JPS5854586Y2 - liquid heating device - Google Patents

liquid heating device

Info

Publication number
JPS5854586Y2
JPS5854586Y2 JP6877078U JP6877078U JPS5854586Y2 JP S5854586 Y2 JPS5854586 Y2 JP S5854586Y2 JP 6877078 U JP6877078 U JP 6877078U JP 6877078 U JP6877078 U JP 6877078U JP S5854586 Y2 JPS5854586 Y2 JP S5854586Y2
Authority
JP
Japan
Prior art keywords
pipe portion
liquid
heating device
discharge
closed loop
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
Application number
JP6877078U
Other languages
Japanese (ja)
Other versions
JPS54169941U (en
Inventor
芳博 滝尻
津芳 長迫
Original Assignee
大阪瓦斯株式会社
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 大阪瓦斯株式会社 filed Critical 大阪瓦斯株式会社
Priority to JP6877078U priority Critical patent/JPS5854586Y2/en
Publication of JPS54169941U publication Critical patent/JPS54169941U/ja
Application granted granted Critical
Publication of JPS5854586Y2 publication Critical patent/JPS5854586Y2/en
Expired legal-status Critical Current

Links

Description

【考案の詳細な説明】 本考案は、例えば塗装前の処理液等の被加熱液を加熱す
るのに用いられるもので、バーナにより噴出される高温
燃焼ガスを、液槽内に浸漬配置した伝熱管内に該伝熱管
の一端導入用管部分から導入するとともに該伝熱管の他
端排出用管部分から排出することにより、前記液槽内の
被加熱液を加熱すべく構成しであるいわゆる浸管式の液
加熱装置に関する。
[Detailed description of the invention] This invention is used to heat liquids to be heated, such as processing liquids before painting, and the high-temperature combustion gas ejected by a burner is transferred to a gas tank immersed in a liquid tank. A so-called immersion liquid is configured to heat the liquid to be heated in the liquid tank by introducing the heat exchanger tube into the heat exchanger tube through an inlet tube section at one end and discharging it from the other end discharge tube section. This invention relates to a tubular liquid heating device.

従来のこの種の液加熱装置においては、第3図に示すよ
うに、液槽a内に浸漬配置される伝熱管すとして、バー
ナCに連結されたその一端の導入用管部分dから加熱作
用部分eを経て他端の排出用管部分子に至る単純屈曲状
あるいは直線状の、換言すれば開ループ型の浸管にて構
成されるものであった。
In a conventional liquid heating device of this kind, as shown in FIG. It consisted of a simply bent or straight, in other words, an open-loop type immersion pipe, which reached the discharge pipe component at the other end through part e.

従って、加熱効率を良くするためには、屈曲数を多くし
て管長さを増したり、あるいは、管径を大きくすること
によって伝熱面積を増大させなければならなかった。
Therefore, in order to improve the heating efficiency, it was necessary to increase the heat transfer area by increasing the number of bends to increase the tube length or by increasing the tube diameter.

しかしながら、このような手段を採用する場合には、伝
熱管すが大型化して槽a内においてその占める体積が大
きくなるために、槽a内の有効作業スペースが圧迫され
て作業性に問題を生じる欠点があり、また、そのために
槽a自体を不当に大型化すると、装置全体の大型下を招
くばかりでなく、処理液量が増えるため、特に、温度分
布に均一性が要求される装置にあっては、液撹拌装置な
どを追設しなければならない、という新さな問題を生じ
る。
However, when such a method is adopted, the heat exchanger tube becomes larger and occupies a larger volume in tank a, which compresses the effective working space in tank a and causes problems in workability. However, if tank a itself is unduly enlarged, the overall size of the equipment will not only be reduced, but the amount of liquid to be processed will also increase, which is especially difficult for equipment that requires uniformity in temperature distribution. In this case, a new problem arises in that a liquid stirring device or the like must be additionally installed.

更に、屈曲数を増して管長さを増す手段によるときは、
管の流動抵抗が増大するために管内流速が低下すること
となり、また、管径を大きくする手段によるときにも、
ベルヌーイの定理から明らかなように、やはり管内流速
が低下することとなるために、対流伝熱係数が低下して
加熱効率の悪化を招く欠点がある。
Furthermore, when increasing the length of the pipe by increasing the number of bends,
As the flow resistance of the pipe increases, the flow velocity in the pipe decreases, and when the pipe diameter is increased,
As is clear from Bernoulli's theorem, since the flow velocity in the pipe also decreases, there is a drawback that the convective heat transfer coefficient decreases and the heating efficiency deteriorates.

そして、このような欠点を解消するためには、バーナC
として噴出圧力の大きい相当大型のものを用いて管内流
速ひいては対流伝熱係数を所定の値に維持するようにし
なければならない。
In order to eliminate these drawbacks, burner C
Therefore, it is necessary to use a fairly large pipe with a high jetting pressure to maintain the flow velocity in the pipe and thus the convective heat transfer coefficient at a predetermined value.

本考案は、かかる従来実情に鑑みてなされたものであっ
て、その目的は、噴出圧力の比較的小さい小型のバーナ
を用いながらも、伝熱管内の流速ひいては対流伝熱係数
を飛躍的に高め得るようにし、もって、伝熱管を、その
槽内において占める割合が小さい可及的に小型のものに
しながらも十分な加熱性能を発揮し得る液加熱装置を提
供せんとすることにある。
The present invention was developed in view of the existing circumstances, and its purpose is to dramatically increase the flow velocity in the heat transfer tube and the convective heat transfer coefficient while using a small burner with relatively low ejection pressure. Therefore, it is an object of the present invention to provide a liquid heating device that can exhibit sufficient heating performance while making the heat exchanger tube as small as possible and occupying a small proportion in the tank.

上記目的を遠戚すべく、本考案による液加熱装置は、冒
頭に記載した構成のものにおいて、前記伝熱管の導入用
管部分と排出用管部分との間に環状閉ループ管部分を形
成するとともに、前記導入用管部分を前記環状閉ループ
管部分に対して略その接線方向に配設し、かつ、前記排
出用管部分を前記環状閉ループ管部分に対してその流動
方向接線とは異なる方向に配設することによって、前記
バーナにより噴出導入される高温燃焼ガスの噴出エネル
ギーを利用して前記環状閉ループ管部分内において高温
燃焼ガスを循環させるべく構成しである、という特徴を
備えている。
In order to achieve the above object, the liquid heating device according to the present invention has the configuration described at the beginning, and includes forming an annular closed loop tube section between the introduction tube section and the discharge tube section of the heat transfer tube. , the inlet tube portion is disposed substantially tangentially to the annular closed loop tube portion, and the discharge tube portion is disposed in a direction different from the flow direction tangent to the annular closed loop tube portion. By providing this, the high-temperature combustion gas is configured to be circulated within the annular closed loop pipe section by utilizing the ejection energy of the high-temperature combustion gas ejected and introduced by the burner.

上記特徴構成によれば、下記のような種々の優れた効果
が発揮される。
According to the above characteristic configuration, various excellent effects as described below are exhibited.

即ち、(ア)バーナから噴出される高温燃焼ガスは、連
続的に環状閉ループ管部分に導入されるが、そのガス導
入方向が閉ループ管部分の流路接線方向となるために、
また、閉ループ管部分からのそのガス排出流路はその閉
ループ管部分内の流動方向とは異なる方向に屈曲させで
あることからその部分においである程度のガス排出抵抗
を生せしめることができるために、環状閉ループ管部分
を通過して帰還してきた高温燃焼ガスの一部は、前記バ
ーナのガス噴出エネルギーに基くイジェクタ効果によっ
て、新たに導入される高温燃焼ガスに吸引混合されるこ
とになり、これによって、閉ループ管部分におけるガス
流量は増大して必然的にその流速が高められ、従って、
対流伝熱係数が高められるのであり、 (イ)また、従来のように伝熱管内に導入した高温燃焼
ガスを、唯一回の加熱作用を行なわせた後でその全量を
そのまま排出するのでは無く、その一部を閉ループ管内
において循環させる構成としたことにより、高温燃焼ガ
スは実際の管長よりも長い管内を通過するのと同義とな
り、従って、その保有熱を可及的に効率よく加熱作用の
ために利用することができ、 (つ)故に、上記(ア)、(イ)の両効果が相俟って、
本考案によれば、高温燃焼ガス生成相のバーナとしては
、噴出圧力が小さな比較的小型のものを用いても、また
、伝熱管として液槽内に占める体積部分の小さな比較的
小型のものを用いても、極めて優れた加熱性能を発揮で
きるコンパクトなしかも作業スペースを十分に確保でき
る液加熱装置を得られるに至ったのである。
That is, (a) high-temperature combustion gas ejected from the burner is continuously introduced into the annular closed loop tube section, but since the gas introduction direction is tangential to the flow path of the closed loop tube section,
In addition, since the gas discharge flow path from the closed loop pipe section is bent in a direction different from the flow direction within the closed loop pipe section, a certain degree of gas discharge resistance can be generated in that section. A part of the high-temperature combustion gas that has passed through the annular closed-loop pipe section and returned is sucked and mixed with the newly introduced high-temperature combustion gas by the ejector effect based on the gas ejection energy of the burner. , the gas flow rate in the closed-loop pipe section is increased, necessarily increasing its flow rate, and thus:
The convection heat transfer coefficient is increased, and (a) the high-temperature combustion gas introduced into the heat exchanger tube is not directly discharged after performing one heating action as in the conventional method. By having a structure in which a part of the gas is circulated in a closed loop pipe, the high-temperature combustion gas is equivalent to passing through a pipe that is longer than the actual pipe length, and therefore, the retained heat is used as efficiently as possible for heating action. Therefore, both effects (a) and (b) above work together,
According to the present invention, a relatively small burner with low ejection pressure can be used as a burner for the high-temperature combustion gas generation phase, and a relatively small one with a small volume occupying a small volume in the liquid tank can be used as a heat transfer tube. Even when using the liquid heating device, we were able to obtain a compact liquid heating device that can exhibit extremely excellent heating performance and that can also secure a sufficient working space.

以下、本考案の実施例を第1図および第2図に基いて説
明する。
Embodiments of the present invention will be described below with reference to FIGS. 1 and 2.

槽1の外壁相当個所に高温燃焼ガスを高速度で噴出する
高速バーナ3を付設し、このバーナ3により噴出される
高温燃焼ガスを、液槽1内の底部に支持台6,6を介し
て浸漬配置した伝熱管2内に該伝熱管2の一端導入用管
部分2Aから導入するとともに該伝熱管2の他端排出用
管部分2Bから排出することにより、前記液槽1内の被
加熱管を加熱すべく構成しである液加熱装置において、
前記伝熱管2の導入用管部分2Aと排出管部分2Bとを
互いに近接させて配置するとともに、その両者2A、2
Bの間にほぼ楕円形の環状閉ループ管部分2Cを形威し
、かつ、前記導入用管部分2Aを前記閉ループ管部分2
Cに対して略その接線方向に配設し、かつ、前記排出用
管部分2Bを前記閉ループ管部分2Cに対してその流動
方向接線とは異なる方向に配設することによって、前記
バーナ3により噴出導入される高温燃焼ガスの噴出エネ
ルギーを利用して、前記閉ループ管部分2C内において
高温燃焼ガスをその平均流速を高めた状態で循環させる
べく構成したものである。
A high-speed burner 3 that spouts high-temperature combustion gas at high speed is attached to a portion corresponding to the outer wall of the tank 1, and the high-temperature combustion gas spouted by the burner 3 is sent to the bottom of the liquid tank 1 via supports 6, 6. The tubes to be heated in the liquid tank 1 are introduced into the heat exchanger tube 2 which is immersed and arranged through the introduction tube section 2A at one end of the heat exchanger tube 2, and discharged from the other end discharge tube section 2B of the heat exchanger tube 2. In a liquid heating device configured to heat a
The introduction pipe portion 2A and the discharge pipe portion 2B of the heat transfer tube 2 are arranged close to each other, and both 2A, 2
A substantially elliptical annular closed loop tube portion 2C is formed between the tube portions B, and the introduction tube portion 2A is connected to the closed loop tube portion 2.
C, and by arranging the discharge pipe portion 2B in a direction different from the flow direction tangent to the closed loop pipe portion 2C, the ejection by the burner 3 is The high temperature combustion gas is configured to be circulated within the closed loop pipe section 2C at an increased average flow velocity by utilizing the ejection energy of the introduced high temperature combustion gas.

そして、前記槽1の底壁1aおよび周側壁1bは良熱伝
導性、例えば、アルミ板などの金属板から構成し、かつ
、この槽1の外側に適宜間隔を隔てて断熱壁4を設ける
ことにより、この断熱壁4と槽1の各金属板壁1a、l
bとの間に、前記槽1の外周面全体に沿うガス排出用流
路5を形成するとともに、この排出用流路5の前記液槽
1の底壁1a下方に位置する部分に、前記伝熱管2の下
向き排出用管部分2Bを連通接続して、その排出口2a
から順次排出される排気ガスを槽1下部および側面に沿
って上昇排出させるように構成しである。
The bottom wall 1a and the peripheral side wall 1b of the tank 1 are made of a metal plate having good thermal conductivity, such as an aluminum plate, and a heat insulating wall 4 is provided on the outside of the tank 1 at an appropriate interval. Accordingly, this heat insulating wall 4 and each metal plate wall 1a, l of tank 1
A gas discharge channel 5 along the entire outer peripheral surface of the tank 1 is formed between the tank 1 and the gas discharge channel 5, and the gas discharge channel 5 is formed in a portion of the discharge channel 5 located below the bottom wall 1a of the liquid tank 1. The downward discharge pipe portion 2B of the heat pipe 2 is connected to the discharge port 2a.
The structure is such that the exhaust gas sequentially discharged from the tank 1 is upwardly discharged along the bottom and side surfaces of the tank 1.

この構成によれば、槽1の外壁1a、lbをも伝熱面積
として利用して排気ガスの残余保有熱を加熱作用に利用
でき、また、槽1外周面からの放熱を排気ガス膜および
断熱壁によって抑制し得るという保温効果も発揮され、
所期の加熱効率向上効果を一層高めることができる。
According to this configuration, the outer walls 1a and 1b of the tank 1 can also be used as a heat transfer area, and the remaining heat of the exhaust gas can be used for the heating effect. It also has a heat retention effect that can be suppressed by the wall,
The desired heating efficiency improvement effect can be further enhanced.

尚、図中7は排気ガスの前記排出用流路5から外部への
排出孔である。
In addition, numeral 7 in the figure is a discharge hole through which exhaust gas is discharged from the discharge flow path 5 to the outside.

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

図面は本考案に係る液加熱装置の実施の態様を例示し、
第1図は一部縦断側面図、第2図は平面図、そして、第
3図は従来装置の説明図である。 1・・・・・・液槽、2・・・・・・伝熱管、2A・・
・・・・導入用管部分、2A・・・・・・排出用管部分
、2C・・・・・・環状閉ループ管部分、4・・・・・
・断熱壁、5・・・・・・排出用流路。
The drawings illustrate embodiments of the liquid heating device according to the present invention,
FIG. 1 is a partially longitudinal side view, FIG. 2 is a plan view, and FIG. 3 is an explanatory diagram of a conventional device. 1...Liquid tank, 2...Heat transfer tube, 2A...
...Introduction pipe part, 2A...Discharge pipe part, 2C...Annular closed loop pipe part, 4...
・Insulating wall, 5... Discharge channel.

Claims (1)

【実用新案登録請求の範囲】 ■ バーナ3により噴出される高温燃焼ガスを、液槽1
内に浸漬配置した伝熱管2内に該伝熱管2の一端導入用
管部分2Aから導入するとともに該伝熱管2の他端排出
用管部分2Bから排出することにより、前記液槽1内の
被加熱液を加熱すべく構成しである液加熱装置であって
、前記伝熱管2の導入用管部分2Aと排出管部分2Bと
の間に環状閉ループ管部分2Cを形成するとともに、前
記導入用管部分2Aを前記環状閉ループ管部分2Cに対
して略その接線方向に配設し、かつ、前記排出用管部分
2Bを前記環状閉ループ管部分2Cに対してその流動方
向接線とは異なる方向に配設することによって、前記バ
ーナ3により噴出導入される高温燃焼ガスの噴出エネル
ギーを利用して前記環状閉ループ管部分2C内において
高温燃焼ガスを循環させるべく構成しであることを特徴
とする液加熱装置。 ■ 前記伝熱管2の導入用管部分2Aと排出用管部分2
Bとを互いに近接させて配置しであることを特徴とする
実用新案登録請求の範囲第■項に記載の液加熱装置。 ■ 前記伝熱管2の排出用管部分2Bを、前記液槽1と
その外側に設けた断熱壁4との間に形成される排出用流
路5に連通させであることを特徴とする実用新案登録請
求の範囲第■項に記載の液加熱装置。 ■ 前記排出用流路5を前記液槽1の外周面全体に沿わ
せて形成するとともに、前記伝熱管2の排出用管部分2
Bを、前記排出用流路5の前記液槽1の下方に位置する
部分に連通させであることを特徴とする実用新案登録請
求の範囲第■項に記載の液加熱装置。
[Scope of claim for utility model registration] ■ The high temperature combustion gas ejected by the burner 3 is
The liquid in the liquid tank 1 is introduced into the heat exchanger tube 2 immersed in the liquid tank 1 through the introduction pipe section 2A at one end of the heat exchanger tube 2, and discharged from the other end through the discharge pipe section 2B. A liquid heating device configured to heat a heating liquid, in which an annular closed loop pipe portion 2C is formed between the introduction pipe portion 2A and the discharge pipe portion 2B of the heat transfer tube 2, and the introduction pipe The portion 2A is disposed approximately in a tangential direction to the annular closed loop pipe portion 2C, and the discharge pipe portion 2B is disposed in a direction different from the flow direction tangent to the annular closed loop pipe portion 2C. A liquid heating device characterized in that the high temperature combustion gas is circulated within the annular closed loop pipe section 2C by utilizing the ejection energy of the high temperature combustion gas ejected and introduced by the burner 3. ■ The introduction pipe portion 2A and the discharge pipe portion 2 of the heat transfer tube 2
A liquid heating device according to claim 2 of the utility model registration claim, characterized in that B and B are arranged close to each other. (2) A utility model characterized in that the discharge pipe portion 2B of the heat transfer tube 2 is communicated with a discharge passage 5 formed between the liquid tank 1 and a heat insulating wall 4 provided on the outside thereof. A liquid heating device according to registered claim No. (2). (2) The discharge flow path 5 is formed along the entire outer peripheral surface of the liquid tank 1, and the discharge pipe portion 2 of the heat transfer tube 2 is formed along the entire outer peripheral surface of the liquid tank 1.
The liquid heating device according to claim 2, wherein B is communicated with a portion of the discharge flow path 5 located below the liquid tank 1.
JP6877078U 1978-05-22 1978-05-22 liquid heating device Expired JPS5854586Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6877078U JPS5854586Y2 (en) 1978-05-22 1978-05-22 liquid heating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6877078U JPS5854586Y2 (en) 1978-05-22 1978-05-22 liquid heating device

Publications (2)

Publication Number Publication Date
JPS54169941U JPS54169941U (en) 1979-11-30
JPS5854586Y2 true JPS5854586Y2 (en) 1983-12-13

Family

ID=28976956

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6877078U Expired JPS5854586Y2 (en) 1978-05-22 1978-05-22 liquid heating device

Country Status (1)

Country Link
JP (1) JPS5854586Y2 (en)

Also Published As

Publication number Publication date
JPS54169941U (en) 1979-11-30

Similar Documents

Publication Publication Date Title
CN207163301U (en) A kind of individual layer heat exchanger provided with efficient spoiler
JPS5549695A (en) Multitubular heat exchanger
JPS5854586Y2 (en) liquid heating device
JP2986982B2 (en) Small gas fired air heater
JPS5773392A (en) Corrugated fin type heat exchanger
CN209027326U (en) A kind of spiral winding heat-dissipating pipe
CN211178061U (en) Chemical reaction cauldron is with outer shell and tube cooling device
CN216205477U (en) Double-water-channel die-casting aluminum radiator
CN215930590U (en) Novel winding tube type steam heat exchanger
RU211314U1 (en) TUBE HEATING RADIATOR
CN218884715U (en) Constant temperature difference heat exchanger
CN212006826U (en) Embossed pipe heat exchanger
CN220911670U (en) Direct-fired hot-blast stove
CN216205472U (en) Novel heat exchanger that heat exchange efficiency is high
CN210645856U (en) Front-end atomization automatic telescopic spray gun for SNCR (selective non-catalytic reduction) system
JPS5565886A (en) Heat exchanger
JPS5839328Y2 (en) small heating device
JPS5541363A (en) Heat exchanger
CN206549616U (en) Outer half coil device of cooling heating
JPS6221878Y2 (en)
JPS54111002A (en) Condenser
JPS593263Y2 (en) Heat exchanger for liquid storage tank
KR0150726B1 (en) Fin for heat exchanger
JPS624809Y2 (en)
RU2018060C1 (en) Hot water boiler