JPS64602B2 - - Google Patents

Info

Publication number
JPS64602B2
JPS64602B2 JP56184608A JP18460881A JPS64602B2 JP S64602 B2 JPS64602 B2 JP S64602B2 JP 56184608 A JP56184608 A JP 56184608A JP 18460881 A JP18460881 A JP 18460881A JP S64602 B2 JPS64602 B2 JP S64602B2
Authority
JP
Japan
Prior art keywords
combustion
air
outer cylinder
reduction catalyst
blower
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
Application number
JP56184608A
Other languages
Japanese (ja)
Other versions
JPS5886318A (en
Inventor
Nobuyuki Kanehara
Yoshifumi Morya
Masaaki Nishihata
Shoichi Hara
Naoki Ishikura
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP56184608A priority Critical patent/JPS5886318A/en
Publication of JPS5886318A publication Critical patent/JPS5886318A/en
Publication of JPS64602B2 publication Critical patent/JPS64602B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C13/00Apparatus in which combustion takes place in the presence of catalytic material

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Combustion Of Fluid Fuel (AREA)
  • Direct Air Heating By Heater Or Combustion Gas (AREA)
  • Gas Burners (AREA)

Description

【発明の詳細な説明】 本発明は温風暖房装置、特に室内開放型温風暖
房装置のクリーン燃焼および排ガス浄化の分野に
関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to the field of clean combustion and exhaust gas purification of hot air heating systems, particularly indoor open type hot air heating systems.

従来の室内開放型温風暖房装置のバーナはブン
ゼンバーナが用いられていたので、NOX値が高
いといつた欠点を有していた。従つて、シユバン
クバーナ等の予混合を用いて低NOXを図る室内
開放型温風暖房装置もこころみられている。
Conventional indoor open-air heating systems used Bunsen burners as burners, which had the disadvantage of high NOx values. Therefore, indoor open-air heating systems that use premixing such as a bunk burner to reduce NOx are also being developed.

しかし、シユバンクバーナは炎口部を形成する
セラミツクプレートの熱容量が大きいので、点着
火時の安定熱焼に達する時間が長い、気流が燃焼
に悪影響を及ぼす、TDRがとれないといつた欠
点を有しているうえに、低NOX化は図れるが人
体への悪影響をおよぼすとされているNO2の比
率が高いという欠点を有していた。
However, because the heat capacity of the ceramic plate that forms the flame nozzle in the sybank burner is large, it takes a long time to reach stable sintering upon ignition, the airflow has a negative effect on combustion, and TDR cannot be achieved. In addition, although it is possible to reduce NOx , it has the disadvantage of a high proportion of NO2 , which is said to have an adverse effect on the human body.

一方、燃焼排気ガスのクリーン化を図る為に燃
焼排気ガス通路に酸化触媒を設け、CO,HC等の
中間生成物を酸化させる手段も提案されている
が、酸化触媒は温度の条件はあるものの触媒雰囲
気の酸素量は一定以上あれば特性に及ぼす影響は
無視出来るものであつたので、その設置条件は、
温度等触媒性能に関する点、通気抵抗等燃焼性能
に関する点を考えてなされていたが、燃焼ガス中
のNO2をNOに還元する手段に関してはほとんど
考えられていなかつた。
On the other hand, in order to make the combustion exhaust gas cleaner, an oxidation catalyst has been proposed in the combustion exhaust gas passage to oxidize intermediate products such as CO and HC, but the oxidation catalyst has certain temperature conditions. If the amount of oxygen in the catalyst atmosphere was above a certain level, the effect on the characteristics could be ignored, so the installation conditions were as follows:
Although considerations have been made regarding catalyst performance, such as temperature, and combustion performance, such as ventilation resistance, little consideration has been given to means of reducing NO 2 in combustion gas to NO.

本発明の目的は、予混合表面燃焼の低負荷燃焼
を可能にすることによつて低NOX化を図ると共
に、燃焼排気ガス中のNOX、特にNO2を効果的
に還元して排気ガス浄化を行うと共に、TDRの
とれる温風暖房装置に関するものである。
The purpose of the present invention is to achieve low NOx by enabling low-load combustion using premixed surface combustion, and to effectively reduce NOx , especially NO2 , in combustion exhaust gas to reduce exhaust gas. This relates to a hot air heating device that not only purifies the air but also provides TDR.

以上、本発明の一実施例について第1図に基づ
いて説明する。
An embodiment of the present invention will be described above based on FIG. 1.

第1図は本発明の温風暖房装置の原理を示す側
断面図である。
FIG. 1 is a side sectional view showing the principle of the hot air heating device of the present invention.

図中1は温風暖房装置のケーシング、2は予混
合表面燃焼を行うバーナーであり、ガスノズル3
と対向して設けられた1次空気口4、混合管5、
混合気室6、燃焼筒7の内側に金網等で構成され
た炎口部8、金属板で形成された燃焼筒7の外筒
9、2次空気の流入を防止する密閉構造とした燃
焼室10で構成されている。
In the figure, 1 is the casing of the hot air heating device, 2 is the burner that performs premixed surface combustion, and the gas nozzle 3
A primary air port 4, a mixing pipe 5, and
A mixture chamber 6, a flame port 8 made of wire mesh or the like on the inside of the combustion tube 7, an outer tube 9 of the combustion tube 7 made of a metal plate, and a combustion chamber with a sealed structure to prevent the inflow of secondary air. It consists of 10.

燃焼室10後流の排ガス通路中に、外筒9より
小径の排気筒11を介して、前記排気筒11とほ
ぼ同径の遷移金属系の還元触媒12を設けてい
る。
A transition metal reduction catalyst 12 having approximately the same diameter as the exhaust pipe 11 is provided in the exhaust gas passage downstream of the combustion chamber 10 via an exhaust pipe 11 having a smaller diameter than the outer cylinder 9 .

送風機13によつて、吸込口14から吸引され
た空気は、外筒9と同径以上のガイド板15を通
過する時、燃焼ガスを吸引し、燃焼筒7の外筒9
の外周の温風通路16を経て吹出口17から送風
される。尚、送風機13、排気ガイド15、還元
触媒12はそれぞれ対向して温風が還元触媒12
面に吹き込まない様に設けられている。
When the air sucked from the suction port 14 by the blower 13 passes through the guide plate 15 which has the same diameter or more as the outer cylinder 9, it sucks combustion gas and causes the air to flow through the outer cylinder 9 of the combustion cylinder 7.
Air is blown from the outlet 17 through the hot air passage 16 on the outer periphery of the air. Note that the blower 13, the exhaust guide 15, and the reduction catalyst 12 are arranged to face each other so that the hot air flows into the reduction catalyst 12.
It is designed to prevent air from blowing onto the surface.

18はガス弁、19はガバナーで、制御回路2
0によつて点火プラグ21で放電、着火し、燃焼
検知素子22の出力を検知し燃焼を制御するもの
であり、燃焼量が大の時は風量も大、燃焼量が小
の時は風量も小とする制御機能を有するものであ
る。
18 is a gas valve, 19 is a governor, and control circuit 2
0, the spark plug 21 discharges and ignites, and the output of the combustion detection element 22 is detected to control combustion. When the combustion amount is large, the air volume is also large, and when the combustion amount is small, the air volume is also controlled. It has a control function that makes it small.

上記構成において、ガスノズル3から噴出した
ガスは、燃焼に必要な空気を、1次空気口4から
1次空気として吸引し、混合管5で混合しながら
混合気室6に導かれる。混合気は金網等で構成さ
れた炎口部8から燃焼室10内に噴出されると同
時に点火プラグ21で放電、着火し、炎口部8で
表面燃焼を行う。
In the above configuration, the gas ejected from the gas nozzle 3 sucks air necessary for combustion as primary air from the primary air port 4, and is guided to the mixture chamber 6 while being mixed in the mixing pipe 5. The air-fuel mixture is ejected into the combustion chamber 10 from a flame port 8 made of a wire mesh or the like, and at the same time is discharged and ignited by a spark plug 21, and surface combustion occurs in the flame port 8.

炎口部8は金網等で形成されているのでその熱
容量は小さく、さらに燃焼筒7の外筒9は金属板
で形成されているので炎口部8から外側に輻射熱
として熱通過量は少ない、従つて低負荷燃焼時、
即ち燃焼量が小の時には送風量が小としたので、
外筒9の外周からの冷却も少なく良好な燃焼を維
持する炎口温度が保たれる。
Since the flame port 8 is formed of wire mesh or the like, its heat capacity is small, and since the outer cylinder 9 of the combustion tube 7 is formed of a metal plate, the amount of heat passing through as radiant heat from the flame port 8 to the outside is small. Therefore, during low load combustion,
In other words, when the combustion amount was small, the airflow amount was small, so
There is little cooling from the outer periphery of the outer cylinder 9, and the flame mouth temperature that maintains good combustion is maintained.

一方、高負荷燃焼時、即ち、燃焼量が大の時に
は燃焼筒7の外筒9の温度が上昇するが、外筒9
の外周が温風通路になつており、かつ、送風量が
大きくなる様にしたので外筒9を冷却し、炎口部
8が異常に高温になるのを防ぐことが出来、バツ
クフアイヤーを起すことはない。
On the other hand, during high-load combustion, that is, when the combustion amount is large, the temperature of the outer cylinder 9 of the combustion tube 7 increases;
Since the outer periphery of the tube is a hot air passage and the amount of air blown is large, the outer tube 9 can be cooled and the flame opening 8 can be prevented from becoming abnormally hot, thereby preventing backfire. There isn't.

さらに、燃焼室10の後流の排ガス通路中にス
テンレス鋼、モリブデン鋼、鉄−クロム鋼等の遷
移金属系の還元触媒12をおおよそ500℃〜700℃
の高温域に外筒9より小径の排気筒11を介して
設けられているので、排ガス中のNO2がNOに還
元される。また前記外筒9よりも小径である排気
筒11、還元触媒12、さらに外筒9と同径のガ
イド板15により、以下の作用効果が生じる。
Furthermore, a reduction catalyst 12 made of a transition metal such as stainless steel, molybdenum steel, or iron-chromium steel is placed in the exhaust gas passage downstream of the combustion chamber 10 at approximately 500°C to 700°C.
Since the exhaust pipe 11 is provided in the high temperature range of the exhaust pipe 11 with a diameter smaller than that of the outer cylinder 9, NO 2 in the exhaust gas is reduced to NO. Furthermore, the exhaust pipe 11 having a smaller diameter than the outer cylinder 9, the reduction catalyst 12, and the guide plate 15 having the same diameter as the outer cylinder 9 produce the following effects.

還元触媒12を小径にすることにより、同触
媒12の単位面積あたりに通過する排気ガス量
が増加するため、同触媒12を低負荷燃焼時に
おいても安定して500℃〜700℃の高温に維持で
きる。このため、高負荷、低負荷時において
も、環元効果を確実に期待できる。
By making the reduction catalyst 12 smaller in diameter, the amount of exhaust gas passing through per unit area of the catalyst 12 increases, so the catalyst 12 can be stably maintained at a high temperature of 500°C to 700°C even during low load combustion. can. Therefore, the ring element effect can be reliably expected even under high and low loads.

外筒9と同径のガイド板15は、同ガイド板
15よりも小径である前記触媒12の面に、送
風機13より誘起された空気が流入することを
完全に防止することができるため、同触媒12
上で、室内空気と排気ガスが混合することがな
い。この結果、同触媒12上での、NOの再酸
化を防止でき、環元効果を維持できる。
The guide plate 15, which has the same diameter as the outer cylinder 9, can completely prevent the air induced by the blower 13 from flowing into the surface of the catalyst 12, which has a smaller diameter than the guide plate 15. Catalyst 12
At the top, indoor air and exhaust gas do not mix. As a result, reoxidation of NO on the catalyst 12 can be prevented and the ring element effect can be maintained.

低負荷燃焼時においても、前記触媒12は高
温に維持されているため、同触媒12からの輻
射熱により、燃焼室10内は同触媒12がない
場合に比べ、高温状態を実現できると共に、同
触媒12上に空気が流入しないことから、燃焼
室10内にも空気が流入せず、火炎を乱すこと
がない。これらにより、低負荷燃焼時における
火炎を安定させることができ、COの発生を著
しく抑制できる。
Since the catalyst 12 is maintained at a high temperature even during low-load combustion, the radiant heat from the catalyst 12 makes it possible to achieve a higher temperature inside the combustion chamber 10 than in the case where the catalyst 12 is not present. Since no air flows into the combustion chamber 12, no air flows into the combustion chamber 10, and the flame is not disturbed. These make it possible to stabilize the flame during low-load combustion and significantly suppress the generation of CO.

燃焼室10は空気の流入の出来ない密閉構造に
したので送風機13による燃焼室10内の燃焼ガ
スの乱れを防ぎ均一燃焼が出来るので燃焼性の悪
化を防止すると共に、バイパス空気として補助空
気が入らないので還元触媒12を通過する燃焼排
ガス中のO2濃度が低くなるので、NOからNO2
の酸化も少なく、かつ、NO2からNOへの環元効
率も向上し低NO2化が達成される。
The combustion chamber 10 has a sealed structure that prevents air from entering, which prevents disturbance of the combustion gas in the combustion chamber 10 by the blower 13 and enables uniform combustion, which prevents deterioration of combustibility and prevents auxiliary air from entering as bypass air. Since the O 2 concentration in the combustion exhaust gas passing through the reduction catalyst 12 is lowered, there is less oxidation of NO to NO 2 , and the efficiency of converting NO 2 to NO is improved, achieving low NO 2 . be done.

第2図は排気筒の他の実施例を示す要部断面図
であり、aは排気筒11′が円錐台状に排気ガス
の流れ方向に従つて小径となつているものであ
り、bは燃焼筒の外筒9の先端を小径とし排気筒
11″をかねた実施例である。
FIG. 2 is a sectional view of a main part showing another embodiment of the exhaust stack, in which a shows the exhaust pipe 11' having a truncated conical shape and whose diameter becomes smaller in the direction of flow of exhaust gas, and b shows the exhaust pipe 11'. This is an embodiment in which the tip of the outer tube 9 of the combustion tube is made small in diameter and serves as an exhaust tube 11''.

これらの実施例は、その作用、効果も第1図の
実施例とほぼ同じである。
The functions and effects of these embodiments are almost the same as those of the embodiment shown in FIG.

以上の説明であきらかな様に、本発明によれ
ば、燃焼室10を2次空気の流入を防止する密閉
構造とし、排気筒11および還元触媒12を外筒
9より小径として送風による環元効果におよぼす
影響を防止しているのでNOからNO2への酸化を
少なくすると共に、NO2からNOへの環元効果を
高め低NO2化を達成している。
As is clear from the above description, according to the present invention, the combustion chamber 10 has a sealed structure that prevents the inflow of secondary air, and the exhaust pipe 11 and the reduction catalyst 12 are made smaller in diameter than the outer pipe 9, so that the ring-forming effect of air blowing is achieved. This prevents the oxidation of NO to NO 2 , and also increases the ring element effect from NO 2 to NO, achieving low NO 2 .

さらに、予混合表面燃焼バーナの燃焼筒7外筒
9を金属板で形成することによつて、低負荷燃焼
が可能となり、低NOX化が図れると共に温風暖
房装置として燃焼量可変にも対応出来るものであ
る。
Furthermore, by forming the combustion tube 7 outer tube 9 of the premixed surface combustion burner with a metal plate, low-load combustion is possible, low NOx is achieved, and the combustion amount can be varied as a hot air heating device. It is possible.

また、還元触媒と送風機の間の送風ガイドを対
向して設け還元触媒に風があたらないようにして
いるので温風式特有の送風によるNO2環元効果
の低下、NOからNO2への酸化の防止、送風の影
響による燃焼悪化の防止を行うことができる。
In addition, the air guides between the reduction catalyst and the blower are placed facing each other to prevent air from hitting the reduction catalyst, which reduces the NO 2 ringing effect and reduces the oxidation of NO to NO 2 due to air blowing, which is unique to hot air systems. It is possible to prevent combustion from worsening due to the influence of air blowing.

さらに燃焼外筒を金属板で形成し、燃焼量の大
小により送風量を大小に制御することより空気比
を一定にして燃焼範囲の拡大を図ることができ
る。
Furthermore, by forming the combustion outer cylinder with a metal plate and controlling the amount of air blown depending on the amount of combustion, it is possible to keep the air ratio constant and expand the combustion range.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明の温風暖房装置の一実施例を示
す側断面図、第2図は排気筒の他の実施例を示す
要部断面図である。 2……バーナ、7……燃焼筒、8……炎口部、
9……外筒、10……燃焼室、11……排気筒、
12……還元触媒、13……送風機、16……温
風通路、20……制御回路。
FIG. 1 is a sectional side view showing one embodiment of the hot air heating device of the present invention, and FIG. 2 is a sectional view of essential parts showing another embodiment of the exhaust stack. 2... Burner, 7... Combustion cylinder, 8... Burner port,
9...Outer cylinder, 10...Combustion chamber, 11...Exhaust pipe,
12...Reduction catalyst, 13...Blower, 16...Hot air passage, 20...Control circuit.

Claims (1)

【特許請求の範囲】[Claims] 1 金属板からなる筒状の燃焼筒外筒の内側に金
網等で炎口部を形成した予混合表面燃焼を行うバ
ーナと温風用送風機を有し、送風ガイドと対向し
て設けた燃焼筒外筒外周を温風通路とし、2次空
気の流入を防止する密閉構造とした燃焼室後流の
燃焼ガス通路に遷移金属系の還元触媒を設け、か
つ前記還元触媒は燃焼筒外筒より小径の排気筒を
介して排気筒とほぼ同径に設け、かつ前記送風
機、送風ガイド還元触媒の順にそれれ対向して設
けると共に、燃焼量の大小に応じて送風量も大小
に制御する制御回路を設けた温風暖房装置。
1 A cylindrical combustion tube made of a metal plate A combustion tube that has a burner that performs premixed surface combustion with a flame port formed with a wire mesh or the like on the inside of the outer cylinder and a hot air blower, and is installed facing a blower guide. The outer periphery of the outer cylinder is a hot air passage, and the combustion chamber has a sealed structure to prevent the inflow of secondary air.A transition metal-based reduction catalyst is provided in the combustion gas passage downstream of the combustion chamber, and the reduction catalyst has a diameter smaller than that of the outer cylinder. A control circuit is provided which is disposed at approximately the same diameter as the exhaust pipe through the exhaust pipe, and is provided facing each other in the order of the blower and the blow guide reduction catalyst, and also controls the blowing amount to be large or small depending on the size of the combustion amount. A warm air heating system is installed.
JP56184608A 1981-11-17 1981-11-17 Hot air space heater Granted JPS5886318A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56184608A JPS5886318A (en) 1981-11-17 1981-11-17 Hot air space heater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56184608A JPS5886318A (en) 1981-11-17 1981-11-17 Hot air space heater

Publications (2)

Publication Number Publication Date
JPS5886318A JPS5886318A (en) 1983-05-23
JPS64602B2 true JPS64602B2 (en) 1989-01-09

Family

ID=16156191

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56184608A Granted JPS5886318A (en) 1981-11-17 1981-11-17 Hot air space heater

Country Status (1)

Country Link
JP (1) JPS5886318A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03119006U (en) * 1990-03-13 1991-12-09

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6096857A (en) * 1983-10-29 1985-05-30 Rinnai Corp Controller for warm air fan of warm air heater
JPS60130366U (en) * 1984-02-10 1985-08-31 シャープ株式会社 Combustion forced convection stove
JP4080492B2 (en) 2005-03-31 2008-04-23 日本発条株式会社 Bonded body and bonding method

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS51129584A (en) * 1975-05-06 1976-11-11 Aisin Seiki Co Ltd An atmosphere type force increasing apparatus
JPS5424327A (en) * 1977-07-25 1979-02-23 Osaka Gas Co Ltd Surface combustion type combusting device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03119006U (en) * 1990-03-13 1991-12-09

Also Published As

Publication number Publication date
JPS5886318A (en) 1983-05-23

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