JPS62142961A - Heat exchanger for use in water heater - Google Patents

Heat exchanger for use in water heater

Info

Publication number
JPS62142961A
JPS62142961A JP28480585A JP28480585A JPS62142961A JP S62142961 A JPS62142961 A JP S62142961A JP 28480585 A JP28480585 A JP 28480585A JP 28480585 A JP28480585 A JP 28480585A JP S62142961 A JPS62142961 A JP S62142961A
Authority
JP
Japan
Prior art keywords
drum
heat exchanger
heat
burner
supplied
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
JP28480585A
Other languages
Japanese (ja)
Other versions
JPH0638003B2 (en
Inventor
Mitsuyoshi Nakamoto
中本 充慶
Kenya Okamoto
岡本 ▲けん▼也
Yoshihisa Oda
小田 善久
Norio Kawabata
川端 教男
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 JP28480585A priority Critical patent/JPH0638003B2/en
Publication of JPS62142961A publication Critical patent/JPS62142961A/en
Publication of JPH0638003B2 publication Critical patent/JPH0638003B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

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

Abstract

PURPOSE:To increase the cooling effect of the titled heat exchanger to reduce the heat storage quantity of a drum and to prevent after-heating after fire extinguishment of a burner by using gas-permeable ceramics consisting of a honey-comb structure for the drum of the heat exchanger, and aligning the direction of cells of the honey-comb structure in the direction of a combustion gas. CONSTITUTION:A combustion gas supplied to a burner 4 forms a flame 10 on a burner, and made into a combustion gas 9 which is supplied to a fin tube heat exchanger 2 to heat water 8 to be heated. The thus heated water is utilized as hot water. A part of heat generated by the burner is supplied to a combustion drum 3. A material used for the drum 3 is ceramics which form a honey-comb structure 12. Cool air 17 within the cells 16 of the honey-comb structure is heated and obtains bouyancy and rises up. Accordingly, cool air brings away heat supplied to the drum 3. Therefore, the heat storage quantity of the drum 3 is small, and after-heating when the burner and the heating of water are stopped is prevented.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は家庭用あるいは業務用等の湯沸器用熱交換器に
関するものである。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a heat exchanger for water heaters for domestic or commercial use.

従来の技術 熱交換器とこの周囲に筒状のドラムを位置させて燃焼室
を構成し、ドラムの周囲には熱交換用チューブを巻き、
材質として銅を用いる事が多い。加熱水はドラムの周囲
の熱交換用チューブとフィンチューブ熱交換器により熱
を受け、湯として利用されていた。
Conventional technology A combustion chamber is constructed by placing a heat exchanger and a cylindrical drum around the heat exchanger, and a heat exchange tube is wrapped around the drum.
Copper is often used as the material. The heated water received heat from the heat exchange tubes surrounding the drum and the fin tube heat exchanger, and was used as hot water.

発明が解決しようとする問題点 このような熱交換器に於いて、バーナを燃焼室の入口に
位置し、バーナ上に形成する火炎の燃焼熱が利用される
。出湯時に湯を止めると、熱交換器に残った湯の温度は
上昇を続ける。この現象は一般に後沸きと云われており
、熱交換器に蓄熱された燃焼熱が水温を上昇させていた
ものと思われる。この後沸きは利用者が再び湯を利用す
る時に、はじめに高温の湯が出る為に、火傷の原因にな
り、安全上問題が多い。
Problems to be Solved by the Invention In such a heat exchanger, a burner is located at the entrance of a combustion chamber, and combustion heat from a flame formed on the burner is utilized. If the hot water is turned off during taping, the temperature of the hot water remaining in the heat exchanger continues to rise. This phenomenon is generally referred to as after-boiling, and it is thought that the combustion heat stored in the heat exchanger caused the water temperature to rise. After boiling, when the user uses the hot water again, the hot water first comes out, which can cause burns and pose many safety problems.

一方、筒状のドラムをセラミックで構成する方法がとら
れだした。これは、熱交換器の小型化と耐久性の向上を
目的としたものである。しがしな≠ヌへ ?″のセラタ
、1.クス珀1rI汁1快博赴砧;曹勅イ君バーナ消火
後もこの熱がフィンチューブ内の水を加熱し、前記欠点
は解消されない。
On the other hand, a method of constructing a cylindrical drum out of ceramic has begun to be used. This is aimed at downsizing the heat exchanger and improving its durability. Shigashina≠nuhe? Even after the burner is extinguished, this heat still heats the water in the fin tube, and the above drawbacks cannot be solved.

本発明はドラムの蓄熱を少くし、後沸き現象を防止する
ものである。
The present invention reduces heat accumulation in the drum and prevents the after-boiling phenomenon.

問題点を解決するための手段 そして上記問題点を解決する本発明の技術的な手段は、
上記熱交換器のドラムにハニカム構造からなる通気性セ
ラミックスを使用し、ハニカムを構成するセルを適当な
方向に位置づけ、セラミックスの表面をち密にして通気
性をなくしている。
Means for solving the problems and technical means of the present invention for solving the above problems are as follows:
Air-permeable ceramics having a honeycomb structure are used for the drum of the heat exchanger, and the cells constituting the honeycomb are positioned in appropriate directions to make the surface of the ceramic dense and eliminate air permeability.

そしてハニカムの上流側は冷却空気が流入できる様に外
気に開放されている。
The upstream side of the honeycomb is open to the outside air so that cooling air can flow into it.

作  用 バーナで燃焼した火炎から発生した熱の一部はふく射で
、一部は燃焼ガスの熱伝達でドラムに供給される。そし
て大部分の熱はフィンチューブ熱交換器に供給される。
Some of the heat generated from the flame burned in the working burner is radiated, and some is supplied to the drum by heat transfer from the combustion gas. Most of the heat is then supplied to the fin-tube heat exchanger.

この時、ドラムに供給された熱はドラムのハニカム部の
空気を加熱する。その為、空気は浮力により上方に流れ
て、セラミックスの熱を奪う。この時、セラミックスの
表面はち密にしているため、ドラム内の気流と外部の気
流とはしゃ断され、外部への熱の損失は少い。またドラ
ム内の空気の浮力効果は大きくドラムの温度上昇は小さ
い。
At this time, the heat supplied to the drum heats the air in the honeycomb portion of the drum. Therefore, the air flows upward due to buoyancy and absorbs heat from the ceramics. At this time, since the surface of the ceramic is dense, the airflow inside the drum is cut off from the airflow outside, and there is little loss of heat to the outside. Furthermore, the buoyancy effect of the air within the drum is large and the temperature rise in the drum is small.

従って、ドラムの蓄熱量は小さく、前述の後沸き現象の
防止が容易になる。
Therefore, the amount of heat stored in the drum is small, and the above-mentioned after-boiling phenomenon can be easily prevented.

実施例 以下本発明の一実施例を添付図面にもとすいて説明する
EXAMPLE An example of the present invention will be described below with reference to the accompanying drawings.

第1図において、1は熱交換器本体、2はフィンチュー
ブ熱交換器、3は筒状のドラム、4は熱交換器本体1を
加熱するバーナである。熱交換器本体1はフィンチュー
ブ熱交換器2とドラム3からなシ、燃焼室6を構成して
いる。
In FIG. 1, 1 is a heat exchanger body, 2 is a fin tube heat exchanger, 3 is a cylindrical drum, and 4 is a burner for heating the heat exchanger body 1. In FIG. The heat exchanger main body 1 includes a fin-tube heat exchanger 2 and a drum 3, and constitutes a combustion chamber 6.

フィンチューブ熱交換器2は多数の平板状のフィン6と
これに直交して蛇行状に配列した水パイプ7から構成さ
れており、水パイプ7には加熱水8が流れ、バーナ4上
で発生した高温の燃焼ガス9により加熱され、湯として
利用される。
The fin tube heat exchanger 2 is composed of a large number of flat fins 6 and water pipes 7 arranged in a meandering manner perpendicular to the fins 6. Heated water 8 flows through the water pipes 7, and the heat generated on the burner 4 is heated. It is heated by the high-temperature combustion gas 9 and used as hot water.

第2図は熱交換器本体1とバーナ4の組立図であシ、第
1図のA−AI!′r面に相当する。10は火炎である
。11は外装の一部である。
Figure 2 is an assembly diagram of the heat exchanger main body 1 and burner 4, and A-AI in Figure 1! 'r plane. 10 is a flame. 11 is a part of the exterior.

第3図はドラム3の一部の詳細図である。ドラム3の材
質はセラミックスであシ、ハニカム構造体12となって
いる。−例として、ハニカム構造体は次のように製造さ
れる。波状シート13と板状シート14を接着してコル
ゲートシートを成形し、各シートの壁をセル壁16とし
て多数のセル16を構成し、ハニカム構造体とする。セ
ル内には冷却空気17が通過する。
FIG. 3 is a detailed view of a portion of the drum 3. The drum 3 is made of ceramic and has a honeycomb structure 12. - By way of example, a honeycomb structure is manufactured as follows. A corrugated sheet is formed by bonding a corrugated sheet 13 and a plate-like sheet 14, and a large number of cells 16 are formed by using the walls of each sheet as cell walls 16 to form a honeycomb structure. Cooling air 17 passes through the cell.

ドラム3のセル16は波状シート13と板状シート14
との空隙であり、セル16は燃焼室の入口18から始ま
り出口19で終了する間に位置している。ドラム3の内
表面20は燃焼室5に、外表面21は大気に開放されて
いる。セラミックスはアルミナ繊維を主成分とし、波状
シートと板状シートによりコルゲートに成形する。この
成形物の表面にセラミックスの粉末を水に懸濁させたス
ラリーを塗布し、空気中に於て1250’Cで焼成する
。この成形物は表面が、ち密で通気性はなく、焼成後の
気孔率は40〜95チとなる。
The cells 16 of the drum 3 are composed of a corrugated sheet 13 and a plate-like sheet 14.
The cell 16 is located between the inlet 18 and the outlet 19 of the combustion chamber. The inner surface 20 of the drum 3 is open to the combustion chamber 5, and the outer surface 21 is open to the atmosphere. The main component of ceramics is alumina fiber, which is formed into a corrugated form using corrugated sheets and plate-like sheets. A slurry of ceramic powder suspended in water is applied to the surface of the molded product, and the molded product is fired at 1250'C in air. The surface of this molded product is dense and has no air permeability, and the porosity after firing is 40 to 95 inches.

次に、この一実施例の構造における作用を説明する。バ
ーナ4に供給された燃焼ガスはバーナ上で火炎1oを形
成し、高温の燃焼ガス9となって、フィンチューブ熱交
換器2に供給され、加熱水8を加熱し、湯として利用さ
れる。バーナで発生した熱の一部はふく射として、他の
一部は高温の燃焼ガスの熱伝達により、ドラム3に供給
される。
Next, the operation of the structure of this embodiment will be explained. The combustion gas supplied to the burner 4 forms a flame 1o on the burner, becomes high-temperature combustion gas 9, is supplied to the fin tube heat exchanger 2, heats the heated water 8, and is used as hot water. Part of the heat generated by the burner is supplied to the drum 3 as radiation, and the other part is supplied to the drum 3 by heat transfer from the high-temperature combustion gas.

この熱はハニカム構造体のセル1e内の冷却空気17を
加熱する。冷却空気は浮力を得て上昇する。
This heat heats the cooling air 17 within the cells 1e of the honeycomb structure. The cooling air gains buoyancy and rises.

従って、ドラム3に供給された熱を冷却空気で持ち去る
のでドラムの蓄熱量は小さい。
Therefore, since the heat supplied to the drum 3 is carried away by the cooling air, the amount of heat stored in the drum is small.

火炎あるいは高温の燃焼ガスからドラムの内表面20に
熱が供給される。表面はち密になっているので、分子拡
散等の気体の流入流出による熱の移動はない。熱の移動
はふく射によるものがほとんどである。そして、この熱
は波状シート13に伝えられる。
Heat is supplied to the inner surface 20 of the drum from the flame or hot combustion gases. Since the surface is dense, there is no heat transfer due to gas inflow or outflow due to molecular diffusion. Most of the heat transfer is due to radiation. This heat is then transferred to the corrugated sheet 13.

この時、冷却空気は板状シート14と波状シート13か
ら熱を奪うが、波状シートは表面積が太きい。従って、
セル16を通過する冷却空気17の持去る熱量は大きい
。また、セル16の周囲のセル壁はセラミックスの断熱
材で構成されているため、冷却空気の浮力を充分に生か
している。シートの気孔率は大きい為に、セラミックス
のシートの内部には冷却空気が流れる。その結果、ドラ
ム外表面21の温度上昇は小さい。
At this time, the cooling air removes heat from the plate-like sheet 14 and the corrugated sheet 13, but the corrugated sheet has a large surface area. Therefore,
The amount of heat carried away by the cooling air 17 passing through the cells 16 is large. Further, since the cell wall around the cell 16 is made of a ceramic heat insulating material, the buoyancy of the cooling air is fully utilized. Since the sheet has a large porosity, cooling air flows inside the ceramic sheet. As a result, the temperature increase on the drum outer surface 21 is small.

また、ドラム3はハニカム構造体12であり、更に表面
はち密であることから構造上強度が大きい。
Further, the drum 3 is a honeycomb structure 12 and has a dense surface, so it has a high structural strength.

第2図に於いて、ドラム3の出口19はフィンチューブ
熱交換器2に位置しており、燃焼ガスが通過する際、冷
却空気17を吹い込むと同時に、加熱された冷却空気を
フィンチューブ熱交換器2で吸熱する。冷却空気17は
セル16内で浮力を受け、更にフィンチューブ熱交換器
で吸引されるため、セル内の流速が大きくなり、セルで
熱を充分に奪う事ができ、外表面の温度は低い。
In FIG. 2, the outlet 19 of the drum 3 is located in the fin tube heat exchanger 2, and when the combustion gas passes through, cooling air 17 is blown into the fin tube heat exchanger 2. Heat is absorbed by exchanger 2. Since the cooling air 17 receives buoyancy within the cell 16 and is further sucked by the fin-tube heat exchanger, the flow velocity within the cell increases, heat can be sufficiently removed by the cell, and the temperature of the outer surface is low.

また、ドラムの外表面が低いため、外装置1との距離を
小さくでき、湯沸器を小形にする事が容易である。
Furthermore, since the outer surface of the drum is low, the distance from the outer device 1 can be shortened, making it easy to make the water heater compact.

次に本発明の他の実施例について説明する。Next, other embodiments of the present invention will be described.

第4図は他の実施例を示しており、この実施例のドラム
の出口22はフィンチューブ熱交換器23の外側に位置
している。このような構造ではドラム24のセル25内
を通過する冷却空気26はドラム出口22から大気に開
放されるため、バーナ及び加熱水を止めた時の後沸きを
更に防止することが可能である。
FIG. 4 shows another embodiment in which the drum outlet 22 is located outside the fin-tube heat exchanger 23. In such a structure, since the cooling air 26 passing through the cells 25 of the drum 24 is released to the atmosphere from the drum outlet 22, it is possible to further prevent after-boiling when the burner and heated water are stopped.

発明の効果 本発明は湯沸器用熱交換器のドラム部にセラミックスの
材質でハニカム構造体を形成し、ドラム部の表面はち密
で通気性はなく、内部は通気性を有し、ハニカム構造体
のセルの方向を燃焼ガスの方向に位置させたものであり
、次の様な効果が得られる。
Effects of the Invention The present invention forms a honeycomb structure in the drum part of a heat exchanger for a water heater using a ceramic material. The direction of the cell is located in the direction of the combustion gas, and the following effects can be obtained.

(1)、バーナから受ける熱を少くし、熱容量の小さイ
ハニカム構造体からなるドラムの空隙部を冷却空気が通
過して、ドラムの熱を奪う事から、ドラムの蓄熱量は小
さく、バーナ消火後の後沸きを防止できる。
(1) The amount of heat stored in the drum is small because the heat received from the burner is reduced, and the cooling air passes through the voids of the drum, which is made of a honeycomb structure with a small heat capacity, and takes away the heat from the drum. After-boiling can be prevented.

(2)、ハニカム構造体であり、通気性を大きくし、表
面をちiにしている事から、軽量で機械強度を充分に保
持できる。
(2) Since it is a honeycomb structure with high air permeability and a hard surface, it is lightweight and has sufficient mechanical strength.

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

第1図は本発明の湯沸器用熱交換器の一実施例における
分解斜視図、第2図は同縦断面図、第3図は同ドラムの
壁を構成する要部斜視図、第4図は同他の実施例の縦断
面図である。 1・・・・・・熱交換器本体、2・・・・・・フィンチ
ューブ熱交換器、3・・・・・・ドラム、4・・・・・
・バーナ、16・・・・・・セル。 代理人の氏名 弁理士 中 尾 敏 男 ほか1名/−
−−熱久長各ト惨  σ〜 赤丸!2−−− 74/f
−7’M=又泉S−6−−− 7(73−m−ドラム 
       7−−− 氷、バイア4− 八−16−
η12絶ホ、 第 1 図                    
q−m−房、!L刀″ス70−−一 入夫 /I−−−クトA長− 18−人口 −q−出口 第 2 図              20−  門
人匍2/−−−外表釦 z2−一一ドフム土口
FIG. 1 is an exploded perspective view of an embodiment of the heat exchanger for a water heater of the present invention, FIG. 2 is a vertical sectional view of the same, FIG. 3 is a perspective view of the main parts constituting the wall of the drum, and FIG. 4 FIG. 2 is a longitudinal cross-sectional view of another embodiment. 1... Heat exchanger body, 2... Fin tube heat exchanger, 3... Drum, 4...
・Burna, 16...Cell. Name of agent: Patent attorney Toshio Nakao and 1 other person/-
−−Etsukyunaga all the misery σ~ Akamaru! 2---74/f
-7'M = Mataizumi S-6--- 7 (73-m-drum
7---- Ice, Bahia 4- 8-16-
η12 absolute ho, Fig. 1
q-m-fusa,! L sword's 70--1 Irio/I--Kut A chief-18-Population-q-Exit 2 Figure 20-Monnin 匍2/---Outer button z2-11 Dohumu Doguchi

Claims (2)

【特許請求の範囲】[Claims] (1)ドラムとフィンチューブ熱交換器とにより燃焼室
を構成する湯沸器用熱交換器に於て、ドラムは複数のセ
ルを有する多孔質セラミックスからなるハニカム構造体
からなり、各セルは熱交換器の燃焼ガスの流れの方向に
位置し、ドラムを形成する多孔質セラミックスの表面を
ち密構造にした事を特徴とする湯沸器用熱交換器。
(1) In a water heater heat exchanger in which a combustion chamber is configured by a drum and a fin-tube heat exchanger, the drum is made of a honeycomb structure made of porous ceramics having multiple cells, and each cell is a heat exchanger. A heat exchanger for a water heater, which is located in the direction of the flow of combustion gas in the water heater, and is characterized by having a porous ceramic surface that forms a drum and has a dense structure.
(2)多孔質のセラミック スの気孔率を40%〜95%とし、表面は通気性のない
薄い層とする特許請求の範囲第1項記載の湯沸器用熱交
換器。
(2) The heat exchanger for a water heater according to claim 1, wherein the porous ceramic has a porosity of 40% to 95%, and the surface is a thin layer with no air permeability.
JP28480585A 1985-12-18 1985-12-18 Heat exchanger for water heater Expired - Lifetime JPH0638003B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28480585A JPH0638003B2 (en) 1985-12-18 1985-12-18 Heat exchanger for water heater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28480585A JPH0638003B2 (en) 1985-12-18 1985-12-18 Heat exchanger for water heater

Publications (2)

Publication Number Publication Date
JPS62142961A true JPS62142961A (en) 1987-06-26
JPH0638003B2 JPH0638003B2 (en) 1994-05-18

Family

ID=17683239

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28480585A Expired - Lifetime JPH0638003B2 (en) 1985-12-18 1985-12-18 Heat exchanger for water heater

Country Status (1)

Country Link
JP (1) JPH0638003B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2022533064A (en) * 2019-05-16 2022-07-21 厦門蜂涛陶瓷有限公司 Thermal energy recovery device and non-contact heating pneumatic electronic cigarette heater equipped with it

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2022533064A (en) * 2019-05-16 2022-07-21 厦門蜂涛陶瓷有限公司 Thermal energy recovery device and non-contact heating pneumatic electronic cigarette heater equipped with it

Also Published As

Publication number Publication date
JPH0638003B2 (en) 1994-05-18

Similar Documents

Publication Publication Date Title
JPS6235013B2 (en)
JP2682362B2 (en) Exhaust heat recovery type combustion device
CN211695439U (en) Gas water heater
JPS62142961A (en) Heat exchanger for use in water heater
JPH0159520B2 (en)
JPS62125259A (en) Heat exchanger for use in water heater
JP3106124B2 (en) Combustion air preheating method and honeycomb-shaped heat storage body
JPH0213884Y2 (en)
JPH0739880B2 (en) Fluid heating device
JP7316669B2 (en) Thermal storage warm air heater
JPS6261643B2 (en)
JPS6135340Y2 (en)
JPH0118965B2 (en)
JPH0229959B2 (en) NETSUKOKANKI
JP2529473B2 (en) Heating device
JP2580581Y2 (en) Heating system
JPH0616281Y2 (en) Exhaust heat recovery device
JPS6096851A (en) Hot water supply device
JPS63279052A (en) Improved fluid heating device
JPH0157243B2 (en)
JPS62233639A (en) Fluid heating apparatus
JPH0221702Y2 (en)
JPH01123950A (en) Fan-driven heater
JPS63210513A (en) Improved fluid heating device
JPS63251751A (en) Device for heating fluid