JPH01266409A - Flame propagating burner - Google Patents
Flame propagating burnerInfo
- Publication number
- JPH01266409A JPH01266409A JP63096469A JP9646988A JPH01266409A JP H01266409 A JPH01266409 A JP H01266409A JP 63096469 A JP63096469 A JP 63096469A JP 9646988 A JP9646988 A JP 9646988A JP H01266409 A JPH01266409 A JP H01266409A
- Authority
- JP
- Japan
- Prior art keywords
- combustion
- ignition
- discharged gas
- gases
- filter
- 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.)
- Granted
Links
- 230000001902 propagating effect Effects 0.000 title abstract 2
- 238000002485 combustion reaction Methods 0.000 claims abstract description 86
- 239000007789 gas Substances 0.000 claims abstract description 63
- 230000001590 oxidative effect Effects 0.000 claims abstract description 7
- 231100000614 poison Toxicity 0.000 claims abstract 3
- 230000007096 poisonous effect Effects 0.000 claims abstract 3
- 230000003647 oxidation Effects 0.000 claims description 37
- 238000007254 oxidation reaction Methods 0.000 claims description 37
- 230000004913 activation Effects 0.000 claims description 8
- 238000010438 heat treatment Methods 0.000 claims description 7
- 239000000446 fuel Substances 0.000 claims 1
- 239000000126 substance Substances 0.000 claims 1
- 239000000203 mixture Substances 0.000 abstract description 5
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 3
- 229910002091 carbon monoxide Inorganic materials 0.000 abstract description 3
- 238000007599 discharging Methods 0.000 abstract 3
- 239000002341 toxic gas Substances 0.000 description 15
- 238000002156 mixing Methods 0.000 description 5
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 4
- 238000011144 upstream manufacturing Methods 0.000 description 4
- 238000009841 combustion method Methods 0.000 description 3
- 238000005260 corrosion Methods 0.000 description 3
- 230000007797 corrosion Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000003054 catalyst Substances 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 2
- 230000001877 deodorizing effect Effects 0.000 description 2
- 229910052697 platinum Inorganic materials 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- 230000003213 activating effect Effects 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 229910052878 cordierite Inorganic materials 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- JSKIRARMQDRGJZ-UHFFFAOYSA-N dimagnesium dioxido-bis[(1-oxido-3-oxo-2,4,6,8,9-pentaoxa-1,3-disila-5,7-dialuminabicyclo[3.3.1]nonan-7-yl)oxy]silane Chemical compound [Mg++].[Mg++].[O-][Si]([O-])(O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2)O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2 JSKIRARMQDRGJZ-UHFFFAOYSA-N 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 229910001120 nichrome Inorganic materials 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 231100000572 poisoning Toxicity 0.000 description 1
- 230000000607 poisoning effect Effects 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Landscapes
- Combustion Of Fluid Fuel (AREA)
- Fluidized-Bed Combustion And Resonant Combustion (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
この発明は、直管状燃焼室内を給気及び排気、点火、燃
焼、消火のサイクルを連続的に(9返しその火炎面か伝
播する燃焼方式の伝播燃焼装置に関する。[Detailed Description of the Invention] [Field of Industrial Application] This invention is a combustion method in which a cycle of air supply, exhaust, ignition, combustion, and extinguishing is carried out continuously (9 times) in a straight-tubular combustion chamber, and the flame front propagates through the cycle. The present invention relates to a propagation combustion device.
従来のこの棟の伝播燃焼装置は、九とえは、第9図に示
さnているように、直管状燃焼室(17の基亀消火部位
(B)’に消火時における火炎流の流速を急激に変化さ
せる友めの狭窄部(57を設けその前流側に混合室(6
7を連設するとともに−先鴫点火部位Wには点火用ヒー
タ(27を臨設ゼしめ、該点火用ヒータ(27の後流側
に排気管(77を直管状燃焼室(1rと連通して設け、
基端混合室(6Fにガスノズル(87を周一に一次空気
取入口(9Fを存して臨ませた構造となっている。The conventional propagation combustion device of this building has a straight pipe combustion chamber (17 base extinguishing part (B)') that controls the flow velocity of the flame flow during extinguishing, as shown in Fig. 9. A companion constriction section (57) is provided for rapid changes, and a mixing chamber (6
At the same time, an ignition heater (27) is provided at the tip ignition site W, and an exhaust pipe (77 is connected to the straight combustion chamber (1r) on the downstream side of the ignition heater (27). established,
It has a structure in which a gas nozzle (87) is located on the base end mixing chamber (6F) and a primary air intake port (9F) is exposed around the circumference.
伝播燃焼装置は、直管状燃焼室内を給気及び排気、点火
、燃焼、消火のサイクルを連続的にくり返し/サイクル
ごとにその火炎面が伝陥する燃焼方式であるため、直管
状燃焼室(1グの先端点火部位Wと基宿消火部位出rの
両廟部に点火時及び消火時に極く少量ではあるが未燃ガ
スが残留することがあり、また、火炎温度の低下による
不完全燃焼が起因する生成物等も残留する。しかし、上
記従来の伝播燃焼装置では、残留未燃〃ヌ等の処理対策
が何ら採られていない丸め排気管(7γから器外へ放出
さnる燃焼排気ガス中に未燃ガス等の有毒ガスか含有す
るという問題があった。The propagation combustion device uses a combustion method in which the cycle of supplying and exhausting air, ignition, combustion, and extinguishing is continuously repeated in the straight-tubular combustion chamber, and the flame front propagates in each cycle. During ignition and extinguishing, a very small amount of unburned gas may remain in both the ignition point W at the tip of the fire extinguisher and the extinguishing point R at the base fire extinguishing point, and incomplete combustion may occur due to a drop in flame temperature. However, in the conventional propagation combustion equipment mentioned above, no measures are taken to deal with residual unburnt gas, etc. There was a problem that it contained toxic gases such as unburned gas.
この発明は、がかる問題点に鑑み、燃焼排気ガス中に含
有する未燃ガス等の有毒ガスを酸化フィルタで酸化除去
せしめることによって排気のクリーン化を図った伝播燃
焼装置の提供を目的としている。In view of this problem, the present invention aims to provide a propagation combustion device that cleans exhaust gas by oxidizing and removing toxic gases such as unburned gas contained in combustion exhaust gas using an oxidation filter.
上記目的を達成する之めに、この発明による伝播燃焼装
置は、直管状燃焼室内を給気及び排気、点火、燃焼、消
火のサイクルを連続的にくり返しその火炎面が伝播する
燃焼方式の伝播燃焼装置において、該直管状燃焼室の先
端点火部位に備え九二クローム線等の点火源の後流側に
耐熱、耐蝕性をもつセラミックヌフオーム等の担体に白
金等の触媒を担持させた部材等よシなる酸化フィルタを
設けて、燃焼排気ガスが該酸化フィルタを通過すること
により該燃焼排気ガス中に含有する未燃ガス等の有毒ガ
スを酸化処理して除去せしめて排出するようにしたもの
である。In order to achieve the above object, the propagation combustion device according to the present invention employs propagation combustion, a combustion method in which the cycle of air supply and exhaust, ignition, combustion, and extinguishing is continuously repeated in a straight-tubular combustion chamber, and the flame front propagates. In the device, a member, etc., in which a catalyst such as platinum is supported on a heat-resistant and corrosion-resistant carrier such as ceramic nuforme, etc., is provided at the tip ignition part of the straight tube-shaped combustion chamber and is placed downstream of an ignition source such as a 92 chrome wire. The combustion exhaust gas is equipped with a good oxidation filter, and the combustion exhaust gas passes through the oxidation filter to oxidize and remove toxic gases such as unburned gases contained in the combustion exhaust gas before being discharged. It is.
また、請求項2は酸化フィルタの近傍に該酸化フィルタ
をその活性化に必要な程度に加熱するアフタバーナを設
けて、該アフタバーナで酸化フィルタをその活性化に最
適な温度に迅速確実に加熱せしめることによって未燃ガ
ス等の有毒ガスの酸化処理がより効率的に行いつるよう
にしたものである。なお−アフタバーナによる酸化フィ
ルタの加熱温度が高すぎるとその活性化ができず、また
、酸化フィルタの焼損も著しく、加熱温度が低すぎても
その活性化ができない。したがって、酸化フィルタの活
性化に最適な加熱温度を得るためには、アフタバーナと
して表面燃焼方式の輻射バーナが適する。Further, a second aspect of the present invention provides that an afterburner is provided near the oxidation filter to heat the oxidation filter to a degree necessary for activation, and the afterburner quickly and reliably heats the oxidation filter to the optimum temperature for activation. This makes it possible to more efficiently oxidize toxic gases such as unburned gas. Note that if the heating temperature of the oxidized filter by the afterburner is too high, it cannot be activated, and the oxidized filter is severely burned out, and even if the heating temperature is too low, it cannot be activated. Therefore, in order to obtain the optimum heating temperature for activating the oxidation filter, a surface combustion type radiation burner is suitable as the afterburner.
又本直管状燃焼室は途中に屈曲等がある場合も含み連続
した管状の燃焼嵐であれはよい。In addition, the main straight tubular combustion chamber may be a continuous tubular combustion chamber, even if there is a bend in the middle.
上記のように構成さnfcn求項/の発明の伝播燃焼装
置は、給気及び排気、点火、燃焼、消火のサイクルの連
続的なくり返しにおいて、次のサイクルにおける給気動
作で先のサイクルの燃焼排気ガスを押し出し放出するも
のであるが、この燃焼排気ガスはその放出時に点火源の
後流側に備えた酸化フィルタを通過することにより該燃
焼排気ガス中に含有する未燃ガス等の有毒ガスを完全に
酸化処理せしめるため一酸化炭素等の有毒ガスを含んだ
排気ガスが器外へ放出さnることはなく、排気のクリー
ン化が図りうるちのである。The propagation combustion device of the invention of NFCN Claim/Constructed as described above, in the continuous repetition of air supply and exhaust, ignition, combustion, and extinguishing cycles, the air supply operation in the next cycle burns the previous cycle. The exhaust gas is pushed out and released, but when this combustion exhaust gas is released, it passes through an oxidation filter provided on the downstream side of the ignition source, thereby removing toxic gases such as unburned gas contained in the combustion exhaust gas. Because the gas is completely oxidized, exhaust gas containing toxic gases such as carbon monoxide is not released outside the device, making the exhaust cleaner.
また、請求項2の酸化フィルタをアフタバーナでその活
性化に最適な温度に加熱せしめると、排気熱だけの加熱
ではその酸化処理効果を発揮するまでにある程度の時間
がかかるが、その活性化が迅速に行われ、しかも、燃焼
排気ガス中に含有する未燃ガス等の有毒ガスの酸化処理
がより効率的に行いうるものである。Furthermore, if the oxidation filter of claim 2 is heated to the optimal temperature for activation using an afterburner, the activation will be rapid, although it will take some time for the oxidation treatment effect to be exerted by heating only with exhaust heat. Furthermore, the oxidation treatment of toxic gases such as unburned gas contained in combustion exhaust gas can be performed more efficiently.
以下この発明による伝播燃焼装置の実施例について図面
を姦照して説明する。Embodiments of the propagation combustion apparatus according to the present invention will be described below with reference to the drawings.
第1肉及び第2図に示し九請求項1の実施例において、
(1)は直管状の燃焼室で、その上流側、すなわち、基
扁消火部位の7に消火時における火炎流の流速を急激に
変化させて遮壁をつくシ消火を確実ならしめるための狭
窄部(EI)Tj:搾シ加工等によシ一体形成せしめる
とともに、該狭窄部(5)の前流側には混合型(6)を
連続して拡開形成せしめている0(2)は前記直管状燃
焼室(υの下流側、すなわち、先廟点火部位(A)に臨
設せしめた点火源で、たとえば、ニクローム線、イグナ
イ゛り、セラミックスヒータ、パイロットバーナ等を用
いる。(3)は前記点火源(2)の後流側に備えた酸化
フィルタで、燃焼室(1)からの燃焼排気ガスが該酸化
フィルタ(8)を通過することで酸化フィルタ(3)を
排気熱で加熱すると同時に燃焼排気ガス中に含有する未
燃ガス等の有毒ガスを酸化処理して除去せしめるもので
めるOこの酸化フィルタ(8)としては、耐熱性、耐蝕
性及び一定の通気性(透過性)をもつ担体に触媒を任意
の手段で担持させたものが適する。たとえば、耐熱、耐
蝕性をもつコージライト (コ獣、 j 5i02’
、2 Al1203)に触媒として白金(ILz Pa
ale )を含浸法等により担持させて形成し圧部材
を一定の肉厚の板状体となし、かつ、その通気孔の形状
としてハニカム状又はフオーム状等のものを用いるのが
よい。そして、上記酸化フィルタ(3)にぺ四1スカイ
ト等を付10ぜしめて脱臭性能をもたせると脱臭効果も
併有し実施上有益でるる。In the embodiment of claim 1 shown in FIG.
(1) is a straight pipe-shaped combustion chamber, and on the upstream side of the combustion chamber, that is, at the base extinguishing area 7, there is a constriction that rapidly changes the flow velocity of the flame flow during extinguishing and provides a barrier to ensure extinguishing. Part (EI) Tj: 0 (2) is integrally formed by squeezing processing, etc., and the mixed mold (6) is continuously expanded and formed on the upstream side of the narrowed part (5). An ignition source installed on the downstream side of the straight-tubular combustion chamber (υ, that is, at the ambulatory ignition site (A), for example, using a nichrome wire, an ignition lamp, a ceramic heater, a pilot burner, etc.). (3) An oxidation filter provided on the downstream side of the ignition source (2) allows combustion exhaust gas from the combustion chamber (1) to pass through the oxidation filter (8) and heat the oxidation filter (3) with exhaust heat. This oxidation filter (8) also oxidizes and removes toxic gases such as unburned gas contained in the combustion exhaust gas.This oxidation filter (8) has heat resistance, corrosion resistance, and a certain level of air permeability. A carrier with a catalyst supported by any means is suitable. For example, cordierite, which has heat resistance and corrosion resistance, is suitable.
, 2 Al1203) with platinum (ILz Pa
It is preferable that the pressure member is formed by supporting the pressure member by an impregnation method or the like, and that the pressure member is a plate-like member having a constant thickness, and that the shape of the vent hole is honeycomb-like or foam-like. Further, if the oxidation filter (3) is provided with a deodorizing property by adding peskite or the like, it will also have a deodorizing effect and be useful in practice.
なお、(7)は直管状燃焼室(1)と連通して設けた排
気管、(3)はガスノズルで、基端混合基(6)に−夕
空気取入口(9)t−周囲に存して臨ませている。In addition, (7) is an exhaust pipe provided in communication with the straight-tubular combustion chamber (1), and (3) is a gas nozzle, which connects the base end mixing group (6), the air intake port (9), and the surrounding area. I am making it happen.
第3図に示した紬求項λの実施例において、(4)は前
記酸化フィルタ(8)をその活性化に必要な程度に加熱
するためのアフタバーナで、酸化フィルタ(8)の前後
側の周壁に複数の輻射バーナを等間隔を存して設置し、
こ扛らの輻射バーナにより酸化フィルタ(3)をその活
性化に最適な温度に迅速確実に加熱できるようになして
、酸化フィルタ(3)の迅速な活性化と、燃焼排気ガス
中に含有する未燃ガス等の有毒ガスのより効率的な酸化
処理とが行いうるようにしたものである。In the embodiment of the oxidation filter (8) shown in FIG. Multiple radiant burners are installed at equal intervals on the surrounding wall,
By using these radiant burners, the oxidation filter (3) can be quickly and reliably heated to the optimum temperature for its activation, and the oxidation filter (3) can be quickly activated and the oxidation filter (3) can be contained in the combustion exhaust gas. This enables more efficient oxidation treatment of toxic gases such as unburned gas.
伝播燃焼装置は、和気及び排気、点火1燃焼1消大のサ
イクルを連続的に(す返しlサイクルごとに火炎面か燃
焼! (1)内を伝播することによシ燃焼! (17の
各部が均等に加熱湯nるものでるるためその放熱か各部
均等となって加熱むらかなく、その熱効率も機めてよい
ことと相まってたとえば、寒冷地における道路等の融雪
装置(道路ヒーティングノあるいは業務用のフライヤ(
場は動機)等の各種ガス燃焼機器類のTJ0熱源として
使用した場合甚だ有益なものでるる。そこで、その燃焼
メカニズムは、ガスノズル(8)からの一定型の燃料ガ
スと一次空気取入口(9)からの一定撤の一次空気とか
混合室(6)へ供給さnて混合し、混合きnた混合気は
混合室(6)から狭窄部(5)を経て直管状燃焼室(1
)内へ供給され、燃焼室(1)内を上流側から下流側へ
流n(図示点線矢印(b)参照フ、先端の点火部位囚の
近(にまでその先端部が達すると、該点火部位(A)に
臨設さnている点火源(2)によりこ扛に点火芒nる。The propagation combustion device continuously performs a cycle of wake and exhaust, ignition 1 combustion 1 extinguishment (returning every cycle, the flame front burns! (1). Because each part heats water evenly, the heat dissipates evenly from each part, so there is no uneven heating, and the thermal efficiency is also good. fryer for (
It is extremely useful when used as a TJ0 heat source for various gas combustion equipment such as Therefore, the combustion mechanism is that a certain type of fuel gas from the gas nozzle (8) and a certain amount of primary air from the primary air intake port (9) are supplied to the mixing chamber (6) and mixed. The mixture flows from the mixing chamber (6) through the narrowed part (5) to the straight combustion chamber (1).
), and flows inside the combustion chamber (1) from the upstream side to the downstream side (see dotted arrow (b) in the figure). The ignition source (2) located at the part (A) ignites the ignition rod.
混合気の先端部に点火嘔扛ると混合気は先端側から燃焼
を始めその火炎流は燃焼室(1)内を下流側から上流側
へ流れ(図示実線矢印fa) *照ン、火炎伝PIMを
行い燃焼室(1)の各Sを均等に加熱する。火炎流の終
海部が基端消火部位(Eの狭窄部(5〕の近くに里で至
ると、該狭窄部(5)で遮壁をつ(り火炎流を堰止めそ
の流速に急激な変化を与えるためその消火は確実に行わ
n1次のサイクルに移行しその給気動作で燃焼室(1)
内の燃焼排気ガスを下流側へ押し出し排気管(7)から
器外へ放出する、という火炎伝播燃焼動作を連続的に(
9返すものでるる。When the tip of the mixture is ignited, the mixture starts to burn from the tip and the flame flows from the downstream side to the upstream side in the combustion chamber (1) (solid line arrow fa in the figure). PIM is performed to uniformly heat each S in the combustion chamber (1). When the final part of the flame flow reaches near the constricted part (5) of the proximal extinguishing site (E), the constricted part (5) blocks the flame flow and causes a sudden change in its flow velocity. The fire is extinguished reliably in order to give a
The flame propagation combustion operation is continuously carried out (
9 I will return it.
上記火炎伝播燃焼動作において、実験によnば、たとえ
は、直管状燃焼室(1)の長さ’r: 10 ”とした
場合、給気及び排気、点火、燃焼、消火の/サイクルが
略30秒〜60秒の割合で行わnlそのインプットが1
000 KcaVhの場合、略100℃〜/20°Cの
加熱温度か燃焼室(1)の各部から均等に得られた。In the above-mentioned flame propagation combustion operation, experiments have shown that, for example, when the length of the straight-tubular combustion chamber (1) is 10'', the cycle of air supply and exhaust, ignition, combustion, and extinguishing is approximately It is done at a rate of 30 seconds to 60 seconds and the input is 1
In the case of 000 KcaVh, a heating temperature of approximately 100°C to 20°C was obtained equally from each part of the combustion chamber (1).
給気及び排気、点火、燃焼、消火のサイクルの連続的な
くり返しによる火炎伝播燃焼動作において、次のサイク
ルにおける混合気を燃焼室(1)へ供給する給気動作時
に先のサイクル時の燃焼排気ガスを該給気で押し出し排
気管(7)から器外へ放出するものであるが、この発明
では、燃焼室(1)の先端点火部位(4)に備えた点火
源(2)の後流側に酸化フィルタ(3)を設けたから、
燃焼排気ガスが該酸化フィルタ(8)を通過することに
よシ酸化フィルタ(3)を加熱すると同時に燃焼排気ガ
ス中に含有する未燃ガス、生成物等の有毒ガスを酪化処
理せしめて排気のクリーン化を図り排気管(7)から器
外へ放出するから一酸化炭素等の有毒ガスを含んだ排気
ガスが器外へ放出嘔nることはない。また、酸化フィル
タ(8Jをアフタバーナ(4)でその活性化に最適な湿
度に加熱せしめると飯化フィルタ(8)の活性化か迅速
となり、かつ、燃焼排気ガス中に含有する未燃ガス等の
有毒ガスの酸化処理がよシ効率的に行いつるため実施上
有益である。なお、アフタバーナ(4)は酸化フィルタ
(8)をその活性化に最適な温度に加熱せしめることを
目的としているが、実際の使用にあたっては、燃焼排気
ガス中に含有する未燃ガス等の有毒ガスの燃焼分解作用
による焼失酸化機能も併せもち、しかも、アフタバーナ
(4)を酸化フィルタ(3)の手前で点火部位(4)の
近(に設置すnは点火源にも併用できるものである。In a flame propagation combustion operation in which the cycles of air supply and exhaust, ignition, combustion, and extinguishing are repeated continuously, the combustion exhaust from the previous cycle is used during the air supply operation to supply the mixture in the next cycle to the combustion chamber (1). The gas is pushed out by the supplied air and released outside the device from the exhaust pipe (7), but in this invention, the ignition source (2) provided at the tip ignition part (4) of the combustion chamber (1) is Since the oxidation filter (3) was installed on the side,
As the combustion exhaust gas passes through the oxidation filter (8), the oxidation filter (3) is heated, and at the same time, toxic gases such as unburned gas and products contained in the combustion exhaust gas are butylated and exhausted. Since the exhaust gas is discharged from the exhaust pipe (7) to the outside of the vessel, exhaust gas containing toxic gases such as carbon monoxide will not be discharged outside the vessel. In addition, if the oxidation filter (8J) is heated with an afterburner (4) to the optimal humidity for activation, the oxidation filter (8) will be activated quickly, and the unburned gas etc. contained in the combustion exhaust gas will be removed. This is useful in practice because the oxidation treatment of toxic gases can be carried out more efficiently.The purpose of the afterburner (4) is to heat the oxidation filter (8) to the optimum temperature for its activation. In actual use, it also has a burnout oxidation function by combustion decomposition of toxic gases such as unburned gas contained in the combustion exhaust gas, and the afterburner (4) is placed at the ignition point ( The n installed near (4) can also be used as an ignition source.
この発明は、以上説明したように構成はnでいるので、
以下の効果を奏する。As explained above, this invention has an n configuration, so
It has the following effects.
伝me焼特有の残留未燃ガス、火炎温度の低下による不
完全燃焼時の生成物等の有毒ガスを含んだ燃焼排気ガス
は酸化フィルタによって酬化処理嘔扛クリーンな排気と
して放出するから、−り化炭素中毒等の危険はなくなり
使用上の安全性番は倍加する。Combustion exhaust gas containing toxic gases such as residual unburnt gas peculiar to denme firing and products of incomplete combustion due to a drop in flame temperature is converted into a gas by an oxidation filter and released as clean exhaust gas. The danger of carbon poisoning is eliminated, and the safety factor for use is doubled.
また、請求項2記載の発明によnは、酸化フィルタの酸
化処理機能が最適な状態に迅速確実に保たれるので、燃
焼排気ガス中に含有する未撚ガス等の有毒ガスの酸化処
理がより効率的に行いつる。Further, according to the invention as claimed in claim 2, the oxidation processing function of the oxidation filter is quickly and reliably maintained in an optimal state, so that the oxidation processing of toxic gases such as untwisted gas contained in combustion exhaust gas is performed. Be more efficient.
!た1これらの特徴を活かし、道路の融雪装置、温室栽
培、業務用のフライヤ等にも最適である。! 1 Taking advantage of these features, it is also ideal for road snow melting equipment, greenhouse cultivation, commercial fryers, etc.
第1図はこの発明の請求項1による伝播燃焼装置の実施
例を示した全体の断面図、第2図は要部の拡大断面図、
第3図は請求項2による伝播燃焼装置の実施例を示した
要部の断面図、第1I図は従来例の全体断面図である。
(1)・・・直管状燃焼室、囚・・・失地点火部位、(
2)・・・点火m、(3)・・・除化フィルタ、(4)
・・・アフタバーナ。FIG. 1 is an overall cross-sectional view showing an embodiment of a propagation combustion apparatus according to claim 1 of the present invention, FIG. 2 is an enlarged cross-sectional view of main parts,
FIG. 3 is a sectional view of essential parts showing an embodiment of a propagation combustion apparatus according to claim 2, and FIG. 1I is an overall sectional view of a conventional example. (1)... Straight tubular combustion chamber, prisoner... misfire area, (
2)...Ignition m, (3)...Division filter, (4)
...afterbana.
Claims (1)
消、消火のサイクルを連続的にくり返しその火炎面が伝
播する燃焼方式の伝播燃焼装置において、該直管状燃焼
室(1)の先端点火部位(A)に備えた点火源(2)の
後流側に酸化フィルタ(3)を設けて、燃焼排気ガス中
に含有する未燃ガス等の有毒ガスを酸化除去して排出せ
しめるようにしたことを特徴とする伝播燃焼装置。 [2]酸化フィルタ(3)の近傍に該酸化フィルタ(3
)をその活性化に必要な程度に加熱せしめるアフタバー
ナ(4)を設けた請求項1記載の伝播燃焼装置。[Scope of Claims] [1] In a combustion type propagation combustion device in which a cycle of supplying air, exhausting air, ignition, combustion, and extinguishing is continuously repeated in a straight pipe combustion chamber (1), and the flame front propagates, An oxidation filter (3) is provided on the downstream side of the ignition source (2) provided at the tip ignition site (A) of the straight tube-shaped combustion chamber (1), and removes unburned gas and other substances contained in the combustion exhaust gas. A propagation combustion device characterized by oxidizing and removing poisonous gases. [2] Place the oxidation filter (3) near the oxidation filter (3).
2. A propagation combustion apparatus according to claim 1, further comprising an afterburner (4) for heating the fuel (4) to an extent necessary for activation thereof.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63096469A JPH01266409A (en) | 1988-04-19 | 1988-04-19 | Flame propagating burner |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63096469A JPH01266409A (en) | 1988-04-19 | 1988-04-19 | Flame propagating burner |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01266409A true JPH01266409A (en) | 1989-10-24 |
JPH0583802B2 JPH0583802B2 (en) | 1993-11-29 |
Family
ID=14165897
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63096469A Granted JPH01266409A (en) | 1988-04-19 | 1988-04-19 | Flame propagating burner |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01266409A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0655009U (en) * | 1991-10-25 | 1994-07-26 | 東邦瓦斯株式会社 | Flame propagation combustion burner |
JP2007237040A (en) * | 2006-03-07 | 2007-09-20 | Nichias Corp | Treatment method of organic solvent-containing air |
-
1988
- 1988-04-19 JP JP63096469A patent/JPH01266409A/en active Granted
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0655009U (en) * | 1991-10-25 | 1994-07-26 | 東邦瓦斯株式会社 | Flame propagation combustion burner |
JP2007237040A (en) * | 2006-03-07 | 2007-09-20 | Nichias Corp | Treatment method of organic solvent-containing air |
Also Published As
Publication number | Publication date |
---|---|
JPH0583802B2 (en) | 1993-11-29 |
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