JPS58123801A - Heat treatment furnace combined with gas converting section in one body - Google Patents

Heat treatment furnace combined with gas converting section in one body

Info

Publication number
JPS58123801A
JPS58123801A JP777982A JP777982A JPS58123801A JP S58123801 A JPS58123801 A JP S58123801A JP 777982 A JP777982 A JP 777982A JP 777982 A JP777982 A JP 777982A JP S58123801 A JPS58123801 A JP S58123801A
Authority
JP
Japan
Prior art keywords
cylinder
heat treatment
treatment furnace
furnace
gas
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
Application number
JP777982A
Other languages
Japanese (ja)
Inventor
Noriaki Kawasaki
川崎 憲明
Yasumasa Kureha
呉羽 康正
Mineo Onoda
小野田 岑夫
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.)
Sumitomo Electric Industries Ltd
Original Assignee
Sumitomo Electric Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sumitomo Electric Industries Ltd filed Critical Sumitomo Electric Industries Ltd
Priority to JP777982A priority Critical patent/JPS58123801A/en
Publication of JPS58123801A publication Critical patent/JPS58123801A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F3/00Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces
    • B22F3/003Apparatus, e.g. furnaces

Landscapes

  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Mechanical Engineering (AREA)
  • Powder Metallurgy (AREA)
  • Tunnel Furnaces (AREA)

Abstract

PURPOSE:To reduce the consumption of energy and the floor space of equipment by providing a reacting cylinder for generation of converted gases in a body of a heat treatment furnace thereby combining a converting furnace and a sintering furnace, etc. into one body. CONSTITUTION:A muffle 12 which is opened at both ends is provided in a body 11 of a heat treatment furnace, and a reacting cylinder 15 for generation of converted gases which is heated by heating elements is mounted on the outside circumference of the muffle 12. The cylinder 15 is formed of double pipes of an inside cylinder 16 and an outside cylinder 17, and a gas passage 18 is formed between both cylinders 16 and 17. An introducing pipe for gaseous raw materials is penetrated into a flange 21 stuck to the cylinder 17 and while the gaseous mixture fed into said pipe passes through the inside of the cylinder 17, the same is brought into contact with catalysts 23, and is thereby converted. The converted gases are passed into the passage 18 between the cylinder 16 and the cylinder 17, and are fed into the muffle 12 through a vent pipe 20. By such mechanism, the co-possession of the heating elements for heat treatment and the heating elements for reaction is made possible, and the consumption of energy is reduced.

Description

【発明の詳細な説明】 この発明はガス変成部を一体化した熱処理炉に関するも
のである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a heat treatment furnace with an integrated gas conversion section.

変成ガスを使用する熱処理炉としては、例えば粉末金属
部品製造のための焼結炉がある。焼結炉においては、炭
化水素系ガスと空気との混合ガスを1000℃以上に加
熱した触媒中を通過させ吸熱形ガスに変成し、その変成
ガスの雰囲気下に詔いて焼結が行なわれる。そのため、
従来は第1図に示すように、変成炉1と焼結炉2を別個
独立に設け、変成炉1において発生された変成ガスを導
管3によって焼結炉2内へ導くようにしていた。
Examples of heat treatment furnaces that use modified gas include sintering furnaces for producing powder metal parts. In a sintering furnace, a mixed gas of hydrocarbon gas and air is passed through a catalyst heated to 1000° C. or higher to be converted into an endothermic gas, and then sintered in an atmosphere of the converted gas. Therefore,
Conventionally, as shown in FIG. 1, a shift furnace 1 and a sintering furnace 2 were provided separately, and the shift gas generated in the shift furnace 1 was guided into the sintering furnace 2 through a conduit 3.

上記の変成炉1は触媒を充填した反応筒4と、その触媒
を加熱するための発熱体5、及び変成ガス中にす\が発
生するこ六を防止するた吟の冷却器6を備えており、ガ
スλと空気すをミキサ7によって混合し、プロア8を通
じて混合ガスを反応筒4に送入するようになっている。
The above-mentioned shift conversion furnace 1 is equipped with a reaction tube 4 filled with a catalyst, a heating element 5 for heating the catalyst, and a cooler 6 for preventing generation of soot in the converted gas. The gas λ and air are mixed by a mixer 7, and the mixed gas is fed into the reaction tube 4 through a blower 8.

混合ガスは反応筒4の内部において触媒により吸熱形ガ
スに変成され、その変成ガスは冷却器6を通過して導管
3から焼結炉2の内部に送り込まれる。焼結炉2はその
内部に発熱体9を有し、ベルトコンベア10上に載せら
れた処理物を上記の変成ガスによる保護雰囲気下におい
て焼結するようになっている。
The mixed gas is converted into an endothermic gas by a catalyst inside the reaction tube 4, and the converted gas passes through the cooler 6 and is sent into the sintering furnace 2 through the conduit 3. The sintering furnace 2 has a heating element 9 therein, and is configured to sinter the processed material placed on a belt conveyor 10 in a protective atmosphere of the above-mentioned modified gas.

従来の装置は上記のように構成されているが、この装置
には次の如き問題がある。
Although the conventional device is constructed as described above, this device has the following problems.

山 変成炉と焼結炉が独立しているため、炉壁及び炉蓋
における熱放散による熱損失が2個所において発生する
Yama: Because the conversion furnace and sintering furnace are independent, heat loss occurs in two places due to heat dissipation in the furnace wall and furnace lid.

(2)  変成炉と焼結粘のそれぞれの設置スペースを
必要とし、またそれぞれの設備費用を必要とする。
(2) Requires installation space for the transformation furnace and sintered clay, and requires equipment costs for each.

(3)  変成炉と焼結炉のそれぞれにおいて運転管理
をする必要がある。
(3) It is necessary to manage the operation of both the conversion furnace and the sintering furnace.

以上のように、従来の装置は変成炉と焼結炉が分離独立
したものであるため、種々の問題があるものであった。
As described above, in the conventional apparatus, the conversion furnace and the sintering furnace are separated and independent, and therefore there are various problems.

そこで、この発明は変成炉と儲結炉を一体化しに熱処理
炉を提供することを目的とするものであ乙。
Therefore, the purpose of this invention is to provide a heat treatment furnace that integrates a conversion furnace and a coalescence furnace.

以下、この発明の構成を第2図以下に基づいて説明する
Hereinafter, the configuration of the present invention will be explained based on FIG. 2 and subsequent figures.

この発明に係る熱処理炉は1.第2図に示すよう:・・
(。
The heat treatment furnace according to the present invention includes 1. As shown in Figure 2:...
(.

に、熱処理炉本体11の内部に両端開放のマツフル12
を設け、その内部にメツシュベルト等ノベルトコンベア
13を通過せしめる。また、上記マツフル12の上下、
即ら炉体11の頂壁及び底壁1こ沿って発熱体14.1
4を設け、マツフル12を通じてコンベア13上の処理
物を加熱するようになっている。
In the heat treatment furnace body 11, there is a matsufuru 12 with both ends open.
A belt conveyor 13 such as a mesh belt is passed through the inside of the belt conveyor 13. In addition, the top and bottom of the above Matsuful 12,
That is, heating elements 14.1 are placed along the top and bottom walls of the furnace body 11.
4 is provided to heat the processed material on the conveyor 13 through the Matsufuru 12.

上記のマツフル12の外周には反応筒15が取付けられ
ている。反応筒15の取付は位置は、炉本体11の断面
積を拡大させず、且つ処理物に与える温度分布の均一性
を阻害しない部位が選定される。例えば、第3図及び第
4図に示すように、マツフル12の斜め上部に取付ける
A reaction tube 15 is attached to the outer periphery of the Matsufuru 12 described above. The mounting position of the reaction tube 15 is selected at a location that does not increase the cross-sectional area of the furnace body 11 and does not impede the uniformity of the temperature distribution given to the processed material. For example, as shown in FIGS. 3 and 4, it is attached diagonally to the upper part of the matsufuru 12.

反応筒11は外筒16と内筒17の2重管によって構成
され、両筒16.17間の間隙がガスの通路18を形成
している。上記外筒16の開放端(図の右端)は、マツ
フル12の7ランジ19を貫通し、且つその貫通部分に
おいて2ランジ19と一体化されている。外筒16の閉
塞端(図の左端)は熱膨張を許容するために非拘束状態
にあり、また中間部分は適宜の支持金具を介してマツフ
ル12に一装着される。また外筒16の一部には上記の
通路18とマツフル12の内部とを連通ずる通気管20
が設けられている(第4図参照)。
The reaction tube 11 is composed of a double tube consisting of an outer tube 16 and an inner tube 17, and a gap between the two tubes 16 and 17 forms a gas passage 18. The open end (right end in the figure) of the outer cylinder 16 passes through the seventh flange 19 of the pine full 12, and is integrated with the second flange 19 at the penetrating portion. The closed end (the left end in the figure) of the outer cylinder 16 is in an unrestricted state to allow thermal expansion, and the intermediate part is attached to the pine full 12 via a suitable support fitting. In addition, a ventilation pipe 20 is provided in a part of the outer cylinder 16, which communicates the passage 18 with the inside of the matsufuru 12.
(See Figure 4).

上記内筒17の一端は、外筒16の開放端を閉塞するフ
ランジ21の内面に固着されており、7ランジ21を外
筒16から外すことにより、内筒17を抜き出せるよう
になっている。内筒17の内部には一定間隔をおいて隔
壁板22が設けられており、隔壁板22相互間の空室に
触媒23を充填しである。各隔壁板22及び内筒17の
閉塞端に通気孔24を設け、各通気孔24の位置を交互
に変えて配列しである。内筒17を固着した上記のフラ
ンジ21には原料ガスの導入管25を貫通しであるので
、ブロア26によって送り込まれた混合ガスは、内筒1
7の内部を通過する間に触媒23に触れて変成され、そ
の変成ガスが外筒16と内周17間の通路1日を通り、
通気管20からマツフル12内に送り込まれる。
One end of the inner cylinder 17 is fixed to the inner surface of a flange 21 that closes the open end of the outer cylinder 16, and by removing the 7 flange 21 from the outer cylinder 16, the inner cylinder 17 can be extracted. . Partition plates 22 are provided inside the inner cylinder 17 at regular intervals, and the spaces between the partition plates 22 are filled with a catalyst 23. Ventilation holes 24 are provided at the closed end of each partition plate 22 and the inner cylinder 17, and the positions of the ventilation holes 24 are alternately arranged. The raw material gas introduction pipe 25 passes through the flange 21 to which the inner cylinder 17 is fixed, so that the mixed gas fed by the blower 26 flows into the inner cylinder 1.
While passing through the inside of the cylinder 7, it touches the catalyst 23 and is transformed, and the transformed gas passes through the passage between the outer cylinder 16 and the inner circumference 17,
It is fed into the Matsufuru 12 from the ventilation pipe 20.

以上はマツフル12を用いζそのマツフル12に反応筒
15を取付ける型式のものであるが、このマツフル12
を省略し、コンベア13を炉本体11の内部にむき出し
のま\通過せしめ、反応筒15を炉本体11の内部に適
宜手段で取付けるようにしてもよい。また、反応筒15
は必ずしも2重管である必要はな(1,基本的には上述
の内管17だけで構成されるものであってもよい。
The above is a type that uses the Matsufuru 12 and attaches the reaction tube 15 to the Matsufuru 12.
may be omitted, the conveyor 13 may be allowed to pass through the interior of the furnace body 11 as is, and the reaction tube 15 may be attached to the interior of the furnace body 11 by appropriate means. In addition, the reaction tube 15
does not necessarily have to be a double pipe (1, basically, it may be composed only of the above-mentioned inner pipe 17).

更に、上記の例は通気管20から変成ガスを直接マツフ
ル12内に導入するようになっているが、マツフル12
内に導入する前に適宜な導管によって炉本体11外へ引
出し、その導管を適宜な冷却器やガス成分調整器を通過
せしめた上で炉本体11内へ導入するようにしてもよい
Furthermore, in the above example, the modified gas is directly introduced into the Matsufuru 12 from the vent pipe 20, but the Matsufuru 12
Before being introduced into the furnace body 11, the gas may be drawn out of the furnace main body 11 through an appropriate conduit, passed through an appropriate cooler or gas composition regulator, and then introduced into the furnace main body 11.

なお、実験結果を示せば表1及び表2のとおりである。The experimental results are shown in Tables 1 and 2.

表1は、従来の装置と本発明の装置とによる焼結製品の
品質を示しており、その成分はFe−1,5%Cu −
Q、5%C成形密度は6.8g/cd  である。また
、表2は製品重量150 Q/Hr 、ガス流量65 
rrl/Hr時の各装置の消費電力を示している。
Table 1 shows the quality of sintered products produced by the conventional device and the device of the present invention, the components of which are Fe-1,5%Cu-
Q, 5% C molding density is 6.8 g/cd. Table 2 also shows product weight 150 Q/Hr and gas flow rate 65
It shows the power consumption of each device at rrl/Hr.

これらの実験結果から、品質の点では従来の装置とはゾ
同等であるが、消費電力の点では本発明の装置が17 
KWH/Hだけ節減できることが理解されよう。
These experimental results show that the device of the present invention is equivalent to the conventional device in terms of quality, but 17% lower in terms of power consumption.
It will be understood that only KWH/H can be saved.

表1 品 質 表2 消費電力 (V、WH/H) 以上のように、この発明は内部に発熱体を有する熱処理
炉本体の内部にその発熱体によって加熱される変成ガス
発生用の反応筒を設けたことにより、熱処理のための発
熱体と反応のための発熱体を共有することができる結果
エネルギーの消費量を低減することができると共に、設
備の設置スペースが小さくなり、また運転管理個所が集
中され、表だ設備費も低減する等の効果を発揮すること
ができる。
Table 1 Quality Table 2 Power consumption (V, WH/H) As described above, the present invention includes a reaction cylinder for generating converted gas heated by the heating element inside the heat treatment furnace main body that has a heating element inside. As a result, the heating element for heat treatment and the heating element for reaction can be shared, reducing energy consumption, reducing equipment installation space, and reducing the number of operational management points. It is possible to achieve effects such as reducing the obvious equipment costs.

なお、変成ガスは一旦熱処理炉本体外へ引出すこともあ
るが、これを引出すことなく、反応筒の出側から直接本
体内へ導入することもでき、その場合はガスの再加熱に
要するエネルギーが不要になる。
Note that the converted gas may be drawn out of the heat treatment furnace body once, but it can also be introduced directly into the main body from the outlet side of the reaction tube without being drawn out. In that case, the energy required to reheat the gas is reduced. becomes unnecessary.

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

第1図は従来の装置の断面図、第2図はこの発明に係る
装置の断面図、第3図は第2図の一部拡大横断平面図、
第4図は第2図の一部拡大縦断側面図である。 11・・・焼結炉本体、14・・・発熱体、15・・・
反応筒、16・・・外筒、17・・・内筒、18・・・
通路、20・・・通気管 特許出願人  住友電気工業株式会社 11゜ 同  代理人  鎌  1) 文  二第1図 第2図 第3図 4==−一
FIG. 1 is a sectional view of a conventional device, FIG. 2 is a sectional view of a device according to the present invention, and FIG. 3 is a partially enlarged cross-sectional plan view of FIG.
FIG. 4 is a partially enlarged longitudinal sectional side view of FIG. 2. 11... Sintering furnace main body, 14... Heating element, 15...
Reaction cylinder, 16... Outer cylinder, 17... Inner cylinder, 18...
Passageway, 20... Ventilation pipe Patent applicant: Sumitomo Electric Industries, Ltd. 11゜ Agent: Kama 1) Text 2 Figure 1 Figure 2 Figure 3 Figure 4 ==-1

Claims (1)

【特許請求の範囲】 、11  内部に発熱体を有する熱処理炉本体の内部に
L記発熱体によって加熱される変成ガス発生用反応筒を
設け、上記反応筒の入側に原料ガス導入部を設け、且つ
その出側と熱処理炉本体内部とを連通せしめたことを特
徴とするガス変成部一体型熱処理炉。 (:2)  上記反応筒の出側と熱処理炉本体内部とを
、変成ガスの冷却部及び成分調整部を経て連通せしめた
ことを特徴とする特許請求の範囲第1項に記載のガス変
成部一体型熱処理炉。
[Scope of Claims] , 11 A reaction cylinder for generating a converted gas heated by the heating element L is provided inside a heat treatment furnace body having a heating element therein, and a raw material gas introduction part is provided on the inlet side of the reaction cylinder. A heat treatment furnace integrated with a gas conversion part, characterized in that the outlet side thereof is communicated with the inside of the heat treatment furnace main body. (:2) The gas conversion unit according to claim 1, wherein the outlet side of the reaction cylinder and the inside of the heat treatment furnace main body are communicated through a conversion gas cooling unit and a component adjustment unit. Integrated heat treatment furnace.
JP777982A 1982-01-20 1982-01-20 Heat treatment furnace combined with gas converting section in one body Pending JPS58123801A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP777982A JPS58123801A (en) 1982-01-20 1982-01-20 Heat treatment furnace combined with gas converting section in one body

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP777982A JPS58123801A (en) 1982-01-20 1982-01-20 Heat treatment furnace combined with gas converting section in one body

Publications (1)

Publication Number Publication Date
JPS58123801A true JPS58123801A (en) 1983-07-23

Family

ID=11675155

Family Applications (1)

Application Number Title Priority Date Filing Date
JP777982A Pending JPS58123801A (en) 1982-01-20 1982-01-20 Heat treatment furnace combined with gas converting section in one body

Country Status (1)

Country Link
JP (1) JPS58123801A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6056730U (en) * 1983-09-22 1985-04-20 株式会社ヤマザキ電機 Energy-saving conveyor type sintering furnace
JPS61162795U (en) * 1985-03-29 1986-10-08
JPS63127943U (en) * 1987-02-09 1988-08-22

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4851809A (en) * 1971-10-27 1973-07-20

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4851809A (en) * 1971-10-27 1973-07-20

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6056730U (en) * 1983-09-22 1985-04-20 株式会社ヤマザキ電機 Energy-saving conveyor type sintering furnace
JPS6344429Y2 (en) * 1983-09-22 1988-11-18
JPS61162795U (en) * 1985-03-29 1986-10-08
JPH0210091Y2 (en) * 1985-03-29 1990-03-13
JPS63127943U (en) * 1987-02-09 1988-08-22

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