JPH01147204A - Liquid-fuel humidifying combustion apparatus - Google Patents
Liquid-fuel humidifying combustion apparatusInfo
- Publication number
- JPH01147204A JPH01147204A JP63215309A JP21530988A JPH01147204A JP H01147204 A JPH01147204 A JP H01147204A JP 63215309 A JP63215309 A JP 63215309A JP 21530988 A JP21530988 A JP 21530988A JP H01147204 A JPH01147204 A JP H01147204A
- Authority
- JP
- Japan
- Prior art keywords
- vaporizer
- air supply
- supply pipe
- combustion
- ultrasonic humidifier
- 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
- 239000000446 fuel Substances 0.000 title claims abstract description 56
- 238000002485 combustion reaction Methods 0.000 title claims abstract description 53
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 41
- 239000006200 vaporizer Substances 0.000 claims abstract description 35
- 239000002245 particle Substances 0.000 claims abstract description 26
- 238000001816 cooling Methods 0.000 claims abstract description 8
- 239000007788 liquid Substances 0.000 claims description 28
- 230000002706 hydrostatic effect Effects 0.000 claims description 19
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 abstract description 17
- 239000007789 gas Substances 0.000 abstract description 7
- 239000004071 soot Substances 0.000 abstract description 7
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical class [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 4
- 150000003467 sulfuric acid derivatives Chemical class 0.000 abstract description 4
- 239000000203 mixture Substances 0.000 abstract 2
- 229910002091 carbon monoxide Inorganic materials 0.000 abstract 1
- -1 i.e. Substances 0.000 abstract 1
- 230000001473 noxious effect Effects 0.000 abstract 1
- 230000010355 oscillation Effects 0.000 abstract 1
- 238000010586 diagram Methods 0.000 description 8
- 238000002347 injection Methods 0.000 description 7
- 239000007924 injection Substances 0.000 description 7
- 239000000839 emulsion Substances 0.000 description 6
- 239000002828 fuel tank Substances 0.000 description 6
- 235000019645 odor Nutrition 0.000 description 5
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 3
- 229910002090 carbon oxide Inorganic materials 0.000 description 3
- 239000010419 fine particle Substances 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 238000004880 explosion Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000013021 overheating Methods 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 238000006116 polymerization reaction Methods 0.000 description 2
- 238000010926 purge Methods 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 230000003213 activating effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 150000004763 sulfides Chemical class 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Landscapes
- Spray-Type Burners (AREA)
- Pressure-Spray And Ultrasonic-Wave- Spray Burners (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は液体燃料を加湿して燃焼させる燃焼装置に係る
もので、詳しくは液化燃料を使用する暖房機の気化器と
燃焼用空気送風機との間に超音波加湿器を設置して燃焼
効率を向上させ、排気ガスに包含された有害成分を除去
し得るようにした液体燃料加湿燃焼装置に関するもので
ある。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a combustion device that humidifies and burns liquid fuel, and specifically relates to a vaporizer and a combustion air blower for a heater that uses liquefied fuel. The present invention relates to a liquid fuel humidification and combustion device in which an ultrasonic humidifier is installed between the exhaust gases to improve combustion efficiency and remove harmful components contained in exhaust gas.
一般に液体燃料の水添加混合燃焼装置は、第4図に示し
たように液体燃料と水とをエマルジョン状態に混合して
燃焼きせる装置(以下、エマルジョン混合燃焼装置と称
す)と、第5図に示したように液体燃料と水とを機械的
に噴射して混合燃焼させる装置(以下、機械的噴射混合
燃焼装置と称す)、並びに第6図に示したように、液体
燃料と水とを機械的に蒸発噴射して混合燃焼させる装置
(以下、機械的蒸発噴射混合燃焼装置と称す)とが用い
られている。In general, a liquid fuel water-added mixing combustion device is a device that mixes liquid fuel and water in an emulsion state and burns it as shown in Fig. 4 (hereinafter referred to as an emulsion mixing combustion device), and a device as shown in Fig. 5. As shown in FIG. A mechanical evaporative injection mixing/combustion device (hereinafter referred to as a mechanical evaporative injection mixing/combustion device) is used.
しかし、このような従来の液体燃料の水添加混合燃焼装
置は次のような欠点があった。However, such a conventional water-added liquid fuel mixing combustion apparatus has the following drawbacks.
〔発明が解決しようとする課題〕
すなわち、従来のエマルジョン混合燃焼装置は主に大型
のボイラーのような産業機械用に適応されていて、第4
図に示したように液体燃料と水とを各々燃料タンク(1
)と水タンク(2)から混合器(3)に供給してエマル
ジョン状態に混合し、そのエマルジョン状態の混合燃料
(M)を空気(A)と混合してバーナー(4)で燃焼さ
せるようになっているため、それらの装置を設置するに
はかなりの空間を必要とすると共に製作及び施設費が高
価になる欠点があった。且つ、液体燃料と水との強い還
元性によりエマルジョン状態が長く維持されず、よって
不完全燃焼になりやすく煤煙が発生する欠点があった。[Problem to be solved by the invention] In other words, the conventional emulsion mixing combustion device is mainly adapted for use in industrial machinery such as large boilers;
As shown in the figure, liquid fuel and water are each stored in a fuel tank (1
) from the water tank (2) to the mixer (3) and mixed into an emulsion state, and the mixed fuel (M) in the emulsion state is mixed with air (A) and burned in the burner (4). Therefore, the installation of these devices requires a considerable amount of space, and the manufacturing and facility costs are high. Furthermore, due to the strong reducing nature of the liquid fuel and water, the emulsion state cannot be maintained for a long time, resulting in incomplete combustion and soot generation.
又、従来の機械的噴射混合燃焼装置は第5図に示したよ
うに、燃料タンク(1)と水タンク (2)から液体燃
料と水とを各々ポンプ(5)(6)により噴射し、その
噴射された燃料(F)と噴射水(W)とを空気(A)と
共に混合してバーナー(4)で燃焼させるようになって
いるため、噴射による騒音がはげしく、且つ、噴射され
た燃料(F)と噴射水(W)との粒子が大きいために完
全燃焼がされない欠点があった。Furthermore, as shown in Fig. 5, the conventional mechanical injection mixing combustion device injects liquid fuel and water from a fuel tank (1) and a water tank (2) using pumps (5) and (6), respectively. Since the injected fuel (F) and the injected water (W) are mixed with air (A) and burned in the burner (4), the noise caused by the injection is loud and the injected fuel There was a drawback that complete combustion could not be achieved because the particles of (F) and injected water (W) were large.
更に、従来の機械的蒸発噴射混合燃焼装置は第6図に示
したように、燃料タンク(1)と水タンク(2)から蒸
発器(7)(8)により各々蒸発されて各ポンプ(9)
(10)により噴射され、空気(A)と混合されてバ
ーナー(4)に送られて燃焼されるようになっているが
、それら燃料と水とを蒸発させるための装置が腐蝕して
破損され易く、よって耐久性が低下し、且つ、蒸発され
ろ水粒子が大きい(20〜50廂程度)ため燃焼効率が
減少して不完全燃焼になり易く、熱量変化による水の供
給量調節がむづかしい欠点があった。Furthermore, as shown in FIG. 6, in the conventional mechanical evaporative injection mixing combustion device, the fuel is evaporated from the fuel tank (1) and the water tank (2) by the evaporators (7) and (8). )
(10), mixed with air (A), sent to burner (4), and burned, but the device for evaporating the fuel and water was corroded and damaged. The drawbacks are that the durability is reduced, and the evaporated water particles are large (approximately 20 to 50 cm), which reduces combustion efficiency and tends to cause incomplete combustion, and that it is difficult to adjust the amount of water supplied due to changes in heat quantity. was there.
このような欠点を解決するため、本発明者達は研究を重
ねた結果次のような液体燃料加湿燃焼装置を提供しよう
とするのである。In order to solve these drawbacks, the inventors of the present invention have conducted extensive research and have attempted to provide the following liquid fuel humidification combustion device.
すなわち、本発明によれば、バーナーが上部に設置され
る気化器と空気を加圧流動させる送風機とを1次空気供
給管に連結し、燃料タンクから供給される液体燃料を前
記気化器に安定に供給する静油面器に前記1次空気供給
管から分岐された加圧管を連結し、前記静油面器から延
設したオリフィスを前記1次空気供給管を通して前記気
化器に連結し、該気化器と前記送風機との間に振動子を
有する超音波加湿器を設置して該超音波加湿器で霧散さ
れる微細な水粒子が空気と共にその気化器に供給されて
燃焼し得るように構成することにより、燃焼効率を増大
すると共に燃料の節約を図り、排気ガス中の有害成分(
窒素酸化物、硫酸化物、−酸化炭素及び煤)の発生を抑
制し、悪臭を顕著に減少させて快適な暖房を図り得るよ
うにしたのである。That is, according to the present invention, a vaporizer in which a burner is installed at the top and a blower that pressurizes and flows air are connected to a primary air supply pipe, and liquid fuel supplied from a fuel tank is stably supplied to the vaporizer. A pressurizing pipe branched from the primary air supply pipe is connected to a hydrostatic level device, and an orifice extending from the hydrostatic level device is connected to the vaporizer through the primary air supply pipe. An ultrasonic humidifier having a vibrator is installed between the vaporizer and the blower, and the fine water particles atomized by the ultrasonic humidifier are supplied to the vaporizer together with air and can be combusted. This increases combustion efficiency, saves fuel, and eliminates harmful components (
This suppresses the generation of nitrogen oxides, sulfates, carbon oxides, and soot, significantly reduces bad odors, and provides comfortable heating.
以下、本発明による実施例を図面を用いて詳細に説明す
るが、本発明は特許請求の範囲をはずれない限り本実施
例に限定されるものでないことは勿論である。Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings, but it goes without saying that the present invention is not limited to these embodiments unless it departs from the scope of the claims.
第1実施例
第1図及び第2図に示したように、バーナー(1)が上
部位に着設された気化器(2)と、空気を加圧して送風
する送風機(3)と、内部に燃料の油面が通常一定に維
持されるように設けられた静油面器(4)とをそれぞれ
具備した液体燃料燃焼装置に於いて、
前記送風器(3)の空気は1次空気供給管(6)を通り
、前記気化器(2)の周囲に形成された冷却筒(7)を
通って前記気化器(2)に導入され、前記1次空気供給
管(6)から一方側に分岐された加圧管(8)を通って
前記静油面器(4)に導入されると共に、他方側に分岐
された連結管(9)を通って超音波加湿器(5)に導入
されるようになっている。1st Embodiment As shown in FIGS. 1 and 2, a vaporizer (2) with a burner (1) installed in the upper part, a blower (3) that pressurizes and blows air, and an internal In a liquid fuel combustion apparatus, the air in the blower (3) is provided as a primary air supply, and a hydrostatic level device (4) provided so that the oil level of the fuel is normally maintained constant. The air is introduced into the vaporizer (2) through a pipe (6), through a cooling tube (7) formed around the vaporizer (2), and from the primary air supply pipe (6) to one side. It is introduced into the hydrostatic level device (4) through a branched pressurizing pipe (8), and into the ultrasonic humidifier (5) through a connecting pipe (9) branched on the other side. It looks like this.
前記静油面器(4)には燃料タンク(20)から燃料を
供給するための燃料供給管(1o)が連結され、その静
油面器(4)の内部には燃料供給電子ポンプ(11)が
設置され、その静油面器(4)から延設したオリフィス
(12)が前記1次空気供給管(6)を通って前記気化
器(2)の内部に露出されている。A fuel supply pipe (1o) for supplying fuel from a fuel tank (20) is connected to the hydrostatic leveler (4), and a fuel supply electronic pump (11) is connected inside the hydrostatic leveler (4). ) is installed, and an orifice (12) extending from the hydrostatic leveler (4) is exposed to the interior of the vaporizer (2) through the primary air supply pipe (6).
前記超音波加湿器(5)には振動子(13)が設けられ
、該振動子(13)の振動により霧散された −微細な
水粒子と空気とが混合されて移動する2次空気供給管(
14)がその超音波加湿器(5)から前記冷却筒(7)
に連結されている。又、前記気化器(2)の周囲には予
熱ヒーター(17)が設置され、その気化器(2)の底
部位にはサーミスタ(18)が設置され、前記バーナー
(1)の上部位には静油板(19)が固設されることに
より、本実施例による液体燃料加湿燃焼装置並びに周辺
の暖房機構が構成されている。The ultrasonic humidifier (5) is provided with a vibrator (13), and the vibration of the vibrator (13) atomizes - A secondary air supply pipe in which fine water particles and air are mixed and moved. (
14) from the ultrasonic humidifier (5) to the cooling cylinder (7)
is connected to. A preheater (17) is installed around the vaporizer (2), a thermistor (18) is installed at the bottom of the vaporizer (2), and a thermistor (18) is installed at the top of the burner (1). By fixing the hydrostatic plate (19), the liquid fuel humidification combustion device and the surrounding heating mechanism according to this embodiment are configured.
図中、未説明符号14′は前記2次空気供給管(14)
下端部位と前記超音波加湿器(5)の振動子(13)側
上部位とに連結される水粒子筒を示し、15は加圧管(
8)に設置されたソレノイド弁を示し、16は気化器(
2)に供給される空気量を調節する空気調節器である。In the figure, an unexplained symbol 14' indicates the secondary air supply pipe (14).
A water particle cylinder is connected to a lower end portion and an upper portion on the vibrator (13) side of the ultrasonic humidifier (5), and 15 is a pressure tube (
8) shows the solenoid valve installed in the carburetor (16).
2) is an air conditioner that adjusts the amount of air supplied to the air conditioner.
このように構成された液体燃料加湿燃焼装置は点火ボタ
ン(図示されていない)を押すと、電気予熱ヒータ(1
7)により前記気化器(2)の温度が230〜240℃
程度に予熱され、この温度がサーミスタ(18)により
検知されて一定温度に維持され、予熱が完了すると送風
機(3)及び燃料供給電子ポンプ(11)が作動するが
この過程をプレパージと称す。このプレパージ過程を約
10〜20秒間行った後、ソレノイド弁(15)と通常
の点火変圧器並びに対流用送風器モーター(図示されて
いない)等が通電されて作動するようになる。When the ignition button (not shown) is pressed, the liquid fuel humidification combustion device configured as described above turns on the electric preheating heater (1
7), the temperature of the vaporizer (2) is 230 to 240°C.
This temperature is detected by the thermistor (18) and maintained at a constant temperature. When the preheating is completed, the blower (3) and fuel supply electronic pump (11) are activated, and this process is called pre-purge. After this pre-purging process has been carried out for about 10-20 seconds, the solenoid valve (15), conventional ignition transformer, convection blower motor (not shown) etc. are energized and activated.
すなわち、電子ポンプ(11)により燃料タンク(20
)から燃料供給管(10)を通って静油面器(4)に供
給された液体燃料はその静油面器(4)で通常一定な油
面に維持され、前記送風機(3)から流入された空気は
加圧管(8)を通って前記静油面器(4)に供給され、
該静油面器(4)内の燃料は加圧されて供給された空気
圧によりオリフィス(12)を通って気化器(2)に送
油される。That is, the fuel tank (20) is pumped by the electronic pump (11).
The liquid fuel supplied from ) to the hydrostatic leveler (4) through the fuel supply pipe (10) is normally maintained at a constant oil level in the hydrostatic leveler (4), and then flows into the hydrostatic leveler (4) from the blower (3). The air is supplied to the hydrostatic level device (4) through a pressurizing pipe (8),
The fuel in the hydrostatic leveler (4) is fed to the carburetor (2) through the orifice (12) by pressurized air pressure.
且つ、送風器(3)から送風される空気の一部は空気調
節器(16)で調節されて1次空気供給管(6)を通っ
て気化器(2)に供給され、オリフィス(12)の一方
端部のノズル(12’)で燃料粒子を微粒子に粉砕して
噴射させる。このように供給される燃料は気化器(2)
の予熱温度約230〜240℃により瞬間的に気化され
て静油板(19)を通過し、バーナー(1)に供給され
て前記1次空気供給管(6)から圧送される空気と混合
して点火放電により燃焼される。In addition, a part of the air blown from the blower (3) is regulated by an air conditioner (16), and is supplied to the vaporizer (2) through the primary air supply pipe (6), and is supplied to the vaporizer (2) through the orifice (12). A nozzle (12') at one end of the pulverizes the fuel particles into fine particles and injects them. The fuel supplied in this way is fed to the carburetor (2)
The air is instantaneously vaporized by the preheating temperature of about 230 to 240°C, passes through the hydrostatic plate (19), is supplied to the burner (1), and mixes with the air that is pressure-fed from the primary air supply pipe (6). It is burned by ignition discharge.
又、前記送風機(3)から超音波加湿器(5)に供給さ
れる空気は2次空気供給管(14)の下端部の水粒子筒
(14’ )を通過しながら振動子(13)により霧化
された10−以下の微細な水粒子と混合され、その2次
空気供給管(14)を通って前記気化器の冷却筒(7)
に供給されて前記気化器(2)の過熱を防止し、バーナ
ー(1)の燃焼を活性化させると共に排気ガス中の有害
成分を抑制させる。且つ、前記振動子(13)を具備し
た加湿器(5)は水位調節弁i図示されていない)によ
り通常一定の水面が維持され、加湿量は燃焼装置の発熱
量及び燃料供給量により調節される。Furthermore, the air supplied from the blower (3) to the ultrasonic humidifier (5) is passed through the water particle tube (14') at the lower end of the secondary air supply pipe (14) and is then cooled by the vibrator (13). It is mixed with atomized fine water particles of 10 or less, and passed through the secondary air supply pipe (14) to the cooling cylinder (7) of the vaporizer.
is supplied to the carburetor (2) to prevent overheating, activate combustion in the burner (1), and suppress harmful components in the exhaust gas. In addition, the humidifier (5) equipped with the vibrator (13) is normally maintained at a constant water level by a water level control valve (not shown), and the amount of humidification is adjusted by the amount of heat generated by the combustion device and the amount of fuel supplied. Ru.
前述の燃焼過程に於いて、超音波加湿器(5)で霧散し
て空気と混合され、2次空気供給管(14)を通ってバ
ーナー(1)に供給される微細な水粒子は次の(1)・
(2)・(3)式のような反応で分解される。In the above-mentioned combustion process, the fine water particles that are atomized by the ultrasonic humidifier (5), mixed with air, and supplied to the burner (1) through the secondary air supply pipe (14) are as follows. (1)・
It is decomposed by the reactions shown in equations (2) and (3).
H20+H−→ I(2+(il+ −−−−−−
−一一−−−−−甲−(1)uzo+o → OH+
011 −−−−−−−−−−−−−−輪−(2)
■2 +0 → □H+ H−−−−−−−−−−−−
−−−(3)そして、OH基の生成を増加させて該OH
基が燃焼の際発生する排気ガスCOと次式(4)のよう
に反応して
Co 十OR−丑 CO□+I+ −−−−−−−
−−−−甲−−(4)COの発生を抑制させる。且つ、
重合反応(polyme−rization)により炭
素の生成を抑制して煤及び臭いを顕著に減少させ、水粒
子の微細爆発に依る燃焼の活性化により完全燃焼を促進
し、硫酸化物(SOX)及びその地下完全燃焼により発
生する汚染物質を減少させる。このように作用される加
湿水添加量は7〜10%で最も好ましくは8%である。H20+H−→ I(2+(il+ −−−−−−
-11------A-(1) uzo+o → OH+
011 ----------------Ring-(2)
■2 +0 → □H+ H−−−−−−−−−−−−
---(3) Then, by increasing the generation of OH groups, the OH
The group reacts with the exhaust gas CO generated during combustion as shown in the following formula (4), resulting in Co
----A--(4) Suppressing the generation of CO. and,
It suppresses the production of carbon through polymerization, significantly reducing soot and odor, and promotes complete combustion by activating combustion through minute explosions of water particles, reducing sulfide (SOX) and its underground Reduces pollutants generated by complete combustion. The amount of humidifying water added that acts in this way is 7 to 10%, and most preferably 8%.
以上説明したように本実施例による液体燃料燃坑装置は
、1次及び2次空気供給管を通って供給される空気と超
音波加湿器により供給される微細な水粒子との混合流入
により燃焼効率が向上して完全燃焼が行われ、排気ガス
中の有害成分(窒素酸化物、硫酸化物、−酸化炭素及び
煤)の発生を抑制し、悪臭を減少させて快適な環境を造
成することができる。As explained above, the liquid fuel combustion equipment according to the present embodiment performs combustion by a mixed inflow of air supplied through the primary and secondary air supply pipes and fine water particles supplied by the ultrasonic humidifier. Efficiency is improved and complete combustion is performed, suppressing the generation of harmful components in exhaust gas (nitrogen oxides, sulfates, carbon oxides and soot), reducing bad odors and creating a comfortable environment. can.
第2実施例
第3図は本発明による第2実施例の液体燃料加湿燃焼装
置を示す系統図で、図面に示したように、送風機(3)
から送風される空気の一部が空気調節器(16)により
調節されて1次空気供給管(6)を通って超音波加湿器
(5)に供給され、振動子(13)により霧散された1
0廂以下の微細な水粒子と混合されてその1次空気供給
管(6)の噴射側(6′)を通って気化器(2)に噴射
され、ノズル(12”)から噴射される液体燃料を微粒
子に粉砕させて霧化させるようになっている。その霧化
された燃料は前記気化器(2)の温度(約230〜24
0℃)により瞬間的に気化されると同時に、空気と共に
供給された微細な水粒子により爆発されて静油板(19
)を通ってバーナー(1)に供給され、点火放電により
点火燃焼される。一方、送風器(3)から送風される空
気の一部は2次空気供給管(14)を通って冷却筒(7
)に供給されて気化器(2)の過熱を防止すると共に燃
焼に必要な2次空気を供給するようになっている。Second Embodiment FIG. 3 is a system diagram showing a liquid fuel humidification combustion apparatus according to a second embodiment of the present invention.
A part of the air blown from the air conditioner (16) is regulated by the air conditioner (16), is supplied to the ultrasonic humidifier (5) through the primary air supply pipe (6), and is atomized by the vibrator (13). 1
Liquid that is mixed with fine water particles of less than 0 feet and injected into the vaporizer (2) through the injection side (6') of the primary air supply pipe (6), and then injected from the nozzle (12''). The fuel is pulverized into fine particles and atomized.The atomized fuel is heated to the temperature of the vaporizer (2) (approximately 230 to 24
At the same time, it is exploded by the fine water particles supplied with the air and becomes an oil hydrostatic plate (19
) is supplied to the burner (1), where it is ignited and burned by an ignition discharge. On the other hand, a part of the air blown from the blower (3) passes through the secondary air supply pipe (14) and passes through the cooling cylinder (7).
) to prevent overheating of the carburetor (2) and to supply secondary air necessary for combustion.
すなわち、1次空気供給管(6)の中間部位に超音波加
湿器(5)を連結し、気化器(2)の冷却筒(7)に連
結される2次空気供給管(14)を前記1次空気供給管
(6)に直接連結し、前記超音波加湿器(5)で霧散さ
れた水粒子がオリフィス(12)に供給される液体燃料
と混合されて前記気化器(2)に供給されるように構成
されている。That is, the ultrasonic humidifier (5) is connected to the middle part of the primary air supply pipe (6), and the secondary air supply pipe (14) connected to the cooling cylinder (7) of the vaporizer (2) is connected to the middle part of the primary air supply pipe (6). Directly connected to the primary air supply pipe (6), water particles atomized by the ultrasonic humidifier (5) are mixed with liquid fuel supplied to the orifice (12) and supplied to the vaporizer (2). is configured to be
よって、前記超音波加湿器(5)で霧散された水粒子が
液体燃料と共に気化器(2)に直接供給されることによ
り燃焼効率が一層向上されて排気ガス中の有害成分が減
少される。Therefore, the water particles atomized by the ultrasonic humidifier (5) are directly supplied to the vaporizer (2) together with the liquid fuel, thereby further improving combustion efficiency and reducing harmful components in the exhaust gas.
それで、前記超音波加湿器(5)で霧散され、前記送風
機(3)から1次空気供給管(6)に供給される空気と
混合して前記気化器(2)に供給されろ水粒子は前記気
化器(2)内で前述の(1)〜(4)式と同様な反応に
よりCOの発生を抑制し、重合反応により炭素の生成を
抑制して煤゛と臭いを顕著に減少させる。又、水粒子の
微細爆発により燃焼が活性化されて完全燃焼を促進し、
硫酸化物(SOX)及び窒素酸化物(NOX)等の汚染
物質の発生を顕著に減少させる。Then, the filtrate particles are atomized by the ultrasonic humidifier (5), mixed with the air supplied from the blower (3) to the primary air supply pipe (6), and supplied to the vaporizer (2). In the vaporizer (2), the generation of CO is suppressed by reactions similar to the above-mentioned equations (1) to (4), and the generation of carbon is suppressed by the polymerization reaction, thereby significantly reducing soot and odor. In addition, combustion is activated by minute explosions of water particles, promoting complete combustion.
Significantly reduces the generation of pollutants such as sulfides (SOX) and nitrogen oxides (NOX).
更に、燃料と共に微細な水粒子を1次空気に混合噴射し
、気化させて燃焼させることにより燃料の液滴中に水の
液滴が包含され、その水の液滴が加熱されて爆発しなが
ら燃料の液滴を微細に爆発させるようになり、微粒子に
なった燃料は空気との接触面積が増大されて燃焼効率は
一層向上される。Furthermore, fine water particles are mixed with the fuel and injected into the primary air, and by vaporizing and burning, water droplets are included in the fuel droplets, and the water droplets are heated and exploded. The fuel droplets are exploded into fine particles, and the contact area of the fuel particles with the air is increased, further improving combustion efficiency.
本実施例による加湿水添加量は10〜30%が好ましく
、20%が最好適である。The amount of humidifying water added in this example is preferably 10 to 30%, most preferably 20%.
以上説明したように、本発明によれば、燃焼用空気送風
機と、燃焼用バーナーとの間に超音波加湿器を設置し、
該超音波加湿器で霧散された微細な水粒子と前記空気送
風機の空気とを混合させてノズルから気化器内に供給し
、気化器内で霧化した燃料の液滴と微細な水粒子が爆発
燃焼されるようになっているため、燃焼効率の向上並び
に有害成分(窒素酸化物、硫酸化物、−酸化炭素及び煤
)の発生を抑制する効果がある。又、燃焼効率の向上と
完全燃焼により燃料費の節約をはかると共に、有害成分
の減少による悪臭を防止して快適な暖房を行い得る効果
がある。As explained above, according to the present invention, an ultrasonic humidifier is installed between the combustion air blower and the combustion burner,
The fine water particles atomized by the ultrasonic humidifier and the air from the air blower are mixed and supplied from the nozzle into the carburetor, where the atomized fuel droplets and fine water particles are mixed. Because it is explosively combusted, it has the effect of improving combustion efficiency and suppressing the generation of harmful components (nitrogen oxides, sulfates, carbon oxides, and soot). In addition, fuel costs can be saved through improved combustion efficiency and complete combustion, and unpleasant odors can be prevented due to the reduction in harmful components, resulting in comfortable heating.
第1図は本発明による第1実施例の液体燃料加湿燃焼装
置の系統図、第2図は、第1図の要部の気化器部の拡大
断面図、第3図は本発明による第2実施例の液体燃料加
湿燃焼装置を示す系統図、第4図乃至第6図は従来液体
燃料の水添加混合燃焼装置を示した図面で、第4図は液
体燃料と水とをエマルジョン状態に混合して燃焼させる
装置の系統図、第5図は液体燃料と水とを機械的に噴射
して混合燃焼させる装置の系統図、第6図は液体燃料と
水とを機械的に蒸発噴射して混合燃焼させる装置の系統
図を示し、
図中、
1:バーナー 2:気化器
゛ 3:送風機 4:静油面器5:超音波加
湿器 6:1次空気供給管7:冷却筒
8:加圧管
9:連結管 12ニオリフイス13:振動子
14:2次空気供給管20:燃料供給タンクFIG. 1 is a system diagram of a liquid fuel humidification combustion apparatus according to a first embodiment of the present invention, FIG. 2 is an enlarged sectional view of the main part of the vaporizer section of FIG. 1, and FIG. A system diagram showing a liquid fuel humidifying combustion device according to an embodiment. FIGS. 4 to 6 are diagrams showing a conventional liquid fuel water-added mixing combustion device. FIG. Fig. 5 is a system diagram of a device that mechanically injects liquid fuel and water to mix and burn it, and Fig. 6 shows a system diagram of a device that mechanically injects liquid fuel and water for evaporative injection. A system diagram of a device for mixed combustion is shown. In the diagram, 1: burner 2: vaporizer 3: blower 4: hydrostatic leveler 5: ultrasonic humidifier 6: primary air supply pipe 7: cooling cylinder
8: Pressure pipe 9: Connecting pipe 12 Niorifice 13: Vibrator 14: Secondary air supply pipe 20: Fuel supply tank
Claims (1)
次空気供給管(6)により送風機(3)に連結され、燃
料供給タンク(20)から供給される液体燃料を前記気
化器(2)に安定に供給するための静油面器(4)を設
置し、該静油面器(4)には前記1次空気供給管(6)
から分岐された加圧管(8)が連結され、その静油面器
(4)から延設されたオリフィス(12)が前記1次空
気供給管(6)の中心を通って前記気化器(2)に連結
された燃料燃焼装置であって、 前記気化器(2)と前記送風機(3)との間に振動子(
13)を有する超音波加湿器(5)を設置して、該超音
波加湿器(5)から霧散された微細な水粒子を前記気化
器(2)に空気と共に供給して燃焼させるように構成す
ることを特徴とする液体燃料加湿燃焼装置。 2、前記1次空気供給管(6)から連結管(9)を分岐
して該連結管(9)を前記超音波加湿器(5)に連結し
、前記気化器(2)の周囲に冷却筒(7)を設置して該
冷却筒(7)と前記超音波加湿器(5)との間に2次空
気供給管(14)を連結することにより霧化した微細な
水粒子と混合された空気をその気化器(2)に供給し得
るようにして成ることを特徴とする特許請求の範囲第1
項記載の液体燃料加湿燃焼装置。 3、前記1次空気供給管(6)の中間部位に前記超音波
加湿器(5)を設置し、その1次空気供給管(6)から
前記2次空気供給管(14)を分岐させて該2次空気供
給管(14)を前記気化器(2)に直接連結して成るこ
とを特徴とする特許請求の範囲第1項記載の液体燃料加
湿燃焼装置。[Claims] 1. The vaporizer (2) with the burner (1) installed on the top is 1.
A hydrostatic level device (4) is connected to the blower (3) by an air supply pipe (6) and is used to stably supply liquid fuel supplied from the fuel supply tank (20) to the vaporizer (2). The primary air supply pipe (6) is installed in the hydrostatic plate (4).
A pressurizing pipe (8) branched from is connected, and an orifice (12) extending from the hydrostatic level device (4) passes through the center of the primary air supply pipe (6) and connects to the vaporizer (2). ), wherein a vibrator (
13) is installed, and the ultrasonic humidifier (5) is configured to supply fine water particles atomized from the ultrasonic humidifier (5) to the vaporizer (2) together with air and burn them. A liquid fuel humidification combustion device characterized by: 2. Branch a connecting pipe (9) from the primary air supply pipe (6), connect the connecting pipe (9) to the ultrasonic humidifier (5), and cool the air around the vaporizer (2). By installing a cylinder (7) and connecting a secondary air supply pipe (14) between the cooling cylinder (7) and the ultrasonic humidifier (5), the air is mixed with atomized fine water particles. Claim 1 characterized in that the air is supplied to the vaporizer (2).
The liquid fuel humidification combustion device described in . 3. Installing the ultrasonic humidifier (5) at an intermediate portion of the primary air supply pipe (6), and branching the secondary air supply pipe (14) from the primary air supply pipe (6). 2. The liquid fuel humidification combustion apparatus according to claim 1, wherein the secondary air supply pipe (14) is directly connected to the vaporizer (2).
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1019870009620A KR900003475B1 (en) | 1987-08-31 | 1987-08-31 | Combustion apparatus adding vapor liquid fuel |
KR9620/1987 | 1987-08-31 | ||
KR12216/1987 | 1987-10-31 | ||
KR1019870012216A KR900001302B1 (en) | 1987-10-31 | 1987-10-31 | Combustion apparatus of fluid fuel adding water vapor |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01147204A true JPH01147204A (en) | 1989-06-08 |
Family
ID=26627745
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63215309A Pending JPH01147204A (en) | 1987-08-31 | 1988-08-31 | Liquid-fuel humidifying combustion apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01147204A (en) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5916650U (en) * | 1982-07-26 | 1984-02-01 | 杉山 紀行 | treatment device |
-
1988
- 1988-08-31 JP JP63215309A patent/JPH01147204A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5916650U (en) * | 1982-07-26 | 1984-02-01 | 杉山 紀行 | treatment device |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US7867324B2 (en) | Fuel system and method of reducing emission | |
CA2449205C (en) | Method and device for low-emission non-catalytic combustion of a liquid fuel | |
JP2008502847A (en) | Reforming non-vaporized atomized hydrocarbon fuel | |
WO1996008643B1 (en) | Method for supplying vaporized fuel oil to a gas turbine combustor and system for same | |
KR20070061325A (en) | Rich catalytic clean burn for liquid fuel with fuel stabilization unit | |
JPH11166705A (en) | Method and apparatus for combusting emulsion of water/ fossil fuel mixture | |
KR0148195B1 (en) | Apparatus and method for decreasing nitrogen oxide emissions from internal combustion power sources | |
JPH01147204A (en) | Liquid-fuel humidifying combustion apparatus | |
KR900003475B1 (en) | Combustion apparatus adding vapor liquid fuel | |
KR900001302B1 (en) | Combustion apparatus of fluid fuel adding water vapor | |
JP2003090227A (en) | Generation plant with heavy oil reformer and its operating method | |
KR20120010581A (en) | Igniting apparatus for boiler emulsion fuel | |
JP2805997B2 (en) | Catalytic combustor | |
JPH0464802A (en) | Liquid fuel burner | |
JP2000319673A (en) | Treating apparatus for waste water by means of emulsion combustion | |
KR900003476B1 (en) | Ultra sonic combustion apparatus | |
JPH08338614A (en) | Liquid fuel vaporization apparatus | |
KR200177774Y1 (en) | An industrial burner using a water and oil as a fuel | |
JPH0439507A (en) | Burner | |
JPH0477201B2 (en) | ||
RU2136942C1 (en) | Method of and system for supply of internal combustion engine and carburetor used in system | |
JPS59147922A (en) | Kerosene gasified burner | |
KR830000915B1 (en) | Combustor for Feeding Mixed Fuels | |
JPH03168505A (en) | Pulse combustion apparatus | |
KR20140046185A (en) | Complete combustion apparatus of a burner using high-temperatureceramic heater |