JPS5815713B2 - Atmosphere heating furnace - Google Patents
Atmosphere heating furnaceInfo
- Publication number
- JPS5815713B2 JPS5815713B2 JP7997879A JP7997879A JPS5815713B2 JP S5815713 B2 JPS5815713 B2 JP S5815713B2 JP 7997879 A JP7997879 A JP 7997879A JP 7997879 A JP7997879 A JP 7997879A JP S5815713 B2 JPS5815713 B2 JP S5815713B2
- Authority
- JP
- Japan
- Prior art keywords
- gas
- furnace
- atmosphere
- oxygen
- heating furnace
- 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
Links
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- Furnace Details (AREA)
Description
【発明の詳細な説明】
本発明は熱効率を高め、燃料消費量を抑制する如くした
雰囲気加熱炉に関するもので競る。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an atmosphere heating furnace that increases thermal efficiency and suppresses fuel consumption.
更に詳細には、大気中の窒素成分と酸素成分とを分離精
製し、窒素成分を加勢rの保護雰囲気ガス午し不使用す
るとともに、猷素□成分を加熱バーナの燃焼酸素として
使用し、或は列熱バーナの燃焼用空気に混合添加し、加
熱バーナの燃焼効率を高め、燃料消費量を減少、抑制せ
しめる如くした雰囲気加熱炉に関する。More specifically, the nitrogen component and oxygen component in the atmosphere are separated and purified, the nitrogen component is not used as a protective atmosphere gas, and the sulfur component is used as combustion oxygen in a heating burner, or The present invention relates to an atmosphere heating furnace in which the combustion air of a row heat burner is mixed and added to increase the combustion efficiency of the heating burner and reduce or suppress fuel consumption.
従来大気中から窒素ガスを分離精製するさい、同時に分
離除去される酸素ガスは大気中に無駄に捨てられている
ため、これの有効な利用が望まれる。Conventionally, when nitrogen gas is separated and purified from the atmosphere, the oxygen gas that is separated and removed at the same time is wasted into the atmosphere, so it is desired to make effective use of this.
特に窒素ガスを雰囲気ガスの一部として使用する雰囲気
加熱炉に窒素ガスを添加する場合、大気中から精製した
窒素ガス以外の酸素ガスは大気中に捨てられている。In particular, when nitrogen gas is added to an atmosphere heating furnace that uses nitrogen gas as part of the atmospheric gas, oxygen gas other than nitrogen gas purified from the atmosphere is thrown away into the atmosphere.
□本発明者等は雰囲気加熱炉の雰囲気反して用
いられる窒素ガス精製時に発生する分離された酸素ガス
の以上の如き無駄を解消すべく杏発明をなしたものであ
る。□The present inventors have made the invention in order to eliminate the above-mentioned waste of the separated oxygen gas generated during the purification of the nitrogen gas used in the atmosphere of the atmosphere heating furnace.
本発明の目的は、大気を窒素ガスと酸素ガスとに分離精
製し、窒素ガスを加熱炉の保護雰囲気ガスと該加熱炉内
に投入する左ともに、酸素ガスをラジアントチューブ等
の加熱バーナの燃焼用酸素として単体、或は空気の混合
体として添加する如くした雰囲気加熱炉を提供する
従って本発明の目的は、前記酸素ガ哀の添加で燃焼温度
を著しく上昇せ、しめ、燃焼効率を高めるとともに、燃
焼用空気量を酸素ガス添加割合だけ減少せしめ、とれに
より燃焼廃ガスの持ち出す熱量が低減し、トータルとし
ての加熱炉の熱効率を高めることふ−で曇、′消費する
燃料ガス量を低減し、操業コス)&低減して経済上有利
である雰囲気加熱炉を提供する。The purpose of the present invention is to separate and refine the atmosphere into nitrogen gas and oxygen gas, to inject the nitrogen gas into the heating furnace as a protective atmosphere gas, and to burn the oxygen gas in a heating burner such as a radiant tube. Therefore, an object of the present invention is to provide an atmosphere heating furnace in which oxygen is added alone or as a mixture with air.The object of the present invention is therefore to significantly raise and reduce the combustion temperature by adding oxygen, thereby increasing the combustion efficiency. By reducing the amount of combustion air by the proportion of oxygen gas added, the amount of heat carried out by the combustion waste gas is reduced, increasing the overall thermal efficiency of the heating furnace. To provide an atmosphere heating furnace that is economically advantageous by reducing operating costs) and reducing costs.
又本発明の目的は、前記炉内の露点、二酸化炭素域は酸
氷量を測定して炭化水素系ガスを添加し、被処理物の酸
化、脱炭を調整、制御するようにした雰囲気加熱炉を提
供する。Another object of the present invention is to measure the dew point and the amount of acid ice in the carbon dioxide region in the furnace and add hydrocarbon gas to adjust and control the oxidation and decarburization of the material to be treated. Provide a furnace.
゛ 。次に、本発明の好適二実施例を添付図面
に従って詳述する。゛. Next, two preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings.
第1図は雰囲気加熱炉の縦断正面図を、第2図は同側面
図を示している。FIG. 1 shows a longitudinal sectional front view of the atmosphere heating furnace, and FIG. 2 shows a side view of the same.
本発明に用いられる加熱炉はラジアントチューブ型で、
加熱炉1は耐火材で構築せ乞炉本体2と、これの外側を
囲む外壁3とからなる。The heating furnace used in the present invention is a radiant tube type,
The heating furnace 1 consists of a furnace body 2 made of refractory material and an outer wall 3 surrounding the outside.
本体2の床2a上には被処理物Wの載置台4が設けられ
るとともに、炉室5内の左右に眸ラジアントチューブ6
.6が垂下配設されている。A mounting table 4 for the workpiece W is provided on the floor 2a of the main body 2, and radiant tubes 6 are provided on the left and right sides of the furnace chamber 5.
.. 6 is arranged hanging down.
ラジアントチューブ6.6は第2図に示される如くU字
型をなし、本体部6aが炉室5内に臨み、入口部6bが
炉本体2及び外壁3の天井2b、3bを縦通して上方に
露出し、又出口部6cも同様に天井2b、 3bを縦
通して上方に露出し、−気一道に接続されるラジアント
チ、ニープロの入口部6bゆ加熱バーナ7を備え、左右
のラジアントチューブ6二1,6−2の各バーナ7の部
分は糸路8を介、して燃料ガス供給源に接続され、燃料
ガス単体、或はこれと空気の混合体がバーナ7に供給さ
れる。The radiant tube 6.6 has a U-shape as shown in FIG. 2, with the main body 6a facing into the furnace chamber 5, and the inlet 6b passing vertically through the furnace main body 2 and the ceilings 2b and 3b of the outer wall 3 and extending upward. The outlet section 6c is also exposed upward through the ceilings 2b and 3b, and is connected to the air passageway. The portions of each burner 7, 621 and 6-2, are connected to a fuel gas supply source through a thread 8, and fuel gas alone or a mixture of fuel gas and air is supplied to the burner 7.
。以上咳おいて、炉1外には空気の分離装置を
設け、具体的には吸着塔8を設け、吸着塔8の上流は冷
却器、9を介して大気に連通せしめる。. In conclusion, an air separation device is provided outside the furnace 1, specifically an adsorption tower 8, and the upstream side of the adsorption tower 8 is communicated with the atmosphere via a cooler 9.
吸着塔8で冷却器9から導入された空気を酸素ガスと窒
素ガスに分離精製し、窒素クスは管路10を介して炉1
の天井3b、2bに縦通設置したノズル11に供給され
、炉室5内に導入される。The adsorption tower 8 separates and refines the air introduced from the cooler 9 into oxygen gas and nitrogen gas, and the nitrogen gas is sent to the furnace 1 via a pipe 10.
is supplied to a nozzle 11 installed vertically in the ceilings 3b, 2b of the furnace chamber 5, and introduced into the furnace chamber 5.
一方、分離精製された酸釆ガスは真空ポンプ等のポンプ
12を備えた管路13でラジアントチューブ6のバーナ
1に送給され、ラジアントチューブ6は左右に6−L
6−2を備えるため、夫々のバーナ1に分岐路13a
、13bを介して接続される。On the other hand, the separated and purified acid solution gas is sent to the burner 1 of the radiant tube 6 through a pipe line 13 equipped with a pump 12 such as a vacuum pump, and the radiant tube 6 has 6-L on the left and right.
6-2, each burner 1 has a branch path 13a.
, 13b.
そして酸素ガスは、バーナ7に酸素ガス単体として、或
は空気と混合し七添力!され、又管路10による窒素ガ
スは炉室う内腎供給さ朴、熱処理の雰囲気ガス成、分の
全部、或は一部として使用される更に加うるに、炉室5
の天井2b、3bを縦曲する如くガス雰囲気検出装置1
4が付設され、これは炉外のガス分析装置15に雰囲気
を報知し、。Oxygen gas is fed to the burner 7 either as a single oxygen gas or mixed with air! In addition, the nitrogen gas supplied through the pipe 10 is used as part or all of the atmosphere gas component for heat treatment.
The gas atmosphere detection device 1 is installed vertically on the ceilings 2b and 3b of the
4 is attached, which notifies the gas analyzer 15 outside the furnace of the atmosphere.
一方、ノズル16が天井2b、3bを縦通する如(設け
られ、これ16は管路11を介して炭化水素系ガス源に
接続される。On the other hand, a nozzle 16 is provided extending vertically through the ceilings 2b and 3b, and is connected to a hydrocarbon gas source via a pipe 11.
そしてこの管路17にコントロールバルブ18が介設さ
れ、コントロールバルブ18は既述のガス分析装置15
で制御され、炉室5内の雰囲気の情報でコントロールパ
ルプ15は選択的に開閉され、炉室5内に炭化水素を供
給する。A control valve 18 is interposed in this conduit 17, and the control valve 18 is connected to the gas analyzer 15 described above.
The control pulp 15 is selectively opened and closed based on information about the atmosphere inside the furnace chamber 5, and hydrocarbons are supplied into the furnace chamber 5.
以上において、空気中から分離精製された窒素ガスはノ
ズル11を介1て炉室5内に供給されるとともに、酸素
ガス(通常は空気中の酸素が21係のものを精製により
35%以上となったガス、即ち酸素が富化されたガス)
はラジアントチューブ6−1.6−2のバーナ7に供輪
され、酸素ガス単体、或は燃焼用空気との混合体として
所定比率添加され、燃焼に供される。In the above, nitrogen gas separated and purified from the air is supplied into the furnace chamber 5 through the nozzle 11, and oxygen gas (normally, the oxygen in the air is reduced to 35% or more by purification) (i.e. oxygen-enriched gas)
Oxygen gas is supplied to the burner 7 of the radiant tube 6-1, 6-2, and is added at a predetermined ratio as oxygen gas alone or as a mixture with combustion air, and is used for combustion.
これによりラジアントチューブ内での燃焼温度は著しく
高まるとともに、燃焼用空気量を酸素ガスの割合だけ少
くすることができ、燃焼廃ガスの持ち出す熱量が低減し
、トータルとしての加熱炉の熱効率が向上する。As a result, the combustion temperature within the radiant tube increases significantly, and the amount of combustion air can be reduced by the proportion of oxygen gas, reducing the amount of heat taken out of the combustion waste gas and improving the overall thermal efficiency of the heating furnace. .
この結果燃料ガスの消費量が低減し、操業費のコス、ト
ダウンを図ることがでする。As a result, fuel gas consumption is reduced, and operating costs can be reduced.
。ところで被処理物を加熱炉内に投入し、熱処理
を行う場合、従来では洗浄することを原則としていたが
、廃水処理の問題から被処理物を力旺後そのままの状態
で炉内に投入する場合が多くなりつつある。. By the way, when the material to be treated is put into a heating furnace and subjected to heat treatment, it has traditionally been the principle that it is washed, but due to problems with wastewater treatment, the material to be treated is sometimes put into the furnace as is after heating. are becoming more common.
このため被処理物表面に付着するオイル、水等が炉内に
持ち込まれ、炉内保護雰囲気中お二酸化炭素量、酸素量
竺のバラつきを生じ、これがため被処理物に酸化、脱炭
等の問題が発生している。For this reason, oil, water, etc. adhering to the surface of the workpiece are brought into the furnace, causing variations in the amount of carbon dioxide and oxygen in the protective atmosphere inside the furnace, which causes oxidation, decarburization, etc. A problem is occurring.
本発明は上記の如き炉内雰囲拭センサ14を備え、セン
サ14で線間”気を検出し、これを分析装置15に送っ
て分析し、炉内雰囲ネの露点、酸素量、二酸化炭素量の
増減に応じて外析装置15でコントロールパルプ18.
を制御し、必要量の炭化水素ガス、例えばプロパンガス
等を炉内に導入して雰囲気中に添加し、被処理物を酸イ
峰、脱炭から保護する。The present invention is equipped with the above-mentioned furnace atmosphere sensor 14, which detects the air between the wires, sends it to the analyzer 15, and analyzes it to determine the dew point, oxygen amount, and dioxide of the furnace atmosphere. Control pulp 18.
A necessary amount of hydrocarbon gas, such as propane gas, is introduced into the furnace and added to the atmosphere to protect the workpiece from acid peaks and decarburization.
次に本発明の具体的実施励を述べる。Next, concrete implementation of the present invention will be described.
6::品、。6:: Goods.
、6え7oえヶ、イ、7、う900℃迄加熱処瑠す□る
ラジアントチューブ型の加熱炉を用い、被処理物100
0kQ/Hを処理した場合、加熱燃料としてブタンガス
を約12m/H消費した。, 6, 7, A, 7, U. Using a radiant tube type heating furnace that heats up to 900°C, 100 pieces of the workpiece are heated.
When processing 0 kQ/H, about 12 m/H of butane gas was consumed as heating fuel.
一方、炉内の保護雰囲気ガスとして窒素ガスを主体とす
る発熱型ガスを約5om/Hな必要とした。On the other hand, as a protective atmosphere gas in the furnace, an exothermic gas mainly composed of nitrogen gas was required at a rate of about 5 om/H.
この保護雰囲気ガスを生成するのに要するブタンガスは
約2577//Hであった。The butane gas required to generate this protective atmosphere gas was approximately 2577//H.
本発明
炉内容積約10−の雰囲気加熱炉で常温から900℃迄
に加熱処理するレジアントチューブ型の加熱炉を用い、
被処理物1000kg/Hを処理した場合、加熱燃焼バ
ーナの燃焼空気中に大気中から分離精製した酸素ガスを
12n//H混合添加したところ、ブタンガスの消費量
は10m/:[(であり、従来に比し燃料消費量の抑制
、低減が顕著であることが判明した
一方、酸素ガスと同時に分離精製された窒素ガスを炉内
の雰囲気ガスとして使用したが、被処理品の酸化、脱炭
の程度は従来法と変化がなかった以上で明らかな如く本
発明に従えば、大気を窒素ガスと酸素ガスとに分離精製
し、窒素ガスを炉内に投入して保護雰囲気ガスとして使
用するとともに、窒素ガス精製時に発生する酸素ガスを
ラジアントチューブの燃焼補助剤、促進剤として単体或
は燃焼用空気に混合添加せしめたため、酸素ガスを無駄
なく使用し、且つ燃焼効率を高め、燃料消費量を低減し
、この種加熱炉の操業費を低減し、被処理品のコストダ
ウンを図り、且つ省エネルギー侯果的に、合理的に図る
ことができる。The present invention uses a resistant tube type heating furnace that heats from room temperature to 900°C in an atmospheric heating furnace with an internal furnace volume of about 10°C.
When processing 1000 kg/H of the material to be treated, when 12 n//H of oxygen gas separated and purified from the atmosphere was mixed and added to the combustion air of the heating combustion burner, the consumption of butane gas was 10 m//H, While it was found that fuel consumption was significantly suppressed and reduced compared to conventional methods, nitrogen gas, which was separated and purified at the same time as oxygen gas, was used as the atmosphere gas in the furnace, but it caused oxidation and decarburization of the processed products. As is clear from the above, according to the present invention, atmospheric air is separated and purified into nitrogen gas and oxygen gas, and nitrogen gas is introduced into the furnace and used as a protective atmosphere gas. The oxygen gas generated during nitrogen gas purification is used as a combustion aid and accelerator for the radiant tube, either alone or mixed with the combustion air, so oxygen gas is used without waste, improving combustion efficiency and reducing fuel consumption. It is possible to reduce the operating cost of this type of heating furnace, reduce the cost of processed products, and reasonably achieve energy savings.
父上記の炉内に雰囲気センサを設け、炉内に炭化水素を
供給しつつこれを雰囲気に応じて制御するようにしたた
め、被処理物の脱炭、酸化を防止することができ、良好
な被処理品を得ることができる。Since an atmosphere sensor is installed in the above furnace and hydrocarbons are supplied into the furnace and controlled according to the atmosphere, decarburization and oxidation of the material to be treated can be prevented, resulting in a good quality of the material being treated. Processed products can be obtained.
面図は本発明の一実施例を示すもので、第1図は炉の縦
断正面図、第2図は同側断面図である冑図面中1は炉、
6はラジアントチューブ、8は窒素、酸素分離精製装置
、10は窒素供給系、13は酸素供給系、14は雰囲気
センサ、17は炭化水素供給系である。The plan view shows one embodiment of the present invention, and FIG. 1 is a longitudinal sectional front view of the furnace, and FIG. 2 is a sectional view of the same side. 1 in the drawing shows the furnace;
6 is a radiant tube, 8 is a nitrogen and oxygen separation and purification device, 10 is a nitrogen supply system, 13 is an oxygen supply system, 14 is an atmosphere sensor, and 17 is a hydrocarbon supply system.
Claims (1)
スを加熱炉や保護雰囲気ガスとして炉内に投入するとと
もに、分離、した酸素ガスを加熱バーナに供給して単体
、歳i燃焼用空気と混合せしめて燃焼せしめる如(シチ
ことを特徴とする雰囲気加熱炉。 2 大気中の窒素ガスと酸素ガスとを分離精製し窒素ガ
スを加熱炉の保護雰囲気ガスとして炉内に投杢すると共
に、炉(ハ)の露点1.二酸化炭素、又は酸素量の内7
m又は二種以上を検出す碑囲犠センサーと被処理物の酸
化、脱炭防止用の炭化水素子ガス供給系とを炉内に望ま
せたことを特徴とする雰囲気加ザ。 、 。1. Nitrogen gas and oxygen gas in the atmosphere are separated and purified, and the nitrogen gas is fed into the furnace as a heating furnace or protective atmosphere gas, and the separated oxygen gas is supplied to a heating burner to be used as a single combustion air. An atmosphere heating furnace characterized by mixing and burning. 2. Separate and refine nitrogen gas and oxygen gas in the atmosphere, and throw the nitrogen gas into the furnace as a protective atmosphere gas for the furnace. Dew point of (c) 1. 7 of carbon dioxide or oxygen amount
1. An atmosphere heating system characterized in that a sacrificial sensor for detecting m or two or more types and a hydrocarbon particle gas supply system for preventing oxidation and decarburization of a material to be treated are arranged in the furnace. , .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7997879A JPS5815713B2 (en) | 1979-06-25 | 1979-06-25 | Atmosphere heating furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7997879A JPS5815713B2 (en) | 1979-06-25 | 1979-06-25 | Atmosphere heating furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS563881A JPS563881A (en) | 1981-01-16 |
| JPS5815713B2 true JPS5815713B2 (en) | 1983-03-26 |
Family
ID=13705407
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7997879A Expired JPS5815713B2 (en) | 1979-06-25 | 1979-06-25 | Atmosphere heating furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5815713B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5852417A (en) * | 1981-09-19 | 1983-03-28 | Osaka Gas Co Ltd | Atmosphere heat treatment device |
| CN109947152A (en) * | 2019-04-03 | 2019-06-28 | 上海颐柏科技股份有限公司 | A kind of gas fired radiant tubes temperature control system and its control method |
-
1979
- 1979-06-25 JP JP7997879A patent/JPS5815713B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS563881A (en) | 1981-01-16 |
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