KR950004149Y1 - Vapor deposition apparatus - Google Patents

Vapor deposition apparatus Download PDF

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KR950004149Y1
KR950004149Y1 KR92016082U KR920016082U KR950004149Y1 KR 950004149 Y1 KR950004149 Y1 KR 950004149Y1 KR 92016082 U KR92016082 U KR 92016082U KR 920016082 U KR920016082 U KR 920016082U KR 950004149 Y1 KR950004149 Y1 KR 950004149Y1
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valve
flow controller
quartz tube
tube
trap
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KR92016082U
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KR940006471U (en
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서일웅
김태환
송정동
정기정
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김주용
현대전자산업 주식회사
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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
    • C23C16/52Controlling or regulating the coating process
    • 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

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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)

Abstract

내용 없음.No content.

Description

기상 증착 장치Vapor deposition apparatus

제1도는 일반적인 기상 증착의 개략설명 구조도.1 is a schematic structural diagram of general vapor deposition.

제2도는 제1도의 구체적인 장치도.2 is a detailed device diagram of FIG.

제3도는 본 고안의 장치도.3 is a device diagram of the present invention.

본 고안은 테트라에톡시 실란(TEOS)개스를 사용하여 SiO2필름을 증착시키는 반도체 기상증착장치에 관한 것이다.The present invention relates to a semiconductor vapor deposition apparatus for depositing SiO 2 film using tetraethoxy silane (TEOS) gas.

CVD(Chemical Vapour Deposition)는 화학반응을 수반하는 기상성장을 뜻하고, 기상속의 열분해, 가수분해, 산화등의 화학반응을 이용하여 기판에 단결정반도체(에피텍셜성장)나 절연막(SiO2, Si3N4, Al2O3)을 성장시키는 방법이다. 이중 SiO2막을 형성하는 과정을 제1도를 들어 설명하면 60-70℃를 유지하는 항온기(10)내에 테트라에톡시실란(이하 TEOS 라함)을 증발가능케하는 용기(11)를 수장하고, 용기(11)출구에는 캐리어개스를 공급하는 공급관(12)과 연결되고 이는 주입관(13)을 통해 석영관(14)으로 공급토록 이루어진다.CVD (Chemical Vapor Deposition) means gas phase growth accompanied by chemical reaction, and single crystal semiconductor (epitaxial growth) or insulating film (SiO 2 , Si 3 ) is used on the substrate by using chemical reaction such as pyrolysis, hydrolysis and oxidation in the gas phase. N 4 , Al 2 O 3 ) to grow. Referring to FIG. 1, a process of forming a SiO 2 film is carried out, and a container 11 for evaporating tetraethoxysilane (hereinafter referred to as TEOS) in a thermostat 10 maintained at 60-70 ° C. 11) The outlet is connected to the supply pipe 12 for supplying the carrier gas, which is made to be supplied to the quartz tube 14 through the injection tube (13).

석영관(14)의 주입관(13)외주에는 히터(15)가 길이방향에 따라 피복된다.The heater 15 is coated along the longitudinal direction on the outer circumference of the injection tube 13 of the quartz tube 14.

석영관(14)내에는 서셉터(16)에 증착할 시료(17)가 놓여지고, 석영관(14)외주에는 600-700℃로 가열되는 전기로(18)가 설치된다. 석영관(14)출구에는 석영관(14)내를 진공으로 만드는 진공펌프와 연결된다.In the quartz tube 14, a sample 17 to be deposited on the susceptor 16 is placed, and an electric furnace 18 heated to 600-700 ° C is provided on the outer circumference of the quartz tube 14. The outlet of the quartz tube 14 is connected to a vacuum pump that vacuums the inside of the quartz tube 14.

이를 좀더 구체적으로 제2도에 도시하면, 쳄버인 석영관(14) 외주에는 전기로(18)를 감싸고, 석영관(14) 입구에는 주입관(13)과 공급관(12)이 각각 연결되고, 출구에는 벨로즈부(20)가 연결된다. 공급관(12)은 질소개스(N2)가 제1보조밸브(V1), 제1유량제어기(F1) 및 제2유량제어기(F2)로 분산되어 선택작동되어 석영관(14)에 공급되도록 이루어지며, 제1유량제어기(F1) 및 제2제어유량기(F2)의 각 주입출력부에는 제1밸브(V10, V11) 및 제2밸브(V20, V21)가 각각 연결된다. 주입관(13)은 항기온(10)내의 용기(11)에 있는 TEOS를 석영관(14)으로 공급하고, 주입관(13) 외주에는 길이방향으로 히터(15)가 피복된다. 주입관(13)은 제3유량제어기(F3)에 의해 유량이 제어되고, 제3밸브(V30, V31)에 의해 개폐되며, TEOS는 집수기에서 TEOS 공급밸브(V42)를 통해 TEOS 밸브(V40, V41)에 의해 공급을 제어한다. 또한 상기 질소개스(N2)는 제2보조밸브(V2)에 의해 제3유량제어기(F3) 입구와 연결되고, 제3유량제어기(F3)입출력부에는 바이패스밸브(V6)가 연결된다.More specifically, as shown in FIG. 2, the outer circumference of the quartz tube 14, which is a chamber, surrounds the electric furnace 18, and the inlet tube 13 and the supply tube 12 are connected to the inlet of the quartz tube 14, respectively. The bellows portion 20 is connected to the outlet. The supply pipe 12 is nitrogen gas (N 2 ) is made to be distributed to the first auxiliary valve (V1), the first flow controller (F1) and the second flow controller (F2) is selectively operated to be supplied to the quartz pipe (14). First injection valves V10 and V11 and second valves V20 and V21 are respectively connected to the injection output units of the first flow controller F1 and the second control flow controller F2. The injection tube 13 supplies TEOS in the container 11 in the constant temperature 10 to the quartz tube 14, and the heater 15 is coated in the longitudinal direction on the outer circumference of the injection tube 13. The flow rate of the injection pipe 13 is controlled by the third flow controller F3, opened and closed by the third valves V30 and V31, and the TEOS is connected to the TEOS valve V40 through the TEOS supply valve V42 in the water collector. , V41) to control the supply. In addition, the nitrogen gas (N 2 ) is connected to the inlet of the third flow controller (F3) by the second auxiliary valve (V 2 ), the bypass valve (V6) is connected to the input and output of the third flow controller (F3). .

상기 밸로즈부(20) 출구에는 수냉트랩(31) 및 미립자트랩(32)이 차례로 직결되는 필터부(30)가 설치되고, 필터부(30) 출력단에는 메인게이트밸(V50)와 소프트스타트밸브(V51)가 나란해 접속된 상태의 밸브부(50)가 연결되며, 밸브부(50)는 진공펌프부(40)에 의해 배출부와 연결되도록 이루어진다.The outlet of the bellows portion 20 is provided with a filter portion 30 which is directly connected to the water cooling trap 31 and the particulate trap 32, the main gate valve (V50) and the soft start valve at the output end of the filter portion 30 The valve unit 50 in a state in which V51 is connected in parallel is connected, and the valve unit 50 is connected to the discharge unit by the vacuum pump unit 40.

상기 제3유량제어부(F3)출구에는 추가로 제3보조밸브(V3)가 연결되어 진공밸브(40) 출력단과 연결되며, 제4유량재어기(F4)는 별도의 질소개스(N2)를 상기 제3보조밸브(V3) 출력단과 연결시킨다. 제3유량제어기(F3) 출력단은 또한 배출밸브(V4, V5)를 거쳐 밸브부(50) 출력단과 연결된다.A third auxiliary valve (V3) is further connected to the outlet of the third flow control unit (F3) is connected to the output end of the vacuum valve 40, the fourth flow controller (F4) is a separate nitrogen gas (N 2 ) It is connected to the output terminal of the third auxiliary valve (V3). The output end of the third flow controller F3 is also connected to the output end of the valve unit 50 via the discharge valves V4 and V5.

이때 제1제어유량제어기(F1)는 1 SLM(Spuare liter per minutes), 제2제어유량제어기(F2)는 20 SLM(Square liter per minutes), 제3제어유량제어기(F3)는 200 SCCM(Square CC per minutes)로 설계되어 사용된다. 즉, 제1유량제어기(F1)는 석영관(14)내에 초기 캐리어 개스인 질소개스(N2)를 적량조절하여 공급하고, 제2유량제어기(F2)는 증착후 증착된 웨이퍼등의 기판을 배출키 위해 대기압을 만들기 위한 것이며, 제3유량제어기(F3)는 TEOS의 공급량을 제어한다. 이때 바이패스밸브(V6)는 초과공급되거나 하여 잔류하는 잔여개스를 벤트시킨다. 제3보조밸브(V3)는 진공펌프부(40)의 출력단인 배출부로 초과 캐리어개스(V2)등을 배출시키며 배출밸브(V4, V5)는 진공펌프부(40)의 입력단돠 연결되어 질소개스(N2)의 배출을 용이하게 한다. 밸로즈부(20)는 진공시 배출되는 파티클등의 이동속도를 감소시키며, 수냉트랩(31)은 가열된 공기를 냉각시키고, 이어 미립자트랩(32)에서 미립자를 걸러낸다.In this case, the first control flow controller F1 is 1 SLM (Spuare liter per minutes), the second control flow controller F2 is 20 SLM (Square liter per minutes), and the third control flow controller (F3) is 200 SCCM (Square). CC per minutes). That is, the first flow controller F1 adjusts and supplies nitrogen gas N 2 , which is an initial carrier gas, in the quartz tube 14, and the second flow controller F2 supplies a substrate such as a wafer deposited after deposition. In order to generate an atmospheric pressure to discharge, the third flow controller F3 controls the supply amount of TEOS. At this time, the bypass valve V6 is oversupplied to vent the remaining gas. The third auxiliary valve V3 discharges the excess carrier gas V2 to the discharge part which is the output end of the vacuum pump part 40, and the discharge valves V4 and V5 are connected to the input end of the vacuum pump part 40 to nitrogen gas. Facilitates the discharge of (N 2 ). The bellows portion 20 reduces the moving speed of particles and the like discharged during vacuum, and the water cooling trap 31 cools the heated air, and then filters the fine particles from the fine particle trap 32.

메닌게이트밸브(V50)는 진공펌프부(40)가 진공(1 torr)을 만들때 진공펌프부(40)와의 연결을 제어하고, 소프트 스타트밸브(V51)는 메인게이트밸브(V50) 작동이전에 석영관(14)내의 진공을 서서히 만들도록 흡입량을 서서히 증대시키는 밸브이다. 즉, 소프트 스타트밸브(V51)가 서서히 진공을 일정레벨(1 torr)로 만들어주면 소프트 스타트밸브(V51)가 닫히고 메인게이트밸브(V50)와 연결되어 석영관(14) 내부의 초기 진공화에 따른 시료의 이탈등을 방지케 한다.The menin gate valve V50 controls the connection with the vacuum pump 40 when the vacuum pump 40 makes a vacuum (1 torr), and the soft start valve (V51) before the main gate valve V50 operates. It is a valve that gradually increases the suction amount so as to gradually create a vacuum in the quartz tube 14. That is, when the soft start valve V51 gradually makes the vacuum to a predetermined level (1 torr), the soft start valve V51 is closed and connected to the main gate valve V50, resulting in an initial vacuum inside the quartz tube 14. This prevents the sample from coming off.

이 경우 TEOS 개스를 공급하는 개스주입관(13)의 길이가 상당히 길어서 개스주입관(13)에서 기화개스인 TEOS가 응결될수 있는 확율이 많고, 개스주입관(13)을 가열시키기 위한 가열테이프등의 히터(15) 길이가 너무 길어 잦은 고장이 발생하였으며 복잡한 공급관(12) 및 주입관(13) 구성으로 인한 유지보수가 어려워 불합리성이 노출되었고, 제3유량제어기(F3)도 자체 히팅이 불가능하여 유량제어에 어려움이 발생되었다.In this case, since the length of the gas injection pipe 13 for supplying the TEOS gas is quite long, there is a high probability of condensation of the vaporized gas TEOS in the gas injection pipe 13, and a heating tape for heating the gas injection pipe 13. The heater (15) of the length is too long to cause frequent breakdowns, difficult maintenance due to the complex supply pipe 12 and the injection pipe 13 configuration exposed irrationality, the third flow controller (F3) is also unable to heat itself Difficulties occurred in flow control.

또한 진공후 대기압으로 만들때 미반응 생성물이 질소개스 공급에 의한 와류 현상으로 웨이퍼기판과의 접촉을 최소화 할수 있는 어떤 수단이 없어서 증착이 끝단후 잦은 파티클(PARTICLE) 및 스포트(SPOT) 발생의 원인이 되어 왔으며, 공정 진행시 석영관(14) 출구쪽으로 불가하게 사용되는 수냉트랩(31)을 적절히 제어하지 못하여 과도한 냉각으로 인한 TEOS의 미반응으로 여러가지 부산물을 형성하여 웨이퍼기판을 손상시키는 문제점을 야기시켜 왔다.In addition, when the atmospheric pressure after vacuum, the unreacted product is a vortex caused by nitrogen gas supply, and there is no means to minimize contact with the wafer substrate, which causes frequent particles and spots after deposition. During the process, the water cooling trap 31, which is impossible to use toward the exit of the quartz tube 14, cannot be properly controlled, and various problems are formed due to the unreaction of TEOS due to excessive cooling, which causes damage to the wafer substrate. come.

본 고안은 이를 해결코자 하는 것로 석영관의 주입관 길이를 최소화하여 주입관 내의 응결을 줄이고 제3유량제어기를 자체 히팅이 가능한 것으로 사용하였으며, 진공작업후 와류를 최소화하기 위하여 추가 소프트 스타트 밸브를 장착하여 백필(BACK FILL)용 질소개스(N2)가 흐르게될때 반응물과 웨이퍼기판의 접촉을 가능한한 줄일수 있도록 함을 특징으로 한다.The present invention solves this problem by minimizing the length of the injection tube of the quartz tube to reduce condensation in the injection tube and to enable the third flow controller to self-heat. An additional soft start valve is provided to minimize the vortex after the vacuum operation. When the nitrogen gas (N 2 ) for the back fill (flow) flows by the mounting it is characterized in that to reduce the contact between the reactant and the wafer substrate as possible.

즉, 제1 내지 제4유량제어기, 석영관, 진공펌프부, 밸브부, TEOS 공급용기, 공급관, 주입관 및 바이패스밸브로 이루어지는 반도체 기상증착 장치에 있어서, 제3유량제어기에 히터를 내장하고 바이패스밸브를 없애며, 제3밸브를 통과한 주입관을 공급관에 직결하며, 밸브부는 석영관 출구와 직결되며 밸브부에는 추가소프트 스타트밸브를 소프트스타트 밸브와 병렬로 추가접속하고, 제4유량제어기 출력단과 밸브부 출력단은 트랩이 연속 배열된 멀티트랩과 연결된 것이다.That is, in the semiconductor vapor deposition apparatus including the first to fourth flow controllers, quartz tubes, vacuum pumps, valves, TEOS supply containers, supply tubes, injection tubes, and bypass valves, the third flow controller includes a heater. Remove the bypass valve, connect the injection pipe passing through the third valve directly to the supply pipe, the valve part is directly connected to the outlet of the quartz tube, and additional soft start valve is connected to the valve part in parallel with the soft start valve, and the fourth flow controller The output stage and the valve output stage are connected to a multi-trap in which traps are continuously arranged.

이하 도면을 참조하여 상세히 설명하면 종래와 동일한 구성은 동일부호를 부기하되 동일한 명칭에 구조가 다른것은 부호에 프라임을 넣어 표기한다.DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the same components as in the related art will be denoted by the same reference numerals, but the structures having the same names but with different structures will be denoted by putting prime marks in the symbols.

본 고안은 제1 내지 제4유량제어기(F1∼F4), 석영관(14), 진공펌프부(40), 밸브부(50), TEOS 공급용기(11), 공급관(12), 주입관(13) 및 바이패스밸브(V6)로 이루어지는 반도체 기상증착 장치에 있어서, 제3유량제어기(F3')에 히터(100)를 내장하고, 제3밸브(V3)를 통과한 주입관(13)을 공급관(12)에 직결하며, 밸브부(50')는 석영관(14)출구와 직결되며 밸브부(50')에는 추가 소프트 스타트밸브(V53)를 소프트 스타트밸브(V51)와 병렬로 추가접속하고, 제4유량제어기(F4) 출력단과 밸브부(50) 출력단은 트랩이 연속 배열된 멀티트랩(200)과 연결된 것이다.The present invention is the first to fourth flow controllers (F1 to F4), quartz tube 14, vacuum pump 40, valve unit 50, TEOS supply container 11, supply tube 12, injection tube ( In the semiconductor vapor deposition apparatus comprising a 13) and a bypass valve V6, a heater 100 is built into the third flow controller F3 'and an injection pipe 13 passing through the third valve V3 is connected. Directly connected to supply pipe 12, valve portion 50 'is directly connected to the outlet of quartz tube 14, and additional soft start valve V53 is connected to valve portion 50' in parallel with soft start valve V51. The fourth flow controller F4 output terminal and the valve unit 50 output terminal are connected to the multi-trap 200 in which the traps are continuously arranged.

본 고안은 사용할 때에는 TEOS가 채워지도록 집수기, TEOS 공급밸브(V42), TEOS 밸브(V41)를 통해 용기(11)에 TEOS를 공급하고, 항온기(10)를 60-70℃로 가온시켜 기화되도록 한다. 이상태에서 제3유량제어기(F3') 및 제3밸브(V31) 작동에 의해 석영관(14)으로 제공된다. 물론 석영관(14)내부에는 제1도에 보인바 있는 서셉터(16)로 시료(17)가 놓여지고, 진공펌프부(40)에 의해 적정진공을 유지한다. 또한 캐리어 질소개스(N2)도 제1유량제어기(F1)를 통해 공급관(12)으로 제공된다. 이때 TEOS 개스는 공급관(12)과 직결되어 석영관(14)에 주입되므로 그만큼 주입관(13)의 길이가 짧아지게 되고, 그에따라 히터(15)에 의한 유지비가 줄어들고 내부 응결의 부작용도 그만큼 감소된다.The present invention supplies TEOS to the container 11 through a water collector, a TEOS supply valve (V42), and a TEOS valve (V41) so that the TEOS is filled, and the thermostat 10 is heated to 60-70 ° C. to vaporize it. do. In this state, the third flow controller F3 ′ and the third valve V31 are provided to the quartz tube 14. Of course, the sample 17 is placed inside the quartz tube 14 by the susceptor 16 as shown in FIG. 1, and the proper vacuum is maintained by the vacuum pump 40. As shown in FIG. Carrier nitrogen gas (N 2 ) is also provided to the supply pipe (12) through the first flow controller (F1). At this time, since the TEOS gas is directly connected to the supply pipe 12 and injected into the quartz pipe 14, the length of the injection pipe 13 is shortened accordingly, thereby reducing the maintenance cost by the heater 15 and reducing the side effects of internal condensation. do.

또한 챔버인 석영관(14)의 출구는 밸브부(50')를 통해 멀티트랩(200)과 연결되고 멀티트랩(200)에서 미반응 개스 및 파티클 등의 다단의 트랩에서 제거되므로 종래의 필터부(30)처럼 수냉트랩(31) 및 미립자트랩(32)의 2부분으로 구성할 필요가 없어 설치가 용이하다. 또한 멀티트랩(200)을 설치함으로써 벨로즈부(20)가 없어도 트랩기능을 수행케되어 벨로즈부(20)에 의한 응결을 예방할수 있다.In addition, the outlet of the quartz tube 14, which is a chamber, is connected to the multi-trap 200 through the valve unit 50 'and is removed from the multi-stage trap such as unreacted gas and particles in the multi-trap 200, and thus, the conventional filter unit. Like 30, the water cooling trap 31 and the particulate trap 32 do not need to be composed of two parts, so that the installation is easy. In addition, by installing the multi-trap 200 it is possible to prevent the condensation by the bellows portion 20 by performing the trap function even without the bellows portion 20.

이와같이 증착하는 공정을 완료하고 석영관(14)을 대기압으로 만들어 증착된 시료를 배출코자 할때에는 유량이 큰 제2유량제어기(F)를 통해 공급한다. 그러나 본고안은 제2유량제어기(F2)를 통한 공급시에 대응하여 추가 소프트 스타트밸브(V53)를 먼저 작동시킨다.When the deposition process is completed as described above and the quartz tube 14 is made at atmospheric pressure to discharge the deposited sample, it is supplied through the second flow controller F having a large flow rate. However, the present proposal first operates the additional soft start valve V53 in response to the supply through the second flow controller F2.

이러한 소프트 스타트밸브(V53)는 관사이즈가 작아 서서히 대기압으로 만들게 작동되므로, 순간적으로 제2유량제어기(F2)로부터 공급되는 질소개스에 의해 웨이퍼시료(17)가 서셉터(16)에서 떨어지거나 미반응된 기체 및 미립자와의 충돌에 의한 표면손상을 막을수 있다.Since the soft start valve V53 has a small pipe size and is operated to gradually bring it to atmospheric pressure, the wafer sample 17 is dropped from the susceptor 16 by a nitrogen gas supplied from the second flow controller F2 at an instant. It can prevent surface damage by collision with reacted gas and fine particles.

Claims (1)

제1 내지 제4유량제어기(F1∼F4), 석영관(14), 진공펌프부(40), 밸브부(50), TEOS 공급용기(11), 공급관(12), 주입관(13) 및 바이패스밸브(V6)로 이루어지는 반도체기상증착 장치에 있어서, 제3유량제어기(F3')에 히터(100)를 내장하고, 제3밸브(V3)를 통과한 주입관(13)을 공급관(12)에 직결하며, 밸브부(50')는 석영관(14) 출구와 직결되며 밸브부(50')에는 추가 소프트 스타트밸브(V53)를 소프트 스타트밸브(V51)와 병렬로 추가접속하고, 제4유량제어기(F4) 출력단과 밸브부(50) 출력단은 트랩이 연속 배열된 멀티트랩(200)과 연결됨을 특징으로 하는 반도체 기상증착 장치.First to fourth flow controllers (F1 to F4), quartz tube 14, vacuum pump portion 40, valve portion 50, TEOS supply container 11, supply tube 12, injection tube 13 and In the semiconductor vapor deposition apparatus comprising the bypass valve V6, the heater 100 is incorporated into the third flow controller F3 ', and the injection pipe 13 passing through the third valve V3 is supplied to the supply pipe 12. Valve part 50 'is directly connected to the quartz tube 14 outlet, and an additional soft start valve V53 is connected to the valve part 50' in parallel with the soft start valve V51. 4 flow controller (F4) output terminal and the valve unit 50 output terminal is a semiconductor vapor deposition apparatus, characterized in that the trap is connected to the multi-trap 200 is arranged continuously.
KR92016082U 1992-08-26 1992-08-26 Vapor deposition apparatus KR950004149Y1 (en)

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