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JPS583192B2 - Atmosphere heating furnace - Google Patents
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JPS583192B2 - Atmosphere heating furnace - Google Patents

Atmosphere heating furnace

Info

Publication number
JPS583192B2
JPS583192B2 JP54141199A JP14119979A JPS583192B2 JP S583192 B2 JPS583192 B2 JP S583192B2 JP 54141199 A JP54141199 A JP 54141199A JP 14119979 A JP14119979 A JP 14119979A JP S583192 B2 JPS583192 B2 JP S583192B2
Authority
JP
Japan
Prior art keywords
furnace
gas
sintering
shutter
closed
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
JP54141199A
Other languages
Japanese (ja)
Other versions
JPS5665904A (en
Inventor
松山晃
清野洋
湯沢幸男
馬来義弘
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.)
Nissan Motor Co Ltd
Original Assignee
Nissan Motor Co 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 Nissan Motor Co Ltd filed Critical Nissan Motor Co Ltd
Priority to JP54141199A priority Critical patent/JPS583192B2/en
Publication of JPS5665904A publication Critical patent/JPS5665904A/en
Publication of JPS583192B2 publication Critical patent/JPS583192B2/en
Expired legal-status Critical Current

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  • Powder Metallurgy (AREA)
  • Tunnel Furnaces (AREA)

Description

【発明の詳細な説明】 本発明は雰囲気加熱炉、特に、アルミ粉末治金部品の焼
結用加熱炉に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an atmosphere heating furnace, and more particularly to a heating furnace for sintering aluminum powder metallurgy parts.

従来,アルミ粉末治金部品の焼結には、特に高純度に雰
囲気を保つため第1図に示すようなハンプパツク形式の
雰囲気加熱炉が用いられており、焼結すべき被処理物品
1を入口端2から脱ろう部3、焼結部4、冷却部5を経
て出口端6に無終端メッシュベルトまたはチェーンコン
ベヤ7によって搬送し、脱ろう部3および焼結部4を順
次に通過スる間にニクロム線の加熱コイル8および9に
よって、それぞれ所定の温度に加熱して脱ろうおよび焼
結し、次で、冷却部5を通過する間に水冷ジャケット1
0の冷却水によって冷却して出口端6から取出すよう構
成されている。
Conventionally, a hump pack type atmosphere heating furnace as shown in Fig. 1 has been used to sinter aluminum powder metallurgy parts in order to maintain a particularly high purity atmosphere. It is conveyed from the end 2 through the dewaxing section 3, the sintering section 4, and the cooling section 5 to the outlet end 6 by an endless mesh belt or chain conveyor 7, and passes through the dewaxing section 3 and the sintering section 4 in sequence. The heating coils 8 and 9 of the nichrome wire are used to heat the wire to a predetermined temperature for dewaxing and sintering, and then the water cooling jacket 1 is heated while passing through the cooling section 5.
0 cooling water and taken out from the outlet end 6.

11は可変モータ(図示せず)によって駆動されるコン
ベヤ駆動ローラ、12ぱ室内ローラを示す。
Reference numeral 11 indicates a conveyor drive roller driven by a variable motor (not shown), and 12 indicates an indoor roller.

そして、脱ろう部3および焼結部4の位置を入口端3、
出口端6より高い位置に配置する。
Then, the positions of the dewaxing part 3 and the sintering part 4 are adjusted to the inlet end 3,
It is placed at a higher position than the outlet end 6.

上述の構成になる加熱炉内を所定のガス雰囲気に維持す
るため、炉出口端側にN2,H2ガス等の雰囲気ガス導
入口13を設け、これにより雰囲気ガス導入口13より
導入された雰囲気ガスおよび脱ろう部3において被処理
物品から揮発したろう蒸気を被処理物品1の搬送方向1
6と逆方向に矢17で示すように流すとともに炉入口端
2および出口端6にN2 ガスによるガスカーテンまた
はフレームカーテンをそれぞれ設けて外気が炉内に侵入
するのを防止する。
In order to maintain a predetermined gas atmosphere inside the heating furnace configured as described above, an atmospheric gas inlet 13 such as N2, H2 gas, etc. is provided at the furnace outlet end. In the dewaxing section 3, the wax vapor evaporated from the article to be treated is transferred to the conveying direction 1 of the article to be treated 1.
6 and in the direction opposite to arrow 17, and a gas curtain or frame curtain made of N2 gas is provided at the furnace inlet end 2 and outlet end 6, respectively, to prevent outside air from entering the furnace.

雰囲気ガスは特に焼結部4において高温になるため軽く
なり高所にある焼結部4に溜り易く他方入口端2あるい
は出口端6から侵入する外気は低温であるため重く、焼
結部4には進入し難い。
Atmospheric gas reaches a high temperature especially in the sintering section 4, so it becomes light and tends to accumulate in the sintering section 4 located at a high place.On the other hand, the outside air that enters from the inlet end 2 or the outlet end 6 is low temperature and therefore heavy. is difficult to enter.

これによってN2,H2および分解NH3ガス雰囲気で
の焼結部4において必要とされる−40℃以下の露点を
有する極めて高純度のガス雰囲気を維持し得るよう構成
している。
This makes it possible to maintain an extremely high purity gas atmosphere having a dew point of -40 DEG C. or lower, which is required in the sintering section 4 in an N2, H2 and decomposed NH3 gas atmosphere.

上述したような構成になる従来の雰囲気加熱炉では、焼
結部4側の炉出口端6が常時開放されているため、この
開放出口端から被処理物品1の取出時等にまれに外気を
炉内に巻込むことがあり、どうしても焼結部4の露点を
−40℃以下に常に安定に保つことはむずかしかった。
In the conventional atmosphere heating furnace configured as described above, the furnace outlet end 6 on the sintering section 4 side is always open, so outside air is rarely allowed to enter when the article to be processed 1 is taken out from this open outlet end. It has been difficult to keep the dew point of the sintered part 4 stable at -40°C or lower at all times because it may get caught up in the furnace.

このため露点を所定温度以下に保つためには雰囲気ガス
の供給量を多くしなければならなかった。
Therefore, in order to keep the dew point below a predetermined temperature, it was necessary to increase the amount of atmospheric gas supplied.

本発明の目的は上述した欠点を除去しようとするもので
、雰囲気加熱炉の出口端を閉鎖し得る構成とすることに
よって、従来に比べ遥かに安定した状態で炉内雰囲気を
高純度に保つことが可能な雰囲気加熱炉を提供しようと
するにある。
The purpose of the present invention is to eliminate the above-mentioned drawbacks, and by providing a structure in which the outlet end of the atmosphere heating furnace can be closed, it is possible to maintain a high purity atmosphere in the furnace in a much more stable state than in the past. We are trying to provide an atmosphere heating furnace that allows for

これがため、本発明による雰囲気加熱炉は、炉出口端に
外気遮蔽出口傾斜通路を設け、この傾斜通路に処理物品
の通過に応答して開閉作動される出口シャツタを設けた
ことを特徴とする。
Therefore, the atmosphere heating furnace according to the present invention is characterized in that an outside air shielding outlet inclined passageway is provided at the furnace outlet end, and an outlet shutter is provided in this inclined passageway, which is opened and closed in response to passage of the article to be processed.

また、本発明を実施するに当り、出口シャツタにより開
閉される出口にガス置換室を設けることによって焼結部
を所要を雰囲気露点に保つに必要な導入ガス流量をさら
に減ずることができる。
Further, in carrying out the present invention, by providing a gas exchange chamber at the outlet that is opened and closed by the outlet shutter, the flow rate of the introduced gas required to maintain the sintered part at the required atmospheric dew point can be further reduced.

以下、本発明を図面につき説明する。The invention will now be explained with reference to the drawings.

第2図ないし第4図は本発明の好適実施列を示し、これ
らの図面において第1図に示す従来構造の雰囲気加熱炉
と同様部分を第1図につき説明したと同じ符号で示す。
2 through 4 illustrate preferred embodiments of the present invention, in which parts similar to the conventional atmosphere furnace shown in FIG. 1 are designated by the same reference numerals as described in connection with FIG.

第2図に示すように、本発明による雰囲気加熱炉では、
脱ろう部3および焼結部4にそれぞれ別個の無終端スク
リーンベルトコンベヤまたはチェーンコンベヤ20.2
1を設け、これらの無終端コンベヤ20,21の駆動ロ
ーラ22,23のそれぞれを別個の可変速モータ(図示
せず)によって駆動して各無終端コンベヤの速度を所望
に応じて変化させて、被処理物品1の形状、成分、密度
等により最適の脱ろうおよび焼結時間の組合せが得られ
るようにする。
As shown in FIG. 2, in the atmosphere heating furnace according to the present invention,
A separate endless screen belt conveyor or chain conveyor 20.2 is provided in the dewaxing section 3 and the sintering section 4 respectively.
1, each of the drive rollers 22, 23 of these endless conveyors 20, 21 is driven by a separate variable speed motor (not shown) to vary the speed of each endless conveyor as desired, An optimal combination of dewaxing and sintering time is obtained depending on the shape, composition, density, etc. of the article 1 to be treated.

かように、焼結部4に被処理物品1を移送するための別
個の無終端コンベヤ21を用いるため、この無終端コン
ベヤ21を前述した従来技術のように炉外に通す場合に
は無終端コンベヤ21によって雰囲気ガスの純度が悪化
される欠点があり、これを防止するため、焼結部4を通
る無終端コンベヤ21を外気に接触させることなく、常
時炉内雰囲気ガス中にあるようにする。
As described above, since a separate endless conveyor 21 is used to transfer the article 1 to be processed to the sintering section 4, when this endless conveyor 21 is passed outside the furnace as in the prior art described above, an endless conveyor 21 is used. The conveyor 21 has the disadvantage that the purity of the atmospheric gas is deteriorated, and in order to prevent this, the endless conveyor 21 passing through the sintering section 4 is kept in the furnace atmospheric gas at all times without contacting the outside air. .

これがため、第3図に示すように雰囲気加熱炉の炉マツ
フル22を上段炉床24および下段炉床25を有する2
重底構造とし、上段炉床24に適当な連通孔26を設け
、連通孔26を経て上下段の炉内雰囲気がほぼ等しくな
るようにし、無終端コンベヤ20.21の搬送部分20
a,21aおよび戻り部分20b,21bを上段炉床2
4の上下に案内ローラ27,28によってそれぞれ案内
する。
For this reason, as shown in FIG.
The upper hearth 24 has a heavy bottom structure, and an appropriate communication hole 26 is provided in the upper hearth 24 so that the atmosphere in the upper and lower furnaces becomes almost equal through the communication hole 26.
a, 21a and return parts 20b, 21b to the upper hearth 2
4 by guide rollers 27 and 28, respectively.

脱ろう部無終端コンベヤ200入口端における案内ロー
ラ27ぱ炉外に設けるも、脱ろう部無終端コンベヤ20
の出口端における案内ローラ27および焼結部無終端コ
ンベヤ210入口端および出口端における案内ローラ2
8,28を脱ろう部3と焼結部4との境界部に設けた炉
内ピット29および炉出口端6に設けた炉内ピット30
内にそれぞれ設ける。
Although the guide roller 27 at the inlet end of the dewaxing section endless conveyor 200 is installed outside the furnace, the dewaxing section endless conveyor 20
guide roller 27 at the outlet end of the sintering section endless conveyor 210 and guide roller 2 at the inlet end and outlet end of the sintering section endless conveyor 210
8, 28 are provided at the boundary between the dewaxing section 3 and the sintering section 4, and an in-furnace pit 29 is provided at the furnace outlet end 6.
Each is provided inside.

炉出口端6に外気遮蔽傾斜通路31を接続し、この傾斜
通路31の出口端部に常閉出ロシャツタ32を取付け、
この出口シャツタ32に油圧シリンダまたはエアシリン
ダのようなアクチュエータ33を連結して開閉作動し得
るようにし、傾斜通路31にも雰囲気ガス導入管34を
接続する。
An outside air shielding inclined passage 31 is connected to the furnace outlet end 6, and a normally closed Roshutter 32 is attached to the outlet end of this inclined passage 31.
An actuator 33 such as a hydraulic cylinder or an air cylinder is connected to the outlet shutter 32 so that it can open and close, and an atmospheric gas introduction pipe 34 is also connected to the inclined passage 31.

出口シャツタ32の前後位置で傾斜通路31上を滑り落
ちる被処理物品によって作動されるリミットスイッチ3
5.36を設け、リミットスイッチ35が被処理物品に
よって作動される際に雰囲気ガス導入管34の遮断弁3
7を開いた後にアクチュエータ33を作動して出口シャ
ツタ32を開き、リミットスイッチ36が被処理物品に
よって作動される際に7クチュエータ33を作動して出
口シャツタ32を閉じた後に遮断弁37を閉じるよう制
御回路38を構成して接続する。
A limit switch 3 activated by the article to be processed sliding down the inclined passageway 31 at the front and back positions of the outlet shirtter 32
5.36 is provided, and when the limit switch 35 is activated by the article to be processed, the cutoff valve 3 of the atmospheric gas introduction pipe 34 is provided.
After opening 7, the actuator 33 is actuated to open the outlet shutter 32, and when the limit switch 36 is actuated by the article to be processed, the actuator 33 is actuated to close the outlet shutter 32 and then close the shutoff valve 37. The control circuit 38 is configured and connected.

上述の構成になる雰囲気加熱炉の作動に際しては、脱ろ
う部コンベヤ20および焼結部コンベヤ21の速度を被
処理物品の形状、寸法、材質、密度等に応じて変化させ
て最適の脱ろう時間および焼結時間の組合せで被処理物
品は脱ろう部3で脱ろうされ、焼結部4で焼結され、冷
却部5で冷却された後、炉出口端6から傾斜通路31の
傾斜面上を滑り落ち、リミットスイッチ35に接触する
When operating the atmosphere heating furnace configured as described above, the speeds of the dewaxing section conveyor 20 and the sintering section conveyor 21 are changed depending on the shape, size, material, density, etc. of the article to be processed to obtain the optimum dewaxing time. The article to be processed is dewaxed in the dewaxing section 3, sintered in the sintering section 4, and cooled in the cooling section 5. and comes into contact with the limit switch 35.

リミットスイッチ35が作動すると同時に遮断弁37が
開き、雰囲気ガス導入管34から傾斜通路31内にN2
ガスが多量に流入して大気が炉内に侵入するのを防止
し得る状態でアクチュエータ33によって出口シャツタ
32が開かれ、これにより被処理物品は出口シャツタ3
2を通過して炉外に取出される。
At the same time as the limit switch 35 operates, the cutoff valve 37 opens, and N2 is introduced into the inclined passage 31 from the atmospheric gas introduction pipe 34.
The outlet shutter 32 is opened by the actuator 33 in a state where a large amount of gas flows in and the atmosphere can be prevented from entering the furnace, so that the article to be processed is transferred to the outlet shutter 3.
2 and taken out of the furnace.

被処理物品は出口シャツタ32を通過後、リミットスイ
ッチ36が作動されて閉じ、遮断弁37も閉じて雰囲気
ガス導入管34からのガス流入を停止させることにより
1サイクルが完了する。
After the article to be processed passes through the outlet shutter 32, the limit switch 36 is operated and closed, and the cutoff valve 37 is also closed to stop gas inflow from the atmospheric gas introduction pipe 34, thereby completing one cycle.

かようにリミットスイッチ35,36、fflロシャツ
タ32および遮断弁37を組合せることによって被処理
物品がシャッタ32を通過する短時間のみは両端開放型
め連続炉であるが、それ以外は入口端だけが開放された
一端開放金端閉鎖型となり、焼結部4での露点保持もし
やすく、かつ消費ガス量も大幅に低減される。
By combining the limit switches 35 and 36, the ffl shutter 32, and the shutoff valve 37, the furnace is a continuous furnace with both ends open only for a short time when the article to be processed passes through the shutter 32, but other than that, only the inlet end is open. It is of an open end type with a metal end closed type, which makes it easy to maintain the dew point in the sintered part 4, and also significantly reduces the amount of gas consumed.

第2図に示すように炉出口側に1個のシャツタ32だけ
を設けた一端閉鎖方式でもかなりの雰囲気露点を確保す
ることは可能であり、実用上は何ら問題はないが、更に
高純度の雰囲気を安定的に必要とする場合は、第4図に
示すような2重シャツタ機構を取入終たガス置換室方式
が適している。
As shown in Fig. 2, it is possible to secure a considerable atmospheric dew point even with a one-end closed system in which only one shutter 32 is provided on the furnace outlet side, and there is no practical problem. If a stable atmosphere is required, a gas exchange chamber system equipped with a double shutter mechanism as shown in FIG. 4 is suitable.

第4図に示す列では、傾斜通路31に2個のシャツタ3
9.40を適当な間隔で離間させて設けて両シャツタ3
9.40間kガス置換室41を画成し、このガス置換室
41内に常時N2 ガスを還流させるための小径のガス
導入管42およびガス排出管43を接続するとともに被
処理物品通過時に大量のN2 ガスを導入し得る大径の
〃ス導入管44を接続し、この大徨ガス導入管44に遮
断弁46を設ける。
In the row shown in FIG.
9.40 are spaced apart at appropriate intervals, and both shirts 3
9. A gas exchange chamber 41 is defined for 40 hours, and a small-diameter gas introduction pipe 42 and a gas discharge pipe 43 are connected to constantly reflux N2 gas into this gas exchange chamber 41. A large-diameter gas introduction pipe 44 capable of introducing N2 gas is connected, and a shutoff valve 46 is provided on this large-diameter gas introduction pipe 44.

ガス置換室入口シャツタ390前後およびガス置換室出
口シャツタ400前後にそれぞれリミットスイッチ47
,48および49,50を設けて傾斜通路31を滑り落
ちる被処理物品が接触することによってそれぞれ作動さ
れるようにし、一方コンプレッサー(図示せず)を電磁
三方弁67.68を介してシャツタ39.40に連結さ
れたアクチュエータ51.52に接続し、リミットスイ
ッチ47が閉じるとシャツタ39を開き、リミットスイ
ッチ48が閉じられるとシャツタ39を閉じ、リミット
スイッチ49が閉じられると遮断弁46を開くとともに
シャツタ40に連結されたアクチュエータ52が作動さ
れてシャツタ40を開き、リミットスイッチ50が閉じ
らねるとシャツタ40を閉じるよう制御回路を構成する
.この制御回路の具体例を第5図およd第6図に示す。
Limit switches 47 are installed before and after the gas exchange chamber inlet shutter 390 and before and after the gas exchange chamber outlet shutter 400, respectively.
, 48 and 49, 50 are provided so as to be actuated by contact with the articles to be treated sliding down the inclined passage 31, while a compressor (not shown) is connected to the compressor 39, 40 via an electromagnetic three-way valve 67, 68. When the limit switch 47 is closed, the shutter 39 is opened, when the limit switch 48 is closed, the shutter 39 is closed, and when the limit switch 49 is closed, the shutoff valve 46 is opened and the shutter 40 is opened. The control circuit is configured such that the actuator 52 connected to the button is actuated to open the shutter 40, and when the limit switch 50 fails to close, the shutter 40 is closed. Specific examples of this control circuit are shown in FIGS. 5 and 6.

E1は電源であり、この電源E1 にリミツトスイツチ
48の常閉接点48bをリレーR1 とリミットスイ
ッチ47の常開接点47aとを直列に接続し、リミット
スイッチ47と並列にリレーR1の常開接点Rl a−
1を接続した電路Aと、リレーR2 と遅延リレーR
D とを並列にした回路とリミットスイッチ50の常閉
接点50bおよびリミットスイッチ49の常開接点49
aとリレーR2の常開鷺点R2 a−1とを並列接続し
た回路とを直列に接続した電路Bとを並列に接続する。
E1 is a power source, to which the normally closed contact 48b of the limit switch 48 is connected in series with the relay R1 and the normally open contact 47a of the limit switch 47, and the normally open contact Rl a of the relay R1 is connected in parallel with the limit switch 47. −
1 connected to electric circuit A, relay R2 and delay relay R
D in parallel with the normally closed contact 50b of the limit switch 50 and the normally open contact 49 of the limit switch 49
A and a circuit in which the normally open point R2a-1 of the relay R2 are connected in parallel, and a circuit B in which the circuit is connected in series are connected in parallel.

一方電源E2に三方弁67とリレーR1の常開接点R1
a−2、電磁遮断弁46とリレー馬の常開接点R2 a
−2、三方弁68と連続リレーRDの常開接点RD&と
を各々直列に接続した各電路を並列に接続する。
On the other hand, the three-way valve 67 and the normally open contact R1 of the relay R1 are connected to the power supply E2.
a-2, solenoid cutoff valve 46 and relay horse normally open contact R2 a
-2. Connect the three-way valve 68 and the normally open contact RD& of the continuous relay RD in parallel to each other.

なお、前記遅延リレーRDは後述のように遮断弁46が
開いてシャツタ39と40との間がN2 ガスで置換さ
れる迄の時間に設定する。
The delay relay RD is set to the time required for the shutoff valve 46 to open and for the space between the shutters 39 and 40 to be replaced with N2 gas, as will be described later.

上述した制御回路を設けることによって、炉出口端6か
ら傾斜通路31に入った被処理物品がリミットスイッチ
47に接触する前は、シャツタ39.40および遮断弁
46は全て閉じており、ガス置換室41内はガス導入管
42より導入されたN2 ガスがガス排出管43より排
出されることによってN2ガス雰囲気に保持されている
By providing the above-mentioned control circuit, before the article to be processed that has entered the inclined passageway 31 from the furnace outlet end 6 contacts the limit switch 47, the shutter shutters 39, 40 and the shutoff valve 46 are all closed, and the gas exchange chamber is closed. The inside of 41 is maintained in an N2 gas atmosphere by the N2 gas introduced through the gas introduction pipe 42 and discharged through the gas exhaust pipe 43.

この状態で、傾斜通路31を滑り落ちてきた被処理物品
がリミットスイッチ47に接触することによってリミッ
トスイッチ47が閉じると、リレーR1が励磁してRl
a−1が閉じ、この電路AIJ烟己保持される。
In this state, when the limit switch 47 is closed due to the object to be processed sliding down the inclined passageway 31 contacting the limit switch 47, the relay R1 is energized and the Rl
a-1 is closed and this electric circuit AIJ is maintained.

これと同時に接点R1a−2が閉じ、三方弁67が開い
てアクチュエータ51が作動し、ガス置換室入口シャツ
タ39が開き、被処理物品はガス置換室41内に入り、
次でリミットスイッチ48に接触し、これにより接点4
8bが開き、リレーR1が消磁され、R’ia−’zが
開き、三方弁67が閉じると共にアクチュエータ51内
のエアを大気に開放し、シャツタ39が閉じる。
At the same time, the contact R1a-2 closes, the three-way valve 67 opens, the actuator 51 operates, the gas exchange chamber inlet shutter 39 opens, and the article to be treated enters the gas exchange chamber 41.
Next, limit switch 48 is contacted, which causes contact 4
8b is opened, relay R1 is demagnetized, R'ia-'z is opened, three-way valve 67 is closed, the air in actuator 51 is released to the atmosphere, and shutter 39 is closed.

次に被処理物品がリミットスイッチ49に接触して接点
49aが閉じることによりりv 7 R2が励磁されて
遮断弁46が開いて多量のN2ガスがガス置換室41内
に導入され、この状態は接点R2 a−1が閉じるので
自己保持される。
Next, when the article to be processed contacts the limit switch 49 and the contact 49a closes, v 7 R2 is energized, the shutoff valve 46 opens, and a large amount of N2 gas is introduced into the gas exchange chamber 41, and this state is Since the contact point R2 a-1 is closed, it is self-held.

又、リミットスイッチ49が閉じると同時に遅延リレー
RDに通電され、シャツタ39と40間がN2ガスで置
換された後、接点RDaが閉じ、三方弁68が開いてア
クチュエータ52を作動させガス置換室出口シャツタ4
0が開く。
Also, at the same time as the limit switch 49 closes, the delay relay RD is energized, and after the space between the shutters 39 and 40 is replaced with N2 gas, the contact RDa is closed, the three-way valve 68 is opened, and the actuator 52 is actuated to open the gas exchange chamber outlet. shirtta 4
0 opens.

これにより被処理物品はガス置換室41を出てリミット
スイッチ50に接触する。
As a result, the article to be processed leaves the gas exchange chamber 41 and comes into contact with the limit switch 50.

リミットスイッチ50が作動されることによって接点5
0bが開き、リレーR2 と遅延リレーもが共に消磁さ
れるので接点R2 a −2 、 RD2が開き三方弁
68が閉じると共にアクチュエータ52内のエアを大気
に開放し、シャツタ40を閉じると共に遮断弁46が閉
じ、かようにして1サイクルが終了する。
When the limit switch 50 is activated, the contact 5
0b opens, and both the relay R2 and the delay relay are demagnetized, so the contacts R2 a -2 and RD2 open, the three-way valve 68 closes, and the air in the actuator 52 is released to the atmosphere, the shutter 40 is closed, and the cutoff valve 46 is opened. is closed, thus completing one cycle.

第7図ないし第11図は2重シャツタ機構を具えるガス
置換室方式の他の実施例を示し、本例では炉出日端に設
けられる傾斜出口通路31と、この入口端および出口端
に設けた扉またはシャツタ53.54とによってガス置
換室55を画成して設ける。
7 to 11 show another embodiment of the gas exchange chamber system equipped with a double shutter mechanism, and in this example, an inclined outlet passage 31 provided at the end of the furnace, and an inlet end and an outlet end thereof. A gas exchange chamber 55 is defined by the provided door or shutter shutter 53,54.

焼結部コンベヤ21の出口端とガス置換室55の入口端
との間に傾斜板56をその一端で枢支軸57により枢支
して回動自在に設け、傾斜板56をばね58によって入
口シャッタ53に後述のように連動するよう連結し、常
時開放位置にある入口シャツタ53により傾斜板56は
遊端がガス置換室55の入口端の下側に掛合して焼結部
コンベヤ21から被処理物品が傾斜板56を滑り落ちて
ガス置換室55に入るよう構成する。
An inclined plate 56 is rotatably provided between the outlet end of the sintering section conveyor 21 and the inlet end of the gas exchange chamber 55, with one end of the inclined plate 56 being pivotally supported by a pivot shaft 57. The inlet shutter 53 is connected to the shutter 53 as described below and is always in the open position, so that the free end of the inclined plate 56 is engaged with the lower side of the inlet end of the gas exchange chamber 55 and is protected from the sintering part conveyor 21. The article to be treated is configured to slide down the inclined plate 56 and enter the gas exchange chamber 55.

入口扉またはシャツタ53および出口扉またはシャツタ
54をそれぞれ第8図および第9図に示すように回転軸
59.59’に取付け、この回転軸59.59’を軸受
60,6σ′によって回転自在に支承し、回転軸59.
59’の一端に固着したピニオン61,61’に噛合さ
せたラック62.62’をエヤシリンダ63.63’に
よってそれぞれ作動するよう連結する。
The entrance door or shutter 53 and the exit door or shutter 54 are respectively attached to a rotating shaft 59.59' as shown in FIGS. Supporting and rotating shaft 59.
Racks 62 and 62' meshed with pinions 61 and 61' fixed to one end of 59' are operably connected by air cylinders 63 and 63', respectively.

エアシリンダ63.63’は電磁三方弁70,70を介
してそれぞれ高圧空気源にまた、ガス置換室55にN2
ガスのような雰囲気ガスの導入管64と排出管65と
を設け、導入管64の電磁弁(図示せず)を常開とし、
排出管65の電磁弁71を常閉とする。
The air cylinders 63 and 63' are connected to a high-pressure air source and to the gas exchange chamber 55 through electromagnetic three-way valves 70 and 70, respectively.
An inlet pipe 64 and an outlet pipe 65 for atmospheric gas such as gas are provided, and a solenoid valve (not shown) of the inlet pipe 64 is kept open.
The solenoid valve 71 of the discharge pipe 65 is normally closed.

さらに、ガス置換室55内にはその傾斜通路上を滑り落
ちる被処理物品によって作動される光電管式のリミット
スイッチ66を設け、このスイッチ66が被処理物品の
通過によって作動するようにする。
Further, a phototube-type limit switch 66 is provided in the gas exchange chamber 55 and is actuated by the article to be treated sliding down the inclined path.

以下、シャツタ53,54、三方弁70,7σ、等の匍
脚回路を第10図、第11図に基づいて説明する。
Hereinafter, the armature circuit including the shirt shutters 53, 54, the three-way valves 70, 7σ, etc. will be explained based on FIGS. 10 and 11.

通電されると第1の所定時間常開接点72a−1,72
a−2、73a−3,72a−4 を閉じるタイマ72
の接点72 66とが作動したときに閉じる接点66aとを並列に接
続した回路と前記タイマ72とを直列に接続した電路C
,通電されると第2の所定時間常開接点73aを閉じる
タイマ73と第3の所定時間作動を遅らす遅延回路74
と前記タイマ72の接点72a−2とを直列に接続した
電路D.および通電されると第4の所定時間経過後接点
75aを閉じる遅延リレー75とタイマ72の接点7
2 a −3 とを直列に接続した電路Eとを電源E
3 に並列に接続する。
When energized, the first normally open contacts 72a-1, 72 for a predetermined time
Timer 72 that closes a-2, 73a-3, 72a-4
A circuit C in which the timer 72 is connected in series with a circuit in which the contacts 72 and 66 are connected in parallel to the contact 66a which is closed when the contacts 72 and 66 are activated.
, a timer 73 that closes the normally open contact 73a for a second predetermined time when energized, and a delay circuit 74 that delays operation for a third predetermined time.
and the contact 72a-2 of the timer 72 are connected in series. and the contact 7 of the delay relay 75 and timer 72, which closes the contact 75a after a fourth predetermined time has elapsed when energized.
2 a - 3 are connected in series to the power supply E.
3 in parallel.

他方、接点72a−4と電磁三方弁70とを直列に接続
した電路F1接点73aと三方弁70′とを直列に接続
した電路G1および接点75aと電磁弁71とを直列に
接続した電路Hとを電源E4に並列に接続する。
On the other hand, an electric line F1 in which the contact 72a-4 and the electromagnetic three-way valve 70 are connected in series, an electric line G1 in which the contact 73a and the three-way valve 70' are connected in series, and an electric line H in which the contact 75a and the electromagnetic valve 71 are connected in series. are connected in parallel to the power supply E4.

次に、上述の構成になる装置の作勲を説明する。Next, the operation of the apparatus configured as described above will be explained.

被処理物品は傾斜板56を経て開いた入口シャど夕53
を通ってガス置換室55に滑り落ちる。
The article to be processed is passed through the entrance shaft 53 which opens through the inclined plate 56.
It slides down through the gas exchange chamber 55.

ここで光電式リミットスイッチ66が被処理物品を検知
して接点66aが閉じる。
Here, the photoelectric limit switch 66 detects the article to be processed and the contact 66a closes.

こδためタイマT2が作動して各接点72a1〜72a
.を閉じる。
Therefore, timer T2 operates and each contact 72a1 to 72a
.. Close.

このため被処理物品がリミットスイッチ66を通過して
も接点72a−1が閉じているのでそのまゝタイマ72
が作動する。
Therefore, even if the article to be processed passes through the limit switch 66, the contact 72a-1 remains closed, so the timer 72 remains closed.
is activated.

同時に、三方弁70が開いて高圧空気がエアシリンダ7
0に入るのでラツク62が押し出され、回転軸59と一
体のピニオン61が回転し、入口シャツタ53がガス置
換室55の入口を閉じる。
At the same time, the three-way valve 70 opens and high pressure air flows into the air cylinder 7.
0, the rack 62 is pushed out, the pinion 61 integrated with the rotating shaft 59 rotates, and the inlet shutter 53 closes the inlet of the gas exchange chamber 55.

次いで第1の所定時間経過後すなわち入口シャツタ53
が完全に閉じた後遅延回路74の作動によりタイマ73
が作動し爾2の所定時間すなわち被処理物品が出口シャ
ツタ64を通過するに要する時間接点73aが閉じ三方
弁70′が開き高圧空気がエアシリンダ63′に供給さ
れてラツク6zを引き戻し、ピニオン61′の回転に従
って回転軸シャツタ54を開く。
Then, after the first predetermined time has elapsed, that is, the entrance shirt shutter 53
After the timer 73 is completely closed, the delay circuit 74 is activated.
is activated, the contact 73a closes and the three-way valve 70' opens, supplying high pressure air to the air cylinder 63' to pull back the rack 6z, and the pinion 61 The rotary shaft shutter 54 is opened according to the rotation of '.

第2の所定時間経過後は接点73aが開き三方弁70′
が閉じると共にエアシリンダ63′内のエアを大気に開
放する。
After the second predetermined time has elapsed, the contact 73a opens and the three-way valve 70'
When the air cylinder 63' is closed, the air inside the air cylinder 63' is released to the atmosphere.

したがってシャツタ54は再び閉じる。Therefore, the shirt flap 54 is closed again.

一方前述のタイマ72が作動してから第40所定時間、
すなわちシャツタ54が閉じるまでの時間経過後、遅延
リレー75励磁し、接点75aが閉じる。
On the other hand, after the 40th predetermined time after the timer 72 is activated,
That is, after the time elapses until the shirt shutter 54 closes, the delay relay 75 is energized and the contact 75a closes.

このため電磁弁71が開き、ガス導入管64からガス置
換室55内に導入されているガスによりガス置換室55
内に入った外気をガス排出管65から追い出す。
Therefore, the solenoid valve 71 opens, and the gas introduced into the gas exchange chamber 55 from the gas introduction pipe 64 causes the gas exchange chamber 55 to
The outside air that has entered the interior is expelled from the gas exhaust pipe 65.

次いで第1の所定時間、すなわちタイマ72に通電され
てからガス置換室55内のガス置換が完了する時間経過
後接点72a−1〜72a−4が開き、タイマ72,7
3、遅延リレー75が非作動となり、入口シャツタ53
が開いて、出口シャツタ54が閉じ、電磁弁71が閉じ
た状態すなわち元の状態に戻り一サイクルを終了する。
Next, after a first predetermined time has elapsed, that is, the time from when the timer 72 is energized to when the gas replacement in the gas replacement chamber 55 is completed, the contacts 72a-1 to 72a-4 open, and the timers 72, 7
3. The delay relay 75 is deactivated and the entrance shutter 53
opens, the outlet shutter 54 closes, and the solenoid valve 71 returns to its closed state, that is, its original state, completing one cycle.

以下、本発明を実施例につき説明する。Hereinafter, the present invention will be explained with reference to examples.

実施例 1 第2図に示す構造の連続式アルミ焼結炉を用いてアルミ
粉末治金部品を焼結した。
Example 1 An aluminum powder metallurgy part was sintered using a continuous aluminum sintering furnace having the structure shown in FIG.

使用したアルミ焼結炉の主な仕様を次に示す。The main specifications of the aluminum sintering furnace used are shown below.

炉全長 8000mm被焼結材置
部 1500mm脱ろう部(ニクロム
線加熱) 2000mm焼結部
2000mm水冷部 10
00mm空冷および傾斜通路部 1500mm
コンベヤ形式:脱ろう部および焼結部ともメッシュベル
ト 駆動速度 : 1 0 〜2 0 0 mm/mi
nマツフル寸法: 1 5 0mm×2 0 0trr
mベルト幅 : 1 8 0wn 混粉成形条件は 混合粉末組成 (重量%) Al−4.4Cu−0.5Mg−0.8Si 1.5
Wax成形圧力 5ton/cm2 成形形状 ISO2740引張試験片(厚さ6mm)であり、焼結
はアンモニア分解ガス中で行なった焼結条件は種々検討
の結果最も強度の出た条件は バーンオフ部の設定温度 400℃〃 メ
ッシュベルト速度 1 5 0 mm/m i n 焼結部の設定温度 600℃〃 メッ
シュベルト速度 1 0 0 mm/m i n であり、引張強度はT6処理後、平均29.5h/7I
IJを示した。
Furnace total length: 8000mm sintered material placement section 1500mm dewaxing section (nichrome wire heating) 2000mm sintering section
2000mm water cooling section 10
00mm Air cooling and inclined passage section 1500mm
Conveyor type: Mesh belt drive speed for both dewaxing section and sintering section: 10 to 200 mm/mi
n Matsuful dimensions: 150mm x 200trr
m Belt width: 180wn Mixed powder molding conditions are mixed powder composition (wt%) Al-4.4Cu-0.5Mg-0.8Si 1.5
Wax molding pressure 5 ton/cm2 Molded shape ISO 2740 tensile test piece (6 mm thickness), sintering was performed in ammonia decomposition gas After various examinations of the sintering conditions, the conditions that yielded the highest strength were the set temperature of the burn-off section. 400℃〃 Mesh belt speed 150 mm/min Set temperature of sintering part 600℃〃 Mesh belt speed 100 mm/min, Tensile strength is 29.5h/7I on average after T6 treatment
IJ was shown.

これを第1図に示すような従来の炉(各部の寸法は前述
したと同様、ただし傾斜部ぱなし)で脱ろう部、焼結部
の設定温度を同じとし、ベルトスピード1 5 0 t
rtm/m i n で流した場合は、焼結時間が若干
短かくなるためT6処理後の引張強度は平均2 5.
4 kg/vtitまでしかならない。
This is done in a conventional furnace as shown in Figure 1 (the dimensions of each part are the same as described above, except for the sloped part), with the same set temperature in the dewaxing part and the sintering part, and a belt speed of 150 t.
When flowing at rtm/min, the sintering time is slightly shorter, so the average tensile strength after T6 treatment is 25.
It can only reach up to 4 kg/vtit.

逆に1 0 0 rrrm/m i n で流した轡合
は、被焼結材が炉に入ってから出てくるまで10min
強も時間がかかるため生産性が落ちる。
On the other hand, when sintering is performed at 100 rrrm/min, it takes 10 min from the time the material to be sintered enters the furnace until it comes out.
However, productivity decreases because it takes time.

また、−60℃のガスを供給し、焼結部4の露点を常に
−40℃以下に保つには、第2図に示す本発明の炉の場
合、全部で5m3/hrの流量で充分であり、被処理物
品1を取り出した場合にも露点の変動は無った。
Furthermore, in the case of the furnace of the present invention shown in Fig. 2, a total flow rate of 5 m3/hr is sufficient to supply gas at -60°C and keep the dew point of the sintering section 4 below -40°C. There was no change in the dew point even when the article to be treated 1 was taken out.

尚、入口端2側は常時開放されており被処理物品1が外
気がまき込んで炉内に入る可能性もあるが、雰囲気ガス
は入口13から入口端2の方向に流れているので焼結部
4まで達することは無い。
Note that the inlet end 2 side is always open, and there is a possibility that outside air may enter the furnace when the article 1 is being sintered, but since the atmospheric gas flows from the inlet 13 toward the inlet end 2, sintering is not possible. It will never reach part 4.

実施列 2 実施列1とまったく同じ第2図に示すような構造の連続
式アルミ焼結炉を用い 混合粉末組成(重量%) Al−2.5%Cu−0.6%Mg−0.5%Si成形
圧力 5 ton /cm2 成形体形状 130φ×40Hブランク材 の成形体をN2 ガス雰囲気中で焼結を行なった後、中
心部および周辺部よりJIS7号試験片を切出し、T6
処理後の強度を調べた。
Implementation row 2 Using a continuous aluminum sintering furnace having the same structure as shown in FIG. 2 as in implementation row 1, mixed powder composition (wt%) Al-2.5%Cu-0.6%Mg-0.5 %Si molding pressure: 5 ton/cm2 After sintering the blank material with a shape of 130φ x 40H in a N2 gas atmosphere, JIS No. 7 test pieces were cut out from the center and periphery, and T6
The strength after treatment was examined.

各種予備実験の結果、最も強度の出た条件は、脱ろう部
の設定温度 400℃〃 メッシュベル
ト速度 10mm/min 焼結部の設定温度 〃 メッシュベルト速度40mm/m i nであり
、T6処理後の強度は平均34kg/mm2を示した。
As a result of various preliminary experiments, the conditions that yielded the highest strength were: Dewaxing section temperature set at 400°C Mesh belt speed 10 mm/min Sintering section set temperature Mesh belt speed 40 mm/min After T6 treatment The average strength was 34 kg/mm2.

これを従来の第1図に示す形式の炉で焼結した場合、ベ
ルトスピードが一定であるため、上記のように脱ろう部
と焼結部のメッシュベルトスピードに差をつけて最適な
メッシュベルトスピードの組合せを得ることはできない
When this is sintered in a conventional furnace of the type shown in Fig. 1, the belt speed is constant, so as mentioned above, the mesh belt speeds in the dewaxing section and the sintering section are set differently to create the optimal mesh belt. You can't get a combination of speeds.

例えば、ベルトスピードをI O rran/m i
n一定とした場合、脱ろうは充分できるが、焼結時間が
長すぎることにより焼結組織の粗大化が生じT6処理後
の引張強度は平均26@/yrt?tまで低下する。
For example, the belt speed is I O rran/m i
When n is constant, dewaxing can be achieved sufficiently, but if the sintering time is too long, the sintered structure becomes coarse and the tensile strength after T6 treatment is 26@/yr on average? decreases to t.

また被焼結材を炉に装入してから焼結完了までの一サイ
クル時間が3時間強余分にかかるという生産上の欠点を
有する。
Furthermore, it has a production disadvantage in that it takes a little more than three hours for one cycle from charging the material to be sintered into the furnace to completing sintering.

ベルトスピード40mm/min一定とすると、脱ろう
時間が足らず充分に脱ろうされない状態で焼結部に入っ
て来るたあ、焼結部へのろう蒸気の混入により焼結雰囲
気の純度が低下し、T6処理後の平均強度は23kg/
mm2程度までしかならない。
If the belt speed is kept constant at 40 mm/min, wax enters the sintering section without being sufficiently dewaxed due to insufficient dewaxing time, and wax vapor enters the sintering section, reducing the purity of the sintering atmosphere. Average strength after T6 treatment is 23kg/
It is only up to about mm2.

また連続して処理しそも焼結部4の露点は常に−40℃
以下に保たれていた。
Also, even if the process is continued, the dew point of the sintered part 4 is always -40℃.
It was kept below.

ガス入口13.14から供給する原料N2 ガスの露点
を−60℃一定とした場合、焼結ゾーンでの雰囲気露点
を−40℃以下に保つには、次に示すような流量が必要
である。
When the dew point of the raw material N2 gas supplied from the gas inlets 13 and 14 is kept constant at -60°C, the following flow rate is required to maintain the atmospheric dew point in the sintering zone at -40°C or less.

イ)一端閉鎖型の本発明の炉(第2図)→9m3/hr ロ)一端閉鎖+ガス置換室を組合せた本発明の炉→6m
3/hr(第2図と第4図の組合せこのように両端開放
の従来型の炉にくらべると本発明の一端閉鎖型の炉はは
るかにガス消費量が少ない利点がある。
A) Furnace of the present invention with one end closed (Fig. 2) → 9 m3/hr B) Furnace of the present invention with a combination of one end closed and a gas exchange chamber → 6 m
3/hr (combination of FIGS. 2 and 4) Compared to the conventional furnace with both ends open, the one-end closed furnace of the present invention has the advantage of much lower gas consumption.

また一端閉鎖型とガス置換室とを組合せた本発明の炉で
はさらにガス消費量が少なくてすむ。
Furthermore, the furnace of the present invention, which combines a one-end closed type furnace with a gas exchange chamber, can consume even less gas.

その上、イ)、の場合は焼結ゾーンの雰囲気露点は−4
5’C程度が限定であるが、ロ)の場合は−53℃程度
まで雰囲気ガス露点を下げることが可能なため、より高
純度な雰囲気を必要とする焼結にはこの方式が適してい
ることを確めた。
Moreover, in case a), the atmospheric dew point of the sintering zone is -4
Although it is limited to about 5'C, in the case of b), it is possible to lower the atmospheric gas dew point to about -53℃, so this method is suitable for sintering that requires a higher purity atmosphere. I made sure of that.

本発明によれば、炉出口端を閉鎖する構成としたことに
よって、焼結部を常に所要の露点に安定して維持するこ
とができた。
According to the present invention, by configuring the furnace outlet end to be closed, the sintered part could always be stably maintained at a required dew point.

.したがって必要なガス消費量も大幅に少なく、熱経済
にも優れ、また炉内雰囲気を従来に比べ高い純度に容易
に保つことができるので不良品の発生を著しく減じ、歩
留りを向上させることができる。
.. Therefore, the required gas consumption is significantly lower, the thermal economy is excellent, and the atmosphere inside the furnace can be easily maintained at a higher purity than before, which significantly reduces the occurrence of defective products and improves yield. .

特に、被処理物品の取出口にガス置換室を設けることに
よって常に炉出口端からの外気の流入を完全に遮断する
よう閉鎖することができ、雰囲気の純度保持が容易であ
り、雰囲気ガス消費量を更に減ずることができる。
In particular, by providing a gas exchange chamber at the outlet of the article to be processed, it can be closed to completely block the inflow of outside air from the furnace outlet end, making it easy to maintain the purity of the atmosphere and reducing atmospheric gas consumption. can be further reduced.

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

第1図は従来構造の焼結用雰囲気加熱炉の線図的縦断面
図、第2図は本発明による焼結用雰囲気加熱炉の線図的
縦断面図、第3−は第2図に示す炉マツフルの断面図、
第4図は炉出口端の傾斜通路に設けられるガス置換室の
概略線図、第5図iよび第6図は第4図に示す置換室の
制御回路図、第7図はガス置換室の他の例を示す概略線
図、第8図および第9図は第7図に示す入口および出口
シャツタの作動部を示す略線図、第10図および第11
図は第7図ないし第9図に示すガス置換室の制御回路図
である。 1・・・被処理物品、2・・・入口端、3・・・脱ろう
部、4・・・焼結部、5・・・冷却部、6・・・出口端
、7・・・コンベヤ、8,9・・・加熱コイル、10・
・・水冷ジャケット、11・・・駆動ローラ、12・・
・案内ローラ、13,14・・・雰囲気ガス導入口、1
5・・・雰囲気ガス放出口、18・・・ガスカーテン噴
出口、20・・・脱ろう部コンベヤ、21・・・焼結部
コンベヤ、22,23・・・駆動ローラ、24・・・上
段炉床、25・・・下段炉床、26・・・連通孔、27
, 2B・・・案内ローラ、29,30・・・炉内ピ
ット、31・・・外気遮蔽傾斜通路、32・・・常閉出
ロシャツタ、33・・・アクチュエータ、34・・・雰
囲気ガス導入管、35.36・・・I) ミットスイッ
チ、37・・・遮断弁、38・・・制御回路、39,4
0・・・シャツタ、41・・・ガス置換室、− 4 2
・・・カス導入管、43・・・ガス排出管、44・・・
ガス導入管、46・・・遮断弁、47,48,49,5
0・・・リミットスイッチ、51.52・・・アクチュ
エータ、53,54・・・シャツタ、55・・・ガス置
換室、56・・・傾斜板、57・・・枢支軸、58・・
・ばね、59・・・回転軸、60・・・軸受、62・・
・ラック、63・・・エヤシリンダ、64・・・雰囲気
ガス導入管、65・・・排出管、66・・・リミットス
イッチ、67,68,70,7σ・・・電磁三方弁、7
1・・・電磁弁、72.73・・・タイマ、74・・・
遅延回路、75・・・遅延リレー。
Fig. 1 is a diagrammatic longitudinal sectional view of a sintering atmosphere heating furnace of conventional structure, Fig. 2 is a diagrammatic longitudinal sectional view of a sintering atmosphere heating furnace according to the present invention, and Fig. 3- is a diagrammatic longitudinal sectional view of a sintering atmosphere heating furnace of a conventional structure. A cross-sectional view of the furnace Matsufuru shown,
Figure 4 is a schematic diagram of the gas exchange chamber provided in the inclined passage at the end of the furnace outlet, Figures 5i and 6 are control circuit diagrams of the exchange chamber shown in Figure 4, and Figure 7 is a diagram of the gas exchange chamber. 8 and 9 are schematic diagrams showing other examples, and FIGS. 10 and 11 are schematic diagrams showing the operating parts of the inlet and outlet shutters shown in FIG.
This figure is a control circuit diagram of the gas replacement chamber shown in FIGS. 7 to 9. DESCRIPTION OF SYMBOLS 1... Article to be processed, 2... Inlet end, 3... Dewaxing section, 4... Sintering section, 5... Cooling section, 6... Outlet end, 7... Conveyor , 8, 9... heating coil, 10.
...Water cooling jacket, 11...Drive roller, 12...
・Guide rollers, 13, 14...Atmospheric gas inlet, 1
5... Atmospheric gas discharge port, 18... Gas curtain outlet, 20... Dewaxing section conveyor, 21... Sintering section conveyor, 22, 23... Drive roller, 24... Upper stage Hearth, 25...Lower hearth, 26...Communication hole, 27
, 2B...Guide roller, 29, 30...Furnace pit, 31...Outside air shielding inclined passage, 32...Normally closed Roshutter, 33...Actuator, 34...Atmospheric gas introduction pipe , 35.36...I) Mitt switch, 37... Shutoff valve, 38... Control circuit, 39,4
0...Shutter, 41...Gas replacement chamber, -4 2
... Waste introduction pipe, 43 ... Gas discharge pipe, 44 ...
Gas introduction pipe, 46...Shutoff valve, 47, 48, 49, 5
0...Limit switch, 51.52...Actuator, 53, 54...Shutter, 55...Gas replacement chamber, 56...Slanted plate, 57...Pivot shaft, 58...
・Spring, 59...Rotating shaft, 60...Bearing, 62...
・Rack, 63... Air cylinder, 64... Atmospheric gas introduction pipe, 65... Discharge pipe, 66... Limit switch, 67, 68, 70, 7σ... Solenoid three-way valve, 7
1...Solenoid valve, 72.73...Timer, 74...
Delay circuit, 75...Delay relay.

Claims (1)

【特許請求の範囲】 1 炉内の雰囲気を一定に保った炉内に搬送装置を設け
、この搬送装置により物品を移動させつつ処理するよう
にした雰囲気加熱炉において、該加熱炉の出口端に連接
して前記物品が滑り落ちる傾斜角度を有する傾斜通路を
設け、該通路に物品の通過を検知して信号を発する検知
手段と該信号に基づいて開閉する出ロシャツタおよび前
記信号に基づいて前記出口シャツタの少くとも開口時に
雰囲気ガスを供給する手段とを設けてなる雰囲気加熱炉
。 2 前記出口シャツタにより開閉される出口に隣接して
ガス置換室を設けたことを特徴とする特許請求の範囲第
1項に記載の雰囲気加熱炉。
[Scope of Claims] 1. In an atmosphere heating furnace in which a conveyance device is provided in a furnace in which the atmosphere inside the furnace is kept constant, and articles are processed while being moved by this conveyance device, there is a device at the outlet end of the heating furnace. An inclined passage having an inclination angle through which the article slides is provided, and the passage includes a detection means for detecting passage of the article and emitting a signal, an exit shirt stopper that opens and closes based on the signal, and an exit shirt stopper that opens and closes based on the signal. and means for supplying atmospheric gas at least when the furnace is opened. 2. The atmosphere heating furnace according to claim 1, wherein a gas replacement chamber is provided adjacent to the outlet opened and closed by the outlet shutter.
JP54141199A 1979-11-02 1979-11-02 Atmosphere heating furnace Expired JPS583192B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP54141199A JPS583192B2 (en) 1979-11-02 1979-11-02 Atmosphere heating furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP54141199A JPS583192B2 (en) 1979-11-02 1979-11-02 Atmosphere heating furnace

Publications (2)

Publication Number Publication Date
JPS5665904A JPS5665904A (en) 1981-06-04
JPS583192B2 true JPS583192B2 (en) 1983-01-20

Family

ID=15286448

Family Applications (1)

Application Number Title Priority Date Filing Date
JP54141199A Expired JPS583192B2 (en) 1979-11-02 1979-11-02 Atmosphere heating furnace

Country Status (1)

Country Link
JP (1) JPS583192B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112556405B (en) * 2020-12-14 2022-06-03 株洲瑞德尔智能装备有限公司 Sintering furnace dewaxing structure and sintering furnace

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2719387C3 (en) * 1977-04-30 1980-12-04 Dr.-Ing. Rudolf Hell Gmbh, 2300 Kiel Device for displaying overcorrections in electronic color correction

Also Published As

Publication number Publication date
JPS5665904A (en) 1981-06-04

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