Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH0587740B2 - - Google Patents
[go: Go Back, main page]

JPH0587740B2 - - Google Patents

Info

Publication number
JPH0587740B2
JPH0587740B2 JP61103599A JP10359986A JPH0587740B2 JP H0587740 B2 JPH0587740 B2 JP H0587740B2 JP 61103599 A JP61103599 A JP 61103599A JP 10359986 A JP10359986 A JP 10359986A JP H0587740 B2 JPH0587740 B2 JP H0587740B2
Authority
JP
Japan
Prior art keywords
water
heat exchange
hot air
porous body
combustion
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 - Lifetime
Application number
JP61103599A
Other languages
Japanese (ja)
Other versions
JPS62261854A (en
Inventor
Kingo Myahara
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.)
SUWAAKU KK
Original Assignee
SUWAAKU 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 SUWAAKU KK filed Critical SUWAAKU KK
Priority to JP10359986A priority Critical patent/JPS62261854A/en
Publication of JPS62261854A publication Critical patent/JPS62261854A/en
Publication of JPH0587740B2 publication Critical patent/JPH0587740B2/ja
Granted legal-status Critical Current

Links

Landscapes

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

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、熱交換多孔体に沿つて流下する冷水
に対し紆余曲折しながら焔上する燃焼熱気を何回
となく直接接触せしめて熱交換面積の拡大を図
り、小型の温水器であつても、大容量の冷水を速
かに高温湯とすることができる許りか、冷水と燃
焼熱気との直接熱交換作用によつて発生した湯気
を適確に吸湿し液化して除去し、湯気がそのまま
温水器外に排気されるのを防止できる直火式温水
器に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention aims to reduce the heat exchange area by bringing hot combustion air, which rises up into flames in many twists and turns, into direct contact with cold water flowing down along a heat exchange porous body. Even with a small water heater, it is possible to quickly turn a large volume of cold water into high-temperature hot water. This invention relates to a direct-fired water heater that absorbs moisture, liquefies it and removes it, and prevents steam from being exhausted outside the water heater as it is.

従来の技術 従来、流下する冷水に焔上する燃焼熱気を直接
接触せしめて、冷水を速かに高温湯とすることが
できる直火式温水器として実公昭57−28036号公
報に示されたものが知られており、これが構成は
第5図に示されたように、温水器本体1の上段位
置に散水シヤワー3を配設した吸熱室2を設け、
温水器本体1の下段に周囲を貯水槽5とした燃焼
室4を立体的に設け、しかも上記燃焼室4内には
バーナ6の一端をのぞませてある。そして前記吸
熱室2内には間隔をおいて複数段に亘り、仕切体
7……を敷設すると共に、上記仕切体7上には耐
熱耐蝕性材質により全体が通焔性に富むよう海綿
状に成形した吸熱材8……を温水器本体1の内壁
に、上記吸熱材8の周縁が密接するよう順次載置
せしめて散布された冷水と焔上する燃焼熱気とを
吸熱材8……の内部において万遍なく直接接触せ
しめて、冷水を速かに高温の湯とした後、該高温
の湯を下部の貯湯槽9に溜めた後、給湯管10を
介して適宜の場所に給湯せしめたものである。
BACKGROUND ART Conventionally, Japanese Utility Model Publication No. 57-28036 discloses a direct-fire water heater that can quickly turn cold water into high-temperature hot water by bringing hot combustion air into direct contact with flowing cold water. As shown in FIG. 5, this is a structure in which an endothermic chamber 2 in which a water shower 3 is disposed is provided in the upper position of the water heater main body 1.
A combustion chamber 4 surrounded by a water storage tank 5 is three-dimensionally provided in the lower part of the water heater main body 1, and one end of a burner 6 is visible inside the combustion chamber 4. In the heat absorption chamber 2, partitions 7 are laid in multiple stages at intervals, and the partitions 7 are made of a heat-resistant and corrosion-resistant material in a spongy shape so that the entire structure is highly flame permeable. The formed heat-absorbing materials 8 are sequentially placed on the inner wall of the water heater body 1 so that the edges of the heat-absorbing materials 8 are in close contact with each other, and the sprayed cold water and the burning hot air are transferred to the inside of the heat-absorbing materials 8. After the cold water is brought into direct contact evenly and quickly to hot water, the high temperature hot water is stored in the lower hot water storage tank 9, and then the hot water is supplied to an appropriate location via the hot water pipe 10. It is.

発明が解決しようとする問題点 ところで、上記公知の直火式温水器にあつて
は、燃焼室上方に熱交換用の吸熱材を複数段に亘
り配置して燃焼室内において発生した燃焼熱気を
上昇させ、吸熱材中を流下する冷水と直接接触さ
せる熱交換作用で冷水を高温湯としたものである
から、冷水と燃焼熱気との熱交換は総て燃焼室の
上部においてのみ行われ、熱交換面積は温水器の
大きさにより限定され大きくできない。
Problems to be Solved by the Invention Incidentally, in the above-mentioned publicly known direct-fired water heater, heat-exchanging heat-absorbing materials are arranged in multiple stages above the combustion chamber to raise the combustion hot air generated in the combustion chamber. Since the cold water is made into high-temperature hot water through the heat exchange effect of direct contact with the cold water flowing down through the heat absorbing material, all heat exchange between the cold water and the hot combustion air takes place only in the upper part of the combustion chamber, resulting in heat exchange. The area is limited by the size of the water heater and cannot be increased.

そして、上記熱交換面積の拡大を図るために吸
熱材の段数を多くすれば、燃焼熱気自体に背圧が
かかつて良好な燃焼状態の維持ができなくなる許
りか、燃焼熱気が吸熱材中を円滑に流通できなく
なつて、熱交換率が激減され高温の湯を連続して
得ることができない。その上、従来公知の直火式
温水器は直接的な熱交換作用で湯を得さしめよう
としたので、熱交換中において多量の湯気が発生
し、これが湯気をそのまま排気筒より直接外部に
排気させていたので、湯気は結露して液化した水
滴が排気筒端よりドレーンとなつた滴下され、温
水器の耐久性が損われるという問題点を有してい
た。
If the number of stages of the heat absorbing material is increased in order to expand the heat exchange area, the combustion hot air will build up back pressure on itself, making it impossible to maintain a good combustion state. As a result, the heat exchange rate is drastically reduced and hot water cannot be continuously obtained. Furthermore, since conventional direct-fired water heaters attempt to obtain hot water through direct heat exchange, a large amount of steam is generated during heat exchange, and this steam is directly discharged from the exhaust pipe to the outside. Because the water heater was vented, the steam condensed and liquefied water droplets dripped from the end of the exhaust pipe, impairing the durability of the water heater.

本発明は、給水器より中空筒状を呈し、かつ空
孔率が大きい竪型の熱交換多孔体中を沿流する冷
水に対し紆余曲折しながら焔上する燃焼熱気を何
回となく直接接触せしめて熱交換面積の拡大を図
り、小型の温水器であつても、大容量の冷水を速
やかに高温の湯とすることができる許りか、冷水
と燃焼熱気との直接接触熱交換作用によつて発生
した湯気を適確に吸湿し液化して除去し、湯気が
そのまま温水器外に排気されるのを防止すること
ができる直火式温水器を提供することを目的とし
ている。
In the present invention, the cold water flowing along the vertical heat exchange porous body, which has a hollow cylindrical shape and has a large porosity, is brought into direct contact many times with the hot combustion air that rises up the flames while twisting and turning. At the very least, it is possible to expand the heat exchange area and quickly turn a large volume of cold water into high-temperature hot water even with a small water heater. To provide a direct-fired water heater capable of properly absorbing moisture, liquefying and removing generated steam, and preventing the steam from being exhausted to the outside of the water heater as it is.

問題を解決するための手段 上記目的を達成するために、請求項1の直火式
温水器においては、温水器本体101の下部には
バーナ104の先端がのぞむ燃焼口102と全体
を漏斗状に形成した湯受体103を設け、上記温
水器本体101内の上部位置には冷水を収容した
給水器105を配設する。
Means for Solving the Problem In order to achieve the above object, in the direct fire type water heater according to claim 1, the lower part of the water heater body 101 has a combustion port 102 through which the tip of the burner 104 can be seen, and the entire body is shaped like a funnel. A hot water receptacle 103 is provided, and a water supply device 105 containing cold water is provided at an upper position within the water heater main body 101.

そして上記湯受体103と給水器105との間
には内部を複数段の燃焼熱気室108,108′,
108″……に仕切り、周囲を空孔率の大きな中
空網筒状に形成した竪型の熱交換多孔体106を
配設する。温水器本体101の内周面と熱交換多
孔体106の外周面との間には、上端側が排気通
路112を経て排気窓113に連通され、かつ燃
焼熱気室108より熱交換多孔体106を通して
周囲に噴出された燃焼熱気を熱交換多孔体106
を通して上段の燃焼熱気室108′へ順次導入せ
しめる複数段の熱気誘導室を配設して、複数段に
亘り設けた燃焼熱気室および熱気誘導室内を紆余
曲折しながら焔上する燃焼熱気と熱交換多孔体1
06に沿つて流下する冷水とを何回となく直接接
触させ、冷水を短時間で高温湯ならしめる。
Between the hot water receiver 103 and the water supply device 105, a plurality of combustion hot air chambers 108, 108' are arranged inside.
A vertical heat exchange porous body 106 which is partitioned into 108″... and whose periphery is formed into a hollow mesh tube shape with a large porosity is provided. A heat exchange porous body 106 is connected between the upper end side and the exhaust window 113 through an exhaust passage 112, and which transfers combustion hot air ejected from the combustion hot air chamber 108 to the surrounding area through the heat exchange porous body 106.
A plurality of stages of hot air induction chambers are arranged to sequentially introduce the hot air through the combustion hot air chamber 108' into the upper combustion hot air chamber 108', thereby exchanging heat with the combustion hot air that rises as it twists and turns inside the combustion hot air chamber and the hot air induction chamber provided over the plurality of stages. Porous body 1
The cold water flowing down along the 06 is brought into direct contact with the cold water several times to make the cold water into hot water in a short time.

熱交換多孔体106上に位置した給水器105
には給水口114を開口して、冷水を連続状に熱
交換多孔体106の壁面中を沿流せしめる。又、
請求項2の直火式温水器においては、温水器10
1の下部にはバーナ104の先端がのぞむ燃焼口
102と全体を漏斗状に形成した湯受体103を
設け、上記温水器本体101内の上部位置には冷
水を収容した給水器105を配設する。
Water supply device 105 located on heat exchange porous body 106
In this step, the water supply port 114 is opened to allow cold water to flow continuously through the wall surface of the heat exchange porous body 106. or,
In the direct-fired water heater according to claim 2, the water heater 10
A combustion port 102 through which the tip of a burner 104 can be seen and a hot water receiver 103 formed entirely in a funnel shape are provided at the bottom of the water heater body 101, and a water supply device 105 containing cold water is provided at an upper position within the water heater body 101. do.

そして、上記湯受体103と給水器105との
間には内部を複数段の燃焼熱気室108,10
8′,108″……に仕切り、周囲を空孔率の大き
な中空網筒状に形成した竪型の熱交換多孔体10
6を配設する。温水器本体101の内周面と熱交
換多孔体106の外周面との間には、上端側が排
気通路112を経て排気窓113に連通され、か
つ燃焼熱気室108より熱交換多孔体106を通
して周囲に噴出された燃焼熱気を熱交換多孔体1
06を通して上段の燃焼熱気室108′へ順次導
入せしめる複数段の熱気誘導室を配設して、複数
段に亘り設けた燃焼熱気室および熱気誘導室内を
紆余曲折しながら焔上する燃焼熱気と熱交換多孔
体106に沿つて流下する冷水とを何回となく直
接接触させ、冷水を短時間で高温湯ならしめる。
Between the hot water receiver 103 and the water supply device 105, a plurality of combustion hot air chambers 108, 10 are arranged inside.
Vertical heat exchange porous body 10 partitioned into 8', 108''... and formed around the periphery into a hollow mesh tube shape with a large porosity.
6 is placed. Between the inner circumferential surface of the water heater body 101 and the outer circumferential surface of the heat exchange porous body 106, the upper end side communicates with an exhaust window 113 via an exhaust passage 112, and the combustion hot air chamber 108 communicates with the surroundings through the heat exchange porous body 106. Heat exchange porous body 1 for the combustion hot air ejected to
A plurality of stages of hot air induction chambers are arranged to sequentially introduce the combustion hot air chamber 108' into the upper stage combustion hot air chamber 108' through the combustion hot air chamber 108'. The cold water flowing down along the exchange porous body 106 is brought into direct contact many times, and the cold water is turned into hot water in a short time.

熱交換多孔体106上に位置した給水器105
には給水口114を開口して、冷水を連続的に熱
交換多孔体106の壁面中を沿流せしめる。そし
て、排気窓113近傍位置の排気通路112中
に、該排気通路112をさえぎるように空孔率の
大きな網状の吸湿多孔体115を配設して排気通
路112に沿い排気窓113から外部に排気され
ようとした湯気を吸湿して結露し、液化した水滴
が排気窓113から外部に滴下しないように形成
したものである。
Water supply device 105 located on heat exchange porous body 106
Then, the water supply port 114 is opened to allow cold water to flow continuously through the wall surface of the heat exchange porous body 106. Then, in the exhaust passage 112 in the vicinity of the exhaust window 113, a net-like moisture absorbing porous body 115 with a large porosity is arranged so as to block the exhaust passage 112, and exhaust air is exhausted from the exhaust window 113 along the exhaust passage 112 to the outside. The exhaust window 113 is designed to absorb moisture from the steam that is about to escape, condense it, and prevent liquefied water droplets from dripping outside from the exhaust window 113.

作 用 請求項1の発明においては、燃焼口102より
下段の燃焼熱気室108内に燃焼熱気を送れば、
該燃焼熱気は、熱交換面積が広く、かつ空孔率が
大きく形成された熱交換多孔体106の壁面中を
通つて外側の熱気誘導室110に出た後、再び熱
気誘導室110より中段の燃焼熱気室108′内
に熱交換多孔体106の壁面中を通つて導入さ
れ、さらに中段の燃焼熱気室108′より熱交換
多孔体106より熱交換多孔体106の壁面中を
通り、中段の熱気誘導室110′に出た後、上段
の燃焼熱気室108′内に熱交換多孔体106の
壁面中を通つて入り、最後に上段の燃焼熱気室1
08″より熱交換多孔体106の壁面中を通つて
上段の熱気誘導室110″に出て、排気通路11
2を通り、排気窓113より温水器本体101外
に排気される。
Effect In the invention of claim 1, if the hot combustion air is sent from the combustion port 102 into the combustion hot air chamber 108 at the lower stage,
The combustion hot air passes through the wall surface of the heat exchange porous body 106, which has a large heat exchange area and a large porosity, and exits to the hot air induction chamber 110 on the outside. The hot air is introduced into the combustion hot air chamber 108' through the wall surface of the heat exchange porous body 106, and further passes through the wall surface of the heat exchange porous body 106 from the heat exchange porous body 106 from the middle stage combustion hot air chamber 108'. After exiting the induction chamber 110', it enters the upper combustion hot air chamber 108' through the wall surface of the heat exchange porous body 106, and finally enters the upper combustion hot air chamber 1.
08'', passes through the wall surface of the heat exchange porous body 106, exits to the upper hot air induction chamber 110'', and enters the exhaust passage 11.
2 and is exhausted to the outside of the water heater main body 101 through the exhaust window 113.

従つて、上述のように燃焼熱気が紆余曲折しな
がら下段より上段に向け順次流通する間に熱交換
多孔体106全体が強烈に加熱されると共に上部
に配設された給水器105も加熱される。
Therefore, as described above, while the hot combustion air twists and turns and sequentially flows from the lower stage to the upper stage, the entire heat exchange porous body 106 is intensely heated, and the water supply device 105 disposed above is also heated. .

そこで、上述のような状態のもとで給水口11
4より幾分昇温された温水を熱交換多孔体106
上へ給水すれば、該湯水は熱交換多孔体106の
広い多孔面に沿いながらゆつくりと流下する間に
下段より上段に向け順次紆余曲折しながら熱交換
多孔体106の壁面中を流通する燃焼熱気と間断
なく直接接触され効率的な熱交換作用が営まれる
と同時にその熱交換は上段より下段に向け順次高
温の燃焼熱気によつて促進されるため、湯水が熱
交換多孔体106の多孔面に沿つて上端側より下
端側に至る間に高温の湯となつて湯受体103内
に収集された後、適宜の場所に給湯される。
Therefore, under the above-mentioned conditions, the water supply port 11
Heat exchange porous body 106 for hot water whose temperature has been raised somewhat from 4.
When water is supplied to the top, the hot water slowly flows down along the wide porous surface of the heat exchange porous body 106, and the combustion occurs as it flows through the wall surface of the heat exchange porous body 106, twisting and turning from the lower stage to the upper stage. The hot air is in direct contact with the hot air without interruption, and an efficient heat exchange action is carried out. At the same time, the heat exchange is promoted by the high-temperature combustion air from the upper stage to the lower stage, so that the hot water flows through the porous surface of the heat exchange porous body 106. From the upper end to the lower end along the line, the hot water becomes high temperature and is collected in the hot water receiver 103, after which it is supplied to an appropriate location.

そして、上記温水作業の継続中においては、給
水器105も燃焼熱気で加熱され続けるので、冷
水は益々高温となり、熱交換多孔体106上に散
布される温水温度も高くなり、高温の湯が連続し
て得られる。又湯水との効率的な熱交換作用によ
り低温化された排熱気は、前記熱交換作用時に発
生した湯気と共に排気通路112を通り、排気窓
113から温水器本体101外に排気される。
又、第2発明にあつては、上記の如き直接的な熱
交換作用によつて排気通路112中に発生した大
量の湯気が熱交換作用により低温化された排熱気
と共に、排気通路112に沿つて排気窓113か
ら直接器外に排気されようとした時に湯気を多く
含んだ排熱気を、排気窓113近傍位置の排気通
路112中に、排気通路112をさえぎるように
配設した空孔率の大きな網状の吸湿多孔体115
中を流通せしめる間に吸湿させ、湯気を結露して
液化させ、発生した水滴を給水器105に沿わせ
て熱交換多孔体106上端側に滴下させこれを高
温化せしめる。
While the above-mentioned hot water work continues, the water supply device 105 also continues to be heated by the hot combustion air, so the cold water becomes increasingly hot, and the temperature of the hot water sprayed onto the heat exchange porous body 106 also increases, so that the hot water is continuously heated. It can be obtained by Furthermore, the exhaust hot air whose temperature has been lowered by the efficient heat exchange action with the hot water passes through the exhaust passage 112 together with the steam generated during the heat exchange action, and is exhausted to the outside of the water heater main body 101 through the exhaust window 113.
Further, in the second invention, a large amount of steam generated in the exhaust passage 112 due to the above-mentioned direct heat exchange action is carried along the exhaust passage 112 together with the exhaust hot air whose temperature has been lowered due to the heat exchange action. When the hot air containing a large amount of steam is directly exhausted from the exhaust window 113 to the outside of the device, the porosity is placed in the exhaust passage 112 near the exhaust window 113 so as to block the exhaust passage 112. Large net-like moisture absorbing porous material 115
While flowing through the water, moisture is absorbed, steam is condensed and liquefied, and the generated water droplets are dripped onto the upper end side of the heat exchange porous body 106 along the water supply device 105 to raise the temperature.

したがつて、排熱気中に含まれた湯気は排気通
路112中に設けられた吸湿多孔体115により
確実に液化して除去されるので、温水器本体10
1より外部に向け多くの湯気が排出されるのが防
止される。
Therefore, the steam contained in the exhaust hot air is reliably liquefied and removed by the moisture absorption porous body 115 provided in the exhaust passage 112, so that the water heater main body 10
1, more steam is prevented from being discharged to the outside.

実施例 以下に本発明に係る直火式温水器の各実施例を
説明する。
Examples Examples of the direct-fired water heater according to the present invention will be described below.

第1図および第2図において、101……は、
断面形状が円筒形状を呈する温水器本体であつ
て、該温水器本体101の下部に、燃焼口102
を上向きに開口し、かつ内部にバーナ104を内
蔵した截頭円錐筒状の湯受体103が配設されて
いる。そして上記温水器本体101内の上部には
冷水を収容した給水器105が配設されている。
106は、表面積が大きく、又三次元網状構成と
して接触反応率を高めた中空筒状を呈する竪型の
熱交換多孔体であつて、該熱交換多孔体106と
して例えばエバーライトスコツト(商品名)を基
材としてこれにセラミツク原料をコーテイング、
焼成したセラミツク多孔体、或は、熔解ステンレ
スを流し込み特殊薬剤で成形したアルミ発泡多孔
体又はステンレス発泡多孔体が考えられる。
In FIGS. 1 and 2, 101... is
The water heater main body has a cylindrical cross-sectional shape, and a combustion port 102 is provided at the lower part of the water heater main body 101.
A hot water receiver 103 is disposed in the shape of a truncated conical cylinder, which is opened upward and has a burner 104 built therein. A water supply device 105 containing cold water is disposed at the upper part of the water heater main body 101.
Reference numeral 106 is a vertical heat exchange porous body having a hollow cylindrical shape with a large surface area and a three-dimensional network structure that increases the contact reaction rate. ) is used as a base material and coated with ceramic raw material,
A fired ceramic porous body, an aluminum foam porous body or a stainless steel foam porous body formed by pouring molten stainless steel and molding with a special agent may be considered.

上記熱交換多孔体106の内部は、複数枚の熱
気仕切板107……により複数段(本発明の実施
例においては上、中、下の3段)に仕切られて、
内部を夫々燃焼熱気室108,108′,10
8″……に形成されており、しかも該熱交換多孔
体106は湯受体103と給水器105との間に
配設されている。
The inside of the heat exchange porous body 106 is partitioned into multiple stages (in the embodiment of the present invention, three stages: upper, middle, and lower) by a plurality of hot air partition plates 107.
The insides are respectively combustion hot air chambers 108, 108', 10.
8''..., and the heat exchange porous body 106 is disposed between the hot water receiver 103 and the water supply device 105.

上記温水器本体101の内周には上端側を開口
した貯水槽109が適当高さに亘り設けられてお
り、しかも、前記貯水槽109の内周面と熱交換
多孔体106の外周面との間には上端側が排気通
路112を経て温水器本体101の天板に開口し
た排気窓113に接続され、しかも内部を熱気仕
切板107,107間に位置するように夫々配設
された環状を呈する複数枚の熱気誘導仕切板11
1……により仕切られた複数段の熱気誘導室11
0,110′,110″……(本発明の実施例にお
いては、上、中、下3段)を設けて、下段の燃焼
熱気室108内に噴焔された燃焼熱気が、下段の
熱気誘導室110、中段の燃焼熱気室108′、
中段の熱気誘導室110′、上段の燃焼熱気室1
08″および上段の熱気誘導室110″内を紆余曲
折しながら順次誘導流通する間に何回となく熱交
換多孔体106の壁面中を円滑に流通せしめて、
下段より上段に向かつて順次高温となる燃焼熱気
により加熱せしめる。
A water storage tank 109 with an open upper end is provided on the inner periphery of the water heater main body 101 over an appropriate height, and the inner peripheral surface of the water storage tank 109 and the outer peripheral surface of the heat exchange porous body 106 are connected to each other. In between, the upper end side is connected to an exhaust window 113 opened in the top plate of the water heater main body 101 through an exhaust passage 112, and the inside is arranged so as to be located between the hot air partition plates 107, 107, respectively, and has an annular shape. Multiple hot air induction partition plates 11
A multi-stage hot air induction chamber 11 partitioned by 1...
0,110',110''... (in the embodiment of the present invention, upper, middle, and lower three stages) are provided so that the hot combustion air injected into the combustion hot air chamber 108 in the lower stage is guided to the hot air in the lower stage. chamber 110, middle combustion hot air chamber 108',
Middle stage hot air induction chamber 110', upper stage combustion hot air chamber 1
08'' and the upper hot air induction chamber 110'' while being guided and distributed in sequence while twisting and turning, the hot air is made to circulate smoothly through the wall surface of the heat exchange porous body 106 many times,
Heating is performed by hot combustion air that gradually becomes hotter from the lower stage to the upper stage.

114は、円筒状を呈する熱交換多孔体106
上端に冷水を給水させるために給水器105の底
部に開口した給水口である。
114 is a heat exchange porous body 106 having a cylindrical shape.
This is a water supply port opened at the bottom of the water supply device 105 for supplying cold water to the upper end.

115は、温水器本体101上端側の内周面
と、給水器105の外周面との間に形成した排気
通路112中に、該排気通路112をさえぎるよ
うに配設した空孔率の大きい中空筒状の吸湿多孔
体であつて、該吸湿多孔体115は、熱交換多孔
体106中を竪流下する冷水と横方向に沿つて何
回となく紆余曲折状に流通する燃焼熱気との直接
接触熱交換用により発生した多量の湯気と低温と
なつた排熱気と共に吸湿多孔体106中を流通す
る間に湯気を結露して液化し、これが水滴を給水
器105周面に沿わせて熱交換多孔体106上へ
滴下させて、湯気が排熱気と共に排気窓113よ
り直接外部に排気されるのを未然に防止せしめ
る。上記の吸湿多孔体115は熱交換多孔体10
5とその構成を同一にすれば、より効果を高める
ことができる。116は、貯水槽109の下部内
周面と湯受体103の外周面との間に形成した貯
湯槽であつて、該貯湯槽116には給湯管117
の基端側が装着されている。118は、先端側を
給水器105内に挿入開口した結水管であり、1
19は排気窓113に接続された吸引排気装置で
ある。120は、一端が給水器105に接続さ
れ、他端を貯水槽109内に挿入開口した給水管
である。したがつて、上記実施例の直火式温水器
にあつては、バーナ104および吸引排気装置1
19を運転すれば、その燃焼熱気は下段の燃焼熱
気室108より周囲下段の熱気誘導室110に出
て、次いで中段の燃焼熱気室108′に入り、さ
らに中段の熱気誘導室110′に出た後、上段の
燃焼熱気室108″に入り最後に上段の熱気誘導
室110″を経て排気通路112に出て排気窓1
13より吸引排気装置119により温水器本体1
01外に排気される。そして燃焼熱気が、上記の
ように紆余曲折しながら順次複数段の燃焼熱気室
108,108′,108″……および熱気誘導室
110,110′,110″内を流通する間に、熱
交換多孔体106全体は勿論のこと、貯水槽10
9および給水器105を加熱して、収容された冷
水を湯水とする。
Reference numeral 115 denotes a hollow hole with a high porosity that is arranged in the exhaust passage 112 formed between the inner peripheral surface of the upper end side of the water heater main body 101 and the outer peripheral surface of the water supply device 105 so as to block the exhaust passage 112. The moisture-absorbing porous body 115 is a cylindrical moisture-absorbing porous body, and the moisture-absorbing porous body 115 is in direct contact with the cold water flowing vertically in the heat exchange porous body 106 and the combustion hot air flowing in many twists and turns along the lateral direction. The steam condenses and liquefies while flowing through the moisture absorbing porous body 106 together with a large amount of steam generated by the heat exchange and the low-temperature exhaust air. The steam is dripped onto the body 106 to prevent the steam from being directly exhausted to the outside through the exhaust window 113 together with the exhaust heat. The above moisture absorbing porous body 115 is the heat exchange porous body 10
If the structure is the same as that of 5, the effect can be further enhanced. 116 is a hot water storage tank formed between the lower inner circumferential surface of the water storage tank 109 and the outer circumferential surface of the hot water receiver 103, and a hot water supply pipe 117 is connected to the hot water storage tank 116.
The proximal end of the is attached. 118 is a water condensation pipe whose tip end is inserted into the water supply device 105;
19 is a suction/exhaust device connected to the exhaust window 113. 120 is a water supply pipe whose one end is connected to the water supply device 105 and whose other end is inserted into the water tank 109 and opened. Therefore, in the direct-fired water heater of the above embodiment, the burner 104 and the suction/exhaust device 1
19, the combustion hot air exits from the lower combustion hot air chamber 108 to the surrounding lower hot air induction chamber 110, then enters the middle combustion hot air chamber 108', and then exits to the middle hot air induction chamber 110'. After that, it enters the upper stage combustion hot air chamber 108'', finally passes through the upper stage hot air induction chamber 110'', exits to the exhaust passage 112, and enters the exhaust window 1.
13 to the water heater body 1 by the suction/exhaust device 119.
01 is exhausted outside. Then, while the hot combustion air twists and turns as described above and sequentially flows through the multiple stages of combustion hot air chambers 108, 108', 108''... and hot air induction chambers 110, 110', 110'', Not only the entire body 106 but also the water tank 10
9 and the water supply device 105 to turn the stored cold water into hot water.

そこで、給水口114より円筒状の熱交換多孔
体106上に、又他の一部を給水管120を介し
て貯水槽109内に給水すれば、該湯水は熱交換
多孔体106の多孔面に沿いながらゆつくりと流
下する間に、下段より上段に向かうに従い順次高
温状態のもとに流通する燃焼熱気と直接接触さ
れ、効率的な熱交換が行われ、高温湯となつて貯
湯槽116内に貯湯される一方、貯水槽109よ
り高温湯となつて、上端開放側より溢流した高温
湯は、さらに熱交換多孔体106に沿つて流下す
る間に流通する燃焼熱気と直接接触され、さらに
高温湯となつて貯湯槽116内に貯湯され、最後
に給湯管117によつて適宜の場所に給湯され
る。
Therefore, if water is supplied from the water supply port 114 onto the cylindrical heat exchange porous body 106 and the other part through the water supply pipe 120 into the water storage tank 109, the hot water will flow onto the porous surface of the heat exchange porous body 106. As the hot water slowly flows along the flow, it comes into direct contact with the hot combustion air flowing in a high-temperature state from the lower stage to the upper stage, and efficient heat exchange takes place, turning into high-temperature hot water and discharging it into the hot water storage tank 116. While the hot water is stored in the water storage tank 109, the hot water that overflows from the open top side further comes into direct contact with the circulating hot combustion air while flowing down along the heat exchange porous body 106. The hot water becomes high temperature hot water and is stored in a hot water storage tank 116, and finally is supplied to an appropriate location via a hot water supply pipe 117.

ところで、上記の如き直接的な熱交換作用によ
り多量に発生した湯気は低温となつた排熱気と共
に排気通路112中を吸引排気装置119の吸引
作用で排気窓113へ向け流通される。ところが
排気窓113近傍位置の排気通路112中には空
孔率の大きな網状の吸湿多孔体115が配設され
ているので、前記多量の湯気を含んだ低温の排燃
焼熱気が吸湿多孔体115中を通過する間に湯気
は結露して液化され水滴となつて給水器105の
周面に沿つて滴下される。それ故、上記の如き温
水作業を長期に亘り継続しても、温水器本体10
1外に湯気が直接排気されることが防止され、長
期に亘り良好な温水作業を継続させることができ
る。
By the way, a large amount of steam generated by the above-mentioned direct heat exchange action is circulated through the exhaust passage 112 toward the exhaust window 113 by the suction action of the suction/exhaust device 119 together with the cooled exhaust air. However, since a mesh-like moisture absorbing porous body 115 with a large porosity is disposed in the exhaust passage 112 in the vicinity of the exhaust window 113, the low-temperature exhaust combustion heat containing a large amount of steam is absorbed into the moisture absorbing porous body 115. While passing through the water supply device 105, the steam condenses and becomes liquefied, becoming water droplets that drip along the circumferential surface of the water supply device 105. Therefore, even if the above-mentioned hot water work is continued for a long time, the water heater main body 10
This prevents steam from being directly exhausted to the outside, allowing good hot water work to continue over a long period of time.

第3図および第4図に示された第2実施例のも
のは、熱交換多孔体106を矩形の板状に形成し
た場合にあつても高温湯を連続に得ることができ
る直火式温水器であつて、第2実施例の直火式温
水器にあつては、温水器本体101′の形状を横
長角筒状に形成し、しかも温水器本体101′の
短辺側の下部一側に燃焼口102を設け、該燃焼
口102′に横型バーナ104′を配設すると共に
湯受体103′は全体を上面が開放された矩形漏
斗状に形成して内部に貯湯槽116′を設ける。
そして上記漏斗状を呈する湯受体103′と温水
器本体101′内の上部に配設した給水器10
5′との間に横長方向に沿つて2枚の矩形板状を
呈する熱交換多孔体106′,106′を間隔をお
いて対設せしめて、2枚の熱交換多孔体106′,
106′間に室を設ける。
The second embodiment shown in FIGS. 3 and 4 is a direct-fire hot water system that can continuously obtain high-temperature hot water even when the heat exchange porous body 106 is formed into a rectangular plate shape. In the case of the direct fire type water heater of the second embodiment, the shape of the water heater body 101' is formed into an oblong rectangular cylinder shape, and one side of the lower part of the short side of the water heater body 101' A combustion port 102 is provided at the combustion port 102', a horizontal burner 104' is disposed in the combustion port 102', and the hot water receiver 103' is formed as a whole into a rectangular funnel shape with an open top surface, and a hot water storage tank 116' is provided inside. .
The funnel-shaped hot water receiver 103' and the water supply device 10 disposed at the upper part of the water heater main body 101'
5', two heat exchange porous bodies 106', 106' having a rectangular plate shape are disposed opposite to each other at an interval along the horizontal direction.
A chamber is provided between 106'.

そして、上記室内を央部に湯水が溜るように凹
ませた複数枚の熱気仕切板107a,107a′,
107a″……により仕切つて、内部容積が下段よ
り上段に向け、順次小さくなつた複数の燃焼熱気
室108a,108a′,108a″,108aに
形成せしめて燃焼熱気の流通速度を早めると共に
温水器本体101′の左右両側内面と左右の熱交
換多孔体106′,106′の外面との間に、内部
が複数枚の熱気誘導仕切111′……により仕切
られた複数段の熱気誘導室110a,110a′,
110a″……を配設して燃焼熱気を第1実施例と
同様に紆余曲折状に流通せしめて給水器105′
に開口した給水口114′より熱交換多孔体10
6′,106′の多孔面に沿つて流下する湯水を熱
交換作用で高温湯とする。
Then, a plurality of hot air partition plates 107a, 107a', which are recessed so that hot water accumulates in the center of the room, are installed.
107a''... are formed into a plurality of combustion hot air chambers 108a, 108a', 108a'', 108a whose internal volumes become smaller in order from the lower stage to the upper stage, thereby accelerating the circulation speed of the combustion hot air and increasing the flow rate of the hot water heater body. A multi-stage hot air induction chamber 110a, 110a whose interior is partitioned by a plurality of hot air induction partitions 111', between the left and right inner surfaces of the left and right inner surfaces of the heat exchange porous body 101' and the outer surfaces of the left and right heat exchange porous bodies 106', 106'. ′、
110a''... is disposed to allow combustion hot air to flow in a twisting and turning manner in the same way as in the first embodiment.
The heat exchange porous body 10 is
The hot water flowing down along the porous surfaces of 6' and 106' is converted into high-temperature hot water by heat exchange.

前記漏斗状を呈する湯受体103′の左右両側
周壁には、適当数の落湯口121……を開口して
板状の熱交換多孔体106′,106′により熱交
換された高温湯が落湯口121……を経て湯受体
103′の底部に接続した給湯管122より適宜
の場所に給湯されるよう構成せしめる。又、温水
器本体101′内の上部位置に設けられた排気通
路112′中には排気窓113′を境として、その
両側に矩形板状の吸湿多孔体115′,115′を
配設して排気通路112′をさえぎるようにして、
低温となつた排熱気と共に排気窓113′より外
部に排気されようとした大量の湯気を結露して液
化し、これが水滴を給水器105′周面に沿わせ
て左右の熱交換多孔体106′,106′上へ滴下
させ、熱交換作用により高温湯とすることができ
る。
A suitable number of hot water drop ports 121 are opened on the left and right peripheral walls of the funnel-shaped hot water receiver 103', and high temperature hot water that has been heat exchanged by the plate-shaped heat exchange porous bodies 106', 106' is dropped. Hot water is supplied to an appropriate location from a hot water supply pipe 122 connected to the bottom of the hot water receiver 103' via sprues 121. In addition, rectangular plate-shaped moisture absorbing porous bodies 115', 115' are arranged in the exhaust passage 112' provided in the upper part of the water heater body 101' on both sides of the exhaust window 113'. so as to block the exhaust passage 112',
A large amount of steam that was about to be exhausted to the outside through the exhaust window 113' together with the low-temperature exhaust air is condensed and liquefied, causing water droplets to flow along the circumferential surface of the water supply device 105' and pass through the left and right heat exchange porous bodies 106'. , 106', and the hot water can be made into hot water by heat exchange action.

その上、前記実施例の直火式温水器にあつて
は、第4図鎖線で示した如く、必要に応じて燃焼
口102′と対向する面にも熱交換多孔体10
6′と同構成の熱交換多孔体106′および熱気誘
導室110aと同構成の熱気誘導室110aを設
けてもよい。
Furthermore, in the direct-fired water heater of the above embodiment, as shown by the chain line in FIG.
A heat exchange porous body 106' having the same configuration as 6' and a hot air induction chamber 110a having the same configuration as the hot air induction chamber 110a may be provided.

前述した温水器本体101および熱交換多孔体
106はその横断面形状を他の任意断面形状に形
成せしめてもよいことは勿論である。
Of course, the water heater main body 101 and the heat exchange porous body 106 described above may have other arbitrary cross-sectional shapes.

発明の効果 要するに本発明は、前記のような技術的手段を
有するので、燃焼口102より噴焔された燃焼熱
気を、熱交換多孔体106の内側に亘り配設され
た複数段の燃焼熱気室108,108′,10
8″……と外側に亘り配設された複数段の熱気誘
導室110,110′,110″……内を下段より
上段に向け交互に、しかも周囲を空孔率の大きな
中空網筒状の熱交換多孔体106中を必らず通過
するように順次流通せしめて、燃焼熱気と冷水と
の直接熱交換面積の拡大と接触時間の増大を極力
図つて、大容量の冷水といえども一回の竪流下の
熱交換作用により高温湯として湯受体103内に
落入させることができる許りか、燃焼熱気はその
流通がよいことで、燃焼熱気に背圧が加えられ
ず、長期に亘り効率的な温水作業を行わせること
ができると共に給水器105は流通する燃焼熱気
で運転開始時より加熱されるため、熱交換多孔体
106に給水される時には湯水となつて熱交換効
率をより一層高め、瞬時に高温湯を得ることがで
きるは勿論のこと、湯水作業中に発生した湯気が
低温となつた排熱気とともに排気通路112を通
つて排気窓113より温水器本体101外に排気
されるのを、排気窓113近傍位置の排気通路1
12中に配設した空孔率の大きな網状の吸湿多孔
体115により結露させて液化し、熱交換多孔体
106上に還元して湯とすることができ、その結
果、排気窓113より水滴が外部に滴下すること
で生ずる腐蝕をなくし、直火式温水器の寿命を長
くできる効果を奏する。
Effects of the Invention In short, the present invention has the above-mentioned technical means, so that the combustion hot air jetted from the combustion port 102 is transferred to a plurality of stages of combustion hot air chambers arranged inside the heat exchange porous body 106. 108,108',10
8''... and multiple stages of hot air induction chambers 110, 110', 110''... arranged over the outside, the insides of which are alternately directed from the lower to the upper, and surrounded by a hollow net cylindrical chamber with a large porosity. The heat exchange porous body 106 is made to flow through the porous body 106 in order to expand the direct heat exchange area and contact time between the hot combustion air and the cold water, so that even a large volume of cold water can be cooled at once. Due to the heat exchange effect of the vertical flow, hot water can fall into the hot water receiver 103 as high-temperature hot water, and due to the good circulation of the combustion hot air, no back pressure is applied to the combustion hot air, resulting in high efficiency over a long period of time. In addition, since the water supply device 105 is heated from the start of operation by the circulating hot combustion air, when the water is supplied to the heat exchange porous body 106, it becomes hot water, further increasing the heat exchange efficiency. Not only can high-temperature hot water be obtained instantaneously, but also the steam generated during the hot water operation is exhausted from the water heater main body 101 through the exhaust passage 112 through the exhaust window 113 along with the cooled exhaust air. , the exhaust passage 1 located near the exhaust window 113
Dew can be condensed and liquefied by the net-like moisture absorption porous body 115 with a large porosity disposed in the heat exchange porous body 106, and can be reduced to hot water on the heat exchange porous body 106. As a result, water droplets are released from the exhaust window 113. It has the effect of eliminating corrosion caused by dripping outside and extending the lifespan of direct-fired water heaters.

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

図面は本発明に係る直火式温水器の各種実施例
を示すものであつて、第1図および第2図は第1
実施例であつて、第1図は一部を切欠した縦断正
面図、第2図は第1図A−A線矢視方向の横断平
面図、第3図および第4図は第2実施例であつ
て、第3図は一部を切欠した縦断正面図、第4図
は第3図B−B線矢視方向の横断平面図、第5図
は従来例の一部切欠した縦断正面図である。 101…温水器本体、102…燃焼口、103
…湯受体、105…給水器、106…熱交換多孔
体、108,108′,108″…燃焼熱気室、1
10,110′,110″…熱気誘導室、112…
排気通路、113…排気窓、114…給水口、1
15…吸湿多孔体。
The drawings show various embodiments of the direct-fired water heater according to the present invention, and FIGS.
FIG. 1 is a longitudinal sectional front view with a part cut away, FIG. 2 is a cross-sectional plan view taken along the line A-A in FIG. 1, and FIGS. 3 and 4 are a second embodiment. FIG. 3 is a partially cutaway vertical sectional front view, FIG. 4 is a cross-sectional plan view taken along line B-B in FIG. 3, and FIG. 5 is a partially cutaway longitudinal sectional front view of the conventional example. It is. 101...Water heater body, 102...Combustion port, 103
... Hot water receiver, 105 ... Water supply device, 106 ... Heat exchange porous body, 108, 108', 108'' ... Combustion hot air chamber, 1
10, 110', 110''...Hot air induction chamber, 112...
Exhaust passage, 113...Exhaust window, 114...Water supply port, 1
15... Moisture-absorbing porous material.

Claims (1)

【特許請求の範囲】 1 下部に燃焼口および湯受体を設けた温水器本
体内の上部に給水器を配設したものにおいて、前
記湯受体と給水器との間に内部を複数段の燃焼熱
気室に仕切り、周囲を空孔率の大きな中空網筒状
に形成した竪型の熱交換多孔体を配設し、温水器
本体の内周面と熱交換多孔体の外周面との間に
は、上端側が排気通路を経て排気窓に連通し、か
つ燃焼熱気室より熱交換多孔体を通して周囲に噴
出された燃焼熱気を熱交換多孔体を通して上段の
燃焼熱気室へ順次導入せしめる複数段の熱気誘導
室を配設すると共に、上記給水器には熱交換多孔
体の壁面中を沿流せしめる給水口を開口したこと
を特徴とする直火式温水器。 2 下部に燃焼口および湯受体を設けた温水器本
体内の上部に給水器を配設したものにおいて、上
記湯受体と給水器との間に内部を複数段の燃焼熱
気室に仕切り、周囲を空孔率の大きな中空網筒状
に形成した竪型の熱交換多孔体を配設し、温水器
本体の内周面と熱交換多孔体の外周面との間に
は、上端側が排気通路を経て排気窓に連通し、か
つ燃焼熱気室より熱交換多孔体を通して周囲に噴
出された燃焼熱気を熱交換多孔体を通して上段の
燃焼熱気室へ順次導入せしめる複数段の熱気誘導
室を配設し、上記給水器には熱交換多孔体の壁面
中を沿流せしめる給水口を開口すると共に、排気
窓近傍位置の排気通路中には排気通路をさえぎる
ように空孔率の大きな網状の吸湿多孔体を配設し
たことを特徴とする直火式温水器。
[Scope of Claims] 1. A water heater in which a water heater is disposed at the upper part of the main body of the water heater, which has a combustion port and a hot water receiver provided at the lower part, in which a plurality of stages are arranged internally between the hot water receiver and the water dispenser. A vertical heat exchange porous body formed into a hollow net tube shape with a large porosity is installed between the combustion hot air chamber and the inner peripheral surface of the water heater body and the outer peripheral surface of the heat exchange porous body. The structure has a plurality of stages, the upper end of which communicates with the exhaust window via the exhaust passage, and which sequentially introduces the combustion hot air ejected from the combustion hot air chamber to the surrounding area through the heat exchange porous body through the heat exchange porous body to the upper combustion hot air chamber. A direct-fired water heater, characterized in that a hot air induction chamber is provided, and a water supply port is opened in the water supply device to allow water to flow along the wall surface of a heat exchange porous body. 2. In a water heater that has a combustion port and a hot water receiver installed at the bottom and a water supply device installed at the top of the main body, the interior is partitioned into multiple stages of combustion hot air chambers between the hot water receiver and the water supply device, A vertical heat exchange porous body whose periphery is formed into a hollow mesh tube shape with a high porosity is provided, and an exhaust gas is provided at the upper end between the inner circumferential surface of the water heater body and the outer circumferential surface of the heat exchange porous body. A multi-stage hot air induction chamber is installed that communicates with the exhaust window through a passage and that sequentially introduces the combustion hot air ejected from the combustion hot air chamber to the surrounding area through the heat exchange porous body and into the upper combustion hot air chamber through the heat exchange porous body. The water supply device has a water supply port that allows the water to flow along the wall of the heat exchange porous body, and a network of moisture absorption holes with a large porosity is provided in the exhaust passage near the exhaust window so as to block the exhaust passage. A direct fire type water heater characterized by the fact that a body is installed.
JP10359986A 1986-05-06 1986-05-06 Direct fire type water heater Granted JPS62261854A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10359986A JPS62261854A (en) 1986-05-06 1986-05-06 Direct fire type water heater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10359986A JPS62261854A (en) 1986-05-06 1986-05-06 Direct fire type water heater

Publications (2)

Publication Number Publication Date
JPS62261854A JPS62261854A (en) 1987-11-14
JPH0587740B2 true JPH0587740B2 (en) 1993-12-17

Family

ID=14358231

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10359986A Granted JPS62261854A (en) 1986-05-06 1986-05-06 Direct fire type water heater

Country Status (1)

Country Link
JP (1) JPS62261854A (en)

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4118618Y1 (en) * 1964-08-18 1966-08-30
JPS50440A (en) * 1973-05-09 1975-01-07
JPS5728036U (en) * 1980-07-24 1982-02-13

Also Published As

Publication number Publication date
JPS62261854A (en) 1987-11-14

Similar Documents

Publication Publication Date Title
RU2011942C1 (en) Tubular heat exchanger
JPH0587740B2 (en)
RU2069829C1 (en) Contact heat recovery unit
JPS62196550A (en) Direct fire type water heater
CN212384536U (en) Dewaxing recovery device for precision casting
CN210762322U (en) Holding vessel is used in bromine production
JPS62196548A (en) Direct fire type water heater
JPH0223950Y2 (en)
JPS5812815Y2 (en) Radiant heat transfer activated carbon regeneration device
JPS62196549A (en) Direct fire type water heater
JPH0350360Y2 (en)
JP3069918B2 (en) Direct fired water heater
SU1041815A2 (en) Heat-and-moisture exchanger
RU183136U1 (en) BAKING ROTARY FURNACE
JP3099130B2 (en) Direct fired water heater
CN105042609B (en) A kind of purifier for industrial vent stack waste gas
CN218281258U (en) Coal-fired flue gas ammonia water wet flue gas desulfurization equipment
JPS5813238Y2 (en) Open fire water heater
RU216163U1 (en) Device for melting and storing viscous petroleum products
JPH09152228A (en) Regenerator
CN113563904B (en) A coke oven heat storage chamber structure
JPS5916107Y2 (en) desuperheater
JPH0531405Y2 (en)
JPS5852426Y2 (en) Burnout prevention device for partition walls in direct-fired water heaters
JP2949553B2 (en) Heat exchanger in direct-fired water heater