JP2008202902A - Hydrogen and oxygen mixed gas mixed combustion burner - Google Patents

Hydrogen and oxygen mixed gas mixed combustion burner Download PDF

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Publication number
JP2008202902A
JP2008202902A JP2007041664A JP2007041664A JP2008202902A JP 2008202902 A JP2008202902 A JP 2008202902A JP 2007041664 A JP2007041664 A JP 2007041664A JP 2007041664 A JP2007041664 A JP 2007041664A JP 2008202902 A JP2008202902 A JP 2008202902A
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hydrogen
burner
oxygen
combustion
boiler
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Tatsuhiro Yasunaga
竜裕 安永
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Abstract

<P>PROBLEM TO BE SOLVED: To burn a toxic gas and substance left unremoved by a conventional burner and generated when burning fossil fuel, and animal and plant oil, by combustion of enhancing gas which is a mixture of nontoxic hydrogen and oxygen at an economical rate at superhigh temperature. <P>SOLUTION: A hydrogen mixed combustion method and a device are characterized by using both of the hydrogen and the oxygen or only the hydrogen provided by a hydrogen generator, as a combustion enhancer, by being supplied to the burner, by arranging the hydrogen generator on the front flow side of a boiler and a water heater. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

本発明は、化石燃料及び動植物性油を燃焼する際に発生する有害物質を水素と酸素を混合したガスを投入することにより高温の火炎を発生させ有害物質を完全燃焼させる方法及びその構造に関するものである。   The present invention relates to a method and a structure for completely burning a harmful substance generated by burning a fossil fuel and animal and vegetable oil with a high temperature flame by introducing a gas mixed with hydrogen and oxygen. It is.

ホテル、旅館、船舶、クリーニング店、病院等では集約した給湯設備を備えており、これらの熱源は重油、灯油等の化石燃料や天然ガスやLPGガス等のボイラーまたは温水器によって水を加熱し温水や蒸気に変えるシステムは図4に示すような装置を用いて行われている。
すなわち、温水や蒸気を発生させるボイラー用バーナに使用される化石燃料は、燃焼時に完全燃焼できず、有害物質である煤塵等を排出してしまう。また、燃焼時に発生し、伝熱面に付着する煤は燃焼効率の低下にもつながり、内部洗浄などのメンテナンス費用もかさんでくる。
メンテナンスを怠ると燃料消費を増大させ、そのために地球温暖化の原因でもある二酸化炭素排出の増大につながる。
Hotels, inns, ships, laundry shops, hospitals, etc. are equipped with centralized hot water supply facilities. These heat sources are heated by using fossil fuels such as heavy oil and kerosene, boilers such as natural gas and LPG gas, or water heaters. The system for converting to steam is performed using an apparatus as shown in FIG.
In other words, fossil fuels used in boiler burners that generate hot water and steam cannot be completely combusted during combustion, and exhaust harmful dust such as dust. In addition, soot generated at the time of combustion and adhering to the heat transfer surface also leads to a decrease in combustion efficiency, which also increases maintenance costs such as internal cleaning.
Neglecting maintenance increases fuel consumption, which leads to an increase in carbon dioxide emissions, which is also the cause of global warming.

本発明は、前記従来のバーナでは取り除くことができなかった化石燃料及び動植物油の燃焼時に発生する有害なガスや物質を超高温かつ無害な水素と酸素を経済的な割合で混合した助燃ガスで燃焼させる。 The present invention is an auxiliary combustion gas in which harmful gases and substances generated during combustion of fossil fuels and animal and vegetable oils, which could not be removed by the conventional burner, are mixed with ultra-high temperature and harmless hydrogen and oxygen at an economical ratio. Burn.

前記目的を達成するための手段としてボイラー及び温水器の前流側に水素発生装置を配置し、これより得られる水素と酸素の両方又は水素だけをバーナに供給し、助燃剤として使用することを特徴とした水素混焼方法である。 As a means for achieving the above object, a hydrogen generator is arranged on the upstream side of the boiler and the water heater, and both hydrogen and oxygen obtained therefrom or only hydrogen is supplied to the burner and used as a combustion aid. This is a characteristic hydrogen co-firing method.

また、第2の解決手段は、ボイラー及び温水器のバーナ中央に主燃料供給ノズルを配置したものにおいて、同ノズルの火炎を取り囲むように形成されたバーナタイル内に同心円状に複数個の水素、酸素供給ノズルを配置する構成としたものである。 In the second solution, a main fuel supply nozzle is arranged at the center of the burner of the boiler and the water heater, and a plurality of hydrogen are concentrically formed in a burner tile formed so as to surround the flame of the nozzle, The oxygen supply nozzle is arranged.

本発明は化石燃料及び動植物性油の主燃料を水素発生装置により製造された水素または水素・酸素混合ガスの高温な火炎により、煤塵、硫黄酸化物、窒素酸化物の削減はもとより、煤の付着が原因で生じる熱効率の低下に伴う燃費の悪化を防止できる。 In the present invention, fossil fuel and animal and vegetable oil main fuel is produced by a hydrogen generator or a high temperature flame of hydrogen / oxygen mixed gas to reduce dust, sulfur oxide, nitrogen oxide, and soot adhesion. It is possible to prevent the deterioration of fuel consumption due to the decrease in thermal efficiency caused by.

本発明は主燃料火炎1の外周部分に発生する有害物質を水素または水素・酸素を混合した助燃ガス2がバーナタイル3を介して噴射することで完全燃焼させるものである。 In the present invention, harmful substances generated in the outer peripheral portion of the main fuel flame 1 are completely burned by injecting through the burner tile 3 an auxiliary combustion gas 2 in which hydrogen or a mixture of hydrogen and oxygen is injected.

助燃ガスとしての水素と酸素の流量、圧力、速度を選択設定することによりさらに燃焼効率の向上を図ることができる。   Combustion efficiency can be further improved by selectively setting the flow rate, pressure, and speed of hydrogen and oxygen as auxiliary combustion gases.

以下、図面に基づいて本発明の実施の形態を説明する。
図1は水素及び酸素混合ガス混合燃焼バーナの全体断面図である。
本発明の一実施の形態に係る発明は、図1に示すように、オイルパイプ19から旋回しながら送り出される主燃料と、アトマイズエアー20から送り出され旋回しながら噴射される空気とが混合して着火し、旋回しながら発火する主燃料火炎1の外周部分にボイラーの前流側に配置した水素発生装置24により得られた水素と酸素もしくは水素だけを水素・酸素混合ガス投入口9から投入し、水素・酸素混合ガスノズル6に送り出され噴射される補助燃料火炎2を燃焼させる。尚、上記説明では、水素酸素混合ガスを使用する場合について説明したが、水素ガスのみ噴出し、酸素は別に供給することもできる。
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
FIG. 1 is an overall cross-sectional view of a hydrogen and oxygen mixed gas mixed combustion burner.
As shown in FIG. 1, the invention according to an embodiment of the present invention is a mixture of main fuel that is sent while turning from an oil pipe 19 and air that is sent from atomized air 20 and injected while turning. Hydrogen and oxygen or only hydrogen obtained by the hydrogen generator 24 arranged on the upstream side of the boiler is introduced from the hydrogen / oxygen mixed gas inlet 9 to the outer peripheral portion of the main fuel flame 1 that is ignited and ignites while turning. Then, the auxiliary fuel flame 2 sent out and injected to the hydrogen / oxygen mixed gas nozzle 6 is burned. In the above description, the case of using a hydrogen-oxygen mixed gas has been described. However, only hydrogen gas can be ejected and oxygen can be supplied separately.

その際、従来は主燃料火炎1で燃焼される火炎の有害物質である煤塵は主燃料火炎1の外周部分に飛散しながら排出する。このため、水素・酸素混合ガスノズル5から噴出する補助燃料火炎2を用いて主燃料火炎1を二次燃焼させる。   At that time, soot dust, which is a harmful substance of the flame burned in the main fuel flame 1, is discharged while being scattered on the outer peripheral portion of the main fuel flame 1. For this reason, the main fuel flame 1 is subjected to secondary combustion using the auxiliary fuel flame 2 ejected from the hydrogen / oxygen mixed gas nozzle 5.

水素・酸素混合ガスノズル5に送られる混合ガスは高温のため、冷却水給水口8から送られる冷却水で循環し水素・酸素混合ガスノズル5を冷やし、冷却水排水口17から排出される。   Since the mixed gas sent to the hydrogen / oxygen mixed gas nozzle 5 has a high temperature, it circulates with the cooling water sent from the cooling water supply port 8, cools the hydrogen / oxygen mixed gas nozzle 5, and is discharged from the cooling water drain port 17.

前述したように、主燃料ノズル18から送り出される燃料だけでは効率の良い燃焼ができないため、燃焼空気投入口12から入った燃焼用の空気を燃焼用空気ノズル10から送り出し主燃料火炎1の一次燃焼を補助する。   As described above, since efficient combustion cannot be performed only with the fuel delivered from the main fuel nozzle 18, the combustion air entered from the combustion air inlet 12 is delivered from the combustion air nozzle 10 to perform primary combustion of the main fuel flame 1. To assist.

ここで、主燃料は油などの液体であるので、霧状にして送り出さなくてはならない。このため、アトマイズエアー投入口15から入ったアトマイズエアー20がオイルパイプ19から来る主燃料と交わり霧状となって主燃料ノズル18から噴霧され着火し主燃料火炎1となる。   Here, since the main fuel is a liquid such as oil, it must be sent out in the form of a mist. For this reason, the atomized air 20 entered from the atomized air inlet 15 is mixed with the main fuel coming from the oil pipe 19 to form a mist, sprayed from the main fuel nozzle 18 and ignited to become the main fuel flame 1.

図3は本発明バーナの主な取付方法である。
ボイラー及び温水器本体26にある前板7を介してバーナ取付部分31に従来のバーナ同様取り付ける。
図3に示すボイラーの形式はあくまでも一例であるが、通常、バーナ取付部分31に取り付けたバーナは燃焼炉30で燃焼し、熱交換用オイル27を熱し給水用パイプ28や循環用パイプ29内を通る冷水を熱交換し温める。
FIG. 3 shows the main mounting method of the burner of the present invention.
It is attached to the burner attachment portion 31 through the front plate 7 in the boiler and water heater body 26 in the same manner as a conventional burner.
The boiler type shown in FIG. 3 is merely an example, but normally, the burner attached to the burner attachment portion 31 burns in the combustion furnace 30, heats the heat exchange oil 27, and passes through the water supply pipe 28 and the circulation pipe 29. Heat and exchange the cold water passing through.

図4に示す従来のバーナであれば図3におけるボイラー及び温水器内の燃焼炉30は燃料が完全燃焼できず、有害物質である煤塵が発生し燃焼炉30内の伝熱面に煤が付着し熱効率の低下が起こる。   If the conventional burner shown in FIG. 4 is used, the combustion furnace 30 in the boiler and water heater shown in FIG. 3 cannot completely burn the fuel, soot that is a harmful substance is generated, and soot adheres to the heat transfer surface in the combustion furnace 30. However, a decrease in thermal efficiency occurs.

図5は煤の付着とボイラー効率の変化を示す図である。
新設時には85%以上あったボイラー効率が、わずか0.7ミリ煤が付着しただけで50%以下にまで低下していることがわかる。
FIG. 5 is a diagram showing fouling adhesion and changes in boiler efficiency.
It can be seen that the boiler efficiency, which was 85% or more at the time of new installation, is reduced to 50% or less with only 0.7 milliliters attached.

図6は本発明のバーナを用いた水素及び酸素の混合ガスと重油との混合燃焼時における排ガス試験結果を示す。
測定方法は本発明のバーナを業務用ボイラーに装着し、1時間燃焼させ煙突出口にて計測した結果である。
FIG. 6 shows an exhaust gas test result at the time of mixed combustion of a mixed gas of hydrogen and oxygen and heavy oil using the burner of the present invention.
The measurement method is the result of mounting the burner of the present invention on a commercial boiler, burning it for 1 hour, and measuring at the smoke outlet.

本発明のバーナの全体断面図である。It is a whole sectional view of the burner of the present invention. 本発明図1のア−ア線矢視図である。FIG. 2 is a view taken along the arrow line of FIG. 本発明のバーナをボイラーへ装着した時の全体図断面図である。It is a general view sectional view when the burner of the present invention is attached to a boiler. 従来のバーナの断面図である。It is sectional drawing of the conventional burner. 煤の付着とボイラー効率の変化を示す図である。It is a figure which shows the adhesion | attachment of a soot and the change of boiler efficiency. 本発明のバーナによる排ガス測定結果を示す図である。It is a figure which shows the exhaust gas measurement result by the burner of this invention.

符号の説明Explanation of symbols

1.主燃料火炎
2.補助燃料火炎
3.バーナタイル
4.冷却水循環パイプ
5.水素・酸素混合ガスノズル
6.水素・酸素混合ガス
7.前板
8.冷却水給水口
9.水素・酸素混合ガス投入口
10.燃焼空気ノズル
11.エアーオリフィル押え
12.燃焼空気投入口
13.燃焼空気室
14.アトマイジングボディ
15.アトマイズエアー入口
16.保護板
17.冷却水排水口
18.主燃料ノズル
19.オイルパイプ
20.アトマイズエアー
21.主燃料戻り口
22.主燃料供給口
23.レギュレチングコック
24.水素発生装置
25.バーナ
26.ボイラー及び温水器本体
27.熱交換用オイル
28.給湯用熱交換パイプ
29.循環用熱交換パイプ
30.燃焼炉
31.排ガス出口煙突
1. 1. Main fuel flame 2. Auxiliary fuel flame Burner tile4. 4. Cooling water circulation pipe 5. Hydrogen / oxygen mixed gas nozzle 6. Hydrogen / oxygen mixed gas Front plate 8. Cooling water supply port 9. 9. Hydrogen / oxygen mixed gas inlet 10. Combustion air nozzle 11. Air Orifil presser 12. Combustion air inlet 13. Combustion air chamber 14. Atomizing body15. Atomized air inlet 16. Protection plate 17. Cooling water drain 18. Main fuel nozzle 19. Oil pipe 20. Atomized air 21. Main fuel return port 22. Main fuel supply port 23. Regulating cock 24. Hydrogen generator 25. Burner 26. Boiler and water heater body 27. Oil for heat exchange 28. Heat exchange pipe for hot water supply 29. Heat exchange pipe for circulation 30. Combustion furnace 31. Flue gas outlet chimney

Claims (2)

ボイラー及び温水器の前流側に水素発生装置を配置し、これより得られる水素と酸素の両方又は水素だけをバーナに供給し、助燃剤として使用することを特徴とした水素混焼方法。
A hydrogen co-firing method characterized in that a hydrogen generator is arranged on the upstream side of a boiler and a water heater, and both hydrogen and oxygen obtained therefrom or only hydrogen is supplied to a burner and used as a combustion aid.
ボイラー及び温水器のバーナ中央に主燃料供給ノズルを配置したものにおいて、同ノズルの火炎を取り囲むように形成されたバーナタイル内に同心円状に複数個の水素、酸素供給ノズルを配置したことを特徴とする水素混焼バーナ。   The main fuel supply nozzle is arranged in the center of the burner of the boiler and the water heater, and a plurality of hydrogen and oxygen supply nozzles are concentrically arranged in a burner tile formed so as to surround the flame of the nozzle. The hydrogen co-firing burner.
JP2007041664A 2007-02-22 2007-02-22 Hydrogen and oxygen mixed gas mixed combustion burner Pending JP2008202902A (en)

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JP2007041664A JP2008202902A (en) 2007-02-22 2007-02-22 Hydrogen and oxygen mixed gas mixed combustion burner

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JP2008202902A true JP2008202902A (en) 2008-09-04

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102230632A (en) * 2011-06-03 2011-11-02 王兴文 Flame burning piece of burner part of waste gas burning hot air furnace
KR101267877B1 (en) * 2011-03-17 2013-05-27 한국에너지기술연구원 Co-combustion burner for low-btu gas with oil
CN107120648A (en) * 2017-05-10 2017-09-01 河南省科学院能源研究所有限公司 A kind of high-temperature biomass gas dedicated burner
WO2022076524A1 (en) * 2020-10-06 2022-04-14 Bloom Engineering Company, Inc. Burner and method for hydrogen combustion with enhanced luminosity
CN114689639A (en) * 2022-03-09 2022-07-01 华东理工大学 Hydrogen-mixed gas test system

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101267877B1 (en) * 2011-03-17 2013-05-27 한국에너지기술연구원 Co-combustion burner for low-btu gas with oil
CN102230632A (en) * 2011-06-03 2011-11-02 王兴文 Flame burning piece of burner part of waste gas burning hot air furnace
CN107120648A (en) * 2017-05-10 2017-09-01 河南省科学院能源研究所有限公司 A kind of high-temperature biomass gas dedicated burner
WO2022076524A1 (en) * 2020-10-06 2022-04-14 Bloom Engineering Company, Inc. Burner and method for hydrogen combustion with enhanced luminosity
CN114689639A (en) * 2022-03-09 2022-07-01 华东理工大学 Hydrogen-mixed gas test system

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