WO2020179575A1 - Film-forming apparatus and material gas feeding method - Google Patents

Film-forming apparatus and material gas feeding method Download PDF

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Publication number
WO2020179575A1
WO2020179575A1 PCT/JP2020/007693 JP2020007693W WO2020179575A1 WO 2020179575 A1 WO2020179575 A1 WO 2020179575A1 JP 2020007693 W JP2020007693 W JP 2020007693W WO 2020179575 A1 WO2020179575 A1 WO 2020179575A1
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Prior art keywords
raw material
pressure
processing container
material tank
forming apparatus
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PCT/JP2020/007693
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French (fr)
Japanese (ja)
Inventor
津田 栄之輔
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東京エレクトロン株式会社
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Publication of WO2020179575A1 publication Critical patent/WO2020179575A1/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
    • C23C16/448Chemical 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 generating reactive gas streams, e.g. by evaporation or sublimation of precursor materials

Definitions

  • the present disclosure relates to a film forming apparatus and a raw material gas supply method.
  • Patent Document 1 discloses a ruthenium (Ru) film forming apparatus, which includes a film forming apparatus main body that performs a film forming process on a semiconductor wafer (hereinafter referred to as “wafer”), and a film forming apparatus main body.
  • a film forming apparatus main body that performs a film forming process on a semiconductor wafer (hereinafter referred to as “wafer”)
  • a film forming apparatus main body an apparatus having a raw material gas supply system for supplying the raw material gas is disclosed.
  • the raw material gas supply system of the film forming apparatus has a raw material tank for storing Ru 3 (CO) 12 as a solid raw material, one end connected to the raw material tank, and the other end connected to a processing container of the main body of the film forming apparatus. And a raw material passage.
  • the processing container has a mounting table on which a wafer is mounted inside, and is connected to a vacuum exhaust system for maintaining a reduced pressure atmosphere in the processing container. Further, in the film forming apparatus, in order to vaporize a large amount of the raw material gas having a low vapor pressure, the pressure in the processing container is lowered and the pressure in the raw material tank is lowered.
  • the technique according to the present disclosure provides a constant supply of a raw material gas to a processing container of a film forming apparatus that forms a predetermined film using a raw material gas generated by vaporizing the raw material, regardless of the pressure inside the processing container. ..
  • One aspect of the present disclosure is a film forming apparatus for forming a predetermined film on a substrate, which is configured to be decompressible, a processing container which stores the substrate, a raw material tank which stores a liquid raw material or a solid raw material, and A pressure sensor for measuring the pressure in the raw material tank, the raw material tank and the processing container so that the raw material gas generated by vaporizing the liquid raw material or the solid raw material in the raw material tank is supplied to the processing container. And a control pipe that controls the pressure control valve based on a measurement result of the pressure sensor.
  • a constant supply of a raw material gas to a processing container of a film forming apparatus that forms a predetermined film by using a raw material gas generated by vaporizing a raw material, regardless of the pressure in the processing container It can be performed.
  • various processes such as a film forming process for forming a predetermined film such as a metal film are repeatedly performed on a semiconductor wafer (hereinafter referred to as “wafer”), thereby forming a predetermined film on the wafer.
  • wafer semiconductor wafer
  • the desired semiconductor device is manufactured.
  • a solid raw material or a liquid raw material may be heated and vaporized to be a raw material gas.
  • a ruthenium (Ru) film when a ruthenium (Ru) film is formed, Ru 3 (CO) 12 that is a solid raw material is heated and sublimated, and the generated raw material gas is generated by a carrier gas. It is made to flow into the processing container of the membrane device.
  • the raw material gas for the Ru film produced by sublimating Ru 3 (CO) 12 as described above has a low vapor pressure. Therefore, in the film forming apparatus disclosed in Patent Document 1, the pressure in the raw material tank is lowered by lowering the pressure in the processing container so that a large amount of raw material gas having a low vapor pressure is vaporized.
  • the technique according to the present disclosure is to constantly supply the raw material gas to the processing container of the film forming apparatus that forms a predetermined film by using the raw material gas generated by vaporizing the raw material, regardless of the pressure in the processing container. Is possible.
  • FIG. 1 is an explanatory view schematically showing an outline of the configuration of the film forming apparatus 1 according to the first embodiment, and shows a part of the film forming apparatus 1 in a cross section.
  • the film forming apparatus 1 of this example is configured to form a Ru film on the wafer W by using Ru 3 (CO) 12 , which is a solid raw material, as a raw material.
  • the film forming apparatus 1 is configured to be decompressible and has a processing container 10 for accommodating a wafer W as a substrate and a raw material gas supply mechanism 50 for supplying a raw material gas to the processing container 10. ..
  • the processing container 10 is made of, for example, a metal material, and the inside thereof is formed in a cylindrical shape.
  • the side wall 11 of the processing container 10 is provided with a carry-in outlet (not shown) for the wafer W, and the carry-in outlet is provided with a gate valve (not shown) for opening and closing the carry-in outlet.
  • a pressure sensor 20 provided outside the processing container 10 is connected to the side wall 11 of the processing container 10 via a pipe 21.
  • the pressure sensor 20 is, for example, a capacitance manometer, and measures the pressure in the processing container 10 via the pipe 21.
  • the measurement result of the pressure sensor 20 is output to the control unit 110 described later.
  • An exhaust port 12a is formed in the bottom wall 12 of the processing container 10.
  • the bottom wall 12 is connected to the accommodation portion 22 so that an opening 22a in the upper portion of the accommodation portion 22 that accommodates a bellows 33, which will be described later, communicates with the exhaust port 12a.
  • the accommodating portion 22 has openings 22a and 22b in the upper and side portions, and the openings 22a and 22b communicate with each other.
  • One end of an exhaust pipe 23 is connected to a side portion of the housing portion 22 so that the processing container 10 is exhausted through the openings 22a and 22b.
  • the other end of the exhaust pipe 23 is connected to an exhaust device 24 which is, for example, a vacuum pump.
  • an APC valve 25 as a pressure adjusting valve for adjusting the pressure inside the processing container 10 is provided upstream of the exhaust device 24 in the exhaust pipe 23.
  • the APC valve 25 has an automatic pressure adjusting function and a shutoff function, and the opening degree of the APC valve 25 is controlled based on a control signal from the control unit 110 described later. With the APC valve 25, the pressure inside the processing container 10 can be adjusted to a preset pressure, and the connection between the processing container 10 and the exhaust device 24 can be cut off.
  • a mounting table 30 having a circular shape in a plan view is provided on which the wafer W is mounted horizontally.
  • a heater (not shown) for heating the wafer W is provided inside the mounting table 30.
  • the bottom wall 12 penetrates through the exhaust port 12a of the bottom wall 12 of the processing container 10, and further extends in the vertical direction so as to penetrate the bottom wall 22c of the accommodating portion 22.
  • the upper end of the supporting member 31 is connected.
  • the lower end of the support member 31 is connected to the lifting mechanism 32.
  • the mounting table 30 can be moved up and down between the upper first position and the lower second position by driving the lifting mechanism 32 controlled by the control unit 110 described later.
  • the first position is a processing position where processing is performed on the wafer W.
  • the processing space S is formed by the mounting table 30 located at the processing position and the partition wall 13 a that extends downward from the top wall 13 of the processing container 10 to partition the inside and outside of the processing container 10.
  • a gap K is formed between the upper surface of the mounting table 30 located at the processing position and the lower surface of the partition wall 13a, and the processing space S can be evacuated through the gap K.
  • the second position is provided below the inside of the processing container 10 and a transfer mechanism (not shown) of the wafer W that enters the processing container 10 through the above-mentioned loading/unloading port (not shown) of the processing container 10. This is a standby position where the mounting table 30 stands by when the wafer W is being delivered to and from the delivery pin (not shown).
  • the support member 31 is provided with a flange 31a.
  • a bellows 33 is provided between the lower surface of the flange 31a and the upper surface of the bottom wall 22c of the housing portion 22 so as to surround the outer periphery of the support member 31. Since the bellows 33 is provided, the airtightness of the processing container 10 is not lost due to the penetrating portion of the support member 31 in the bottom wall 22c of the housing portion 22.
  • an obstacle plate 40 is provided in parallel with the mounting table 30 as a gas flow forming member for forming the flow of the raw material gas in the processing space S.
  • the baffle plate 40 is a member that partitions the processing space S into upper and lower parts, and is supported by a supporting member (not shown).
  • the baffle plate 40 forms the following flow of raw material gas. That is, the raw material gas supplied through the gas supply port 13b provided in the center of the top wall 13 of the processing container 10 moves outward along the upper surface of the baffle plate 40, and then outside the baffle plate 40. This is the flow of the raw material gas that moves downward from that portion and moves toward the wafer W on the mounting table 30.
  • a source gas supply mechanism 50 is connected to the ceiling wall 13 of the processing container 10.
  • the raw material gas supply mechanism 50 has a raw material tank 51 that stores a solid raw material.
  • FIG. 2 is an explanatory view schematically showing an outline of the configuration of the raw material tank 51, and the raw material tank 51 is shown in a vertical cross section.
  • the raw material tank 51 has a housing 51a formed in a cylindrical shape using a metal material or the like.
  • An accommodation chamber R1 for accommodating the solid raw material M is formed in the housing 51a, and in the accommodation chamber R1, base trays 51b and 2 having a circular shape in plan view are provided as trays on which the solid raw material M is placed.
  • Two upper trays 51c each having an annular shape in plan view are provided. The number of upper trays 51c may be one or three or more.
  • a partition wall 51d is formed by the outer wall of each tray 51b, 51c.
  • the partition wall 51d is formed so as to connect the top wall 51e and the bottom wall 51f of the housing 51a, and partitions the space inside the housing 51a into the inside and the outside.
  • a carrier gas supply space 51h is formed between the partition wall 51d and the outer peripheral wall 51g of the housing 51a.
  • the carrier gas supply space 51h is connected to one end of a conduit 51j formed inside the frame portion of the housing 51a.
  • the pipeline 51j is formed so that the carrier gas passes through the top wall 51e, the outer peripheral wall 51g, and the bottom wall 51f to reach the carrier gas supply space 51h.
  • the other end of the conduit 51j is connected to one end of a supply pipe 61 of a carrier gas supply mechanism 60 that supplies a carrier gas.
  • the other end of the supply pipe 61 is connected to the carrier gas supply source 62.
  • the supply pipe 61 is provided with a flow rate control unit (not shown) such as a mass flow controller and an opening/closing valve 63 for starting or stopping the supply of carrier gas.
  • the carrier gas supplied from the carrier gas supply mechanism 60 is carbon monoxide (CO) gas.
  • the supply pipe 61 is provided with a carrier gas heating unit (not shown) for heating the carrier gas.
  • the flow rate control unit, the on-off valve 63, and the carrier gas heating unit are controlled by the control unit 110 described later.
  • the supply pipe 61 is provided with a temperature sensor (not shown) for controlling the temperature of the supply pipe 61. The measurement result by the temperature sensor is output to the control unit 110 described later. For this temperature sensor, for example, a sensor using platinum is used.
  • openings 51k are formed in the outer wall of each of the base tray 51b and the upper tray 51c.
  • the carrier gas supplied from the carrier gas supply mechanism 60 is supplied from the outside of the trays 51b and 51c above the solid raw material M placed on the base tray 51b and the upper tray 51c. After that, the carrier gas is supplied to the processing container 10 through the opening 51m formed in the center of the top wall 51e toward the center of the housing 51a, together with the source gas generated by the sublimation of the solid material M.
  • the housing 51a is provided with a tank heating unit 70 so as to cover the entire body.
  • the tank heating unit 70 heats the raw material tank 51, specifically, the casing 51a.
  • the heating by the tank heating unit 70 can promote the sublimation of the solid raw material in the housing 51a.
  • the tank heating unit 70 is controlled by the control unit 110 described later.
  • a pressure sensor 80 provided outside the housing 51a is connected to the top wall 51e of the housing 51a via a pipe 81.
  • the pressure sensor 80 is, for example, a capacitance manometer, and measures the pressure inside the housing 51a as the pressure of the raw material tank 51 via the pipe 81.
  • a temperature sensor 90 for measuring the temperature of the raw material tank 51 specifically, the temperature of the housing 51a is provided on the outer peripheral wall 51g of the housing 51a.
  • the temperature sensor 90 is, for example, a sensor using platinum. Although the number of temperature sensors 90 is one in the example shown in the figure, a plurality of temperature sensors 90 may be provided. The measurement results of the pressure sensor 80 and the temperature sensor 90 are output to the control unit 110 described later.
  • the raw material gas supply mechanism 50 has, in addition to the above-described raw material tank 51, a supply pipe 52 that connects the raw material tank 51 and the processing container 10 to supply the raw material gas from the raw material tank 51 to the processing container 10.
  • a supply pipe 52 that connects the raw material tank 51 and the processing container 10 to supply the raw material gas from the raw material tank 51 to the processing container 10.
  • One end of the supply pipe 52 is connected to the top wall 51e of the housing 51a of the raw material tank 51, and the other end is connected to the top wall 13 of the processing container 10.
  • the top wall 51e is connected via the supply pipe 52. 51m and the gas supply port 13b of the ceiling wall 13 communicate with each other.
  • the supply pipe 52 is provided with an on-off valve 53 that opens or closes the pipeline in the supply pipe 52.
  • the on-off valve 53 is controlled by the control unit 110 described later.
  • a pressure adjusting valve for adjusting the pressure in the raw material tank 51 specifically, the pressure in the housing 51a of the raw material tank 51 is provided.
  • APC valve 54 is provided.
  • the APC valve 54 has an automatic pressure adjusting function and a shutoff function, and the opening degree of the APC valve 54 is controlled based on a control signal from the control unit 110 described later.
  • the pressure in the raw material tank 51 (specifically, the pressure in the housing 51a of the raw material tank 51) is adjusted to a preset pressure, or the pipeline in the supply pipe 52 is closed. You can
  • the supply pipe 52 is provided with a supply pipe heating unit 55.
  • the supply pipe heating unit 55 heats the entire supply pipe 52 including the on-off valve 53 and the APC valve 54. As a result, it is possible to prevent the raw material gas from solidifying and adhering to the supply pipe 52 including the on-off valve 53 and the APC valve 54.
  • the processing container heating unit 100 for heating the processing container 10 is provided in the film forming apparatus 1.
  • the supply pipe heating unit 55 and the processing container heating unit 100 are controlled by the control unit 110 described later. Further, a temperature sensor (not shown) is provided in the supply pipe 52 for temperature control of the supply pipe 52 by the supply pipe heating unit 55, and the processing container 10 is provided for temperature control of the processing container 10 by the processing container heating unit 100. For example, a temperature sensor (not shown) is provided on the side wall 11. The measurement results by these temperature sensors are output to the control unit 110 described later. As these temperature sensors, for example, a sensor using platinum is used.
  • the film forming apparatus 1 configured as described above is provided with the control unit 110.
  • the control unit 110 is composed of, for example, a computer equipped with a CPU, a memory, or the like, and has a program storage unit (not shown).
  • the program storage unit also stores a program for controlling the APC valves 25 and 54, the on-off valve 53, and the like to realize the wafer processing described later in the film forming apparatus 1.
  • the program may be stored in a computer-readable storage medium and installed in the control unit 110 from the storage medium. Further, part or all of the program may be realized by dedicated hardware (circuit board).
  • the pressure sensor 20 In a state where the on-off valve 53 and 63 and the APC valve 54 is closed, together with the direct N 2 gas is supplied from the N 2 gas supply line (not shown) into the processing chamber 10, the pressure sensor 20 The opening degree of the APC valve 25 is adjusted on the basis of the measurement result in (1), and the inside of the processing container 10 is set to a predetermined pressure (for example, 7 to 10 Torr).
  • a gate valve (not shown) provided at a carry-in/out port (not shown) of the wafer W of the processing container 10 is opened, and a transfer chamber (not shown) in a vacuum atmosphere adjacent to the processing container 10 is opened.
  • a transfer mechanism (not shown) holding the wafer W is inserted into the processing container 10 through the carry-in / out port. Then, the wafer W is conveyed above the mounting table 30 located at the above-mentioned standby position. Next, the wafer W is transferred onto the raised support pins (not shown), and then the transfer mechanism is taken out of the processing container 10 and the gate valve is closed. At the same time, the support pins are lowered and the mounting table 30 is raised, the wafer W is mounted on the mounting table 30, the mounting table 30 is moved to the processing position, and the processing space S is formed. ..
  • the wafer W is heated to a predetermined temperature (for example, 120 to 250 ° C.) by the heater provided on the mounting table 30.
  • the opening degree of the APC valve 25 is adjusted, and the pressure inside the processing container 10 is reduced to a predetermined pressure (for example, 5 mTorr to 100 mTorr).
  • a predetermined pressure for example, 5 mTorr to 100 mTorr.
  • the on-off valves 53 and 63 are opened and the opening degree of the APC valve 54 is increased so that the supply of the raw material gas to the processing space S in the processing container 10 is started. Adjusted. As a result, the formation of the Ru film on the wafer W in the processing space S by CVD (Chemical Vapor Deposition) is started.
  • the opening degree of the APC valve 54 is set by, for example, the pressure inside the raw material tank 51 (specifically, the pressure inside the housing 51a of the raw material tank 51) after the on-off valves 53 and 63 are opened. It is adjusted to be gradually increased until it reaches 40 mTorr to 150 mTorr). When the set pressure is reached, thereafter, the opening of the APC valve 54 is controlled based on the measurement result of the pressure sensor 80 until the Ru film formation is completed, and the pressure in the raw material tank 51 is set to the set pressure. Is adjusted to be constant. When the pressure in the raw material tank 51 is maintained constant at the set pressure, the on-off valve 63 on the carrier gas supply mechanism 60 is closed. The on-off valve 63 is opened to adjust the pressure whenever fluctuations (such as an increase in the opening of the APC valve 25) occur downstream of the raw material tank 51.
  • the opening/closing valves 53 and 63 are closed, and the wafer W is unloaded from the processing container 10 in the reverse procedure.
  • a predetermined temperature for example, 80 ° C.
  • the carrier gas heated to the surface is supplied at a constant flow rate.
  • the temperatures of the raw material tank 51, the supply pipe 52, and the processing container 10 are set to the heating units 70, 55 based on the measurement results of the corresponding temperature sensors so that the raw material gas does not solidify at least. , 100 is constantly heated so as to be constant at a predetermined temperature.
  • the supply pipe 52 and the processing container 10 are heated and controlled so as to be constant at 80 ° C.
  • the raw material tank 51 has a temperature slightly lower than that of the supply pipe 52 and the processing container 10 and higher than that of the supply pipe 52 and the processing container 10. Therefore, the heating is controlled so as to be constant at a predetermined temperature lower than the decomposition temperature of the solid raw material (for example, 70 ° C. to 100 ° C. lower than the decomposition temperature at the set pressure).
  • the supply pipe 52 that connects the raw material tank 51 and the processing container 10 to each other is formed on the basis of the pressure sensor 80 that measures the pressure in the housing 51a of the raw material tank 51 during film formation.
  • the APC valve 54 provided is controlled. Therefore, in the Ru film forming process, the pressure in the raw material tank 51 can be kept constant regardless of the pressure in the processing container 10. Therefore, the raw material gas can be constantly supplied regardless of the pressure in the processing container 10. Further, since the pressure in the raw material tank 51 is controlled only by adjusting the opening degree of the APC valve 54, the control is easy.
  • the fact that the pressure in the processing container 10 and the pressure in the raw material tank 51 are independently controlled as in the present embodiment means that the pressure in the processing container 10 and the supply amount of the raw material gas are controlled. It means that they are controlled independently.
  • the pressure inside the processing container 10 and the supply amount of the raw material gas are independently controlled. Therefore, when a problem occurs in the film forming process, the problem is the pressure inside the processing container 10. It is possible to distinguish whether the cause is the treatment condition related to the above or the processing condition related to the supply amount of the raw material gas.
  • the conductance inside the processing container 10 is also different.
  • the pressure on the upstream side of the different part also differs. Therefore, when the internal structure of the processing container 10 is different, the internal pressure of the raw material tank is different and the supply amount of the raw material gas is also different in the structure of Patent Document 1.
  • the pressure of the raw material tank 51 is controlled independently, the same amount of raw material gas can be supplied even when the internal structure of the processing container 10 is different.
  • the set pressure in the raw material tank 51 may be variable depending on the measurement result of the pressure sensor 20 for the processing container 10. For example, when the measurement result by the pressure sensor 20 is high so that the pressure difference between the pressure in the raw material tank 51 and the pressure in the processing container 10 is constant, the pressure in the raw material tank 51 is increased to increase the pressure sensor. When the measurement result at 20 is low, the pressure in the raw material tank 51 may be lowered.
  • the temperature of the housing 51a of the raw material tank 51 is set to be high. Specifically, the temperature of the raw material tank 51 is set to be constant at a predetermined temperature (for example, 90 to 100 ° C.) which is higher than the supply pipe 52 and the processing container 10 and lower than the decomposition temperature of the solid raw material. There is. Therefore, the supply amount of the raw material gas is the same as when the pressure in the housing 51a of the raw material tank 51 is higher than the pressure in the processing container 10 but the pressure in the housing 51a is substantially equal to the pressure in the processing container 10. It can be equal or higher.
  • the temperature of the housing 51a of the raw material tank 51 may be variable according to the set pressure in the raw material tank 51. For example, when the set pressure is high, the temperature of the housing 51a of the raw material tank 51 may be raised. As a result, the supply amount of the raw material gas can be increased as long as the solid raw material is not decomposed.
  • a temperature sensor 90 using platinum is used as the temperature sensor 90 for measuring the temperature of the housing 51a of the raw material tank 51. Therefore, the temperature of the housing 51a of the raw material tank can be controlled with high accuracy based on the measurement result of the temperature sensor 90, and the supply amount of the raw material gas can be controlled with high accuracy.
  • a platinum sensor is also used as the temperature sensor for the processing container 10 and the supply pipes 52 and 61. Therefore, the temperatures of the processing container 10 and the supply pipes 52 and 61 can be controlled with high accuracy.
  • the APC valve 54 is operated from the time when the on-off valve 53 is opened until the pressure in the raw material tank 51 reaches the set pressure, that is, in the initial stage of the Ru film formation.
  • the opening degree of is gradually increased. Therefore, it is possible to prevent a large amount of the raw material gas accumulated in the raw material tank 51 from flowing into the processing container 10 while the APC valve 54 is closed in the initial stage of the Ru film formation.
  • both the opening/closing valve 53 and the APC valve 54 are closed when the wafer W is loaded/unloaded or when the wafer W is heated, but only the APC valve 54 may be closed. ..
  • the source gas is supplied to the processing container 10 in the low pressure atmosphere from the casing 51a of the raw material tank 51 in the atmosphere higher than the pressure inside the processing container 10, that is, the high pressure atmosphere. Therefore, since the raw material gas from the raw material tank 51 in the high-pressure atmosphere expands in the processing container 10, the number of molecules that react with the wafer W in the processing space S is large, so that the film formation rate can be increased.
  • the APC valve 54 may be arranged in the immediate vicinity of the processing container 10. More specifically, the distance from the upper surface of the ceiling wall 13 of the processing container 10 to the lower surface of the APC valve 54 is 10 mm or less. It may be placed in. Considering from the raw material tank 51 to the APC valve 54 of the supply pipe 52 as a raw material gas storage container, by disposing the APC valve 54 near the processing container 10, the raw material gas in the storage container is processed by the processing container. When supplied to the inside of the processing container 10, the pressure is first lowered in the immediate vicinity of the processing container 10. Therefore, decomposition of the raw material gas due to the pressure gradient can be prevented up to the vicinity of the top wall 13 of the processing container 10.
  • FIG. 3 is an explanatory view schematically showing the outline of the configuration of the film forming apparatus 1a according to the second embodiment, and a part of the film forming apparatus 1a is shown in cross section.
  • one end of the exhaust bypass pipe 120 is connected between the on-off valve 53 and the APC valve 54 in the supply pipe 52.
  • the other end of the exhaust bypass pipe 120 is connected to the exhaust device 24.
  • the exhaust bypass pipe 120 communicates the raw material tank 51 and the exhaust device 24 without passing through the processing container 10.
  • the exhaust bypass pipe 120 is provided with an on-off valve 121 that opens or closes the pipeline of the exhaust bypass pipe 120.
  • an exhaust bypass pipe heating unit for heating the exhaust bypass pipe 120 is provided in the film forming apparatus 1. ing. Further, in order to control the temperature of the exhaust bypass pipe 120, the exhaust bypass pipe 120 is provided with a temperature sensor (not shown) that measures the temperature of the exhaust bypass pipe 120. The measurement result of this temperature sensor is output to the control unit 110, and the exhaust bypass pipe 120 is controlled by the control unit 110.
  • the APC valve 54 is closed and the opening/closing valve 63 of the carrier gas supply mechanism 60 is closed when the wafer W is loaded and unloaded. It was on the other hand, in the wafer processing performed using the film forming apparatus 1a, the opening of the APC valve 54 is constantly adjusted based on the measurement result of the pressure sensor 80, including when the wafer W is loaded and unloaded, and the opening/closing valve is opened. 63 is opened. However, while the on-off valve 53 is in the closed state, the on-off valve 121 provided in the exhaust bypass pipe 120 is in the open state.
  • the open/close valve 53 is changed from the closed state to the open state, and the open/close valve 121 is changed from the open state to the closed state.
  • the on-off valve 53 is changed from the closed state to the open state, the on-off valve 121 provided in the exhaust bypass pipe 120 may be left in the open state.
  • FIG. 4 is an explanatory view schematically showing an outline of the configuration of the film forming apparatus 1b according to the third embodiment, and shows a part of the film forming apparatus 1b in a cross section.
  • the housing 51a of the raw material tank 51 has a buffer chamber R2 inside which stores the raw material gas on the downstream side of the storage chamber R1.
  • the storage chamber R1 and the buffer chamber R2 are separated by a partition wall 51n having an opening 51p. According to the present embodiment, since the raw material gas can be accumulated in the buffer chamber R2, the raw material gas can be stably supplied to the processing container 10.
  • the pressure measurement target by the pressure sensor 80 may be the buffer chamber R2 instead of the accommodation chamber R1.
  • the supply destination of the gas from the carrier gas supply mechanism 60 may be the buffer chamber R2 instead of the accommodation chamber R1.
  • the casing 51a of the raw material tank 51 is heated by one heating unit, but the region of the casing 51a is divided into a plurality of regions, the heating unit is provided for each region, and the temperature control is performed for each region. You may do it.
  • the heating section for the supply pipe 52, the processing container 10, and the carrier gas supply pipe When heating is performed for each region as described above, one or a plurality of temperature sensors are provided for each region.
  • the members such as the supply pipes 52 and 61 that are provided with various valves and flow rate control units the regions where various valves are provided and other regions are different. You may divide. This is because the temperatures of various valves and flow control units and the piping may differ even if the amount of heating is the same.
  • the set temperature of the raw material tank 51 (specifically, the set temperature of the housing 51a) and the set temperature of other parts such as the supply pipe 52 may be independent, but depending on the set temperature of the raw material tank 51, The set temperature of the other parts may be changed.
  • Ru 3 (CO) 12 is used as the solid raw material for the Ru film, but other solid raw materials may be used.
  • a liquid raw material may be used instead of the solid raw material.
  • the solid raw material means a solid raw material at atmospheric pressure and room temperature
  • the liquid raw material means a liquid raw material at atmospheric pressure and room temperature.
  • the Ru film was formed.
  • the technique according to the present disclosure can also be applied to an apparatus that forms another film by using a raw material gas generated by vaporizing a solid raw material or a liquid raw material.
  • CO gas is used as the carrier gas, but a rare gas such as Ar gas or an inert gas such as N 2 can be used. However, by using CO gas, decomposition of the raw material gas can be prevented.
  • the APC valve 54 is provided on the upstream side of the opening/closing valve 53, but the APC valve 54 may be provided on the downstream side of the opening/closing valve 53. Further, the opening/closing valve 53 may be omitted, and the APC valve 54 may be provided at the position of the opening/closing valve 53, that is, the position of the supply pipe 52 on the processing container 10 side.
  • a film forming apparatus for forming a predetermined film on a substrate, A processing container that is configured to be depressurizable and that stores the substrate, A raw material tank for storing a liquid raw material or a solid raw material, A supply pipe connecting the raw material tank and the processing container, so that the raw material gas generated by vaporizing the liquid raw material or the solid raw material in the raw material tank is supplied to the processing container, A pressure adjusting valve provided in the supply pipe and having a variable opening degree; A pressure sensor for measuring the pressure in the raw material tank, A film forming apparatus including a control unit that controls the pressure adjusting valve based on the measurement result of the pressure sensor.
  • the pressure regulating valve provided in the supply pipe connecting the raw material tank and the processing container is controlled based on the measurement result of the pressure sensor that measures the pressure in the raw material tank. Therefore, in the predetermined film forming process, the pressure in the raw material tank can be kept constant regardless of the pressure in the processing container. Therefore, a constant supply of the raw material gas can be performed regardless of the pressure in the processing container.
  • a temperature sensor for measuring the temperature of the raw material tank and It has a heating unit that heats the raw material tank, The control unit further controls the heating unit so that the temperature of the raw material tank becomes higher than the temperature of the supply pipe based on the measurement result of the temperature sensor, according to the above (1) or (2).
  • a raw material gas supply method for supplying a raw material gas into a processing container of a film forming apparatus that forms a predetermined film on a substrate A step of adjusting the opening degree of a pressure adjusting valve provided in a supply pipe connecting the raw material tank and the processing container based on the pressure in the raw material tank for storing the liquid raw material or the solid raw material. A step of vaporizing the liquid raw material or the solid raw material in the raw material tank to generate the raw material gas, and A method for supplying a raw material gas, comprising a step of supplying the generated raw material gas to the processing container via the supply pipe.

Abstract

This film-forming apparatus is for forming a predetermined film on a substrate, and has: a treatment container which is configured to be capable of being decompressed and which houses the substrate therein; a material tank in which a liquid material or a solid material is stored; a feed pipe which connects the material tank and the treatment container in such a manner as to allow a material gas generated by vaporization of the liquid or solid material within the material tank to be fed into the treatment container; a pressure regulation valve which is provided to the feed pipe and which is capable of adjusting a valve opening thereof; a pressure sensor for measuring the pressure inside the material tank; and a control unit for controlling the pressure regulation valve on the basis of a measurement result of the pressure sensor.

Description

成膜装置及び原料ガス供給方法Film formation equipment and raw material gas supply method
 本開示は、成膜装置及び原料ガス供給方法に関する。 The present disclosure relates to a film forming apparatus and a raw material gas supply method.
 特許文献1には、ルテニウム(Ru)膜の成膜装置であって、半導体ウェハ(以下、「ウェハ」という。)に対して成膜処理を施す成膜装置本体と、この成膜装置本体に対して原料ガスを供給する原料ガス供給システムとを有する装置が開示されている。上記成膜装置の原料ガス供給システムは、固体原料であるRu(CO)12を貯留する原料タンクと、原料タンクに一端が接続され上記成膜装置本体が有する処理容器に他端が接続された原料通路と、を有する。上記処理容器は、ウェハが載置される載置台が内部に設けられており、当該処理容器内を減圧雰囲気に維持するための真空排気系が接続されている。そして、上記成膜装置では、蒸気圧の低い原料ガスを多く気化させるために、処理容器内の圧力を下げ原料タンク内の圧力を下げるようにしている。 Patent Document 1 discloses a ruthenium (Ru) film forming apparatus, which includes a film forming apparatus main body that performs a film forming process on a semiconductor wafer (hereinafter referred to as “wafer”), and a film forming apparatus main body. On the other hand, an apparatus having a raw material gas supply system for supplying the raw material gas is disclosed. The raw material gas supply system of the film forming apparatus has a raw material tank for storing Ru 3 (CO) 12 as a solid raw material, one end connected to the raw material tank, and the other end connected to a processing container of the main body of the film forming apparatus. And a raw material passage. The processing container has a mounting table on which a wafer is mounted inside, and is connected to a vacuum exhaust system for maintaining a reduced pressure atmosphere in the processing container. Further, in the film forming apparatus, in order to vaporize a large amount of the raw material gas having a low vapor pressure, the pressure in the processing container is lowered and the pressure in the raw material tank is lowered.
特開2009-84625号公報JP-A-2009-84625
 本開示にかかる技術は、原料を気化させ生成した原料ガスを用いて所定の膜を形成する成膜装置の処理容器に対し、当該処理容器内の圧力によらない、原料ガスの一定供給を行う。 The technique according to the present disclosure provides a constant supply of a raw material gas to a processing container of a film forming apparatus that forms a predetermined film using a raw material gas generated by vaporizing the raw material, regardless of the pressure inside the processing container. ..
 本開示の一態様は、基板に所定の膜を形成する成膜装置であって、減圧可能に構成され、前記基板を収容する処理容器と、液体原料または固体原料を貯留する原料タンクと、前記原料タンク内の圧力を測定する圧力センサと、前記液体原料または前記固体原料が前記原料タンク内で気化して生成された原料ガスが前記処理容器に供給されるよう、前記原料タンクと前記処理容器とを接続する供給管と、前記供給管に設けられた、開度可変な圧力調整弁と、前記圧力センサでの測定結果に基づいて、前記圧力調整弁を制御する制御部と、を有する。 One aspect of the present disclosure is a film forming apparatus for forming a predetermined film on a substrate, which is configured to be decompressible, a processing container which stores the substrate, a raw material tank which stores a liquid raw material or a solid raw material, and A pressure sensor for measuring the pressure in the raw material tank, the raw material tank and the processing container so that the raw material gas generated by vaporizing the liquid raw material or the solid raw material in the raw material tank is supplied to the processing container. And a control pipe that controls the pressure control valve based on a measurement result of the pressure sensor.
 本開示にかかる技術によれば、原料を気化させ生成した原料ガスを用いて所定の膜を形成する成膜装置の処理容器に対し、当該処理容器内の圧力によらない、原料ガスの一定供給を行うことができる。 According to the technique of the present disclosure, a constant supply of a raw material gas to a processing container of a film forming apparatus that forms a predetermined film by using a raw material gas generated by vaporizing a raw material, regardless of the pressure in the processing container It can be performed.
第1実施形態にかかる成膜装置の構成の概略を模式的に示す説明図である。It is explanatory drawing which shows the outline of a structure of the film-forming apparatus concerning 1st Embodiment typically. 原料タンクの構成の概略を模式的に示す説明図である。It is explanatory drawing which shows the outline of a structure of a raw material tank typically. 第2実施形態にかかる成膜装置の構成の概略を模式的に示す説明図である。It is explanatory drawing which shows the outline of a structure of the film-forming apparatus concerning 2nd Embodiment typically. 第3実施形態にかかる成膜装置の構成の概略を模式的に示す説明図である。It is explanatory drawing which shows the outline of a structure of the film-forming apparatus concerning 3rd Embodiment typically.
 半導体デバイスの製造工程では、半導体ウェハ(以下、「ウェハ」という。)に対して、金属膜等の所定の膜を形成する成膜処理等の各種処理が繰り返し行われ、これにより、ウェハ上に所望の半導体デバイスが製造される。 In the manufacturing process of a semiconductor device, various processes such as a film forming process for forming a predetermined film such as a metal film are repeatedly performed on a semiconductor wafer (hereinafter referred to as “wafer”), thereby forming a predetermined film on the wafer. The desired semiconductor device is manufactured.
 ところで、成膜処理では、固体原料または液体原料を加熱して気化させ、原料ガスとすることがある。
 例えば、特許文献1に開示の成膜装置では、ルテニウム(Ru)膜を形成する場合、固体原料であるRu(CO)12を加熱して昇華させ、生成された原料ガスをキャリアガスによって成膜装置の処理容器内に流すようにしている。
 なお、上述のようにRu(CO)12を昇華して生成されるRu膜用の原料ガスは蒸気圧が低い。そのため、特許文献1に開示の成膜装置では、処理容器内の圧力を下げることで原料タンク内の圧力を下げ、蒸気圧の低い原料ガスが多く気化するようにしている。
By the way, in the film forming process, a solid raw material or a liquid raw material may be heated and vaporized to be a raw material gas.
For example, in the film forming apparatus disclosed in Patent Document 1, when a ruthenium (Ru) film is formed, Ru 3 (CO) 12 that is a solid raw material is heated and sublimated, and the generated raw material gas is generated by a carrier gas. It is made to flow into the processing container of the membrane device.
The raw material gas for the Ru film produced by sublimating Ru 3 (CO) 12 as described above has a low vapor pressure. Therefore, in the film forming apparatus disclosed in Patent Document 1, the pressure in the raw material tank is lowered by lowering the pressure in the processing container so that a large amount of raw material gas having a low vapor pressure is vaporized.
 しかし、特許文献1に開示のように、処理容器内の圧力を下げることで原料タンク内の圧力を下げる場合、原料タンク内の圧力は処理容器内の圧力の影響を受ける。したがって、原料タンク内の固体原料の気化量は、処理容器内の圧力によって変化するため、処理容器内の圧力に応じて原料ガスの供給量は変化してしまう。つまり、処理容器内の圧力によらない、原料ガスの一定供給を行うことができない。 However, when the pressure in the raw material tank is lowered by lowering the pressure in the processing container as disclosed in Patent Document 1, the pressure in the raw material tank is affected by the pressure in the processing container. Therefore, since the vaporization amount of the solid raw material in the raw material tank changes depending on the pressure in the processing container, the supply amount of the raw material gas changes depending on the pressure in the processing container. That is, the constant supply of the source gas cannot be performed regardless of the pressure in the processing container.
 そこで、本開示にかかる技術は、原料を気化させ生成した原料ガスを用いて所定の膜を形成する成膜装置の処理容器に対し、当該処理容器内の圧力によらない、原料ガスの一定供給を可能とする。 Therefore, the technique according to the present disclosure is to constantly supply the raw material gas to the processing container of the film forming apparatus that forms a predetermined film by using the raw material gas generated by vaporizing the raw material, regardless of the pressure in the processing container. Is possible.
 以下、本実施形態にかかる成膜装置及び原料ガス供給方法について、図面を参照しながら説明する。なお、本明細書及び図面において、実質的に同一の機能構成を有する要素については、同一の符号を付することにより重複説明を省略する。 The film forming apparatus and the source gas supply method according to this embodiment will be described below with reference to the drawings. In this specification and the drawings, elements having substantially the same functional configuration are designated by the same reference numerals, and duplicate description will be omitted.
(第1実施形態)
 図1は、第1実施形態にかかる成膜装置1の構成の概略を模式的に示す説明図であり、成膜装置1の一部を断面で示している。本例の成膜装置1は、原料として個体原料であるRu(CO)12を用いてウェハW上にRu膜を形成するように構成されている。
 図1に示すように、成膜装置1は、減圧可能に構成され、基板としてのウェハWを収容する処理容器10と、処理容器10に原料ガスを供給する原料ガス供給機構50と、を有する。
(First embodiment)
FIG. 1 is an explanatory view schematically showing an outline of the configuration of the film forming apparatus 1 according to the first embodiment, and shows a part of the film forming apparatus 1 in a cross section. The film forming apparatus 1 of this example is configured to form a Ru film on the wafer W by using Ru 3 (CO) 12 , which is a solid raw material, as a raw material.
As shown in FIG. 1, the film forming apparatus 1 is configured to be decompressible and has a processing container 10 for accommodating a wafer W as a substrate and a raw material gas supply mechanism 50 for supplying a raw material gas to the processing container 10. ..
 処理容器10は、例えば、金属材料を用いて、その内部が円筒形状に構成されている。
 処理容器10の側壁11には、ウェハWの搬入出口(図示せず)が設けられており、この搬入出口には、当該搬入出口を開閉するゲートバルブ(図示せず)が設けられている。
 また、処理容器10の側壁11には、処理容器10の外部に設けられた圧力センサ20が配管21を介して接続されている。圧力センサ20は、例えばキャパシタンスマノメータであり、配管21を介して処理容器10内の圧力を測定する。圧力センサ20での測定結果は、後述の制御部110に出力される。
The processing container 10 is made of, for example, a metal material, and the inside thereof is formed in a cylindrical shape.
The side wall 11 of the processing container 10 is provided with a carry-in outlet (not shown) for the wafer W, and the carry-in outlet is provided with a gate valve (not shown) for opening and closing the carry-in outlet.
Further, a pressure sensor 20 provided outside the processing container 10 is connected to the side wall 11 of the processing container 10 via a pipe 21. The pressure sensor 20 is, for example, a capacitance manometer, and measures the pressure in the processing container 10 via the pipe 21. The measurement result of the pressure sensor 20 is output to the control unit 110 described later.
 処理容器10の底壁12には、排気口12aが形成されている。また、底壁12には、後述のベローズ33を収容する収容部22の上部の開口22aと排気口12aとが連通するように、当該収容部22が接続されている。収容部22は、上部と側部に開口22a、22bを有し、開口22aと開口22bが互いに連通している。これら開口22a、22bを介して処理容器10が排気されるように、収容部22の側部には、排気管23の一端部が接続されている。排気管23の他端部は、例えば真空ポンプにより構成される排気装置24に接続されている。また、排気管23の排気装置24より上流側には、処理容器10内の圧力を調整するための圧力調整弁としてのAPCバルブ25が設けられている。APCバルブ25は、自動圧力調整機能及び遮断機能を備えており、後述の制御部110からの制御信号に基づいて当該APCバルブ25の開度は制御される。APCバルブ25によって、処理容器10内の圧力を予め設定された圧力になるよう調整したり、処理容器10と排気装置24との接続を遮断したりすることができる。 An exhaust port 12a is formed in the bottom wall 12 of the processing container 10. In addition, the bottom wall 12 is connected to the accommodation portion 22 so that an opening 22a in the upper portion of the accommodation portion 22 that accommodates a bellows 33, which will be described later, communicates with the exhaust port 12a. The accommodating portion 22 has openings 22a and 22b in the upper and side portions, and the openings 22a and 22b communicate with each other. One end of an exhaust pipe 23 is connected to a side portion of the housing portion 22 so that the processing container 10 is exhausted through the openings 22a and 22b. The other end of the exhaust pipe 23 is connected to an exhaust device 24 which is, for example, a vacuum pump. Further, an APC valve 25 as a pressure adjusting valve for adjusting the pressure inside the processing container 10 is provided upstream of the exhaust device 24 in the exhaust pipe 23. The APC valve 25 has an automatic pressure adjusting function and a shutoff function, and the opening degree of the APC valve 25 is controlled based on a control signal from the control unit 110 described later. With the APC valve 25, the pressure inside the processing container 10 can be adjusted to a preset pressure, and the connection between the processing container 10 and the exhaust device 24 can be cut off.
 処理容器10内には、ウェハWが水平に載置される平面視円形状の載置台30が設けられている。載置台30の内部には、ウェハWを加熱するためのヒータ(図示せず)が設けられている。載置台30の下面側中央部には、処理容器10の底壁12の排気口12aを通じて底壁12を貫通し、さらに、収容部22の底壁22cを貫通するように、上下方向に延在する支持部材31の上端部が接続されている。支持部材31の下端は、昇降機構32に接続されている。後述の制御部110に制御される昇降機構32の駆動によって、載置台30は、上方の第1の位置と下方の第2の位置との間を上下に移動することができる。 In the processing container 10, a mounting table 30 having a circular shape in a plan view is provided on which the wafer W is mounted horizontally. A heater (not shown) for heating the wafer W is provided inside the mounting table 30. In the central portion on the lower surface side of the mounting table 30, the bottom wall 12 penetrates through the exhaust port 12a of the bottom wall 12 of the processing container 10, and further extends in the vertical direction so as to penetrate the bottom wall 22c of the accommodating portion 22. The upper end of the supporting member 31 is connected. The lower end of the support member 31 is connected to the lifting mechanism 32. The mounting table 30 can be moved up and down between the upper first position and the lower second position by driving the lifting mechanism 32 controlled by the control unit 110 described later.
 上記第1の位置は、ウェハWに処理が行われる処理位置である。処理位置に位置する載置台30と、処理容器10の天壁13から下方に延び出し処理容器10内の内外を仕切る隔壁13aとにより、処理空間Sが形成される。なお、処理位置に位置する載置台30の上面と隔壁13aの下面との間には隙間Kが形成されており、この隙間Kを介して処理空間S内は排気可能である。
 上記第2の位置は、処理容器10の前述の搬出入口(図示せず)から処理容器10内に進入するウェハWの搬送機構(図示せず)と、処理容器10内の下方に設けられた受け渡しピン(図示せず)との間で、ウェハWを受け渡している時に載置台30が待機する待機位置である。
The first position is a processing position where processing is performed on the wafer W. The processing space S is formed by the mounting table 30 located at the processing position and the partition wall 13 a that extends downward from the top wall 13 of the processing container 10 to partition the inside and outside of the processing container 10. A gap K is formed between the upper surface of the mounting table 30 located at the processing position and the lower surface of the partition wall 13a, and the processing space S can be evacuated through the gap K.
The second position is provided below the inside of the processing container 10 and a transfer mechanism (not shown) of the wafer W that enters the processing container 10 through the above-mentioned loading/unloading port (not shown) of the processing container 10. This is a standby position where the mounting table 30 stands by when the wafer W is being delivered to and from the delivery pin (not shown).
 また、支持部材31には、フランジ31aが設けられている。そして、このフランジ31aの下面と、収容部22の底壁22cの上面との間には、支持部材31の外周を囲むように、ベローズ33が設けられている。このベローズ33が設けられているため、収容部22の底壁22cにおける支持部材31の貫通部分によって処理容器10の気密性が失われることがない。 Further, the support member 31 is provided with a flange 31a. A bellows 33 is provided between the lower surface of the flange 31a and the upper surface of the bottom wall 22c of the housing portion 22 so as to surround the outer periphery of the support member 31. Since the bellows 33 is provided, the airtightness of the processing container 10 is not lost due to the penetrating portion of the support member 31 in the bottom wall 22c of the housing portion 22.
 また、処理容器10内における載置台30の上方には、処理空間S内における原料ガスの流れを形成するガス流形成部材として、邪魔板40が、載置台30と平行に設けられている。邪魔板40は、処理空間Sを上下に仕切る部材であり、支持部材(図示せず)に支持されている。この邪魔板40は、以下のような原料ガスの流れを形成する。すなわち、処理容器10の天壁13の中央に設けられたガス供給口13bを介して供給される原料ガスが、邪魔板40の上面に沿って外側に向けて移動した後、邪魔板40の外方の部分から下側に移動し、載置台30上のウェハWの方向へ移動する、原料ガスの流れである。 Further, above the mounting table 30 in the processing container 10, an obstacle plate 40 is provided in parallel with the mounting table 30 as a gas flow forming member for forming the flow of the raw material gas in the processing space S. The baffle plate 40 is a member that partitions the processing space S into upper and lower parts, and is supported by a supporting member (not shown). The baffle plate 40 forms the following flow of raw material gas. That is, the raw material gas supplied through the gas supply port 13b provided in the center of the top wall 13 of the processing container 10 moves outward along the upper surface of the baffle plate 40, and then outside the baffle plate 40. This is the flow of the raw material gas that moves downward from that portion and moves toward the wafer W on the mounting table 30.
 さらに、処理容器10の天壁13には、原料ガス供給機構50が接続されている。 Further, a source gas supply mechanism 50 is connected to the ceiling wall 13 of the processing container 10.
 原料ガス供給機構50は、固体原料を貯留する原料タンク51を有する。 The raw material gas supply mechanism 50 has a raw material tank 51 that stores a solid raw material.
 ここで、図2を用いて原料タンク51について説明する。図2は、原料タンク51の構成の概略を模式的に示す説明図であり、原料タンク51については縦断面で示している。
 原料タンク51は、金属材料等を用いて円筒形状に構成された筐体51aを有する。
 筐体51a内には、固体原料Mを収容する収容室R1が形成されており、収容室R1内には、固体原料Mが載置されるトレーとして、平面視円形状のベーストレー51bと2つの平面視円環状の上部トレー51cとが設けられている。上部トレー51cの数は、1つであっても3以上であってもよい。
Here, the raw material tank 51 will be described with reference to FIG. FIG. 2 is an explanatory view schematically showing an outline of the configuration of the raw material tank 51, and the raw material tank 51 is shown in a vertical cross section.
The raw material tank 51 has a housing 51a formed in a cylindrical shape using a metal material or the like.
An accommodation chamber R1 for accommodating the solid raw material M is formed in the housing 51a, and in the accommodation chamber R1, base trays 51b and 2 having a circular shape in plan view are provided as trays on which the solid raw material M is placed. Two upper trays 51c each having an annular shape in plan view are provided. The number of upper trays 51c may be one or three or more.
 積層された2つの上部トレー51cがベーストレー51b上に積層されると、各トレー51b、51cの外壁により、隔壁51dが形成される。隔壁51dは、筐体51aの天壁51eと底壁51fとを接続するように形成され、筐体51a内の空間を内外に仕切る。この隔壁51dと筐体51aの外周壁51gとの間には、キャリアガス供給空間51hが形成される。キャリアガス供給空間51hは、筐体51aの枠体部分内部に形成された管路51jの一端と接続されている。管路51jは、キャリアガスが、天壁51e、外周壁51g及び底壁51f内を通り、キャリアガス供給空間51hに至るように形成されている。また、管路51jの他端は、キャリアガスを供給するキャリアガス供給機構60の供給管61の一端に接続されている。供給管61の他端はキャリアガス供給源62に接続されている。供給管61には、マスフローコントローラ等の流量制御部(図示せず)やキャリアガスの供給を開始または停止する開閉弁63が設けられている。なお、本例において、キャリアガス供給機構60から供給されるキャリアガスは一酸化炭素(CO)ガスである。また、供給管61には、キャリアガスを加熱するためのキャリアガス加熱部(図示せず)が設けられている。これら流量制御部や開閉弁63、キャリアガス加熱部は後述の制御部110によって制御される。さらに、供給管61には、当該供給管61の温度制御のため、温度センサ(図示せず)が設けられている。温度センサによる測定結果は後述の制御部110に出力される。なお、この温度センサには、例えば、白金を用いたセンサが用いられる。 When the two stacked upper trays 51c are stacked on the base tray 51b, a partition wall 51d is formed by the outer wall of each tray 51b, 51c. The partition wall 51d is formed so as to connect the top wall 51e and the bottom wall 51f of the housing 51a, and partitions the space inside the housing 51a into the inside and the outside. A carrier gas supply space 51h is formed between the partition wall 51d and the outer peripheral wall 51g of the housing 51a. The carrier gas supply space 51h is connected to one end of a conduit 51j formed inside the frame portion of the housing 51a. The pipeline 51j is formed so that the carrier gas passes through the top wall 51e, the outer peripheral wall 51g, and the bottom wall 51f to reach the carrier gas supply space 51h. Further, the other end of the conduit 51j is connected to one end of a supply pipe 61 of a carrier gas supply mechanism 60 that supplies a carrier gas. The other end of the supply pipe 61 is connected to the carrier gas supply source 62. The supply pipe 61 is provided with a flow rate control unit (not shown) such as a mass flow controller and an opening/closing valve 63 for starting or stopping the supply of carrier gas. In this example, the carrier gas supplied from the carrier gas supply mechanism 60 is carbon monoxide (CO) gas. Further, the supply pipe 61 is provided with a carrier gas heating unit (not shown) for heating the carrier gas. The flow rate control unit, the on-off valve 63, and the carrier gas heating unit are controlled by the control unit 110 described later. Further, the supply pipe 61 is provided with a temperature sensor (not shown) for controlling the temperature of the supply pipe 61. The measurement result by the temperature sensor is output to the control unit 110 described later. For this temperature sensor, for example, a sensor using platinum is used.
 また、ベーストレー51b及び上部トレー51cそれぞれの外壁には開口51kが形成されている。 Also, openings 51k are formed in the outer wall of each of the base tray 51b and the upper tray 51c.
 このような構成により、キャリアガス供給機構60から供給されたキャリアガスが、各トレー51b、51cの外側から、ベーストレー51b及び上部トレー51cに載置された固体原料Mの上方に供給される。その後、キャリアガスは、固体原料Mが昇華して生成された原料ガスと共に、筐体51a内の中央に向かい、天壁51eの中央に形成された開口51mを介して、処理容器10に供給される。 With such a configuration, the carrier gas supplied from the carrier gas supply mechanism 60 is supplied from the outside of the trays 51b and 51c above the solid raw material M placed on the base tray 51b and the upper tray 51c. After that, the carrier gas is supplied to the processing container 10 through the opening 51m formed in the center of the top wall 51e toward the center of the housing 51a, together with the source gas generated by the sublimation of the solid material M. To.
 また、筐体51aには、その全体を覆うように、タンク加熱部70が設けられている。タンク加熱部70は、原料タンク51を加熱し、具体的には、筐体51aを加熱するものである。タンク加熱部70による加熱によって、筐体51a内の固体原料の昇華を促進させることができる。このタンク加熱部70は、後述の制御部110によって制御される。 Further, the housing 51a is provided with a tank heating unit 70 so as to cover the entire body. The tank heating unit 70 heats the raw material tank 51, specifically, the casing 51a. The heating by the tank heating unit 70 can promote the sublimation of the solid raw material in the housing 51a. The tank heating unit 70 is controlled by the control unit 110 described later.
 さらに、筐体51aの天壁51eには、筐体51aの外部に設けられた圧力センサ80が配管81を介して接続されている。圧力センサ80は、例えばキャパシタンスマノメータであり、配管81を介して、原料タンク51の圧力として、筐体51a内の圧力を測定する。
 さらにまた、筐体51aの外周壁51gには、原料タンク51の温度、具体的には筐体51aの温度を測定する温度センサ90が設けられている。温度センサ90は、例えば、白金を用いたセンサである。温度センサ90は、図の例では1つであるが、複数設けられてもよい。
 圧力センサ80や温度センサ90での測定結果は、後述の制御部110に出力される。
Further, a pressure sensor 80 provided outside the housing 51a is connected to the top wall 51e of the housing 51a via a pipe 81. The pressure sensor 80 is, for example, a capacitance manometer, and measures the pressure inside the housing 51a as the pressure of the raw material tank 51 via the pipe 81.
Furthermore, a temperature sensor 90 for measuring the temperature of the raw material tank 51, specifically, the temperature of the housing 51a is provided on the outer peripheral wall 51g of the housing 51a. The temperature sensor 90 is, for example, a sensor using platinum. Although the number of temperature sensors 90 is one in the example shown in the figure, a plurality of temperature sensors 90 may be provided.
The measurement results of the pressure sensor 80 and the temperature sensor 90 are output to the control unit 110 described later.
 図1の説明に戻る。
 原料ガス供給機構50は、上述の原料タンク51の他、原料タンク51からの原料ガスを処理容器10に供給するために原料タンク51と処理容器10とを接続する供給管52を有する。供給管52の一端は、原料タンク51の筐体51aの天壁51eに接続され、他端は、処理容器10の天壁13に接続されており、この供給管52を介して、天壁51eの開口51mと天壁13のガス供給口13bとが連通している。
Returning to the explanation of FIG.
The raw material gas supply mechanism 50 has, in addition to the above-described raw material tank 51, a supply pipe 52 that connects the raw material tank 51 and the processing container 10 to supply the raw material gas from the raw material tank 51 to the processing container 10. One end of the supply pipe 52 is connected to the top wall 51e of the housing 51a of the raw material tank 51, and the other end is connected to the top wall 13 of the processing container 10. The top wall 51e is connected via the supply pipe 52. 51m and the gas supply port 13b of the ceiling wall 13 communicate with each other.
 供給管52には、当該供給管52内の管路を開放または閉止する開閉弁53が設けられている。この開閉弁53は後述の制御部110によって制御される。
 また、供給管52における開閉弁53と原料タンク51との間には、原料タンク51内の圧力、具体的には、原料タンク51の筐体51a内の圧力を調整するための圧力調整弁としてのAPCバルブ54が設けられている。APCバルブ54は、自動圧力調整機能及び遮断機能を備えており、後述の制御部110からの制御信号に基づいて当該APCバルブ54の開度は制御される。APCバルブ54によって、原料タンク51内の圧力(具体的には原料タンク51の筐体51a内の圧力)を予め設定された圧力になるよう調整したり、供給管52内の管路を閉止したりすることができる。
The supply pipe 52 is provided with an on-off valve 53 that opens or closes the pipeline in the supply pipe 52. The on-off valve 53 is controlled by the control unit 110 described later.
Further, between the opening/closing valve 53 in the supply pipe 52 and the raw material tank 51, a pressure adjusting valve for adjusting the pressure in the raw material tank 51, specifically, the pressure in the housing 51a of the raw material tank 51 is provided. APC valve 54 is provided. The APC valve 54 has an automatic pressure adjusting function and a shutoff function, and the opening degree of the APC valve 54 is controlled based on a control signal from the control unit 110 described later. By the APC valve 54, the pressure in the raw material tank 51 (specifically, the pressure in the housing 51a of the raw material tank 51) is adjusted to a preset pressure, or the pipeline in the supply pipe 52 is closed. You can
 また、供給管52には、供給管加熱部55が設けられている。供給管加熱部55は、開閉弁53及びAPCバルブ54を含む供給管52全体を加熱する。これにより、原料ガスが再固化し、開閉弁53及びAPCバルブ54を含む供給管52に付着するのを防ぐことができる。
 なお、原料ガスが再固化し、処理容器10の内壁に付着することを防止するため、処理容器10を加熱する処理容器加熱部100が成膜装置1には設けられている。
Further, the supply pipe 52 is provided with a supply pipe heating unit 55. The supply pipe heating unit 55 heats the entire supply pipe 52 including the on-off valve 53 and the APC valve 54. As a result, it is possible to prevent the raw material gas from solidifying and adhering to the supply pipe 52 including the on-off valve 53 and the APC valve 54.
In order to prevent the raw material gas from resolidifying and adhering to the inner wall of the processing container 10, the processing container heating unit 100 for heating the processing container 10 is provided in the film forming apparatus 1.
 供給管加熱部55や処理容器加熱部100は後述の制御部110によって制御される。
 また、供給管加熱部55による供給管52の温度制御のため、供給管52に温度センサ(図示せず)が設けられ、処理容器加熱部100による処理容器10の温度制御のため、処理容器10の例えば側壁11に温度センサ(図示せず)が設けられている。これら温度センサによる測定結果は後述の制御部110に出力される。なお、これら温度センサには、例えば、白金を用いたセンサが用いられる。
The supply pipe heating unit 55 and the processing container heating unit 100 are controlled by the control unit 110 described later.
Further, a temperature sensor (not shown) is provided in the supply pipe 52 for temperature control of the supply pipe 52 by the supply pipe heating unit 55, and the processing container 10 is provided for temperature control of the processing container 10 by the processing container heating unit 100. For example, a temperature sensor (not shown) is provided on the side wall 11. The measurement results by these temperature sensors are output to the control unit 110 described later. As these temperature sensors, for example, a sensor using platinum is used.
 以上のように構成される成膜装置1には、制御部110が設けられている。制御部110は、例えばCPUやメモリ等を備えたコンピュータにより構成され、プログラム格納部(図示せず)を有している。プログラム格納部には、APCバルブ25、54や開閉弁53等を制御して、成膜装置1における後述のウェハ処理を実現するためのプログラムも格納されている。なお、上記プログラムは、コンピュータに読み取り可能な記憶媒体に記録されていたものであって、当該記憶媒体から制御部110にインストールされたものであってもよい。また、プログラムの一部または全ては専用ハードウェア(回路基板)で実現してもよい。 The film forming apparatus 1 configured as described above is provided with the control unit 110. The control unit 110 is composed of, for example, a computer equipped with a CPU, a memory, or the like, and has a program storage unit (not shown). The program storage unit also stores a program for controlling the APC valves 25 and 54, the on-off valve 53, and the like to realize the wafer processing described later in the film forming apparatus 1. The program may be stored in a computer-readable storage medium and installed in the control unit 110 from the storage medium. Further, part or all of the program may be realized by dedicated hardware (circuit board).
 続いて、成膜装置1を用いて行われるウェハ処理について説明する。 Next, the wafer processing performed using the film forming apparatus 1 will be described.
 まず、開閉弁53、63及びAPCバルブ54が閉状態とされている状態において、Nガス供給ライン(図示せず)から処理容器10内へ直接Nガスが供給されると共に、圧力センサ20での測定結果に基づいてAPCバルブ25の開度が調整され、処理容器10内が所定の圧力(例えば7~10Torr)とされる。この状態で、処理容器10のウェハWの搬出入口(図示せず)に設けられたゲートバルブ(図示せず)が開かれ、処理容器10に隣接する真空雰囲気の搬送室(図示せず)から、上記搬出入口を介して、ウェハWを保持した搬送機構(図示せず)が処理容器10内に挿入される。そして、ウェハWが、前述の待機位置に位置する載置台30の上方に搬送される。次いで上昇した支持ピン(図示せず)の上にウェハWが受け渡され、その後、上記搬送機構は処理容器10から抜き出され、上記ゲートバルブが閉じられる。それと共に、上記支持ピンの下降、載置台30の上昇が行われ、載置台30上にウェハWが載置され、該載置台30が前述の処理位置へ移動され、処理空間Sが形成される。 First, in a state where the on-off valve 53 and 63 and the APC valve 54 is closed, together with the direct N 2 gas is supplied from the N 2 gas supply line (not shown) into the processing chamber 10, the pressure sensor 20 The opening degree of the APC valve 25 is adjusted on the basis of the measurement result in (1), and the inside of the processing container 10 is set to a predetermined pressure (for example, 7 to 10 Torr). In this state, a gate valve (not shown) provided at a carry-in/out port (not shown) of the wafer W of the processing container 10 is opened, and a transfer chamber (not shown) in a vacuum atmosphere adjacent to the processing container 10 is opened. A transfer mechanism (not shown) holding the wafer W is inserted into the processing container 10 through the carry-in / out port. Then, the wafer W is conveyed above the mounting table 30 located at the above-mentioned standby position. Next, the wafer W is transferred onto the raised support pins (not shown), and then the transfer mechanism is taken out of the processing container 10 and the gate valve is closed. At the same time, the support pins are lowered and the mounting table 30 is raised, the wafer W is mounted on the mounting table 30, the mounting table 30 is moved to the processing position, and the processing space S is formed. ..
 次いで、載置台30に設けられたヒータによってウェハWが所定の温度(例えば120~250℃)まで加熱される。 Next, the wafer W is heated to a predetermined temperature (for example, 120 to 250 ° C.) by the heater provided on the mounting table 30.
 ウェハWの温度が上記所定の温度に到達すると、APCバルブ25の開度が調整され、処理容器10内が所定の圧力(例えば5mTorr~100mTorr)へ減圧される。
 処理容器10内の減圧が完了すると、処理容器10内の処理空間Sへの原料ガスの供給が開始されるよう、開閉弁53,63が開状態とされると共に、APCバルブ54の開度が調整される。これによって、CVD(Chemical Vapor Deposition)による、処理空間S内のウェハW上へのRu膜の形成が開始される。APCバルブ54の開度は、例えば、開閉弁53,63が開状態とされてから、原料タンク51内の圧力(具体的には原料タンク51の筐体51a内の圧力)が設定圧力(例えば40mTorr~150mTorr)に到達するまでの間は、段階的に大きくなるよう調整される。そして、上記設定圧力に到達すると、以後、Ru膜形成が完了するまで、APCバルブ54の開度は、圧力センサ80での測定結果に基づいて制御され、原料タンク51内の圧力が上記設定圧力で一定になるよう調整される。原料タンク51内の圧力が上記設定圧力で一定に維持されたら、キャリアガス供給機構60にかかる開閉弁63は閉状態とされる。この開閉弁63は、以後、原料タンク51より下流側で変動(APCバルブ25の開度の上昇等)が発生する度に、調圧のため開状態とされる。
When the temperature of the wafer W reaches the predetermined temperature, the opening degree of the APC valve 25 is adjusted, and the pressure inside the processing container 10 is reduced to a predetermined pressure (for example, 5 mTorr to 100 mTorr).
When the depressurization in the processing container 10 is completed, the on-off valves 53 and 63 are opened and the opening degree of the APC valve 54 is increased so that the supply of the raw material gas to the processing space S in the processing container 10 is started. Adjusted. As a result, the formation of the Ru film on the wafer W in the processing space S by CVD (Chemical Vapor Deposition) is started. The opening degree of the APC valve 54 is set by, for example, the pressure inside the raw material tank 51 (specifically, the pressure inside the housing 51a of the raw material tank 51) after the on-off valves 53 and 63 are opened. It is adjusted to be gradually increased until it reaches 40 mTorr to 150 mTorr). When the set pressure is reached, thereafter, the opening of the APC valve 54 is controlled based on the measurement result of the pressure sensor 80 until the Ru film formation is completed, and the pressure in the raw material tank 51 is set to the set pressure. Is adjusted to be constant. When the pressure in the raw material tank 51 is maintained constant at the set pressure, the on-off valve 63 on the carrier gas supply mechanism 60 is closed. The on-off valve 63 is opened to adjust the pressure whenever fluctuations (such as an increase in the opening of the APC valve 25) occur downstream of the raw material tank 51.
 Ru膜形成が完了すると、開閉弁53、63が閉状態にされる等して、上記と逆の手順で、ウェハWが処理容器10から搬出される。 When the formation of the Ru film is completed, the opening/ closing valves 53 and 63 are closed, and the wafer W is unloaded from the processing container 10 in the reverse procedure.
 なお、Ru膜の形成処理中、つまり、開閉弁53、63が開状態とされてから閉状態とされるまでの間、キャリアガス加熱部(図示せず)により所定の温度(例えば80℃)に加熱されたキャリアガスが一定流量で供給される。
 また、上述のウェハ処理中、原料タンク51、供給管52及び処理容器10の温度は、少なくとも原料ガスが再固化しないように、対応する温度センサでの測定結果に基づいて、加熱部70、55、100によって所定の温度で一定になるように常時加熱される。例えば、供給管52及び処理容器10は80℃で一定になるよう加熱制御され、原料タンク51は、供給管52や処理容器10より若干低い温度から供給管52や処理容器10より高い温度であって、固体原料の分解温度未満の所定の温度(例えば、上記設定圧力時の分解温度未満の70℃~100℃)で一定になるように加熱制御される。
During the formation process of the Ru film, that is, from the opening state to the closing state of the on-off valves 53 and 63, a predetermined temperature (for example, 80 ° C.) is provided by the carrier gas heating unit (not shown). The carrier gas heated to the surface is supplied at a constant flow rate.
Further, during the wafer processing described above, the temperatures of the raw material tank 51, the supply pipe 52, and the processing container 10 are set to the heating units 70, 55 based on the measurement results of the corresponding temperature sensors so that the raw material gas does not solidify at least. , 100 is constantly heated so as to be constant at a predetermined temperature. For example, the supply pipe 52 and the processing container 10 are heated and controlled so as to be constant at 80 ° C., and the raw material tank 51 has a temperature slightly lower than that of the supply pipe 52 and the processing container 10 and higher than that of the supply pipe 52 and the processing container 10. Therefore, the heating is controlled so as to be constant at a predetermined temperature lower than the decomposition temperature of the solid raw material (for example, 70 ° C. to 100 ° C. lower than the decomposition temperature at the set pressure).
 以上のように、本実施形態では、成膜中において、原料タンク51の筐体51a内の圧力を測定する圧力センサ80に基づいて、原料タンク51と処理容器10とを接続する供給管52に設けられたAPCバルブ54を制御する。したがって、Ru膜の形成処理において、処理容器10内の圧力によらず、原料タンク51内の圧力を一定にすることができる。そのため、処理容器10内の圧力によらない、原料ガスの一定供給を行うことができる。
 また、原料タンク51内の圧力に関する制御を、APCバルブ54の開度の調整のみで行っているため、当該制御が容易である。
As described above, in the present embodiment, the supply pipe 52 that connects the raw material tank 51 and the processing container 10 to each other is formed on the basis of the pressure sensor 80 that measures the pressure in the housing 51a of the raw material tank 51 during film formation. The APC valve 54 provided is controlled. Therefore, in the Ru film forming process, the pressure in the raw material tank 51 can be kept constant regardless of the pressure in the processing container 10. Therefore, the raw material gas can be constantly supplied regardless of the pressure in the processing container 10.
Further, since the pressure in the raw material tank 51 is controlled only by adjusting the opening degree of the APC valve 54, the control is easy.
 なお、本実施形態のように処理容器内10内の圧力と原料タンク51内の圧力とを独立して制御しているということは、処理容器内10内の圧力と、原料ガスの供給量とを独立に制御しているということを意味する。本実施形態では、処理容器内10内の圧力と、原料ガスの供給量とを独立に制御しているため、成膜処理に問題が生じた場合に、その問題が、処理容器10内の圧力に関する処理条件と原料ガスの供給量に関する処理条件とのどちらに起因しているかを切り分けることができる。 In addition, the fact that the pressure in the processing container 10 and the pressure in the raw material tank 51 are independently controlled as in the present embodiment means that the pressure in the processing container 10 and the supply amount of the raw material gas are controlled. It means that they are controlled independently. In the present embodiment, the pressure inside the processing container 10 and the supply amount of the raw material gas are independently controlled. Therefore, when a problem occurs in the film forming process, the problem is the pressure inside the processing container 10. It is possible to distinguish whether the cause is the treatment condition related to the above or the processing condition related to the supply amount of the raw material gas.
 また、処理容器10内の構成が異なる場合(例えば邪魔板40の形状が変わっても)、処理容器10内のコンダクタンスも異なるようになるので、圧力センサ20での測定結果が同じでも、上記構成が異なる部分より上流側の圧力も異なってくる。したがって、処理容器10内の構成が異なる場合、特許文献1のような構成では、原料タンク内の圧力も異なり、原料ガスの供給量も異なってくる。それに対し、本実施形態では、原料タンク51の圧力を独立して制御しているため、処理容器10内の構成が異なる場合でも、同じ量の原料ガスを供給することができる。 Further, when the configuration inside the processing container 10 is different (for example, even when the shape of the baffle plate 40 is changed), the conductance inside the processing container 10 is also different. The pressure on the upstream side of the different part also differs. Therefore, when the internal structure of the processing container 10 is different, the internal pressure of the raw material tank is different and the supply amount of the raw material gas is also different in the structure of Patent Document 1. On the other hand, in the present embodiment, since the pressure of the raw material tank 51 is controlled independently, the same amount of raw material gas can be supplied even when the internal structure of the processing container 10 is different.
 なお、原料タンク51内の設定圧力は、処理容器10に対する圧力センサ20での測定結果に応じて、可変としてもよい。例えば、原料タンク51内の圧力と処理容器10内の圧力との差圧が一定になるように、圧力センサ20での測定結果が高いときは、原料タンク51内の圧力を高くし、圧力センサ20での測定結果が低いときは、原料タンク51内の圧力を低くするようにしてもよい。 The set pressure in the raw material tank 51 may be variable depending on the measurement result of the pressure sensor 20 for the processing container 10. For example, when the measurement result by the pressure sensor 20 is high so that the pressure difference between the pressure in the raw material tank 51 and the pressure in the processing container 10 is constant, the pressure in the raw material tank 51 is increased to increase the pressure sensor. When the measurement result at 20 is low, the pressure in the raw material tank 51 may be lowered.
 さらに、本実施形態では、原料タンク51の筐体51aが高温になるようにしている。具体的には、原料タンク51の温度を、供給管52や処理容器10より高い温度であって、固体原料の分解温度未満の所定の温度(例えば90~100℃)で一定になるようにしている。したがって、原料ガスの供給量を、原料タンク51の筐体51a内の圧力が処理容器10内の圧力より高くても、上記筐体51a内の圧力が処理容器10内の圧力と略等しいときと同等以上とすることができる。
 なお、原料タンク51の筐体51aの温度は、原料タンク51内の設定圧力に応じて可変としてもよい。例えば、上記設定圧力が高いときは、原料タンク51の筐体51aの温度を高くしてもよい。これにより、個体原料が分解しない範囲で、原料ガスの供給量を増加させることができる。
Further, in the present embodiment, the temperature of the housing 51a of the raw material tank 51 is set to be high. Specifically, the temperature of the raw material tank 51 is set to be constant at a predetermined temperature (for example, 90 to 100 ° C.) which is higher than the supply pipe 52 and the processing container 10 and lower than the decomposition temperature of the solid raw material. There is. Therefore, the supply amount of the raw material gas is the same as when the pressure in the housing 51a of the raw material tank 51 is higher than the pressure in the processing container 10 but the pressure in the housing 51a is substantially equal to the pressure in the processing container 10. It can be equal or higher.
The temperature of the housing 51a of the raw material tank 51 may be variable according to the set pressure in the raw material tank 51. For example, when the set pressure is high, the temperature of the housing 51a of the raw material tank 51 may be raised. As a result, the supply amount of the raw material gas can be increased as long as the solid raw material is not decomposed.
 さらにまた、本実施形態では、原料タンク51の筐体51aの温度を測定する温度センサ90として、白金を用いたものを用いている。したがって、温度センサ90での測定結果に基づいて、原料タンクの筐体51aの温度を高精度に制御することができ、原料ガスの供給量を高精度に制御することができる。
 なお、処理容器10や供給管52,61に対する温度センサにも、白金を用いたセンサを用いている。したがって、処理容器10や供給管52、61の温度を高精度に制御することができる。
Furthermore, in the present embodiment, a temperature sensor 90 using platinum is used as the temperature sensor 90 for measuring the temperature of the housing 51a of the raw material tank 51. Therefore, the temperature of the housing 51a of the raw material tank can be controlled with high accuracy based on the measurement result of the temperature sensor 90, and the supply amount of the raw material gas can be controlled with high accuracy.
A platinum sensor is also used as the temperature sensor for the processing container 10 and the supply pipes 52 and 61. Therefore, the temperatures of the processing container 10 and the supply pipes 52 and 61 can be controlled with high accuracy.
 さらにまた、本実施形態では、ウェハ処理において、開閉弁53を開状態にしてから原料タンク51内の圧力が設定圧力に到達するまでの間、すなわち、Ru膜形成の初期段階において、APCバルブ54の開度を段階的に大きくしている。したがって、Ru膜形成の初期段階において、APCバルブ54を閉止している間に原料タンク51内に蓄積された原料ガスが、処理容器10内に大量に流れ込むのを防ぐことができる。
 なお、以上の説明では、ウェハWの搬出入時やウェハWの加熱時に、開閉弁53及びAPCバルブ54の両方を閉状態としているが、APCバルブ54のみを閉状態とするようにしてもよい。
Furthermore, in the present embodiment, in the wafer processing, the APC valve 54 is operated from the time when the on-off valve 53 is opened until the pressure in the raw material tank 51 reaches the set pressure, that is, in the initial stage of the Ru film formation. The opening degree of is gradually increased. Therefore, it is possible to prevent a large amount of the raw material gas accumulated in the raw material tank 51 from flowing into the processing container 10 while the APC valve 54 is closed in the initial stage of the Ru film formation.
In the above description, both the opening/closing valve 53 and the APC valve 54 are closed when the wafer W is loaded/unloaded or when the wafer W is heated, but only the APC valve 54 may be closed. ..
 また、本実施形態では、処理容器10内の圧力より高い雰囲気すなわち高圧雰囲気の原料タンク51の筐体51aから、低圧雰囲気の処理容器10へ原料ガスを供給している。したがって、高圧雰囲気の原料タンク51からの原料ガスは、処理容器10内で膨張するため、処理空間SにおいてウェハWと反応する分子の数が多いので、成膜速度を高くすることができる。 Further, in the present embodiment, the source gas is supplied to the processing container 10 in the low pressure atmosphere from the casing 51a of the raw material tank 51 in the atmosphere higher than the pressure inside the processing container 10, that is, the high pressure atmosphere. Therefore, since the raw material gas from the raw material tank 51 in the high-pressure atmosphere expands in the processing container 10, the number of molecules that react with the wafer W in the processing space S is large, so that the film formation rate can be increased.
 なお、APCバルブ54は、処理容器10の直近に配置してもよく、より具体的には、処理容器10の天壁13の上面から当該APCバルブ54の下面までの距離が10mm以下となるように配置してもよい。原料タンク51から供給管52のAPCバルブ54までを原料ガスの収納容器と考えると、APCバルブ54を処理容器10の近くに配設しておくことで、上記収納容器内の原料ガスは処理容器10内に供給されるときに当該処理容器10の直近で初めて低圧化される。したがって、圧力勾配による原料ガスの分解等を処理容器10の天壁13の直近まで防ぐことができる。 The APC valve 54 may be arranged in the immediate vicinity of the processing container 10. More specifically, the distance from the upper surface of the ceiling wall 13 of the processing container 10 to the lower surface of the APC valve 54 is 10 mm or less. It may be placed in. Considering from the raw material tank 51 to the APC valve 54 of the supply pipe 52 as a raw material gas storage container, by disposing the APC valve 54 near the processing container 10, the raw material gas in the storage container is processed by the processing container. When supplied to the inside of the processing container 10, the pressure is first lowered in the immediate vicinity of the processing container 10. Therefore, decomposition of the raw material gas due to the pressure gradient can be prevented up to the vicinity of the top wall 13 of the processing container 10.
(第2実施形態)
 図3は、第2実施形態にかかる成膜装置1aの構成の概略を模式的に示す説明図であり、成膜装置1aの一部を断面で示している。
 図3の成膜装置1aでは、供給管52における開閉弁53とAPCバルブ54との間に、排気バイパス管120の一端が接続されている。排気バイパス管120の他端は、排気装置24に接続されている。この排気バイパス管120により、処理容器10を介さずに原料タンク51と排気装置24とが通じている。排気バイパス管120には、当該排気バイパス管120の管路を開放または閉止する開閉弁121が設けられている。
 なお、原料ガスが再固化し、排気バイパス管120の内壁に付着することを防止するため、排気バイパス管120を加熱する排気バイパス管加熱部(図示せず)が成膜装置1には設けられている。また、排気バイパス管120の温度制御のため、排気バイパス管120には、当該排気バイパス管120の温度を測定する温度センサ(図示せず)が設けられている。この温度センサでの測定結果は、制御部110に出力され、排気バイパス管120は制御部110に制御される。
(Second embodiment)
FIG. 3 is an explanatory view schematically showing the outline of the configuration of the film forming apparatus 1a according to the second embodiment, and a part of the film forming apparatus 1a is shown in cross section.
In the film forming apparatus 1a of FIG. 3, one end of the exhaust bypass pipe 120 is connected between the on-off valve 53 and the APC valve 54 in the supply pipe 52. The other end of the exhaust bypass pipe 120 is connected to the exhaust device 24. The exhaust bypass pipe 120 communicates the raw material tank 51 and the exhaust device 24 without passing through the processing container 10. The exhaust bypass pipe 120 is provided with an on-off valve 121 that opens or closes the pipeline of the exhaust bypass pipe 120.
In order to prevent the raw material gas from resolidifying and adhering to the inner wall of the exhaust bypass pipe 120, an exhaust bypass pipe heating unit (not shown) for heating the exhaust bypass pipe 120 is provided in the film forming apparatus 1. ing. Further, in order to control the temperature of the exhaust bypass pipe 120, the exhaust bypass pipe 120 is provided with a temperature sensor (not shown) that measures the temperature of the exhaust bypass pipe 120. The measurement result of this temperature sensor is output to the control unit 110, and the exhaust bypass pipe 120 is controlled by the control unit 110.
 続いて、成膜装置1aを用いて行われるウェハ処理について説明する。 Next, the wafer processing performed using the film forming apparatus 1a will be described.
 第1実施形態の成膜装置1を用いたウェハ処理では、ウェハWの搬入出時等において、APCバルブ54は閉状態とされ、キャリアガス供給機構60にかかる開閉弁63は閉状態とされていた。
 それに対し、成膜装置1aを用いて行われるウェハ処理では、ウェハWの搬入出時も含め、常時、APCバルブ54は圧力センサ80での測定結果に基づいてその開度が調整され、開閉弁63は開状態とされる。ただし、開閉弁53が閉状態とされている間は、排気バイパス管120に設けられた開閉弁121が開状態とされる。
 そして、本ウェハ処理では、処理容器10への原料ガスの供給を開始する際、開閉弁53を閉状態から開状態とすると共に、開閉弁121を開状態から閉状態とする。これにより、開閉弁53を開状態とした直後に、大量の原料ガスが処理容器10内に流れ込むのを防いでいる。
 なお、開閉弁53を閉状態から開状態とするときに、排気バイパス管120に設けられた開閉弁121を開状態のままとしてもよい。
In the wafer processing using the film forming apparatus 1 of the first embodiment, the APC valve 54 is closed and the opening/closing valve 63 of the carrier gas supply mechanism 60 is closed when the wafer W is loaded and unloaded. It was
On the other hand, in the wafer processing performed using the film forming apparatus 1a, the opening of the APC valve 54 is constantly adjusted based on the measurement result of the pressure sensor 80, including when the wafer W is loaded and unloaded, and the opening/closing valve is opened. 63 is opened. However, while the on-off valve 53 is in the closed state, the on-off valve 121 provided in the exhaust bypass pipe 120 is in the open state.
Then, in the present wafer processing, when the supply of the source gas to the processing container 10 is started, the open/close valve 53 is changed from the closed state to the open state, and the open/close valve 121 is changed from the open state to the closed state. As a result, a large amount of raw material gas is prevented from flowing into the processing container 10 immediately after the on-off valve 53 is opened.
When the on-off valve 53 is changed from the closed state to the open state, the on-off valve 121 provided in the exhaust bypass pipe 120 may be left in the open state.
(第3実施形態)
 図4は、第3実施形態にかかる成膜装置1bの構成の概略を模式的に示す説明図であり、成膜装置1bの一部を断面で示している。
 図4の成膜装置1bは、原料タンク51の筐体51aが、収容室R1の下流側に、原料ガスを蓄積するバッファ室R2を内部に有する。収容室R1とバッファ室R2との間は、開口51pを有する隔壁51nにより仕切られている。
 本実施形態によれば、バッファ室R2に原料ガスを蓄積することができるため、原料ガスを処理容器10に安定的に供給することができる。
(Third Embodiment)
FIG. 4 is an explanatory view schematically showing an outline of the configuration of the film forming apparatus 1b according to the third embodiment, and shows a part of the film forming apparatus 1b in a cross section.
In the film forming apparatus 1b of FIG. 4, the housing 51a of the raw material tank 51 has a buffer chamber R2 inside which stores the raw material gas on the downstream side of the storage chamber R1. The storage chamber R1 and the buffer chamber R2 are separated by a partition wall 51n having an opening 51p.
According to the present embodiment, since the raw material gas can be accumulated in the buffer chamber R2, the raw material gas can be stably supplied to the processing container 10.
 なお、本実施形態のようにバッファ室R2を設ける場合、圧力センサ80による圧力測定対象は、収容室R1ではなく、バッファ室R2としてもよい。また、キャリアガス供給機構60からのガスの供給先を、収容室R1ではなく、バッファ室R2としてもよい。 When the buffer chamber R2 is provided as in the present embodiment, the pressure measurement target by the pressure sensor 80 may be the buffer chamber R2 instead of the accommodation chamber R1. Further, the supply destination of the gas from the carrier gas supply mechanism 60 may be the buffer chamber R2 instead of the accommodation chamber R1.
 以上の説明では、原料タンク51の筐体51aを1つの加熱部で加熱していたが、筐体51aの領域を複数に分割し、領域毎に加熱部を設け、領域毎に温度制御を行うようにしてもよい。供給管52や処理容器10、キャリアガス供給管に対する加熱部についても同様である。なお、上述のように領域毎に加熱する場合、領域毎に1または複数の温度センサが設けられる。
 また、上述のように領域毎に加熱する場合、供給管52、61等、各種弁や流量制御部が設けられている部材については、各種弁等が設けられている領域と他の領域とで区分してもよい。各種弁や流量制御部と配管とでは同じ加熱量であっても温度が異なることがあるからである。
In the above description, the casing 51a of the raw material tank 51 is heated by one heating unit, but the region of the casing 51a is divided into a plurality of regions, the heating unit is provided for each region, and the temperature control is performed for each region. You may do it. The same applies to the heating section for the supply pipe 52, the processing container 10, and the carrier gas supply pipe. When heating is performed for each region as described above, one or a plurality of temperature sensors are provided for each region.
When heating in each region as described above, regarding the members such as the supply pipes 52 and 61 that are provided with various valves and flow rate control units, the regions where various valves are provided and other regions are different. You may divide. This is because the temperatures of various valves and flow control units and the piping may differ even if the amount of heating is the same.
 各加熱部には、シリコンラバーヒータやジャケット式ヒータ、リボンヒータ等の各種ヒータを用いることができる。
 また、原料タンク51の設定温度(具体的には筐体51aの設定温度)と、供給管52などの他の部分の設定温度は独立としてもよいが、原料タンク51の設定温度に応じて、上記他の部分の設定温度を変更するようにしてもよい。
Various heaters such as a silicon rubber heater, a jacket type heater, and a ribbon heater can be used for each heating unit.
Further, the set temperature of the raw material tank 51 (specifically, the set temperature of the housing 51a) and the set temperature of other parts such as the supply pipe 52 may be independent, but depending on the set temperature of the raw material tank 51, The set temperature of the other parts may be changed.
 以上の説明では、Ru膜に対する固体原料として、Ru(CO)12を用いていたが他の固体原料であってもよい。
 また、固体原料の代わりに液体原料を用いてもよい。なお、固体原料とは、大気圧、室温で固体の原料を意味し、液体原料とは、大気圧、室温で液体の原料を意味する。
In the above description, Ru 3 (CO) 12 is used as the solid raw material for the Ru film, but other solid raw materials may be used.
A liquid raw material may be used instead of the solid raw material. The solid raw material means a solid raw material at atmospheric pressure and room temperature, and the liquid raw material means a liquid raw material at atmospheric pressure and room temperature.
 以上の説明では、Ru膜を成膜していた。しかし、本開示にかかる技術は、固体原料または液体原料を気化して生成した原料ガスを用いて他の膜を形成する装置にも適用することができる。 In the above explanation, the Ru film was formed. However, the technique according to the present disclosure can also be applied to an apparatus that forms another film by using a raw material gas generated by vaporizing a solid raw material or a liquid raw material.
 また、以上の説明では、キャリアガスとしてCOガスを用いていたが、Arガスなどの希ガスやN等の不活性ガスを用いることができる。ただし、COガスを用いることで、原料ガスの分解を防ぐことができる。 Further, in the above description, CO gas is used as the carrier gas, but a rare gas such as Ar gas or an inert gas such as N 2 can be used. However, by using CO gas, decomposition of the raw material gas can be prevented.
 なお、以上の説明では、開閉弁53の上流側にAPCバルブ54が設けられていたが、開閉弁53の下流側にAPCバルブ54を設けてもよい。また、開閉弁53を省略し、開閉弁53の位置、すなわち、供給管52における処理容器10側の位置に、APCバルブ54を設けるようにしてもよい。 In the above description, the APC valve 54 is provided on the upstream side of the opening/closing valve 53, but the APC valve 54 may be provided on the downstream side of the opening/closing valve 53. Further, the opening/closing valve 53 may be omitted, and the APC valve 54 may be provided at the position of the opening/closing valve 53, that is, the position of the supply pipe 52 on the processing container 10 side.
 今回開示された実施形態はすべての点で例示であって制限的なものではないと考えられるべきである。上記の実施形態は、添付の請求の範囲及びその主旨を逸脱することなく、様々な形態で省略、置換、変更されてもよい。 The embodiments disclosed this time should be considered to be exemplary in all respects and not restrictive. The above-described embodiment may be omitted, replaced, or changed in various forms without departing from the scope of the appended claims and the gist thereof.
 なお、以下のような構成も本開示の技術的範囲に属する。
(1)基板に所定の膜を形成する成膜装置であって、
減圧可能に構成され、前記基板を収容する処理容器と、
液体原料または固体原料を貯留する原料タンクと、
前記液体原料または前記固体原料が前記原料タンク内で気化して生成された原料ガスが前記処理容器に供給されるよう、前記原料タンクと前記処理容器とを接続する供給管と、
前記供給管に設けられた、開度可変な圧力調整弁と、
前記原料タンク内の圧力を測定する圧力センサと、
前記圧力センサでの測定結果に基づいて、前記圧力調整弁を制御する制御部と、を有する、成膜装置。
 前記(1)では、原料タンク内の圧力を測定する圧力センサでの測定結果に基づいて、原料タンクと処理容器とを接続する供給管に設けられた圧力調整弁を制御する。したがって、所定の膜の形成処理において、処理容器内の圧力によらず、原料タンク内の圧力を一定にすることができる。そのため、処理容器内の圧力によらない、原料ガスの一定供給を行うことができる。
The following configurations also belong to the technical scope of the present disclosure.
(1) A film forming apparatus for forming a predetermined film on a substrate,
A processing container that is configured to be depressurizable and that stores the substrate,
A raw material tank for storing a liquid raw material or a solid raw material,
A supply pipe connecting the raw material tank and the processing container, so that the raw material gas generated by vaporizing the liquid raw material or the solid raw material in the raw material tank is supplied to the processing container,
A pressure adjusting valve provided in the supply pipe and having a variable opening degree;
A pressure sensor for measuring the pressure in the raw material tank,
A film forming apparatus including a control unit that controls the pressure adjusting valve based on the measurement result of the pressure sensor.
In the above (1), the pressure regulating valve provided in the supply pipe connecting the raw material tank and the processing container is controlled based on the measurement result of the pressure sensor that measures the pressure in the raw material tank. Therefore, in the predetermined film forming process, the pressure in the raw material tank can be kept constant regardless of the pressure in the processing container. Therefore, a constant supply of the raw material gas can be performed regardless of the pressure in the processing container.
(2)前記制御部は、成膜時において、前記原料タンク内の圧力が前記処理容器内の圧力より高くなるように前記圧力調整弁を制御する、前記(1)に記載の成膜装置。 (2) The film forming apparatus according to (1), wherein the control unit controls the pressure adjusting valve so that the pressure in the raw material tank becomes higher than the pressure in the processing container at the time of film formation.
(3)前記原料タンクの温度を測定する温度センサと、
前記原料タンクを加熱する加熱部と、を有し、
前記制御部はさらに、前記温度センサでの測定結果に基づいて、前記原料タンクの温度が前記供給管の温度より高くなるように、前記加熱部を制御する、前記(1)または(2)に記載の成膜装置。
 前記(3)によれば、原料タンクが高温になるようにしているため、原料ガスの供給量を、原料タンク内の圧力が処理容器内の圧力より高くても、原料タンク内の圧力が処理容器内の圧力と略等しいときと同等以上とすることができる。
(3) A temperature sensor for measuring the temperature of the raw material tank and
It has a heating unit that heats the raw material tank,
The control unit further controls the heating unit so that the temperature of the raw material tank becomes higher than the temperature of the supply pipe based on the measurement result of the temperature sensor, according to the above (1) or (2). The film forming apparatus described.
According to (3) above, since the raw material tank is made to have a high temperature, the pressure in the raw material tank processes the supply amount of the raw material gas even if the pressure in the raw material tank is higher than the pressure in the processing container. It can be equal to or higher than the pressure in the container.
(4)前記温度センサは、白金を用いたものである、前記(3)に記載の成膜装置。
 前記(4)によれば、高精度に原料タンクの温度を制御することができ、原料ガスの供給量を高精度に制御することができる。
(4) The film forming apparatus according to (3) above, wherein the temperature sensor uses platinum.
According to the above (4), the temperature of the raw material tank can be controlled with high accuracy, and the supply amount of the raw material gas can be controlled with high accuracy.
(5)前記原料タンクは、前記液体原料または前記固体原料を収容する収容室の下流側に、原料ガスを蓄積するバッファ室を有する、前記(1)~(4)のいずれか1に記載の成膜装置。 (5) The raw material tank according to any one of (1) to (4) above, wherein the raw material tank has a buffer chamber for accumulating the raw material gas on the downstream side of the storage chamber for accommodating the liquid raw material or the solid raw material. Film forming equipment.
(6)前記原料タンクにキャリアガスを供給するキャリアガス供給機構をさらに有する、前記(1)~(5)のいずれか1に記載の成膜装置。 (6) The film forming apparatus according to any one of (1) to (5), further including a carrier gas supply mechanism that supplies a carrier gas to the raw material tank.
(7)前記所定の膜は、ルテニウム膜である、前記(1)~(6)のいずれか1に記載の成膜装置。 (7) The film forming apparatus according to any one of (1) to (6) above, wherein the predetermined film is a ruthenium film.
(8)基板に所定の膜を形成する成膜装置の処理容器内に原料ガスを供給する原料ガス供給方法であって、
液体原料または固体原料を貯留する原料タンク内の圧力に基づいて、前記原料タンクと前記処理容器とを接続する供給管に設けられた圧力調整弁の開度を調整する工程と、
前記原料タンク内の前記液体原料または前記固体原料を気化させ前記原料ガスを生成する工程と、
生成された原料ガスを前記供給管を介して前記処理容器に供給する工程と、を有する、原料ガスの供給方法。
(8) A raw material gas supply method for supplying a raw material gas into a processing container of a film forming apparatus that forms a predetermined film on a substrate.
A step of adjusting the opening degree of a pressure adjusting valve provided in a supply pipe connecting the raw material tank and the processing container based on the pressure in the raw material tank for storing the liquid raw material or the solid raw material.
A step of vaporizing the liquid raw material or the solid raw material in the raw material tank to generate the raw material gas, and
A method for supplying a raw material gas, comprising a step of supplying the generated raw material gas to the processing container via the supply pipe.
1、1a、1b 成膜装置
10      処理容器
51      原料タンク
52      供給管
54      APCバルブ
80      圧力センサ
110     制御部
W       ウェハ
1, 1a, 1b Film deposition equipment 10 Processing container 51 Raw material tank 52 Supply pipe 54 APC valve 80 Pressure sensor 110 Control unit W wafer

Claims (8)

  1. 基板に所定の膜を形成する成膜装置であって、
    減圧可能に構成され、前記基板を収容する処理容器と、
    液体原料または固体原料を貯留する原料タンクと、
    前記液体原料または前記固体原料が前記原料タンク内で気化して生成された原料ガスが前記処理容器に供給されるよう、前記原料タンクと前記処理容器とを接続する供給管と、
    前記供給管に設けられた、開度可変な圧力調整弁と、
    前記原料タンク内の圧力を測定する圧力センサと、
    前記圧力センサでの測定結果に基づいて、前記圧力調整弁を制御する制御部と、を有する、成膜装置。
    A film forming apparatus for forming a predetermined film on a substrate,
    A processing container that is configured to be depressurizable and that stores the substrate,
    A raw material tank for storing a liquid raw material or a solid raw material,
    A supply pipe connecting the raw material tank and the processing container, so that the raw material gas generated by vaporizing the liquid raw material or the solid raw material in the raw material tank is supplied to the processing container,
    A pressure adjusting valve provided in the supply pipe and having a variable opening degree;
    A pressure sensor for measuring the pressure in the raw material tank,
    A film forming apparatus including a control unit that controls the pressure adjusting valve based on the measurement result of the pressure sensor.
  2. 前記制御部は、成膜時において、前記原料タンク内の圧力が前記処理容器内の圧力より高くなるように前記圧力調整弁を制御する、請求項1に記載の成膜装置。 The film forming apparatus according to claim 1, wherein the control unit controls the pressure adjusting valve so that the pressure in the raw material tank becomes higher than the pressure in the processing container during film formation.
  3. 前記原料タンクの温度を測定する温度センサと、
    前記原料タンクを加熱する加熱部と、を有し、
    前記制御部はさらに、前記温度センサでの測定結果に基づいて、前記原料タンクの温度が前記供給管の温度より高くなるように、前記加熱部を制御する、請求項1または2に記載の成膜装置。
    A temperature sensor for measuring the temperature of the raw material tank,
    It has a heating unit that heats the raw material tank,
    The result according to claim 1 or 2, wherein the control unit further controls the heating unit so that the temperature of the raw material tank becomes higher than the temperature of the supply pipe based on the measurement result of the temperature sensor. Membrane device.
  4. 前記温度センサは、白金を用いたものである、請求項3に記載の成膜装置。 The film forming apparatus according to claim 3, wherein the temperature sensor uses platinum.
  5. 前記原料タンクは、前記液体原料または固体原料を収容する原料室の下流側に、原料ガスを蓄積するバッファ室を有する、請求項1~4のいずれか1項に記載の成膜装置。 The film forming apparatus according to any one of claims 1 to 4, wherein the raw material tank has a buffer chamber for accumulating the raw material gas downstream of the raw material chamber for accommodating the liquid raw material or the solid raw material.
  6. 前記原料タンクにキャリアガスを供給するキャリアガス供給機構をさらに有する、請求項1~5のいずれか1項に記載の成膜装置。 The film forming apparatus according to any one of claims 1 to 5, further comprising a carrier gas supply mechanism for supplying carrier gas to the raw material tank.
  7. 前記所定の膜は、ルテニウム膜である、請求項1~6のいずれか1項に記載の成膜装置。 The film forming apparatus according to any one of claims 1 to 6, wherein the predetermined film is a ruthenium film.
  8. 基板に所定の膜を形成する成膜装置の処理容器内に原料ガスを供給する原料ガス供給方法であって、
    液体原料または固体原料を貯留する原料タンク内の圧力に基づいて、前記原料タンクと前記処理容器とを接続する供給管に設けられた圧力調整弁の開度を調整する工程と、
    前記原料タンク内の前記液体原料または前記固体原料を気化させ前記原料ガスを生成する工程と、
    生成された原料ガスを前記供給管を介して前記処理容器に供給する工程と、を有する、原料ガスの供給方法。
    A raw material gas supply method for supplying a raw material gas into a processing container of a film forming apparatus that forms a predetermined film on a substrate.
    Based on the pressure in the raw material tank that stores the liquid raw material or the solid raw material, a step of adjusting the opening degree of the pressure adjusting valve provided in the supply pipe connecting the raw material tank and the processing container,
    A step of vaporizing the liquid raw material or the solid raw material in the raw material tank to generate the raw material gas, and
    A method for supplying a raw material gas, comprising a step of supplying the generated raw material gas to the processing container via the supply pipe.
PCT/JP2020/007693 2019-03-07 2020-02-26 Film-forming apparatus and material gas feeding method WO2020179575A1 (en)

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JP2002162285A (en) * 2000-10-31 2002-06-07 Applied Materials Inc Liquid storing container and level detecting method
JP2010109302A (en) * 2008-10-31 2010-05-13 Horiba Ltd Material gas concentration control system
JP2017205736A (en) * 2016-05-20 2017-11-24 日本エア・リキード株式会社 Sublimation gas supply system and sublimation gas supply method

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Publication number Priority date Publication date Assignee Title
JP2002162285A (en) * 2000-10-31 2002-06-07 Applied Materials Inc Liquid storing container and level detecting method
JP2010109302A (en) * 2008-10-31 2010-05-13 Horiba Ltd Material gas concentration control system
JP2017205736A (en) * 2016-05-20 2017-11-24 日本エア・リキード株式会社 Sublimation gas supply system and sublimation gas supply method

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