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JPS5934959B2 - Heat recovery method - Google Patents
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JPS5934959B2 - Heat recovery method - Google Patents

Heat recovery method

Info

Publication number
JPS5934959B2
JPS5934959B2 JP1932377A JP1932377A JPS5934959B2 JP S5934959 B2 JPS5934959 B2 JP S5934959B2 JP 1932377 A JP1932377 A JP 1932377A JP 1932377 A JP1932377 A JP 1932377A JP S5934959 B2 JPS5934959 B2 JP S5934959B2
Authority
JP
Japan
Prior art keywords
water
heat
cooler
exhaust gas
heat transfer
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
JP1932377A
Other languages
Japanese (ja)
Other versions
JPS53105745A (en
Inventor
崇文 中原
誠 藤原
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP1932377A priority Critical patent/JPS5934959B2/en
Publication of JPS53105745A publication Critical patent/JPS53105745A/en
Publication of JPS5934959B2 publication Critical patent/JPS5934959B2/en
Expired legal-status Critical Current

Links

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  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Treating Waste Gases (AREA)

Description

【発明の詳細な説明】 従来電気炉、転炉等では1000°C近い高温の排ガス
が廃棄されている。
DETAILED DESCRIPTION OF THE INVENTION Conventionally, in electric furnaces, converters, etc., high temperature exhaust gas of nearly 1000°C is disposed of.

一般にこのような高温排ガスに対してはエネルギ節約の
観点から排ガスボイラを設けることが多い。
Generally, an exhaust gas boiler is often provided for such high-temperature exhaust gas from the viewpoint of energy saving.

しかしながら、これらの炉の場合、排ガス中に含まれる
ダスト量が非常に多いこと、炉の作業が間歇的であるこ
と等の理由から、殆ど排熱回収を行わず、冷却塔を用い
た間接冷却や水を直接スプレィする直接冷却等によって
排ガスを減温したのち集塵器に送っている。
However, in the case of these furnaces, because the amount of dust contained in the exhaust gas is extremely large and the furnace operation is intermittent, exhaust heat is rarely recovered and indirect cooling using cooling towers is used. The temperature of the exhaust gas is lowered by direct cooling, such as by direct spraying with water, and then sent to the dust collector.

本発明はこのような実情に鑑みて提案されたものであっ
て、大気中に開放された貯湯式のガス冷却器内の水溜り
部にダスト含有量の多い間歇的に発生する高温排ガスを
導入して、前記水溜り部の水を沸騰させるとともに、同
冷却器の水溜り部に配設された伝熱管に熱吸収媒体を流
して、同媒体を介して前記排ガスの熱を回収することを
特徴とする熱回収方法に係り、その目的とする処は、炉
の操業に悪影響を与えずに、簡単な回収装置によって有
効に清浄な熱エネルギを安定して回収する新規有用な熱
回収方法を供する点にある。
The present invention was proposed in view of these circumstances, and involves introducing high-temperature exhaust gas that is intermittently generated and has a high dust content into a water pool in a hot water storage type gas cooler that is open to the atmosphere. and boiling the water in the water reservoir, flowing a heat absorption medium through a heat transfer tube disposed in the water reservoir of the cooler, and recovering the heat of the exhaust gas through the medium. The purpose of this heat recovery method is to develop a new and useful heat recovery method that effectively and stably recovers clean thermal energy using a simple recovery device without adversely affecting the operation of the furnace. It is in the point of providing.

以下本発明を図示の実施例について説明する。The present invention will be described below with reference to the illustrated embodiments.

第1図において、1は貯湯式の冷却器で、その下部に炉
からの高温排ガスのダクト2が貫通され、同排ガスはダ
クト2の出口で所定の温度まで冷却されるようになって
いる。
In FIG. 1, reference numeral 1 denotes a hot water storage type cooler, through which a duct 2 for high-temperature exhaust gas from a furnace passes through the lower part of the cooler 1, and the exhaust gas is cooled to a predetermined temperature at the outlet of the duct 2.

なお前記ダクト2は大径に形成され、ダスト含有量の多
い排ガスによって、仮にダストの堆積があっても、簡単
に掃除できるようになっている。
The duct 2 is formed to have a large diameter so that even if dust is accumulated due to the exhaust gas containing a large amount of dust, it can be easily cleaned.

前記冷却器1は大容積で大気開放型に構成され、水を容
れた水溜り部1aの上部には熱吸収媒体の通るコイル状
若しくは群管状の伝熱管3が配設されている。
The cooler 1 has a large capacity and is open to the atmosphere, and a coiled or grouped heat transfer tube 3 through which a heat absorbing medium passes is disposed above a water reservoir 1a containing water.

前記冷却器1内の水は、必要に応じて液面調節計4によ
って給水弁5を開き、水を補給するようになっている。
The water in the cooler 1 is replenished by opening a water supply valve 5 using a liquid level controller 4 as necessary.

前記伝熱管3に接続された伝熱回路6は閉回路に構成さ
れ、循環ポンプ7によって水、その他N2 、He等の
ガス体、フレオンやエチレン等の液状物質よりなる熱吸
収媒体が循環されるようになっている。
The heat transfer circuit 6 connected to the heat transfer tube 3 is configured as a closed circuit, and a heat absorption medium made of water, other gases such as N2 and He, and liquid substances such as Freon and ethylene is circulated by a circulation pump 7. It looks like this.

なお前記冷却器1中の水は大気に開放されているので、
ダクト2を通る排ガスによって温度上昇して沸騰しても
その最高温度供100°Cであるから、前記回路6中の
媒体が水でも沸騰することはないが、媒体の循環を停止
した時等の安全を考慮すると若干の加圧をすることが望
ましい。
Note that since the water in the cooler 1 is open to the atmosphere,
Even if the temperature rises and boils due to the exhaust gas passing through the duct 2, the maximum temperature is 100°C, so even if the medium in the circuit 6 is water, it will not boil, but when the circulation of the medium is stopped, etc. Considering safety, it is desirable to apply some pressure.

8はこの加圧用のN2ボンベで9は加圧器を示す。8 is an N2 cylinder for this pressurization, and 9 is a pressurizer.

なお前記媒体として100℃で沸騰しないような液体を
使用した場合にはこのような装置は不要である。
Note that such a device is not necessary when a liquid that does not boil at 100° C. is used as the medium.

前記伝熱回路6には2次側熱交換器10内に延びる伝熱
部11が設けられ、同熱交換器10には給水部12と利
用部13とが接続されている。
The heat transfer circuit 6 is provided with a heat transfer section 11 extending into a secondary heat exchanger 10, and a water supply section 12 and a utilization section 13 are connected to the heat exchanger 10.

図示の実施例において、前記ダクト2内に矢印に示す如
く高温排ガスが流れると、冷却器1における水溜り部1
aの水の温度が上昇して沸騰を開始する。
In the illustrated embodiment, when high-temperature exhaust gas flows into the duct 2 as shown by the arrow, a water reservoir 1 in the cooler 1
The temperature of the water in a rises and begins to boil.

而して前記冷却器1は大気開放型であるので、最高10
0°Cまで温度上昇する。
Since the cooler 1 is open to the atmosphere, the maximum
The temperature rises to 0°C.

従って前記循環ポンプ7によって伝熱管3内を循環する
熱吸収媒体が、前記冷却器1中の沸騰水によって加温さ
れ、2次側熱交換器10における伝熱部11に供送され
、同熱交換器10に供給される冷水と熱交換される。
Therefore, the heat absorption medium circulating in the heat transfer tubes 3 by the circulation pump 7 is heated by the boiling water in the cooler 1, and is sent to the heat transfer section 11 in the secondary heat exchanger 10, where the heat absorption medium is Heat is exchanged with the cold water supplied to the exchanger 10.

従って必要に応じて利用部13の弁(図示せず)を開く
と、温水が供給され、給水管12より冷水が補給される
Therefore, when a valve (not shown) of the usage part 13 is opened as necessary, hot water is supplied and cold water is replenished from the water supply pipe 12.

ここにおいても水以外の媒体が利用可能であるが、一般
には水が最も利用され易い。
Although media other than water can be used here as well, water is generally the easiest to use.

なお前記熱交換器10で回収した熱を工業用の何かのプ
ロセスの予熱等に利用する場合には、前記熱交換器10
内に必要な流体を入れるとその効果が挙がる。
Note that when the heat recovered by the heat exchanger 10 is used for preheating of some industrial process, the heat exchanger 10
Putting the necessary fluid inside will increase its effectiveness.

第2図に示す実施例においては、前記伝熱管3に接続さ
れた伝熱回路6が開回路に構成され、その入口部14は
上水道等に接続されており、伝熱回路6に介装された弁
15を開くと温水が供給されるようになっている。
In the embodiment shown in FIG. 2, the heat transfer circuit 6 connected to the heat transfer tube 3 is configured as an open circuit, and its inlet portion 14 is connected to a water supply or the like, and the heat transfer circuit 6 is connected to the heat transfer circuit 6. When the valve 15 is opened, hot water is supplied.

なお図中、前記実施例と均等部分には同一符号が附され
ている。
In the figure, parts equivalent to those of the above embodiment are given the same reference numerals.

第3図及び第4図に示す実施例においては、大気に開放
された竪型の冷却器1の底部に、大径の排ガスダクト2
が接続され、同ダクト2より冷却器1内に供送された高
温排ガスは冷却器1底部に連通ずる垂直ガス通路16を
上昇し、冷却器1の上端に連通ずる排気ダクト17より
所定の温度にまで冷却されて排出される。
In the embodiment shown in FIGS. 3 and 4, a large-diameter exhaust gas duct 2 is installed at the bottom of a vertical cooler 1 that is open to the atmosphere.
is connected, and the high-temperature exhaust gas fed into the cooler 1 from the same duct 2 rises through the vertical gas passage 16 communicating with the bottom of the cooler 1, and then reaches a predetermined temperature through the exhaust duct 17 communicating with the upper end of the cooler 1. It is cooled down to a temperature and then discharged.

前記ガス通路16は多数の煙管18によって構成され、
外板19と煙管18群とによって囲繞された区域は水溜
り部1aに構成され、伝熱管3は煙管18群の間に配設
され、伝熱回路6に接続されている。
The gas passage 16 is constituted by a large number of smoke pipes 18,
The area surrounded by the outer plate 19 and the group of smoke tubes 18 constitutes a water reservoir portion 1a, and the heat transfer tubes 3 are arranged between the groups of smoke tubes 18 and connected to the heat transfer circuit 6.

なお図示の例では同回路6は閉回路に構成されているが
、開回路でもよい。
Although the circuit 6 is configured as a closed circuit in the illustrated example, it may be an open circuit.

図中前記実施例と均等部分には同一符号が附されている
In the figure, parts equivalent to those of the above embodiment are given the same reference numerals.

なお前記実施例による熱回収方法は第1図に示した実施
例の場合と同一であるから説明を省略する。
Note that the heat recovery method according to the embodiment described above is the same as that in the embodiment shown in FIG. 1, so a description thereof will be omitted.

本実施例の場合、冷却器1を竪型にすることによってダ
ストの堆積を防止し、有効に熱を回収するようにしたも
のである。
In the case of this embodiment, the cooler 1 is made vertical to prevent dust from accumulating and to effectively recover heat.

本発明においては前記したように、大気中に開放された
水溜り部を有する貯湯式のガス冷却器を使用して、同冷
却器中に間歇的に発生する高温排ガスを導入して水溜り
部の水を沸騰させることによって、冷却器内に配設され
た伝熱管に流された熱吸収媒体を介して間接的に前記排
ガスの熱を回収するようにしたので、前記水溜り部によ
り、間歇的に発生する排ガスの熱を平均化して利用し易
くなり、また前記したように排ガスの熱回収を間歇的と
することによって排ガス中のダストの除去を可能ならし
め、また前記水溜り部を大気に開放された沸騰形とする
ことにより冷却器中の水溜りの温度を定常化し、強制冷
却用の冷却塔を不要ならしめ、建設費、経常費を大幅に
節減しうるものである。
As described above, in the present invention, a hot water storage type gas cooler having a water reservoir portion open to the atmosphere is used, and high temperature exhaust gas generated intermittently is introduced into the cooler to create a water reservoir. By boiling the water, the heat of the exhaust gas is indirectly recovered through the heat absorption medium flowing through the heat transfer tube installed in the cooler. This makes it easier to use the heat of the exhaust gas that is generated by averaging it, and as mentioned above, by making the heat recovery of the exhaust gas intermittent, it becomes possible to remove dust from the exhaust gas, and the water pool is removed from the atmosphere. By using a boiling type that is open to water, the temperature of the water pool in the cooler can be stabilized, making a cooling tower for forced cooling unnecessary, and greatly reducing construction costs and ordinary costs.

以上本発明を実施例について説明したが、勿論本発明は
このような実施例にだけ局限されるものではなく、本発
明の精神を逸脱しない範囲内で種種の設計の改変を施し
うるものである。
Although the present invention has been described above with reference to embodiments, it goes without saying that the present invention is not limited to such embodiments, and that various design modifications can be made without departing from the spirit of the present invention. .

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

第1図は本発明に係る熱回収方法を実施するための熱回
収装置の一実施例の縦断面図、第2図は他の実施例の部
分縦断面図、第3図は更に他の実施例の縦断面図、第4
図は第3図の矢視IV−IV図である。 1・・・・・・冷却器、1a・・・・・・水溜り部、2
・・・・・・ダクト、3・・・・・・伝熱管、6・・・
・・・伝熱回路、7・・・・・・循環ポンプ。
FIG. 1 is a vertical sectional view of one embodiment of a heat recovery device for carrying out the heat recovery method according to the present invention, FIG. 2 is a partial vertical sectional view of another embodiment, and FIG. 3 is a further embodiment of another embodiment. Example longitudinal section, 4th
The figure is a view taken along arrows IV-IV in FIG. 1...Cooler, 1a...Water pool, 2
...Duct, 3...Heat transfer tube, 6...
...Heat transfer circuit, 7...Circulation pump.

Claims (1)

【特許請求の範囲】[Claims] 1 大気中に開放された貯湯式のガス冷却器内の水溜り
部にダスト含有量の多い間歇的に発生する高温排ガスを
導入して、前記水溜り部の水を沸騰させるとともに、同
冷却器の水溜り部に配設された伝熱管に熱吸収媒体を流
して、同媒体を介して前記排ガスの熱を回収することを
特徴とする熱回収方法。
1. Introducing intermittently generated high-temperature exhaust gas with a high dust content into a water pool in a hot water storage type gas cooler open to the atmosphere, boiling the water in the water pool, and cooling the water cooler. A heat recovery method comprising: flowing a heat absorption medium through a heat transfer tube disposed in a water reservoir, and recovering heat from the exhaust gas through the medium.
JP1932377A 1977-02-25 1977-02-25 Heat recovery method Expired JPS5934959B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1932377A JPS5934959B2 (en) 1977-02-25 1977-02-25 Heat recovery method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1932377A JPS5934959B2 (en) 1977-02-25 1977-02-25 Heat recovery method

Publications (2)

Publication Number Publication Date
JPS53105745A JPS53105745A (en) 1978-09-14
JPS5934959B2 true JPS5934959B2 (en) 1984-08-25

Family

ID=11996186

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1932377A Expired JPS5934959B2 (en) 1977-02-25 1977-02-25 Heat recovery method

Country Status (1)

Country Link
JP (1) JPS5934959B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113959231B (en) * 2021-10-25 2023-08-22 株洲火炬工业炉有限责任公司 A tin-smelting electric furnace tail gas treatment and waste heat utilization device

Also Published As

Publication number Publication date
JPS53105745A (en) 1978-09-14

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