JPS5810670B2 - Atmosphere heating furnace - Google Patents
Atmosphere heating furnaceInfo
- Publication number
- JPS5810670B2 JPS5810670B2 JP54098996A JP9899679A JPS5810670B2 JP S5810670 B2 JPS5810670 B2 JP S5810670B2 JP 54098996 A JP54098996 A JP 54098996A JP 9899679 A JP9899679 A JP 9899679A JP S5810670 B2 JPS5810670 B2 JP S5810670B2
- Authority
- JP
- Japan
- Prior art keywords
- gas
- furnace
- atmosphere
- heating
- fuel
- 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
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/40—Solar thermal energy, e.g. solar towers
- Y02E10/44—Heat exchange systems
Landscapes
- Heat Treatments In General, Especially Conveying And Cooling (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
- Furnace Details (AREA)
- Solid-Phase Diffusion Into Metallic Material Surfaces (AREA)
Description
【発明の詳細な説明】
本発明はラジアントチューブ型の雰囲気加熱炉に関する
ものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a radiant tube type atmosphere heating furnace.
更に詳細には、ラジアントチューブ型の炉で、ろう付、
ガス軟窒化処理、浸炭、焼鈍、規準等の熱処理に用いら
れる雰囲気加熱炉であって、所定空燃比の燃料を用いた
加熱用バーナの燃焼度ガスに含まれるN2を回収、精製
し、これを炉内雰囲気ガスの一部として用いる如くし、
省資源、ガスの有効利用を図った雰囲気加熱炉に関する
。More specifically, in a radiant tube type furnace, brazing,
This is an atmospheric heating furnace used for heat treatments such as gas nitrocarburizing, carburizing, annealing, and standardization, and it collects and refines the N2 contained in the burnup gas of the heating burner using fuel at a predetermined air-fuel ratio. It is used as part of the furnace atmosphere gas,
This article relates to an atmosphere heating furnace that saves resources and makes effective use of gas.
ろう付、ガス軟窒化、ガス浸炭、焼鈍、規準等の熱処理
を鉄系部材に施こす場合には、鉄系部材を処理温度迄加
熱するための加熱源と、加熱中の被処理品の酸化、脱炭
を防止するための保護雰囲気ガス、或はガス浸炭やガス
軟窒化処理を行う場合にはキャリヤガスを必要とする。When performing heat treatments such as brazing, gas nitrocarburizing, gas carburizing, annealing, and standardization on iron-based parts, a heat source for heating the iron-based parts to the treatment temperature and oxidation of the workpiece during heating are required. , a protective atmosphere gas to prevent decarburization, or a carrier gas when performing gas carburizing or gas nitrocarburizing.
従って加熱源としての電力や各種燃料を必要とすると同
時に保護雰囲気ガスとして単体ガス若しくは各種変成ガ
スを必要とする。Therefore, electric power and various fuels are required as heating sources, and at the same time, simple gases or various converted gases are required as protective atmosphere gases.
この熱処理に用いられる加熱源、即ち加熱エネルギーと
保護雰囲気ガスの一覧は以下の如くである。A list of heating sources, ie, heating energy, and protective atmosphere gas used in this heat treatment is as follows.
以上の如き熱処理に電力を加熱源として用いることは、
エネルギー変換時の効率ロスが犬であり、又ガス加熱に
よる熱処理では廃ガスの熱回収を一部実施するのみでそ
の殆んどを大気中に放出し、炉内雰囲気ガスとして高価
な単体ガス若しくは変成ガスを製造使用しているのが現
状である。Using electricity as a heating source for the above heat treatment,
Efficiency loss during energy conversion is significant, and heat treatment using gas heating only recovers part of the heat from the waste gas, but most of it is released into the atmosphere. Currently, metamorphosed gas is used in production.
そして吸熱型変成ガスは燃料ガスの他に製造過程で更に
電力を必要とし、又発熱型ガスは製造過程で発生する熱
エネルギーを無駄にしている。In addition to fuel gas, endothermic converted gas requires additional electricity in the manufacturing process, and exothermic gas wastes thermal energy generated in the manufacturing process.
本発明者等は従来の雰囲気加熱炉の上記エネルギーロス
を改善すべく本発明をなしたものである。The present inventors have devised the present invention in order to improve the above-mentioned energy loss of conventional atmosphere heating furnaces.
本発明の目的は、ラジアントチューブ型の雰囲気加熱炉
において、加熱用バーナで空気と燃料ガスを所定の割合
で混合した燃料を燃焼せしめ、燃焼廃ガスに含まれるN
2を精製回収せしめ、エネルギーの有効利用、省エネル
ギーを効果的に図り、省資源上有利である雰囲気加熱炉
を提供する。An object of the present invention is to burn fuel, which is a mixture of air and fuel gas at a predetermined ratio, in a heating burner in a radiant tube type atmosphere heating furnace, and to reduce the amount of N contained in the combustion waste gas.
To provide an atmosphere heating furnace which purifies and recovers 2, effectively utilizes energy, saves energy, and is advantageous in terms of saving resources.
次に本発明の好適一実施例を添付図面に従って詳述する
。Next, a preferred embodiment 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側面図、第2図は同正面図
を示している。FIG. 1 shows a vertical side view of the atmosphere heating furnace, and FIG. 2 shows a front view thereof.
炉1は枠2で囲まれた耐火材よりなる炉体3を備え、炉
体3の床部材4上には被処理物Wを載置搬送するレール
5が設けられている。The furnace 1 includes a furnace body 3 made of a refractory material surrounded by a frame 2, and on a floor member 4 of the furnace body 3, a rail 5 for placing and transporting a workpiece W is provided.
床部材4上の左右には凹部6,6が設けられ、これにラ
ジアントチューブ7.7のU字型屈曲部7aが臨み、ラ
ジアントチューブ7.7は炉体3内の左右に組をなす如
く前後方向に図示例では縦に複数設けられている。Recesses 6, 6 are provided on the left and right sides of the floor member 4, into which the U-shaped bent portions 7a of the radiant tubes 7.7 face, and the radiant tubes 7.7 are arranged in pairs on the left and right sides of the furnace body 3. In the illustrated example, a plurality of them are provided vertically in the front-rear direction.
ラジアントチューブ7.7は知られているように耐火材
や耐熱特殊金属の筒体からなり、これをU字型に折曲し
、両端7b、7cを炉体3、枠2の天井3a、2aから
外部へ導出し、一方7cを排出口とする。As is known, the radiant tube 7.7 is made of a cylindrical body made of refractory material or heat-resistant special metal, which is bent into a U shape, and both ends 7b and 7c are connected to the furnace body 3 and the ceiling 3a, 2a of the frame 2. 7c is used as a discharge port.
他方7bは入口部とし、この部分に加熱バーナ8が各設
置され、バーナ7は管路9を介して空気と燃料ガスの混
合されたものが供給される。On the other hand, 7b is an inlet portion, and heating burners 8 are installed in this portion, and a mixture of air and fuel gas is supplied to the burners 7 via a pipe 9.
ラジアントチューブ7・・・の燃料排ガス用出ロアc・
・・は管体10で連通合流せしめ、管体10は炉外で分
岐して分岐路の一方10aを煙道へ接続し、他方10b
はこれを延出し、コンプレッサ11を管路10b中に介
設し、コンプレッサ11の下流には冷却器12を接続し
てN20を除去し得る如くする。Radiant tube 7... fuel exhaust gas outlet lower c.
... are connected and merged by a pipe body 10, and the pipe bodies 10 are branched outside the furnace, and one branch path 10a is connected to the flue, and the other branch path 10b is connected to the flue.
This is extended, a compressor 11 is interposed in the conduit 10b, and a cooler 12 is connected downstream of the compressor 11 so that N20 can be removed.
この冷却器12の下流はC02の除去を目的とする吸着
塔13が接続され、これの下流にタンク14を接続し、
タンク14は管路15に接続され、管路15の端部15
aは炉1の処理室S内に臨み連通接続され、管路15中
にはN2の流量を制御するフローメータ16が介設され
ている。An adsorption tower 13 for the purpose of removing CO2 is connected downstream of this cooler 12, and a tank 14 is connected downstream of this,
Tank 14 is connected to conduit 15 and end 15 of conduit 15
A is connected to and faces the processing chamber S of the furnace 1, and a flow meter 16 for controlling the flow rate of N2 is interposed in the pipe line 15.
炉1の天井には炉気センサ17が臨み、センサ17はガ
ス分析装置18に情報を送信するとともに、炉1の天井
には炭化水素系ガスの供給口19が設けられ、これの管
路20はコントロールバルブ21を介してガス源に接続
される。A furnace air sensor 17 faces the ceiling of the furnace 1, and the sensor 17 transmits information to the gas analyzer 18. A hydrocarbon gas supply port 19 is provided on the ceiling of the furnace 1, and a conduit 20 for this is provided. is connected to a gas source via a control valve 21.
そしてコントロールバルブ21の分析装置18で制御さ
れ、必要に応じて開閉され、室S内にガスを供給する。Then, it is controlled by the analyzer 18 of the control valve 21, and is opened and closed as necessary to supply gas into the chamber S.
以上においてバーナ8に供給する燃料としてはプロパン
ガスなどの炭化水素系ガスと空気との混合体を用い、こ
れを燃焼せしめ、ラジアントチュブフ内に燃焼ガスを通
し、これの輻射熱で被処理物Wを加熱処理する。In the above, a mixture of hydrocarbon gas such as propane gas and air is used as the fuel to be supplied to the burner 8, and this is combusted, and the combustion gas is passed through the radiant tube, and the radiant heat of this is used to heat-treated.
そして室S内には処理に応じた雰囲気ガスが導入され、
例えばガス軟窒化処理において炉内の処理ガスとして
0吸熱型変成ガスとアンモニアガス(NH3)との混合
体
O発熱型変成ガスとメタノール分解ガスとアンモニアガ
ス(NH3)との混合体
等が用いられる。Then, atmospheric gas according to the process is introduced into the chamber S,
For example, in gas nitrocarburizing treatment, a mixture of 0 endothermic modified gas and ammonia gas (NH3), a mixture of 0 exothermic modified gas, methanol decomposition gas, and ammonia gas (NH3), etc. are used as the processing gas in the furnace. .
燃焼廃ガスはラジアントチューブ7内を通って管体10
に合流し、管体10内の通路はコンプレッサ11で吸引
され、廃ガスは煙道を通って排出されるとともに、分岐
管路10bを通って冷却器12に導かれ、ここでN20
を除去される。The combustion waste gas passes through the radiant tube 7 and enters the pipe body 10.
The passage in the pipe body 10 is suctioned by the compressor 11, and the waste gas is discharged through the flue and led to the cooler 12 through the branch pipe 10b, where it is converted into N20
will be removed.
そして次段の吸着塔でCO2を除去され、N2を主成分
とするガスに精製され、タンク14に貯溜され、フロー
メータ16でフローコントロールされ、必要な量を制御
しつつ管路15を介して炉内S内に供給口15aを介し
て投入される。Then, CO2 is removed in the adsorption tower of the next stage, and the gas is purified into a gas containing N2 as its main component.The gas is stored in a tank 14, the flow is controlled by a flow meter 16, and the required amount is controlled through a pipe 15. It is put into the furnace S through the supply port 15a.
即ち燃焼廃ガスを回収精製してN2のみを炉室S内に投
入する。That is, the combustion waste gas is recovered and purified, and only N2 is introduced into the furnace chamber S.
ところでバーナ8には燃料ガス供給装置22及び空気供
給装置23から燃料ガスと空気の混合体が流量を制御さ
れつつ供給され、混合体として燃焼に供されるが、本発
明では燃料と空気の混合比を理論空燃比より、空気を若
干少なめにして行い、廃ガス中に酸素の残存するのを僅
少或は無くする。By the way, a mixture of fuel gas and air is supplied to the burner 8 from the fuel gas supply device 22 and the air supply device 23 while the flow rate is controlled, and is used for combustion as a mixture. However, in the present invention, the mixture of fuel gas and air is The air-fuel ratio is set slightly lower than the stoichiometric air-fuel ratio to minimize or eliminate residual oxygen in the exhaust gas.
燃料ガスとしてプロパンガスを用いた場合の廃ガスの精
製後の成分と空気、燃料との空燃比の関係を下記に示す
。The relationship between the refined components of waste gas, air, and fuel in the air-fuel ratio when propane gas is used as the fuel gas is shown below.
このように上記空燃比により02は炉内に設置した炉気
センサーから送られる信号に従がって、炉内に炭化水素
系ガスを添加する事により、酸素ポテンシャルを低くお
さえる事が出来るので無視できる程度となり、N2が大
部分を占め、これを炉内に投入して保護雰囲気ガスや処
理ガスとする。In this way, with the above air-fuel ratio, 02 can be ignored because it is possible to keep the oxygen potential low by adding hydrocarbon gas into the furnace according to the signal sent from the furnace air sensor installed in the furnace. N2 occupies most of the amount, which is then injected into the furnace to be used as a protective atmosphere gas or processing gas.
以上はガス軟窒化を例にとったが、炉中ろう付、ガス浸
炭、焼鈍、規準の処理、雰囲気としてN2を廃ガスから
回収精製して投入し、用い得ること勿論である。Although gas nitrocarburizing has been taken as an example above, it goes without saying that it can also be used in furnace brazing, gas carburizing, annealing, standard treatments, and by collecting and purifying N2 from waste gas and introducing it as an atmosphere.
以上の如く本発明に従えば、一定の空燃比の燃料を燃焼
バーナで燃焼した廃ガスからN2を回収精製し、これを
炉内の雰囲気、処理ガスとして用いるようにしたため、
従来熱回収を目的として一部しか用いられていなかった
廃ガスを雰囲気、処理ガスとして有効に用いることがで
き、結局N2単体ガスの精製を燃料の燃焼で行わせるの
と同じとなり、熱エネルギーを取り出しつつこれを被処
理物の加熱源とし、併せてN2ガスの精製を行うことと
なり、エネルギーの有効利用の促進と省資源を図ること
ができ、実用的効果類る甚大である。As described above, according to the present invention, N2 is recovered and purified from the waste gas produced by burning fuel with a constant air-fuel ratio in a combustion burner, and this is used as the atmosphere in the furnace and as a processing gas.
Waste gas, which in the past was only partially used for the purpose of heat recovery, can be effectively used as an atmosphere and processing gas, and in the end, it is the same as refining N2 gas by burning fuel, which saves thermal energy. While being taken out, this is used as a heating source for the object to be treated, and at the same time, the N2 gas is purified, making it possible to promote effective use of energy and save resources, which has enormous practical effects.
そして上記はラジアントチューブの廃ガスの配管と付属
機器を付設するだけで足り、省エネルギー、省資源の雰
囲気加熱炉を比較的簡易に提供でき、トータルとしての
操業費の低減を効果的に図ることができる。The above requires only the installation of radiant tube waste gas piping and accessory equipment, making it possible to provide an energy-saving and resource-saving atmosphere heating furnace relatively easily, and effectively reducing total operating costs. can.
図面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図は同縦断側面図である。
尚図面中1は炉、7はラジアントチューブ、10〜16
はN2の回収精製及び供給系である。The drawings show one embodiment of the present invention, and FIG. 1 is a longitudinal sectional front view of the furnace, and FIG. 2 is a longitudinal sectional side view thereof. In the drawing, 1 is a furnace, 7 is a radiant tube, 10 to 16
is a N2 recovery, purification and supply system.
Claims (1)
ジアントチューブの加熱用バーナの燃焼度ガスに含まれ
るN2を回収精製する装置を設け、この装置と、N2が
炉内保護雰囲気ガスとして使用される炉内とをN2供給
管で連通接続せしめたことを特徴とする雰囲気加熱炉。1. In a radiant tube type atmosphere heating furnace, a device is installed to recover and purify N2 contained in the burnup gas of the heating burner of the radiant tube, and this device and the inside of the furnace where N2 is used as a protective atmosphere gas in the furnace are installed. An atmosphere heating furnace characterized in that these are connected in communication through a N2 supply pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP54098996A JPS5810670B2 (en) | 1979-08-02 | 1979-08-02 | Atmosphere heating furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP54098996A JPS5810670B2 (en) | 1979-08-02 | 1979-08-02 | Atmosphere heating furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5623688A JPS5623688A (en) | 1981-03-06 |
| JPS5810670B2 true JPS5810670B2 (en) | 1983-02-26 |
Family
ID=14234581
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP54098996A Expired JPS5810670B2 (en) | 1979-08-02 | 1979-08-02 | Atmosphere heating furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5810670B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2014074566A (en) * | 2012-10-05 | 2014-04-24 | Kanto Yakin Kogyo Co Ltd | Heat treat furnace of steel |
-
1979
- 1979-08-02 JP JP54098996A patent/JPS5810670B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5623688A (en) | 1981-03-06 |
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