JPS6014974B2 - Forced supply/exhaust type combustion device - Google Patents
Forced supply/exhaust type combustion deviceInfo
- Publication number
- JPS6014974B2 JPS6014974B2 JP5490877A JP5490877A JPS6014974B2 JP S6014974 B2 JPS6014974 B2 JP S6014974B2 JP 5490877 A JP5490877 A JP 5490877A JP 5490877 A JP5490877 A JP 5490877A JP S6014974 B2 JPS6014974 B2 JP S6014974B2
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- JP
- Japan
- Prior art keywords
- air
- combustion
- amount
- pressure
- gas
- 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
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- Regulation And Control Of Combustion (AREA)
Description
【発明の詳細な説明】
本発明は燃焼用空気を送風機で供給し、ガス燃料と混合
してバーナで燃焼させ、その発生熱を流体あるいは固体
と熱交換する強制給排気型燃焼装置に関するものである
。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a forced air supply/exhaust type combustion device that supplies combustion air with a blower, mixes it with gas fuel, burns it with a burner, and exchanges the generated heat with a fluid or solid. be.
さらに詳しく述べると、本発明は燃焼用空気と応動して
ガス量を調節する手段を有し、燃焼量を手動あるいは自
動調節する装置に関するものであり、燃焼量に応じて空
燃比を変化させることを特徴とするものである。本発明
は送風量の低下を損なうことなく送風機を小型化、ある
いは熱交換効率の低下を損なうことなく熱交換器を小型
化することを目的としたものである。さらに本発明の他
の目的は縞霧による熱交換器の腐蝕を防止することにあ
る。さらに本発明の他の目的は低燃焼量時における空燃
比の制御性を良好にすることにある。燃焼用空気を送風
機で供給し、かつ燃焼量を調節できる燃焼装置の燃焼量
に対する空燃比の特性の従来例を第1図に示す。More specifically, the present invention relates to a device that has means for adjusting the amount of gas in response to combustion air, and that manually or automatically adjusts the amount of combustion, and that changes the air-fuel ratio according to the amount of combustion. It is characterized by: An object of the present invention is to downsize a blower without reducing the amount of air blown, or to downsize a heat exchanger without reducing heat exchange efficiency. Still another object of the present invention is to prevent corrosion of a heat exchanger due to striped fog. Still another object of the present invention is to improve the controllability of the air-fuel ratio when the combustion amount is low. FIG. 1 shows a conventional example of the characteristics of the air-fuel ratio with respect to the combustion amount of a combustion device in which combustion air is supplied by a blower and the combustion amount can be adjusted.
すなわち実線Aに示すごとく空燃比は燃焼量の増減にか
かわらず常に一定となるように設計される。送風量調節
装置やガス量調節装置の性能が十分でない場合には、破
線Bあるいは破線Cのように空燃比の変動があるものの
理想的には実線Aの特性になるように構成される。しか
しながら、実線Aの特性の燃焼装置においては次のよう
な欠点があった。すなわち、第1の欠点としては、空燃
比一定で燃焼量が増加すると、燃焼空気量も燃焼量と一
定の比率で増加させねばならず、バーナ、熱交換器、給
排気路の圧力損失となり、大型の送風機が必要となる点
である。第2の欠点としては空燃比一定で燃焼量が変化
すると、燃焼量が大の場合には熱交換効率を高く保つた
めに熱交換面積の大きい比較的大型の熱交換器を必要と
し、燃焼量が小の場合には熱効率が高過ぎて熱交換器内
で結霧が発生し腐蝕を起こし耐久性が劣るという欠点で
ある。本発明はこのような従来の欠点を除去したもので
、以下その実施例について説明する。That is, as shown by the solid line A, the air-fuel ratio is designed to remain constant regardless of the increase or decrease in the combustion amount. If the performance of the air flow rate adjusting device or the gas amount adjusting device is not sufficient, the air-fuel ratio will fluctuate as shown by the broken line B or the broken line C, but ideally it will be configured to have the characteristics shown by the solid line A. However, the combustion device having the characteristics shown by the solid line A had the following drawbacks. That is, the first drawback is that when the combustion amount increases at a constant air-fuel ratio, the amount of combustion air must also increase at a constant ratio to the combustion amount, resulting in pressure loss in the burner, heat exchanger, and air supply and exhaust passages. This requires a large blower. The second drawback is that when the combustion amount changes at a constant air-fuel ratio, a relatively large heat exchanger with a large heat exchange area is required to maintain high heat exchange efficiency when the combustion amount is large. If is small, the thermal efficiency is too high, causing fog to form inside the heat exchanger, causing corrosion and resulting in poor durability. The present invention eliminates these conventional drawbacks, and embodiments thereof will be described below.
第2図は本発明の燃焼量と空燃比の関係をあらわしたも
のである。第2図に示すように本発明は燃焼量が小なる
ときは空燃比を高く保ち、燃焼量が増加するにつれて空
燃比を低く保つようにするものである。上記の目的を達
するための具体的な構成を第3図に示す。第3図は空燃
比制御装置であり、燃焼用空気の通風路中に空気ノズル
1を有する差圧発生部2を設け、ガス圧力調節器3の調
節弁4を固定した主ダイアフラム5のガス圧力室6と対
抗するダイアフラム室7に上記差圧発生部2の高圧部8
の圧力を導圧管9で導き、かっぱね10の荷重と調節弁
4、バランスダイアフラム11、主ダイアフラム5など
の可動部の重量とをつり合わせ、このガス圧力調節器3
の出力圧力を差圧発生部2の高圧部8の圧力とを主ダイ
アフラム5でつり合わせて空燃比を制御するものである
。その燃焼空気量とガス量の混合の関係は次に述べると
うりである。すなわち、差圧発生部2の高圧部8の圧力
をPai、低圧部12の圧力をPno、ガス圧力調節器
3の入口部13の圧力をPzj、出口部14の圧力をP
zo、調節弁4、バランスダイアフラム11、主ダイア
フラム5などの可動部重量をW、調節弁4の弁座15に
密着した位置を基準とした変位をx、調節弁4の変位x
=0のときのばね10の荷重をF、ばね10のばね定数
をk、バランスダイアフラム11の有効受圧面積をAb
、主ダイアフラム5の有効受圧面積をAm、調節弁4に
ガス入口圧力Pzjおよびガス出口圧力Pzoが作用す
る面積をAv、空気の比重量をya、ガスの比重量をy
g、重力の加速度をgとすると燃焼用空気側の差圧発生
部2においては燃焼用空気量QaはQa二KaJ雀(P
a←Pn。FIG. 2 shows the relationship between combustion amount and air-fuel ratio according to the present invention. As shown in FIG. 2, the present invention maintains the air-fuel ratio high when the amount of combustion is small, and keeps the air-fuel ratio low as the amount of combustion increases. A specific configuration for achieving the above purpose is shown in FIG. FIG. 3 shows an air-fuel ratio control device, in which a differential pressure generating section 2 having an air nozzle 1 is provided in the combustion air ventilation path, and the gas pressure of the main diaphragm 5 to which the control valve 4 of the gas pressure regulator 3 is fixed. A high pressure section 8 of the differential pressure generating section 2 is placed in a diaphragm chamber 7 opposite to the chamber 6.
The gas pressure regulator 3
The main diaphragm 5 balances the output pressure with the pressure of the high pressure section 8 of the differential pressure generating section 2 to control the air-fuel ratio. The relationship between the amount of combustion air and the amount of gas mixed is as described below. That is, the pressure of the high pressure part 8 of the differential pressure generating part 2 is Pai, the pressure of the low pressure part 12 is Pno, the pressure of the inlet part 13 of the gas pressure regulator 3 is Pzz, and the pressure of the outlet part 14 is Pz.
zo, the weight of the movable parts such as the control valve 4, balance diaphragm 11, and main diaphragm 5 is W, the displacement based on the position of the control valve 4 in close contact with the valve seat 15 is x, and the displacement of the control valve 4 is x.
When = 0, the load of the spring 10 is F, the spring constant of the spring 10 is k, and the effective pressure receiving area of the balance diaphragm 11 is Ab
, the effective pressure receiving area of the main diaphragm 5 is Am, the area on which the gas inlet pressure Pzz and the gas outlet pressure Pzo act on the control valve 4 is Av, the specific weight of air is ya, the specific weight of gas is y
g, and the acceleration of gravity is g, then in the combustion air side differential pressure generating section 2, the combustion air amount Qa is Qa2KaJ (P
a←Pn.
) ‘11であらわされる。ここでKaは空気ノズル
1の形状によって決定される定数である。一方ガス量Q
gは
Qg=KgJ策(PZ。) '11. Here, Ka is a constant determined by the shape of the air nozzle 1. On the other hand, gas amount Q
g is Qg=KgJ plan (PZ.
−Pn。) ■であらわされる。ここでKgはガス
ノズル16の形状によって決定される定数である。ガス
圧力調節器3においてはダイアフラム室7に差圧発生部
2の高圧部8の圧力Paiが導かれることにより次の式
が成り立つ。PzoAv十PziAb十PzoAm+V
V=PziAv+PzoAb+PaiAm+F−kx‘
3’
ここでバランスダイアフラム11の有効面積Abと、調
節弁4にガス入口圧力Pzjおよびガス出口圧力Pzo
が作用する面積Avを等しく設定すると、【3’式は、
PZ。-Pn. ) ■Represented by. Here, Kg is a constant determined by the shape of the gas nozzle 16. In the gas pressure regulator 3, the pressure Pai of the high pressure section 8 of the differential pressure generating section 2 is introduced into the diaphragm chamber 7, so that the following equation holds true. PzoAv ten PziAb ten PzoAm+V
V=PziAv+PzoAb+PaiAm+F−kx'
3' Here, the effective area Ab of the balance diaphragm 11, the gas inlet pressure Pzz and the gas outlet pressure Pzo of the control valve 4 are calculated.
If the area Av on which is applied is set equal, the formula [3' becomes,
PZ.
=Pai+忘(F−w−kX) ‘41■式を‘2}
式に代入するとQg=Kg偽JPai−W−(F−kX
)−Pn。=Pai+Forget(F-w-kX) '41■Formula '2}
Substituting into the equation, Qg=Kg false JPai-W-(F-kX
)-Pn.
‘5’Am空燃比Rは であらわされる。'5'Am air fuel ratio R is It is expressed as
ここ鴇馬事偽第4図は燃焼量と空気ノズル間差圧Pai
−Pnoの関係をあらわしたものであり、Pai−Pn
oは燃焼量の2乗に比例して増加する。Figure 4 shows the combustion amount and air nozzle differential pressure Pai.
-Pno, and Pai-Pn
o increases in proportion to the square of the combustion amount.
さて燃焼量が小(第4図におけるS点)なる場合にF−
kxs<Wとなるようにばね10で調節を行なうと{6
}式よりとなる。ここで第4図から明らかなように4・
燃焼量時のPai−Pnoは比較的小さいのでQs>1
となってRsは高い値になる。次に燃焼量が大の場合(
L点)には‘6}式はとなる。Now, when the combustion amount is small (point S in Figure 4), F-
When adjusting with spring 10 so that kxs<W, {6
}From the formula. Here, as is clear from Figure 4, 4.
Since Pai-Pno at the time of combustion is relatively small, Qs>1
Therefore, Rs becomes a high value. Next, if the combustion amount is large (
At point L), the formula '6} becomes.
調節弁4の変位幻m−xsおよびばね10のばね定数k
‘ま小さいのでk(xm−総)の値は無視してもよく、
Pai夕−Pnoその著しい増加によりQそ二1になり
、空燃比Rそは低い値になる。すなわち第2図に示す空
燃焼比特性が得られる。第5図はガス圧力調節装置のガ
ス量Qgすなわち燃焼量に対するガス出口圧力Pzoと
空気ノズル高圧部圧力Paiの差圧との関係をあらわし
たもので、上記のように譲圧するとAのような特性とな
る。第2図のような空燃比特性を得る他の方法のガス調
節装置の特性を第5図に示す。Displacement illusion m-xs of control valve 4 and spring constant k of spring 10
' Since it is small, the value of k (xm - total) can be ignored,
Due to the significant increase in Pai and Pno, Q becomes 1, and the air-fuel ratio R becomes a low value. That is, the air-fuel ratio characteristics shown in FIG. 2 are obtained. Figure 5 shows the relationship between the gas outlet pressure Pzo and the air nozzle high pressure part pressure Pai relative to the gas amount Qg of the gas pressure regulator, that is, the combustion amount. Becomes a characteristic. FIG. 5 shows the characteristics of a gas regulating device using another method for obtaining the air-fuel ratio characteristics as shown in FIG.
第5図において、Bは通常の特性であり、Cは本発明に
採用される特性である。すなわちガス流量の増加に伴な
し・ガス出口圧力が高くなるように構成する。具体的に
はガス出口部にベンチュリ管を設け、その低圧部の圧力
をダイアフラム室7に導くことによって得られる。第5
図のような特性のガス圧力調節器を使用することにより
、大燃焼量時に空燃比が低くなることは明らかである。
第6図は本発明の他の実施例を示すもので、ガス量(す
なわち燃焼量)に応動して燃焼用空気量を制御するブロ
ック線図である。In FIG. 5, B is a normal characteristic, and C is a characteristic adopted in the present invention. In other words, the configuration is such that the gas outlet pressure increases as the gas flow rate increases. Specifically, it is obtained by providing a venturi pipe at the gas outlet and guiding the pressure of the low pressure part to the diaphragm chamber 7. Fifth
It is clear that by using a gas pressure regulator with the characteristics shown in the figure, the air-fuel ratio becomes low when the combustion amount is large.
FIG. 6 shows another embodiment of the present invention, and is a block diagram for controlling the amount of combustion air in response to the amount of gas (that is, the amount of combustion).
電気式あるいは機械式のガス量制御器で調節されたガス
量をオリフィスあるいはベンチュリ管などの差圧発生部
で叢圧に変換し、圧力変換器で電気量に変換し、燃焼用
空気通風路に設けられた差圧発生部からの信号と比較し
、さらにその差を基準電圧と比較して、トリガ回路によ
ってサイリスタの導通用を制御してモー外こ供給する電
力量を変化させ、送風機の回転数を制御して空燃比を調
節するものである。基準電圧を0とすると空燃比は第7
図に示したRs,Pm,Rそのように空燃比は一定にな
る。すなわち、たとえば空気量が多いと空気側の圧力変
換器の出力が高くなり、モータに供給される電力量を減
少させ、送風機の回転数を低下させて空気量を減少させ
るように作動する。空燃比はガスあるいは空気側に設け
られた差圧発生部の形状によって決定される。しかるに
基準電圧を正の一定値に保っておくと、小燃焼量時には
燃焼用空気量が多くすなわち空燃比が高く、大燃焼量時
には差圧発生部の形状によって定まる空燃比に近づき、
差圧発生部を空燃比が低くなるように設定しておけば空
燃比は低くすることが可能である。すなわち第7図の実
線の特性が得られる。Bは通常の特性であり、Cは本発
明に採用される特性である。The amount of gas adjusted by an electrical or mechanical gas amount controller is converted into a plexus pressure using a differential pressure generator such as an orifice or venturi tube, and then converted into an electrical amount by a pressure converter, which is then sent to the combustion air ventilation path. The signal is compared with the signal from the installed differential pressure generating section, and the difference is compared with a reference voltage, and the trigger circuit controls the conduction of the thyristor to change the amount of electric power supplied to the outside of the motor, thereby controlling the rotation of the blower. The air-fuel ratio is adjusted by controlling the number of fuels. If the reference voltage is 0, the air-fuel ratio is 7th.
As shown in the figure, Rs, Pm, R, the air-fuel ratio becomes constant. That is, for example, when the amount of air is large, the output of the pressure transducer on the air side becomes high, which reduces the amount of electric power supplied to the motor, lowers the rotational speed of the blower, and operates to reduce the amount of air. The air-fuel ratio is determined by the shape of the differential pressure generating section provided on the gas or air side. However, if the reference voltage is kept at a constant positive value, when the combustion amount is small, the amount of combustion air is large, that is, the air-fuel ratio is high, and when the combustion amount is large, the air-fuel ratio approaches the shape determined by the shape of the differential pressure generating part.
The air-fuel ratio can be lowered by setting the differential pressure generating section so that the air-fuel ratio is lower. That is, the characteristics shown by the solid line in FIG. 7 are obtained. B is a normal characteristic, and C is a characteristic adopted in the present invention.
すなわちガス流量の増加に伴ないガス出口圧力が高くな
るように構成する。具体的にはガス出口部にベンチュリ
管を設け、その低圧部の圧力をダイアフラ,ム室7に導
くことによって得られる。第5図のような特性のガス圧
力調節器を使用することにより、大燃焼量時に空燃比が
低くなることは明らかである。以上のように本発明によ
れば次のようなすぐれた効果が期待できるものである。In other words, the configuration is such that the gas outlet pressure increases as the gas flow rate increases. Specifically, this can be obtained by providing a venturi pipe at the gas outlet and guiding the pressure of the low pressure part to the diaphragm chamber 7. It is clear that by using a gas pressure regulator having the characteristics as shown in FIG. 5, the air-fuel ratio becomes low when the combustion amount is large. As described above, according to the present invention, the following excellent effects can be expected.
1 大燃焼量時に空燃比が低いので燃焼空気量が少なく
なり、送風機の必要風量が減少し送風機が小型になる。1. When the combustion volume is large, the air-fuel ratio is low, so the amount of combustion air decreases, the required air volume of the blower decreases, and the blower becomes smaller.
0 大燃焼量時に空燃比が低いので、熱交換効率が高く
なり、同一熱交換効率においては熱交換器を小型にでき
る。m 小燃焼量時に空燃比が高いので、熱効率の過度
の上昇によって結霧を起こすことがなく、熱交換器の腐
蝕を防止できる。0 Since the air-fuel ratio is low when the combustion amount is large, the heat exchange efficiency is high, and the heat exchanger can be made smaller for the same heat exchange efficiency. m Since the air-fuel ratio is high when the combustion amount is small, fog formation does not occur due to an excessive increase in thermal efficiency, and corrosion of the heat exchanger can be prevented.
W 小燃焼量時に空燃比が高いので、第4図に示すよう
に空気ノズル間差圧Pai−Pnoが大きな値となり■
式から明らかなようにガス入口圧力の変動に対して空燃
比の安定性が高い。W Since the air-fuel ratio is high when the combustion amount is small, the air nozzle differential pressure Pai-Pno becomes a large value as shown in Figure 4.■
As is clear from the equation, the air-fuel ratio is highly stable against fluctuations in gas inlet pressure.
第1図は従来の空燃比制御の特性を示すグラフ、第2図
は本発明の空燃比制御の特性を示すグラフ、第3図は本
発明の実施例を示す断面図、第4図は本発明の燃焼量と
空気ノズル間差圧との関係を示したグラフ、第5図は本
発明の他の実施例であるガス圧力調節器の特性を示すグ
ラフ、第6図は本発明の他の実施例を示すブロック線図
、第7図は空燃比の特性を示すグラフである。
1・・・・・・空気ノズル、2・・・・・・差圧発生部
、3・・・・・・ガス量制御装置(ガス圧力調節器)、
8・・・・・・高圧部、12・・・・・・低圧部、16
・・・・・・ガスノズル。
第1図第2図
第3図
第4図
第5図
第6図
第7図Fig. 1 is a graph showing the characteristics of conventional air-fuel ratio control, Fig. 2 is a graph showing the characteristics of the air-fuel ratio control of the present invention, Fig. 3 is a sectional view showing an embodiment of the present invention, and Fig. 4 is a graph showing the characteristics of the air-fuel ratio control of the present invention. A graph showing the relationship between the combustion amount and the differential pressure between air nozzles according to the invention, FIG. 5 is a graph showing the characteristics of a gas pressure regulator according to another embodiment of the invention, and FIG. A block diagram showing the embodiment, FIG. 7 is a graph showing air-fuel ratio characteristics. 1...Air nozzle, 2...Differential pressure generating section, 3...Gas amount control device (gas pressure regulator),
8...High pressure part, 12...Low pressure part, 16
...Gas nozzle. Figure 1 Figure 2 Figure 3 Figure 4 Figure 5 Figure 6 Figure 7
Claims (1)
熱交換器と、燃焼用空気を供給する送風機と、燃焼用空
気量に応動してガス燃料を調節するガス量制御装置もし
くはガス量に応動して燃焼用空気量を調節する風量制御
装置とを有し、燃焼量が大のとき空燃比を低く、燃焼量
が小のとき空燃比を高くした強制給排気型燃焼装置。 2 燃焼用空気通風路中に差圧発生部を設け、この差圧
発生部の抵圧部にガスノズルを設け、上記差圧発生部の
高圧部の圧力をガス量制御装置に導通し、ガス量制御装
置の出口圧力を差圧発生部の高圧部の圧力よりも低く設
定した特許請求の範囲第1項記載の強制給排気型燃焼装
置。 3 ガス量制御装置の出口圧力と空気ノズル高圧部圧力
との差圧を燃焼量の増加に伴なって大きくする特許請求
の範囲第1項記載の強制給排気型燃焼装置。[Claims] 1. A burner, a heat exchanger that exchanges heat with combustion gas from the burner, a blower that supplies combustion air, and a gas amount control that adjusts gas fuel in response to the amount of combustion air. Forced supply/exhaust combustion that has a device or an airflow control device that adjusts the amount of combustion air in response to the amount of gas, and lowers the air-fuel ratio when the amount of combustion is large, and increases the air-fuel ratio when the amount of combustion is small. Device. 2. A differential pressure generating section is provided in the combustion air ventilation path, a gas nozzle is provided in the resistance pressure section of the differential pressure generating section, and the pressure of the high pressure section of the differential pressure generating section is conducted to the gas amount control device to control the gas amount. 2. The forced air supply/exhaust type combustion apparatus according to claim 1, wherein the outlet pressure of the control device is set lower than the pressure of the high pressure section of the differential pressure generating section. 3. The forced air supply/exhaust type combustion device according to claim 1, wherein the pressure difference between the outlet pressure of the gas amount control device and the air nozzle high pressure portion pressure is increased as the combustion amount increases.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5490877A JPS6014974B2 (en) | 1977-05-12 | 1977-05-12 | Forced supply/exhaust type combustion device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5490877A JPS6014974B2 (en) | 1977-05-12 | 1977-05-12 | Forced supply/exhaust type combustion device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS53139236A JPS53139236A (en) | 1978-12-05 |
| JPS6014974B2 true JPS6014974B2 (en) | 1985-04-17 |
Family
ID=12983690
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5490877A Expired JPS6014974B2 (en) | 1977-05-12 | 1977-05-12 | Forced supply/exhaust type combustion device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6014974B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61120576U (en) * | 1985-01-17 | 1986-07-30 |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59229112A (en) * | 1983-06-08 | 1984-12-22 | Osaka Gas Co Ltd | Premixture combustion device |
| JP7718183B2 (en) * | 2021-08-31 | 2025-08-05 | 三浦工業株式会社 | boiler |
-
1977
- 1977-05-12 JP JP5490877A patent/JPS6014974B2/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61120576U (en) * | 1985-01-17 | 1986-07-30 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS53139236A (en) | 1978-12-05 |
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