JPS60109219A - Gas phase reactor - Google Patents
Gas phase reactorInfo
- Publication number
- JPS60109219A JPS60109219A JP58216166A JP21616683A JPS60109219A JP S60109219 A JPS60109219 A JP S60109219A JP 58216166 A JP58216166 A JP 58216166A JP 21616683 A JP21616683 A JP 21616683A JP S60109219 A JPS60109219 A JP S60109219A
- Authority
- JP
- Japan
- Prior art keywords
- holding jig
- wafers
- wafer holding
- wafer
- reaction
- 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
Links
Classifications
-
- H—ELECTRICITY
- H10—SEMICONDUCTOR DEVICES; ELECTRIC SOLID-STATE DEVICES NOT OTHERWISE PROVIDED FOR
- H10P—GENERIC PROCESSES OR APPARATUS FOR THE MANUFACTURE OR TREATMENT OF DEVICES COVERED BY CLASS H10
- H10P14/00—Formation of materials, e.g. in the shape of layers or pillars
- H10P14/20—Formation of materials, e.g. in the shape of layers or pillars of semiconductor materials
- H10P14/34—Deposited materials, e.g. layers
- H10P14/3402—Deposited materials, e.g. layers characterised by the chemical composition
- H10P14/3404—Deposited materials, e.g. layers characterised by the chemical composition being Group IVA materials
- H10P14/3408—Silicon carbide
-
- H—ELECTRICITY
- H10—SEMICONDUCTOR DEVICES; ELECTRIC SOLID-STATE DEVICES NOT OTHERWISE PROVIDED FOR
- H10P—GENERIC PROCESSES OR APPARATUS FOR THE MANUFACTURE OR TREATMENT OF DEVICES COVERED BY CLASS H10
- H10P14/00—Formation of materials, e.g. in the shape of layers or pillars
- H10P14/20—Formation of materials, e.g. in the shape of layers or pillars of semiconductor materials
- H10P14/24—Formation of materials, e.g. in the shape of layers or pillars of semiconductor materials using chemical vapour deposition [CVD]
-
- H—ELECTRICITY
- H10—SEMICONDUCTOR DEVICES; ELECTRIC SOLID-STATE DEVICES NOT OTHERWISE PROVIDED FOR
- H10P—GENERIC PROCESSES OR APPARATUS FOR THE MANUFACTURE OR TREATMENT OF DEVICES COVERED BY CLASS H10
- H10P14/00—Formation of materials, e.g. in the shape of layers or pillars
- H10P14/20—Formation of materials, e.g. in the shape of layers or pillars of semiconductor materials
- H10P14/34—Deposited materials, e.g. layers
- H10P14/3438—Doping during depositing
- H10P14/3441—Conductivity type
- H10P14/3442—N-type
-
- H—ELECTRICITY
- H10—SEMICONDUCTOR DEVICES; ELECTRIC SOLID-STATE DEVICES NOT OTHERWISE PROVIDED FOR
- H10P—GENERIC PROCESSES OR APPARATUS FOR THE MANUFACTURE OR TREATMENT OF DEVICES COVERED BY CLASS H10
- H10P14/00—Formation of materials, e.g. in the shape of layers or pillars
- H10P14/20—Formation of materials, e.g. in the shape of layers or pillars of semiconductor materials
- H10P14/34—Deposited materials, e.g. layers
- H10P14/3438—Doping during depositing
- H10P14/3441—Conductivity type
- H10P14/3444—P-type
Abstract
Description
【発明の詳細な説明】
本発明は半導体ウェーハおよびその他の部材表面上に薄
膜を形成する場合に用いて好適な気相反応技術に関する
ものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a gas phase reaction technique suitable for use in forming thin films on the surfaces of semiconductor wafers and other members.
半導体装置の製造工程に不可欠のCVD(Chemic
alVapore Deposition) 、エピタ
キシー、スパッター等の所謂気相反応技術では、従来、
多数枚の半導体ウェーハな一度に処理するバッチ式方式
が利用されている(特開昭53−142387号公報)
。CVD (Chemical CVD) is essential to the manufacturing process of semiconductor devices.
In so-called gas phase reaction techniques such as alVapore Deposition, epitaxy, and sputtering, conventionally,
A batch method is used to process a large number of semiconductor wafers at once (Japanese Unexamined Patent Publication No. 142387/1987).
.
そして、このパッチ式方式では、ウェーハの直径が76
■から100K、125fiと大口径化されるのに応じ
て装置を大型化し、処理ウェーハの枚数があまり減少さ
れないようにしてスループット(1時間当りの処理枚数
)の減少を防いできて(・る。しかし装置の主要部を構
成する石英ガラス與反応管やSiCコート・グラファイ
ト製サセプタ等の大型化が近年次第に限界に近づいてき
ており。In this patch method, the diameter of the wafer is 76 mm.
As the diameter has increased from (1) to 100K and 125fi, the equipment has been increased in size and the number of wafers processed has been kept from decreasing too much to prevent a decrease in throughput (number of wafers processed per hour). However, in recent years, the increasing size of the quartz glass reaction tube, SiC-coated graphite susceptor, etc. that constitute the main parts of the device has gradually approached its limits.
単に装置を大型化するだけでスループットの減少に対処
することは困難な状況になってきている。It has become difficult to cope with the decrease in throughput simply by increasing the size of the device.
特に−ウェーハの直径が175關以上に大口径化された
場合には反応管の口径を少し位大きくした程度では1バ
ツ≠内のウェーッ・のチャージ数の減少は避けられない
。また、このように反応管およびこれに伴なってサセプ
タ等の大型化を図ると、これらの分解、洗浄1組立て等
のメンテナンスが困難になり、しかも装置コストが増大
するという問題が生ずる。一方、石英管の長さを大きく
してチャージ数の減少i止ないし、増大を図奎ことも考
えられるが、単に長くするのみでは前述のようにメンテ
ナンス、コスト上あ問題がある上に、サセプタへのウェ
ーハの着脱作業が困難になりかつ反応管内の反応ガスの
均一性を確保することが困難になるという問題も生じる
。In particular, when the diameter of the wafer is increased to 175 mm or more, a decrease in the number of wafer charges within 1 x is unavoidable even if the diameter of the reaction tube is slightly increased. Furthermore, if the reaction tube and the susceptor are made larger in size, maintenance such as disassembly, cleaning, and reassembly of the tube becomes difficult, and the cost of the apparatus increases. On the other hand, it is possible to increase the number of charges by increasing the length of the quartz tube, but simply increasing the length of the quartz tube may cause maintenance and cost problems as described above, and the susceptor Problems also arise in that it becomes difficult to attach and detach wafers to and from the reactor, and it becomes difficult to ensure uniformity of the reaction gas within the reaction tube.
他方、ウェーハの大口径化に対処する別の方式としてウ
ェーッ・を1枚づつ処理する枚葉式装置が考えられる。On the other hand, as another method for dealing with the increase in the diameter of wafers, a single wafer type apparatus that processes wafers one by one may be considered.
しかし、枚葉式の場合には当然にスループットが減少し
、これな防ぐためには複数台の装置を設けて並列的に運
転させる必要があり。However, in the case of a single-wafer type, the throughput naturally decreases, and to prevent this, it is necessary to install multiple devices and operate them in parallel.
装置の占有面積の増加に伴なって面積効率(1平米当り
の処理枚数)が低下すると共に装置コストの増大を生ず
るという問題がある。As the area occupied by the apparatus increases, area efficiency (the number of sheets processed per square meter) decreases, and the cost of the apparatus increases.
本発明の目的は反応管の直径を大型化することなく大口
径ウェーハの多数枚処理を可能にし、メンテナンスの容
易化やコスlトの低減を図ることができる気相反応技術
を提供することにある。The purpose of the present invention is to provide a gas phase reaction technology that enables processing of a large number of large diameter wafers without increasing the diameter of the reaction tube, and that facilitates maintenance and reduces costs. be.
また本発明の他の目的はメンテナンスと共にウェーハの
着脱の容易化を図りかつ内部の反応ガスの均一化を実現
できる気相反応技術を提供するととKある。Another object of the present invention is to provide a gas phase reaction technique that facilitates maintenance, wafer attachment and detachment, and uniformity of internal reaction gas.
本発明の前記ならびにそのほかの目的と新規な特徴は、
本明細書の記述および添付図面からあきらかになるであ
ろう。The above and other objects and novel features of the present invention include:
It will become clear from the description of this specification and the accompanying drawings.
本願において開示される発明のうち代表的なものの概要
を簡単に説明すれば、下記のとおりである。A brief overview of typical inventions disclosed in this application is as follows.
すなわち、ウェーハ保持治具を内装する反応管を長さ方
向に分割形成して、各部を独立して長さ方向に移動でき
るように構成し、更に必要に応じて反応管の各部間にガ
スノズルを配設することにより1反応管を大口径化する
ことなくしかもメンテナンスの困難やコストの増大を生
ずることなくウェーハの処理効率を向上し、かつウェー
ッ・の着脱を容易忙しかつ均一なガス条件での良好な気
相′反応を達成するものである。In other words, the reaction tube containing the wafer holding jig is divided into parts in the length direction so that each part can be moved independently in the length direction, and gas nozzles are installed between each part of the reaction tube as necessary. This arrangement improves wafer processing efficiency without increasing the diameter of one reaction tube, making maintenance difficult or increasing costs, and makes it easy to attach and detach wafers in a busy and uniform gas condition. This achieves a good gas phase reaction.
第1図は本発明を縦型気相反応装置、所謂バレル型装置
に適用した実施例であり1石英ガラス製の円形の反応管
1’&上下方向に延設し、その中心位置にウェーハ保持
治具2を内装している。このウェーハ保持治具2はSI
Cコーテングのグラファイト製で、短冊形(矩形)の板
材を例えば6枚組合わせて6角柱状に形成し、その各表
面上に大口径ウェーハWを上下K例えば4枚づつ保持で
きるようにしている。前記ウェーハ保持治具2は上部中
心位置に設けたスリーブ3により基板4に懸吊支持され
る。スリーブ3は基板4に回転可能に軸支され、貫通し
た上端部には回転機構5を設けている。回転機構5は、
スリーブ3の上端に置局方向に等配した複数伜のマグネ
ットからなる内輪マグネット6と、その外側九同心配置
した環状ギヤ7に取殖された複数個の゛マグネットから
なる外輪マグネット8と、前記環状ギヤ7に噛合するビ
ニオンを軸転させるモータ9とを備え、モータ9を駆動
することにより環状ギヤ7と共に外輪マグネット8を回
転させ、磁力によりて更に内輪マグネット6、つまりス
リーブ3とウェーハ保持治具2を軸転させることができ
る。なお、ウェーハ保持治具2の中心位置には温度測定
センサを内装した保護管10を垂架している。Figure 1 shows an embodiment in which the present invention is applied to a vertical gas phase reactor, a so-called barrel-type reactor, in which a circular reaction tube 1' made of quartz glass is installed extending vertically, and a wafer is held at its center. A jig 2 is installed inside. This wafer holding jig 2 is SI
It is made of C-coated graphite and is formed by combining, for example, six strip-shaped (rectangular) plates to form a hexagonal column shape, so that it is possible to hold, for example, four large diameter wafers W on the top and bottom K on each surface of the hexagonal column. . The wafer holding jig 2 is suspended and supported on the substrate 4 by a sleeve 3 provided at the upper center position. The sleeve 3 is rotatably supported by a base plate 4, and a rotating mechanism 5 is provided at the upper end thereof. The rotation mechanism 5 is
An inner ring magnet 6 consisting of a plurality of magnets equally arranged in the positioning direction on the upper end of the sleeve 3, an outer ring magnet 8 consisting of a plurality of magnets attached to an annular gear 7 arranged nine concentrically on the outside thereof; It is equipped with a motor 9 that rotates a pinion that meshes with the annular gear 7. By driving the motor 9, the outer ring magnet 8 is rotated together with the annular gear 7, and the inner ring magnet 6, that is, the sleeve 3, and the wafer holding jig are further rotated by magnetic force. The tool 2 can be rotated. Note that a protection tube 10 having a temperature measurement sensor installed therein is suspended vertically at the center of the wafer holding jig 2.
一方1石英管1は長さ方向(上下方向)lc2分された
上管11と下管12とで構成している。土管11は円筒
状、下管12は下端を絞った円筒状として形成し、両管
11,12はスペースリング13”k介して長さ方向に
直列配置すると共に、上管11上縁に配したスペースリ
ング14により前記基板4の下面に接続している。前記
スペースリング13.14は夫々両端面にシールリング
を有し1両管11.12や上管11と基板4間を気密に
保っている。そして、上側のスペースリング14には主
反応ガスノズル15を設け、下側のスペースリング13
には補充ガスノズル16を設けている。更に前記上管1
1.上管12には夫々周囲に赤外線ランプからなる加熱
源17.18を一体的に設げ、石英管1内部を輻射加熱
するよう処している。なお、上管12の下端は排気口と
され、また前記基板4と上管11は図外のソフト機構に
よって夫々独立して上下動できるよう罠なっている。On the other hand, one quartz tube 1 is composed of an upper tube 11 and a lower tube 12, which are divided into two parts lc in the length direction (vertical direction). The clay pipe 11 was formed into a cylindrical shape, and the lower pipe 12 was formed into a cylindrical shape with a narrowed lower end, and both pipes 11 and 12 were arranged in series in the length direction via a space ring 13''k, and were arranged at the upper edge of the upper pipe 11. It is connected to the lower surface of the substrate 4 by a space ring 14.The space rings 13, 14 each have a seal ring on both end surfaces to keep the space between the two tubes 11, 12 or the upper tube 11 and the substrate 4 airtight. The upper space ring 14 is provided with a main reaction gas nozzle 15, and the lower space ring 13 is provided with a main reaction gas nozzle 15.
A replenishment gas nozzle 16 is provided. Furthermore, the upper pipe 1
1. Heat sources 17 and 18 consisting of infrared lamps are integrally provided around the upper tube 12, respectively, so that the inside of the quartz tube 1 is heated by radiation. The lower end of the upper tube 12 is used as an exhaust port, and the substrate 4 and the upper tube 11 are configured to be able to move up and down independently by means of a software mechanism (not shown).
以上の構成の気相反応装置を用いて、シリコンウェーハ
のエピタキシャル成長を行なう場合の操作を説明する。The operation for epitaxial growth of a silicon wafer using the gas phase reaction apparatus having the above configuration will be explained.
先ず、第2図に示すように、回転機構5を設けた基板4
を図外のソフト機構によって上動させ、これと共にウェ
ーハ保持治具2を一体にその上部約半分が露出されるま
で上動させる。そして、この状態でウェーハ保持治具2
の上半分表面に大口径のウェーハWを全チャージ数の半
数だけロードする。First, as shown in FIG. 2, the substrate 4 provided with the rotation mechanism 5 is
is moved upward by a software mechanism (not shown), and together with this, the wafer holding jig 2 is moved upward until about half of its upper portion is exposed. In this state, the wafer holding jig 2
Large-diameter wafers W are loaded onto the upper half surface of the wafer W by half of the total number of charges.
次に、図外のソフト機構により上管11を加熱源17と
共に第3図のように上動させ、露出したウェーハ保持治
具2の下半分の表面に残りの半数のウェーハWをロード
する。これ忙より全てのウェーハのロードが完了され、
その後上管11および基板4と一体のウェーハ保持治具
2等を下動させ、第1図に示す状態に設定する。Next, the upper tube 11 and the heat source 17 are moved upward as shown in FIG. 3 by a software mechanism (not shown), and the remaining half of the wafers W are loaded onto the exposed lower half surface of the wafer holding jig 2. All wafers have been loaded completely during this busy period.
Thereafter, the upper tube 11 and the wafer holding jig 2 integrated with the substrate 4 are moved down to set the state shown in FIG.
その後、ウェーハ保持治具2を回転させ、主反応ガスノ
ズル15および必要圧応じて補充ガスノズル16更に回
転機構5部内に設けた図外のパーシロからN、ガスを反
応管1内に供給して管内の空気をパージし1次にH,ガ
スでNtガスをパージして反応管1内の空気を完全にH
7で置換する。Thereafter, the wafer holding jig 2 is rotated, and N gas is supplied into the reaction tube 1 from the main reaction gas nozzle 15 and, depending on the required pressure, the supplementary gas nozzle 16, and from a persilo (not shown) provided in the rotation mechanism 5. Purge the air and then purge the Nt gas with H and gas to completely make the air in the reaction tube 1 H.
Replace with 7.
このとき、反応管1内を図外の真空ポンプで排気してガ
ス置換をし、管内を低圧Hz(50〜80rorr )
の状態に保持してもよい。At this time, the inside of the reaction tube 1 is evacuated using a vacuum pump (not shown) to replace the gas, and the inside of the tube is kept at a low pressure of Hz (50 to 80 rorr).
It may be kept in this state.
次に、加熱源17.18によりウェーハWを900〜1
150CK輻射加熱し、反応ガス(SiH4tSiHt
C4、SiC,6,等)とドーピングガス(PHI I
B、H・等)と’&H,ガスと共に反応管1内に流し、
ウェーハW上にStをエピタキシャル成長させる。Next, the wafer W is heated to 900 to 1
150CK radiation heating, reactant gas (SiH4tSiHt
C4, SiC, 6, etc.) and doping gas (PHI I
B, H, etc.) and '&H, flowed into the reaction tube 1 together with the gas,
St is epitaxially grown on the wafer W.
この際、H,ガス、反応ガスおよびドーピングガスは通
常主反応ガスノズル15より反応管1内に導入する。但
し、ウェーハ保持治具2の下部にロードしたウェーハW
上のエピタキシャル膜の膜質および抵抗率均一性制御の
ため、必要に応じ補充ガスノズル16よりH,ガスと共
忙反応ガスおよびドーピングガスな一諸にまたは単独に
導入することができる。At this time, H, gas, reaction gas, and doping gas are usually introduced into the reaction tube 1 through the main reaction gas nozzle 15. However, the wafer W loaded at the bottom of the wafer holding jig 2
In order to control the film quality and resistivity uniformity of the above epitaxial film, H, gas, co-active reaction gas, and doping gas can be introduced together or singly from the supplementary gas nozzle 16 as needed.
気相反応終了後のウェーハの取り出しは、ウェーハロー
ドのときの操作を逆に行なえばよい。即ち、加熱停止後
所定温度までH1ガス中で冷却し。To take out the wafer after the gas phase reaction is completed, the operation for loading the wafer may be performed in reverse. That is, after heating is stopped, it is cooled in H1 gas to a predetermined temperature.
低圧反応のときには常圧に戻し、■、をN、ガス圧置換
する。そして、ウェーハ保持治具2と上管11とを上動
して第3図の状態で下半分のウェーハWをアンロードし
、次に上管11を下動して第2図の状態で上半分のウェ
ーハWをアンロードすればよい。なお、この状態で直ち
に次のウェーハをロードできる。In the case of a low-pressure reaction, the pressure is returned to normal pressure, and ① is replaced with N gas pressure. Then, the wafer holding jig 2 and the upper tube 11 are moved upward to unload the lower half of the wafers W in the state shown in FIG. It is sufficient to unload half of the wafers W. Note that in this state, the next wafer can be loaded immediately.
したがって、以上の構成および操作説明から判るように
1反応管1は上管11と上管12とで分割形成している
ため、反応管1を長い寸法とした場合にもその半分の長
さの取扱いでよく1分解。Therefore, as can be seen from the above configuration and operation explanation, one reaction tube 1 is divided into an upper tube 11 and an upper tube 12, so even if the reaction tube 1 is made long, it will be half the length. It often disassembles after handling.
洗浄1組立て等のメンテナンスを容易なものにできる。Maintenance such as cleaning and assembly can be made easier.
また、ウェーハWのロード、アンロードに際してもウェ
ーハ保持治具2を反応管1の半分の長さ上動させるだけ
でよく、ロード、アンロードを容易なものにする。更に
反応管1の中間に補充ガスノズル16’&設けているの
で反応管内のガスの均一化を図り、均一厚のエピタキシ
ャル層を形成できる。Further, when loading and unloading the wafer W, it is only necessary to move the wafer holding jig 2 upward by half the length of the reaction tube 1, making loading and unloading easy. Further, since a supplementary gas nozzle 16' is provided in the middle of the reaction tube 1, the gas inside the reaction tube can be made uniform, and an epitaxial layer with a uniform thickness can be formed.
第4図は本発明の変形例であり、第1図と同一部分には
同一符号を付して説明は省略する。本例では、反応管l
の分割に対応してウェーハ保持治具2Aを上、下2段構
成とし、上段19と下lR2Oとを連結スリーブ21で
連結している。これら、上段19と下段20とは連結ス
リーブ21部分において分離可能であり、メンテナンス
時に分離すればその取扱いが容易になる。この装置にお
いても前述の例と全く同様の気相反応を行なうことがで
きる。FIG. 4 shows a modification of the present invention, and the same parts as those in FIG. 1 are given the same reference numerals and their explanation will be omitted. In this example, the reaction tube l
The wafer holding jig 2A has an upper and a lower two-stage configuration corresponding to the division, and the upper stage 19 and the lower lR2O are connected by a connecting sleeve 21. These upper stage 19 and lower stage 20 can be separated at the connection sleeve 21 portion, and if they are separated during maintenance, handling becomes easier. In this apparatus as well, the same gas phase reaction as in the above-mentioned example can be carried out.
(1)反応管を長さ方向に分割形成し、各部χ独立して
移動できるようにしているので、反応管の長さを大きく
して大口径ウェーッ・のチャージ数の増大を図った場合
にも1反応管を各部に分割して洗浄しかつ再組立てを行
なうことができ、メンテナンスを容易なものにできる。(1) The reaction tube is divided into sections in the length direction so that each part can move independently, so when the length of the reaction tube is increased to increase the number of charges for large-diameter wafers. Also, one reaction tube can be divided into various parts, cleaned, and reassembled, making maintenance easier.
(2)反応管な分割したことによりウェーハ保持治具の
移動量を小さくしても全ウェーハのロード。(2) By dividing the reaction tube, all wafers can be loaded even if the amount of movement of the wafer holding jig is reduced.
アンロードが可能であり、ロード、アンロード操作を極
めて容易なものにできる。It can be unloaded, making loading and unloading operations extremely easy.
(3)反応管の長さを大きくしてウェーッ・のチャージ
数を増大しているので1反応管を大口径に形成する必要
はなく、大口径ウェーハの多数枚のバッチ処理を可能に
してスループットの向上を達成できる。(3) Since the length of the reaction tube is increased to increase the number of wafers charged, there is no need to form one reaction tube with a large diameter, making it possible to batch process a large number of large diameter wafers, increasing throughput. can achieve improvements in
(4) 補充ガスノズルを分割反応管の中間に設けて。(4) Install a supplementary gas nozzle in the middle of the divided reaction tubes.
反応ガスとドーピングガスとを一諸に又は単独に導入で
き、しかも反応中にウェーハ保持治具を回転することが
できるので、気相成長層の膜厚や抵抗率の均一性を良好
なものKできる。Since the reaction gas and doping gas can be introduced together or individually, and the wafer holding jig can be rotated during the reaction, the uniformity of the film thickness and resistivity of the vapor-phase grown layer can be improved. can.
以上本発明者によってなされた発明を実施例にもとづき
具体的に説明したが、本発明は上記実施例に限定される
ものではなく、その要旨を逸脱しない範囲で種々変更可
能であることはいうまでもない。たとえば、反応管の分
割数は3個以上に設定してもよく、ウェーハ保持治具も
これに合わせて多数段に形感してもよい。更に、これに
応じて補充ガスノズル数を増加してもよい。また、本実
施例ではウェーハ保持治具はウェーハを垂直方向に保持
するように設けて゛いるが、ウェーハを水平方向に保持
できるような構成にしても良い。Although the invention made by the present inventor has been specifically explained above based on Examples, it goes without saying that the present invention is not limited to the above Examples and can be modified in various ways without departing from the gist thereof. Nor. For example, the number of divisions of the reaction tube may be set to three or more, and the wafer holding jig may also be arranged in multiple stages accordingly. Furthermore, the number of supplementary gas nozzles may be increased accordingly. Further, in this embodiment, the wafer holding jig is provided to hold the wafer vertically, but it may be configured to hold the wafer horizontally.
以上の説明では主として本発明者によってなされた発明
をその背景となった利用分野であるバレル型の気相反応
装置に適用した場合について説明したが、それに限定さ
れるものではなく、横型の反応管構造の装置にも適用で
きる。In the above explanation, the invention made by the present inventor was mainly applied to a barrel-type gas phase reactor, which is the background field of application, but the invention is not limited thereto. It can also be applied to structural devices.
第1図は本発明の一実施例装置の断面図。
第2図および第3図は操作を説明するための破断圧面図
、
第4図は変形例の断面図である。
1・・・反応管、2・・・ウェーハ保持治具、4・・・
基板。
5・・・回転機構、11・・・上管、12・・・上管、
13゜14・・・xヘースy yy、15・・・主反応
ガスノズル、16・・・補充ガスノズル、17.18・
・・加熱源、19・・・上段、20・・・下段、W・・
・ウェーハ。
第 1 図
第 2 図
第 3′ 図FIG. 1 is a sectional view of an apparatus according to an embodiment of the present invention. 2 and 3 are fracture pressure surface views for explaining the operation, and FIG. 4 is a sectional view of a modified example. 1... Reaction tube, 2... Wafer holding jig, 4...
substrate. 5... Rotation mechanism, 11... Upper tube, 12... Upper tube,
13゜14...x Hose y yy, 15... Main reaction gas nozzle, 16... Replenishment gas nozzle, 17.18.
...Heating source, 19...Upper stage, 20...Lower stage, W...
・Wafer. Figure 1 Figure 2 Figure 3'
Claims (1)
ハ保持治具にウェーハを保持しかつ前記反応管内を所定
のガス雰囲気に保って気相反応を行なう装置であって、
前記反応管はその長さ方向に複数個に分割形成したこと
を特徴とする気相反応装置。 2、 ウェーハ保持治具と分割した反応管とは独立して
長さ方向に移動できるよう構成してなる特許請求の範囲
第1項記載の気相反応装置。 3、分割した反応管の間に補充ガスノズルを設けてなる
特許請求の範囲第1項又は第2項記載の気相反応装置。 4、 ウェーハ保持治具を長さ方向に多段に分割してな
る特許請求の範囲第1項ないし第3項のいずれかに記載
の気相反応装置。[Scope of Claims] 1. An apparatus that includes a wafer holding jig inside a reaction tube, holds a wafer in the wafer holding jig, and performs a gas phase reaction by maintaining a predetermined gas atmosphere inside the reaction tube. ,
A gas phase reactor characterized in that the reaction tube is divided into a plurality of pieces in the length direction thereof. 2. The gas phase reaction apparatus according to claim 1, wherein the wafer holding jig and the divided reaction tubes are configured to be able to move independently in the length direction. 3. The gas phase reactor according to claim 1 or 2, wherein a supplementary gas nozzle is provided between the divided reaction tubes. 4. The gas phase reaction apparatus according to any one of claims 1 to 3, wherein the wafer holding jig is divided into multiple stages in the length direction.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58216166A JPS60109219A (en) | 1983-11-18 | 1983-11-18 | Gas phase reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58216166A JPS60109219A (en) | 1983-11-18 | 1983-11-18 | Gas phase reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS60109219A true JPS60109219A (en) | 1985-06-14 |
Family
ID=16684317
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58216166A Pending JPS60109219A (en) | 1983-11-18 | 1983-11-18 | Gas phase reactor |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60109219A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62245623A (en) * | 1986-04-18 | 1987-10-26 | Hitachi Ltd | heat treatment equipment |
-
1983
- 1983-11-18 JP JP58216166A patent/JPS60109219A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62245623A (en) * | 1986-04-18 | 1987-10-26 | Hitachi Ltd | heat treatment equipment |
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