JPS59161609A - Liquid fuel evaporating device - Google Patents
Liquid fuel evaporating deviceInfo
- Publication number
- JPS59161609A JPS59161609A JP3478583A JP3478583A JPS59161609A JP S59161609 A JPS59161609 A JP S59161609A JP 3478583 A JP3478583 A JP 3478583A JP 3478583 A JP3478583 A JP 3478583A JP S59161609 A JPS59161609 A JP S59161609A
- Authority
- JP
- Japan
- Prior art keywords
- liquid fuel
- fuel
- temperature
- metal
- evaporation
- 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.)
- Pending
Links
Abstract
Description
【発明の詳細な説明】 本発明は液体燃料気化装置に関する。[Detailed description of the invention] The present invention relates to a liquid fuel vaporization device.
従来のこの独の装置には、例えは実開昭55−1627
24号公報に開示されているようなものがあり、当該公
報に開示された装置は第1図に示されている、そして、
第2図には、前記従来の気化装置における気化器が示さ
れている。これら従来の気化装置を示す第1図および第
2図において、1は通気性物質、2は電熱ヒータ、3は
外壁筒体、4は内壁m)体、および5は燃料送油管を示
している。For example, the conventional German device is
There is a device such as that disclosed in Publication No. 24, and the device disclosed in the publication is shown in FIG.
FIG. 2 shows a vaporizer in the conventional vaporizer. In FIGS. 1 and 2 showing these conventional vaporizers, 1 is a breathable material, 2 is an electric heater, 3 is an outer wall cylinder, 4 is an inner wall body, and 5 is a fuel oil pipe. .
このように構成された従来の気化装置では、液体燃料と
して灯油を例とした場合、予め電熱ヒータ2により約2
50℃前後(灯油の核沸ルヶ温度)に調整された気化室
内に送油管を通って灯油が気化至内に注入供給てれ、で
きるだけ短時間に灯油が気化されるようにされていた。In the conventional vaporizer configured in this way, when kerosene is used as the liquid fuel, the electric heater 2 is used to preheat about 2
Kerosene was injected into the vaporization chamber through an oil pipe into the vaporization chamber, which was adjusted to around 50°C (kerosene's nucleate boiling temperature), so that the kerosene would be vaporized in as short a time as possible.
し〃・しながら、側床のこのような加熱気化式石油燃焼
装置では、気化温度が液体燃料の核沸騰温屓頴域温K(
約150〜280℃)であp、気化温贋内での分子の重
合、又は微少残留物(不純物)などの堆積によシ徐々に
タール化し、このタール量は燃焼時間の経過と共に増大
する。加熱気化面又は気化室内にこのタールが堆積した
場合は、気化の時間的変動(脈りが大きくなる。また、
気化燃料ガスの流通路にタールが堆積しfC場合は、バ
ーナ一部への気化燃料ガスの流入が阻害される。However, in such heating vaporization type oil combustion equipment on the side floor, the vaporization temperature is lower than the nucleate boiling temperature range temperature K (
(approximately 150 to 280°C), it gradually turns into tar due to polymerization of molecules within the vaporization temperature or the accumulation of minute residues (impurities), and the amount of tar increases with the passage of combustion time. If this tar accumulates on the heating vaporization surface or in the vaporization chamber, temporal fluctuations in vaporization (pulsations become large.
If tar accumulates in the flow path of the vaporized fuel gas and if fC occurs, the inflow of the vaporized fuel gas into a part of the burner is inhibited.
いずれの場所にタールが堆積しても安定な燃焼は阻害さ
れ、やがては使用不能となる欠点があシ寿命的な問題が
あった。If tar accumulates anywhere, stable combustion will be inhibited, and the product will eventually become unusable, resulting in problems with the service life of the product.
従って、本発明の目的は、刀・がる従来の欠点を改善す
るものであって、気化の時間的変動(脈動)を無くして
安定した燃焼を連続的に持続し、更に気化時にづb生す
るタールの生成量を犬11届に該受さぜる液体燃料気化
装置を提供することにある。Therefore, an object of the present invention is to improve the shortcomings of the conventional swords, and to eliminate temporal fluctuations (pulsations) in vaporization, continuously maintain stable combustion, and further improve b production during vaporization. An object of the present invention is to provide a liquid fuel vaporization device that reduces the amount of tar generated.
以下、本発明の液体燃料気化装置を冷付図面に示された
好適な実施例を参照して更に詳A’illに説明する。DESCRIPTION OF THE PREFERRED EMBODIMENTS The liquid fuel vaporization apparatus of the present invention will be explained in more detail below with reference to preferred embodiments shown in the cooling drawings.
第3図には本発明の液体燃料気化装置の一実施例が示さ
れている。この第3図において、10は気化器、11は
該気化器10の内部に形成された気化室、12は該気化
室11の底部を構成する金属板、13は該金属板の下側
に配置された電熱ヒータ、14は前記金属板上に密着し
て載置された金属多孔体、15は前記金属板内に挿入配
置された温度調歪用センサー、16は前記気化室11を
区画する側壁を部分的に側方外向きに突出させ、その先
端部に開口を形成して成る気化ガス吐出ノベル、17は
バーナ一部、18は前記気化ガス吐出ノズル16に対面
し且つ該ノズルと間隔をあけて配置された前記″バーナ
一部の空気取入れ口、19は一端を気化室11内に位置
し他端を燃料タンク20内に位置した液体燃料送油管、
21は該液体燃料送油骨19の気化室11内に位置する
前記一端たる液体燃料部下ノズル、22は前記液体燃料
送油管19に設けられたポンプ、23は燃料タンク20
内に収容された例えば灯油などの燃料をそnぞれ示して
いる。FIG. 3 shows an embodiment of the liquid fuel vaporization device of the present invention. In FIG. 3, 10 is a vaporizer, 11 is a vaporization chamber formed inside the vaporizer 10, 12 is a metal plate forming the bottom of the vaporization chamber 11, and 13 is arranged below the metal plate. 14 is a metal porous body placed in close contact with the metal plate; 15 is a temperature adjustment strain sensor inserted into the metal plate; 16 is a side wall that partitions the vaporization chamber 11; 17 is a part of the burner, and 18 is facing the vaporized gas discharge nozzle 16 and is spaced apart from the nozzle. an air intake port for a portion of the burner 19 which is open and arranged; a liquid fuel oil pipe 19 having one end located in the vaporization chamber 11 and the other end located in the fuel tank 20;
Reference numeral 21 indicates a lower liquid fuel nozzle which is one end of the liquid fuel supply pipe 19 and is located in the vaporization chamber 11 of the liquid fuel supply pipe 19. Reference numeral 22 indicates a pump provided on the liquid fuel supply pipe 19. Reference numeral 23 indicates a fuel tank 20.
The fuel, for example kerosene, contained therein is shown in each case.
前述した液体燃料送油管19の液体燃料部下、イズル2
1は、第3図から明らかなように、金属板12上の金属
多孔体14の表面に対して垂直に向けられておシ、その
端部は斜めに切断されて形成され、その端面先端縁が前
記金属多孔体14上に点接触されている。The liquid fuel lower part of the liquid fuel oil supply pipe 19 mentioned above, Izuru 2
As is clear from FIG. 3, 1 is oriented perpendicularly to the surface of the metal porous body 14 on the metal plate 12, and its end is cut obliquely, and the tip edge of the end face is is in point contact on the metal porous body 14.
このように構成された液体燃、科気化装置を灯油を例に
してその動作を説明すると、予め電熱ヒータ13に通電
することにょシ、金籾板12および金、属多孔体14が
液体燃料の膜沸騰領域温度(灯油の場合約280℃〜最
高350℃)まで加熱される。To explain the operation of the liquid fuel/fuel vaporizer constructed in this manner using kerosene as an example, the electric heater 13 is energized in advance, and the metal rice plate 12 and the metal/metal porous body 14 are exposed to the liquid fuel. It is heated to the film boiling region temperature (approximately 280° C. to maximum 350° C. for kerosene).
次いで、ポンプ22により液体燃料送油g19を介して
液体燃料部下ノズル21よp液体燃料が加熱金属板表面
14上に滴下注入される。金属多孔体14の液体燃料と
の接触部は、ン薗下液体燃料により局部的に温度低下を
起すが、?画工燃料は短時間に気化してしまい、気化後
における散体燃料と接触した釡慮多孔体の局部は連やか
に初期の設定温度に回1反し、連続的な安定気化が行な
われる。。Next, the liquid fuel is dripped onto the heating metal plate surface 14 from the liquid fuel lower nozzle 21 via the liquid fuel feed g19 by the pump 22. The temperature of the porous metal body 14 in contact with the liquid fuel locally decreases due to the liquid fuel, but? The artist's fuel is vaporized in a short time, and the local part of the porous body that has come into contact with the dispersed fuel after vaporization returns to the initially set temperature one after another, resulting in continuous and stable vaporization. .
史に、気化時に生成したタール分(尚沸点残留vD)は
局部的な液体燃料との接触部の温度回俊に伴ない篩部度
域気化が行なわれ、kL#:的には設定温度の最高温度
(例として350℃)の気化が実施できる。Historically, the tar generated during vaporization (residual boiling point vD) was vaporized in the sieve temperature range as the temperature at the contact area with the liquid fuel locally increased. Vaporization at maximum temperatures (eg 350° C.) can be carried out.
なお、前述した装置では、金属板即ち加熱金属板上に多
孔体金属を密着して載直し、液体燃料の高温安定気化を
可能としたが、密着させる物質としては、多孔体金属以
外に金網又は加熱金属板表面の凸凹表面加工などによっ
てもよい。In the above-mentioned device, the porous metal is placed tightly on the metal plate, that is, the heated metal plate, and stable vaporization of the liquid fuel at a high temperature is made possible. It may also be done by processing the surface of the heated metal plate into irregularities.
lだ、前述の説明では燃料として灯油を例にあげたが、
灯油の気化のみならず、その他の液体燃料にもオリ用で
きることは勿論である。In the above explanation, kerosene was used as an example of fuel, but
Of course, it can be used not only for vaporizing kerosene but also for other liquid fuels.
一本発明は、以上説明したように、気化室内に設けた加
熱金属部に液体燃料を部下注入し、気化室内で気化させ
る場合、液体燃料と接触する加熱金属部表面に液体燃料
と加熱金属′ViVS表面との接触面積を増大させるべ
く加熱金属板上に金属多孔体を載置するか又は加熱金属
板表面そのものを凹凸加工面としたことによシ、液体燃
料加熱金属部を液体燃料の膜沸騰温度領域温度(灯油の
」易合約280℃〜350℃)に加熱して安定気化させ
ることができ、その結果気化時に生成するタールの量を
犬1隅に減少させることができる。As explained above, when liquid fuel is injected downward into the heating metal part provided in the vaporization chamber and vaporized in the vaporization chamber, the liquid fuel and the heating metal ' In order to increase the contact area with the ViVS surface, a porous metal body is placed on the heating metal plate, or the surface of the heating metal plate itself is made into an uneven surface, so that the liquid fuel heating metal part becomes a liquid fuel film. Stable vaporization can be achieved by heating to a temperature in the boiling temperature range (approximately 280°C to 350°C for kerosene), and as a result, the amount of tar produced during vaporization can be reduced to one level.
第1図は従来の液°体燃料気化装置を示す平面図、第2
図は第1図に示された従来の液体燃料気化装置における
気化器を示す断面図、第3図は本発明の液体燃料気化装
置における一実施例を示す断面図である。
10・・・気化器、11・・気化室、12・・・金属板
、13・・・電熱ヒータ、14・・・金属多孔体、19
・・・液体燃料送油管、21・・・液体燃料部下ノズル
。
なお、図中同一符号は同一部分又は相当する部分を示す
。
代理人 葛 野 信 −
第 2 図
41−Figure 1 is a plan view showing a conventional liquid fuel vaporization device;
This figure is a cross-sectional view showing a vaporizer in the conventional liquid fuel vaporizer shown in FIG. 1, and FIG. 3 is a cross-sectional view showing an embodiment of the liquid fuel vaporizer of the present invention. DESCRIPTION OF SYMBOLS 10... Vaporizer, 11... Vaporization chamber, 12... Metal plate, 13... Electric heater, 14... Metal porous body, 19
...Liquid fuel oil supply pipe, 21...Liquid fuel lower nozzle. Note that the same reference numerals in the figures indicate the same or corresponding parts. Agent Shin Kuzuno - Figure 2 41-
Claims (3)
に液体燃料を注入し、気化燃焼させるようにした液体燃
料気化装置において、液体燃料のJ探触する前記金属部
の液体燃料との接触面積を太きくすべく該金属部を金属
多孔体又は凹凸ノ1目工面としたことを特徴とする液体
燃料気化装置。(1) In a liquid fuel vaporizer in which liquid fuel is injected onto a heated metal part using heat such as electric peaks and vaporized and burned, the liquid fuel on the metal part to be probed and A liquid fuel vaporization device characterized in that the metal part is made of a metal porous body or a textured first surface in order to increase the contact area of the metal part.
料気化装置において、?画工燃料と接触するiiJ比金
属部を液体燃料の暎i1.l18ルζ温吸領域温度に加
熱することを持仏とする液体燃料気化装置。(2) Patent N! In the dispersion fuel vaporization device described in item ``Section 1'', ? iiJ ratio metal parts that come into contact with the artist's fuel are mixed with liquid fuel i1. A liquid fuel vaporization device whose purpose is to heat the fuel to a temperature in the thermal absorption region.
化表16において、1)1J記加熱釦ob表面へ数体燃
料をf同下するノズルが糾めに切断され、その端面最下
城がt410已方1k・ン金〃為部六面と点接触するよ
うに設置されていることを待鎮とする液体燃料気化装置
。(3) In the fuel vaporization table 16 described in Section 1 of the request for patent d1-1, 1) the nozzle for discharging several fuels onto the surface of the heating button 1J is sharply cut; A liquid fuel vaporization device whose end face is installed so that the lowest part of the end face is in point contact with the 6th face of the 1k metal part on the t410 side.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3478583A JPS59161609A (en) | 1983-03-03 | 1983-03-03 | Liquid fuel evaporating device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3478583A JPS59161609A (en) | 1983-03-03 | 1983-03-03 | Liquid fuel evaporating device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS59161609A true JPS59161609A (en) | 1984-09-12 |
Family
ID=12423927
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3478583A Pending JPS59161609A (en) | 1983-03-03 | 1983-03-03 | Liquid fuel evaporating device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59161609A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62108911A (en) * | 1985-11-08 | 1987-05-20 | Mitsubishi Electric Corp | Liquid fuel burner |
JPH0325203A (en) * | 1989-06-20 | 1991-02-04 | Mitsubishi Electric Corp | Liquid fuel combustion device |
EP0688587A3 (en) * | 1994-06-21 | 1996-04-10 | Eppendorf Geraetebau Netheler | Process and system for quantitative enrichment of volatile compounds by capillary distillation |
-
1983
- 1983-03-03 JP JP3478583A patent/JPS59161609A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62108911A (en) * | 1985-11-08 | 1987-05-20 | Mitsubishi Electric Corp | Liquid fuel burner |
JPH0478885B2 (en) * | 1985-11-08 | 1992-12-14 | Mitsubishi Electric Corp | |
JPH0325203A (en) * | 1989-06-20 | 1991-02-04 | Mitsubishi Electric Corp | Liquid fuel combustion device |
EP0688587A3 (en) * | 1994-06-21 | 1996-04-10 | Eppendorf Geraetebau Netheler | Process and system for quantitative enrichment of volatile compounds by capillary distillation |
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