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JP3094615B2 - Combustion device soot clogging safety device - Google Patents
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JP3094615B2 - Combustion device soot clogging safety device - Google Patents

Combustion device soot clogging safety device

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Publication number
JP3094615B2
JP3094615B2 JP04008347A JP834792A JP3094615B2 JP 3094615 B2 JP3094615 B2 JP 3094615B2 JP 04008347 A JP04008347 A JP 04008347A JP 834792 A JP834792 A JP 834792A JP 3094615 B2 JP3094615 B2 JP 3094615B2
Authority
JP
Japan
Prior art keywords
heat exchanger
combustion
hot water
soot
burner
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 - Lifetime
Application number
JP04008347A
Other languages
Japanese (ja)
Other versions
JPH05196229A (en
Inventor
孝二 伊藤
廣志 川崎
清一 大川
直樹 小谷
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.)
Panasonic Corp
Panasonic Holdings Corp
Original Assignee
Panasonic Corp
Matsushita Electric Industrial 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 Panasonic Corp, Matsushita Electric Industrial Co Ltd filed Critical Panasonic Corp
Priority to JP04008347A priority Critical patent/JP3094615B2/en
Publication of JPH05196229A publication Critical patent/JPH05196229A/en
Application granted granted Critical
Publication of JP3094615B2 publication Critical patent/JP3094615B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Regulation And Control Of Combustion (AREA)
  • Control Of Combustion (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】本発明はガスや石油燃料を熱源と
する給湯器、温水循環式暖房装置の加熱器、浴槽水の循
環加熱器、温風循環式暖房器等の燃焼器具に関し、特に
水や空気を瞬間的に通水加熱する熱交換器が煤詰りした
とき安全な運転を入手できる装置に係る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a combustion apparatus such as a water heater using gas or petroleum fuel as a heat source, a heater for a hot water circulating heating device, a circulating heater for bathtub water, and a hot air circulating heater. The present invention relates to a device capable of obtaining safe operation when a heat exchanger for instantaneously passing and heating water or air is clogged with soot.

【0002】[0002]

【従来の技術】従来、この種の燃焼器具の熱交換器は、
バーナの燃焼開始および停止等の発停時に不完全燃焼を
生じ、燃料としてのガスや石油から未燃の炭素等を出し
て熱交換器の燃焼熱吸収用のフィン等に付着させ、バー
ナの燃焼状態を悪化させていた。そして、未燃炭素はい
わゆる煤として燃焼中にも発生するようになり、フィン
等の煤詰りが加速して熱交換器の熱吸収率としての熱効
率が低下する。この熱吸収率の低下は熱交換器の燃焼室
温度を異常に上昇し、過昇温度検出器を燃焼室側壁外周
等に備えて過昇温度を検出し、危険な運転として運転禁
止の処置を取っていた。
2. Description of the Related Art Conventionally, a heat exchanger of a combustion appliance of this kind has
Incomplete combustion occurs when the burner starts and stops, such as when the burner starts and stops.Unburned carbon, etc. is emitted from gas or oil as fuel and adheres to the fins for absorbing heat absorbed by the heat exchanger to burn the burner. The condition was getting worse. Unburned carbon is also generated during combustion as so-called soot, soot clogging of fins and the like is accelerated, and the heat efficiency as a heat absorption rate of the heat exchanger is reduced. This decrease in the heat absorption rate causes the temperature of the combustion chamber of the heat exchanger to rise abnormally, and an overheating temperature detector is provided on the outer periphery of the side wall of the combustion chamber to detect the overheating temperature. I was taking.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、上記構
成では過昇温度検出器が異常検出時には既に使用上危険
な状態、例えば燃焼室が局部的に破損して燃焼ガスが器
具内の部品を過熱し、火災危険等に到ることがあった。
このため、過昇温度検出器の検出温度を下げると異常で
ないにも拘らず検出して誤動作する不具合いがあり、熱
交換器の煤詰りによる危険を効果的に回避する手段が望
まれていた。
However, in the above configuration, when the overheated temperature detector detects an abnormality, it is already in a dangerous state for use, for example, the combustion chamber is locally damaged and the combustion gas overheats the parts in the appliance. Fire hazard.
For this reason, when the detection temperature of the over-temperature detector is lowered, there is a problem that the detection is performed erroneously even though the temperature is not abnormal, and a means for effectively avoiding danger due to soot clogging of the heat exchanger has been desired. .

【0004】そこで、本発明は熱交換器の煤詰りにより
危険に到る以前に、煤詰りの度合いを検出できる燃焼器
具の煤詰り安全装置を提供する。
Accordingly, the present invention provides a soot clogging safety device for a combustion apparatus, which can detect the degree of soot clogging before a danger due to soot clogging of a heat exchanger.

【0005】[0005]

【課題を解決するための手段】そして、上記目的を達成
するために、本発明による燃焼器具の煤詰り安全装置の
第1手段は、熱交換器への入水温度を検出する入水温度
検出器および通水流量を検出する水量検出器および入水
を加熱するバーナと、バーナへの燃料供給量を調節する
燃料制御手段と、熱交換器からの出湯温度を検出する湯
温検出器および設定する湯温設定器と、前記各検出器と
湯温設定器からの信号を受信し、熱交換器の加熱負荷を
演算して燃料制御手段へ燃料供給量調節の指示信号を出
力する燃焼量指示器および熱交換器の熱効率を演算し
定の熱効率と比較して熱交換器がバーナからの燃焼ガス
通路に煤詰りした度合いを判定する煤詰り効率判定器を
備えたものである。
Means for Solving the Problems In order to achieve the above-mentioned object, a first means of the soot clogging safety device for a combustion appliance according to the present invention comprises: an inlet water temperature detector for detecting an inlet water temperature to a heat exchanger; a burner for heating the water detector and the incoming water to detect the water flow rate, a fuel control means for adjusting the amount of fuel supplied to the burner, hot water detects the hot water temperature from the heat exchanger temperature detector and the hot water set temperature A setter, a combustion amount indicator for receiving signals from each of the detectors and the hot water setter, calculating a heating load of the heat exchanger, and outputting an instruction signal for fuel supply amount adjustment to fuel control means; plant calculates the thermal efficiency of the exchanger
The heat exchanger includes a soot clogging efficiency determiner that determines a degree of soot clogging of the combustion gas passage from the burner as compared with a fixed thermal efficiency .

【0006】[0006]

【0007】[0007]

【0008】[0008]

【作用】上記した第1手段によると、本発明の燃焼器具
の煤詰り安全装置は、熱交換器がバーナの燃焼熱を吸収
するフィン等の燃焼ガス通路に未燃の燃料により煤詰り
の状態を進行させると、煤詰り効率判定器が入水温度検
出器、水量検出器、湯温検出器からの各検出信号を受信
して熱交換器の熱出力を演算する。また、燃焼量指示器
がバーナへ燃料供給量を指示するときに演算した加熱負
荷に対応する熱入力で除算し、熱交換器の熱効率を演算
する。
According to the first means described above, the soot clogging safety device for a combustion appliance according to the present invention is characterized in that the heat exchanger is in a state of soot clogging with unburned fuel in a combustion gas passage such as a fin for absorbing the combustion heat of the burner. Proceeds, the soot clogging efficiency determiner receives each detection signal from the incoming water temperature detector, the water amount detector, and the hot water temperature detector, and calculates the heat output of the heat exchanger. Further, the heat efficiency is calculated by dividing by the heat input corresponding to the heating load calculated when the combustion amount indicator indicates the fuel supply amount to the burner.

【0009】一方、煤詰り効率判定器は熱交換器のフィ
ン等の煤詰りの度合いに応じた熱効率の実験データを基
にし、熱交換器がフィン等の煤詰りにより異常に過熱さ
れて大きな熱応力や高温酸化等を生じ、亀裂や破損等に
より高温の燃焼ガスを熱交換器より他の器具内に漏洩
し、火災危険に到る以前の、未だ安全なときの所定熱効
率を予め比較基準として入力されている。そして、運転
中は熱交換器の熱効率を演算すると所定熱効率と比較
し、前記危険に到る前に所定熱効率を検出でき、煤詰り
の度合いに応じて予告、警告、禁止処置等に周到に活用
し、運転の安全性を確保できる。
On the other hand, the soot clogging efficiency judging device is based on the experimental data of the heat efficiency according to the degree of clogging of the fins of the heat exchanger and the like. Stress, high-temperature oxidation, etc., causing high-temperature combustion gas to leak into other equipment from the heat exchanger due to cracks, breakage, etc. Has been entered. When the heat efficiency of the heat exchanger is calculated during the operation, the heat efficiency can be compared with the predetermined heat efficiency, and the predetermined heat efficiency can be detected before the danger is reached, and utilized for a notice, a warning, a prohibition measure, etc. according to the degree of soot clogging. And driving safety can be ensured.

【0010】[0010]

【0011】[0011]

【0012】[0012]

【実施例】以下、添付図面に示した具体的な実施例によ
り、本発明による燃焼器具の煤詰り安全装置について更
に詳しく説明する。
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a perspective view showing a safety device for combusting soot of a combustion appliance according to the present invention.

【0013】図1は本発明の一実施例として、ガスを燃
料とする瞬間加熱式の給湯器を示し、水道管等から給水
を受ける給水路1は、給水流量を検出する水量検出器
2、給水温度を検出する入水温度検出器3を備え、熱交
換器4に給水する。熱交換器4はバーナ5の燃焼熱を吸
収する多数のフィン6、フィン6をロー付け等により有
して通過する給水を瞬間的に加熱する加熱パイプ7、バ
ーナ5を燃焼させる広い空間を有した燃焼室8、および
伝熱後の燃焼ガスを収集して排出する排気室9等を備え
る。
FIG. 1 shows, as one embodiment of the present invention, a water heater of an instant heating type using gas as a fuel, and a water supply passage 1 for receiving water from a water pipe or the like has a water amount detector 2 for detecting a flow rate of water supply, The apparatus is provided with an incoming water temperature detector 3 for detecting the temperature of supplied water, and supplies water to the heat exchanger 4. The heat exchanger 4 has a large number of fins 6 for absorbing the heat of combustion of the burner 5, a heating pipe 7 for instantaneously heating the feed water passing therethrough by brazing or the like, and a large space for burning the burner 5. And a discharge chamber 9 for collecting and discharging the combustion gas after heat transfer.

【0014】また、ガス供給管等から燃料としてのガス
供給を受けるガス路10は、途中にガス供給量を比例的
に調節する比例弁11を有し、バーナ5に燃料供給す
る。給水を加熱した熱交換器4は給湯路12へ温水を出
湯し、給湯路12は出湯温度を検出する湯温検出器1
3、出湯流量を調節する水量制御弁14を介し、給湯栓
15から温水を給湯する。
The gas passage 10 that receives gas supply as fuel from a gas supply pipe or the like has a proportional valve 11 that adjusts the gas supply proportionally on the way, and supplies fuel to the burner 5. The heat exchanger 4 that has heated the water supply supplies hot water to the hot water supply path 12, and the hot water supply path 12 detects the hot water temperature by the hot water temperature detector 1.
3. Hot water is supplied from a hot water tap 15 via a water flow control valve 14 for adjusting the flow rate of hot water.

【0015】バーナ5の燃焼用空気は、燃焼室8に気密
に取り付けた送風ファン16より供給し、送風ファン1
6の回転数は回転数検出器17で検出する。比例弁11
等は図の破線で示すように制御器18と電気的に接続
し、信号の送受信を行う。制御器18には送風ファン1
6や比例弁11等に駆動信号を出力する駆動手段として
の駆動回路19、駆動回路19へ指示信号を出力する燃
焼量指示器20、駆動回路19からのファン駆動電流を
検出するファン駆動電流検出器としての電流検出回路2
1、熱交換器4の熱効率からフィン6等の煤詰りを判定
する煤詰り効率判定器としての効率判定回路22、送風
ファン16の回転数に応じたファン駆動電流からフィン
6等の煤詰りを判定する煤詰り電流判定器としてのファ
ン電流判定回路23等を設ける。
The combustion air of the burner 5 is supplied from a blower fan 16 airtightly attached to the combustion chamber 8,
The rotation number 6 is detected by a rotation number detector 17. Proportional valve 11
And the like are electrically connected to the controller 18 as shown by the broken lines in FIG. The controller 18 has a blower fan 1
6, a drive circuit 19 as drive means for outputting a drive signal to the proportional valve 11, etc., a combustion amount indicator 20 for outputting an instruction signal to the drive circuit 19, and a fan drive current detection for detecting a fan drive current from the drive circuit 19 Current detection circuit 2 as a detector
1. An efficiency determination circuit 22 as a soot clogging efficiency determiner for determining soot clogging of the fins 6 and the like from the heat efficiency of the heat exchanger 4, and a soot clogging of the fins 6 and the like from a fan drive current corresponding to the rotation speed of the blower fan 16. A fan current determination circuit 23 and the like as a soot clogging current determination device are provided.

【0016】制御器18には操作盤24も電気的に接続
し、操作盤24は制御器18への外部電源入力を指示す
る運転スイッチ25、湯温表示や熱交換器4の煤詰り異
常等を表示する表示器26、給湯栓15からの給湯温度
を設定する湯温設定器27等を備える。
An operation panel 24 is also electrically connected to the controller 18. The operation panel 24 includes an operation switch 25 for instructing input of an external power supply to the controller 18, a hot water temperature display, a soot clogging abnormality of the heat exchanger 4, and the like. And a hot water temperature setting device 27 for setting the hot water temperature from the hot water tap 15.

【0017】以上の構成に基づいて、先ず熱交換器4の
熱吸収動作が煤詰りにより阻害されて悪化する原理から
説明する。図2は熱交換器4を部分的に拡大して示し、
加熱パイプ7は狭い間隔B0 で多数のフィン6を炉中ロ
ー付け加工等により備えている。そして、バーナ5の燃
焼火炎Fが図の白抜き矢印の燃焼ガスGとなり、フィン
6の狭い間隔B0 を通過して熱q0 をフィン6の広い面
積Sに与える。この熱q0 は加熱パイプ7に熱q1 とし
て伝導され、加熱パイプ7内を通過する給水に熱q2
伝熱して温水を加工する。バーナ5は燃焼を開始する点
着火時と加熱燃焼移行初期や燃焼停止時に火炎温度が低
かったり、ガスと空気のバランス等の種々な不安定条件
により不完全燃焼をし、ガスが未燃状態または炭素を分
解しただけでフィン6を通過する。
Based on the above configuration, the principle that the heat absorbing operation of the heat exchanger 4 is hindered and deteriorated by soot clogging will be described first. FIG. 2 shows the heat exchanger 4 partially enlarged.
Heating pipe 7 has a large number of fins 6 by a furnace brazing process or the like at a narrow interval B 0. Then, the combustion gas G next to the combustion flame F of the burner 5 is hollow arrows, and passes through the narrow gap B 0 of fins 6 applies heat q 0 a large area S of the fins 6. The heat q 0 is transmitted to the heating pipe 7 as heat q 1 , and transfers the heat q 2 to the water supply passing through the heating pipe 7 to process hot water. The burner 5 has a low flame temperature at the time of the point ignition for starting the combustion, at the beginning of the transition to the heating combustion, or at the time of the combustion stop, or incomplete combustion due to various unstable conditions such as a balance between the gas and the air. It passes through the fins 6 only by decomposing the carbon.

【0018】そして、図3に示すように内部に低温の給
水を通過して表面温度が低い加熱パイプ7とフィン6の
表面に高温の燃焼ガスGに含有し、燃焼で生じた水分が
結露した所に未燃の燃料や分解された炭素が付着する。
また、分解時に帯電した炭素は電気的にも付着力を有す
る。付着物は燃焼ガスGにより加熱されるが、完成燃焼
するだけの十分な温度条件にないために所謂炭化レベル
の不完全燃焼をし、フィン6や加熱パイプ7に図3に示
すように煤Cとして付着堆積する。また、排気室9の排
気口9a等の他の燃焼ガス通路にも堆積する。
Then, as shown in FIG. 3, high-temperature combustion gas G is contained on the surfaces of the heating pipe 7 and the fin 6 having low surface temperature after passing through the low-temperature water supply, and the moisture generated by the combustion is condensed. Unburned fuel and decomposed carbon adhere to the place.
Further, the carbon charged at the time of decomposition has an electrical adhesive force. The deposits are heated by the combustion gas G. However, since the temperature condition is not sufficient to complete combustion, so-called incomplete combustion at the carbonization level is performed, and soot C is added to the fins 6 and the heating pipe 7 as shown in FIG. Adheres and deposits. Further, it is also deposited on other combustion gas passages such as the exhaust port 9a of the exhaust chamber 9.

【0019】この煤Cは使用時間経過とともに次第に成
長し、例えば図の状態では燃焼ガスGはフィン6や加熱
パイプ7にダイレクトに熱を与えることがなく、伝熱の
不良導体としての煤Cを介して間接的に加熱し、燃焼ガ
スGは十分に放熱せずに排気室9から排出され、熱交換
器4の熱効率が低下する。この熱効率の低下の度合いは
煤Cが付着堆積した層の厚さに比例する。
The soot C gradually grows with the lapse of use time. For example, in the state shown in the figure, the combustion gas G does not directly apply heat to the fins 6 and the heating pipe 7, and the soot C as a poor conductor of heat transfer is removed. The combustion gas G is exhausted from the exhaust chamber 9 without sufficiently radiating heat, and the heat efficiency of the heat exchanger 4 is reduced. The degree of the decrease in the thermal efficiency is proportional to the thickness of the layer on which the soot C is deposited.

【0020】また、煤Cがフィン6に付着して層が成長
すると、燃焼ガスGが通過する間隔Bが逆に狭小化し、
送風ファン16は通気抵抗が増加して送風量を減少す
る。つまり、送風ファン16は駆動回路19によって所
定回転数に制御されるが、煤Cが増加すると清浄時より
も仕事量が小さくなり、駆動回路19が送風ファン16
に与える駆動電流値は次第に少くなって行く。このた
め、比例弁11の燃料供給量に対して送風量が低下し、
燃料と空気のバランスが崩れて空気不足の不完全燃焼と
なり、バーナ5は給水を加熱する通常燃焼時においても
多量の炭素を発生し、フィン6の煤Cは加速度を有して
増大する。排気口9a等についても同様に増える。
Further, when the soot C adheres to the fins 6 and the layer grows, the interval B through which the combustion gas G passes is narrowed.
The blower fan 16 has an increased ventilation resistance and reduces the amount of blown air. In other words, the blower fan 16 is controlled to a predetermined rotation speed by the drive circuit 19, but when the soot C increases, the work becomes smaller than in the clean operation, and the drive circuit 19
, The drive current value gradually decreases. For this reason, the air blowing amount is reduced with respect to the fuel supply amount of the proportional valve 11, and
The balance between fuel and air is lost, resulting in incomplete combustion of insufficient air, the burner 5 generates a large amount of carbon even during normal combustion for heating the feed water, and the soot C of the fins 6 increases with acceleration. Similarly, the number of the exhaust ports 9a increases.

【0021】フィン6等が多量の煤Cで詰ってくると、
バーナ5は不完全燃焼により燃焼火炎Fが大きくなる。
燃焼火炎Fの放射熱による過熱を防止して十分広い燃焼
スペースを設定した燃焼室8は、燃焼火炎Fが増大して
燃焼火炎Fとの距離が減少し、距離の逆二乗に比例する
受熱量が著しく増大して過熱される。過熱を受ける燃焼
室8は熱応力が発生して加工部等に無理な力が加わるこ
とにより亀裂を生じる。また、高温に過熱された銅等の
材料が高温腐蝕により劣化して磨耗し、部分的に欠落し
て破損する。この現象時には亀裂部分や欠落破損部分か
ら燃焼ガスGが器内に漏洩し、信号線の合成樹脂製被覆
や他の可燃物を損傷、発火させる危険状態となる。
When the fins 6 and the like are clogged with a large amount of soot C,
The combustion flame F of the burner 5 increases due to incomplete combustion.
The combustion chamber 8 in which a sufficiently large combustion space is set by preventing overheating due to the radiant heat of the combustion flame F has an increased combustion flame F, a reduced distance from the combustion flame F, and a heat reception amount proportional to the inverse square of the distance. Is significantly increased and overheated. In the combustion chamber 8 which receives overheating, a thermal stress is generated and an unreasonable force is applied to a processed portion or the like, so that a crack is generated. In addition, a material such as copper that has been overheated to a high temperature is deteriorated and abraded by high-temperature corrosion, and is partially lost and damaged. At the time of this phenomenon, the combustion gas G leaks from the cracked portion or the broken portion into the inside of the vessel, and there is a danger of damaging or igniting the synthetic resin coating and other combustibles of the signal line.

【0022】図4は煤Cが成長して付着堆積量が時間経
過と共に進行するレベルを横軸とし、縦軸に熱交換器4
の熱効率または送風ファン16の駆動電流が変化する状
態を図示している。使用初期からレベルCaまでは僅か
な減少傾向にあるが、点bでは下降勾配Tbは相当大き
くなり、点cの下降勾配Tcは著しく大きい。点aは未
だ使用に耐えるが煤Cの堆積を注意すべき状態にあり、
点bではこの後は熱効率やファン駆動電流が加速度的に
悪化する状態にある。そして、点cに到っては末期的
態であり、燃焼室8に亀裂や破損が生じる極めて危険な
燃焼をしている。これ等の点a、b、cは過去の使用実
績や実験データにより十分確かに把握可能となる。
FIG. 4 is a graph in which the horizontal axis represents the level at which the soot C grows and the amount of deposit accumulates with the passage of time, and the vertical axis represents the heat exchanger 4.
3 shows a state in which the thermal efficiency of the fan or the drive current of the blower fan 16 changes. There is a slight decrease from the initial stage of use to the level Ca, but at the point b, the descending gradient Tb is considerably large, and the descending gradient Tc at the point c is extremely large. Point a is in a state where it can still be used but care must be taken for the accumulation of soot C.
At the point b, the thermal efficiency and the fan drive current thereafter deteriorate in an accelerated manner. Then, the point c is in a terminal stage , and the combustion chamber 8 is performing extremely dangerous combustion in which cracks and breakage occur. These points a, b, and c can be grasped with sufficient certainty based on past use results and experimental data.

【0023】次に、効率判定回路22とファン電流判定
回路23が熱交換器4の煤詰りを判定し、煤詰り状態の
レベルに応じて処置する動作について、図5に示すフロ
ーチャートに従って順次説明する。
Next, the operation of the efficiency judgment circuit 22 and the fan current judgment circuit 23 for judging the soot clogging of the heat exchanger 4 and taking action according to the level of the soot clogging state will be described sequentially according to the flowchart shown in FIG. .

【0024】S1(左肩に示す信号で、以下みな同じ)
で運転スイッチ25をオン操作して外部電源から制御器
18に電源投入し、運転スタートの準備をする。S2で
給湯栓15を開栓すると、水量検出器2が給水路1への
通水を検出し、この検出信号を受信した制御器18は運
転スタートを判定する。そして、S3で燃焼量指示器2
0は水量検出器2と入水温度検出器3からの検出信号
と、給湯栓15の開栓時に入力された湯温設定器27の
設定信号に基づいて給湯負荷を演算する。給湯負荷が給
湯器の最大能力を超えるときには駆動回路19に指示
し、給湯流量を最大能力相当に絞り調節する。給湯負荷
を演算すると比例弁11と送風ファン16からの各供給
量を求めて指示信号を出力し、この信号を受信した駆動
回路19は比例弁11と送風ファン16に駆動電流を出
力する。S4では送風ファン16が供給する燃焼用空気
と比例弁11が供給するガスにより、バーナ5が燃焼し
て熱交換器4を通過する給水を加熱昇温し、給湯栓15
から設定温度の温水を供給する。
S1 (signal shown on left shoulder, the same applies hereinafter)
Then, the operation switch 25 is turned on to turn on the power to the controller 18 from the external power supply, and prepare for the operation start. When the hot water tap 15 is opened in S2, the water amount detector 2 detects the flow of water to the water supply channel 1, and the controller 18 receiving this detection signal determines the operation start. Then, in S3, the combustion amount indicator 2
0 calculates the hot water supply load based on the detection signals from the water amount detector 2 and the incoming water temperature detector 3 and the setting signal of the hot water temperature setting device 27 input when the hot water tap 15 is opened. When the hot water supply load exceeds the maximum capacity of the water heater, an instruction is given to the drive circuit 19 to throttle the hot water supply flow rate to the maximum capacity. When the hot water supply load is calculated, the respective supply amounts from the proportional valve 11 and the blower fan 16 are obtained, and an instruction signal is output. The drive circuit 19 receiving this signal outputs a drive current to the proportional valve 11 and the blower fan 16. In S4, the burner 5 burns and the feed water passing through the heat exchanger 4 is heated and heated by the combustion air supplied by the blower fan 16 and the gas supplied by the proportional valve 11, and the hot water tap 15
Supplies hot water at the set temperature.

【0025】バーナ5の燃焼が所定時間経過して安定し
た後も継続されると、S5で電流検出回路21は駆動回
路19が送風ファン16に出力しているファン駆動電流
Iを検出する。一方、効率判定回路22は水量検出器
2、入水温度検出器3、および湯温検出器13からの各
検出信号に基づき、熱交換器4の熱出力を演算し、更に
この熱出力と燃焼量指示器20が演算した給湯負荷に見
合った熱入力とから熱交換器4の熱効率ηを演算する。
この演算熱効率ηとファン駆動電流IはS6からS7の
各フローにおいて、効率判定回路22とファン電流判定
回路23により以下のように判定される。
When the combustion of the burner 5 is continued after the predetermined time has elapsed and stabilized, the current detection circuit 21 detects the fan drive current I which the drive circuit 19 outputs to the blower fan 16 in S5. On the other hand, the efficiency determination circuit 22 calculates the heat output of the heat exchanger 4 based on the detection signals from the water amount detector 2, the incoming water temperature detector 3, and the hot water temperature detector 13, and further calculates the heat output and the combustion amount. The heat efficiency η of the heat exchanger 4 is calculated from the heat input corresponding to the hot water supply load calculated by the indicator 20.
The calculated thermal efficiency η and the fan drive current I are determined as follows by the efficiency determination circuit 22 and the fan current determination circuit 23 in each flow from S6 to S7.

【0026】S6では図4に示した点aに到達したか否
かを判定し、縦軸の値Aに相当する効率ηa、電流Ia
の基準値と、前記検出値としての電流Iと効率ηを各々
比較する。電流Iと効率ηが各々電流Ia、効率ηaを
オーバーしているときは、S7で次のレベルである点b
に到達したか否かを判定する。点bに到達していないと
きには未だ使用上は問題はないが、点aの警告レベルに
あることを表示器26に表示し、やがて使用状態が悪化
する旨を予め報知し、S9に示すように運転は継続す
る。S7で点bをオーバーしたときは、その後は加速度
的に燃焼状態が悪化し、いずれ早期に点cの危険な状態
に到る。そこで、効率判定回路22とファン電流判定回
路23は、S10に示すように直ちに運転を停止し、そ
の後の運転を禁止する処置を行い、表示器26にはその
旨を表示する。
In S6, it is determined whether or not the point a shown in FIG. 4 has been reached, and the efficiency ηa and the current Ia corresponding to the value A on the vertical axis are determined.
Are compared with the current I as the detection value and the efficiency η. When the current I and the efficiency η exceed the current Ia and the efficiency ηa, respectively, a point b at the next level is obtained in S7.
Is determined. When the point b has not been reached, there is no problem in use yet, but the warning level at the point a is displayed on the display 26, and it is notified in advance that the use state will soon deteriorate, and as shown in S9. Driving continues. When the point b is exceeded in S7, the combustion state deteriorates at an accelerated rate thereafter, and the dangerous state at the point c is reached soon. Therefore, the efficiency determination circuit 22 and the fan current determination circuit 23 immediately stop the operation as shown in S10, perform a measure to prohibit the subsequent operation, and display the fact on the display 26.

【0027】上記したS6とS7の判定は2箇の判定回
路22、23の判定を複合し、判定の信頼性を向上して
いる。しかし、必ずしも複合判定によらず、一方の判定
回路が正しい判定動作不能なときには、他の判定回路単
独の判定結果を採用する。つまり、両判定回路22、2
3には各々判定不能な使用状態も存在する。例えば、フ
ァン電流判定回路23の場合は、屋外の設定基準を超え
る強風が排気室9に印加されると、送風ファン16は強
い抵抗を受ける。そして、煤詰りによる抵抗と区別がで
きない状態となる。ところが、効率判定回路22は燃焼
状態が不良になっても、尚ファン電流判定回路23より
良好な状態を検出する。つまり、両判定回路22、23
の判定結果が不一致するときは、良好な判定結果に基づ
いた処置を取る。また、給湯流量が少くて給湯負荷が小
さいときには熱効率は他の給湯負荷時より低下する。し
かし、ファン電流判定回路23が給湯負荷に比例した駆
動電流の煤詰りに対する比率データから判定を下し、給
湯負荷の多少に拘らず判定能力を有し、単独で正しい判
定が可能になっている。
The above determinations in S6 and S7 combine the determinations of the two determination circuits 22 and 23, thereby improving the reliability of the determination. However, when one of the determination circuits cannot perform the correct determination operation, the determination result of the other determination circuit alone is adopted, not necessarily based on the composite determination. That is, the two determination circuits 22, 2
3 also has use states that cannot be determined. For example, in the case of the fan current determination circuit 23, when a strong wind exceeding the outdoor setting reference is applied to the exhaust chamber 9, the blower fan 16 receives a strong resistance. Then, the state cannot be distinguished from the resistance due to soot clogging. However, even if the combustion state becomes poor, the efficiency determination circuit 22 detects a better state than the fan current determination circuit 23. That is, the two determination circuits 22 and 23
If the judgment results do not match, take action based on the good judgment result. When the flow rate of hot water supply is small and the load of hot water supply is small, the thermal efficiency is lower than at other hot water supply loads. However, the fan current determination circuit 23 makes a determination based on the ratio data for soot clogging of the drive current proportional to the hot water supply load, has a determination ability regardless of the degree of the hot water supply load, and can make a correct determination independently. .

【0028】次に、図6は本発明の他の実施例を示し、
前記実施例とは制御器28が異っている。制御器28は
駆動回路19、燃焼量指示器20は変わらず、電圧検出
回路29は駆動回路19が送風ファン16に出力する駆
動電圧を検出する。また、熱交換器の煤詰りの度合いを
判定する煤詰り回転数判定器としての回転数判定回路3
0を備える。そして、上記実施例と同様にして熱交換器
4が煤詰り状態を進行すると、電圧検出回路29は駆動
回路19によって送風ファン16に出力された駆動電圧
を検出し、回転数判定回路30に出力する。ファン駆動
電流は熱交換器4が煤詰りすると、送風ファン16の仕
事量低下に基づいた回転数の減少により、同一の供給電
圧に対して電流値が変化する。このため、送風ファン1
6への駆動信号としての駆動電流に代えて駆動電圧を検
出している。この検出駆動電圧は熱交換器4の煤詰りの
度合いに対応し、警告や運転禁止の複数の比較基準と比
較し、煤詰りの度合いを進行レベルに応じて判定でき
る。
FIG. 6 shows another embodiment of the present invention.
The controller 28 is different from the above embodiment. The controller 28 does not change the drive circuit 19 and the combustion amount indicator 20, and the voltage detection circuit 29 detects the drive voltage output from the drive circuit 19 to the blower fan 16. Further, a rotation speed determination circuit 3 as a soot rotation speed determination device for determining the degree of clogging of the heat exchanger.
0 is provided. When the heat exchanger 4 advances in the soot clogging state in the same manner as in the above embodiment, the voltage detection circuit 29 detects the drive voltage output to the blower fan 16 by the drive circuit 19 and outputs the drive voltage to the rotation speed determination circuit 30. I do. When the heat exchanger 4 is clogged with soot, the fan drive current changes its current value with respect to the same supply voltage due to a decrease in the number of revolutions based on a decrease in the work amount of the blower fan 16. For this reason, the blower fan 1
6, a drive voltage is detected instead of the drive current as the drive signal to the drive signal 6. This detected drive voltage corresponds to the degree of soot clogging of the heat exchanger 4 and can be compared with a plurality of comparison criteria for warning and operation prohibition, and the degree of soot clogging can be determined according to the progress level.

【0029】このように、本実施例によると送風ファン
16を所定回転数に制御する面倒な制御シーケンスが不
要となり、判定動作の簡略化が図れると共に、例えば燃
焼停止後の熱交換器4が燃焼中の蓄熱をして滞留水を沸
騰する、いわゆる後沸き防止のために送風ファン16で
冷却送風するポストパージ中等に極めて容易、かつ単純
な回路構成により煤詰りを判定できる。
As described above, according to the present embodiment, a troublesome control sequence for controlling the blower fan 16 to a predetermined number of rotations becomes unnecessary, so that the determination operation can be simplified and, for example, the heat exchanger 4 after the combustion is stopped is burned. Soot clogging can be determined by a very easy and simple circuit configuration during the post-purge, in which the accumulated heat is stored and the accumulated water is boiled, and the cooling fan is blown by the blower fan 16 to prevent so-called after-boiling.

【0030】なお、本発明は上記給湯器に限定するもの
ではなく、室内放熱器に温水を循環する温水暖房装置の
加熱器、浴槽水を循環加熱する風呂追焚加熱器、室内空
気を循環加熱して居室暖房する温風暖房器等の燃焼器具
にも広く活用でき、熱交換器が使用末期に危険な状態に
到る使用状態を改善できる。
The present invention is not limited to the above-mentioned water heater, but includes a heater of a hot water heating device for circulating hot water to an indoor radiator, a bath reheating heater for circulating and heating bath water, and a circulating heater for indoor air. It can also be widely used for combustion equipment such as a warm air heater for heating a living room, and can improve a use condition in which the heat exchanger reaches a dangerous state at the end of use.

【0031】[0031]

【発明の効果】以上に説明したように、本発明の燃焼器
具の煤詰り安全装置の請求項1では、熱交換器がバーナ
からの燃焼ガスの通路に未燃焼の炭素等により煤を付着
堆積し、排気閉塞の状態になったとき、煤詰り効率判定
器が各検出器の検出信号等に基づいて演算した熱交換器
の熱効率を所定の熱効率と比較するので、正確に煤詰ま
りの度合を判定、例えば入水温度が低くて出湯温度が設
定温度に達しないような場合は煤詰まりに対しては正常
と判断し低温ながらとりあえず湯を使用することが出来
るが、入水温度が高くて出湯温度が設定温度に達しない
場合は当然熱効率が低下していることになるのでこれを
煤詰まりと判定することになり、使い勝手を損なうこと
なく正確に煤詰りの度合いを判定することができる。よ
って熱交換器が末期的に亀裂や破損を生じて危険な運転
に到達する以前の状態を検出し、使用禁止やそれ以前の
使用警告等の周到な報知や運転処置等ができ、使用末期
状態等の燃焼器具をより安全に、かつ安心して使用でき
る。
As described above, according to the first aspect of the present invention, there is provided a safety device for clogging soot of a burning appliance, in which the heat exchanger deposits soot on the passage of the combustion gas from the burner by unburned carbon or the like. However, when the exhaust gas is blocked, the soot clogging efficiency determiner compares the heat efficiency of the heat exchanger calculated based on the detection signals of the respective detectors with a predetermined heat efficiency, so that the soot clogging is accurately performed.
Level, for example, when the incoming water temperature is low and the
Normal for soot clogging when temperature does not reach constant temperature
You can use hot water for the time being at low temperature
But the inlet temperature is too high and the outlet temperature does not reach the set temperature
In this case, it is natural that the thermal efficiency is
Judgment of soot clogging, which impairs usability
The degree of soot clogging can be accurately determined without any problem. Yo
As a result, it is possible to detect the condition before the heat exchanger cracks or breaks at the end of the process and reaches dangerous operation. It is possible to use the burning appliance in a safe state and with security.

【0032】[0032]

【0033】[0033]

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

【図1】本発明の燃焼器具の煤詰り安全装置の一実施例
を示す構成図
FIG. 1 is a configuration diagram showing an embodiment of a soot clogging safety device for a combustion appliance of the present invention.

【図2】同装置の熱交換器の部分拡大断面図FIG. 2 is a partially enlarged sectional view of a heat exchanger of the apparatus.

【図3】同装置の熱交換器の部分拡大断面図FIG. 3 is a partially enlarged sectional view of a heat exchanger of the apparatus.

【図4】燃焼器具の煤詰りにより変化する特性図FIG. 4 is a characteristic diagram that changes due to soot clogging of a combustion appliance.

【図5】同動作を示すフローチャートFIG. 5 is a flowchart showing the operation.

【図6】本発明の他の実施例を示す制御器の構成図FIG. 6 is a configuration diagram of a controller showing another embodiment of the present invention.

【符号の説明】[Explanation of symbols]

16 送風ファン 17 回転数検出器 19 駆動回路 20 燃焼量指示器 21 電流検出回路 22 効率判定回路 23 ファン電流判定回路 29 電圧検出回路 30 回転数判定回路 Reference Signs List 16 blower fan 17 rotation number detector 19 drive circuit 20 combustion amount indicator 21 current detection circuit 22 efficiency determination circuit 23 fan current determination circuit 29 voltage detection circuit 30 rotation number determination circuit

───────────────────────────────────────────────────── フロントページの続き (72)発明者 小谷 直樹 大阪府門真市大字門真1006番地 松下電 器産業株式会社内 (56)参考文献 特開 昭62−200133(JP,A) 特開 平2−146412(JP,A) (58)調査した分野(Int.Cl.7,DB名) F23N 5/24 104 F23N 5/14 370 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Naoki Kotani 1006 Kazuma Kadoma, Osaka Prefecture Matsushita Electric Industrial Co., Ltd. (56) References JP-A-62-200133 (JP, A) JP-A-2-2 146412 (JP, A) (58) Field surveyed (Int. Cl. 7 , DB name) F23N 5/24 104 F23N 5/14 370

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】熱交換器への入水温度を検出する入水温度
検出器および通水流量を検出する水量検出器および入水
を加熱するバーナと、バーナへの燃料供給量を調節する
燃料制御手段と、熱交換器からの出湯温度を検出する湯
温検出器および設定する湯温設定器と、前記各検出器と
湯温設定器からの信号を受信し、熱交換器の加熱負荷を
演算して燃料制御手段へ燃料供給量調節の指示信号を出
力する燃焼量指示器および熱交換器の熱効率を演算し所
定の熱効率と比較して熱交換器がバーナからの燃焼ガス
通路に煤詰りした度合いを判定する煤詰り効率判定器
備えた燃焼器具の煤詰り安全装置。
1. An incoming water temperature detector for detecting an incoming water temperature to a heat exchanger, a water amount detector for detecting a passing water flow rate, a burner for heating the incoming water, and a fuel control means for adjusting a fuel supply amount to the burner. A hot water temperature detector for detecting a hot water temperature from the heat exchanger and a hot water temperature setting device for setting, receiving signals from the detectors and the hot water temperature setting device, and calculating a heating load of the heat exchanger. Calculate the thermal efficiency of the burner indicator and the heat exchanger that output a command signal for adjusting the fuel supply to the fuel control means and compare it with a predetermined thermal efficiency to determine the degree to which the heat exchanger has clogged the combustion gas passage from the burner. and determining soot clogging efficiency determination unit
Soot clogging safety device combustion instrument with a.
JP04008347A 1992-01-21 1992-01-21 Combustion device soot clogging safety device Expired - Lifetime JP3094615B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP04008347A JP3094615B2 (en) 1992-01-21 1992-01-21 Combustion device soot clogging safety device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP04008347A JP3094615B2 (en) 1992-01-21 1992-01-21 Combustion device soot clogging safety device

Publications (2)

Publication Number Publication Date
JPH05196229A JPH05196229A (en) 1993-08-06
JP3094615B2 true JP3094615B2 (en) 2000-10-03

Family

ID=11690689

Family Applications (1)

Application Number Title Priority Date Filing Date
JP04008347A Expired - Lifetime JP3094615B2 (en) 1992-01-21 1992-01-21 Combustion device soot clogging safety device

Country Status (1)

Country Link
JP (1) JP3094615B2 (en)

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JP3687087B2 (en) * 1999-03-26 2005-08-24 株式会社ノーリツ Abnormality judgment device for combined combustion equipment
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JP6674789B2 (en) * 2016-02-12 2020-04-01 リンナイ株式会社 Combustion water heater
CN111623365A (en) * 2020-05-06 2020-09-04 国家电投集团电站运营技术(北京)有限公司 Rotary air preheater refined automatic soot blowing system and soot blowing control method
CN111998384B (en) * 2020-08-27 2023-04-04 广州龙鑫蓄热工业炉有限公司 Automatic timing adjusting method for heat accumulating type burner
JP7564440B2 (en) * 2020-12-22 2024-10-09 株式会社ノーリツ Hot water supply equipment

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