JPH01147254A - Forced air supply/exhaust hot air fan - Google Patents

Forced air supply/exhaust hot air fan

Info

Publication number
JPH01147254A
JPH01147254A JP62307860A JP30786087A JPH01147254A JP H01147254 A JPH01147254 A JP H01147254A JP 62307860 A JP62307860 A JP 62307860A JP 30786087 A JP30786087 A JP 30786087A JP H01147254 A JPH01147254 A JP H01147254A
Authority
JP
Japan
Prior art keywords
exhaust gas
heat
exhaust
heat exchanger
humidifying
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
Application number
JP62307860A
Other languages
Japanese (ja)
Inventor
Hitoshi Naganuma
長沼 仁
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 JP62307860A priority Critical patent/JPH01147254A/en
Publication of JPH01147254A publication Critical patent/JPH01147254A/en
Pending legal-status Critical Current

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  • Instantaneous Water Boilers, Portable Hot-Water Supply Apparatuses, And Control Of Portable Hot-Water Supply Apparatuses (AREA)
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Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は排気ガスの放熱損失を小さくするとともに、公
害防止を考慮した強制給排気式温風機に関するものであ
る。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a forced air supply/exhaust hot air fan that reduces the heat radiation loss of exhaust gas and takes pollution prevention into consideration.

従来の技術 従来の一般的な強制給排気式温風機は屋外の空気を使っ
て石油等を燃焼させ、その燃焼熱を温風機内の熱交換器
によって屋内へ取り込み、燃焼によシ生じた排気ガスは
屋外に排出する構成となっていた。
Conventional technology Conventional forced air hot air fans use outdoor air to combust oil, etc., bring the combustion heat indoors through a heat exchanger inside the hot air fan, and then release the exhaust gas produced by the combustion. The gas was configured to be exhausted outdoors.

また、加湿機能を有するものとして、温風機水2 ・ 
−7 体の熱交換器上部に加湿皿を設けたものがあるが、これ
は熱交換器および燃焼室の輻射熱によって加湿皿を加熱
して水を気化させ、室内を加湿するものであった。
In addition, as a device with a humidifying function, hot air machine water 2 ・
-7 There is a model that has a humidifying tray installed above the heat exchanger of the body, and the radiant heat from the heat exchanger and combustion chamber heats the humidifying tray to vaporize water and humidify the room.

発明が解決しようとする問題点 しかしながらこのような強制排気式温風機は高温(12
0′c〜150℃)の排気ガスを直接屋外へ排出してお
り、燃料消費量に対する放熱損失が大きく、さらに環境
的に熱公害をきたす要因にもなっていた。
Problems to be Solved by the Invention However, such forced-exhaust hot-air fans operate at high temperatures (12
Exhaust gas (0'C to 150C) is directly discharged outdoors, resulting in a large heat radiation loss relative to fuel consumption and also causing environmental thermal pollution.

また、排気ガスは給排気部において給気および外気と熱
交換し、排気ガス中の水分が凝縮する。
Furthermore, the exhaust gas exchanges heat with the supply air and outside air in the supply/exhaust section, and moisture in the exhaust gas condenses.

この凝縮水は排気ガス中の窒素酸化物および硫黄酸化物
など溶解し、pH2〜4程度の酸性を呈し、屋外ヘドレ
ンとして排出されるが、この酸性凝縮水は排気管の腐食
を促進するとともに環境汚染の要因ともなっていた。
This condensed water dissolves nitrogen oxides and sulfur oxides in the exhaust gas, has an acidic pH of about 2 to 4, and is discharged as outdoor hedren. It was also a source of pollution.

さらに加湿機能を有するものにおいては熱交換器と加湿
皿の間で熱の移動が効果的でないので加湿皿の温度が低
くて水がほとんど気化されず、加3 /、−7 湿効果はほとんどなかった。
Furthermore, in devices with a humidifying function, heat transfer between the heat exchanger and the humidifying tray is not effective, so the temperature of the humidifying tray is low and almost no water is vaporized, resulting in almost no humidifying effect. Ta.

問題点を解決するだめの手段 本発明の強制給排気式温風機は上記問題点を解決するた
め、排気管内に排気ガスと加湿用水の間で熱交換する熱
交換器を設けるとともに、前記排気管内の熱交換器下部
にマグネシウム合金を配設したものである。
Means for Solving the Problems In order to solve the above-mentioned problems, the forced air supply/exhaust hot air fan of the present invention is provided with a heat exchanger for exchanging heat between exhaust gas and humidifying water in the exhaust pipe, and A magnesium alloy is placed at the bottom of the heat exchanger.

作  用 上記構成において、排気ガスは排気管内に設けられた熱
交換器を介して加湿用水を温める。1だ排気ガスの熱交
換によシ生じた凝縮水はマグネシウム合金により中和さ
れて排水される。
Function In the above configuration, the exhaust gas warms the humidifying water via the heat exchanger provided in the exhaust pipe. Condensed water generated by heat exchange of the exhaust gas is neutralized by the magnesium alloy and drained.

実施例 以下、本発明の一実施例について図面を参照して説明す
る。
EXAMPLE Hereinafter, an example of the present invention will be described with reference to the drawings.

第1図は本実施例の強制排気式温風機の断面図、第2図
は同要部を拡大した断面図である。
FIG. 1 is a cross-sectional view of the forced exhaust hot air fan of this embodiment, and FIG. 2 is an enlarged cross-sectional view of the main parts thereof.

図に示すように、コ・rル型熱交換器1は排気管2内に
設置され、このコイル型熱交換器1は加湿用水タンク3
と加湿皿4に加湿用水管5,6で連結されている。した
がって、加湿用水は加湿用水タンク3から加湿用水管5
.コイル型熱交換器1゜加湿水管6を順に通って加湿皿
4に入る。
As shown in the figure, a coil type heat exchanger 1 is installed in an exhaust pipe 2, and this coil type heat exchanger 1 is connected to a humidifying water tank 3.
and is connected to the humidifying tray 4 through humidifying water pipes 5 and 6. Therefore, the humidifying water flows from the humidifying water tank 3 to the humidifying water pipe 5.
.. The coil type heat exchanger 1° passes through the humidifying water tube 6 in order and enters the humidifying tray 4.

一方、燃焼用空気は給気管7から給気ファン8によって
給気され通気管9を介して燃焼室10に導入される。燃
焼室10では点火ヒータ11によって気化した灯油と上
記燃焼用空気の混合気体に点火する。そして燃焼室10
で生じた排気ガスは熱交換器12を通って排気ファン1
3によって排気管2に送られ、ここでコイル型熱交換器
1と接触して屋外へ排出される。
On the other hand, combustion air is supplied from the air supply pipe 7 by the air supply fan 8 and introduced into the combustion chamber 10 via the ventilation pipe 9. In the combustion chamber 10, an ignition heater 11 ignites the gas mixture of vaporized kerosene and the combustion air. and combustion chamber 10
The exhaust gas generated in the heat exchanger 12 passes through the exhaust fan 1.
3 to the exhaust pipe 2, where it comes into contact with the coil heat exchanger 1 and is discharged outdoors.

捷た、室内内封流用ファン14によって発生する風は本
体内の燃焼室10および熱交換器12と接触して排気ガ
スと熱交換し、屋内へ温風として送られる。
The broken air generated by the indoor confinement fan 14 contacts the combustion chamber 10 and the heat exchanger 12 in the main body, exchanges heat with the exhaust gas, and is sent indoors as warm air.

排気管2内のコイル型熱交換器1の部分で燃焼排ガスと
加湿水が熱交換されて発生する凝縮水は、排気管2の溝
部に取付けたマグネシウム合金15を通過して、屋外ヘ
ドレン水として排出される。
The condensed water generated by heat exchange between combustion exhaust gas and humidifying water in the coil-type heat exchanger 1 in the exhaust pipe 2 passes through the magnesium alloy 15 installed in the groove of the exhaust pipe 2 and is used as outdoor hedrine water. It is discharged.

さらに加温された加湿水は繊維よりなる吸」皿体5−1
−ン 16によって吸い上げられて、室内へ放出される温風と
ともに室内へ供給される。
Furthermore, the heated humidifying water is absorbed by the fiber body 5-1.
- The air is sucked up by the air vent 16 and supplied into the room along with the warm air that is discharged into the room.

次に上述した構成による作用効果について説明する。Next, the effects of the above-described configuration will be explained.

排気管2内で加湿水と燃焼排ガスとの温度差を利用して
熱交換するコイル型熱交換器1は、排ガス熱量Q、(l
al)、排気ガス量mcKp:)、排ガスの定圧比熱C
p(cal/に9・”C,)  、排ガス温度T2〔℃
〕、熱交換によって冷却される排ガス温度Tx〔℃〕と
の間には次の(I)式が成立する。
The coil type heat exchanger 1 exchanges heat using the temperature difference between humidifying water and combustion exhaust gas in the exhaust pipe 2, and the exhaust gas heat quantity Q, (l
al), exhaust gas amount mcKp:), constant pressure specific heat C of exhaust gas
p (cal/9・"C,), exhaust gas temperature T2 [℃
] and the exhaust gas temperature Tx [° C.] cooled by heat exchange, the following equation (I) holds true.

Q−mCp(T2−Tx)   ・・・・旧・・(I)
−例として、150〔℃〕 の排気ガスを20C℃)の
水で熱交換し、その熱交換条件を次のように設定した場
合冷却されて排出ガス温度は約40 [℃:IIとなる
Q-mCp (T2-Tx)...Old...(I)
- As an example, if exhaust gas at 150[°C] is heat exchanged with water at 20[°C] and the heat exchange conditions are set as follows, the exhaust gas temperature will be approximately 40[°C:II] after being cooled.

熱交換器:コイル型熱交換器 熱交換器の伝熱面積:01〔扉〕 排気ガスの流量: 10 t31/h ’)壕だ排出さ
れる排気ガスから水分を除いた乾排ガスの保有熱量は次
の(n)式のようになる。
Heat exchanger: Coil type heat exchanger Heat transfer area of heat exchanger: 01 [door] Flow rate of exhaust gas: 10 t31/h') The amount of heat retained in the dry exhaust gas after removing moisture from the exhaust gas discharged from the trench is The following equation (n) is obtained.

6  /、−: ただしくn)式において、 L   :乾排気ガスの保有熱量(1cal/Kg:]
(C):燃料中の炭素質量比〔%〕 (CO2):排気ガス中の二酸化旋素容積比〔%〕(C
○):排気ガス中の一酸化炭素容積比〔%〕Cp  :
排ガスの定圧比熱CmVKグ・℃〕tq  :排気温度
〔℃〕 ta  :給気温度(’C) である。
6 /, -: where n) In the formula, L: Heat capacity of dry exhaust gas (1cal/Kg:]
(C): Carbon mass ratio in fuel [%] (CO2): Volume ratio of carbon dioxide in exhaust gas [%] (C
○): Volume ratio of carbon monoxide in exhaust gas [%] Cp:
Constant-pressure specific heat of exhaust gas CmVKg·°C] tq: Exhaust temperature [°C] ta: Supply air temperature ('C).

(II)式より排ガス温度に比例して放熱損失も大きく
なることがわかる。例として、15oc”c’)と40
〔℃〕の排ガスを上記(II)式にあてはめてみると1
50C℃)の場合は損失熱量が40 (℃〕の場合の約
4倍となる。
It can be seen from equation (II) that the heat radiation loss also increases in proportion to the exhaust gas temperature. For example, 15oc"c') and 40
Applying the exhaust gas at [℃] to the above equation (II), we get 1
When the temperature is 50℃, the amount of heat loss is about four times that when the temperature is 40℃.

すなわち、本実施例では加湿用水の熱交換によって排ガ
ス温度を低下させることができるので熱損失が少なく、
しかも熱的な公害をおこすことはなく、さらにとの熱交
換によシ加湿用水の温度が7・へ−−1 」−昇するので、室内へ加湿する水の蒸発か促進される
In other words, in this embodiment, the exhaust gas temperature can be lowered by heat exchange with the humidifying water, so there is less heat loss.
Moreover, it does not cause thermal pollution, and the temperature of the humidifying water increases by 7 to 1 inch due to heat exchange with the humidifying water, thereby promoting the evaporation of the water humidifying the room.

寸だ、この排ガスの熱交換により生じた凝縮水はマグネ
シウム合金と(In)式に示す化学反応によって中和さ
れ、ドレン水による環境汚染が防止されるものである。
In fact, the condensed water generated by heat exchange of the exhaust gas is neutralized by the chemical reaction shown in the formula (In) with the magnesium alloy, thereby preventing environmental pollution due to drain water.

Mg+2HNO→H2→Mg(NO3)2・・(Ill
)発明の効果 以上の実施例の説明より明らかなように、本発明の強制
給排気式温風機は、排気ガスの熱を加湿用水の加温のた
めに用いることによシ放熱損失を抑え、熱効率が向上す
る。したがって屋外に放出される熱量も減少するのて環
境に対する熱公害も少なくなる。
Mg+2HNO→H2→Mg(NO3)2...(Ill
) Effects of the Invention As is clear from the above description of the embodiments, the forced air supply/exhaust hot air fan of the present invention suppresses heat radiation loss by using the heat of the exhaust gas to heat the humidifying water. Improves thermal efficiency. Therefore, the amount of heat released outdoors is also reduced, which reduces thermal pollution to the environment.

さらに排気ガス中の水分が凝縮した酸性の凝縮水は排気
管の熱交換器下部に設けたマグネシウム合金によシ中和
されて屋外に排水されるため、環境汚染が抑えられる。
Furthermore, the acidic condensed water produced by the condensation of water in the exhaust gas is neutralized by a magnesium alloy installed at the bottom of the heat exchanger in the exhaust pipe and drained outdoors, thereby reducing environmental pollution.

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

第1図は本発明の一実施例を示す強制給排気式温風機の
構成図、第2図は同要部の拡大構成図である。 1・・・・・・コイル型熱交換器、2・・・・・・排気
管、3・・・・・加湿用水タンク、4・・・・・・加湿
皿、5,6・・・・・・加湿用水管、15・・・・・・
マグネシウム合金。
FIG. 1 is a configuration diagram of a forced air supply/exhaust hot air fan showing an embodiment of the present invention, and FIG. 2 is an enlarged configuration diagram of the main parts thereof. 1... Coil type heat exchanger, 2... Exhaust pipe, 3... Humidifying water tank, 4... Humidifying plate, 5, 6...・・Humidifying water pipe, 15・・・・・・
Magnesium alloy.

Claims (1)

【特許請求の範囲】[Claims] 排気管内に排気ガスと加湿用水の間で熱交換をする熱交
換器を設けるとともに、前記排気管内の熱交換器の下部
にマグネシウム合金を配設した強制給排気式温風機。
A forced air supply/exhaust type hot air fan in which a heat exchanger for exchanging heat between exhaust gas and humidifying water is provided in an exhaust pipe, and a magnesium alloy is disposed below the heat exchanger in the exhaust pipe.
JP62307860A 1987-12-04 1987-12-04 Forced air supply/exhaust hot air fan Pending JPH01147254A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62307860A JPH01147254A (en) 1987-12-04 1987-12-04 Forced air supply/exhaust hot air fan

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62307860A JPH01147254A (en) 1987-12-04 1987-12-04 Forced air supply/exhaust hot air fan

Publications (1)

Publication Number Publication Date
JPH01147254A true JPH01147254A (en) 1989-06-08

Family

ID=17974041

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62307860A Pending JPH01147254A (en) 1987-12-04 1987-12-04 Forced air supply/exhaust hot air fan

Country Status (1)

Country Link
JP (1) JPH01147254A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012057822A (en) * 2010-09-06 2012-03-22 Corona Corp Exhauster
US10465286B2 (en) 2002-07-23 2019-11-05 Entegris, Inc. Method and apparatus to help promote contact of gas with vaporized material

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10465286B2 (en) 2002-07-23 2019-11-05 Entegris, Inc. Method and apparatus to help promote contact of gas with vaporized material
JP2012057822A (en) * 2010-09-06 2012-03-22 Corona Corp Exhauster

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