a combustion device of a type in which combustion control is performed by varying the air supply amount of the fan so that the fuel supply amount is equal to the fan air supply amount, the fan air supply amount data may be used as the fuel supply amount data. The amount of air supplied may be treated as the amount of fan air blown by the number of fan rotations.

【0045】[0045]

【発明の効果】本発明は、燃焼装置の煤詰まりを、バー
ナの燃焼運転時の熱交換器の入側と出側の加熱媒体の温
度情報と、加熱媒体の流量と、燃料供給量とに基づい
て、熱効率が逐次演算モニタされ、この熱効率の演算値
が基準熱効率の値よりも許容偏差を越えて低下したとき
に煤詰まりがあったものと判断して、煤詰まり検知信号
を出力しており、従来のように、人間の感覚に頼らず
に、燃焼装置の煤詰まりが自動的に検知できるようにな
る。
Industrial Applicability According to the present invention, the soot clogging of the combustion device is determined by the temperature information of the heating medium on the inlet side and the outlet side of the heat exchanger during the burner combustion operation, the flow rate of the heating medium, and the fuel supply amount. Based on this, the thermal efficiency is sequentially monitored, and when the calculated value of this thermal efficiency falls below the reference thermal efficiency value by more than the allowable deviation, it is judged that there is soot clogging, and the soot clogging detection signal is output. Therefore, it becomes possible to automatically detect the soot clogging of the combustion device without relying on the human sense as in the conventional case.

【0046】また、COセンサ付燃焼装置にあっては、
上記のように、煤詰まりの検知があるものと判断されて
も、COセンサによるCO安全動作が行われないときに
は、COセンサの故障が自動的に検知され、COガスに
対する対策は万全なものとなる。
Further, in the combustion device with a CO sensor,
As described above, even if it is determined that the soot clogging is detected, when the CO safety operation by the CO sensor is not performed, the failure of the CO sensor is automatically detected, and the measures against the CO gas are considered to be perfect. Become.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明に係る燃焼装置の煤詰まり検知方法とそ
れを利用したCOセンサ付燃焼装置のCOセンサ故障検
知方法を行う第1の実施例のブロック構成図である。
FIG. 1 is a block diagram of a first embodiment for carrying out a soot clogging detection method for a combustion apparatus according to the present invention and a CO sensor failure detection method for a combustion apparatus with a CO sensor using the method.

【図2】同実施例に使用される給湯器のシステム構成図
である。
FIG. 2 is a system configuration diagram of a water heater used in the embodiment.

【図3】同実施例において煤詰まりがあるときとないと
きの熱効率の経時変化を示すグラフである。
FIG. 3 is a graph showing changes with time in thermal efficiency with and without soot clogging in the example.

【図4】本発明をFF型石油ファンヒータに適用した第
2の実施例の構成図である。
FIG. 4 is a configuration diagram of a second embodiment in which the present invention is applied to an FF type oil fan heater.

【図5】燃焼ファンを排気側に配設したタイプの給湯器
の煤詰まりの態様を示す説明図である。
FIG. 5 is an explanatory view showing a mode of soot clogging of a water heater of a type in which a combustion fan is arranged on the exhaust side.

【図6】燃焼ファンを給気側に配設したタイプの給湯器
の煤詰まりの態様を示す説明図である。
FIG. 6 is an explanatory view showing a mode of soot clogging of a water heater of a type in which a combustion fan is arranged on the air supply side.

【符号の説明】[Explanation of symbols]

1 バーナ 2 熱交換器 3 燃焼ファン 1 burner 2 heat exchanger 3 combustion fan

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 バーナに供給される燃料を、燃焼ファン
の回転によって取り込まれる空気を利用して燃焼し、こ
の燃焼火力でもって熱交換器を通る加熱媒体を加熱する
燃焼装置の煤詰まり検知方法であって、熱交換器の入側
と出側における加熱媒体の温度情報と、燃料供給量と、
加熱媒体の流量とを含む情報を取り込んで、バーナの燃
焼運転時に熱効率を逐次演算モニタし、予め与えられる
基準熱効率の値と比較し、熱効率の演算値が基準熱効率
の値よりも所定の許容偏差を越えて低下したときに熱交
換器の煤詰まりが発生したと判断して煤詰まり検知信号
を出力する燃焼装置の煤詰まり検知方法。
1. A soot clogging detection method for a combustion device, in which fuel supplied to a burner is burned by using air taken in by rotation of a combustion fan, and a heating medium passing through a heat exchanger is heated by the combustion power. And, the temperature information of the heating medium on the inlet side and the outlet side of the heat exchanger, the fuel supply amount,
The information including the flow rate of the heating medium is taken in, the thermal efficiency is sequentially calculated and monitored during the burner combustion operation, and it is compared with the reference thermal efficiency value given in advance, and the calculated thermal efficiency value has a predetermined allowable deviation from the reference thermal efficiency value. A soot clogging detection method for a combustion device, which judges that the soot clogging of the heat exchanger has occurred when the temperature falls below the limit and outputs a soot clogging detection signal.
【請求項2】 燃焼装置に排気ガス中のCO濃度を検出
するCOセンサと、COセンサのCO検出濃度が予め与
えられる基準濃度に達したときにCO安全動作を行うC
O安全装置が設けられ、請求項1記載の方法で演算され
る熱効率の演算値が予め与えられる基準熱効率の値より
も所定の許容偏差を越えて低下したときにCOセンサの
故障検知信号を出力するCOセンサ付燃焼装置のCOセ
ンサの故障検知方法。
2. A CO sensor for detecting a CO concentration in exhaust gas in a combustion apparatus, and a C sensor for performing a CO safe operation when the detected CO concentration of the CO sensor reaches a predetermined reference concentration.
An O safety device is provided and outputs a CO sensor failure detection signal when the calculated value of the thermal efficiency calculated by the method according to claim 1 is lower than a predetermined reference thermal efficiency value by a predetermined allowable deviation. Method for detecting failure of CO sensor in combustion apparatus with CO sensor.
JP24592293A 1993-09-06 1993-09-06 Combustion apparatus, method for detecting soot clogging thereof, and method for detecting failure of CO sensor in combustion apparatus with CO sensor using the same Expired - Fee Related JP3312968B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24592293A JP3312968B2 (en) 1993-09-06 1993-09-06 Combustion apparatus, method for detecting soot clogging thereof, and method for detecting failure of CO sensor in combustion apparatus with CO sensor using the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24592293A JP3312968B2 (en) 1993-09-06 1993-09-06 Combustion apparatus, method for detecting soot clogging thereof, and method for detecting failure of CO sensor in combustion apparatus with CO sensor using the same

Publications (2)

Publication Number Publication Date
JPH0777327A true JPH0777327A (en) 1995-03-20
JP3312968B2 JP3312968B2 (en) 2002-08-12

Family

ID=17140845

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24592293A Expired - Fee Related JP3312968B2 (en) 1993-09-06 1993-09-06 Combustion apparatus, method for detecting soot clogging thereof, and method for detecting failure of CO sensor in combustion apparatus with CO sensor using the same

Country Status (1)

Country Link
JP (1) JP3312968B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000274678A (en) * 1999-03-26 2000-10-03 Noritz Corp Abnormality judging unit for combination combustor
CN106527382A (en) * 2016-12-14 2017-03-22 南京南瑞继保电气有限公司 Coke oven thermal efficiency online monitoring method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000274678A (en) * 1999-03-26 2000-10-03 Noritz Corp Abnormality judging unit for combination combustor
CN106527382A (en) * 2016-12-14 2017-03-22 南京南瑞继保电气有限公司 Coke oven thermal efficiency online monitoring method

Also Published As

Publication number Publication date
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