JP2002333212A - Water heater - Google Patents

Water heater

Info

Publication number
JP2002333212A
JP2002333212A JP2001134809A JP2001134809A JP2002333212A JP 2002333212 A JP2002333212 A JP 2002333212A JP 2001134809 A JP2001134809 A JP 2001134809A JP 2001134809 A JP2001134809 A JP 2001134809A JP 2002333212 A JP2002333212 A JP 2002333212A
Authority
JP
Japan
Prior art keywords
drain
heat exchanger
water heater
combustion gas
heat
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
JP2001134809A
Other languages
Japanese (ja)
Other versions
JP4710164B2 (en
Inventor
Shinya Nakajima
真也 中島
Tomohiro Ichikawa
智浩 市川
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.)
Paloma Kogyo KK
Original Assignee
Paloma Kogyo KK
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 Paloma Kogyo KK filed Critical Paloma Kogyo KK
Priority to JP2001134809A priority Critical patent/JP4710164B2/en
Publication of JP2002333212A publication Critical patent/JP2002333212A/en
Application granted granted Critical
Publication of JP4710164B2 publication Critical patent/JP4710164B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24HFLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H8/00Fluid heaters characterised by means for extracting latent heat from flue gases by means of condensation
    • F24H8/003Fluid heaters characterised by means for extracting latent heat from flue gases by means of condensation having means for moistening the combustion air with condensate from the combustion gases
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Instantaneous Water Boilers, Portable Hot-Water Supply Apparatuses, And Control Of Portable Hot-Water Supply Apparatuses (AREA)
  • Details Of Fluid Heaters (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a water heater that does not require neutralizing treatment on drains and is high in thermal efficiency. SOLUTION: Since the drain generated from the auxiliary heat exchanger 8 of this water heater is evaporated by means of a drain evaporator 9, this water heater does not discharge the drain to the outside and, accordingly, does not require neutralizing treatment on the drain. In addition, since almost all of the sensible heat in combustion gas is recovered by means of a main heat exchanger 7, the auxiliary heat exchanger 8, and a wound pipe 20, the thermal efficiency of this water heater is improved greatly. Moreover, since the combustion gas can also be introduced smoothly to the upper part of an auxiliary heat transfer pipe 8a in which the flow of the combustion gas is disturbed by the drain evaporator 9, the heat exchange in the upper part is activated and the thermal efficiency of this water heater can be improved further.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、燃焼ガスにより通
水を加熱する熱交換器を備えた湯沸器に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water heater provided with a heat exchanger for heating water flow with combustion gas.

【0002】[0002]

【従来の技術】従来から、台所等で主に使用される瞬間
湯沸器としては、給水管及び出湯管が接続される熱交換
器と、この熱交換器を加熱するバーナとを備え、バーナ
の燃焼により熱交換器で通水を加熱し、出湯管より出湯
するものが一般的に知られている。こうした湯沸器で
は、熱交換器にドレン(凝縮水)が発生することを防止
するために、熱交換器からかなり高温の燃焼ガスを排出
しており高い熱効率が得られていない。ドレンは、燃焼
ガスが露点(およそ50〜60℃)以下になると発生す
るものであるから、原理的には、熱交換器でドレンを発
生させずに露点まで熱交換して、燃焼ガス中の顕熱を回
収することが可能である。しかしながら、熱交換器には
通水部である伝熱管のような局所的な低温部が存在する
ので、実際には、低温部での部分的なドレン発生を防ぐ
ために、燃焼ガスをかなりの高温で排出しなければなら
ず、十分な顕熱を回収ができていない。
2. Description of the Related Art Conventionally, an instantaneous water heater mainly used in a kitchen or the like includes a heat exchanger to which a water supply pipe and a tapping pipe are connected, and a burner for heating the heat exchanger. It is generally known that water is heated by a heat exchanger by the combustion of water and is discharged from a tapping pipe. In such a water heater, in order to prevent generation of drain (condensed water) in the heat exchanger, a considerably high temperature combustion gas is discharged from the heat exchanger, and high heat efficiency is not obtained. Drain is generated when the combustion gas falls below the dew point (approximately 50 to 60 ° C.). Therefore, in principle, the heat exchanger exchanges heat to the dew point without generating drain to generate heat in the combustion gas. It is possible to recover sensible heat. However, in the heat exchanger, there is a local low-temperature part such as a heat transfer tube that is a water passage part.In practice, in order to prevent partial drainage in the low-temperature part, the combustion gas is heated to a considerably high temperature. And sufficient sensible heat has not been recovered.

【0003】ところで、浴槽へ給湯したり、シャワー等
へ大量にお湯を供給する大出力の給湯器では、燃焼ガス
流路中の上流側に主に顕熱回収を目的とした主熱交換器
を、下流側に主に潜熱回収を目的とした副熱交換器を設
けて高い熱効率を得る潜熱回収型給湯器が一般的に知ら
れている。このような潜熱回収型給湯器では、副熱交換
器で主熱交換器で回収できなかった顕熱に加え、燃焼ガ
ス温が露点以下になるとドレンが発生するため潜熱も回
収することができる。このため、燃焼ガス中のほとんど
の熱エネルギー(顕熱+潜熱)を回収できるので非常に
高い熱効率を達成することが可能である。
Meanwhile, in a high-power water heater for supplying hot water to a bathtub or supplying a large amount of hot water to a shower or the like, a main heat exchanger mainly for recovering sensible heat is provided upstream in a combustion gas flow path. In general, a latent heat recovery type water heater that obtains high thermal efficiency by providing a sub heat exchanger mainly for the purpose of latent heat recovery on the downstream side is generally known. In such a latent heat recovery type water heater, in addition to the sensible heat that could not be recovered by the main heat exchanger in the sub heat exchanger, when the temperature of the combustion gas falls below the dew point, drain is generated, so that the latent heat can be recovered. For this reason, since most of the thermal energy (sensible heat + latent heat) in the combustion gas can be recovered, it is possible to achieve extremely high thermal efficiency.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、凝縮し
たドレンが燃焼ガス中の硫黄(S)や窒素(N)と反応
してpH3程度の酸性になるため、上述したような潜熱
回収型の器具では、下水道等の一般排水通路に排出する
前に中和処理をしなければならず、中和器を備える等器
具の構造が複雑になり製造コストが高くなってしまう。
そこで、本発明の湯沸器は上記課題を解決し、ドレン排
水の中和処理が不要な高熱効率の湯沸器を提供すること
を目的とする。
However, since the condensed drain reacts with sulfur (S) and nitrogen (N) in the combustion gas to become acidic at a pH of about 3, the above-described latent heat recovery type appliance is used. In addition, a neutralization process must be performed before the wastewater is discharged to a general drainage passage such as a sewage system, which complicates the structure of a device including a neutralizer and increases the manufacturing cost.
Therefore, an object of the present invention is to solve the above-described problem and to provide a water heater with high thermal efficiency that does not require a neutralization treatment of drain water.

【0005】[0005]

【課題を解決するための手段】上記課題を解決する本発
明の請求項1記載の湯沸器は、燃焼室内で燃料を燃焼す
るバーナと、上記バーナの上方に設けられ、該バーナの
燃焼ガスから顕熱を回収して伝熱管内の通水を加熱する
主熱交換器と、上記主熱交換器の上方に設けられ、該主
熱交換器を通過した燃焼ガスから該主熱交換器で回収し
きれなかった顕熱に加えて、潜熱を回収して伝熱管内の
通水を加熱する副熱交換器とを備えた湯沸器において、
上記副熱交換器の下方で上記主熱交換器の上方に設けら
れ、上記副熱交換器での潜熱回収によって発生したドレ
ンを受けると共に該ドレンを燃焼ガスにより加熱して蒸
発させるドレン蒸発器と、上記ドレン蒸発器の横を流れ
る上記主熱交換器を通過した燃焼ガスを、上記副熱交換
器の伝熱管に向けて案内する整流板とを備えることを要
旨とする。
According to a first aspect of the present invention, there is provided a water heater, comprising: a burner for burning fuel in a combustion chamber; and a burner gas provided above the burner. And a main heat exchanger that recovers sensible heat from the main heat exchanger and heats water flowing in the heat transfer tube, and is provided above the main heat exchanger and is separated from the combustion gas passing through the main heat exchanger by the main heat exchanger. In addition to the sensible heat that could not be recovered, in the water heater with a sub heat exchanger that recovers latent heat and heats the water flow in the heat transfer tube,
A drain evaporator that is provided below the sub heat exchanger and above the main heat exchanger, receives the drain generated by latent heat recovery in the sub heat exchanger, and heats and evaporates the drain with a combustion gas. And a flow straightening plate for guiding the combustion gas passing through the main heat exchanger flowing beside the drain evaporator toward the heat transfer tube of the sub heat exchanger.

【0006】また、本発明の請求項2記載の湯沸器は、
上記請求項1記載の湯沸器において、上記副熱交換器
は、伝熱管が前後に2列で配列され、上記整流板は、上
記伝熱管の間に該伝熱管と平行に延設され、その断面が
略V字状であることを要旨とする。
[0006] The water heater according to claim 2 of the present invention comprises:
2. The water heater according to claim 1, wherein the auxiliary heat exchanger has heat transfer tubes arranged in two rows in front and back, and the straightening plate extends between the heat transfer tubes in parallel with the heat transfer tubes, The gist is that the cross section is substantially V-shaped.

【0007】また、本発明の請求項3記載の湯沸器は、
上記請求項1又は請求項2記載の湯沸器において、上記
ドレン蒸発器は、多孔質の耐熱・耐硝酸性の材料からな
りドレンを受けて全体に浸透するドレン浸透体と、該ド
レン浸透体を載置する浸透体載置板とを有し、該浸透体
載置板の載置面には、複数の開口が設けられていること
を要旨とする。
[0007] The water heater according to claim 3 of the present invention comprises:
3. The water heater according to claim 1 or 2, wherein the drain evaporator is made of a porous heat-resistant and nitric acid-resistant material, and receives a drain and permeates the entire drain; And a plurality of openings are provided on the mounting surface of the penetrating body mounting plate.

【0008】また、本発明の請求項4記載の湯沸器は、
上記請求項1〜3のいずれか1項に記載の湯沸器におい
て、上記整流板には、燃焼ガスが通過する複数の開口が
設けられていることを要旨とする。
Further, the water heater according to claim 4 of the present invention,
In the water heater according to any one of claims 1 to 3, the gist is characterized in that the current plate is provided with a plurality of openings through which combustion gas passes.

【0009】また、本発明の請求項5記載の湯沸器は、
上記請求項3又は請求項4記載の湯沸器において、上記
燃焼室の側壁に段部を形成し、該段部と上記浸透体載置
板とで上記ドレン浸透体を挟み込んで該ドレン浸透体の
抜け止めをすることを要旨とする。
Further, the water heater according to claim 5 of the present invention,
5. The water heater according to claim 3, wherein a step is formed on a side wall of the combustion chamber, and the drain penetrant is sandwiched between the step and the permeant placement plate. 6. The gist is to prevent the falling off.

【0010】上記構成を有する本発明の請求項1記載の
湯沸器は、バーナの燃焼ガスが主熱交換器を加熱してか
ら余熱で副熱交換器を加熱する。この際、燃焼ガスは、
ドレン蒸発器も加熱する。従って、燃焼ガスは、まず主
熱交換器で冷却されて顕熱の多くが回収され、次に副熱
交換器でドレンの発生する温度まで冷却されてドレンを
発生して主熱交換器で回収できなかった顕熱に加え潜熱
も回収される。副熱交換器で発生したドレンは、ドレン
蒸発器で受け取られ蒸発して燃焼ガス中に戻るため、湯
沸器の外部へドレンは排出しない。この結果、ドレンを
蒸発させるために、回収した潜熱分と同量の熱量が奪わ
れるが、副熱交換器では、主熱交換器とは違いドレンが
発生しないようにしておく必要がないために、器具から
排出される燃焼ガスの排気温度を十分に下げることがで
き、主熱交換器で回収できなかった顕熱を回収できる。
従って、器具全体としては燃焼ガスが持っている熱エネ
ルギーのうちの大部分の顕熱を回収していることにな
る。このようにして、ドレンを器具外に排出することな
く、主熱交換器と副熱交換器とで効率良く通水を加熱し
て出湯する。また、副熱交換器の下方にドレン蒸発器が
設けられているので、副熱交換器の伝熱管への燃焼ガス
の流れが悪くなっているが、整流板がドレン蒸発器の横
を流れる燃焼ガスをこの伝熱管へ円滑に導くために、伝
熱管にも燃焼ガスを良好に接触させることができ、熱交
換が促進される。
[0010] In the water heater according to the first aspect of the present invention, the combustion gas of the burner heats the main heat exchanger and then heats the sub heat exchanger with residual heat. At this time, the combustion gas is
The drain evaporator also heats. Therefore, the combustion gas is first cooled by the main heat exchanger to recover most of the sensible heat, and then cooled to the temperature at which drain is generated by the sub heat exchanger to generate drain and recovered by the main heat exchanger. Latent heat is recovered in addition to sensible heat that could not be obtained. The drain generated in the sub heat exchanger is received by the drain evaporator, evaporated and returned to the combustion gas, so that the drain is not discharged to the outside of the water heater. As a result, in order to evaporate the drain, the same amount of heat as the recovered latent heat is taken, but in the sub heat exchanger, unlike the main heat exchanger, it is not necessary to keep drain from being generated. In addition, the exhaust temperature of the combustion gas discharged from the appliance can be sufficiently reduced, and sensible heat that cannot be recovered by the main heat exchanger can be recovered.
Therefore, the entire apparatus collects most of the sensible heat of the thermal energy of the combustion gas. In this way, the water is efficiently heated and discharged from the main heat exchanger and the sub heat exchanger without discharging the drain out of the apparatus. Also, since the drain evaporator is provided below the sub heat exchanger, the flow of the combustion gas to the heat transfer tubes of the sub heat exchanger is deteriorated. In order to smoothly guide the gas to the heat transfer tube, the combustion gas can be brought into good contact with the heat transfer tube, and heat exchange is promoted.

【0011】また、本発明の請求項2記載の湯沸器は、
前後2列に配列された副熱交換器の伝熱管の間に、断面
が略V字状に形成された整流板を伝熱管と平行に延設す
ることによって、両方の伝熱管に良好に燃焼ガスを導く
ことができ、副熱交換器での熱回収を十分に行うことが
できる。
Further, the water heater according to claim 2 of the present invention,
By rectifying plates having a substantially V-shaped cross section extending in parallel with the heat transfer tubes between the heat transfer tubes of the sub heat exchangers arranged in the front and rear two rows, both the heat transfer tubes can be favorably burned. Gas can be introduced, and heat recovery in the sub heat exchanger can be sufficiently performed.

【0012】また、本発明の請求項3記載の湯沸器は、
浸透体載置板に載置されたドレン浸透体が副熱交換器か
ら滴下してくるドレンを受け、受けられたドレンは多孔
体であるドレン浸透体内全体に浸透していく。浸透体載
置板には載置面に複数の開口が設けられているため、ド
レン浸透体内を浸透体載置板との接触面まで浸透してき
たドレンは、燃焼ガスと直接接触して加熱され、熱を無
駄に使うことなく効率良く蒸発させられる。又、ドレン
浸透体により広い範囲で蒸発するために部分的な突沸に
よる異音も発生しない。
Further, the water heater according to claim 3 of the present invention is characterized in that:
The drain penetrating body placed on the penetrating body mounting plate receives the drain dripped from the sub heat exchanger, and the received drain penetrates into the entire drain penetrating body which is a porous body. Since the penetrating body mounting plate has a plurality of openings on the mounting surface, the drain that has penetrated the drain penetrating body to the contact surface with the penetrating body mounting plate is heated by coming into direct contact with the combustion gas. , And can be efficiently evaporated without wasting heat. In addition, since a wide range is evaporated by the drain penetrant, abnormal noise due to partial bumping does not occur.

【0013】また、本発明の請求項4記載の湯沸器は、
燃焼ガス流路中に設けられた整流板に燃焼ガスが通過す
る複数の開口を設けることにより、燃焼ガスの排気抵抗
の低減がはかられる。
Further, the water heater according to claim 4 of the present invention,
By providing a plurality of openings through which the combustion gas passes through the current plate provided in the combustion gas passage, the exhaust resistance of the combustion gas can be reduced.

【0014】また、本発明の請求項5記載の湯沸器は、
ドレン浸透体を燃焼室の側壁に形成された段部と浸透体
載置板とではさむことにより、ドレン浸透体の抜け止め
をすることができる。さらに、副熱交換器の伝熱管が貫
通している燃焼室の側壁のまわりで発生し側壁を伝わっ
て下に垂れていくドレンを、段部で側壁と接触している
ドレン浸透体により確実に受けることができるので、ド
レンが下方に位置する主熱交換器やバーナなどにたれる
ことはない。
Further, the water heater according to claim 5 of the present invention,
By sandwiching the drain penetrant between the step formed on the side wall of the combustion chamber and the penetrant mounting plate, the drain penetrant can be prevented from coming off. Furthermore, the drain generated around the side wall of the combustion chamber through which the heat transfer tube of the sub-heat exchanger penetrates and runs down along the side wall is surely drained by the drain penetrator in contact with the side wall at the step portion. The drain does not fall on the main heat exchanger or burner located below.

【発明の実施の形態】以上説明した本発明の構成・作用
を一層明らかにするために、以下本発明の湯沸器の好適
な一実施形態について図1〜図6を用いて説明する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS In order to further clarify the structure and operation of the present invention described above, a preferred embodiment of a water heater according to the present invention will be described below with reference to FIGS.

【0015】図1は、一実施形態としての元止め式瞬間
湯沸器1の概略構成図であり、図2は、湯沸器1の外観
図であり、図3は、通水順路を示した図である。器具正
面には、点消火操作,水量調節及び出湯温調節するため
の操作ボタン2と、ガス量調節レバー3とが設けられ
る。操作ボタン2は、プッシュ式ボタンではあるものの
回動自在に設けられ、点消火操作はプッシュ操作によ
り、水量調節による出湯温調節は回し操作により行われ
る。器具本体4ケースには、操作ボタン2の周囲に温調
用の目盛りが印刷されており、操作ボタン2のツマミ2
aをあわすことにより出湯温及び水量が無段階調節され
る。また、ガス量調節レバー3を左側の能力小の位置か
ら右側の能力大の位置まで操作することによって供給ガ
ス量は無断階調節される。
FIG. 1 is a schematic configuration diagram of a main stop type instantaneous water heater 1 as one embodiment, FIG. 2 is an external view of the water heater 1, and FIG. FIG. On the front of the appliance, there are provided an operation button 2 for performing a point fire extinguishing operation, water amount adjustment and hot water temperature adjustment, and a gas amount adjustment lever 3. The operation button 2 is a push-type button, but is rotatably provided. The point fire extinguishing operation is performed by a push operation, and the tapping water temperature adjustment by water flow adjustment is performed by a turning operation. A scale for temperature control is printed around the operation button 2 on the case of the appliance body 4.
By adjusting a, the tapping temperature and the amount of water are continuously adjusted. Further, by operating the gas amount adjusting lever 3 from the small capacity position on the left side to the large capacity position on the right side, the supply gas amount is continuously adjusted.

【0016】器具本体4内には、図1に示すように、燃
焼室5が設けられ、燃焼室5内には、下から順に、燃料
ガスを燃焼するバーナ6と、バーナ6からの燃焼ガスの
顕熱の多くを回収するフィンチューブ式の主熱交換器7
と、ドレンを受けて蒸発させるドレン蒸発器9と、燃焼
ガスの流れの向きを変化させる整流板10と、主熱交換
器7で回収しきれなかった顕熱と潜熱とを回収する副熱
交換器8とが設けられる。尚、副熱交換器8とドレン蒸
発器9と整流板10とは、副熱交換ユニット11とし
て、一体に形成されるものであり、これについての詳細
は後述する。燃焼室5の上面には、主熱交換器7,副熱
交換器8で熱交換後の燃焼ガスを器体外へ排出する排気
口12が形成されており、この排気口12は、器具本体
4の上面に開口された排気穴13に臨んでいる。尚、排
気穴13の上方に、器具外へ排出された燃焼ガスを前方
に導くと共に、器具内にごみが落下するのを防ぐ図示し
ない略L字状の排気フードを設けても良い。また、器具
本体4及び燃焼室5の下面は、バーナ6の燃焼用空気を
取り込むために開口されており、さらに、器具本体4の
側面には給気口30も設けられる。
As shown in FIG. 1, a combustion chamber 5 is provided in the appliance body 4, and a burner 6 for burning fuel gas and a combustion gas from the burner 6 are arranged in the combustion chamber 5 in order from the bottom. Fin-tube type main heat exchanger 7 that recovers much of the sensible heat
A drain evaporator 9 for receiving and evaporating the drain, a flow straightening plate 10 for changing the direction of the flow of the combustion gas, and a sub heat exchange for recovering sensible heat and latent heat that could not be recovered by the main heat exchanger 7. Vessel 8 is provided. The sub heat exchanger 8, the drain evaporator 9, and the rectifier plate 10 are integrally formed as a sub heat exchange unit 11, and details thereof will be described later. On the upper surface of the combustion chamber 5, an exhaust port 12 for discharging the combustion gas after the heat exchange in the main heat exchanger 7 and the sub heat exchanger 8 to the outside of the body is formed. And faces the exhaust hole 13 opened on the upper surface of the device. Note that a substantially L-shaped exhaust hood (not shown) may be provided above the exhaust hole 13 to guide the combustion gas discharged to the outside of the appliance forward and to prevent dust from falling into the appliance. The lower surfaces of the appliance main body 4 and the combustion chamber 5 are opened to take in the combustion air of the burner 6, and an air supply port 30 is provided on the side surface of the appliance main body 4.

【0017】水入口からの給水経路には、操作ボタン2
による手動操作に連動して流路を開閉する水栓14が設
けられ、その下流には水圧応動装置15が設けられる。
水圧応動装置15の下流側の流路には、操作ボタン2の
回し操作と連動して出湯量を調節する水量調節軸16が
設けられる。水量調節軸16で流路は、2方向に分岐さ
れ、一方には副熱交換器8への給水管17が、もう一方
には主熱交換器7からの出湯管18に接続されるバイパ
ス管19が設けられる。従って、副熱交換器8及び主熱
交換器7を通ってきた湯(内胴通過水)とバイパス管1
9を通ってきた水(バイパス水)との混合湯が器具から
出湯することとなる。
An operation button 2 is provided in the water supply path from the water inlet.
A water faucet 14 that opens and closes a flow path in conjunction with manual operation by the user is provided, and a water pressure responsive device 15 is provided downstream thereof.
In the flow path on the downstream side of the water pressure responsive device 15, a water amount adjusting shaft 16 for adjusting the amount of hot water in conjunction with the turning operation of the operation button 2 is provided. The water flow adjusting shaft 16 branches the flow path in two directions, one of which is a water supply pipe 17 to the sub heat exchanger 8 and the other is a bypass pipe connected to a tapping pipe 18 from the main heat exchanger 7. 19 are provided. Therefore, the hot water (inner body passing water) that has passed through the sub heat exchanger 8 and the main heat exchanger 7 and the bypass pipe 1
Hot water mixed with water (bypass water) that has passed through 9 flows out of the appliance.

【0018】図3に示すように、給水管17は副熱交換
器8として設けられ前後2列で平行に配列された副伝熱
管8aの入口に接続され、副伝熱管8aの出口は燃焼室
5を外側で巻回する巻回管20の入口に接続され、巻回
管20の出口は主熱交換器7に設けられフィン7bを貫
通して複数回蛇行する主伝熱管7aの入口に接続され、
主伝熱管7aの出口は出湯管18に接続される。また、
給水管17の先端には、湯沸器1を使用後に凍結防止な
どの目的のために通水路中の水を抜くための分岐管21
が設けられており、この分岐管21の先端には水抜き栓
22が設けられる。さらに、この湯沸器1の通水順路
が、上方に位置する副伝熱管8a→下方に位置する巻回
管20→上方に位置する主伝熱管7aとなるため、この
分岐管21のみで通水路中全ての水を抜こうとしても巻
回管20に水が溜まってしまうので、この水を抜くため
に巻回管20の最も低い位置に水抜き管23が設けられ
る。
As shown in FIG. 3, a water supply pipe 17 is provided as a sub heat exchanger 8 and is connected to an inlet of a sub heat transfer pipe 8a arranged in two rows in front and rear in parallel, and an outlet of the sub heat transfer pipe 8a is connected to a combustion chamber. 5 is connected to the inlet of a winding tube 20 that winds the outside 5 and the outlet of the winding tube 20 is connected to the inlet of a main heat transfer tube 7a provided in the main heat exchanger 7 and penetrating through the fins 7b a plurality of times. And
The outlet of the main heat transfer pipe 7a is connected to the tapping pipe 18. Also,
A branch pipe 21 for draining water in the water passage for the purpose of preventing freezing after using the water heater 1 is provided at the end of the water supply pipe 17.
The drain pipe 22 is provided at the tip of the branch pipe 21. Further, the water flow path of the water heater 1 is changed from the sub heat transfer pipe 8a located above to the wound pipe 20 located below and the main heat transfer pipe 7a located above, so that the water is passed only by the branch pipe 21. Even if it is attempted to drain all the water in the water channel, water accumulates in the winding tube 20. Therefore, a draining tube 23 is provided at the lowest position of the winding tube 20 to drain the water.

【0019】ガス入口からバーナ6へのガス供給経路に
は、燃焼中に図示しない熱電対の熱起電力により開弁保
持されるマグネット安全弁24と、通水に関連して前述
の水圧応動装置15により通水時のみガス流路を開成す
る水圧応動弁25と、操作ボタン2による手動操作に連
動してガス流路を開閉する器具栓26と、ガス量調節レ
バー3の手動操作と連動してガス供給量を調節するガス
量調節軸27が設けられる。
The gas supply path from the gas inlet to the burner 6 includes a magnet safety valve 24 that is opened and held by the thermoelectromotive force of a thermocouple (not shown) during combustion, and the above-described hydraulic pressure responsive device 15 relating to water flow. , A water pressure responsive valve 25 that opens the gas flow path only when water is supplied, an instrument plug 26 that opens and closes the gas flow path in conjunction with manual operation by the operation button 2, and a manual operation of the gas amount adjustment lever 3. A gas amount adjusting shaft 27 for adjusting the gas supply amount is provided.

【0020】次に、副熱交換器8とドレン蒸発器9と整
流板10とからなる副熱交換ユニット11について図4
〜図6を用いて詳述する。図4は副熱交換ユニット11
の上面図、図5は正面図、図6は図4及び図5中の一点
鎖線A−Aでの断面図である。尚、図4中においてはド
レン蒸発器9が省略してあり、図5中においては整流板
10及び燃焼室5を形成するための前板31と後板32
が省略してある。副熱交換器8は、前後2列で平行に配
列された前副伝熱管8aAと後副伝熱管8aBとから構
成されている。以下説明にあたり、前副伝熱管8aAと
後副伝熱管8aBとを区別しない場合には、副伝熱管8
aという。副伝熱管8aの両端は、燃焼室5の側壁を貫
通して突出しており、その一端で曲管28によって接合
される。そして後副伝熱管8aBの別の一端に給水管1
7が接続され、前副伝熱管8aAの別の一端に巻回管2
0が接続される。
Next, a sub heat exchange unit 11 composed of a sub heat exchanger 8, a drain evaporator 9, and a flow straightening plate 10 will be described with reference to FIG.
This will be described in detail with reference to FIG. FIG. 4 shows the auxiliary heat exchange unit 11
, FIG. 5 is a front view, and FIG. 6 is a cross-sectional view taken along dashed line AA in FIGS. 4 and 5. In FIG. 4, the drain evaporator 9 is omitted, and in FIG. 5, a front plate 31 and a rear plate 32 for forming the flow straightening plate 10 and the combustion chamber 5 are shown.
Has been omitted. The sub heat exchanger 8 includes a front sub heat transfer tube 8aA and a rear sub heat transfer tube 8aB which are arranged in parallel in two front and rear rows. In the following description, when it is not necessary to distinguish between the front auxiliary heat transfer tube 8aA and the rear auxiliary heat transfer tube 8aB,
called a. Both ends of the sub heat transfer tube 8a protrude through the side wall of the combustion chamber 5, and are joined at one end by a curved tube. The water supply pipe 1 is connected to another end of the rear auxiliary heat transfer pipe 8aB.
7 is connected to another end of the front auxiliary heat transfer tube 8aA.
0 is connected.

【0021】前副伝熱管8aAと後副伝熱管8aBの真
下には、それぞれ、副伝熱管8aで燃焼ガスの潜熱を回
収することによって発生したドレンを受けて、受けたド
レンを燃焼ガスにより加熱して蒸発させるドレン蒸発器
9が設けられる。ドレン蒸発器9は、副伝熱管8aから
滴下してくるドレンを受けるドレン浸透体9aと、ドレ
ン浸透体9aを支える浸透体載置板9bとからなる。ド
レン浸透体9aは、耐熱及び耐ドレン性に優れた多孔質
のセラミックス製であり、浸透体載置板9bは、ステン
レス製の板をV字状に折り曲げてその両端を燃焼室5の
側壁に接合して形成される。そして、ドレン浸透体9a
は、この浸透体載置板9bの上に2個づつ載置される。
また、浸透体載置板9bには、複数の蒸発開口9cが設
けられる。
Immediately below the front auxiliary heat transfer tube 8aA and the rear auxiliary heat transfer tube 8aB, the drain generated by recovering the latent heat of the combustion gas in the auxiliary heat transfer tube 8a is received, and the received drain is heated by the combustion gas. A drain evaporator 9 for evaporating the fuel is provided. The drain evaporator 9 includes a drain penetrating body 9a that receives drain dripped from the sub heat transfer tube 8a, and a penetrating body mounting plate 9b that supports the drain penetrating body 9a. The drain penetrating body 9a is made of porous ceramics having excellent heat resistance and drain resistance, and the penetrating body mounting plate 9b is formed by bending a stainless steel plate into a V-shape and forming both ends thereof on the side wall of the combustion chamber 5. It is formed by joining. And the drain penetrant 9a
Are placed two by two on this penetrant placement plate 9b.
Further, a plurality of evaporating openings 9c are provided in the penetrating body mounting plate 9b.

【0022】副伝熱管8aより下方の燃焼室5の側壁に
は、その横幅が大きくなるように段部29が形成されて
おり、この段部29と浸透体載置板9bとでドレン浸透
体9aを挟み込んで抜け止めする。整流板10は、溶融
アルミニウムめっき鋼板を略V字状に形成し、前後2列
の副伝熱管8aの中間位置に、副伝熱管8aと平行に延
設され、その両端が燃焼室5の側壁に接合される構成で
ある。この整流板10には、燃焼ガスを通過させる複数
の通気孔10aが開口される。このような副熱交換ユニ
ット11は、一体的に組み立てられたユニットとなって
おり、主熱交換器7の上に載置され、ビスでとめて固定
されるものである。
A step portion 29 is formed on the side wall of the combustion chamber 5 below the auxiliary heat transfer tube 8a so as to increase its lateral width, and the step portion 29 and the permeation member mounting plate 9b form a drain permeation member. 9a is sandwiched and retained. The flow straightening plate 10 is formed by forming a hot-dip aluminum-plated steel plate into a substantially V shape, and is provided at an intermediate position between two rows of front and rear sub heat transfer tubes 8a in parallel with the sub heat transfer tubes 8a. It is the structure joined to. A plurality of ventilation holes 10a through which the combustion gas passes are opened in the current plate 10. Such a sub heat exchange unit 11 is a unit integrally assembled, mounted on the main heat exchanger 7 and fixed with screws.

【0023】上述したように構成された湯沸器1では、
操作ボタン2の手動操作と連動して器具栓26及び水栓
14が開き通水が開始される。水入口より流入した水
(図中破線矢印)は、水栓14、水圧応動装置15を通
り水量調節軸16より、一方は給水管17を経て副熱交
換器8、巻回管20、主熱交換器7を通り出湯管18
へ、他方はバイパス管19を通って出湯管18からの湯
と混合される。また、水圧応動装置15に通水されると
水圧応動弁25とマグネット安全弁24が開弁され、バ
ーナ6にガスが供給され、図示しない電極からの連続ス
パークにより着火する。バーナ6の燃焼中は、図示しな
い熱電対の熱起電力によりマグネット安全弁24の開弁
状態が維持され、燃焼が維持される。
In the water heater 1 configured as described above,
In conjunction with the manual operation of the operation button 2, the appliance plug 26 and the faucet 14 are opened to start water flow. The water flowing from the water inlet (broken arrow in the figure) passes through a water faucet 14 and a water pressure responsive device 15 and passes through a water amount adjusting shaft 16, one of which passes through a water supply pipe 17, a sub heat exchanger 8, a winding pipe 20, Hot water pipe 18 through exchanger 7
And the other is mixed with hot water from the tapping pipe 18 through the bypass pipe 19. When water is passed through the hydraulic pressure responsive device 15, the hydraulic pressure responsive valve 25 and the magnet safety valve 24 are opened, gas is supplied to the burner 6, and ignition is caused by continuous spark from an electrode (not shown). During the combustion of the burner 6, the open state of the magnet safety valve 24 is maintained by the thermoelectromotive force of a thermocouple (not shown), and the combustion is maintained.

【0024】燃料ガスのバーナ6での燃焼に伴い、器具
本体4の下面の開口や、側面に設けられた給気口30よ
り外気が器具本体4内に吸引され、燃焼室5下面の開口
を通ってバーナ6へ導入されて燃焼用空気として燃焼に
供される。バーナ6の炎口近傍では混合気が燃焼して火
炎を形成し、主熱交換器7の上流近傍に至る間に燃焼が
完結(完全燃焼)する。主熱交換器7を燃焼ガス流路の
上流に設け、副熱交換器8を燃焼ガス流路の下流に設け
たため、バーナ6からの高温の燃焼ガスが、自然ドラフ
ト力により主熱交換器7の各フィン7b間を貫流し良好
に熱交換し、これにより温度の下がった燃焼ガスが副熱
交換器8においても熱交換して排気口12から器具の外
へ排出される。また、燃焼ガスは、主熱交換器7に入る
前に、燃焼室5の外側を巻回している巻回管20でも熱
交換して通水を加熱する。
With the combustion of the fuel gas by the burner 6, outside air is sucked into the instrument body 4 from an opening on the lower face of the instrument body 4 and an air supply port 30 provided on the side face, and the opening on the lower face of the combustion chamber 5 is closed. The fuel gas passes through the burner 6 and is burned as combustion air. The air-fuel mixture burns near the flame opening of the burner 6 to form a flame, and the combustion is completed (complete combustion) while reaching the vicinity of the upstream of the main heat exchanger 7. Since the main heat exchanger 7 is provided upstream of the combustion gas flow path and the sub heat exchanger 8 is provided downstream of the combustion gas flow path, the high-temperature combustion gas from the burner 6 is supplied to the main heat exchanger 7 by natural draft force. The fins 7b flow through the fins 7b and exchange heat satisfactorily. As a result, the combustion gas whose temperature has decreased is also exchanged in the auxiliary heat exchanger 8 and discharged from the exhaust port 12 to the outside of the appliance. Further, before entering the main heat exchanger 7, the combustion gas also exchanges heat with the winding tube 20 wound around the outside of the combustion chamber 5 to heat the water flow.

【0025】主熱交換器7及び巻回管20では、ドレン
を発生させずに燃焼ガスから顕熱だけを回収しているわ
けであるが、通水部である主伝熱管7aのような局所的
な低温部が存在するので、このような低温部での部分的
なドレン発生を防止するために燃焼ガスの排気温度が十
分下がるまで熱交換できず、潜熱だけではなく顕熱の一
部も回収できない。一方、副熱交換器8の副伝熱管8a
では、主熱交換器7を通過してきた燃焼ガスをさらに冷
却し、ドレンを発生させて潜熱を回収するわけである
が、この際、主熱交換器7及び巻回管20で回収しきれ
なかった顕熱も回収する。発生したドレンは、副伝熱管
8aの真下に設けられたドレン蒸発器9で受けられ、主
熱交換器7を通過してきた燃焼ガスによって加熱され蒸
発する。この際、回収した潜熱と同量の熱量を燃焼ガス
中へ放出してしまうが、副熱交換器8では、主熱交換器
7及び巻回管20とは違いドレンが発生しないようにし
ておく必要がないため、器具から排出される燃焼ガスの
排気温度が十分に下がるまで熱交換して、主熱交換器7
及び巻回管20で回収できなかった顕熱を回収できるの
で、器具全体としては、燃焼ガス中の大部分の顕熱を回
収していることになる。従って、ドレンを排出せずに、
高熱効率を達成できる。
In the main heat exchanger 7 and the winding tube 20, only sensible heat is recovered from the combustion gas without generating drain. In order to prevent partial drainage in such a low temperature area, heat exchange cannot be performed until the exhaust gas temperature of the combustion gas drops sufficiently, and not only latent heat but also some sensible heat Cannot be recovered. On the other hand, the sub heat exchanger tube 8a of the sub heat exchanger 8
Then, the combustion gas that has passed through the main heat exchanger 7 is further cooled to generate drain and recover latent heat, but at this time, the latent heat cannot be recovered by the main heat exchanger 7 and the winding tube 20. Also recovers sensible heat. The generated drain is received by a drain evaporator 9 provided immediately below the sub heat transfer tube 8a, and is heated and evaporated by the combustion gas passing through the main heat exchanger 7. At this time, the same amount of heat as the recovered latent heat is released into the combustion gas. However, in the sub heat exchanger 8, unlike the main heat exchanger 7 and the winding tube 20, no drain is generated. Since there is no necessity, the heat exchange is performed until the exhaust gas temperature of the combustion gas discharged from the appliance is sufficiently lowered, and the main heat exchanger 7
In addition, since the sensible heat that could not be recovered by the winding tube 20 can be recovered, the entire apparatus recovers most of the sensible heat in the combustion gas. Therefore, without draining,
High thermal efficiency can be achieved.

【0026】また、副伝熱管8aの真下にドレン蒸発器
9が設けられているために、副伝熱管8aへの燃焼ガス
の流れが悪くなってしまうが、整流板10によって燃焼
ガスの流れの向きが変えられて副伝熱管8aへも燃焼ガ
スが円滑に流れる。このため、副伝熱管8aにも燃焼ガ
スが良好に接触して熱交換が促進される。また、バーナ
6の燃焼用空気を自然ドラフト力のみによって取り込ん
でいるこのような自然燃焼式の器具では、ファンによっ
て強制的に取り込む強制燃焼式の器具と比べ、燃焼ガス
流路中に整流板10のような異物を設けることによる燃
焼ガスの排気抵抗の増大が大きな問題となるが、整流板
10に燃焼ガスが通過する通気穴10aを複数設けるこ
とにより、このような排気抵抗の増大を抑制しバーナ6
の燃焼状態を良好に維持することができる。
Further, since the drain evaporator 9 is provided immediately below the sub heat transfer tube 8a, the flow of the combustion gas to the sub heat transfer tube 8a is deteriorated. The direction is changed, and the combustion gas flows smoothly to the sub heat transfer tube 8a. For this reason, the combustion gas satisfactorily comes into contact with the auxiliary heat transfer tube 8a, thereby promoting heat exchange. In addition, in such a natural combustion type appliance in which the combustion air of the burner 6 is taken in only by the natural draft force, a rectifying plate 10 is provided in the combustion gas flow path as compared with a forced combustion type appliance in which a fan is forcibly taken in. An increase in the exhaust resistance of the combustion gas due to the provision of such foreign matter is a serious problem. However, by providing a plurality of ventilation holes 10a through which the combustion gas passes through the current plate 10, such an increase in the exhaust resistance can be suppressed. Burner 6
Can maintain a good combustion state.

【0027】多孔質のドレン浸透体9aに滴下したドレ
ンは、ドレン浸透体9a内全体に浸透していく。そし
て、ドレン浸透体9a内を浸透体載置板9bとの接触面
まで浸透してきたドレンは、浸透体載置板9bに複数の
蒸発開口9cが設けられているため、燃焼ガスと直接接
触して加熱されて、熱を無駄に使うことなく良好に蒸発
する。又、ドレン浸透体9aにより広い範囲で蒸発させ
るので、部分的な突沸による異音の発生も防止できる。
The drain dropped into the porous drain penetrant 9a permeates the entire drain permeant 9a. The drain that has penetrated the inside of the drain permeant 9a to the contact surface with the permeant mounting plate 9b comes into direct contact with the combustion gas because a plurality of evaporation openings 9c are provided in the permeant mounting plate 9b. And evaporates well without wasting heat. Further, since the vapor is evaporated in a wide range by the drain penetrating body 9a, generation of abnormal noise due to partial bumping can be prevented.

【0028】しかも、ドレン浸透体9aを燃焼室5の側
壁に形成された段部29と浸透体載置板9bとではさむ
ことにより、副熱交換器8の伝熱管が貫通している燃焼
室5の側壁のまわりで発生し側壁を伝わって下に垂れて
いくドレンを、側壁の段部29で側壁と接触しているド
レン浸透体9aにより確実に受けることができるので、
ドレンが下方に位置する主熱交換器7やバーナ6などに
垂れることはない。
Further, the drain permeator 9a is sandwiched between the stepped portion 29 formed on the side wall of the combustion chamber 5 and the permeant mount plate 9b, so that the heat transfer tube of the sub heat exchanger 8 is penetrated. The drain generated around the side wall 5 and drips down along the side wall can be reliably received by the drain penetrating body 9a in contact with the side wall at the step 29 of the side wall.
The drain does not drop on the main heat exchanger 7 or the burner 6 located below.

【0029】さらに、給水流路中で最も低温の水を副伝
熱管8aに通水することで、大きな温度差の中で、効率
良く燃焼ガス中の潜熱及び顕熱を回収できる。さらに、
副伝熱管8aでの加熱により冷水は予熱されるため、巻
回管20にまかれた燃焼室5の内壁でのドレン発生を抑
制できる。そして、最後に主伝熱管7aに給水流路中で
最も高温の湯を通水できるので、そこでのドレン発生を
効果的に抑制できる。
Further, by passing the coldest water in the water supply passage to the sub heat transfer pipe 8a, the latent heat and sensible heat in the combustion gas can be efficiently recovered within a large temperature difference. further,
Since the cold water is preheated by the heating in the sub heat transfer tube 8a, the generation of drain on the inner wall of the combustion chamber 5 covered with the winding tube 20 can be suppressed. Finally, since the hottest water can be passed through the main heat transfer pipe 7a in the water supply flow path, drainage there can be effectively suppressed.

【0030】以上本発明の実施形態について説明した
が、本発明はこうした実施形態に何等限定されるもので
はなく、本発明の要旨を逸脱しない範囲において、種々
なる態様で実施し得ることは勿論である。
Although the embodiments of the present invention have been described above, the present invention is not limited to these embodiments at all, and it goes without saying that the present invention can be implemented in various modes without departing from the gist of the present invention. is there.

【0031】[0031]

【発明の効果】以上詳述したように、本発明の請求項1
記載の湯沸器によれば、副熱交換器で発生したドレンを
ドレン蒸発器で蒸発させるため、ドレンを器具外へ排出
せずドレンの中和処理が不要で、かつ燃焼ガス中の大部
分の顕熱を回収できるために熱効率が非常に高くなる。
そして、ドレン蒸発器によって燃焼ガスの流れが妨害さ
れる副熱交換器の伝熱管へも円滑に燃焼ガスを導くこと
ができるので、そこでの熱交換が促進されて、さらに熱
効率を向上させることができる。
As described in detail above, claim 1 of the present invention
According to the described water heater, since the drain generated in the sub heat exchanger is evaporated by the drain evaporator, the drain is not discharged to the outside of the apparatus, the drain does not need to be neutralized, and most of the combustion gas Sensible heat can be recovered, so that the thermal efficiency becomes very high.
And, since the combustion gas can be smoothly guided to the heat transfer tube of the sub heat exchanger where the flow of the combustion gas is obstructed by the drain evaporator, heat exchange there is promoted, and the heat efficiency can be further improved. it can.

【0032】更に、本発明の請求項2記載の湯沸器によ
れば、副熱交換器と整流板とを簡単な構造で実施するこ
とができるので、湯沸器を製造するコストを抑制でき
る。
Further, according to the water heater according to the second aspect of the present invention, since the auxiliary heat exchanger and the current plate can be implemented with a simple structure, the cost for manufacturing the water heater can be suppressed. .

【0033】更に、本発明の請求項3記載の湯沸器によ
れば、ドレンを燃焼ガスによって直接加熱することがで
きるため、ドレンを良好に蒸発させることができる。
Further, according to the water heater of the third aspect of the present invention, since the drain can be directly heated by the combustion gas, the drain can be satisfactorily evaporated.

【0034】更に、本発明の請求項4記載の湯沸器によ
れば、燃焼ガスの排気抵抗を低減し、バーナの燃焼を良
好に維持することができる。
Further, according to the water heater of the fourth aspect of the present invention, the exhaust resistance of the combustion gas can be reduced and the combustion of the burner can be favorably maintained.

【0035】更に、本発明の請求項5記載の湯沸器によ
れば、燃焼室の側壁を伝わって下方へ流れ落ちるドレン
をドレン浸透体で確実に受けることができるため、主熱
交換器やバーナがドレンによって腐食されることを防止
できる。
Further, according to the water heater of the fifth aspect of the present invention, the drain flowing down the side wall of the combustion chamber can be reliably received by the drain penetrant, so that the main heat exchanger and the burner Can be prevented from being corroded by the drain.

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

【図1】本実施形態の湯沸器の概略構成図である。FIG. 1 is a schematic configuration diagram of a water heater of the present embodiment.

【図2】本実施形態の湯沸器の外観図である。FIG. 2 is an external view of a water heater of the present embodiment.

【図3】本実施形態の湯沸器の通水順路を示した図であ
る。
FIG. 3 is a diagram showing a water flow path of the water heater of the present embodiment.

【図4】本実施形態の副熱交換ユニットの上面図であ
る。
FIG. 4 is a top view of the sub heat exchange unit of the present embodiment.

【図5】本実施形態の副熱交換ユニットの正面図であ
る。
FIG. 5 is a front view of the sub heat exchange unit of the embodiment.

【図6】本実施形態の副熱交換ユニットの断面図であ
る。
FIG. 6 is a cross-sectional view of the sub heat exchange unit of the present embodiment.

【符号の説明】[Explanation of symbols]

1…湯沸器、5…燃焼室、6…バーナ、7…主熱交換
器、7a…主伝熱管、8…副熱交換器、8a…副伝熱
管、8aA…前副伝熱管、8aB…後副伝熱管、9…ド
レン蒸発器、9a…ドレン浸透体、9b…浸透体載置
板、9c…蒸発開口、10…整流板、10a…通気孔、
29…段部。
DESCRIPTION OF SYMBOLS 1 ... Boiler, 5 ... Combustion chamber, 6 ... Burner, 7 ... Main heat exchanger, 7a ... Main heat exchanger tube, 8 ... Sub heat exchanger, 8a ... Sub heat exchanger tube, 8aA ... Pre-sub heat exchanger tube, 8aB ... Rear auxiliary heat transfer tube, 9: drain evaporator, 9a: drain penetrant, 9b: penetrant mounting plate, 9c: evaporation opening, 10: rectifying plate, 10a: vent hole,
29 ... Stepped part.

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 燃焼室内で燃料を燃焼するバーナと、 上記バーナの上方に設けられ、該バーナの燃焼ガスから
顕熱を回収して伝熱管内の通水を加熱する主熱交換器
と、 上記主熱交換器の上方に設けられ、該主熱交換器を通過
した燃焼ガスから該主熱交換器で回収しきれなかった顕
熱に加えて、潜熱を回収して伝熱管内の通水を加熱する
副熱交換器とを備えた湯沸器において、 上記副熱交換器の下方で上記主熱交換器の上方に設けら
れ、上記副熱交換器での潜熱回収によって発生したドレ
ンを受けると共に該ドレンを燃焼ガスにより加熱して蒸
発させるドレン蒸発器と、 上記ドレン蒸発器の横を流れる上記主熱交換器を通過し
た燃焼ガスを、上記副熱交換器の伝熱管に向けて案内す
る整流板とを備えることを特徴とする湯沸器。
A burner that burns fuel in a combustion chamber; a main heat exchanger that is provided above the burner and recovers sensible heat from combustion gas of the burner to heat water flowing in a heat transfer tube; It is provided above the main heat exchanger and collects latent heat in addition to the sensible heat that could not be recovered by the main heat exchanger from the combustion gas that passed through the main heat exchanger, and passed water through the heat transfer tube. A water heater provided with a sub heat exchanger for heating the main heat exchanger, below the sub heat exchanger, and receiving the drain generated by latent heat recovery in the sub heat exchanger. A drain evaporator that heats and evaporates the drain with the combustion gas, and guides the combustion gas passing through the main heat exchanger flowing beside the drain evaporator toward a heat transfer tube of the sub heat exchanger. A water heater comprising: a current plate.
【請求項2】 上記副熱交換器は、伝熱管が前後に2列
で配列され、 上記整流板は、上記伝熱管の間に該伝熱管と平行に延設
され、その断面が略V字状であることを特徴とする請求
項1記載の湯沸器。
2. The sub-heat exchanger has heat transfer tubes arranged in two rows in front and back, and the rectifying plate extends between the heat transfer tubes in parallel with the heat transfer tubes, and has a substantially V-shaped cross section. The water heater according to claim 1, wherein the water heater is in a shape.
【請求項3】 上記ドレン蒸発器は、多孔質の耐熱・耐
硝酸性の材料からなりドレンを受けて全体に浸透するド
レン浸透体と、該ドレン浸透体を載置する浸透体載置板
とを有し、該浸透体載置板の載置面には、複数の開口が
設けられていることを特徴とする請求項1又は請求項2
記載の湯沸器。
3. The drain evaporator according to claim 1, wherein the drain evaporator is made of a porous heat- and nitrate-resistant material, and receives a drain and permeates the entirety of the drain evaporator; The mounting surface of the penetrant mounting plate is provided with a plurality of openings.
The described water heater.
【請求項4】 上記整流板には、燃焼ガスが通過する複
数の開口が設けられていることを特徴とする請求項1〜
3のいずれか1項に記載の湯沸器。
4. The current plate is provided with a plurality of openings through which combustion gas passes.
4. The water heater according to any one of the above items 3.
【請求項5】 上記燃焼室の側壁に段部を形成し、該段
部と上記浸透体載置板とで上記ドレン浸透体を挟み込ん
で該ドレン浸透体の抜け止めをすることを特徴とする請
求項3又は請求項4記載の湯沸器。
5. A step is formed in a side wall of the combustion chamber, and the drain penetrant is sandwiched between the step and the permeant placement plate to prevent the drain penetrant from coming off. The water heater according to claim 3 or 4.
JP2001134809A 2001-05-02 2001-05-02 Water heater Expired - Lifetime JP4710164B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001134809A JP4710164B2 (en) 2001-05-02 2001-05-02 Water heater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001134809A JP4710164B2 (en) 2001-05-02 2001-05-02 Water heater

Publications (2)

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JP2002333212A true JP2002333212A (en) 2002-11-22
JP4710164B2 JP4710164B2 (en) 2011-06-29

Family

ID=18982416

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Link
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1508756A1 (en) * 2003-08-20 2005-02-23 Paloma Industries, Ltd. Water heater
EP1544555A2 (en) 2003-12-19 2005-06-22 Paloma Industries, Ltd. Hot water apparatus
JP2015010753A (en) * 2013-06-28 2015-01-19 株式会社アタゴ製作所 Water heater

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4897763U (en) * 1972-02-19 1973-11-19
JPS55105846U (en) * 1979-01-18 1980-07-24
JPS572841U (en) * 1980-06-04 1982-01-08
JPH05141777A (en) * 1991-11-22 1993-06-08 Paloma Ind Ltd Inflated water processor for hot-water supplier
JPH09189491A (en) * 1996-10-14 1997-07-22 Paloma Ind Ltd Heat exchanger

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4897763U (en) * 1972-02-19 1973-11-19
JPS55105846U (en) * 1979-01-18 1980-07-24
JPS572841U (en) * 1980-06-04 1982-01-08
JPH05141777A (en) * 1991-11-22 1993-06-08 Paloma Ind Ltd Inflated water processor for hot-water supplier
JPH09189491A (en) * 1996-10-14 1997-07-22 Paloma Ind Ltd Heat exchanger

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1508756A1 (en) * 2003-08-20 2005-02-23 Paloma Industries, Ltd. Water heater
US6971335B2 (en) 2003-08-20 2005-12-06 Paloma Industries, Limited Water heater
EP1544555A2 (en) 2003-12-19 2005-06-22 Paloma Industries, Ltd. Hot water apparatus
EP1544555A3 (en) * 2003-12-19 2006-05-03 Paloma Industries, Ltd. Hot water apparatus
US7360535B2 (en) 2003-12-19 2008-04-22 Paloma Industries, Limited Hot water apparatus
JP2015010753A (en) * 2013-06-28 2015-01-19 株式会社アタゴ製作所 Water heater

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