JPH03195861A - Immersion pipe heater - Google Patents

Immersion pipe heater

Info

Publication number
JPH03195861A
JPH03195861A JP1335713A JP33571389A JPH03195861A JP H03195861 A JPH03195861 A JP H03195861A JP 1335713 A JP1335713 A JP 1335713A JP 33571389 A JP33571389 A JP 33571389A JP H03195861 A JPH03195861 A JP H03195861A
Authority
JP
Japan
Prior art keywords
combustion gas
combustion
burner
liquid
pipe
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
Application number
JP1335713A
Other languages
Japanese (ja)
Other versions
JP2839165B2 (en
Inventor
Jiro Nakamaru
中丸 治郎
Yoshiyuki Sano
義之 佐野
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.)
Tokyo Gas Co Ltd
Original Assignee
Tokyo Gas 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 Tokyo Gas Co Ltd filed Critical Tokyo Gas Co Ltd
Priority to JP33571389A priority Critical patent/JP2839165B2/en
Publication of JPH03195861A publication Critical patent/JPH03195861A/en
Application granted granted Critical
Publication of JP2839165B2 publication Critical patent/JP2839165B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

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  • Combustion Of Fluid Fuel (AREA)
  • Heat-Pump Type And Storage Water Heaters (AREA)
  • Gas Burners (AREA)
  • Incineration Of Waste (AREA)

Abstract

PURPOSE:To restrict a noise level to a lower level and improve an efficiency of combustion by a method wherein an extreme end of a burner is mounted below a liquid surface of heated liquid and a catalyst reacting part is constituted at a downstream side of the burner. CONSTITUTION:A burner 7 is ignited, a combustion gas of high temperature flows in a combustion gas passage 6 toward a flowing-out port 4 so as to heat liquid 2 around a flow pipe 5. In the midway part of the combustion gas passage 6 is formed a catalyst reaction part 9. If a carrier 10 is made by a ceramic honeycomb structure 11, it has many communication holes 13 in it, so that the combustion gas may flow through the communication holes 13 and the gas is discharged out of the pipe 5. When the combustion gas passes through a catalyst reaction part 9, the combustion gas reacts rapidly with remaining combustion air to make a complete combustion, so that it is possible to prevent harmful carbon oxide from being discharged. There is no useless discharging of energy, so that it is possible to keep a high efficiency of combustion. In addition, the ceramic honeycomb 11 has an action to store high temperature and an efficiency of thermal condition is further improved. The combustion gas flow passage downstream side of the catalyst reaction part 9 is throttled to be narrow and noise caused by a phenomenon of resonance in the pipe 5 is restricted to a low level.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、例えば金属溶湯等の液状物質を加熱するヒー
タに関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a heater for heating a liquid substance such as molten metal.

(従来の技術) 従来の浸管ヒータとしては、例えば第4図に示すものが
ある。この浸管ヒータaは、加熱対象とする液体すの中
に、液面上に、燃焼ガス流入口Cと流出口dを有する管
eを、液体すの中に浸漬し、そして前記液面に位置する
流入口C内にバーナfを設置して、該バーナに於いて発
生する高温の燃焼ガスを管e内に送り込んで、管eそし
て液体bを加熱するものである。
(Prior Art) As a conventional immersion tube heater, there is one shown in FIG. 4, for example. This immersion tube heater a is constructed by immersing a tube e having a combustion gas inlet C and an outlet d above the liquid level in a liquid to be heated, and then placing it above the liquid level. A burner f is installed in the inlet C, and high-temperature combustion gas generated by the burner is sent into the tube e to heat the tube e and the liquid b.

(発明が解決しようとする課題) 前記のような従来の浸管ヒータaでは、バーナfを液体
すの表面よりも下に位置させると、バーナfの火炎が急
速に冷やされて燃焼が不完全となり、この結果−酸化炭
素が発生して燃焼ガス流出口dより外部に排出されてし
まうので、これを防ぐためバーナfは図示の通り、液体
すの表面よりも上に位置させている。しかし、このよう
にバーナfを液体すの表面よりも上に位置させたことに
より、バーナf周囲の管eが非常に高い温度になって危
険であることに加え、液体すの加熱に寄与しない無駄な
放熱が多くなって熱効率が低いという課題がある。
(Problems to be Solved by the Invention) In the conventional immersion tube heater a as described above, when the burner f is located below the surface of the liquid, the flame of the burner f is rapidly cooled and combustion is incomplete. As a result, carbon oxide is generated and discharged to the outside from the combustion gas outlet d. To prevent this, the burner f is positioned above the surface of the liquid as shown in the figure. However, by locating the burner f above the surface of the liquid bath, the temperature of the tube e surrounding the burner f becomes extremely high, which is dangerous, and it does not contribute to the heating of the liquid bath. There is a problem that there is a lot of wasted heat radiation and the thermal efficiency is low.

さらに、従来のこのような浸管ヒータaにおいては、燃
焼ガスの流速が小さいと、管eの内側面に生じる境膜の
影響により、燃焼ガスから液体すへの伝熱効率は極めて
悪くなるので、流速をある程度大きくする必要がある。
Furthermore, in the conventional immersion tube heater a, if the flow rate of the combustion gas is low, the efficiency of heat transfer from the combustion gas to the liquid becomes extremely poor due to the influence of the film formed on the inner surface of the tube e. It is necessary to increase the flow velocity to some extent.

しかし、あまり流速を上げ過ぎると、今度は管eの共鳴
現象により大きな騒音が発生してしまうのであまり大き
くすることができず、したがって加熱効率が低く抑えら
れてしまうという課題もある。
However, if the flow rate is increased too much, a large noise will be generated due to the resonance phenomenon of the tube e, so it cannot be increased too much, and therefore there is a problem that the heating efficiency is kept low.

本発明は以上のような課題を解決することを目的とする
ものである。
The present invention aims to solve the above problems.

(課題を解決するための手段) 前記課題を解決するための手段を、実施例に対応する第
1図〜第3図に基づいて説明すると、まず特許請求の範
囲第1項記載の浸管ヒータ1は、加熱対象液体2内に、
燃焼ガス流入口3と流出口4を有する管5を、流入口3
と流出口4の双方が液体2の表面よりも上に位置するよ
うに、液体2内に浸漬して、液体2内に燃焼ガス流路6
を形成体2の液面下になるように設置すると共に、燃焼
ガス流路6のバーナ7よりも下流側の適所に、燃焼ガス
が通過可能な触媒反応部9を構成したものである。
(Means for Solving the Problems) The means for solving the problems will be explained based on FIGS. 1 to 3 corresponding to the embodiments. First, the immersion tube heater according to claim 1 1 is in the liquid to be heated 2,
A pipe 5 having a combustion gas inlet 3 and an outlet 4 is connected to the inlet 3
The combustion gas flow path 6 is immersed in the liquid 2 such that both the and the outlet 4 are located above the surface of the liquid 2.
is installed below the liquid level of the forming body 2, and a catalytic reaction section 9 through which the combustion gas can pass is constructed at a suitable location downstream of the burner 7 in the combustion gas passage 6.

次に、第2項記載の浸管ヒータ1は前記第1項記載の触
媒反応部9の担体10を、セラミックハニカム11で構
成したものである。
Next, in the immersion tube heater 1 described in item 2, the carrier 10 of the catalytic reaction section 9 described in item 1 is made of a ceramic honeycomb 11.

第3項記載の浸管ヒータ1は、前記第1項記載の燃焼ガ
ス流路6の触媒反応部9よりも下流側を、その上流側よ
りも細く絞ったものである。
The immersion tube heater 1 described in item 3 is such that the downstream side of the catalytic reaction section 9 of the combustion gas flow path 6 described in item 1 is narrowed narrower than the upstream side thereof.

第4項記載の浸管ヒータ1は、前記第1項記載の触媒反
応部9の担体10をセラミックハニカム11で構成する
と共に、燃焼ガス流路6の触媒反応部9よりも下流側を
、その上流側よりも細く絞ったものである。
In the immersion tube heater 1 described in item 4, the carrier 10 of the catalytic reaction section 9 described in item 1 is constituted by a ceramic honeycomb 11, and the downstream side of the catalytic reaction section 9 of the combustion gas flow path 6 is It is narrower than the upstream side.

また第5項記載の浸管ヒータ1は、前記第1項記載の燃
焼ガス流路6の触媒反応部9よりも下流側をコルゲート
管12で構成したものである。
In the immersion tube heater 1 described in item 5, the downstream side of the catalytic reaction section 9 of the combustion gas flow path 6 described in item 1 is constructed with a corrugated pipe 12.

(作用および実施例) バーナ7を点火し、これを燃焼状態とすれば、高温の燃
焼ガスが発生し、燃焼ガス流路6を下流側すなわち燃焼
ガス流出口4に向って流れながら、管5そしてその周囲
の液体2を加熱する。燃焼ガス流路6の途中には、触媒
反応部9を構成しているが、例えばこの担体10を、例
えばセラミックハニカム11で構成すれば、これには多
数の連通孔13が開いているので、燃焼ガスはこの連通
孔13を通って上流側から下流側へ流れることができ、
そして流出口4に達した燃焼ガスは管5外に排出される
(Operations and Examples) When the burner 7 is ignited and put into a combustion state, high-temperature combustion gas is generated, and while flowing through the combustion gas passage 6 toward the downstream side, that is, toward the combustion gas outlet 4, the pipe 5 Then, the liquid 2 around it is heated. A catalytic reaction section 9 is formed in the middle of the combustion gas flow path 6, and if this carrier 10 is formed of, for example, a ceramic honeycomb 11, a large number of communication holes 13 are opened therein. Combustion gas can flow from the upstream side to the downstream side through this communication hole 13,
The combustion gas that has reached the outlet 4 is discharged to the outside of the pipe 5.

本発明においては、さらにバーナ7を、少なくとも、そ
の先端部8を加熱対象液体2の表面下になるように設置
したので、液体2の表面よりも上に位置させた場合に比
較して、バーナ7周囲の管5が非常に高い温度に上昇す
ることはなく、したがって安全であると同時に、液体2
の加熱に寄与しない無駄な放熱量を減らすことができる
。もちろん、このようにバーナ7の先端部8を液体2の
表面下に位置させると、バーナ7の火炎が急速に冷やさ
れて、燃焼がある程度不完全となり、そして−酸化炭素
を発生するが、燃焼ガス流路6のバーナ7の下流側適所
に触媒反応部9を構成したため、燃焼ガスがここを通過
する際に燃焼ガスと共に流路6すなわち管5内を流れる
燃焼用残存空気と速やかに反応して完全燃焼するので、
流出口4から有害な一酸化炭素が排出するのを抑制でき
ると共に、無駄なエネルギー放出がないので高い燃焼効
率を維持することができる。
In the present invention, the burner 7 is further installed so that at least its tip 8 is below the surface of the liquid 2 to be heated. 7 The surrounding tube 5 does not rise to a very high temperature and is therefore safe, while at the same time the liquid 2
The amount of wasted heat radiation that does not contribute to heating can be reduced. Of course, by locating the tip 8 of the burner 7 below the surface of the liquid 2, the flame of the burner 7 is rapidly cooled, the combustion is somewhat incomplete, and - producing carbon oxides, but the combustion Since the catalytic reaction section 9 is configured at a suitable location on the downstream side of the burner 7 in the gas flow path 6, when the combustion gas passes through here, it quickly reacts with the combustion residual air flowing in the flow path 6, that is, the pipe 5, together with the combustion gas. Since it burns completely,
Not only can harmful carbon monoxide be suppressed from being discharged from the outlet 4, but also high combustion efficiency can be maintained since no wasteful energy is released.

触媒反応部9の担体10をセラミックハニカム11で構
成すれば、前記のように触媒反応部9を燃焼ガスが通過
可能に構成し得ることに加えて、セラミックハニカム1
1には蓄熱作用があり、したがって液体2への伝熱効率
をさらに改善することができる。
If the carrier 10 of the catalytic reaction section 9 is made of the ceramic honeycomb 11, the catalytic reaction section 9 can be configured to allow combustion gas to pass therethrough as described above.
1 has a heat storage effect, and therefore the heat transfer efficiency to the liquid 2 can be further improved.

しかもセラミックハニカム11には整流作用もあるので
、触媒反応部9よりも下流側の燃焼ガス流路6を、その
上流側よりも細く絞って、ここを流れる燃焼ガスの流速
を大きくしても、管5の共鳴現象による騒音の発生は低
いレベルに抑えることができ、したがって効果的に管5
の内側面に生じる境膜の影響を排除して、液体2への伝
熱効率をさらに向上させることができる。また、このよ
うにセラミックハニカム11の下流側では管fの共鳴現
象が起きにくいので、例えば表面を波状にして伝熱効率
を改善したコルゲート管12で流路6を構成すれば、騒
音の発生を低く抑えながら、液体2への伝熱効率、した
がって浸管ヒータ1の燃焼効率をさらに改善することが
できる。
Moreover, the ceramic honeycomb 11 also has a rectifying effect, so even if the combustion gas flow path 6 on the downstream side of the catalytic reaction section 9 is narrowed narrower than that on the upstream side and the flow velocity of the combustion gas flowing therein is increased, The generation of noise due to the resonance phenomenon of the pipe 5 can be suppressed to a low level, and therefore the pipe 5 can be effectively
It is possible to further improve the heat transfer efficiency to the liquid 2 by eliminating the influence of the film produced on the inner surface of the liquid 2. Furthermore, since the resonance phenomenon of the tubes f is less likely to occur on the downstream side of the ceramic honeycomb 11, for example, if the flow path 6 is constructed of a corrugated tube 12 with a corrugated surface to improve heat transfer efficiency, noise generation can be reduced. The heat transfer efficiency to the liquid 2, and therefore the combustion efficiency of the immersion tube heater 1, can be further improved while suppressing the heat transfer.

このように、本発明の浸管ヒータ1の燃焼効率は非常に
高くし得るので、燃焼ガス流路6を短くする等して小型
化しても、充分な加熱作用を維持することができる。
As described above, the combustion efficiency of the immersion tube heater 1 of the present invention can be made very high, so even if the combustion gas flow path 6 is shortened or otherwise miniaturized, a sufficient heating effect can be maintained.

(発明の効果) 以上のように本発明の浸管ヒータはバーナ周囲の管が非
常に高い温度に上昇することがなく安全であり、しかも
騒音の発生を低いレベルに抑えながら、燃焼効率の高い
コンパクトな液体加熱手段を提供し得るという効果があ
る。
(Effects of the Invention) As described above, the immersion tube heater of the present invention is safe because the tube surrounding the burner does not rise to an extremely high temperature, and has high combustion efficiency while suppressing noise generation to a low level. This has the effect of providing a compact liquid heating means.

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

第1図〜第3図は本発明の実施例に対応するもので、第
1図は全体系統図、第2図は要部斜視図、第3図は要部
系統図、第4図は従来例の全体系統図である。 符号1・・・浸管ヒータ、2・・・加熱対象液体、3・
・・燃焼ガス流入口、4・・・燃焼ガス流出口、5・・
・管、6・・・燃焼ガス流路、7・・・バーナ、8・・
・バーナ先端部、9・・・触媒反応部、10・・・担体
、11・・・セラミックハニカム、12・・・コルゲー
ト管、13・・・連通孔。 第  1  tl
Figures 1 to 3 correspond to embodiments of the present invention, where Figure 1 is an overall system diagram, Figure 2 is a perspective view of main parts, Figure 3 is a system diagram of main parts, and Figure 4 is a conventional system diagram. FIG. 2 is an example overall system diagram. Code 1: Immersion tube heater, 2: Liquid to be heated, 3:
... Combustion gas inlet, 4... Combustion gas outlet, 5...
・Pipe, 6... Combustion gas flow path, 7... Burner, 8...
- Burner tip, 9... Catalytic reaction part, 10... Carrier, 11... Ceramic honeycomb, 12... Corrugated pipe, 13... Communication hole. 1st tl

Claims (5)

【特許請求の範囲】[Claims] (1)加熱対象液体内に、燃焼ガス流入口と流出口を有
する管を、該流入口と流出口の双方が前記液体表面より
も上に位置するように、前記液体内に浸漬して、前記液
体内に燃焼ガス流路を形成すると共に、前記燃焼ガス流
入口近傍の管内にバーナを設置した浸管ヒータにおいて
、前記バーナを少くともその先端部が前記加熱対象液体
の液面下になるように設置すると共に、前記燃焼ガス流
路の該バーナよりも下流側適所に、前記燃焼ガスが通過
可能な触媒反応部を構成したことを特徴とする浸管ヒー
タ。
(1) Immersing a pipe having a combustion gas inlet and an outlet in the liquid to be heated, such that both the inlet and the outlet are located above the surface of the liquid; In an immersion tube heater in which a combustion gas flow path is formed in the liquid and a burner is installed in a pipe near the combustion gas inlet, at least the tip of the burner is below the surface of the liquid to be heated. The immersion tube heater is characterized in that the immersion tube heater is installed as shown in FIG.
(2)請求項1記載の触媒反応部の担体は、セラミック
ハニカムで構成したことを特徴とする浸管ヒータ。
(2) An immersion tube heater, wherein the carrier of the catalytic reaction section according to claim 1 is made of a ceramic honeycomb.
(3)請求項1記載の燃焼ガス流路は、触媒反応部より
も下流側を、その上流側よりも細く絞ったことを特徴と
する浸管ヒータ。
(3) The immersion tube heater according to claim 1, wherein the combustion gas flow path is narrower on the downstream side of the catalytic reaction section than on the upstream side thereof.
(4)請求項1記載の触媒反応部の担体は、セラミック
ハニカムで構成すると共に、燃焼ガス流路は触媒反応部
よりも下流側を、その上流側よりも細く絞ったことを特
徴とする浸管ヒータ。
(4) The carrier of the catalytic reaction section according to claim 1 is constructed of a ceramic honeycomb, and the combustion gas flow path is narrower on the downstream side of the catalytic reaction section than on the upstream side. tube heater.
(5)請求項1記載の燃焼ガス流路の触媒反応部よりも
下流側は、コルゲート管で構成したことを特徴とする浸
管ヒータ。
(5) An immersion tube heater, wherein the combustion gas passage according to claim 1, downstream of the catalytic reaction section, is constructed of a corrugated tube.
JP33571389A 1989-12-25 1989-12-25 Immersion tube heater Expired - Fee Related JP2839165B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33571389A JP2839165B2 (en) 1989-12-25 1989-12-25 Immersion tube heater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33571389A JP2839165B2 (en) 1989-12-25 1989-12-25 Immersion tube heater

Publications (2)

Publication Number Publication Date
JPH03195861A true JPH03195861A (en) 1991-08-27
JP2839165B2 JP2839165B2 (en) 1998-12-16

Family

ID=18291645

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33571389A Expired - Fee Related JP2839165B2 (en) 1989-12-25 1989-12-25 Immersion tube heater

Country Status (1)

Country Link
JP (1) JP2839165B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0838635A3 (en) * 1996-10-28 1999-05-19 Carrier Corporation Noise reducing device for combustion driven heating apparatus
WO2001057442A1 (en) * 2000-02-02 2001-08-09 J. Eberspächer Gmbh & Co. Burner system, especially for a heater

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0838635A3 (en) * 1996-10-28 1999-05-19 Carrier Corporation Noise reducing device for combustion driven heating apparatus
WO2001057442A1 (en) * 2000-02-02 2001-08-09 J. Eberspächer Gmbh & Co. Burner system, especially for a heater

Also Published As

Publication number Publication date
JP2839165B2 (en) 1998-12-16

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