JPS6331694B2 - - Google Patents

Info

Publication number
JPS6331694B2
JPS6331694B2 JP57061463A JP6146382A JPS6331694B2 JP S6331694 B2 JPS6331694 B2 JP S6331694B2 JP 57061463 A JP57061463 A JP 57061463A JP 6146382 A JP6146382 A JP 6146382A JP S6331694 B2 JPS6331694 B2 JP S6331694B2
Authority
JP
Japan
Prior art keywords
gas
pressure
combustion
variable throttle
throttle mechanism
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
Application number
JP57061463A
Other languages
Japanese (ja)
Other versions
JPS58178117A (en
Inventor
Hideo Uematsu
Takashi Tanahashi
Yoshuki Yokoajiro
Tomohide Matsumoto
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 Holdings Corp
Original Assignee
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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP57061463A priority Critical patent/JPS58178117A/en
Publication of JPS58178117A publication Critical patent/JPS58178117A/en
Publication of JPS6331694B2 publication Critical patent/JPS6331694B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N1/00Regulating fuel supply
    • F23N1/08Regulating fuel supply conjointly with another medium, e.g. boiler water
    • F23N1/082Regulating fuel supply conjointly with another medium, e.g. boiler water using electronic means
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N2225/00Measuring
    • F23N2225/02Measuring filling height in burners
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N2225/00Measuring
    • F23N2225/08Measuring temperature
    • F23N2225/18Measuring temperature feedwater temperature
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N2233/00Ventilators
    • F23N2233/06Ventilators at the air intake
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N2235/00Valves, nozzles or pumps
    • F23N2235/12Fuel valves

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Control Of Combustion (AREA)
  • Feeding And Controlling Fuel (AREA)

Description

【発明の詳細な説明】 本発明は、ガス燃焼機器、とりわけガス給湯装
置に於ける燃焼出力範囲拡大の為の一手段に関す
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a means for expanding the combustion output range of gas combustion equipment, particularly gas water heaters.

従来のガス給湯装置は第1図に示すように構成
されている。すなわち、ガス系統は、第1の電磁
弁1、第2の電磁弁2、ガス圧力制御弁3がシリ
ーズに結合され、さらにガス圧力制御弁3に固定
ノズル4が結合され、制御された燃料ガスが、予
混合バーナ5に供給されるように構成されてい
る。予混合バーナ5の上部または下部には熱交換
器6が配置され、この熱交換器6で水を温水にす
べく燃焼ガスのもつ熱量を熱交換している。熱交
換器6の出湯口には、温度検知器7が取付けられ
ており、その電気信号が、フアン8用の電気制御
回路()9に導びかれている。
A conventional gas water heater is constructed as shown in FIG. That is, in the gas system, a first solenoid valve 1, a second solenoid valve 2, and a gas pressure control valve 3 are connected in series, and a fixed nozzle 4 is further connected to the gas pressure control valve 3 to control the controlled fuel gas. is supplied to the premix burner 5. A heat exchanger 6 is disposed above or below the premix burner 5, and the heat exchanger 6 exchanges heat of the combustion gas in order to turn water into hot water. A temperature detector 7 is attached to the outlet of the heat exchanger 6, and its electrical signal is led to an electrical control circuit () 9 for the fan 8.

10は、フアン8の送風管11のある個所と燃
料ガス及び空気との混合部12との差圧を検出す
る圧力検出器であり、この圧力検出器10からの
電気信号が、ガス圧力制御弁3用の電気制御回路
()13に導びかれている。
Reference numeral 10 denotes a pressure detector that detects the differential pressure between the blow pipe 11 of the fan 8 and the fuel gas and air mixing section 12, and an electrical signal from this pressure detector 10 is transmitted to the gas pressure control valve. It is led to an electric control circuit ( ) 13 for 3.

上記構成に於いて、定格最大燃焼状態から順次
燃焼量を絞つていく場合を想定し第1図と第2図
を使つて説明する。
In the above configuration, a case where the combustion amount is sequentially reduced from the rated maximum combustion state will be explained using FIGS. 1 and 2.

すなわち、例えば出湯量を減少させると、温度
検知器7からフアン8の送風量を減少させるよう
な電気信号が、電気制御回路()9に入力さ
れ、フアン8の送風量を減少させる。したがつ
て、送風量の変化に対応した電気信号が圧力検出
器10に発生し、この電気信号は、即,ガス圧力
制御弁3用の電気制御回路()13でガス圧力
制御弁3の駆動用電気信号に処理されて、送風量
に対応した燃焼ガスになるべくガス制御弁3を制
御する。
That is, for example, when the amount of hot water dispensed is decreased, an electrical signal for reducing the amount of air blown by the fan 8 is inputted from the temperature sensor 7 to the electric control circuit ( ) 9, and the amount of air blown by the fan 8 is decreased. Therefore, an electric signal corresponding to the change in air flow rate is generated in the pressure detector 10, and this electric signal is immediately used to drive the gas pressure control valve 3 in the electric control circuit ( ) 13 for the gas pressure control valve 3. The gas control valve 3 is processed into an electrical signal to control the gas control valve 3 so that the combustion gas corresponds to the amount of air blown.

第2図は、横軸に圧力検出器10の差圧ΔPを
とり縦軸に、燃焼流量Q(この従来例では空気流
量)をとつている。今定格最大燃焼量qnaxの状態
から上記に説明した如く例えば出湯量を減少させ
るなどしてqnio迄燃焼量を絞ると、例えばTDR=
qnio/qnax=1/5にすると、燃焼流量Qと圧力検出
器10の差圧ΔPの間にはQ∝√の関係にある
のでqnioの時のΔPは、qnaxの1/25になる、例え
ば、qnaxのときのΔPが50mmH2Oの場合、qnioのと
きのΔPは2mmH2Oになる。
In FIG. 2, the horizontal axis represents the differential pressure ΔP of the pressure detector 10, and the vertical axis represents the combustion flow rate Q (air flow rate in this conventional example). If we reduce the combustion amount from the current rated maximum combustion amount q nax to q nio by reducing the amount of hot water as explained above, for example, TDR =
When q nio /q nax = 1/5, there is a relationship of Q∝√ between the combustion flow rate Q and the differential pressure ΔP of the pressure detector 10, so ΔP when q nio is 1/25 of q nax For example, if ΔP when q nax is 50 mmH 2 O, ΔP when q nio is 2 mmH 2 O.

またqnio/qnax=1/10に燃焼量を絞ろうとする
とqnioの時のΔPはqnaxの1/100迄小さく制御され
る必要がある。すなわち前の例と同じくqnaxのと
きΔPが50mmH2Oとすると、qnioのときのΔPの値
は0.5mmH2Oという非常に小さな値にまで制御さ
れる必要があり、かつ圧力検出器10には厳しい
精度が要求されることになる。したがつて、圧力
検出器10の圧力の変化で燃焼流量を精度よく制
御しようとした場合、圧力検出器に対する要求精
度がTDR=qnio/qnaxを小さくすればするほど厳
しくなるので実用的には、TDRが1/3〜1/5の値
が限界の値であつた。
In addition, in order to reduce the combustion amount to q nio /q nax = 1/10, ΔP at the time of q nio needs to be controlled to be as small as 1/100 of q nax . That is, as in the previous example, if ΔP is 50 mmH 2 O when q nax , the value of ΔP when q nio needs to be controlled to a very small value of 0.5 mmH 2 O, and the pressure sensor 10 requires strict precision. Therefore, when trying to accurately control the combustion flow rate by changing the pressure of the pressure detector 10, the accuracy required for the pressure detector becomes stricter as TDR = q nio /q nax becomes smaller, so it is not practical. The limit value was a TDR of 1/3 to 1/5.

本発明は、上記従来の欠点を解消するもので、
使用圧力検出器の要求精度をゆるくして、または
検出範囲出力比Δqnio/Δqnaxをできるだけ大きい
値で、燃焼範囲TDRを大ならしめることを目的
とするものである。
The present invention solves the above-mentioned conventional drawbacks,
The purpose is to increase the combustion range TDR by relaxing the required accuracy of the pressure detector used or by setting the detection range output ratio Δq nio /Δq nax to a value as large as possible.

この目的を達成する為に本発明は、出湯温度を
検知する温度検出器と、温度設定部からの温度偏
差信号により、ガス燃焼量を制御する可変絞り機
構を有し、この可変絞り機構の上流と下流の差圧
を検出する圧力検知器を設け、この圧力検知器か
らの電気信号によりガス圧力制御弁を制御するよ
うに構成したものである。
In order to achieve this object, the present invention has a temperature detector that detects the hot water temperature and a variable throttle mechanism that controls the amount of gas combustion based on the temperature deviation signal from the temperature setting section, and upstream of this variable throttle mechanism. A pressure sensor is provided to detect the differential pressure between the gas pressure sensor and the downstream pressure, and the gas pressure control valve is controlled by an electrical signal from the pressure sensor.

この構成によつて、温度偏差信号により、ガス
燃焼量を制御すべく可変絞り機構,すなわち,ノ
ズル,またはオリフイスの流路断面積を可変する
ことで、燃焼流量の圧力制御特性そのものを横断
的に変化させ、容易に燃焼制御範囲TDRの拡大
を可能ならしめたものである。
With this configuration, the temperature deviation signal can be used to control the gas combustion amount by varying the cross-sectional area of the variable throttle mechanism, that is, the nozzle or orifice, thereby controlling the pressure control characteristics of the combustion flow rate. This makes it possible to easily expand the combustion control range TDR.

以下、本発明の一実施例を第3図〜第6図にも
とずいて説明する。なお第3図中第1図と同一部
品については同一番号を付している。
Hereinafter, one embodiment of the present invention will be described based on FIGS. 3 to 6. Note that parts in FIG. 3 that are the same as those in FIG. 1 are given the same numbers.

第3図に於いて4Aは、温度偏差信号をうけて
流路断面積が可変制御される可変絞り機構、14
は温度設定部、15は比較部、判断部からなる調
節操作部、16は温度偏差信号、17は電気信号
である。
In FIG. 3, 4A is a variable throttle mechanism 14 in which the cross-sectional area of the flow path is variably controlled in response to a temperature deviation signal.
15 is a temperature setting section, 15 is an adjustment operation section consisting of a comparison section and a judgment section, 16 is a temperature deviation signal, and 17 is an electric signal.

第4図及び第5図に於いて、横軸は圧力検出器
10の差圧ΔP、縦軸は燃焼流量Qを表わす燃焼
流量の圧力制御特性を示している。
In FIGS. 4 and 5, the horizontal axis shows the differential pressure ΔP of the pressure detector 10, and the vertical axis shows the combustion flow rate Q, which is the pressure control characteristic of the combustion flow rate.

φ1〜φ5(または第5図に於けるφ6)は可変絞り
機構の流路等価断面積を記号で表わし、φ1が、
定格最大燃焼時に於ける可変絞り機構の流路等価
断面積の大きさである。以下φ2,φ3……となる
にしたがい流路等価断面積が小さくなつている。
φ 1 to φ 5 (or φ 6 in Fig. 5) represent the equivalent cross-sectional area of the flow path of the variable throttle mechanism with symbols, and φ 1 is
This is the size of the equivalent cross-sectional area of the flow path of the variable throttle mechanism at the time of maximum rated combustion. Below, as φ 2 , φ 3 . . . , the equivalent cross-sectional area of the flow path becomes smaller.

また、第4図に於ける曲線a〜eは、φ1〜φ5
に夫々対応している燃焼流量の圧力制御特性曲線
である。そして、イは定格最大燃焼時に於ける圧
力検知器10の差圧、ロは本発明に於けるTDR
最小時に於ける差圧、ハは従来例の固定ノズルを
使つた場合(したがつて燃焼流量の圧力制御特性
曲線はaのみである。)のTDR最小時に於ける差
圧の値を示している。
Moreover, curves a to e in FIG. 4 are φ 1 to φ 5
2 is a pressure control characteristic curve of combustion flow rate corresponding to each of the following. A is the differential pressure of the pressure detector 10 at the time of maximum rated combustion, and B is the TDR in the present invention.
The differential pressure at the minimum time, c, shows the value of the differential pressure at the minimum TDR when the conventional fixed nozzle is used (therefore, the combustion flow rate pressure control characteristic curve is only a). .

上記構成に於いて、定格最大燃焼状態から順次
燃焼量を絞つてきた場合を説明する。すなわち,
例えば、出湯量を減少させるとあるいは出湯温度
を低く設定すると、温度検知器7からの電気信号
あるいは温度設定部14からの電気信号が、15
の調節操作部で、比較判断され、温度偏差信号1
6として、4Aの可変絞り機構へ出力される。そ
して、可変絞り機構4Aの流路等価断面積の面積
をφ1からφ2あるいはさらにφ3へと順次温度偏差
信号16に対応した値に変化するように作用す
る。一方、流路等価断面積φ1の値が変化するの
に対応し圧力検知器10の値も変化し、電気信号
17を出力する。この電気信号17は電気制御回
路()13で、ガス圧力制御弁3の操作信号と
して処理されると同時に圧力検知器10の差圧が
小さくなり燃焼量が減少されるようにガス圧力制
御弁3へ出力するものである。
In the above configuration, a case where the combustion amount is sequentially reduced from the rated maximum combustion state will be explained. That is,
For example, when the amount of hot water discharged is decreased or the hot water temperature is set low, the electric signal from the temperature detector 7 or the electric signal from the temperature setting section 14 becomes 15.
The temperature deviation signal 1 is compared and judged in the adjustment operation section of
6, it is output to the 4A variable aperture mechanism. Then, the area of the flow path equivalent cross-sectional area of the variable throttle mechanism 4A is changed from φ 1 to φ 2 or further to φ 3 to a value corresponding to the temperature deviation signal 16 sequentially. On the other hand, as the value of the flow path equivalent cross-sectional area φ 1 changes, the value of the pressure sensor 10 also changes, and an electrical signal 17 is output. This electric signal 17 is processed by the electric control circuit () 13 as an operation signal for the gas pressure control valve 3, and at the same time, the gas pressure control valve 3 This is what is output to.

すなわち、第4図に於いて、曲線aなる燃焼流
量の圧力制御特性曲線上にあつて、φ1の流路等
価断面積の定格最大燃焼量qnaxのとき圧力検知器
10の値がイのとき、出湯量を減少させるあるい
は出湯温度を低く設定しなおすと、従来は、曲線
aの燃焼流量の圧力制御特性曲線上に沿つて変化
していたもので、本発明では可変絞り機構の流路
等価断面積がφ1から順次減少する方向及び、圧
力検知器10の差圧ΔPが減少する方向に制御さ
れるので、第4図のFなるほゞ直線に沿つて制御
されるものである。
That is, in FIG. 4, on the combustion flow rate pressure control characteristic curve a, when the rated maximum combustion amount q nax of the flow path equivalent cross-sectional area of φ 1 , the value of the pressure sensor 10 is i. In the past, when the amount of hot water discharged was reduced or the temperature of hot water discharged was reset to a lower value, the combustion flow rate would change along the pressure control characteristic curve of curve a, but in the present invention, the flow path of the variable throttle mechanism changes. Since it is controlled in the direction in which the equivalent cross-sectional area decreases sequentially from φ 1 and in the direction in which the differential pressure ΔP of the pressure sensor 10 decreases, it is controlled substantially along the straight line F in FIG. 4.

したがつて、第4図をみれば明らかのように最
小燃焼流量値qnioに対応した最小制御圧力が従来
ハであつたものが、本発明では、ロの如く大きな
値になる。つまり、可変絞り機構4Aにより第4
図に示す如く燃焼流量の圧力流量制御特性を変換
し、曲線e上のロに示す如く、従来(曲線a上の
ハ)よりも大きい圧力Δpで最小燃焼流量値qnio
制御できるようにしたので、圧力検知器には高い
精度が要求されない。すなわち、従来と同じ圧力
検知器を使用しても従来より最小燃焼流量値qnio
をより小さく制御できる。
Therefore, as is clear from FIG. 4, the minimum control pressure corresponding to the minimum combustion flow rate value q nio , which was conventionally C, becomes a large value as B in the present invention. In other words, the variable diaphragm mechanism 4A
As shown in the figure, the pressure flow rate control characteristics of the combustion flow rate have been changed, and the minimum combustion flow rate value q nio can be controlled at a pressure Δp greater than the conventional one (c on the curve a), as shown in b on the curve e. Therefore, pressure detectors do not require high accuracy. In other words, even if the same pressure detector is used as before, the minimum combustion flow rate q nio
can be controlled to a smaller extent.

また、この場合、流路等価断面積のみがφ1
ら順次変化して、圧力検知器10の検知する差
圧、すなわち可変絞り機構の上流,下流の差圧
ΔPが一定になるように、ガス圧力制御弁を制御
するようにすると第5図に示す如く差圧がイ′で
すなわち定格最大燃焼時に於ける圧力のまま一定
で、直線Gに沿つて制御されることになる。
In addition, in this case, only the flow path equivalent cross-sectional area changes sequentially from φ 1 , and the gas is When the pressure control valve is controlled, the differential pressure is kept constant at A', that is, the pressure at the maximum rated combustion, as shown in FIG. 5, and is controlled along the straight line G.

次に第3図に於ける可変絞り機構4Aの具体的
構成の一実施例として第6図に示す。
Next, FIG. 6 shows an example of a specific configuration of the variable diaphragm mechanism 4A shown in FIG. 3.

101は可変絞り機構本体、102は弁座、1
03は弁軸、104はオーリングである。弁軸1
03と歯車A105および、ステツピングモータ
106が同軸上で締結されている。そして、歯車
A105から歯車B107を介して、ポテンシヨ
メータ108が回転駆動されるよう配置されてい
る。
101 is the variable throttle mechanism main body, 102 is the valve seat, 1
03 is a valve stem, and 104 is an O-ring. Valve stem 1
03, a gear A105, and a stepping motor 106 are coaxially connected. The potentiometer 108 is arranged to be rotationally driven from the gear A105 to the gear B107.

第6図をみれば明らかのように、温度偏差信号
16に対応して、ステツピングモータ106が回
転駆動され、したがつて、弁座102と、弁軸1
03とで形成される隙間すなわち流路等価断面積
が変化し、ガス燃料流量が前記説明した如く制御
されるものである。
As is clear from FIG. 6, the stepping motor 106 is rotated in response to the temperature deviation signal 16, and therefore the valve seat 102 and the valve shaft 1 are rotated.
03, that is, the equivalent cross-sectional area of the flow path changes, and the gas fuel flow rate is controlled as described above.

以上の説明から明らかなように、本発明のガス
燃焼比例制御装置は、出湯温度の温度偏差信号に
よりガス燃焼量を制御する可変絞り機構を具備
し、この可変絞り機構の上流と下流の差圧を圧力
検知器で検知し、この圧力検知信号でガス圧力制
御弁を制御するようにしたことで、従来のような
固定ノズル方式と比較して、圧力を小さな値まで
制御する必要がなくなり、したがつてガス燃料の
流量制御精度が著しく向上するばかりでなく、定
格最大燃焼流量qnaxと最小燃焼流量qnioの比、い
わゆるTDR(qnio/qnax)を著じるしく小さくで
きるものである。いいかえれば燃焼出力調整範囲
が従来より、大巾に拡大できるものである。
As is clear from the above description, the gas combustion proportional control device of the present invention is equipped with a variable throttle mechanism that controls the amount of gas combustion based on the temperature deviation signal of the outlet temperature, and the differential pressure between the upstream and downstream of the variable throttle mechanism is By detecting this with a pressure detector and using this pressure detection signal to control the gas pressure control valve, there is no need to control the pressure to a small value compared to the conventional fixed nozzle method, which reduces the This not only significantly improves the accuracy of gas fuel flow rate control, but also significantly reduces the ratio of the rated maximum combustion flow rate qnax to the minimum combustion flow rate qnio , the so-called TDR ( qnio / qnax ). . In other words, the combustion output adjustment range can be expanded to a greater extent than in the past.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は従来のガス燃焼比例制御装置の概略シ
ステム図、第2図は従来のガス燃焼比例制御装置
に於ける燃焼流量の圧力制御特性図、第3図は本
発明の一実施例によるガス燃焼比例制御装置の概
略システム図、第4図および第5図は本発明の燃
料流量の圧力制御特性図、第6図は本発明に於け
る可変絞り機構の一実施例である。 3…ガス圧力制御弁、4A…可変絞り機構、7
…温度検知器、10…圧力検知器、14…温度設
定部、16…温度偏差信号、17…電気信号。
Fig. 1 is a schematic system diagram of a conventional gas combustion proportional control device, Fig. 2 is a pressure control characteristic diagram of combustion flow rate in the conventional gas combustion proportional control device, and Fig. 3 is a gas combustion proportional control device according to an embodiment of the present invention. A schematic system diagram of the combustion proportional control device, FIGS. 4 and 5 are fuel flow rate pressure control characteristic diagrams of the present invention, and FIG. 6 is an embodiment of the variable throttle mechanism in the present invention. 3...Gas pressure control valve, 4A...Variable throttle mechanism, 7
...Temperature detector, 10...Pressure detector, 14...Temperature setting section, 16...Temperature deviation signal, 17...Electric signal.

Claims (1)

【特許請求の範囲】 1 ガス給湯装置の出湯温度を検知する温度検出
器と、温度設定部からの温度偏差信号により、ガ
ス燃焼量を制御する可変絞り機構を有し、この可
変絞り機構の上流と下流の差圧を検出する圧力検
知器を設け、この圧力検知器からの電気信号によ
り制御されかつ前記可変絞り機構と直列に配設さ
れたガス圧力制御弁とからなるガス燃焼比例制御
装置。 2 可変絞り機構の上流、下流の差圧がほぼ一定
になるように制御されるガス圧力制御弁とからな
る特許請求の範囲第1項記載のガス燃焼比例制御
装置。 3 可変絞り機構を操作する温度偏差信号により
燃焼に必要な空気量を同時に制御する調節操作部
を有する特許請求の範囲第1項記載のガス燃焼比
例制御装置。
[Claims] 1. A temperature sensor that detects the hot water temperature of the gas water heater, and a variable throttle mechanism that controls the amount of gas burned based on a temperature deviation signal from the temperature setting section, and a variable throttle mechanism that controls the amount of gas burned. A gas combustion proportional control device comprising: a gas pressure control valve which is provided with a pressure sensor for detecting a pressure difference between the pressure sensor and the downstream pressure sensor, and is controlled by an electric signal from the pressure sensor and is arranged in series with the variable throttle mechanism. 2. The gas combustion proportional control device according to claim 1, comprising: a gas pressure control valve that is controlled so that the differential pressure between the upstream and downstream sides of the variable throttle mechanism is approximately constant. 3. The gas combustion proportional control device according to claim 1, further comprising an adjusting operation section that simultaneously controls the amount of air required for combustion based on a temperature deviation signal that operates the variable throttle mechanism.
JP57061463A 1982-04-12 1982-04-12 Proportioning controller for gas combustion Granted JPS58178117A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57061463A JPS58178117A (en) 1982-04-12 1982-04-12 Proportioning controller for gas combustion

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57061463A JPS58178117A (en) 1982-04-12 1982-04-12 Proportioning controller for gas combustion

Publications (2)

Publication Number Publication Date
JPS58178117A JPS58178117A (en) 1983-10-19
JPS6331694B2 true JPS6331694B2 (en) 1988-06-24

Family

ID=13171750

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57061463A Granted JPS58178117A (en) 1982-04-12 1982-04-12 Proportioning controller for gas combustion

Country Status (1)

Country Link
JP (1) JPS58178117A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0315970Y2 (en) * 1984-10-31 1991-04-05
JPS63197946U (en) * 1987-05-29 1988-12-20
JPH01111125A (en) * 1987-09-10 1989-04-27 Samsung Electronics Co Ltd Gas flow controller

Also Published As

Publication number Publication date
JPS58178117A (en) 1983-10-19

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