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KR100443598B1 - Apparatus for Chemical Vapor Deposition - Google Patents

Apparatus for Chemical Vapor Deposition Download PDF

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Publication number
KR100443598B1
KR100443598B1 KR10-2001-0068511A KR20010068511A KR100443598B1 KR 100443598 B1 KR100443598 B1 KR 100443598B1 KR 20010068511 A KR20010068511 A KR 20010068511A KR 100443598 B1 KR100443598 B1 KR 100443598B1
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gas
reaction chamber
purge gas
wafer support
gas outlet
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KR20030037471A (en
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심경식
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주성엔지니어링(주)
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Priority to US10/282,304 priority patent/US7390366B2/en
Priority to JP2002316228A priority patent/JP4078185B2/en
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    • CCHEMISTRY; METALLURGY
    • C23COATING 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
    • C23CCOATING 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
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/44Chemical 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
    • C23C16/4401Means for minimising impurities, e.g. dust, moisture or residual gas, in the reaction chamber
    • CCHEMISTRY; METALLURGY
    • C23COATING 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
    • C23CCOATING 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
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/44Chemical 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
    • C23C16/4412Details relating to the exhausts, e.g. pumps, filters, scrubbers, particle traps
    • CCHEMISTRY; METALLURGY
    • C23COATING 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
    • C23CCOATING 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
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/44Chemical 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
    • C23C16/455Chemical 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 characterised by the method used for introducing gases into reaction chamber or for modifying gas flows in reaction chamber
    • C23C16/45563Gas nozzles
    • C23C16/4558Perforated rings
    • CCHEMISTRY; METALLURGY
    • C23COATING 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
    • C23CCOATING 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
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/44Chemical 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
    • C23C16/458Chemical 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 characterised by the method used for supporting substrates in the reaction chamber
    • C23C16/4582Rigid and flat substrates, e.g. plates or discs
    • C23C16/4583Rigid and flat substrates, e.g. plates or discs the substrate being supported substantially horizontally
    • C23C16/4586Elements in the interior of the support, e.g. electrodes, heating or cooling devices

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  • Chemical & Material Sciences (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)

Abstract

반응챔버 내측면에 설치되는 기체 포커스 링(70)에 의하여 웨이퍼 지지대(50)의 상부공간 중심부로 공정기체가 분사된다. 공정기체는 반응챔버(10) 저면으로부터 공급되는 퍼지기체 때문에 반응챔버(10)의 하부공간으로는 내려가지 못하다. 따라서, 파티클 소스를 최소화시킬 수 있을 뿐만 아니라 장비의 정검주기를 연장시킬 수 있다. 또한, 퍼지가스 역시 공정기체의 압력에 의하여 반응챔버(10)의 상부공간으로 올라가지 못하므로 퍼지기체에 의해 CVD 공정이 영향을 받는 일은 없다. 공정기체 및 퍼지기체는 반응챔버(10) 측벽에 환형홈 형태로 설치되는 기체배출구(80)를 통하여 배출된다. 기체배출구(80) 중간부분에는 공정기체와 퍼지기체의 혼합에 의한 와류가 발생하지 않도록 환형 차단막(85)이 수평하게 설치된다. 차단막(85) 하부 및 상부는 차단막(85)보다 더 큰 내경을 갖는 환형의 하부분할막(84) 및 상부분할막(86)이 각각 설치된다. 상부분할막(86) 및 하부분할막(84)에 의하여 형성된 공간에 의하여 공정기체 및 퍼지기체 각각이 여러 부분에서 조금씩 배출되기 때문에 와류현상은 더욱 감소하게 된다.The process gas is injected into the center of the upper space of the wafer support 50 by the gas focus ring 70 installed on the inner side of the reaction chamber. The process gas cannot be lowered into the lower space of the reaction chamber 10 because of the purge gas supplied from the bottom of the reaction chamber 10. Thus, the particle source can be minimized as well as the equipment's inspection cycle can be extended. In addition, since the purge gas does not rise to the upper space of the reaction chamber 10 due to the pressure of the process gas, the CVD process is not affected by the purge gas. The process gas and the purge gas are discharged through the gas discharge port 80 which is installed in the annular groove form on the side wall of the reaction chamber (10). In the middle portion of the gas discharge port 80, the annular blocking film 85 is horizontally installed so that vortices due to the mixing of the process gas and the purge gas do not occur. Lower and upper portions of the barrier layer 85 are provided with an annular lower portion 84 and an upper portion 86 having an inner diameter larger than that of the barrier layer 85. Due to the space formed by the upper dividing layer 86 and the lower dividing layer 84, each of the process gas and the purge gas is slightly discharged from various parts, thereby further reducing the vortex phenomenon.

Description

CVD 장치{Apparatus for Chemical Vapor Deposition}Apparatus for Chemical Vapor Deposition

본 발명은 CVD 장치에 관한 것으로서, 특히 반응챔버 하부공간에 원하지 않게 박막이 증착되어 이 부분이 파티클 소스로 작용하는 것을 방지할 수 있는 CVD 장치에 관한 것이다.The present invention relates to a CVD apparatus, and more particularly, to a CVD apparatus capable of preventing undesired deposition of a thin film in the reaction chamber subspace, thereby acting as a particle source.

종래의 CVD 장치는 기체배출구가 주로 반응챔버의 저면에 설치된다. 따라서, 박막증착에 기여하지 못한 기체들이 기체배출구를 통해서 외부로 배출될 때 반응챔버 하부공간에 증착되어 이 부분이 파티클 발생 소스(source)로 작용하는 문제가 있다.In a conventional CVD apparatus, a gas outlet is mainly provided at the bottom of the reaction chamber. Therefore, when gases which do not contribute to the thin film deposition are discharged to the outside through the gas discharge port is deposited in the reaction chamber lower space there is a problem that this portion acts as a particle generation source (source).

따라서, 본 발명이 이루고자 하는 기술적 과제는, 박막증착에 기여하지 못한 기체들이 반응챔버 하부공간으로 내려가지 못하도록 하여 파티클 소스를 없애므로써 장비정검주기를 연장시킬 수 있는 CVD 장치를 제공하는 데 있다.Accordingly, an aspect of the present invention is to provide a CVD apparatus capable of extending the equipment inspection cycle by eliminating particle sources by preventing gases that do not contribute to thin film deposition into the reaction chamber lower space.

도 1a 및 도 1b는 본 발명에 따른 CVD 장치를 설명하기 위한 개략도들이다.1A and 1B are schematic diagrams for explaining a CVD apparatus according to the present invention.

< 도면의 주요 부분에 대한 참조번호의 설명 ><Description of Reference Numbers for Main Parts of Drawings>

10: 반응챔버 20: 석영돔10: reaction chamber 20: quartz dome

30: 벨자 40: 벨자히터30: Belza 40: Belzaheater

50: 웨이퍼 지지대 52: 지지축50: wafer support 52: support shaft

60: 웨이퍼 70: 기체 포커스 링60: wafer 70: gas focus ring

72: 분사공 74: 기체공급라인72: injection hole 74: gas supply line

80: 기체배출구 82: 펌핑라인80: gas outlet 82: pumping line

84: 하부분할막 86: 상부분할막84: lower partition 86: upper partition

85: 차단막 87: 상부기체배출구85: blocking film 87: upper gas outlet

88: 하부기체배출구 90: 퍼지기체 공급구88: lower gas outlet 90: purge gas supply port

상기 기술적 과제를 달성하기 위한 본 발명에 따른 CVD 장치는, 화학기상증착 공정이 진행되는 반응챔버; 상기 반응챔버 내부에 설치되며 웨이퍼가 안착되어지는 웨이퍼 지지대; 상기 웨이퍼 지지대 주위로부터 상기 웨이퍼 지지대의 상부공간 중심부로 공정기체를 분사하도록 상기 반응챔버 측면부에 설치되는 기체 포커스 링; 상기 반응챔버 내부로 퍼지기체를 공급하기 위하여 상기 반응챔버 저면에 설치되는 퍼지기체 공급구; 상기 기체 포커스 링을 통하여 분사되는 공정기체 및 상기 퍼지기체 공급구를 통해서 공급되는 퍼지기체를 배출시키기 위하여, 상기 기체 포커스 링보다는 하부에 위치하고 상기 반응챔버의 저면으로부터 소정의 높이에 위치하도록, 상기 반응챔버의 측벽을 따라 수평한 환형링 형태로 설치되는 기체배출구; 상기 기체배출구와 진공펌프를 서로 연결하는 하나의 펌핑라인; 상기 기체배출구를 통해서 배출되는 공정기체와 퍼지기체가 상기 기체배출구 입구 부위에서 서로 혼합되지 않도록 상기 기체배출구 중간부분에 위치하도록 상기 기체배출구에 환형으로 수평하게 설치되는 차단막; 상기 차단막 하부의 기체배출구 부분을 복수개의 공간으로 나눠지도록 수평분할하며 상기 차단막보다 더 큰 내경을 가지는 복수개의 환형 하부분할막; 상기 차단막 상부의 기체배출구 부분을 복수개의 공간으로 나눠지도록 수평분할하며 상기 차단막보다 더 큰 내경을 가지는 복수개의 환형 상부분할막; 을 구비하는 것을 특징으로 한다.CVD apparatus according to the present invention for achieving the above technical problem, the reaction chamber is a chemical vapor deposition process is carried out; A wafer support installed in the reaction chamber and on which a wafer is seated; A gas focus ring installed at a side surface of the reaction chamber to inject a process gas from around the wafer support to the center of the upper space of the wafer support; A purge gas supply port provided at a bottom of the reaction chamber to supply a purge gas into the reaction chamber; In order to discharge the process gas injected through the gas focus ring and the purge gas supplied through the purge gas supply port, the reaction gas is positioned below the gas focus ring and positioned at a predetermined height from the bottom of the reaction chamber. A gas outlet installed in a horizontal annular ring shape along the side wall of the chamber; One pumping line connecting the gas discharge port and the vacuum pump to each other; A barrier membrane horizontally installed in the gas outlet so that the process gas and the purge gas discharged through the gas outlet are located at the middle of the gas outlet so that they are not mixed with each other at the gas outlet inlet; A plurality of annular lower subdivision membranes which are horizontally divided to divide the gas outlet portion of the lower portion of the barrier layer into a plurality of spaces and have a larger inner diameter than the barrier layer; A plurality of annular upper dividing membranes which are horizontally divided to divide the gas outlet portion of the upper portion of the barrier layer into a plurality of spaces and have a larger inner diameter than the barrier layer; It characterized by having a.

이하에서, 본 발명의 바람직한 실시예를 첨부한 도면을 참조하여 상세히 설명한다.Hereinafter, with reference to the accompanying drawings, preferred embodiments of the present invention will be described in detail.

도 1a 및 도 1b는 본 발명에 따른 CVD 장치를 설명하기 위한 개략도들이다.1A and 1B are schematic diagrams for explaining a CVD apparatus according to the present invention.

도 1a 및 도 1b를 참조하면, 반응챔버(10)는 웨이퍼가 한장씩 장입되는 매엽식 반응챔버이고, 반응챔버(10) 상부는 석영돔(20)으로 이루어진다. 석영돔(20) 외측에는 석영돔(20)을 덮는 벨자(30)가 설치되며 벨자(30) 내측에는 벨자히터(40)가설치된다. 반응챔버(10) 내부에는 웨이퍼 지지대(50)가 설치되며, 웨이퍼(60)는 웨이퍼 지지대(50) 상에 놓여진다.1A and 1B, the reaction chamber 10 is a single-leaf reaction chamber in which wafers are loaded one by one, and the upper portion of the reaction chamber 10 includes a quartz dome 20. A bell jar 30 covering the quartz dome 20 is installed outside the quartz dome 20, and a bell jar heater 40 is installed inside the bell jar 30. The wafer support 50 is installed in the reaction chamber 10, and the wafer 60 is placed on the wafer support 50.

웨이퍼 지지대(50)에는 화학기상증착이 일어날 수 있는 적절한 온도로 웨이퍼(60)를 가열하기 위한 메인히터(미도시)가 설치된다. 웨이퍼 지지대(50)는 지지축(52)에 의해 지지되는데, 지지축(52)은 벨로우즈(55)로 둘러싸여져 벨로우즈(55)에 의해 지지축(52)이 상하 이송되더라도 외부와 반응챔버(10) 내부는 밀폐 상태를 유지하게 된다.The wafer support 50 is provided with a main heater (not shown) for heating the wafer 60 to an appropriate temperature at which chemical vapor deposition can occur. The wafer supporter 50 is supported by the support shaft 52. The support shaft 52 is surrounded by the bellows 55 so that the support shaft 52 is vertically transferred by the bellows 55 even though the reaction chamber 10 The inside is kept sealed.

기체 포커스 링(70)은 웨이퍼 지지대(50) 측면을 둘러싸도록 반응챔버(10) 내측면에 설치된다. 기체 포커스 링(70)에는 복수개의 분사공(72)이 형성되어 있다. 분사공(72) 대신에 환형의 분사링이 형성될 수도 있다.The gas focus ring 70 is installed at the inner side of the reaction chamber 10 to surround the side of the wafer support 50. A plurality of injection holes 72 are formed in the gas focus ring 70. Instead of the injection hole 72, an annular injection ring may be formed.

반응챔버(10)의 저면에는 반응챔버(10) 내부로 N2 또는 Ar 등의 퍼지기체를 공급하기 위한 퍼지기체 공급구(90)가 설치된다.A purge gas supply port 90 for supplying a purge gas such as N2 or Ar into the reaction chamber 10 is installed at the bottom of the reaction chamber 10.

반응챔버(10)의 측면에는 기체 포커스 링(70)을 통하여 분사되는 공정기체 및 퍼지기체 공급구(90)를 통해서 공급되는 퍼지기체를 배출시키기 위한 기체배출구(80)가 설치된다. 기체배출구(80)는 기체 포커스 링(70)보다는 하부에 위치하며 환형 홈의 형태를 갖는다. 기체배출구(80)는 웨이퍼 지지대(50)와 같은 높이에 설치되는 것이 바람직하다. 기체배출구(80)는 펌핑라인(82)에 의해 하나의 진공펌프(미도시)에 연결된다.Side of the reaction chamber 10 is provided with a gas discharge port 80 for discharging the process gas injected through the gas focus ring 70 and the purge gas supplied through the purge gas supply port 90. The gas outlet 80 is located below the gas focus ring 70 and has the form of an annular groove. The gas discharge port 80 is preferably installed at the same height as the wafer support 50. The gas outlet 80 is connected to one vacuum pump (not shown) by the pumping line 82.

기체배출구(80)에서 공정기체와 퍼지기체가 서로 혼합되지 않도록 기체배출구(80) 중간부분에는 차단막(85)이 환형으로 수평하게 설치된다. 따라서, 기체배출구(80)는 하부기체배출구(88)와 상부기체배출구(87)로 분할된다. 퍼지기체 공급구(90)를 통해서 주입되는 퍼지기체는 하부기체배출구(88)를 통하여 배출되고, 기체 포커스 링(70)을 통해서 주입되는 공정기체는 상부기체배출구(87)를 통하여 배출된다.In the gas discharge port 80, the blocking film 85 is horizontally installed in the middle of the gas discharge port 80 so that the process gas and the purge gas are not mixed with each other. Accordingly, the gas outlet 80 is divided into a lower gas outlet 88 and an upper gas outlet 87. The purge gas injected through the purge gas supply port 90 is discharged through the lower gas discharge port 88, and the process gas injected through the gas focus ring 70 is discharged through the upper gas discharge port 87.

기체배출구(80)는 차단막(85)에 의하여 상하 공간으로 분리되기는 하지만 완전히 분리되는 것이 아니라 차단막(85)의 끝부분에서는 이러한 상하공간이 연결되도록 설치된다. 기체배출구(80)로 들어온 공정기체 및 퍼지기체는 펌핑라인(82)을 통하여 외부로 배출된다.The gas discharge port 80 is separated into the upper and lower spaces by the blocking membrane 85 but is not completely separated, but is installed to connect the upper and lower spaces at the end of the blocking membrane 85. Process gas and purge gas entering the gas discharge port 80 is discharged to the outside through the pumping line (82).

하부기체배출구(88)는 두 개의 환형 하부분할막(84)의 수평 분할에 의하여 세 개의 공간(88a, 88b, 88c)으로 나눠진다. 하부분할막(84)은 차단막(85)보다는 큰 내경을 가진다. 이 공간들(88a, 88b, 88c)은 위로 갈수록 높이가 점점 높아진다. 하부기체배출구(88)가 분할되지 않으면 이 부분에 퍼지기체가 한꺼번에 몰려들어 와류가 생기게 된다. 그러나, 이렇게 공간들(88a, 88b, 88c)이 있으면 아래의 공간으로부터 퍼지기체가 순차적으로 조금씩 배출되기 때문에 와류가 생기지 않게 된다. 상부기체배출구(87)도 마찬가지로 이유로 두 개의 환형 상부분할막(86)의 수평 분할에 의하여 세 개의 공간(87a, 87b, 87c)으로 나뉘어지며, 이 공간들(87a, 87b, 87c)은 위에서 아래로 갈수록 그 높이가 점점 높아진다. 상부분할막(87) 역시 차단막(85)보다는 큰 내경을 가진다.The lower gas outlet 88 is divided into three spaces 88a, 88b, and 88c by the horizontal division of the two annular lower segmental membranes 84. The lower partition film 84 has a larger inner diameter than the blocking film 85. These spaces 88a, 88b, 88c become higher in height as they go upwards. If the lower gas outlet 88 is not divided, the purge gas is gathered in this portion at once, causing vortices. However, if there are spaces 88a, 88b, and 88c, vortices are not generated because the purge gas is sequentially discharged little by little from the space below. The upper gas outlet 87 is likewise divided into three spaces 87a, 87b and 87c by the horizontal division of the two annular upper dividing layers 86, and these spaces 87a, 87b and 87c are from top to bottom. The height gets higher as you go. The upper dividing film 87 also has a larger inner diameter than the blocking film 85.

기체공급라인(74)을 통하여 기체 포커스 링(70)에 공정기체를 주입하면, 공저기체는 분사공(72)을 통하여 웨이퍼 지지대(50) 주위로부터 웨이퍼 지지대(50)의상부공간 중심부로 분사된다. 웨이퍼 지지대(50)의 상부공간 중심부로 분사된 공정기체는 벨자히터(40)에 의하여 가열되고 있는 석영돔(20)에 부딪혀서 열분해되면서 웨이퍼 지지대(50) 상부공간에 골고루 분포된다. 따라서, 웨이퍼(60)가 대구경일지라도 웨이퍼(60) 전면에 균일한 화학기상증착이 일어난다.When the process gas is injected into the gas focus ring 70 through the gas supply line 74, the co-gas is injected from the periphery of the wafer support 50 to the center of the upper space of the wafer support 50 through the injection hole 72. . The process gas injected into the center of the upper space of the wafer support 50 is uniformly distributed in the upper space of the wafer support 50 while being thermally decomposed by hitting the quartz dome 20 being heated by the bell heater. Therefore, even if the wafer 60 is large in diameter, uniform chemical vapor deposition occurs on the entire surface of the wafer 60.

화학기상증착에 관여하지 못한 잔류 공정기체는 기체배출구(80)를 통하여 외부로 배출된다. 이 때, 공정기체가 반응챔버(10)의 아랫부분으로 내려오지 못하도록 퍼지기체 공급구(90)를 통하여 퍼지기체를 적절한 유속으로 공급한다. 물론, 공정기체의 압력에 의하여 퍼지기체도 반응챔버(10)의 윗부분으로 올라갈 수 없도록해야 한다.Residual process gas not involved in chemical vapor deposition is discharged to the outside through the gas outlet (80). At this time, the purge gas is supplied at an appropriate flow rate through the purge gas supply port 90 to prevent the process gas from descending to the lower portion of the reaction chamber 10. Of course, purge gas should not be able to rise to the upper portion of the reaction chamber 10 by the pressure of the process gas.

공정기체는 퍼지기체의 공급에 의하여 웨이퍼 지지대(50)의 하부공간으로 내려오지 못하므로, 웨이퍼 지지대(50), 지지축(52) 등 반응챔버(10)의 아랫부분 내벽에 박막이 증착되는 것이 방지된다. 퍼지기체 역시 웨이퍼 지지대(50) 상부공간으로 올라갈 수 없으므로 화학기상증착에 영향을 미치지 않게 되어 퍼지기체에 의하여 박막의 균일도 및 증착속도가 영향을 받는 현상은 나타나지 않는다. 차단막(85)의 설치에 의하여 이러한 효과들은 더욱 크게 나타난다.Since the process gas cannot be lowered to the lower space of the wafer supporter 50 by the supply of the purge gas, it is possible to deposit a thin film on the inner wall of the lower part of the reaction chamber 10 such as the wafer supporter 50 and the support shaft 52. Is prevented. Since the purge gas cannot rise to the upper space of the wafer supporter 50, the purge gas does not affect chemical vapor deposition, and thus the uniformity and deposition rate of the thin film are not affected by the purge gas. By installing the blocking film 85, these effects are even greater.

상술한 바와 같은 본 발명에 따른 CVD 장치에 의하면, 공정기체는 퍼지가스의 압력에 의하여 반응챔버(10)의 하부공간으로 내려오지 못하므로 공정기체가 반응챔버(10)의 하부공간에 증착되는 것을 방지할 수 있다. 따라서, 파티클 소스를최소화 시킬 수 있을 뿐만 아니라 장비의 정검주기를 연장시킬 수 있다. 또한, 퍼지가스 역시 공정기체의 압력에 의하여 반응챔버(10)의 상부공간으로 올라가지 못하므로 퍼지기체에 의해 CVD 공정이 영향을 받는 일은 없다.According to the CVD apparatus according to the present invention as described above, since the process gas is not lowered to the lower space of the reaction chamber 10 by the pressure of the purge gas, the process gas is deposited in the lower space of the reaction chamber 10. You can prevent it. Thus, the particle source can be minimized, as well as the equipment's inspection cycle can be extended. In addition, since the purge gas does not rise to the upper space of the reaction chamber 10 due to the pressure of the process gas, the CVD process is not affected by the purge gas.

차단막(85)을 설치하여 2단 펌핑 구조를 취함으로써 공정기체 및 퍼지기체의 혼합에 의한 와류 발생이 방지된다. 만약 기체배출구(80)에서 와류가 발생하면 기체가 다소 정체하게 되면 웨이퍼 지지대(50)에 설치된 메인히터의 열기에 의하여 버닝(burning) 현상이 나타나게 된다. 그리고, 상부분할막(86) 및 하부분할막(84)에 의하여 형성된 공간에 의하여 공정기체 및 퍼지기체 각각이 여러 부분에서 조금씩 배출되기 때문에 이러한 와류현상은 더욱 감소하게 된다. 배출량은 차단막(80) 쪽으로 갈수록 점점 더 많아진다.By installing the blocking film 85 to take a two-stage pumping structure, vortex generation due to mixing of the process gas and the purge gas is prevented. If the vortex occurs at the gas outlet 80, when the gas is stagnated somewhat, a burning phenomenon occurs due to the heat of the main heater installed in the wafer support 50. In addition, since the process gas and the purge gas are each slightly discharged from the various portions by the space formed by the upper partition 86 and the lower partition 84, the vortex phenomenon is further reduced. Emissions increase more and more toward the barrier 80.

본 발명은 상기 실시예에만 한정되지 않으며, 본 발명의 기술적 사상 내에서 당 분야에서 통상의 지식을 가진 자에 의해 많은 변형이 가능함은 명백하다.The present invention is not limited to the above embodiments, and it is apparent that many modifications are possible by those skilled in the art within the technical spirit of the present invention.

Claims (6)

화학기상증착 공정이 진행되는 반응챔버;A reaction chamber in which a chemical vapor deposition process is performed; 상기 반응챔버 내부에 설치되며 웨이퍼가 안착되어지는 웨이퍼 지지대;A wafer support installed in the reaction chamber and on which a wafer is seated; 상기 웨이퍼 지지대 주위로부터 상기 웨이퍼 지지대의 상부공간 중심부로 공정기체를 분사하도록 상기 반응챔버 내측면에 설치되는 기체 포커스 링;A gas focus ring installed on an inner surface of the reaction chamber to inject a process gas from the periphery of the wafer support to the center of the upper space of the wafer support; 상기 반응챔버 내부로 퍼지기체를 공급하기 위하여 상기 반응챔버 저면에 설치되는 퍼지기체 공급구;A purge gas supply port provided at a bottom of the reaction chamber to supply a purge gas into the reaction chamber; 상기 기체 포커스 링을 통하여 분사되는 공정기체 및 상기 퍼지기체 공급구를 통해서 공급되는 퍼지기체를 배출시키기 위하여, 상기 기체 포커스 링보다는 하부에 위치하고 상기 반응챔버의 저면으로부터 소정의 높이에 위치하도록, 상기 반응챔버의 측벽을 따라 수평한 환형링 형태로 설치되는 기체배출구;In order to discharge the process gas injected through the gas focus ring and the purge gas supplied through the purge gas supply port, the reaction gas is positioned below the gas focus ring and positioned at a predetermined height from the bottom of the reaction chamber. A gas outlet installed in a horizontal annular ring shape along the side wall of the chamber; 상기 기체배출구와 진공펌프를 서로 연결하는 하나의 펌핑라인;One pumping line connecting the gas discharge port and the vacuum pump to each other; 상기 기체배출구를 통해서 배출되는 공정기체와 퍼지기체가 상기 기체배출구 입구 부위에서 서로 혼합되지 않도록 상기 기체배출구 중간부분에 위치하도록 상기 기체배출구에 환형으로 수평하게 설치되는 차단막;A barrier membrane horizontally installed in the gas outlet so that the process gas and the purge gas discharged through the gas outlet are located at the middle of the gas outlet so that they are not mixed with each other at the gas outlet inlet; 상기 차단막 하부의 기체배출구 부분을 복수개의 공간으로 나눠지도록 수평분할하며 상기 차단막보다 더 큰 내경을 가지는 복수개의 환형 하부분할막;A plurality of annular lower subdivision membranes which are horizontally divided to divide the gas outlet portion of the lower portion of the barrier layer into a plurality of spaces and have a larger inner diameter than the barrier layer; 상기 차단막 상부의 기체배출구 부분을 복수개의 공간으로 나눠지도록 수평분할하며 상기 차단막보다 더 큰 내경을 가지는 복수개의 환형 상부분할막; 을 구비하는 것을 특징으로 하는 CVD 장치.A plurality of annular upper dividing membranes which are horizontally divided to divide the gas outlet portion of the upper portion of the barrier layer into a plurality of spaces and have a larger inner diameter than the barrier layer; CVD apparatus comprising a. 제1항에 있어서, 상기 반응챔버는 상부가 석영돔으로 이루어지고, 상기 석영돔 외측에는 상기 석영돔을 덮는 벨자히터가 설치되는 것을 특징으로 하는 CVD 장치.The CVD apparatus according to claim 1, wherein the reaction chamber is formed of a quartz dome on an upper portion of the reaction chamber, and a bell jar heater is installed outside the quartz dome to cover the quartz dome. 제1항에 있어서, 상기 반응챔버는 상기 웨이퍼 지지대가 1개 설치되어 웨이퍼가 한장씩 장입되는 매엽식 반응챔버인 것을 특징으로 하는 CVD 장치.The CVD apparatus according to claim 1, wherein the reaction chamber is a single-sheet reaction chamber in which one wafer support is installed and one wafer is charged. 제1항에 있어서, 상기 기체배출구가 상기 웨이퍼 지지대와 같은 높이에 설치되는 것을 특징으로 하는 CVD 장치.The CVD apparatus according to claim 1, wherein the gas discharge port is provided at the same height as the wafer support. 제1항에 있어서, 상기 하부분할막에 의하여 형성되는 복수개의 공간은 아래에서 위로 갈수록 그 높이가 점점 더 높아지고, 상기 상부분할막에 의하여 형성되는 복수개의 공간은 위에서 아래로 갈수록 그 높이가 점점 더 높아지는 것을 특징으로 하는 CVD 장치.The method of claim 1, wherein the height of the plurality of spaces formed by the lower portion of the subdividing film becomes higher and higher, and the height of the plurality of spaces formed by the upper portion of the dividing film gradually increases from the top to the bottom. CVD apparatus, characterized in that high. 제1항에 있어서, 상기 웨이퍼 지지대 내부에 히터가 설치되어 있는 것을 특징으로 하는 CVD 장치.The CVD apparatus according to claim 1, wherein a heater is provided inside the wafer support.
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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05175130A (en) * 1991-12-20 1993-07-13 Nippon Steel Corp Plasma cvd apparatus
JPH1140553A (en) * 1997-07-16 1999-02-12 Matsushita Electric Ind Co Ltd Plasma CVD method and apparatus
US6103304A (en) * 1996-11-15 2000-08-15 Anelva Corporation Chemical vapor deposition apparatus
US6223684B1 (en) * 1997-07-07 2001-05-01 Canon Kabushiki Kaisha Film deposition apparatus

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05175130A (en) * 1991-12-20 1993-07-13 Nippon Steel Corp Plasma cvd apparatus
US6103304A (en) * 1996-11-15 2000-08-15 Anelva Corporation Chemical vapor deposition apparatus
US6223684B1 (en) * 1997-07-07 2001-05-01 Canon Kabushiki Kaisha Film deposition apparatus
JPH1140553A (en) * 1997-07-16 1999-02-12 Matsushita Electric Ind Co Ltd Plasma CVD method and apparatus

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