TW449789B - Furnace for semiconductor manufacture - Google Patents
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- TW449789B TW449789B TW89116214A TW89116214A TW449789B TW 449789 B TW449789 B TW 449789B TW 89116214 A TW89116214 A TW 89116214A TW 89116214 A TW89116214 A TW 89116214A TW 449789 B TW449789 B TW 449789B
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449 789 五、發明說明U) 發明之領域 本發明提供一種具有雙層外管的半導體爐管裝置,尤 指一種具有一石英(quartz)外管(outer tube)以及一礙化 妙(silicon carbide, SiC)外管雙層外管的半導體爐管裝 置。. 背景說明 化學氣相沈積法(chemical vapor deposition,CVD) 是目前半導體製程中最主要的薄膜沈積方式。一般的CVD 系統均包含有一個反應器、一組氣體傳輸系統、排氣系統 (exhaust)以及製程控制系統(process control system) 等。CVD的反應器(reaction chamber/reactor )依其不同 的應用及設計有多種類型,例如常壓(AP )、低壓(LP )以及 電漿(PE)反應器。隨著半導體製程的曰益精進,為了增加 產能(throughput)’現今大多採用整批式(batch)的製程 設計,使得爐管式(tubular type)的反應器成為一種經最 常被運用的熱壁式(hot wal 1)反應器,用來進行多晶矽 (polysilicon)、二氧化石夕(siiiC0I1 dioxide)以及氮化石夕 (silicon nitride)等材料的沈積製程。 請參考圖一’圊—為習知半導體爐管裝置1〇之示意 圖。習知半導體爐管裝置1〇主要包含有一進氣艙12、一石 449 789 五、發明說明_(2)449 789 V. Description of the invention U) Field of the invention The present invention provides a semiconductor furnace tube device having a double-layer outer tube, in particular a type having a quartz outer tube and a silicon carbide, SiC) semiconductor furnace tube device with double outer tube outer tube. Background Description Chemical vapor deposition (CVD) is currently the most important method of thin film deposition in semiconductor processes. A typical CVD system includes a reactor, a set of gas delivery systems, an exhaust system, and a process control system. CVD reactors (reaction chamber / reactor) have many types according to their different applications and designs, such as atmospheric pressure (AP), low pressure (LP) and plasma (PE) reactors. With the advancement of the semiconductor process, in order to increase throughput, most of the batch process design is used today, so that the furnace-type reactor has become the most commonly used hot wall. A hot wal 1 reactor is used to perform the deposition process of polysilicon, siiiC0I1 dioxide, and silicon nitride. Please refer to Fig. 1 '-a schematic diagram of a conventional semiconductor furnace tube device 10. The conventional semiconductor furnace tube device 10 mainly includes an intake chamber 12, a stone 449 789, and a description of the invention _ (2)
英外管16、一碳化,石夕内管(inner tube)18以及一晶舟 (boat)22。進氣艙12設於爐管裝置10底部’使製程氣體可 由進氣艙12的入口處送入爐管裝置10内。進氣擒12頂部係 由—平板1 4構成,而破化石夕内管1 8則是跨放在平板1 4之 上。石英外管16是設於爐管裝置1〇的最外層’並以環形密 封墊(0 - r i n g ) 2 6加以密封’避免製程氣體外洩。此外’位 於碳化梦内管1 8之内的晶舟2 2係用於沈積反應製程中將成 批(約2 5至2 0 0片)晶圓插入或拔出爐管的冶金工具,通 常皆以高純度的石英或加工的碳化石夕(S i C)製作’以降低 微粒(p a r t i c 1 e )污染的情形。 習知在進行多晶矽的沈積製程時,是先將矽甲烷 (s i lane,SiH4)經加熱解離(decompose)後通入爐管裝置 1 0中。矽曱烷氣體沿著圖一中的氣流方向2 8流動,經由進 氣艙1 2頂部進入複化矽内管1 8中’使晶舟2 2上置放的晶圓 (未顯示)可以均勻地處於矽甲烷的氣氛中。接著製程氣體 會流動至碳化矽内管1 8頂部,然後穿過碳化矽内管1 8頂部 開口流出,並沿著碳化矽内管1 8與石英外管1 6之間的空隙 向下流動8最後再藉由一連接於出氣口 2 4的抽氣設備來將 該剩餘之製程氣體抽出。 由於在進行多晶矽的化學氣相沈積(CVD)製程時,最 p 初通入矽甲烷時的溫度約為6 4 0°C,隨後經過反覆昇降溫 度的製程,最後會降至3 0°C左右。但是習知爐管裝置1 〇使British outer tube 16, a carbonized, inner tube 18 (stone tube) and a boat (22). The air inlet chamber 12 is provided at the bottom of the furnace tube device 10 so that the process gas can be sent into the furnace tube device 10 from the inlet of the air inlet chamber 12. The top of the air intake trap 12 is composed of a flat plate 14, and the inner tube 18 of the broken fossil evening tube is placed on the flat plate 14. The quartz outer tube 16 is provided at the outermost layer 'of the furnace tube device 10 and is sealed with a ring-shaped gasket (0-r i n g) 2 6' to avoid leakage of process gas. In addition, the wafer boat 2 2 within the carbonized inner tube 18 is a metallurgical tool used to insert or remove batches (about 25 to 200 pieces) of wafers in the furnace during the deposition reaction process. High-purity quartz or processed carbonite (S i C) is made 'to reduce particulate pollution (partic 1e). It is conventionally known that in the process of depositing polycrystalline silicon, silanium (Si lane) (SiH4) is decomposed by heating and then introduced into a furnace tube device 10. Silane gas flows along the direction of the airflow 28 in Figure 1, and enters the compound silicon inner tube 18 through the top of the air intake chamber 12 to make the wafers (not shown) placed on the wafer boat 2 2 uniform. The ground is in an atmosphere of silicon methane. The process gas will then flow to the top of the silicon carbide inner tube 18, then flow out through the top opening of the silicon carbide inner tube 18, and flow down the gap between the silicon carbide inner tube 18 and the quartz outer tube 16. 8 Finally, the remaining process gas is extracted by an extraction device connected to the air outlet 24. During the chemical vapor deposition (CVD) process of polycrystalline silicon, the temperature at the time of the initial introduction of silicon methane is about 640 ° C, and then after repeated temperature rise and fall processes, it will eventually drop to about 30 ° C. . However, the conventional furnace tube device 10
第5頁 449789 ^ 49 78 9 _;_ 五、發明說明’(3) 用碳化碎以及石英分別作為内管1 8以及外管1 6的材料’碳 化石夕在6 0 (TC時的熱膨脹係數(C T E )約為4 . 1 9 X 1 0 -6 /°C, 石英的熱膨脹係數約為0 . 5 5至0 . 7 (x 1 0 -6广C ),而多晶 矽的熱膨脹係數約在2 . 5至4. 5 (X 1 0 -6 /°c )之間’與石英 的熱膨脹係數相距甚大,而較接近於碳化矽在6 0 OeC時的 熱膨脹係數。 因此在前述之降溫過程中,石英外管16將會對附著於 管壁上的多晶矽薄膜造成拉應力(即張力,tension)。 然而多晶矽的拉應力僅有497 0Psi ’小於壓縮應力 (compression)7500Psi甚多,故會造成多晶矽薄膜發生剝 裂的現象,使得後續附著沈積於裂縫開口處之多晶矽,容 易形成相當數量的多晶梦微粒。也就是說,石英外管1 6上 附著的多晶矽薄膜將會因爐管裝置1 0的昇溫、降溫而不斷 剝落,進而直接對晶圓表面造成微粒(particle)污染,或 是隨著製程氣體的氣流在爐管裝置1〇内循環影響晶圓'表面 以及爐管裝置1 〇的潔淨度。 為了解決上述爐管裝置1 〇所發生之微粒污染的 因此目前内管1 8及晶舟2 2多已採用熱膨脹係數 U化妙作為製作材料。然而,外管1δ :Page 5 449789 ^ 49 78 9 _; _ 5. Description of the invention '(3) Use carbonized crushed and quartz as materials for the inner tube 18 and outer tube 16' Carbonite thermal expansion coefficient at 6 0 (TC (CTE) is about 4.19 X 1 0 -6 / ° C, the thermal expansion coefficient of quartz is about 0.5 5 to 0.7 (x 1 0 -6 wide C), and the thermal expansion coefficient of polycrystalline silicon is about 2 Between 5 and 4.5 (X 1 0 -6 / ° c), the thermal expansion coefficient of quartz is very large, and it is closer to the thermal expansion coefficient of silicon carbide at 60 OeC. Therefore, during the aforementioned temperature reduction process, The quartz outer tube 16 will cause tensile stress (ie, tension) on the polycrystalline silicon film attached to the tube wall. However, the tensile stress of polycrystalline silicon is only 497 0 Psi ', which is much smaller than the compression stress (compression) 7500 Psi, so it will cause polycrystalline silicon film. The occurrence of spalling makes subsequent polycrystalline silicon deposited on the crack openings easy to form a considerable number of polycrystalline dream particles. That is, the polycrystalline silicon film attached to the quartz outer tube 16 will be affected by the furnace tube device 10 Heating, cooling, and continuous peeling, which directly causes particles on the wafer surface particle) pollution, or the cleanliness of the wafer 'surface and the furnace tube device 10 as the gas flow of the process gas circulates in the furnace tube device 10. In order to solve the particulate pollution that occurs in the furnace tube device 10 above, At present, the inner tube 18 and the crystal boat 22 have already adopted the thermal expansion coefficient U Huamiao as the production material. However, the outer tube 1δ:
碳化妙材料,主要因為兩項問題無法克ί矣製 Θ 匕^係為一種多孔隙的材料,若採用碳化ϋ 3 最外層外管的材料,將無法形成一相對密閉之空匕:作^The carbonized material is mainly because two problems cannot be made. The Θ dagger is a porous material. If the material of the outermost tube of carbide 3 is used, it will not be able to form a relatively closed hollow dagger:
第6頁 449789 五、發明說明(4) 管裝置1 0内部完全與外界隔絕。而在進行多晶矽沈積時, 該具有毒性之矽甲烷氣體可能會因此而外洩出來,因此不 I可能直接以碳化矽作為外管之材料。另一方面,依目前工Page 6 449789 V. Description of the invention (4) The inside of the pipe device 10 is completely isolated from the outside. During the deposition of polycrystalline silicon, the toxic silicon dioxide gas may leak out because of this, so it is possible to directly use silicon carbide as the material of the outer tube. On the other hand,
I 藝技術而言,尚無法製作一體成型之碳化矽外管,僅能以 數個中空之塊錠狀碳化矽加以接合,然接合處之密合度必 無法達到完全密封製程氣體。 (2)碳化石夕的熱傳導係數(thermal conductivity)約為 3 6W/m°C,石英的熱傳導係數則僅為〇. 14 W/m°C。因此在 使用環形密封墊2 6將外管密封時,若採用碳化矽作為外管 1 6材料,則容易因碳化矽的熱傳導能力過於良好,而使熱 能迅速由外管1 6主體傳導至環形密封墊2 6處,進而將環形 密封墊2 6劣化、損毀,破壞爐管裝置1 0的密封真空度。 發明概述 因此本發明之主要目的在提供一種具有一石英外管以 及一碳化矽外管雙層外管的半導體爐管裝置,以解決上述 習知技術之問題。 在本發明之最佳實施例中,該爐管包含有一平板,以 及一石英外管、一熱緩衝層、一碳化矽外管、一碳化矽内 管與一晶舟由外而内依序設於該平板之上。該石英外管係 用來將該爐管裝置與外界隔絕,該碳化矽外管是用來避免 粒子殘留於該石英外管内壁表面,而該熱緩衝層則是用來 449789 五、發明說明(5) 降低兩外管間之熱應力並避免僉碳化矽内管中之氣體外 曳。 .本發明設計是利用碳化矽外管來避免多晶矽微粒的生 成,以確保晶圓表面及爐管裝置的潔淨度,進而減少爐管 裝置清洗淨化的次數。此外,於雙層外管之間通入氮氣所 形成之熱緩衝層,不但可以減缓該碳化矽外管與該石英外 管之溫度差異所產生的熱應力,更能避免該碳化矽内管中 之製程氣體外洩至該碳化矽外管與該石英外管之間。 發明之詳細說明 請參考圖二,圖二為本發明半導體爐管裝置40之示意 圖。本發明之爐管裝置4 0主要包含有一進氣艙42、一石英 外管4 6、一碳化石夕外管5 0、一碳化石夕内管4 8以及一晶舟 52〇 進氣艙42設於爐管裝置4 0底部,製程氣體可由進氣艙 42的入口處送入爐管裝置40内。進氣艙42項部係由一平板 4 4構成,而碳化矽内管4 8跨放在平板4 4之上。位於碳化矽 内管4 8之内的晶舟5 2係用於沈積反應製程中將成批(約2 5 至2 0 0片)晶圓插入或拔出爐管的冶金工具,通常皆以高 純度的石英或加工的碳化矽(S i C)製作,以降低微粒污染 的情形βAs far as I technology is concerned, it is not yet possible to make a single-piece silicon carbide outer tube. It can only be joined by several hollow ingot-like silicon carbides, but the tightness of the joint must not be able to achieve a completely sealed process gas. (2) The thermal conductivity of carbonized stone is about 36 W / m ° C, and the thermal conductivity of quartz is only 0.14 W / m ° C. Therefore, when using an annular gasket 26 to seal the outer tube, if silicon carbide is used as the material of the outer tube 16, it is easy for the thermal conductivity of the silicon carbide to be too good, so that the heat energy is quickly conducted from the main body of the outer tube 16 to the annular seal. The gasket 26 deteriorates and damages the ring-shaped gasket 26 and destroys the sealing vacuum degree of the furnace tube device 10. SUMMARY OF THE INVENTION Therefore, the main object of the present invention is to provide a semiconductor furnace tube device having a quartz outer tube and a silicon carbide outer tube double-layer outer tube to solve the problems of the conventional technology. In a preferred embodiment of the present invention, the furnace tube includes a flat plate, and a quartz outer tube, a thermal buffer layer, a silicon carbide outer tube, a silicon carbide inner tube, and a wafer boat are sequentially arranged from the outside to the inside. On the tablet. The quartz outer tube is used to isolate the furnace tube device from the outside, the silicon carbide outer tube is used to prevent particles from remaining on the inner wall surface of the quartz outer tube, and the thermal buffer layer is used for 449789 V. Description of the invention ( 5) Reducing the thermal stress between the two outer tubes and avoiding the drag of the gas in the silicon carbide inner tube. The design of the present invention is to use a silicon carbide outer tube to avoid the generation of polycrystalline silicon particles to ensure the cleanliness of the wafer surface and the furnace tube device, thereby reducing the number of cleaning and purification of the furnace tube device. In addition, the thermal buffer layer formed by passing nitrogen gas between the double-layer outer tubes can not only slow down the thermal stress caused by the temperature difference between the silicon carbide outer tube and the quartz outer tube, but also avoid the silicon carbide inner tube. The intermediate process gas is leaked between the silicon carbide outer tube and the quartz outer tube. Detailed description of the invention Please refer to FIG. 2. FIG. 2 is a schematic diagram of a semiconductor furnace tube device 40 of the present invention. The furnace tube device 40 of the present invention mainly includes an air inlet chamber 42, a quartz outer tube 46, a carbonized petrified tube 50, a carbonized petrified tube 48, and a wafer boat 52. Located at the bottom of the furnace tube device 40, the process gas can be sent into the furnace tube device 40 from the inlet of the air inlet cabin 42. The 42th part of the air intake cabin is composed of a flat plate 4 4, and a silicon carbide inner tube 4 8 is placed on the flat plate 4 4. The wafer boat 5 2 within the silicon carbide inner tube 4 8 is a metallurgical tool used to insert or pull out batches (about 25 to 200 pieces) of wafers in the furnace during the deposition reaction process, usually with high purity. Made of quartz or processed silicon carbide (S i C) to reduce particulate contamination β
第8頁 4 49 78 9 五、發明說明(6) 石英外管46是設於爐管裝置40的最外層,用來將該爐 管裝置與外界隔絕,並以環形密封墊(0- r i ng) 5 6加以密 封,避免製程氣體外洩。本發明之爐管裝置4 0另包含有一 碳化矽外管5 0設於碳化矽内管4 8與石英外管4 6之間,用來 避免多晶矽微粒殘留於石英外管4 6内壁。 當利用本發明之裝置來進行多晶矽的沈積製程時,是 先將矽甲烧(3]_18116,3丨114)由進氣艙42通入爐管裝置40中 進行加熱解離。由於進氣艙4 2頂部開口與碳化矽内管4 8底 部密合連接,因此該通入之矽甲烧氣體便會沿圖二中的氣 流方向5 8進入碳化矽内管4 6之中,使晶舟2 2上置放的晶圓 能得以均勻地處於矽甲烷的氣氛中。接著製程氣體會流動 至碳化矽内管4 8頂部,然後順著頂部開口流出,並沿著碳 化矽内管4 8與碳化矽外管5 0間向下流動。最後再藉由一連 接於出氣口 5 4的抽氣設備(未顯示)來將該剩餘之製程氣體 抽出。 本發明之爐管裝置4 0於碳化矽外管5 0與石英外管4 6間 另包含有一熱緩衝層62。熱缓衝層62係一填充有氮氣氣體 之區域所構成,該區域的氣體壓力係大於或等於該碳化矽 内管中之氣體的壓力,以形成一氣障,使碳化矽外管5 0的 外壁所受的氣體(氮氣)壓力大於内壁所受的氣體(矽甲 烷)壓力,進而避免碳化矽内管4 8中之製程氣體外洩至碳Page 8 4 49 78 9 V. Description of the invention (6) The quartz outer tube 46 is provided on the outermost layer of the furnace tube device 40, and is used to isolate the furnace tube device from the outside. A ring seal (0-ri ng ) 5 6 Seal to avoid leakage of process gas. The furnace tube device 40 of the present invention further includes a silicon carbide outer tube 50 disposed between the silicon carbide inner tube 48 and the quartz outer tube 46 to prevent polycrystalline silicon particles from remaining on the inner wall of the quartz outer tube 46. When the device of the present invention is used to perform the polycrystalline silicon deposition process, the silicon sintered (3) -18116, 3 丨 114) is first passed through the air inlet chamber 42 into the furnace tube device 40 for heating and dissociation. Since the top opening of the air intake chamber 4 2 is tightly connected to the bottom of the silicon carbide inner tube 4 8, the silicon gas burned in will enter the silicon carbide inner tube 4 6 along the flow direction 5 8 in FIG. 2. The wafers placed on the wafer boat 22 can be evenly placed in a silicon methane atmosphere. Then the process gas will flow to the top of the silicon carbide inner tube 48, and then flow out along the top opening, and flow down along the silicon carbide inner tube 48 and the silicon carbide outer tube 50. Finally, a gas extraction device (not shown) connected to the gas outlet 54 is used to extract the remaining process gas. The furnace tube device 40 of the present invention includes a thermal buffer layer 62 between the silicon carbide outer tube 50 and the quartz outer tube 46. The thermal buffer layer 62 is composed of a region filled with nitrogen gas, and the gas pressure in the region is greater than or equal to the pressure of the gas in the silicon carbide inner tube to form a gas barrier, so that the outer wall of the silicon carbide outer tube 50 The pressure of the gas (nitrogen) is greater than the pressure of the gas (silicon methane) on the inner wall, thereby preventing the process gas in the silicon carbide inner tube 48 from leaking to the carbon.
第9頁 i 449 789 五、發明說明(7) ' 化矽外管5 0與石英外管4 6之間,而於石英外管4 6的;内壁上 形成多晶矽薄膜,甚至外洩出爐管裝置4 0之外。而熱緩衝 層6 2的出〇可連接至與製程氣體同一抽氣裝置,以將氮氣 抽出。 丨.Page 9 i 449 789 V. Description of the invention (7) '' Between the silicon outer tube 50 and the quartz outer tube 46, and between the quartz outer tube 46; a polycrystalline silicon film is formed on the inner wall, and even the furnace tube device leaks out Other than 4 0. The output of the thermal buffer layer 62 can be connected to the same pumping device as the process gas to pump out nitrogen.丨.
I ! 在本發明的另一實施例中,碳化矽外管5 0與石英外管 46亦可結合為一複合式外管,亦即石英外管46與碳化矽外 管5 0之間(複合式外管的中間層)以一可以降低石英外管 4 6與碳化矽外管5 0間熱應力的材料來製作熱缓衝層6 2,或 是先將碳化矽外管5 0之外壁塗佈一高緻密材料之後,再與 石英外管4 6相結合成一複合式外管,並將碳化矽外管5 0與 (::: 石英外管4 6中間抽成真空或填充一氣體當作熱緩衝層6 2, 形成該複合式外管。 由於碳化矽材料的熱膨脹係數(CTE )與多晶矽近似 (6 0 0°C時,碳化矽的熱膨脹係數約為4. 1 9χ 1 0 —6 /°C,而 多晶矽的熱膨脹係數約在2. 5x 1 0 ―6 /°C至4 · 5 X 1 0 _6 /°C 之間),因此在多晶矽化學氣相沈積(C VD )製程的升降溫 過程中,不但可減少多晶矽微粒的生成,而且爐管所需的 爭化次數亦較少,因此被工業界廣為用以之製作半導體前 端製程之冶具。然而在高溫爐管裝置中,受限於前述(背 ,..、 景說明)兩項固難無法突破,外管無法直接使用碳化矽加 以製作。I! In another embodiment of the present invention, the silicon carbide outer tube 50 and the quartz outer tube 46 may also be combined into a composite outer tube, that is, between the quartz outer tube 46 and the silicon carbide outer tube 50 (composite Middle layer of the outer tube) using a material that can reduce the thermal stress between the quartz outer tube 46 and the silicon carbide outer tube 50 to make the thermal buffer layer 62, or first coat the outer wall of the silicon carbide outer tube 50 After distributing a high-density material, it is combined with the quartz outer tube 4 6 to form a composite outer tube. The middle of the silicon carbide outer tube 50 and (::: quartz outer tube 4 6 is evacuated or filled with a gas as The thermal buffer layer 62 forms the composite outer tube. Because the thermal expansion coefficient (CTE) of the silicon carbide material is similar to that of polycrystalline silicon (at 60 ° C, the thermal expansion coefficient of silicon carbide is approximately 4.1 9χ 1 0 -6 / ° C, and the thermal expansion coefficient of polycrystalline silicon is about 2.5x 1 0 -6 / ° C to 4 · 5 X 1 0 _6 / ° C), so the temperature rise and fall in polycrystalline silicon chemical vapor deposition (C VD) process In the process, not only the generation of polycrystalline silicon particles can be reduced, but also the number of contention of the furnace tube is less, so it is widely used in the industry to make half The rule of precursor process ends. However, in a high temperature furnace tube devices, limited by the foregoing (back, .., King described) two hard solid can not break through the outer tube can not be directly applied to produce silicon carbide.
第10頁Page 10
J 449789 五、發明說明(8) 但是本發明之爐管裝置40中採用雙層外管( 與碳化矽外管)的設計有以下優點: (1) 石英的熱膨脹係數約為0 . 5 5至0 . 7 (X 1 0 _ 與欲進行沈積之多晶矽的熱膨脹係數相距甚大, 明以熱膨脹係數(CTE )與多晶矽近似的碳化矽材却 層外管中内層的外管。在進行多晶石夕的沈積製程 沿著圖二中方向5 8流動,主要接觸較不易生成微 石夕内管5 0,且碳化石夕外管5 0外壁又有一氮氣形成 缓衝層6 2,因此矽甲烷氣流甚少與石英外管4 6内 故避免石英外管4 6内壁生成有多晶矽微粒,影響 或爐管裝置40的潔淨度。 (2) 最外層外鲁4 6製作時仍以石英做為材料, 置4 0内部得以完全與外界隔絕,且進行多晶矽沈 的矽曱烷毒氣不致外洩。另一方面,石英的熱傳 低,因此在使用環形密封墊5 6將外管4 6密封時, 環形密封墊5 6的完整以及爐管裝置4 0的密封真空 相較於習知製作之爐管裝置1 0,本發明使用 管5 0、石英外管4 6的雙層外管設計,是利用碳化 避免多晶矽微粒的生成,以確保晶圓表面及爐管 淨度,進而減少爐管裝置清洗淨化的次數。此外 外管之間通入氮氣所形成之熱緩衝層,不但可以 化矽外管與該石英外管之溫度差異所產生的熱應 避免該碳化矽内管十之製程氣體外洩至該碳化矽 石英外管 6 /〇C ), 因此本發 +製作雙 時,氣流 粒的碳化 之氣障熱 壁接觸, 晶圓表面 使爐管裝 積時使用 導係數較 可以確保 度。 碳化矽外 矽外管來 裝置的潔 ,於雙層 減缓該碳 力,更能 外管與該 449 78 9 五 '發明說明(9) 石英外管之間。 以上所述僅本發明之較佳實施例,凡依本發明申請專 利範圍所做之均等變化與修飾,皆應屬本發明專利之涵蓋 範圍。J 449789 V. Description of the invention (8) However, the design of the double-layer outer tube (and silicon carbide outer tube) in the furnace tube device 40 of the present invention has the following advantages: (1) The thermal expansion coefficient of quartz is about 0.5 5 to 0.7 (X 1 0 _ is far from the thermal expansion coefficient of the polycrystalline silicon to be deposited. It is clear that the silicon carbide material with a coefficient of thermal expansion (CTE) similar to that of polycrystalline silicon has an inner tube and an outer tube. The deposition process flows along the direction 58 in Figure 2. The main contact is less likely to generate micro-stone inner tube 50, and the outer wall of carbonized carbide outer tube 50 has a nitrogen gas to form a buffer layer 62. Therefore, the flow of silicon methane is very low. The outer wall of the quartz outer tube 4 6 should avoid polycrystalline silicon particles generated on the inner wall of the quartz outer tube 4 6 and affect or clean the furnace tube device 40. (2) The outer outer layer 4 6 is still made of quartz as the material. The inside of the valve is completely isolated from the outside, and the siloxane gas of polysilicon precipitation does not leak out. On the other hand, the heat transfer of quartz is low, so when the outer tube 4 6 is sealed with a ring seal 6, the ring is sealed. Completeness of gasket 5 6 and sealing of furnace tube device 40 Compared with the conventionally made furnace tube device 10, the present invention uses a double-layer outer tube design of tube 50 and quartz outer tube 46. The use of carbonization avoids the generation of polycrystalline silicon particles to ensure the wafer surface and the furnace tube. Clarity, thereby reducing the number of times of cleaning and purification of the furnace tube device. In addition, a thermal buffer layer formed by passing nitrogen gas between the outer tubes can not only convert the heat generated by the temperature difference between the silicon outer tube and the quartz outer tube, but also avoid carbonization The process gas of the silicon inner tube is leaked out to the silicon carbide quartz outer tube 6/0 C), so when the present + production dual, the carbonized gas barrier of the gas flow particles contacted the hot wall, and when the furnace surface was assembled on the wafer surface The use of the derivative coefficient can ensure the degree. Silicon carbide outside the silicon tube to clean the device, double-layer to slow down the carbon force, and more between the outer tube and the 449 78 9 5 'Invention Note (9) Quartz outer tube. The above are only the preferred embodiments of the present invention, and all equivalent changes and modifications made in accordance with the scope of the patent application of the present invention shall fall within the scope of the patent of the present invention.
第12頁 449 789 - 圖式簡單說明 圖示之簡單說明 圖一為習知半導體爐管裝置之示意圖。 圖二為本發明半導體爐管裝置之示意圖。 圖示之符號說明 10、 40 爐管裝置 12、 42 進氣搶 14、 44 平板 1 6 ' 46 石英外管 18' 48 碳化矽内管 22 ' 52 晶舟 24 > 54 出氣口 26、 5 6 環形密封墊 ,v. f ί._ )' 28' 58 氣汰方向 50 碳化矽外管 1* 62 熱緩衝層Page 12 449 789-Simple illustration of the diagram Simple illustration of the diagram Figure 1 is a schematic diagram of a conventional semiconductor furnace tube device. FIG. 2 is a schematic diagram of a semiconductor furnace tube device according to the present invention. Symbols shown in the figure 10, 40 furnace tube device 12, 42 intake air grab 14, 44 flat plate 1 6 '46 quartz outer tube 18' 48 silicon carbide inner tube 22 '52 wafer boat 24 > 54 air outlet 26, 5 6 Annular gasket, v. F ί._) '28' 58 Gas direction 50 Silicon carbide outer tube 1 * 62 Thermal buffer layer
第13頁Page 13
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