JPH0311366B2 - - Google Patents
Info
- Publication number
- JPH0311366B2 JPH0311366B2 JP3081884A JP3081884A JPH0311366B2 JP H0311366 B2 JPH0311366 B2 JP H0311366B2 JP 3081884 A JP3081884 A JP 3081884A JP 3081884 A JP3081884 A JP 3081884A JP H0311366 B2 JPH0311366 B2 JP H0311366B2
- Authority
- JP
- Japan
- Prior art keywords
- combustion
- temperature
- fuel
- amount
- vaporizer
- 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
Links
- 238000002485 combustion reaction Methods 0.000 claims description 53
- 239000000446 fuel Substances 0.000 claims description 48
- 239000006200 vaporizer Substances 0.000 claims description 17
- 239000007788 liquid Substances 0.000 claims description 10
- 238000001514 detection method Methods 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 4
- 238000001704 evaporation Methods 0.000 description 19
- 230000008020 evaporation Effects 0.000 description 19
- 230000008016 vaporization Effects 0.000 description 14
- 238000009834 vaporization Methods 0.000 description 12
- 230000007423 decrease Effects 0.000 description 6
- 239000000567 combustion gas Substances 0.000 description 4
- 230000003111 delayed effect Effects 0.000 description 4
- 235000019645 odor Nutrition 0.000 description 4
- 238000009825 accumulation Methods 0.000 description 3
- 238000009835 boiling Methods 0.000 description 2
- 239000002737 fuel gas Substances 0.000 description 2
- 239000002828 fuel tank Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- 244000171022 Peltophorum pterocarpum Species 0.000 description 1
- 230000002159 abnormal effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000010349 pulsation Effects 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000004071 soot Substances 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
Landscapes
- Control Of Combustion (AREA)
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、気化面を用いて燃料を蒸発させる液
体燃料燃焼装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a liquid fuel combustion device that evaporates fuel using a vaporizing surface.
従来例の構成とその問題点
従来、この種の液体燃料燃焼装置は、気化器の
下部に加熱ヒータを埋設し、この気化器の側壁に
送風フアンに連結した送風通路と先端がノスルを
構成した燃料細管を燃料ポンプと連結して臨ませ
てある。気化器の上部には燃焼筒を設けてある。Conventional configuration and its problems Conventionally, this type of liquid fuel combustion device had a heater embedded in the lower part of the carburetor, and the side wall of the carburetor had a ventilation passage connected to a ventilation fan and the tip formed a nostle. The fuel capillary is connected to the fuel pump and exposed. A combustion tube is provided at the top of the carburetor.
気化器は温度検知器(サーミスタ等)が埋め込
まれ、加熱ヒータをコントロールする。この構成
により、燃焼中、燃焼ガスと、燃焼火炎からの伝
導熱により気化器を加熱される。この加熱量は、
燃焼量の変化と通路、受熱構成により増減する。
また、気化器の温度が十分でない時は、温度検知
器が動作し、加熱ヒータを通電し一定の温度を保
つていた。 A temperature sensor (thermistor, etc.) is embedded in the vaporizer to control the heater. With this configuration, during combustion, the carburetor is heated by the combustion gas and conductive heat from the combustion flame. This heating amount is
It increases or decreases depending on changes in combustion amount, passages, and heat receiving configuration.
Also, when the temperature of the vaporizer was not sufficient, a temperature detector was activated and the heater was energized to maintain a constant temperature.
そのため、燃焼量が増減した場合も、気化器の
壁面は一定の温度に保たれていた。このため、燃
焼量が少ない時、燃料が壁面から受ける気化熱量
が少ないため蒸発過程における燃料温度が高くな
り燃料が玉コロ状となり蒸発速度が遅くなり、燃
空比の時間的みだれを生じ火炎の脈動を生じ、臭
気、矢火を生じた。また、燃焼量が増大した時
は、逆に、燃料量が多いため気化熱量が多くなり
燃料が壁面から多く熱量を吸収するため気化壁面
と燃料の温度勾配が大きくなり、壁面の温度が高
いにもかかわらず、燃料の温度が低く、蒸発遅れ
による燃料だまりや燃料の分解によるタールの発
生を生じた。そのため気化遅れによる燃焼のみだ
れ、未燃ガスの流出、臭気を生じ、タールの発生
は、燃焼のコントロールを不可能とならしめ、矢
火、立炎等危険を生じ、長期間使用できなかつ
た。 Therefore, even when the amount of combustion increased or decreased, the wall surface of the carburetor was kept at a constant temperature. For this reason, when the amount of combustion is small, the amount of heat of vaporization that the fuel receives from the wall surface is small, so the fuel temperature during the evaporation process becomes high, the fuel forms a ball, and the evaporation rate slows down. It produced pulsation, odor, and fire. In addition, when the amount of combustion increases, conversely, because the amount of fuel is large, the amount of heat of vaporization increases, and the fuel absorbs a lot of heat from the wall surface, so the temperature gradient between the vaporization wall surface and the fuel becomes large, and the temperature of the wall surface becomes high. Despite this, the temperature of the fuel was low, resulting in fuel pools due to delayed evaporation and tar generation due to fuel decomposition. As a result, the vaporization was delayed, resulting in sloppy combustion, the outflow of unburned gas, and odor, and the generation of tar, which made it impossible to control the combustion, creating dangers such as flames and standing flames, and making it unusable for a long period of time.
発明の目的
本発明は燃焼の安定と維持を図ることを目的と
する。Purpose of the Invention The purpose of the present invention is to stabilize and maintain combustion.
発明の構成
本発明は燃料の蒸発する気化器の気化器温度検
出手段の設定温度を、液体燃料の多い時は高く、
また少ない時は低く設定温度を変化させることに
より蒸発速度を早くし、気化遅れを生じることな
く燃焼を安定して生じしめるものである。Structure of the Invention The present invention sets the set temperature of the vaporizer temperature detection means of the vaporizer in which the fuel evaporates to be high when there is a large amount of liquid fuel.
Also, when the amount is low, the evaporation rate is increased by changing the set temperature to a low value, thereby stably producing combustion without causing a vaporization delay.
実施例の説明 以下、本発明の一実施例に基づいて説明する。Description of examples Hereinafter, an explanation will be given based on one embodiment of the present invention.
第1図において、有底状の気化器1側面下方部
の円周方向に加熱ヒータ2を埋設し、開放面に絞
り形状を有する混合板3を装着している。さらに
気化器1の側周壁に送風通路4を介して送風フア
ン5を具備するとともに、先端がノズルを構成し
てなる燃料細管6を送風通路4中を通して空気ガ
イド7より気化器1に臨ませ、この燃料細管6の
他端は燃料ポンプ8を介して燃料タンク9に接続
されている。気化器1の上部には、その円周方向
に沿つて、多数の細孔10を有しかつ円筒状に成
形した整流筒11と、この整流筒11の周囲に整
流空間12を介して設けた燃焼金網13からなる
燃焼筒14を設け、この燃焼筒14は閉鎖板15
により上端を閉塞されている。また燃焼筒14の
周囲に閉鎖板15により一端が閉塞された燃焼空
間16を介して外筒17を設け、この外筒17の
他端は支持筒18で覆われ、燃焼ガスはこの支持
筒18に設けられた噴出口21により外部へ流れ
出る通路を構成する。 In FIG. 1, a heater 2 is embedded in the circumferential direction at the lower side of a bottomed vaporizer 1, and a mixing plate 3 having a diaphragm shape is attached to the open surface. Further, a blower fan 5 is provided on the side circumferential wall of the carburetor 1 via a blower passage 4, and a thin fuel tube 6 whose tip constitutes a nozzle is passed through the blower passage 4 to face the carburetor 1 from an air guide 7. The other end of this fuel thin tube 6 is connected to a fuel tank 9 via a fuel pump 8. In the upper part of the vaporizer 1, along the circumferential direction, there is provided a rectifying cylinder 11 having a large number of pores 10 and formed into a cylindrical shape, and a rectifying space 12 provided around the rectifying cylinder 11. A combustion tube 14 made of a combustion wire mesh 13 is provided, and this combustion tube 14 has a closing plate 15.
The upper end is closed by Further, an outer cylinder 17 is provided around the combustion cylinder 14 through a combustion space 16 whose one end is closed by a closing plate 15. The outlet 21 provided in the outlet forms a passageway for flowing out to the outside.
気化器1の壁面19中には、温度を検知する温
度検知器20(サーミスタ等)を埋め込み、加熱
ヒータ2の入切をコントロールする。すなわち、
燃焼量の少ない時は、温度検知器20の動作設定
値を280〜320℃するとともに、燃焼量の増加にし
たがつて上昇させ、燃焼量の多い時は、温度検知
器20の動作設定値を380〜450℃とする。つま
り、温度検知器20の検知した温度と燃焼量が大
の時に高く、小の時に低い設定温度の比較による
出力をうけた制御手段22がヒータ2の入力を制
御するものである。また、燃焼ガスからの気化器
1への受熱量を燃焼火炎からの気化室1への受熱
量より多くなる様に、各構成部品の形状、材質と
通路面積を設定する。 A temperature detector 20 (such as a thermistor) for detecting temperature is embedded in the wall surface 19 of the vaporizer 1 to control whether the heater 2 is turned on or off. That is,
When the amount of combustion is small, the operating setting value of the temperature detector 20 is set to 280 to 320°C, and it is increased as the amount of combustion increases, and when the amount of combustion is large, the operating setting value of the temperature sensor 20 is The temperature shall be 380-450℃. In other words, the control means 22 controls the input to the heater 2 after receiving an output from a comparison between the temperature detected by the temperature detector 20 and the set temperature, which is high when the combustion amount is large and low when it is small. Further, the shape, material, and passage area of each component are set so that the amount of heat received by the vaporizer 1 from the combustion gas is greater than the amount of heat received by the vaporization chamber 1 from the combustion flame.
この構成により、気化器1における加熱ヒータ
2を通電することにより気化器1が加熱される。
この後送風通路4を介して設けられた送風フアン
5を駆動させることにより、気化器1内に空気ガ
イド7から燃焼用空気が送入される。続いて燃料
ポンプ8の駆動により燃料タンク9から燃料が吸
引され、燃料細管6の先端ノズル部より燃料は、
気化器1内に噴出される。噴出した燃料は粒状と
なり気化器1の壁面19に衝突し、高温である壁
面19の熱を受け気化ガスとなり、上部に配した
混合板3の絞り部を通過して、燃焼筒14へ流れ
出る。このとき気化した燃料ガスは、燃焼用空気
と混合され、予混合気として金網を配した燃焼筒
14の周囲から外方向に流出し、外筒17と燃焼
筒14の間の燃焼空間16で点火器(図示せず)
により着火され、燃焼金網13表面にて、燃焼火
炎を形成する。 With this configuration, the vaporizer 1 is heated by energizing the heater 2 in the vaporizer 1.
Thereafter, by driving the blower fan 5 provided through the blower passage 4, combustion air is introduced into the carburetor 1 from the air guide 7. Next, fuel is sucked from the fuel tank 9 by driving the fuel pump 8, and the fuel flows from the tip nozzle of the fuel tube 6.
It is ejected into the vaporizer 1. The ejected fuel becomes granular and collides with the wall surface 19 of the carburetor 1, receives heat from the high-temperature wall surface 19, becomes vaporized gas, passes through the constriction part of the mixing plate 3 disposed above, and flows into the combustion tube 14. At this time, the vaporized fuel gas is mixed with combustion air, flows outward from the periphery of the combustion tube 14 equipped with a wire mesh as a premixture, and is ignited in the combustion space 16 between the outer tube 17 and the combustion tube 14. vessel (not shown)
ignition, and a combustion flame is formed on the surface of the combustion wire mesh 13.
この場合、燃焼空間16より、気化器1側面を
通つて支持筒18に設けられた噴出口より外部へ
拡散する燃焼ガスと、燃焼火炎からの伝導熱によ
り気化器1を加熱される。この加熱熱量は、燃焼
量の変化と通路、受熱構成により増減する。すな
わち、燃焼ガスの温度は、燃焼量の増加にしたが
つて高温となり気化器1の受熱量は増加する。一
方、燃焼火炎からの伝導熱は、燃焼量が増加する
と炎は炎口より遠くなり、炎口付近の温度は低下
する。このため、燃焼量が増加すると気化器1の
受熱量は減少する。そのため、両者の受熱量をコ
ントロールし、燃焼量が少ない時、気化器1の壁
面の温度を300℃程度とし、燃焼量が多い時、気
化器1の壁面の温度を450℃程度となる様に構成
してある。また、燃焼による気化器1への熱のフ
イードバツクが十分でない時は、温度検知器20
が感知し燃焼量に応じた設定値になるまで加熱ヒ
ータ2により温度上昇させる。燃料の燃焼量(燃
料気化量)変化による蒸発速度と気化面温度の傾
向を第2図に示す。燃料の高温壁面による蒸発速
度は壁面温度が上昇するに比例して増加するが、
ある温度になると燃料が玉コロ状となり燃料と壁
面の間に燃料ガスが溜り熱伝達が低下し、蒸発速
度が壁面温度上昇にかかわらず低下する。すなわ
ち核騰沸蒸発から膜騰沸蒸発に移行する。さらに
温度が上昇すると蒸発速度は早くなる。燃料を空
気との比を安定させ、タール生成・蓄積を防止す
る為には気化遅れを生じない蒸発速度のできるだ
け早いことが望ましい。しかし燃料であるため、
あまり高温にすると発火を生じる。第2図から明
らかなように、燃焼量が少ない時は、蒸発熱量が
少ない為、燃料全体の温度上昇が均一に高くな
り、壁面温度が250℃程度で蒸発速度のピークを
示す。また燃焼量が多い時は、逆に、燃料の蒸発
熱量が多いため、燃料の厚さ方向に温度勾配を生
じ、壁面温度も壁中より低くなる。そのため燃料
全体としては、壁面設定温度より低くなるため、
壁面温度が400℃程度で蒸発速度のピークを示す。
これから判るとうり、燃焼量に応じて壁面温度を
上下コントロールすることにより常に蒸発速度の
ピークにて気化を行なわしめることができる。そ
のため燃料はすみやかに蒸発し、気化遅れによる
燃焼みだれ、臭気、スモークを生じなく、タール
の生成・蓄積を防止できる。そして、温度検知器
20を気化器1の燃料が直接当り蒸発する気化面
近くに設けることにより上記設定温度が常に最適
に制御できるものである。また、上記設定温度を
液体燃料の燃焼量の増加に応じて連続的に高く、
また上記減少時は低く設けることにより、負荷に
応じて燃焼量が増減した時も常に設定温度を最も
気化速度の早い温度を維持できるものである。 In this case, the carburetor 1 is heated by the combustion gas that diffuses from the combustion space 16 to the outside through the jet port provided in the support tube 18 through the side surface of the carburetor 1, and by the conductive heat from the combustion flame. The amount of heating heat increases or decreases depending on changes in combustion amount, passages, and heat receiving configuration. That is, the temperature of the combustion gas increases as the amount of combustion increases, and the amount of heat received by the vaporizer 1 increases. On the other hand, as the amount of heat conducted from the combustion flame increases, the flame moves farther away from the flame mouth, and the temperature near the flame mouth decreases. Therefore, as the amount of combustion increases, the amount of heat received by the carburetor 1 decreases. Therefore, by controlling the amount of heat received by both, when the amount of combustion is small, the temperature of the wall surface of the carburetor 1 is set to about 300℃, and when the amount of combustion is large, the temperature of the wall surface of the carburetor 1 is set to about 450℃. It is configured. In addition, when the heat feedback to the vaporizer 1 due to combustion is not sufficient, the temperature sensor 20
is detected and the temperature is raised by the heater 2 until it reaches a set value corresponding to the combustion amount. Figure 2 shows trends in evaporation rate and vaporization surface temperature due to changes in fuel combustion amount (fuel vaporization amount). The evaporation rate of fuel on the high-temperature wall surface increases in proportion to the rise in wall temperature;
When a certain temperature is reached, the fuel forms a ball and fuel gas accumulates between the fuel and the wall, reducing heat transfer and reducing the evaporation rate regardless of the rise in wall temperature. That is, there is a transition from nuclear boiling evaporation to film boiling evaporation. As the temperature further increases, the rate of evaporation increases. In order to stabilize the ratio of fuel to air and prevent tar formation and accumulation, it is desirable that the evaporation rate be as fast as possible without causing any evaporation delay. However, since it is a fuel,
Excessively high temperatures may cause ignition. As is clear from Fig. 2, when the amount of combustion is small, the amount of heat of evaporation is small, so the temperature rise of the entire fuel is uniformly high, and the evaporation rate peaks when the wall surface temperature is around 250°C. Conversely, when the amount of combustion is large, the amount of heat of vaporization of the fuel is large, so a temperature gradient occurs in the thickness direction of the fuel, and the wall surface temperature becomes lower than the inside of the wall. Therefore, the overall temperature of the fuel will be lower than the wall surface temperature,
The evaporation rate peaks when the wall temperature is around 400℃.
As can be seen from this, by controlling the wall surface temperature up and down according to the amount of combustion, vaporization can always be carried out at the peak of the evaporation rate. As a result, the fuel evaporates quickly, eliminating the generation of combustion drips, odors, and smoke due to delayed evaporation, and preventing the generation and accumulation of tar. By providing the temperature sensor 20 near the vaporizing surface of the vaporizer 1 where the fuel directly hits and evaporates, the set temperature can always be optimally controlled. In addition, the above set temperature is continuously increased in accordance with the increase in the amount of liquid fuel burned.
Further, by setting the temperature at a low value when the temperature decreases, the set temperature can always be maintained at the temperature at which the vaporization rate is the fastest even when the combustion amount increases or decreases depending on the load.
発明の効果
本発明は燃料の蒸発する気化器の温度検知手段
の設定値を液体燃料の多い時は高く設定し、液体
燃料の少ない時は低く設定することにより、蒸発
速度を早くでき、燃空比の乱れによる異常燃焼
(ススの発生、黄炎の立炎、臭気)を生じること
なく、また気化遅れによるタール生成蓄積による
失火、燃料溜り等を発生することなく長く使用可
能となるものである。さらに、燃焼の安定化は、
燃焼量可変輻を拡大可能となり負荷に対する制御
性が向上し、快適性、省エネルギ性が高められ
る。Effects of the Invention The present invention increases the evaporation rate by setting the temperature detection means of the fuel vaporizer high when there is a lot of liquid fuel and low when there is little liquid fuel. It can be used for a long time without causing abnormal combustion (soot generation, standing yellow flame, odor) due to imbalance in the ratio, and without misfires or fuel stagnation caused by accumulation of tar generated due to delayed vaporization. . Furthermore, the stabilization of combustion is
It is possible to expand the variable combustion rate, improving load controllability and increasing comfort and energy savings.
第1図は本発明の一実施例を示す断面図、第2
図は燃料の蒸発速度を示す図である。
1……気化器、2……加熱ヒータ、5……送風
フアン、8……燃料ポンプ、14……燃焼筒、2
0……温度検知器。
FIG. 1 is a cross-sectional view showing one embodiment of the present invention, and FIG.
The figure shows the evaporation rate of fuel. 1... Carburizer, 2... Heater, 5... Blowing fan, 8... Fuel pump, 14... Combustion tube, 2
0...Temperature detector.
Claims (1)
気化器温度検知手段を有する気化器を燃焼部に連
結するとともに、上記温度検知手段の検知出力と
設定温度を比較して上記加熱手段の入力を制御す
る制御手段を設け、上記設定温度を上記液体燃料
の多い時は高く設定し、上記液体燃料の少ない時
は低く設定した液体燃料燃焼装置。1. A vaporizer having a means for supplying liquid fuel and air, a heating means, and a vaporizer temperature detection means is connected to the combustion section, and the detection output of the temperature detection means is compared with a set temperature to determine the input of the heating means. A liquid fuel combustion device comprising a control means for controlling the temperature, and setting the set temperature high when the liquid fuel is large and low when the liquid fuel is small.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59030818A JPS60175918A (en) | 1984-02-21 | 1984-02-21 | liquid fuel combustion equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59030818A JPS60175918A (en) | 1984-02-21 | 1984-02-21 | liquid fuel combustion equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60175918A JPS60175918A (en) | 1985-09-10 |
| JPH0311366B2 true JPH0311366B2 (en) | 1991-02-15 |
Family
ID=12314279
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59030818A Granted JPS60175918A (en) | 1984-02-21 | 1984-02-21 | liquid fuel combustion equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60175918A (en) |
-
1984
- 1984-02-21 JP JP59030818A patent/JPS60175918A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60175918A (en) | 1985-09-10 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EXPY | Cancellation because of completion of term |