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JPS6041848B2 - High temperature diffusion furnace - Google Patents
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JPS6041848B2 - High temperature diffusion furnace - Google Patents

High temperature diffusion furnace

Info

Publication number
JPS6041848B2
JPS6041848B2 JP13406977A JP13406977A JPS6041848B2 JP S6041848 B2 JPS6041848 B2 JP S6041848B2 JP 13406977 A JP13406977 A JP 13406977A JP 13406977 A JP13406977 A JP 13406977A JP S6041848 B2 JPS6041848 B2 JP S6041848B2
Authority
JP
Japan
Prior art keywords
temperature
furnace
tube
diffusion furnace
silicon carbide
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
JP13406977A
Other languages
Japanese (ja)
Other versions
JPS5467764A (en
Inventor
陽一 水品
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.)
Kokusai Denki Electric Inc
Original Assignee
Kokusai Electric 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 Kokusai Electric Co Ltd filed Critical Kokusai Electric Co Ltd
Priority to JP13406977A priority Critical patent/JPS6041848B2/en
Publication of JPS5467764A publication Critical patent/JPS5467764A/en
Publication of JPS6041848B2 publication Critical patent/JPS6041848B2/en
Expired legal-status Critical Current

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  • Resistance Heating (AREA)
  • Control Of Resistance Heating (AREA)

Description

【発明の詳細な説明】 本発明は高温にて動作可能な拡散炉に関する。[Detailed description of the invention] The present invention relates to a diffusion furnace that can operate at high temperatures.

たとえば電力用トランジスタ、サイリスタ等の製造にお
ける拡散酸化には一般に長時間作業が多くこの短縮が強
く望まれている。作業時間の短縮によつて生産量が増え
、生産量を一定とすれば設備が少くて済むが、拡散炉は
大量に使用されることが多いため、消費電力の低減は大
きな利点となる。さて本発明では拡散に要する時間は拡
散温度を高くできれば短縮できることおよび拡散炉の一
般的な使用においても炉のヒートアップ(Heatup
)およびクールダウン(Cooldown)を早く行え
ば常時所定の温度に炉を保つ必要はなく、作業中のみ昇
温保持すればよいこと(これはライニングコストの低減
になる)に着目して炉を構成した。
For example, diffusion oxidation in the manufacture of power transistors, thyristors, etc. generally requires long hours of work, and there is a strong desire to shorten this time. Shortening work time increases production, and if production remains constant, less equipment is required, but since diffusion furnaces are often used in large quantities, reducing power consumption is a major advantage. Now, in the present invention, the time required for diffusion can be shortened by increasing the diffusion temperature, and also in the general use of a diffusion furnace.
) and cool down quickly, there is no need to keep the furnace at a predetermined temperature all the time, and the furnace only needs to be raised and maintained during work (this reduces lining costs). did.

以下図面によつて説明する。図1は従来の拡散炉の構造
例図で、1は石英製プロセチユーブ(反応管)、2はア
ルミナ製ライナーチューブ(均熱管)、3は加熱用ヒー
タ、4は断熱材、5は炉体または炉の外被である。
This will be explained below with reference to the drawings. Figure 1 shows an example of the structure of a conventional diffusion furnace. 1 is a quartz process tube (reaction tube), 2 is an alumina liner tube (soaking tube), 3 is a heater, 4 is a heat insulating material, and 5 is a furnace body or It is the outer covering of the furnace.

熱処理物は反応管1の一端から出し入れし、lbは排気
ポンプ等に導かれる排気口である。従来はこのようにヒ
ータ3として金属発熱体(商品名ニクロム、カンタル等
)を使用した抵抗加熱式炉が用いられているが、金属発
熱体の最高使用温度は1375℃であつて電気炉として
常用できるのは約12800Cが限度である。
The heat-treated product is taken in and out from one end of the reaction tube 1, and lb is an exhaust port that is led to an exhaust pump or the like. Conventionally, a resistance heating type furnace using a metal heating element (product name: Nichrome, Kanthal, etc.) as the heater 3 has been used, but the maximum operating temperature of the metal heating element is 1375°C, so it cannot be used regularly as an electric furnace. The maximum temperature that can be achieved is approximately 12,800C.

このため深い拡散や厚い酸化膜を得ようとすれは長時間
炉を動作させることが必要で、生産量の制限、電力費の
増大等の問題がある。本発明は上記の欠点を取除いたも
ので、図2および図3はそれぞれ本発明を実施した拡散
炉の構造例概要図である。
Therefore, in order to achieve deep diffusion and a thick oxide film, it is necessary to operate the furnace for a long time, which poses problems such as limited production and increased power costs. The present invention eliminates the above-mentioned drawbacks, and FIGS. 2 and 3 are schematic diagrams of structural examples of diffusion furnaces embodying the present invention, respectively.

これらの図において1は石英J製反応管、3aは1〜3
分割補助ヒータ、6はシリコンカーバイト (炭化ケイ
素、以下SiCと略記する)を用いた均熱管、7は端子
、8は変圧器、9は電源、10は電源入力制御器(サイ
リスタ使用)、11はSiC製反応管で、第3図は第2
図に丁おける石英反応管1を省き、SiC製均熱管で兼
用するように構成したものである。図2および図3から
明らかなように本発明の炉においてはSiC均熱管6ま
たはSiC反応管11を主発熱体とし、その外部に金属
発熱体を用いた補助発熱体3aを配置することが特徴で
、これらを用いて精密な温度制御および温度分布制御を
行うことによつて、従来の金属発熱体を使用した電気炉
に比べてより高温を短時間に得ることができる。その理
由および方法を次に説明する。SlCは低温状態では抵
抗値が高くしかも抵抗温度係数は負で(金属抵抗よりは
小さいが)あるため、これを発熱体として使用するには
初期に高電圧を与えて発熱させ次に除々に印加電圧を下
げてゆく手順が必要て、この制御には複雑な装置が必要
になるという欠点があつた。
In these figures, 1 is a reaction tube made of quartz J, and 3a is 1 to 3.
Divided auxiliary heater, 6 is a heat soaking tube using silicon carbide (silicon carbide, hereinafter abbreviated as SiC), 7 is a terminal, 8 is a transformer, 9 is a power supply, 10 is a power input controller (using a thyristor), 11 is a reaction tube made of SiC, and Fig. 3 is a reaction tube made of SiC.
The quartz reaction tube 1 shown in the figure is omitted, and a SiC soaking tube is used for the same purpose. As is clear from FIGS. 2 and 3, the furnace of the present invention is characterized in that the SiC soaking tube 6 or the SiC reaction tube 11 is used as the main heating element, and an auxiliary heating element 3a using a metal heating element is disposed outside thereof. By using these to perform precise temperature control and temperature distribution control, higher temperatures can be obtained in a shorter time than in electric furnaces that use conventional metal heating elements. The reason and method will be explained below. SlC has a high resistance value at low temperatures and a negative temperature coefficient of resistance (though smaller than metal resistance), so in order to use it as a heating element, it is necessary to first apply a high voltage to generate heat, then gradually apply it. The drawback was that a step was required to lower the voltage, and this control required complicated equipment.

本発明では金属発熱体を用いた補助ヒータ3aを設け、
最初補助ヒータ3aに通電してある温度までSiC管6
または11を昇温させた後、抵抗値が低下したSlC管
に電力を投入して容易に高温を得られるようにしている
。SiC管では最高2000′Cまで得られるが、シリ
コンSiの融点が1420℃であるから炉内温度は14
00℃前後が望ましく、この程度の温度に維持できれば
拡散工程の所要時間は著しく短縮できる。図4は本発明
による炉の温度特性で、横軸の1は炉軸に沿つた炉の入
口端よりの距離、T1はSiC主ヒータの温度、TOは
炉内の所要温度を示している。TOとT1の差ΔTE,
ΔTOは分割ヒータ3aの各ヒータが分担して上昇させ
なければならない温度である。なお主ヒータの温度をT
。まで上げることは容易であつてこの場合には分割ヒー
タ3aの中央のヒータは省いてよいことは明らかである
が、前記のように初期の電力を節減したり、作業中のみ
昇温するなどの利点を活用するには一般に必要である。
図5は本発明の炉の温度制御装置の構成例図で、温度を
制御すべき各ヒータに熱電対のような温度検出器13と
その出力によつて電力制御器(たとえばサイリスタ)1
0を制御する温度自動制御器12を設けて、あらかじめ
定められた温度制御を行わせることが可能なことはよく
知られているので説明は省略する。
In the present invention, an auxiliary heater 3a using a metal heating element is provided,
Initially, the auxiliary heater 3a is energized until the SiC tube 6 reaches a certain temperature.
Alternatively, after raising the temperature of 11, power is applied to the SlC tube whose resistance value has decreased so that a high temperature can be easily obtained. In a SiC tube, temperatures up to 2000'C can be obtained, but since the melting point of silicon Si is 1420°C, the temperature inside the furnace is 14°C.
The temperature is preferably around 00°C, and if the temperature can be maintained at this level, the time required for the diffusion process can be significantly shortened. FIG. 4 shows the temperature characteristics of the furnace according to the present invention, where 1 on the horizontal axis represents the distance from the inlet end of the furnace along the furnace axis, T1 represents the temperature of the SiC main heater, and TO represents the required temperature inside the furnace. Difference ΔTE between TO and T1,
ΔTO is the temperature that each heater of the divided heater 3a must share in raising. In addition, the temperature of the main heater is T.
. It is easy to raise the temperature to 100%, and in this case it is obvious that the central heater of the divided heaters 3a can be omitted, but as mentioned above, it is possible to save initial power or raise the temperature only during work. Generally necessary to take advantage of the benefits.
FIG. 5 is a configuration example diagram of a furnace temperature control device according to the present invention, in which each heater whose temperature is to be controlled has a temperature detector 13 such as a thermocouple, and a power controller (for example, a thyristor) 1 according to the output thereof.
It is well known that it is possible to perform predetermined temperature control by providing an automatic temperature controller 12 that controls 0, so a description thereof will be omitted.

以上のように本発明の炉は従来の拡散炉に比べて高温が
得られるので、拡散に要する時間が短縮され、電力費の
低減と設備の効率向上従つて小形化が実現できるなど工
業上の効果は明白である。
As described above, since the furnace of the present invention can obtain a higher temperature than the conventional diffusion furnace, the time required for diffusion is shortened, and it is possible to reduce the power cost, improve the efficiency of equipment, and realize miniaturization. The effect is obvious.

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

図1は従来の拡散炉の構造例図、図2および図3はそれ
ぞれ本発明を実施した炉の構造例図、図4はその温度特
性図、図5は本発明の炉の温度制御装置の構成例図であ
る。 1・・・・・・反応管、2・・・・・・均熱管、3・・
・・・・ヒータ、3a・・・・・・分割ヒータ、4・・
・・・・断熱材、5・・・・・・炉の外囲、6・・・・
・・SiCを用いた均熱管、7・・・・・・端子、8・
・・・・・変圧器、9・・・・・・電源、10・・・・
・・電力制御器、11・・・・・・SiCを用いた反応
管、12・・・・・温度自動制御器、13・・・・・・
温度検出器。
FIG. 1 is a structural example of a conventional diffusion furnace, FIGS. 2 and 3 are structural examples of a furnace according to the present invention, FIG. 4 is a temperature characteristic diagram thereof, and FIG. 5 is a diagram of a temperature control device for a furnace according to the present invention. It is a configuration example diagram. 1... Reaction tube, 2... Soaking tube, 3...
...Heater, 3a...Split heater, 4...
... Insulation material, 5 ... Furnace enclosure, 6 ...
・・Soaking tube using SiC, 7・・・・Terminal, 8・
...Transformer, 9...Power supply, 10...
...Power controller, 11...Reaction tube using SiC, 12...Temperature automatic controller, 13...
Temperature detector.

Claims (1)

【特許請求の範囲】 1 通電によつて加熱されるシリコンカーバイト製管を
炉の主発熱体とし、その外側に金属製発熱体よりなる補
助ヒータを配置し、両発熱体にそれぞれ与える電力を加
減することによつて上記管内の温度を所要の高温度に維
持することを特徴とする高温拡散炉。 2 シリコンカーバイト製管の内部に熱処理物を収める
石英製炉心管を設けたことを特徴とする特許請求範囲第
1項記載の高温拡散炉。 3 シリコンカーバイト製管をその内部に熱処理物を収
めるように構成したことを特徴とする特許請求の範囲第
1項記載の高温拡散炉。
[Claims] 1. A silicon carbide tube that is heated by electricity is used as the main heating element of the furnace, and an auxiliary heater made of a metal heating element is arranged outside of the silicon carbide tube, and electric power is supplied to each of the two heating elements. A high-temperature diffusion furnace characterized in that the temperature inside the tube is maintained at a required high temperature by controlling the temperature. 2. The high-temperature diffusion furnace according to claim 1, characterized in that a quartz furnace core tube for storing a heat-treated material is provided inside a silicon carbide tube. 3. The high-temperature diffusion furnace according to claim 1, characterized in that the silicon carbide tube is configured to house a heat-treated material therein.
JP13406977A 1977-11-10 1977-11-10 High temperature diffusion furnace Expired JPS6041848B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13406977A JPS6041848B2 (en) 1977-11-10 1977-11-10 High temperature diffusion furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13406977A JPS6041848B2 (en) 1977-11-10 1977-11-10 High temperature diffusion furnace

Publications (2)

Publication Number Publication Date
JPS5467764A JPS5467764A (en) 1979-05-31
JPS6041848B2 true JPS6041848B2 (en) 1985-09-19

Family

ID=15119641

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13406977A Expired JPS6041848B2 (en) 1977-11-10 1977-11-10 High temperature diffusion furnace

Country Status (1)

Country Link
JP (1) JPS6041848B2 (en)

Also Published As

Publication number Publication date
JPS5467764A (en) 1979-05-31

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