JPH01193588A - Atmosphere gas furnace equipped with exhaust combustion gas refining device - Google Patents
Atmosphere gas furnace equipped with exhaust combustion gas refining deviceInfo
- Publication number
- JPH01193588A JPH01193588A JP1567988A JP1567988A JPH01193588A JP H01193588 A JPH01193588 A JP H01193588A JP 1567988 A JP1567988 A JP 1567988A JP 1567988 A JP1567988 A JP 1567988A JP H01193588 A JPH01193588 A JP H01193588A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- furnace
- port
- temperature
- cooler
- 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.)
- Pending
Links
- 239000007789 gas Substances 0.000 title claims abstract description 139
- 239000000567 combustion gas Substances 0.000 title abstract 5
- 238000007670 refining Methods 0.000 title description 2
- 238000002485 combustion reaction Methods 0.000 claims abstract description 25
- 230000001590 oxidative effect Effects 0.000 claims abstract description 25
- 238000010438 heat treatment Methods 0.000 claims abstract description 16
- 230000001681 protective effect Effects 0.000 claims description 13
- 239000000446 fuel Substances 0.000 claims description 7
- 238000000746 purification Methods 0.000 claims description 6
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 5
- 239000003546 flue gas Substances 0.000 claims description 5
- 238000010744 Boudouard reaction Methods 0.000 claims description 3
- 238000001816 cooling Methods 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 3
- 238000007599 discharging Methods 0.000 abstract 3
- 238000006243 chemical reaction Methods 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 6
- 239000000463 material Substances 0.000 description 3
- 239000000498 cooling water Substances 0.000 description 1
- 230000001687 destabilization Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000002341 toxic gas Substances 0.000 description 1
Landscapes
- Furnace Details (AREA)
Abstract
Description
【発明の詳細な説明】 本願発明は次に述べる問題点の解決を目的とする。[Detailed description of the invention] The present invention aims to solve the following problems.
(産業上の利用分野) この発明は保護ガス中で熱処理
材の熱処理をするようにしてある雰囲気炉に関し、更に
詳しくは、雰囲気炉における加熱装置から生じた燃焼排
ガスを精製して、その精製されたガスを炉内の保護ガス
として用いるようにしてある燃焼排ガス精製装置付雰囲
気炉に関するものである。(Industrial Application Field) The present invention relates to an atmospheric furnace that heat-treats heat-treated materials in a protective gas, and more specifically, it purifies combustion exhaust gas generated from a heating device in an atmospheric furnace, and The present invention relates to an atmospheric furnace equipped with a combustion exhaust gas purification device, which uses the gas as a protective gas in the furnace.
(従来の技術) このような雰囲気炉にあっては、加熱
装置から出てくる燃焼排ガスをガスクーラを通すことに
よって急冷し、その冷やされたガスを酸化性ガス除去装
置に通すことによって酸化性ガスを除去し、その後のガ
スを保護ガスとして雰囲気炉に戻すようにしてある。上
記のようなサイクルを行なう場合、上記燃焼排ガスは急
冷しないとブードア反応により平衡が崩れて組成が不安
定になり、使用不能となる。このことからして、上記ガ
スクーラにおいては大量の冷却水を用いて800〜90
0℃の燃焼排ガスを常温に近い温度例えば40℃程度ま
で急激に冷却し、それによって良質な保護ガスを雰囲気
炉に供給することを可能にしていた。しかしこのように
したのでは、雰囲気炉からの燃焼排ガスの高熱エネルギ
ーを無駄に廃棄してしまうことになって、熱エネルギー
上の損失が大きい問題点があった。それのみならず、上
記ガスクーラにおいては高温の燃焼排ガスを急冷する為
に多大の運転経費も要する問題点があり、それらの問題
点の解決が望まれている。(Prior art) In such an atmosphere furnace, combustion exhaust gas coming out of a heating device is rapidly cooled by passing through a gas cooler, and the cooled gas is passed through an oxidizing gas removal device to remove oxidizing gas. is removed and the remaining gas is returned to the atmosphere furnace as a protective gas. When carrying out the above cycle, unless the combustion exhaust gas is rapidly cooled, the equilibrium will be disrupted by the Boudouard reaction and the composition will become unstable, making it unusable. Based on this, in the above gas cooler, a large amount of cooling water is used to
The combustion exhaust gas at 0° C. is rapidly cooled to a temperature close to room temperature, for example, about 40° C., thereby making it possible to supply high-quality protective gas to the atmospheric furnace. However, in this case, the high thermal energy of the combustion exhaust gas from the atmospheric furnace is wasted, resulting in a large loss of thermal energy. In addition, the above-mentioned gas cooler has the problem of requiring a large amount of operating cost to rapidly cool the high-temperature combustion exhaust gas, and it is desired to solve these problems.
(発明が解決しようとする諜R) この発明は上記従来
の問題点を除き、炉から排出される燃焼排ガス中の熱エ
ネルギーを保護ガスとして炉内に戻されるガスと共に炉
内に戻すことができて省エネルギーを図ることができる
と同時に、ガスクーラの運転経費も低く抑えることがで
きるようにした燃焼排ガス精製装置付雰囲気炉を提供し
ようとするものである。(Intelligence to be Solved by the Invention) This invention eliminates the above-mentioned conventional problems and allows the thermal energy in the flue gas discharged from the furnace to be returned to the furnace together with the gas returned to the furnace as a protective gas. An object of the present invention is to provide an atmospheric furnace with a combustion exhaust gas purification device that can save energy and at the same time keep operating costs of the gas cooler low.
本願発明の構成は次の通りである。The configuration of the present invention is as follows.
(課題を解決する為の手段) 本願発明は前記請求の範
囲記載の通りの手段を講じたものであってその作用は次
の通りである。(Means for Solving the Problems) The present invention takes the measures as described in the claims above, and its effects are as follows.
(作用) 排出口から排出された燃焼排ガスは熱交換器
を通した後ガスクーラで急冷され、次に酸化性ガス除去
装置において酸化性ガスが除去される。除去後のガスは
上記熱交換器を通した後雰囲気炉における供給口に保護
ガスとして送り込まれる。上記の場合、排出口からガス
クーラに至るガスの熱は上記熱交換器において酸化性ガ
ス除去装置から供給口に至るガスに与えられる。その結
果供給口に至るガスは高温化する一方、ガスクーラに至
るガスは低温化する。(Operation) After the combustion exhaust gas discharged from the exhaust port passes through a heat exchanger, it is rapidly cooled in a gas cooler, and then the oxidizing gas is removed in an oxidizing gas removal device. The removed gas passes through the heat exchanger and is sent as a protective gas to the supply port in the post-atmosphere furnace. In the above case, the heat of the gas from the exhaust port to the gas cooler is given to the gas from the oxidizing gas removal device to the supply port in the heat exchanger. As a result, the gas reaching the supply port becomes hotter, while the gas reaching the gas cooler becomes colder.
(実施例)以下本願の実施例を示す図面について説明す
る。1は雰囲気炉、2は雰囲気炉に接続した精製装置を
示し、ガスクーラ3、ガス移送用のコンプレッサー4、
酸化性ガス除去装置5、熱交換器6を有する。(Embodiments) The drawings showing the embodiments of the present application will be explained below. 1 is an atmospheric furnace, 2 is a purification device connected to the atmospheric furnace, a gas cooler 3, a compressor 4 for gas transfer,
It has an oxidizing gas removal device 5 and a heat exchanger 6.
上記雰囲気炉1において、1oは中空の炉体で、内部に
は熱処理空間11を有し、そこには熱処理材12が周知
の如く存1されるようになっている。13は熱処理空間
11に保護ガスを供給する為の供給口を示す、14は炉
体10に取付けた加熱装置で、燃料の燃焼によって炉内
を加熱するようにしたちの例えばラジアントチューブが
用いられる。これにおいて、15は燃料供給口、16は
空気供給口、17は燃焼排ガスの排出口を夫々示す、1
8は炉体1oに取付けた攪拌装置で、周知の如くファン
19とそれを回動させる為のモータ20を有する。In the atmospheric furnace 1, 1o is a hollow furnace body, which has a heat treatment space 11 therein, in which a heat treatment material 12 is placed as is well known. Reference numeral 13 indicates a supply port for supplying protective gas to the heat treatment space 11. Reference numeral 14 indicates a heating device attached to the furnace body 10, which uses, for example, a radiant tube to heat the inside of the furnace by burning fuel. In this, 15 indicates a fuel supply port, 16 indicates an air supply port, and 17 indicates a combustion exhaust gas discharge port.
8 is a stirring device attached to the furnace body 1o, which, as is well known, has a fan 19 and a motor 20 for rotating the fan 19.
次に酸化性ガス除去装置5において、21.21は酸化
性ガス除去塔で、周知の如く二つが交互使用されるよう
になっている。22は吸引ポンプで、上記除去塔21の
再生を行う場合に使用されるものである。23は蓄圧タ
ンクで、上記二つの除去塔21.21を切り替える時の
ショックをやわらげる為のものである。Next, in the oxidizing gas removal device 5, 21 and 21 are oxidizing gas removal towers, and as is well known, the two are used alternately. Reference numeral 22 denotes a suction pump, which is used when regenerating the removal column 21. 23 is a pressure accumulator tank, which is used to soften the shock when switching between the two removal towers 21 and 21.
次に熱交換器6は周知のように第1の導入口25及び導
出口26と第2の導入口27及び導出口28を有し、そ
れらは図示の如く配管されている。Next, as is well known, the heat exchanger 6 has a first inlet 25, an outlet 26, a second inlet 27, and an outlet 28, which are piped as shown.
上記構成のものにあっては、雰囲気炉lの加熱装置14
において燃料供給口15に供給される燃料が空気供給口
16に供給される空気により空燃費λ−1,0以下で燃
焼される。燃焼により生じた熱により炉内の保護ガスが
加熱され、またそのガスはファン19で攪拌され、炉内
の熱処理材12の熱処理が行われる。上記加熱装置14
における燃焼によって生じた燃焼排ガスは排出口17か
ら排出される。その組成はCOが1〜2%、CO2が1
2〜14%Hz Oが12〜14%、H2が1〜2%で
あり、又その温度は800〜900 ’Cである。上記
燃焼排ガスは熱交換器6の第1導入口25から第1導出
口26に至る間において後述の精製ガスに熱を与え、自
体は低温化(例えば500℃)する。そのガスはガスク
ーラ3に至り、そこでブードア反応が生ずる温度領域以
下の温度でかつ酸化性ガス除去装置に送り込み可能な温
度例えば40’Cまで急冷される。In the case of the above configuration, the heating device 14 of the atmospheric furnace l
The fuel supplied to the fuel supply port 15 is combusted by the air supplied to the air supply port 16 at an air fuel consumption of λ-1.0 or less. The heat generated by the combustion heats the protective gas inside the furnace, and the gas is stirred by the fan 19, so that the heat-treated material 12 inside the furnace is heat-treated. The heating device 14
The combustion exhaust gas generated by the combustion in is discharged from the exhaust port 17. Its composition is 1-2% CO and 1% CO2.
2-14% Hz O is 12-14%, H2 is 1-2%, and the temperature is 800-900'C. The above-mentioned combustion exhaust gas gives heat to the purified gas, which will be described later, during the period from the first inlet 25 to the first outlet 26 of the heat exchanger 6, and the temperature itself is lowered (for example, to 500° C.). The gas reaches the gas cooler 3, where it is rapidly cooled to a temperature below the temperature range in which the Boudouard reaction occurs and to a temperature at which it can be sent to the oxidizing gas removal device, for example, 40'C.
冷却されたガスはコンプレフサ4を経た後、酸化性ガス
除去塔21に至りそこでCOzやH,O等の酸化性ガス
が除去されて精製ガス(精製発熱ガス)となる。そのガ
スは蓄圧タンク23に一時的に蓄えられた後、熱交換器
6をその第2導入口27から第2導出口28へ通過する
。その過程で、上記精製ガスはそれまで低温(例えば1
0℃)であったものが上記燃焼排ガスの顕熱を受は取っ
て高温化しく例えば350℃)、その高温化した精製ガ
スが雰囲気炉1の保護ガス供給口13に送られ、そこか
ら雰囲気炉1の熱処理空間11に送り込まれる。After passing through the compressor 4, the cooled gas reaches the oxidizing gas removal tower 21, where oxidizing gases such as COz, H, and O are removed, and becomes purified gas (purified exothermic gas). After the gas is temporarily stored in the pressure accumulator tank 23, it passes through the heat exchanger 6 from its second inlet 27 to its second outlet 28. In the process, the purified gas is kept at a low temperature (e.g. 1
The purified gas, which was at 0°C), absorbs the sensible heat of the combustion exhaust gas and becomes high in temperature (for example, 350°C), and the heated purified gas is sent to the protective gas supply port 13 of the atmosphere furnace 1, and from there the atmosphere It is sent into the heat treatment space 11 of the furnace 1.
上記のように加熱装置14での燃料の燃焼によりて生じ
た燃焼排ガスを精製する場合、上記燃焼排ガスはNXリ
ーンの使いかたである為、上記燃焼排ガスを熱交換器6
で一旦冷却しその後ガスクーラ3で急冷しても、ガスの
平衡の崩れによる組成の不安定化は極めて僅かである−
0例えば熱交換器の第1導出口26におけるガスの組成
はcoが0.8〜1.8 %、COtが12.2〜14
.2%、H2Cが12.2〜14.2%、H7が0.8
〜1.8%である。従って、上記のような精製ガスの利
用になんら問題を生じない。When refining the flue gas generated by combustion of fuel in the heating device 14 as described above, the flue gas is used for NX Lean, so the flue gas is transferred to the heat exchanger 6.
Even if it is cooled once in the gas cooler 3 and then rapidly cooled in the gas cooler 3, the destabilization of the composition due to the collapse of the gas equilibrium is extremely small.
For example, the composition of the gas at the first outlet 26 of the heat exchanger is 0.8 to 1.8% CO and 12.2 to 14% COt.
.. 2%, H2C 12.2-14.2%, H7 0.8
~1.8%. Therefore, no problem arises in the use of purified gas as described above.
次に上記熱交換器6の使用による省エネルギー効果を試
算した結果を示せば次の通りである。Next, the results of a trial calculation of the energy saving effect by using the heat exchanger 6 are as follows.
ラジアントチューブバーナ2本分 80 n(N/hの
とき 供給口13への精製ガスの予熱温度350℃この
ように上記熱交換器6の使用により金額にして例えば年
間100万円の省エネルギーを図ることができる。For 2 radiant tube burners: 80 n (N/h) Preheating temperature of purified gas to supply port 13: 350°C By using the heat exchanger 6, energy savings of, for example, 1 million yen per year can be achieved. Can be done.
(発明の効果) 以上のように一本発明にあっては、雰
囲気炉1における加熱装置14の排出口17から排出さ
れた燃焼排ガスを、ガスクーラ3で急冷し、酸化性ガス
除去装置5で酸化性ガスを除去して、そのガスを雰囲気
炉1における保護ガスの供給口13に炉内の保護ガスと
して戻して再使用できるは勿論のこと、
上記の場合、熱交換器6を設けたことによって、排出口
17からガスクーラ3へ行くガスの熱が、酸化性ガス除
去装置5から供給口13に行くガスに与えられて、前者
のガスは低温化する一方、後者のガスは高温化する特長
がある。(Effects of the Invention) As described above, in the present invention, the combustion exhaust gas discharged from the outlet 17 of the heating device 14 in the atmospheric furnace 1 is rapidly cooled in the gas cooler 3, and then oxidized in the oxidizing gas removal device 5. Of course, it is possible to remove the toxic gas and return the gas to the protective gas supply port 13 in the atmospheric furnace 1 for reuse as a protective gas in the furnace.In the above case, by providing the heat exchanger 6, , the heat of the gas going from the discharge port 17 to the gas cooler 3 is given to the gas going from the oxidizing gas removal device 5 to the supply port 13, so that the former gas becomes lower in temperature, while the latter gas becomes hotter. be.
このことは、第1点として、供給口13から炉内へ戻さ
れるガスに関しては、少ない熱エネルギーの付加のみで
炉内の高温のガスに馴染ませられる省エネルギー上の効
果と、
第2点として、ガスクーラ3へ行くガスに関しては、そ
のガスを必要充分な低温まで冷却する為にガスクーラ3
で低温化させねばならぬ度合が少なくて足り、ガスクー
ラ3の小型化による設備費の低減効果と設置スペースの
低減効果と運転経費を低く抑え得る効果等を同時に発揮
させられる有益性がある。The first point is that the gas returned from the supply port 13 into the furnace can be made to adapt to the high temperature gas in the furnace by adding only a small amount of thermal energy, and the second point is that: Regarding the gas going to gas cooler 3, the gas cooler 3 is used to cool the gas to a necessary and sufficient temperature.
The degree to which the temperature must be lowered is sufficient, and there is the advantage that the effect of reducing the equipment cost by downsizing the gas cooler 3, the effect of reducing the installation space, and the effect of keeping operating costs low at the same time.
図面は本願の実施例を示すもので、第1図は燃焼排ガス
精製装置付雰囲気炉の系統図。
1・・・雰囲気炉、3・・・ガスクーラ、5・・・酸化
性ガス除去装置、6・・・熱交換器、13・・・保護ガ
スの供給口、14・・・加熱装置、17・・・燃焼排ガ
スの排出口。The drawings show an embodiment of the present application, and FIG. 1 is a system diagram of an atmospheric furnace with a combustion exhaust gas purification device. DESCRIPTION OF SYMBOLS 1... Atmosphere furnace, 3... Gas cooler, 5... Oxidizing gas removal device, 6... Heat exchanger, 13... Protective gas supply port, 14... Heating device, 17... ...Exhaust port for combustion exhaust gas.
Claims (1)
た加熱装置が備えてある雰囲気炉を有し、上記加熱装置
における燃焼排ガスの排出口には、排出された燃焼排ガ
スをブードア反応が生ずる温度領域以下の温度でかつ酸
化性ガス除去装置に送り込み可能な温度まで急冷する為
のガスクーラを接続し、上記ガスクーラには、ガスクー
ラから送り出されたガス中から酸化性ガスを除去して、
除去後のガスを上記雰囲気炉における保護ガスの供給口
に送るようにした酸化性ガス除去装置を接続してある燃
焼排ガス精製装置付雰囲気炉において、上記酸化性ガス
除去装置と上記供給口との間には、酸化性ガス除去装置
から供給口へ至るガスを、上記排出口から排出された燃
焼排ガスの熱で高温化させる為の熱交換器を介設し、し
かも上記熱交換器は、上記排出口から上記ガスクーラへ
至る燃焼排ガスが、上記酸化性ガス除去装置から供給口
へ至るガスに熱が与えられることによって低温化される
よう、上記排出口とガスクーラとの間に介入させたこと
を特徴とする燃焼排ガス精製装置付雰囲気炉。It has an atmosphere furnace equipped with a heating device that heats the inside of the furnace by burning fuel, and the exhaust port of the combustion exhaust gas in the heating device has a temperature range in which the Boudouard reaction occurs in the discharged combustion exhaust gas. A gas cooler is connected to the gas cooler for rapidly cooling the gas to the following temperature and at a temperature that can be sent to the oxidizing gas removal device, and the gas cooler is connected to the gas cooler to remove the oxidizing gas from the gas sent out from the gas cooler.
In an atmospheric furnace with a flue gas purification device connected to an oxidizing gas removal device that sends the removed gas to a protective gas supply port in the atmospheric furnace, a connection between the oxidizing gas removal device and the supply port is provided. A heat exchanger is interposed between the oxidizing gas removal device and the supply port to raise the temperature of the gas from the oxidizing gas removal device to the supply port using the heat of the combustion exhaust gas discharged from the exhaust port, and the heat exchanger intervening between the exhaust port and the gas cooler so that the combustion exhaust gas flowing from the exhaust port to the gas cooler is cooled by heat being given to the gas flowing from the oxidizing gas removal device to the supply port; Features: Atmospheric furnace with combustion exhaust gas purification device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1567988A JPH01193588A (en) | 1988-01-26 | 1988-01-26 | Atmosphere gas furnace equipped with exhaust combustion gas refining device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1567988A JPH01193588A (en) | 1988-01-26 | 1988-01-26 | Atmosphere gas furnace equipped with exhaust combustion gas refining device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01193588A true JPH01193588A (en) | 1989-08-03 |
Family
ID=11895436
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1567988A Pending JPH01193588A (en) | 1988-01-26 | 1988-01-26 | Atmosphere gas furnace equipped with exhaust combustion gas refining device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01193588A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2012111995A (en) * | 2010-11-25 | 2012-06-14 | Jfe Steel Corp | Method for adjusting furnace atmosphere of continuous annealing furnace |
-
1988
- 1988-01-26 JP JP1567988A patent/JPH01193588A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2012111995A (en) * | 2010-11-25 | 2012-06-14 | Jfe Steel Corp | Method for adjusting furnace atmosphere of continuous annealing furnace |
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