JP3306162B2 - High efficiency water heater - Google Patents

High efficiency water heater

Info

Publication number
JP3306162B2
JP3306162B2 JP8923093A JP8923093A JP3306162B2 JP 3306162 B2 JP3306162 B2 JP 3306162B2 JP 8923093 A JP8923093 A JP 8923093A JP 8923093 A JP8923093 A JP 8923093A JP 3306162 B2 JP3306162 B2 JP 3306162B2
Authority
JP
Japan
Prior art keywords
hot water
water
water supply
ejector
bathtub
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP8923093A
Other languages
Japanese (ja)
Other versions
JPH06272965A (en
Inventor
修 福田
重信 奥田
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.)
Osaka Gas Co Ltd
Original Assignee
Osaka 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 Osaka Gas Co Ltd filed Critical Osaka Gas Co Ltd
Priority to JP8923093A priority Critical patent/JP3306162B2/en
Publication of JPH06272965A publication Critical patent/JPH06272965A/en
Application granted granted Critical
Publication of JP3306162B2 publication Critical patent/JP3306162B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、熱交換器を二段にして
排熱を回収するようにした高効率の給湯装置に関するも
のである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a high-efficiency hot water supply apparatus having a two-stage heat exchanger for recovering waste heat.

【0002】[0002]

【従来の技術】図2は従来のこの種の高効率給湯装置を
示したもので、ガスバーナ1で加熱される給湯用熱交換
器を上下二段2a,2bに分け、その中間部に上段の熱
交換器2aで発生する凝縮水を受ける受け皿3を設ける
と共に、この受け皿3に連結された排水管7に中和器1
1を介装したものである。これは、通常200℃で廃棄
される排ガスを上段に付加された熱交換器2aに通し
て、排ガス温度が100℃以下になるまで排熱を回収す
るものであり、その時発生する凝縮水は、排ガス中のN
OxやSOxなどが溶け込んで強酸性となっているため
に、これが下段の熱交換器2bやガスバーナ1を腐食し
ないように、受け皿3で受けて、凝縮水中和器5で中和
処理したのち、下水へ排水している。
2. Description of the Related Art FIG. 2 shows a conventional high-efficiency hot water supply apparatus of this type, in which a heat exchanger for hot water supply heated by a gas burner 1 is divided into two upper and lower stages 2a and 2b, and an upper stage is provided at an intermediate portion. A receiving tray 3 for receiving condensed water generated in the heat exchanger 2a is provided, and a neutralizer 1 is connected to a drain pipe 7 connected to the receiving tray 3.
1 is interposed. In this method, exhaust gas normally discarded at 200 ° C. is passed through a heat exchanger 2a added at the upper stage to recover exhaust heat until the exhaust gas temperature becomes 100 ° C. or less, and condensed water generated at that time is N in exhaust gas
Since Ox and SOx are dissolved and become strongly acidic, they are received by the receiving tray 3 and neutralized by the condensed water neutralizer 5 so that they do not corrode the lower heat exchanger 2b and the gas burner 1. Drains to sewage.

【0003】[0003]

【発明が解決しようとする課題】しかし上述の従来構成
は、凝縮水中和器11が大形で設置場所をとる上に、処
理量が多いために中和器11を構成しているマグネシウ
ム棒の間隙が酸化物によって目詰まりを起こし易く、消
耗が激しいという問題があった。本発明は上記の問題点
を解消して中和器を小型化ることができる高効率給湯
装置を提供することを目的とするものである。
However, in the above-mentioned conventional structure, the condensed water neutralizer 11 is large and requires a large installation space. The gaps are liable to be clogged by oxides, and have a problem of severe wear. The present invention aims to provide a highly efficient water heater can it to reduce the size of the neutralizer to eliminate the problems set forth above.

【0004】[0004]

【課題を解決するための手段】本発明による高効率給湯
装置は、図1に示すように、ガスバーナ1で加熱される
給湯用熱交換器を上下二段2a,2bに分け、その中間
部に上段の熱交換器2aで発生する凝縮水を受ける受け
皿3を設け、給湯配管4から分岐した浴槽給湯配管5に
エゼクター6を介装して、このエゼクター6の注入口に
上記受け皿3からの排水管7を接続することにより、浴
槽8へ供給される温水に凝縮水を混入せしめると共に
上記排水管7に介装した貯水タンク9のオーバーフロー
管10を中和器11に接続して、余剰の凝縮水を中和処
理したのち外部へ排出するようにしたものである。
As shown in FIG. 1, a high-efficiency hot-water supply apparatus according to the present invention divides a hot-water supply heat exchanger heated by a gas burner 1 into upper and lower two-stage heat exchangers 2a and 2b. A receiving tray 3 for receiving condensed water generated in the upper heat exchanger 2a is provided, an ejector 6 is interposed in a bathtub hot water supply pipe 5 branched from a hot water supply pipe 4, and drainage from the receiver 3 is provided at an inlet of the ejector 6. by connecting tube 7, Rutotomoni allowed mixed condensate in the hot water supplied to the tub 8,
The overflow pipe 10 of the water storage tank 9 interposed in the drain pipe 7 is connected to a neutralizer 11 so that excess condensed water is neutralized and then discharged to the outside.

【0005】[0005]

【作用】上記構成において、浴槽給湯時には凝縮水をエ
ゼクター6により吸引して浴槽8の湯に混入させること
ができるので、凝縮水中和器11の能力を節減して小型
化できる。この場合、凝縮水はPH値=3の強酸である
が、例えば1回の「お湯はり」で発生する凝縮水の量は
数10ミリリットル程度であり、一方浴槽には通常15
0リットル程度の水が使用され、また一般家庭において
入浴に使用される水量は全使用量の約半分であるから、
凝縮水は1000〜2000倍程度に希釈されることと
なってPH値=6以上となり、飲用としても問題にはな
らない。また給湯栓13のみを使用している間は、凝縮
水を貯湯タンク9に溜めておき、浴槽使用時にこれを消
することができるので、更に中和器11を小型化でき
る。更にシャワー用給湯配管12を凝縮水吸引用エゼク
ター6の下流側から分岐させて、シャワーを多用する夏
期においても凝縮水を浴槽給湯配管5で希釈処理できる
ようにすれば、上記貯水タンク9の使用と相まって、中
和器11を省略することも可能となる。
In the above construction, when hot water is supplied to the bathtub, the condensed water can be sucked by the ejector 6 and mixed with the hot water in the bathtub 8, so that the capacity of the condensed water neutralizer 11 can be reduced and the size can be reduced. In this case, the condensed water is a strong acid having a PH value = 3, for example, the amount of condensed water generated by one “hot water streak” is about several tens of milliliters, while the amount of water in a bathtub is usually about 15 ml.
About 0 liters of water is used, and the amount of water used for bathing in ordinary households is about half of the total usage,
The condensed water is diluted to about 1000 to 2000 times, and has a PH value of 6 or more, so that there is no problem for drinking. Also, while only the hot water tap 13 is used, the condensed water is stored in the hot water storage tank 9 and can be digested when the bathtub is used, so that the neutralizer 11 can be further downsized. Further, if the shower hot water supply pipe 12 is branched from the downstream side of the condensed water suction ejector 6 so that the condensed water can be diluted by the bathtub hot water supply pipe 5 even in the summertime when showers are frequently used, the use of the water storage tank 9 can be improved. Therefore, the neutralizer 11 can be omitted.

【0006】[0006]

【実施例】図1は本発明の一実施例を示したもので、ガ
スバーナ1で加熱される給湯用熱交換器は上下二段2
a,2bに分けられており、下段で温水を80〜90℃
まで加熱して200℃前後まで温度低下した排ガスは、
上段で水道水を予熱して、例えば70〜90℃まで温度
低下し、その際に排ガス中に含まれていた水蒸気が凝縮
して、上下の熱交換器2a,2bの中間に設けられてい
る受け皿3に流下し、一旦貯水タンク9に溜められたの
ち、排水管7によってエゼクター6の注入口へ送られ
る。一方熱交換器2a,2bを経た給湯配管4から、浴
槽給湯配管5が分岐されており、浴槽給湯配管5には逆
止弁14を介して凝縮水吸引用エゼクター6が介装さ
れ、このエゼクター6の注入口に受け皿3からの排水管
7が接続されている。エゼクターは、断面積を小さくし
て流速を大きくした隘路に、側方から注入路を開口させ
たものであり、この場合は水道圧によって浴槽8へ供給
される温水に凝縮水を吸引させるようにしたものであ
る。
FIG. 1 shows an embodiment of the present invention, in which a heat exchanger for hot water supply heated by a gas burner 1 has two upper and lower stages.
a, 2b, hot water is 80-90 ° C at the bottom
Exhaust gas heated to around 200 ° C
In the upper stage, tap water is preheated to lower the temperature to, for example, 70 to 90 ° C., and at that time, water vapor contained in the exhaust gas is condensed and provided between the upper and lower heat exchangers 2a and 2b. After flowing down to the receiving tray 3 and temporarily stored in the water storage tank 9, it is sent to the injection port of the ejector 6 by the drain pipe 7. On the other hand, a bathtub hot water supply pipe 5 is branched from the hot water supply pipe 4 passing through the heat exchangers 2a and 2b. The bathtub hot water supply pipe 5 is provided with an ejector 6 for condensed water suction via a check valve 14, and this ejector A drain pipe 7 from the tray 3 is connected to the inlet 6. The ejector has an injection passage opened from the side in a narrow passage having a reduced cross-sectional area and an increased flow velocity. In this case, the condensed water is drawn into hot water supplied to the bathtub 8 by tap water pressure. It was done.

【0007】貯水タンク9には、上部にオーバーフロー
管10が接続されており、浴槽8が使用されずに給湯栓
13のみが使用されている間は、貯水タンク9に凝縮水
が溜るので、余った凝縮水をオーバーフローさせ、中和
器11に送って中和処理したのち外部へ排出する。また
エゼクター6の下流側の浴槽給湯配管5からシャワー用
給湯配管12が分岐されており、夏期などに浴槽を使用
せずシャワーを多用する家庭でも、冬期と同様に浴槽給
湯配管5で凝縮水が処理されるようになっており、従っ
てこの場合には、ユーザの選択によって中和器11を省
略することも可能である。
[0007] An overflow pipe 10 is connected to the upper part of the water storage tank 9, and condensed water is accumulated in the water storage tank 9 while the hot tub 13 is used without using the bathtub 8. The condensed water overflows and is sent to a neutralizer 11 where it is neutralized and then discharged outside. Also, a shower hot water supply pipe 12 branches off from the bathtub hot water supply pipe 5 on the downstream side of the ejector 6, and even in a home where a shower is frequently used without using a bathtub in summer or the like, condensed water is supplied to the bathtub hot water supply pipe 5 as in winter. In this case, the neutralizer 11 can be omitted according to the user's selection.

【0008】本発明では、浴槽の湯に排ガス中の炭酸ガ
スを溶解させる所謂炭酸風呂の機能を持たせている。す
なわち浴槽給湯配管5の上記シャワー給湯配管12への
分岐点の下流側には、「お湯はり」電磁弁15を介し
て、第二のエゼクターすなわち排ガス吸引用エゼクター
16が介装され、上下の熱交換器2a,2bを通った排
ガスの一部が、このエゼクター16の注入口に導入され
ており、更にその下流側に気水分離器17が介装されて
いる。気水分離器17としては、エア抜き弁あるいは上
部にエア抜き孔を有する貯水タンクを用いることができ
る。エゼクター16と気水分離器17の間の配管内で、
温水中に排ガス中の炭酸ガスが溶解し、余剰のガスが気
水分離器17から外部に排出される。なお中和器11を
省略する場合には、凝縮水吸引用エゼクター6から排ガ
スを吸引することも起こり得るので、排ガス吸引用エゼ
クター16を使用しない場合でも、気水分離器17は設
けておく必要がある。
In the present invention , a so-called carbonated bath function is provided for dissolving carbon dioxide in exhaust gas in hot water in a bathtub. That is, a second ejector, that is, an exhaust gas suction ejector 16 is disposed downstream of the junction of the bathtub hot water supply pipe 5 and the shower hot water supply pipe 12 through a “hot water beam” solenoid valve 15, and the upper and lower heat sources are disposed. A part of the exhaust gas that has passed through the exchangers 2a and 2b is introduced into the injection port of the ejector 16, and a steam separator 17 is further interposed downstream. As the steam separator 17, an air release valve or a water storage tank having an air release hole in the upper part can be used. In the pipe between the ejector 16 and the steam separator 17,
The carbon dioxide gas in the exhaust gas is dissolved in the warm water, and the surplus gas is discharged from the steam separator 17 to the outside. If the neutralizer 11 is omitted, the exhaust gas may be sucked from the condensed water suction ejector 6, so that even when the exhaust gas suction ejector 16 is not used, the steam separator 17 must be provided. There is.

【0009】[0009]

【発明の効果】本発明によれば上述のように、高効率給
湯のために発生する凝縮水を、浴槽給湯時にエゼクター
により吸引して浴槽の湯に混入させることができる
に、給湯栓のみを使用している間は凝縮水を貯湯タンク
に溜めておいて、浴槽使用時にこれを消化することがで
きるので、従来大きな設置スペースを必要とする上に、
損耗の激しかった凝縮水中和器を小型化することができ
という利点がある。
According to the present invention as described above, on the condensed water generated due to the high efficiency water can be mixed into hot water bath by suction by ejector at bathtub hot water
The condensate is stored in a hot water storage tank while only the hot water tap is used.
Can be digested when using the bathtub.
It requires a large installation space,
The condensed water neutralizer, which was severely worn, can be downsized.
There is an advantage of that.

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

【図1】本発明の一実施例の系統図。FIG. 1 is a system diagram of one embodiment of the present invention.

【図2】従来例の系統図。FIG. 2 is a system diagram of a conventional example.

【符号の説明】[Explanation of symbols]

1 ガスバーナ 2a 上段熱交換器 2b 下段熱交換器 3 受け皿 4 給湯配管 5 浴槽給湯配管 6 凝縮水吸引用エゼクター 7 排水管 8 浴槽 9 貯水タンク 10 オーバーフロー管 11 中和器 12 シャワー給湯配管 13 給湯栓 14 逆止弁 15 「お湯はり」電磁弁 16 排ガス吸引用エゼクター 17 気水分離器 DESCRIPTION OF SYMBOLS 1 Gas burner 2a Upper heat exchanger 2b Lower heat exchanger 3 Receiving tray 4 Hot water supply pipe 5 Bath tub hot water pipe 6 Ejector for condensed water suction 7 Drain pipe 8 Bath tub 9 Water storage tank 10 Overflow pipe 11 Neutralizer 12 Shower hot water pipe 13 Hot water tap 14 Check valve 15 "Hot water" solenoid valve 16 Ejector for exhaust gas suction 17 Steam-water separator

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) F24H 9/00 A47K 3/00 F24H 1/10 - 1/14 ──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int. Cl. 7 , DB name) F24H 9/00 A47K 3/00 F24H 1/10-1/14

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 ガスバーナで加熱される給湯用熱交換器
を上下二段に分け、その中間部に上段の熱交換器で発生
する凝縮水を受ける受け皿を設けて、給湯配管から分岐
した浴槽給湯配管にエゼクターを介装し、該エゼクター
の注入口に上記受け皿からの排水管を接続することによ
り、浴槽へ供給される温水に上記凝縮水を混入せしめる
と共に、上記排水管に貯水タンクを介装し、該貯水タン
クのオーバーフロー管を中和器に接続して、余剰の凝縮
水を中和処理したのち外部へ排出するようにしたことを
特徴とする高効率給湯装置。
1. A hot water supply heat exchanger heated by a gas burner.
Is divided into upper and lower stages, and generated in the middle part by the upper heat exchanger
With a receiving tray to receive condensed water from the hot water supply pipe
An ejector is interposed in the hot tub hot water supply pipe
By connecting the drain from the pan to the
And mix the above condensed water into the hot water supplied to the bathtub.
At the same time, a water storage tank is interposed in the drainage pipe,
Connect the overflow pipe of the
That water is neutralized and then discharged to the outside
High efficiency water heater.
JP8923093A 1993-03-24 1993-03-24 High efficiency water heater Expired - Fee Related JP3306162B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8923093A JP3306162B2 (en) 1993-03-24 1993-03-24 High efficiency water heater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8923093A JP3306162B2 (en) 1993-03-24 1993-03-24 High efficiency water heater

Publications (2)

Publication Number Publication Date
JPH06272965A JPH06272965A (en) 1994-09-27
JP3306162B2 true JP3306162B2 (en) 2002-07-24

Family

ID=13964952

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8923093A Expired - Fee Related JP3306162B2 (en) 1993-03-24 1993-03-24 High efficiency water heater

Country Status (1)

Country Link
JP (1) JP3306162B2 (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100474177B1 (en) * 2002-06-10 2005-03-08 주식회사 경동보일러 Condensing Gas Boiler using Cistern Tank
US6631623B1 (en) * 2002-09-05 2003-10-14 Wcm Industries, Inc. Condensate drain coupling and method of use thereof
JP2005127648A (en) * 2003-10-27 2005-05-19 Paloma Ind Ltd Water heater
CN104596086B (en) * 2015-01-16 2017-07-25 芜湖美的厨卫电器制造有限公司 Gas heater and its control method
CN111721004B (en) * 2017-03-09 2022-03-18 芜湖美的厨卫电器制造有限公司 Water heater and control method thereof
JP7097156B2 (en) * 2017-04-04 2022-07-07 リンナイ株式会社 Bathtub cleaning device
CN109140755A (en) * 2018-10-11 2019-01-04 浙江建设职业技术学院 A kind of gas heater waste heat reclaiming system and method

Also Published As

Publication number Publication date
JPH06272965A (en) 1994-09-27

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