JPS6152231B2 - - Google Patents
Info
- Publication number
- JPS6152231B2 JPS6152231B2 JP12556383A JP12556383A JPS6152231B2 JP S6152231 B2 JPS6152231 B2 JP S6152231B2 JP 12556383 A JP12556383 A JP 12556383A JP 12556383 A JP12556383 A JP 12556383A JP S6152231 B2 JPS6152231 B2 JP S6152231B2
- Authority
- JP
- Japan
- Prior art keywords
- film
- reaction chamber
- quartz window
- reaction
- chamber
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 239000010408 film Substances 0.000 claims description 76
- 239000010453 quartz Substances 0.000 claims description 35
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 35
- 238000006243 chemical reaction Methods 0.000 claims description 30
- 239000007789 gas Substances 0.000 claims description 17
- 239000012495 reaction gas Substances 0.000 claims description 16
- 239000000758 substrate Substances 0.000 claims description 12
- 239000010409 thin film Substances 0.000 claims description 12
- 238000010926 purge Methods 0.000 claims description 11
- 235000012431 wafers Nutrition 0.000 claims description 11
- 238000002834 transmittance Methods 0.000 claims description 8
- 238000004519 manufacturing process Methods 0.000 claims description 7
- 238000004804 winding Methods 0.000 claims description 4
- 229920011301 perfluoro alkoxyl alkane Polymers 0.000 description 25
- 238000005229 chemical vapour deposition Methods 0.000 description 10
- 239000007795 chemical reaction product Substances 0.000 description 9
- 238000010586 diagram Methods 0.000 description 7
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 6
- 229910052753 mercury Inorganic materials 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 5
- 238000003860 storage Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 230000003287 optical effect Effects 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000000295 emission spectrum Methods 0.000 description 2
- 229910052731 fluorine Inorganic materials 0.000 description 2
- 239000011737 fluorine Substances 0.000 description 2
- 238000010574 gas phase reaction Methods 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 229910021420 polycrystalline silicon Inorganic materials 0.000 description 2
- 229920005591 polysilicon Polymers 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 239000004809 Teflon Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229920013653 perfluoroalkoxyethylene Polymers 0.000 description 1
- 238000005268 plasma chemical vapour deposition Methods 0.000 description 1
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 1
- 239000004810 polytetrafluoroethylene Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000002250 progressing effect Effects 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
- BFKJFAAPBSQJPD-UHFFFAOYSA-N tetrafluoroethene Chemical group FC(F)=C(F)F BFKJFAAPBSQJPD-UHFFFAOYSA-N 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/44—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
- C23C16/48—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating by irradiation, e.g. photolysis, radiolysis, particle radiation
- C23C16/482—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating by irradiation, e.g. photolysis, radiolysis, particle radiation using incoherent light, UV to IR, e.g. lamps
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/44—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
- C23C16/48—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating by irradiation, e.g. photolysis, radiolysis, particle radiation
- C23C16/488—Protection of windows for introduction of radiation into the coating chamber
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Toxicology (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Chemical Vapour Deposition (AREA)
Description
半導体のデバイスプロセス技術は、常に進歩し
ているが特に薄膜生成の技術は生成温度の低温化
を指向している。低温化の手段としてプラズマ
CVD(化学的気相成長)膜生成技術がすでに知
られているが、最近光CVD膜の生成技術が注目
されている。本発明は光CVD装置の薄膜生成反
応炉の改良に関するものである。
まず光CVD法について説明する。光CVD法は
反応ガスが光エネルギで反応し、生成温度を低温
化できるのみならず、プラズマCVD法における
イオンや電子などの高いエネルギ粒子が存在しな
いので、生長膜へのイオンなどによる損傷が少な
く、また光の照射強度を均一にすることが容易な
ため、生長膜の膜厚の均一が容易で、かつ大口径
ウエハの処理が容易という特長があり、ステツプ
カバリージも良いこと、(基板上の薄膜のパター
ンに生ずる段差のくぼみが少ないこと)から、今
後のCVD膜生成技術の重要な部門として期待さ
れている。
光CVD法の反応式は次式で表わされる。
hν+Hgは光エネルギとして水銀ランプによ
る紫外線のエネルギを利用し、かつ触媒的にHg
(ガス)を使用することを意味し、100〜200℃は
ウエハ上の薄膜の生成温度を表わしている。上記
いずれの反応においても、目下は第1図に示され
る発光スペクトラムを有する低圧水銀灯を光源と
しているものが多い。
第2図は従来の光CVD反応炉の代表的な一例
の構造概要図である。図中の1は紫外線をよく通
すための石英窓板で、これより上部が光源室、こ
れより下部が反応室をそれぞれ形成している。2
は紫外線用水銀ランプユニツト、3は反射板、4
はウエハ(基板)群でサセプタ5上に載せてあ
る。6は赤外線ランプユニツト、7は熱電対、8
は補助ヒータ、9は反応室内へのガス入口、10
は真空ポンプへの排気口である。この反応炉では
基板4を赤外線ランプユニツト6にて加熱する
(補助ヒータ8は基板に直接赤外光が照射される
ことを防ぎ、基板の温度分布を良好にする補助板
である)と共に、基板上に生成する薄膜によつて
定まる材料の反応ガスをガス入口9から反応炉内
に流通させ、他方水銀ランプユニツト2より石英
窓板1を透過して来る紫外線のエネルギをとり入
れて、基板上に低温にて薄膜を生成させるもので
ある。しかしこのような構造の炉では石英板1の
入射窓面(反応室側の面、図では下面)に生成膜
が次第に付着し、照射光量が減少するという欠点
がある。この現象はポリ(Poly)シリコン膜の場
合、生成膜が300Å以上になると極端に生成速度
が低下するという報告があるが、現状ではこの問
題を解決する装置は未だ見出されない。本発明は
この問題を解決するために行つたもので、以下詳
細に説明する。
第3図は本発明を実施した光CVD反応炉の構
造概要図である。図中の記号1,2,4,5,6
は第1図に共通であるが、炉の構造、従つて配置
は異なつている。すなわち1は無水石英の窓
(板)で、紫外線などの光エネルギを反応室12
内に高い透過率で透過させる。反応室上部はこの
石英窓1とOリングにより外気と遮断されて真空
シールされている。石英窓1には紫外線の透過率
が優れた無水の石英材を使用する。2はウエハ4
の表面近傍に紫外線の光エネルギを供給する水銀
ランプユニツト、4はウエハ(基板)でこの表面
に気相反応による薄膜が形成される。5はウエハ
(主にシリコン)を間接加熱するサセプタで、
SiCを被覆したカーボン材が用いられる。6はサ
セプタ5を加熱する赤外線ランプユニツトで、ラ
ンプにはハロゲンランプが通常用いられ、またラ
ンプ光を前面に照射させるためリフレクタが付属
している。このランプユニツトは反応室外に設け
てランプの交換を容易にすると共に、上下左右の
移動機構が設けてある。11は赤外線の光エネル
ギを気相反応が行われる反応室12内のサセプタ
5に透過させる第2の石英窓(板)で、反応室下
部はこの石英窓とOリングによつて外気と遮断さ
れている。13はPFAフイルムで、反応生成物
および反応ガスを石英窓1に付着させないよう
に、反応室12内を石英窓1側と反応室12側に
空間分離する役目を持つている。PFAフイルム
は後にさらに説明するが、耐熱性があり紫外線の
透過率の良いフイルムである。14はPFAフイ
ルムのロール、15はロール14に回転運動を与
えるためのフイルムローラ、16は補助ローラ
で、PFAフイルム13の巻取りおよび供給を円
滑に行うためのものである。17はフイルム供給
室20aおよびフイルム収納室20bのチヤン
バ、18はガスパージポートで、反応生成物およ
び反応ガスが石英窓1に回わりこむのを防止す
る。この部分は第4図のパージガスおよび反応ガ
スの流れ図に詳細に示してある。第4図中に示し
た19aは上ガイド、19bは下ガイド22は反
応ガス、23はパージガス、24は排気である。
第3図に戻つて20aはフイルム供給室で補助ロ
ーラ16、フイルムローラ15、PFAフイルム
ロール14を収納する。20bはフイルム収納室
で補助ローラ16、フイルムローラ15PFAフ
イルムロール14を収納する。21は水冷ジヤケ
ツトで、反応室12内のOリングの過熱防止、フ
イルムおよびフイルム供給室20a、フイルム収
納室20bの過熱防止を行う。
さて第3図の本発明の反応炉の特長は、前記従
来の問題点を解決するため水銀ランプの光を透過
する石英窓1の直下に設けた使用耐熱温度が高く
かつ紫外線の透過率の良いPFAフイルムを介し
て反応室12と石英窓1の間にガスパージ室(ガ
スパージポート18を含む中間排気が可能となつ
ている)を設けて、第4図に示すようにガスの出
入を行い、石英窓1に反応生成物が付着しないよ
うに構成して、反応生成物はPFAフイルムにの
み付着するようにし、反応生成物が付着したフイ
ルムは任意時間に自動的に巻取つて、常に新しい
フイルムを反応室内に供給し、ランプユニツト2
よりの入射光量の低下を防いでいることにある。
第5図は無水石英板の光の波長に対する透過率
特性を厚さ1.5mm、10mm、30mmの石英板について
示したもので、厚さによる相違は小さい。第6図
はPFAフイルムの光の波長に対する透過率特性
で、フイルムの厚さはAが70μ、Bが90μの場合
である。PFAフイルムは4フツ化エチレンとパ
ーフロロアルコキシエチレンとの共重合体からな
るフツ素フイルムで、従来からあるPTFE(通称
テフロン)を特に熱可塑性を強化したものと考え
られる。わが国においては市販品としてトヨフロ
ンPFAフイルム(商品名)などがある。このフ
イルムは高温時の機械的強度はフツ素フイルム中
最高、化学的にも安定でほとんどすべての化学薬
品や溶剤、油脂に侵されない。またその性質は次
表のようである。
一般にPFAフイルムのような合成樹脂性のフ
イルムでは、紫外線を照射した場合フイルム自身
が発熱固化する性質があるが、本発明構造の反応
炉ではこのような性質は致命的な欠陥をもたらす
Semiconductor device process technology is constantly progressing, and thin film production technology in particular is oriented towards lowering the production temperature. Plasma as a means of lowering the temperature
CVD (chemical vapor deposition) film production technology is already known, but photo-CVD film production technology has recently been attracting attention. The present invention relates to an improvement of a thin film producing reactor for a photo-CVD apparatus. First, the optical CVD method will be explained. In the photo-CVD method, the reaction gas reacts with light energy, and not only can the generation temperature be lowered, but also there is no high-energy particles such as ions and electrons in the plasma CVD method, so there is less damage to the grown film by ions. In addition, since it is easy to make the irradiation intensity of light uniform, it is easy to make the thickness of the grown film uniform, and it is also easy to process large diameter wafers. It is expected to become an important branch of CVD film production technology in the future because of the small number of step depressions that occur in the thin film pattern. The reaction formula of the photoCVD method is expressed by the following formula. hν+Hg uses ultraviolet energy from a mercury lamp as light energy and catalytically generates Hg.
(gas) is used, and 100 to 200°C represents the temperature at which a thin film is formed on a wafer. In any of the above reactions, a low-pressure mercury lamp having the emission spectrum shown in FIG. 1 is currently used as the light source in many cases. FIG. 2 is a schematic structural diagram of a typical example of a conventional photo-CVD reactor. Reference numeral 1 in the figure is a quartz window plate that allows ultraviolet rays to pass through.The upper part forms the light source chamber, and the lower part forms the reaction chamber. 2
is a mercury lamp unit for ultraviolet light, 3 is a reflector, 4 is
is a group of wafers (substrates) placed on the susceptor 5. 6 is an infrared lamp unit, 7 is a thermocouple, 8
is an auxiliary heater, 9 is a gas inlet into the reaction chamber, 10 is
is the exhaust port to the vacuum pump. In this reactor, the substrate 4 is heated by an infrared lamp unit 6 (the auxiliary heater 8 is an auxiliary plate that prevents the substrate from being directly irradiated with infrared light and improves the temperature distribution of the substrate). A reaction gas of a material determined by the thin film formed on the substrate is passed into the reactor from the gas inlet 9, and the energy of ultraviolet light transmitted through the quartz window plate 1 is taken in from the mercury lamp unit 2 to be applied onto the substrate. It produces a thin film at low temperatures. However, a furnace having such a structure has the drawback that a produced film gradually adheres to the entrance window surface (the surface facing the reaction chamber, the bottom surface in the figure) of the quartz plate 1, and the amount of irradiated light decreases. It has been reported that this phenomenon occurs in the case of polysilicon films, and that the formation rate drops dramatically when the formed film exceeds 300 Å, but at present no device has been found that can solve this problem. The present invention was made to solve this problem, and will be described in detail below. FIG. 3 is a schematic structural diagram of a photo-CVD reactor in which the present invention is implemented. Symbols 1, 2, 4, 5, 6 in the diagram
are common to FIG. 1, but the structure and therefore the arrangement of the furnaces are different. In other words, 1 is a window (plate) made of anhydrous quartz, which transmits light energy such as ultraviolet rays into the reaction chamber 12.
Transmits light into the interior with high transmittance. The upper part of the reaction chamber is isolated from the outside air and vacuum-sealed by the quartz window 1 and the O-ring. For the quartz window 1, an anhydrous quartz material with excellent ultraviolet transmittance is used. 2 is wafer 4
A mercury lamp unit supplies ultraviolet light energy near the surface of the wafer, and 4 is a wafer (substrate) on which a thin film is formed by gas phase reaction. 5 is a susceptor that indirectly heats the wafer (mainly silicon);
A carbon material coated with SiC is used. Reference numeral 6 denotes an infrared lamp unit for heating the susceptor 5. A halogen lamp is usually used as the lamp, and a reflector is attached to irradiate the front surface with lamp light. This lamp unit is installed outside the reaction chamber to facilitate lamp replacement, and is also provided with a mechanism for moving it vertically and horizontally. Reference numeral 11 denotes a second quartz window (plate) that transmits infrared light energy to the susceptor 5 in the reaction chamber 12 where a gas phase reaction is carried out, and the lower part of the reaction chamber is isolated from the outside air by this quartz window and the O-ring. ing. Reference numeral 13 denotes a PFA film, which serves to spatially separate the interior of the reaction chamber 12 into the quartz window 1 side and the reaction chamber 12 side so as to prevent reaction products and reaction gas from adhering to the quartz window 1. As will be explained further later, PFA film is heat resistant and has good UV transmittance. 14 is a roll of PFA film, 15 is a film roller for imparting rotational motion to the roll 14, and 16 is an auxiliary roller for smoothly winding and feeding the PFA film 13. 17 is a chamber for the film supply chamber 20a and the film storage chamber 20b, and 18 is a gas purge port, which prevents reaction products and reaction gas from entering the quartz window 1. This section is shown in detail in the purge gas and reaction gas flow chart of FIG. 4, 19a is an upper guide, 19b is a lower guide 22 for reaction gas, 23 is a purge gas, and 24 is an exhaust gas.
Returning to FIG. 3, 20a is a film supply chamber in which an auxiliary roller 16, a film roller 15, and a PFA film roll 14 are stored. A film storage chamber 20b stores an auxiliary roller 16, a film roller 15, and a PFA film roll 14. A water-cooled jacket 21 serves to prevent overheating of the O-ring in the reaction chamber 12, the film, the film supply chamber 20a, and the film storage chamber 20b. Now, the feature of the reactor of the present invention shown in FIG. 3 is that, in order to solve the above-mentioned conventional problems, it has a high usable heat resistance temperature and has a good transmittance of ultraviolet rays. A gas purge chamber (which allows intermediate exhaust including a gas purge port 18) is provided between the reaction chamber 12 and the quartz window 1 via a PFA film to allow gas to enter and exit the quartz window as shown in FIG. Window 1 is configured to prevent reaction products from adhering to the PFA film, and the film with reaction products adhering to it is automatically wound up at any time to ensure that a new film is always replaced. Supplied into the reaction chamber, lamp unit 2
This is because it prevents the amount of incident light from decreasing further. FIG. 5 shows the transmittance characteristics of anhydrous quartz plates with respect to the wavelength of light for quartz plates with thicknesses of 1.5 mm, 10 mm, and 30 mm, and the differences depending on the thickness are small. Figure 6 shows the transmittance characteristics of a PFA film with respect to the wavelength of light, when the film thicknesses are A: 70μ and B: 90μ. PFA film is a fluorine film made of a copolymer of tetrafluoroethylene and perfluoroalkoxyethylene, and is considered to be a thermoplastic version of the conventional PTFE (commonly known as Teflon). In Japan, commercially available products include Toyoflon PFA Film (trade name). This film has the highest mechanical strength among fluorine films at high temperatures, and is chemically stable and is not attacked by almost all chemicals, solvents, and oils. Its properties are shown in the table below. Generally, synthetic resin films such as PFA films have the property of generating heat and solidifying themselves when irradiated with ultraviolet rays, but in the reactor with the structure of the present invention, this property causes a fatal defect.
【表】
ので、PFAフイルムについて紫外線照射テスト
を行つた。室温でのテストの結果、フイルムの温
度は40℃以下であつて固化は全く見られず、実用
に十分耐えることが実証された。
次に第4図によつて本発明反応炉の一部構造に
ついて更に説明を加える。石英窓1の下面に反応
生成物が付着することをできるだけ少なくするた
め、反応室部12と石英窓1の間は紫外線の入射
路以外はPFAフイルムガイド19a,19b
(第4図の斜線を施した部分)で仕切られてい
る。さらに石英窓1には反応ガスが回りこまない
ように石英窓1側のフランジには内周、外周に1
個ずつの溝が設けてあり、この溝の内周側からガ
スパージ18をし、外周側より排気24をするこ
とによつて、反応ガスが石英窓1に流れこむのを
防止するようになつている。しかも石英窓1側の
圧力を反応室12の圧力より少しでも高くしてお
けば、このガスパージ方式の反応ガスパージ効果
はより高くなるので、反応ガスが石英窓1に到達
する確率は極めて小さい。従つて石英窓1の面へ
の反応生成物の付着はほとんど起らない。
またCVD膜生成中にはPFAフイルムに反応生
成物が付着し、紫外線の照射光量が減少し生成速
度の低下が見られるが、フイルム上に一定膜厚の
反応生成物が付着した時には、フイルム13を第
3図右端のフイルム収納室20bのロール14に
巻取り、フイルム供給室20aのロールから新し
いフイルムを供給すれば、再び紫外線の照射光量
が復活し生成速度が増大する。そしてこのような
動作を繰返すことにより、所望の膜厚(通常5000
Å〜10000Å)のCVD膜を得ることができる。
次にフイルムの交換を容易にする構造が望まし
いことは言うまでもない。そのためPFAフイル
ムガイド(第4図斜線部分)は19a,19bの
上、下ガイドに分離できる構造とし、フイルムを
交換するには上ガイド19aが固定されているフ
ランジおよび各ロール室17の上フランジを開け
ば簡単に行われるようになつている。
またロール室17は反応室12との間で中間排
気されているため、反応ガスの流入はほとんどな
い。従つて反応ガスによる汚れの問題は生じな
い。他方このロール室には駆動部があるため微量
の微粉末発生の危険性は多少あるが、排気24で
中間排気が行われているため、この微粉末が反応
室12に入りこむことはほとんどない。
最後にPFAフイルムの冷却について説明す
る。PFAフイルムは前記の表に示したように、
使用限界温度は高温側260℃であつて、できるだ
け低温とすることが望ましい。このため反応室側
面および下ガイド19bの下面は水冷されてい
る。
なおPFAフイルムはたとえば厚さ25、50、
75、100、125(各μm)の5種類、幅500、1000
(各mm)の2種類、フイルム長50mのものが市販
されている。厚さ125μmのPFAフイルムの平方
メートル当りの単価は現在5600円程である。試算
によれば4インチのウエハに6000Åのポリシリコ
ン膜を生成した場合のウエハ1枚当りのフイルム
代は1020円となるが、PFAフイルムは洗浄が可
能である。なおフイルム13はPFAフイルムに
限定されることはなく、耐熱温度が高く紫外線透
過率の高いPFA相当フイルムならば使用できる
ことは言うまでもない。
以上詳細に説明したように、本発明の光CVD
装置反応炉は、表面に薄膜を生成する基板にその
上方から石英窓を通じて紫外線を与えるようにし
た場合に、反応室内の反応生成物が石英窓に付着
し、反応室内に入射する光エネルギを減少させる
ことを防止するために、PFAフイルムを石英窓
の直下、反応室の上部に張りめぐらせたもので、
薄膜の生成速度の向上および薄膜の品質向上に著
しい効果があり、また従来は石英窓に付着する反
応生成物の除去にかなりの労力が必要であつたの
に対し、本発明はフイルムの巻取り更新のみでよ
いので、労力はほとんど不要(将来は自動巻取り
とすることも可能)で経済的であるなど実用上の
効果は大きい。[Table] Therefore, we conducted an ultraviolet irradiation test on PFA film. As a result of a test at room temperature, the temperature of the film was below 40°C, and no solidification was observed, demonstrating that it is sufficiently durable for practical use. Next, a partial structure of the reactor of the present invention will be further explained with reference to FIG. In order to minimize the adhesion of reaction products to the lower surface of the quartz window 1, PFA film guides 19a and 19b are used between the reaction chamber 12 and the quartz window 1 except for the path of incidence of ultraviolet rays.
(the shaded area in Figure 4). Furthermore, in order to prevent the reaction gas from going around the quartz window 1, the flange on the quartz window 1 side has a
Individual grooves are provided, and the reaction gas is prevented from flowing into the quartz window 1 by performing gas purge 18 from the inner circumferential side of the grooves and exhaust gas 24 from the outer circumferential side. There is. Moreover, if the pressure on the quartz window 1 side is made even slightly higher than the pressure in the reaction chamber 12, the reaction gas purge effect of this gas purge method will be further enhanced, so the probability that the reaction gas will reach the quartz window 1 is extremely small. Therefore, adhesion of reaction products to the surface of the quartz window 1 hardly occurs. Also, during CVD film formation, reaction products adhere to the PFA film, reducing the amount of ultraviolet irradiation and slowing down the formation rate. When the film is wound onto the roll 14 in the film storage chamber 20b at the right end in FIG. 3 and a new film is supplied from the roll in the film supply chamber 20a, the amount of ultraviolet ray irradiation is restored and the generation speed is increased. By repeating this operation, the desired film thickness (usually 5000
It is possible to obtain a CVD film with a thickness of 10,000 Å to 10,000 Å. Needless to say, a structure that facilitates film replacement is desirable. Therefore, the PFA film guide (shaded area in Figure 4) has a structure that allows it to be separated into upper and lower guides 19a and 19b.To replace the film, the flange to which the upper guide 19a is fixed and the upper flange of each roll chamber 17 are separated. It is now easy to do once you open it. Further, since the roll chamber 17 is intermediately exhausted between the reaction chamber 12 and the reaction chamber 12, there is almost no inflow of reaction gas. Therefore, there is no problem of contamination due to reaction gas. On the other hand, since this roll chamber has a drive unit, there is a slight risk of generating a small amount of fine powder, but since intermediate exhaust is performed by the exhaust 24, this fine powder hardly ever enters the reaction chamber 12. Finally, we will explain the cooling of PFA film. As shown in the table above, PFA film is
The limit temperature for use is 260°C on the high temperature side, and it is desirable to keep it as low as possible. Therefore, the side surfaces of the reaction chamber and the lower surface of the lower guide 19b are water-cooled. For example, PFA film has a thickness of 25, 50,
5 types: 75, 100, 125 (each μm), width 500, 1000
Two types (each mm) and one with a film length of 50 m are commercially available. The unit price per square meter of PFA film with a thickness of 125 μm is currently around 5,600 yen. According to an estimate, if a 6,000 Å thick polysilicon film is formed on a 4-inch wafer, the film cost per wafer will be 1,020 yen, but PFA film can be washed. Note that the film 13 is not limited to a PFA film, and it goes without saying that any PFA-equivalent film with high heat resistance and high ultraviolet transmittance can be used. As explained in detail above, the optical CVD of the present invention
In the device reactor, when ultraviolet rays are applied from above through a quartz window to a substrate on which a thin film is to be formed on the surface, reaction products in the reaction chamber adhere to the quartz window, reducing the light energy entering the reaction chamber. In order to prevent this, a PFA film is placed directly under the quartz window and above the reaction chamber.
This invention has a remarkable effect on increasing the production rate of thin films and improving the quality of thin films, and whereas conventional methods required considerable effort to remove reaction products that adhere to quartz windows, the present invention can Since it only needs to be updated, it requires almost no effort (automatic winding may be possible in the future), is economical, and has great practical effects.
第1図は低圧水銀灯の発光スペクトラムの一例
図、第2図は従来の光CVD装置の反応炉の代表
的構造概要図、第3図は本発明による光CVD装
置の反応炉の構造概要図、第4図は第3図中の一
部の詳細図で、パージガスと反応ガスの流れを示
す。第5図は無水石英板の光透過特性図、第6図
はPFAフイルムの光透過特性図である。
1……石英窓(板)、2……紫外線ランプユニ
ツト、3……反射板、4……基板(ウエハ)、5
……サセプタ、6……赤外線ランプユニツト、7
……熱電対、8……補助ヒータ、9……ガス入
口、10……真空ポンプ入口、11……第2の石
英窓(板)、12……反応室、13……PFAフイ
ルム、14……フイルムロール、15……フイル
ムローラ、16……補助ローラ、17……フイル
ムチヤンバ(フイルム室20a,20bを含
む)、18……ガスパージポート、19……ガイ
ド、20a……フイルム供給室、20b……フイ
ルム収納室、21……水冷ジヤケツト、22……
反応ガス流、23……反応ガス入力、24……排
気。
FIG. 1 is an example of the emission spectrum of a low-pressure mercury lamp, FIG. 2 is a typical structural schematic diagram of a reactor in a conventional optical CVD device, and FIG. 3 is a schematic structural diagram of a reactor in an optical CVD device according to the present invention. FIG. 4 is a detailed view of a portion of FIG. 3, showing the flow of purge gas and reaction gas. FIG. 5 is a light transmission characteristic diagram of an anhydrous quartz plate, and FIG. 6 is a light transmission characteristic diagram of a PFA film. 1... Quartz window (plate), 2... Ultraviolet lamp unit, 3... Reflection plate, 4... Substrate (wafer), 5
...Susceptor, 6...Infrared lamp unit, 7
... Thermocouple, 8 ... Auxiliary heater, 9 ... Gas inlet, 10 ... Vacuum pump inlet, 11 ... Second quartz window (plate), 12 ... Reaction chamber, 13 ... PFA film, 14 ... ...Film roll, 15...Film roller, 16...Auxiliary roller, 17...Film chamber (including film chambers 20a, 20b), 18...Gas purge port, 19...Guide, 20a...Film supply chamber, 20b...Film storage chamber, 21...Water cooling jacket, 22...
Reaction gas flow, 23...Reaction gas input, 24...Exhaust.
Claims (1)
れ、サセプタとその上に並べた基板(ウエハ)群
を収めた反応室と、上記上方の石英窓板を通じて
反応室内に紫外線を照射する光源ユニツトと、上
記下方の石英窓板とサセプタを通じて基板群を加
熱する熱源ユニツトと、上記上方の石英窓の直下
にあつて反応室内を一方向に移動可能で、移動後
は反応室外に巻取られる耐熱性が高く紫外線透過
率の良好なフイルムとその巻込み、巻取りを行う
フイルムローラ装置と、フイルムの反応室への入
出口にそれぞれフイルムに沿つた上下のガイドの
途中に設けられた反応ガス導入溝と、パージガス
排出溝とを具備して基板面上に光CVDによる一
様な薄膜を生成するようにしたことを特徴とす
る、光CVD装置の薄膜生成反応炉。1. A reaction chamber that is sealed by upper and lower transparent quartz window plates and side walls and contains a susceptor and a group of substrates (wafers) lined up on it, and a light source that irradiates ultraviolet rays into the reaction chamber through the upper quartz window plate. unit, a heat source unit that heats the substrate group through the lower quartz window plate and the susceptor, and a heat source unit that is located directly below the upper quartz window and can be moved in one direction within the reaction chamber, and after being moved, it is rolled up outside the reaction chamber. A film with high heat resistance and good UV transmittance, a film roller device for winding and winding the film, and a reaction gas installed in the middle of upper and lower guides along the film at the entrance and exit of the film into the reaction chamber. 1. A thin film production reactor for a photo-CVD apparatus, characterized in that it is equipped with an introduction groove and a purge gas discharge groove to produce a uniform thin film on a substrate surface by photo-CVD.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12556383A JPS6021381A (en) | 1983-07-12 | 1983-07-12 | Thin film forming reaction furnace of photo-cvd apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12556383A JPS6021381A (en) | 1983-07-12 | 1983-07-12 | Thin film forming reaction furnace of photo-cvd apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6021381A JPS6021381A (en) | 1985-02-02 |
| JPS6152231B2 true JPS6152231B2 (en) | 1986-11-12 |
Family
ID=14913286
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12556383A Granted JPS6021381A (en) | 1983-07-12 | 1983-07-12 | Thin film forming reaction furnace of photo-cvd apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6021381A (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61295373A (en) * | 1985-06-25 | 1986-12-26 | Canon Inc | Method and apparatus for forming accumulated film by photochemical vapor phase growth method |
| JPS6274081A (en) * | 1985-09-28 | 1987-04-04 | Agency Of Ind Science & Technol | Method and apparatus for producing thin film |
| JP2777899B2 (en) * | 1989-03-03 | 1998-07-23 | 富士通株式会社 | Recording device |
| CA2001009C (en) * | 1989-10-19 | 2000-11-28 | Richard S. Adams | Infrared window |
| FI129557B (en) * | 2019-11-28 | 2022-04-29 | Picosun Oy | Substrate processing apparatus and method |
-
1983
- 1983-07-12 JP JP12556383A patent/JPS6021381A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6021381A (en) | 1985-02-02 |
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