WO2013008344A1 - Plasma processing apparatus - Google Patents
Plasma processing apparatus Download PDFInfo
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- WO2013008344A1 WO2013008344A1 PCT/JP2011/071657 JP2011071657W WO2013008344A1 WO 2013008344 A1 WO2013008344 A1 WO 2013008344A1 JP 2011071657 W JP2011071657 W JP 2011071657W WO 2013008344 A1 WO2013008344 A1 WO 2013008344A1
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- gas
- processing apparatus
- cathode electrode
- plasma processing
- plasma
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Images
Classifications
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01J—ELECTRIC DISCHARGE TUBES OR DISCHARGE LAMPS
- H01J37/00—Discharge tubes with provision for introducing objects or material to be exposed to the discharge, e.g. for the purpose of examination or processing thereof
- H01J37/32—Gas-filled discharge tubes
- H01J37/32431—Constructional details of the reactor
- H01J37/32532—Electrodes
- H01J37/32568—Relative arrangement or disposition of electrodes; moving means
-
- H—ELECTRICITY
- H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
- H05H—PLASMA TECHNIQUE; PRODUCTION OF ACCELERATED ELECTRICALLY-CHARGED PARTICLES OR OF NEUTRONS; PRODUCTION OR ACCELERATION OF NEUTRAL MOLECULAR OR ATOMIC BEAMS
- H05H1/00—Generating plasma; Handling plasma
- H05H1/24—Generating plasma
- H05H1/46—Generating plasma using applied electromagnetic fields, e.g. high frequency or microwave energy
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/22—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the deposition of inorganic material, other than metallic material
- C23C16/30—Deposition of compounds, mixtures or solid solutions, e.g. borides, carbides, nitrides
- C23C16/34—Nitrides
- C23C16/345—Silicon nitride
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/22—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the deposition of inorganic material, other than metallic material
- C23C16/30—Deposition of compounds, mixtures or solid solutions, e.g. borides, carbides, nitrides
- C23C16/40—Oxides
- C23C16/401—Oxides containing silicon
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/44—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
- C23C16/455—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for introducing gases into reaction chamber or for modifying gas flows in reaction chamber
- C23C16/45563—Gas nozzles
- C23C16/45565—Shower nozzles
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/44—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
- C23C16/50—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating using electric discharges
- C23C16/505—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating using electric discharges using radio frequency discharges
- C23C16/509—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating using electric discharges using radio frequency discharges using internal electrodes
- C23C16/5096—Flat-bed apparatus
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01J—ELECTRIC DISCHARGE TUBES OR DISCHARGE LAMPS
- H01J37/00—Discharge tubes with provision for introducing objects or material to be exposed to the discharge, e.g. for the purpose of examination or processing thereof
- H01J37/32—Gas-filled discharge tubes
- H01J37/32431—Constructional details of the reactor
- H01J37/3244—Gas supply means
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01J—ELECTRIC DISCHARGE TUBES OR DISCHARGE LAMPS
- H01J37/00—Discharge tubes with provision for introducing objects or material to be exposed to the discharge, e.g. for the purpose of examination or processing thereof
- H01J37/32—Gas-filled discharge tubes
- H01J37/32431—Constructional details of the reactor
- H01J37/32532—Electrodes
-
- H—ELECTRICITY
- H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
- H05H—PLASMA TECHNIQUE; PRODUCTION OF ACCELERATED ELECTRICALLY-CHARGED PARTICLES OR OF NEUTRONS; PRODUCTION OR ACCELERATION OF NEUTRAL MOLECULAR OR ATOMIC BEAMS
- H05H1/00—Generating plasma; Handling plasma
- H05H1/24—Generating plasma
- H05H1/46—Generating plasma using applied electromagnetic fields, e.g. high frequency or microwave energy
- H05H1/4645—Radiofrequency discharges
Definitions
- the present invention relates to a plasma processing apparatus for generating a plasma to perform substrate processing.
- a plasma processing apparatus is used in a film forming process, an etching process, an ashing process, and the like because of high-precision process control.
- a plasma processing apparatus for example, a plasma chemical vapor deposition (CVD) apparatus, a plasma etching apparatus, a plasma ashing apparatus, and the like are known.
- CVD plasma chemical vapor deposition
- a plasma etching apparatus a plasma ashing apparatus, and the like are known.
- a plasma CVD apparatus a raw material gas is turned into plasma by high-frequency power or the like, and a thin film is formed on a substrate by a chemical reaction.
- a processing apparatus has been proposed (see, for example, Patent Document 1).
- an object of the present invention is to provide a plasma processing apparatus capable of stably generating uniform and high-density plasma on both surfaces of a cathode electrode.
- an anode electrode on which a processing substrate is mounted a cathode electrode that is disposed so as to face the anode electrode, and has a through-hole that is provided with an opening on the facing surface, the anode electrode and the cathode
- a gas supply device for introducing a process gas between the electrodes; an AC power supply for supplying AC power between the anode electrode and the cathode electrode to bring the process gas into a plasma state between the anode electrode and the cathode electrode; and the anode electrode and the cathode electrode
- a plasma processing apparatus including a chamber for storing the gas, an exhaust pump for evacuating the chamber, an exhaust speed controller for adjusting the exhaust speed, and a pressure measuring device for measuring the pressure inside the chamber.
- the present invention it is possible to provide a plasma processing apparatus capable of stably generating uniform and high-density plasma on both sides of the cathode electrode.
- the plasma processing apparatus 10 includes an anode electrode 11 on which a processing substrate is mounted, and a through-hole 120 in which an opening is provided on a surface facing the anode electrode 11.
- a cathode electrode 12 having a gas source, a gas supply device 13 for introducing a process gas 100 between the anode electrode 11 and the cathode electrode 12, and an AC power supply between the anode electrode 11 and the cathode electrode 12, 12 and an AC power supply 14 for bringing the process gas 100 into a plasma state.
- the anode electrode 11 and the cathode electrode 12 are flat plate types, and the plasma processing apparatus 10 utilizes capacitively coupled plasma. It is desirable that the distance between the capacitive coupling type electrodes be approximately uniform.
- the cathode electrode 12 provided with an opening on the surface functions as a hollow cathode electrode for generating a hollow cathode discharge.
- hollow cathode discharge will be described.
- ionization is maintained by ionizing gas molecules in a chain manner starting from secondary electrons emitted by ions incident on the surface of the cathode electrode 12.
- plasma generation on the surface of the cathode electrode 12 excluding the inside of the through hole 120 corresponds to this.
- the plasma generation inside the through hole 120 is a hollow cathode discharge, and in the hollow cathode discharge, electrons are confined in the through hole 120 and have kinetic energy in the through hole 120 of the cathode electrode 12, thereby having high density. An electron space is formed.
- debye blocking is caused by the cathode drop generated on the side wall of the through hole 120 provided in the cathode electrode 12, and electrons do not enter the side wall of the through hole 120 and disappear. That is, a high-density electron space is formed inside the through-hole 120 by repeating repulsion called “Pendulum effect” in which the electrons are repelled from the opposing wall surface inside the through-hole 120. Electrons that collide with gas molecules repeat inelastic collisions to maintain and promote ionization. These electrons are scattered in various directions inside the through hole 120 and repeat ionization amplification and cumulative ionization.
- FIG. 2 is an enlarged view of the region A shown in FIG.
- a glow discharge region 101 is formed between the anode electrode 11 and the cathode electrode 12, and a hollow discharge region 102 is formed inside the through hole 120 formed in the cathode electrode 12.
- a sheath region 200 is formed between the anode electrode 11 and the cathode electrode 12 and the glow discharge region 101, respectively.
- a sheath region 200 is formed between the cathode electrode 12 and the hollow discharge region 102 inside the through hole 120.
- the distance between the anode electrode 11 and the cathode electrode 12 is a distance S.
- the ions 50 that have entered the through hole 120 are accelerated by the sheath region 200 and collide with the inner wall surface of the cathode electrode 12.
- the secondary electrons 60 radiated from the wall surface are accelerated in a direction perpendicular to the wall surface by the sheath electric field.
- the electrons 61 that have reached the vicinity of the opposite wall surface are repelled by the opposite sheath electric field and pushed back into the plasma.
- This is called the pendulum motion effect, and the establishment of the presence of electrons in the through-hole 120 increases dramatically.
- the inside of the through hole 120 is maintained at a high electron density, and a plasma structure different from the glow discharge formed between the parallel plates is obtained.
- the gas molecules that have entered the high electron density region repeat ionization and recombination, and are observed as high-luminance emission during recombination.
- the precursor 80 generated in the high-density plasma is a radical species and diffuses to the outside of the through-hole 120 regardless of the electrode potential, and forms a thin film on the substrate surface disposed on the anode electrode 11, for example.
- the diameter of the through-hole 120 to obtain a uniform and high electron density efficiently is considered from the pressure, temperature, process gas type and the mean free path of the electrons.
- the diameter of the through hole 120 will be described later.
- the cathode electrode 12 is preferably made of a carbon material that is inexpensive, easy to process, and easy to maintain such as cleaning.
- the cathode electrode 12 made of a carbon material can be cleaned by hydrofluoric acid treatment.
- the use of the carbon material does not cause deformation due to high temperature in the plasma treatment process.
- an aluminum alloy or the like on which a metal oxide film is easily formed is a material suitable for a hollow cathode electrode.
- carbon containing carbon fiber, stainless alloy, copper, copper alloy, glass, ceramics, and the like can be used for the cathode electrode 12.
- the above material may be coated by alumite treatment, plating, or thermal spraying.
- a carbon material is also preferably used for the anode electrode 11. Further, carbon containing carbon fiber, aluminum alloy, stainless alloy, copper, copper alloy, glass, ceramics, and the like can be used for the anode electrode 11. Alternatively, these materials may be coated by alumite treatment, plating, or thermal spraying.
- a large number of through holes 120 that generate hollow cathode discharge are formed at a constant density on the surface of the cathode electrode 12, thereby generating a uniform high electron density electric field on both surfaces of the cathode electrode 12. Can be easily achieved. This is because the difference in density of the plasma density on both sides of the cathode electrode 12 is automatically corrected due to the bipolar diffusion property of the plasma through the through hole 120.
- This comparative example is an example employing a shower electrode to which the process gas 100 is supplied from the inside of the cathode electrode 12A.
- the inside of the recess 601 is a space where high-density plasma is generated by hollow cathode discharge.
- the process gas 100 is efficiently passed through the high-density plasma space by ejecting the process gas 100 from a fine gas ejection port 602 formed on the bottom surface of the recess 601.
- the process gas is stably flowed in the vicinity of the through-hole 120 where high-density plasma is generated by hollow cathode discharge. For this reason, the uniformity of the discharge is maintained on the entire surfaces of both surfaces of the cathode electrode 12.
- the through-hole 120 is formed so that the openings are arranged closest to the surface of the cathode electrode 12 as in a hexagonal close-packed arrangement. Thereby, uniformly high-density plasma is formed on the surface of the cathode electrode 12.
- FIG. 7 shows an example of the surface of the cathode electrode 12 in which the opening of the through hole 120 is formed.
- the center-to-center distance between the through holes 120 adjacent in the vertical direction is 3 mm
- the left and right between the through holes 120 adjacent in the diagonal direction are Set the distance in the direction to 5.2 mm.
- the gas supply nozzle 130 that ejects the process gas 100 of the gas supply device 13 faces the bottom surface of the cathode electrode 12, and when there are a plurality of gas supply nozzles 130, A gas supply nozzle 130 is arranged along the bottom surface of the electrode 12. By directing the gas supply nozzle 130 toward the bottom surface of the cathode electrode 12, the process gas 100 can be supplied to both surfaces of the cathode electrode 12 almost evenly.
- the process gas 100 is a gas in which a plurality of types of gases are mixed
- the process gas 100 in which all the gases are mixed may be supplied from the gas supply nozzle 130, or the gas supply nozzle 130 that is different for each type of gas.
- the gas may be supplied from each.
- FIG. 9 shows details of the discharge state in region A of FIG. Electrons repel the cathode electrode 12 without being able to penetrate inside the Debye length ⁇ d.
- FIG. 11 is a table showing the conditions of the pressure P at which hollow cathode discharge occurs and the diameter d of the through hole 120 when the gas type is ammonia and the temperature is 673K.
- the ratio of the diameter d of the through hole 120 to the electron mean free path Y is 2.38, and the number of collisions is 3.7.
- the length c decreases and it becomes difficult to secure a plasma generation space.
- FIG. 12 shows the relationship between the electron mean free path Y and the pressure P when the temperature is 673K.
- the circles indicate the mean free process in ammonia (NH 3 ) gas
- the triangles indicate the mean free process in monosilane (SiH 4 ) gas.
- FIG. 13 shows an example of the calculated value of the Debye length ⁇ d.
- the Debye length ⁇ d was calculated using the electron temperature and electron density of a general high-density glow discharge plasma.
- Equation (4) T is the ambient temperature (K), P is the pressure (Pa), and D is the diameter (m) of the gas molecules.
- the diameter d of the through hole 120 can be determined by setting the optimum length c as described above. That is, it is possible to prepare the cathode electrode 12 that is designed specifically for the hollow cathode discharge to be generated most efficiently by a predetermined pressure, ambient temperature, and gas type.
- the mean free path of electrons is determined by the atmospheric temperature and pressure, and the size of gas molecules.
- the inventors conducted experiments using the cathode electrode 12 having a large number of through-holes 120 and using a mixed gas of monosilane (SiH 4 ) gas and ammonia (NH 3 ) gas as the process gas 100.
- the atmospheric temperature T is set to 350 ° C. to 450 ° C.
- the “multi-hollow discharge” is a discharge generated on the surface of the cathode electrode 12 by combining the hollow cathode discharges generated in the respective through holes 120.
- the diameter d of the through hole 120 was estimated based on the mean free path of electrons in ammonia gas having a large gas flow rate ratio. Specifically, when a mixed gas of monosilane gas and ammonia gas is used, the ambient temperature T is 400 ° C., and the pressure P is 67 Pa, the diameter d of the through hole 120 is set to 5 mm, and the uniform multi-hollow on both surfaces of the cathode electrode 12 is used. Discharge is obtained.
- CVD process gas is usually introduced by mixing gas species such as monosilane, hydrogen, nitrogen, etc. However, in examining the diameter of the through-hole 120, focusing on the gas type with the longest mean free path in the mixed gas, The optimum value of the diameter of the hole 120 was derived.
- the diameter d of the through hole 120 is set to about 3.8 mm to 8.0 mm. These dimensions are easier than forming the 0.3 mm to 0.4 mm holes required to manufacture the shower electrode. For this reason, the manufacturing cost of the plasma processing apparatus 10 can be reduced.
- the through hole 120 has a circular cross section.
- the cross-section of the through-hole 120 may be a polygon having an approximate diameter of about 3.8 mm to 8.0 mm.
- a large number of through holes 120 having the same cross-sectional shape along the long axis direction may be formed in the cathode electrode 12, or through holes having different cross-sectional sizes or shapes along the long axis direction may be formed. 120 may be mixed and formed. By mixing the through holes 120 having different diameters d, multi-hollow discharges can be obtained under a plurality of conditions with different pressures, temperatures, gas types, and the like.
- the length of the through-hole 120 in the major axis direction, that is, the thickness t of the cathode electrode 12 is set to about 3 mm to 10 mm, preferably about 5 mm so that hollow cathode discharge is likely to occur.
- the distance S between the anode electrode 11 and the cathode electrode 12 is preferably about 10 mm to 40 mm. Thereby, plasma can be generated uniformly between the anode electrode 11 and the cathode electrode 12.
- the process gas 100 is only discharged uniformly from the concave portion 601 where the high-density plasma is generated by the hollow cathode discharge like a shower, and then the entire surface of the cathode electrode 12A. Plasma uniformity can be obtained.
- the process gas 100 is introduced without passing through the cathode electrode 12. Since the diameter d of the through hole 120 is considerably larger than the diameter of the hole necessary for the shower electrode, there is no concern about clogging, and maintenance is easy.
- the plasma processing apparatus 10 it is preferable to introduce the process gas 100 between the anode electrode 11 and the cathode electrode 12 from below to above.
- the process gas 100 By introducing the process gas 100 from below, gas molecules and radical particles having a light specific gravity that have been turned into plasma naturally flow upward on the surface of the cathode electrode 12 as an upward flow. Therefore, the process gas is uniformly supplied to the surface of the cathode electrode 12 without using a complicated structure such as a shower electrode.
- the space in which high-density plasma is generated by the hollow cathode discharge is the through-hole 120, the continuity of the plasma is secured on the front and back of the cathode electrode 12, and the density of the plasma density is automatically corrected mutually. . Therefore, the plasma processing apparatus 10 can generate a uniform high-density plasma on both surfaces of the cathode electrode 12.
- the surface of the cathode electrode 12 is smooth so that the process gas 100 flows smoothly, and the surface roughness is finished to 3 ⁇ m or less except for the inner surface of the through hole 120.
- the surface of the cathode electrode 12 is flattened to such an extent that the finish symbol is represented by “ ⁇ ”. That is, it is preferable that the maximum height Ry is 6.3S, the ten-point average roughness Rz is 6.3Z, and the arithmetic average roughness Ra is smaller than 1.6a.
- the plasma processing apparatus 10 according to the first embodiment of the present invention, by forming the through-hole 120 in the cathode electrode 12, uniform and high-density plasma on both surfaces of the cathode electrode 12. Can be stably generated. Furthermore, the manufacturing period of the plasma processing apparatus 10 is shorter and the manufacturing yield is improved as compared with an apparatus using a shower electrode that requires processing of several thousand or more micro holes. For this reason, the increase in the manufacturing cost of the plasma processing apparatus 10 is suppressed.
- the plasma processing apparatus 10 it is possible to generate a uniform high-density plasma in a large area regardless of the frequency of the AC power supplied from the AC power supply 14. Even if the frequency of the AC power supplied by the AC power supply 14 is set to, for example, about 60 Hz to 27 MHz, uniform and high-density plasma can be generated. That is, there is no need to use an AC power supply that supplies expensive VHF band AC power.
- the plasma density can be improved and In order to eliminate the non-uniformity of the plasma density due to waves, it was necessary to use a VHF band frequency such as 27 MHz of 13.56 MHz or higher.
- AC power output from the AC power source 14 may be supplied between the anode electrode 11 and the cathode electrode 12 via a pulse generator.
- the output of the pulse generator is supplied to the cathode electrode 12, and the anode electrode 11 is grounded.
- plasma is stably formed. This is because by providing a stop period for the supply of AC power, the temperature of the electrons is lowered and the stability of the discharge is improved.
- the AC power is supplied between the anode electrode 11 and the cathode electrode 12 so that the ON time is 600 ⁇ s and the OFF time when the AC power supply is stopped is 50 ⁇ s, and the ON time and the OFF time are alternately repeated. Supplied.
- the on-time is preferably set in the range of about 100 ⁇ s to 1000 ⁇ s, and the off-time is preferably set in the range of about 10 ⁇ s to 100 ⁇ s.
- the supply of AC power between the anode electrode 11 and the cathode electrode 12 is pulse-controlled and the supply of AC power is periodically turned on / off, thereby suppressing the occurrence of abnormal discharge.
- FIG. 14 shows an example of the plasma processing apparatus 10 when there is one anode electrode 11.
- the cathode back plate 121 is disposed at a position of a distance k from the surface of the cathode electrode 12 where the plasma is not excited.
- the distance k is set so that k ⁇ b (b: electron mean free path) so that plasma is not generated between the cathode electrode 12 and the cathode back plate 121.
- AC power is supplied from the AC power source 14 to the cathode electrode 12 and the cathode back plate 121.
- a process gas 100 is introduced between the anode electrode 11 and the cathode electrode 12 and between the cathode electrode 12 and the cathode back plate 121.
- FIG. 15 An example in which the plasma processing apparatus 10 has a plurality of cathode electrodes 12 is shown in FIG.
- the anode electrodes 11 and the cathode electrodes 12 are alternately arranged, and the anode electrode 11 is arranged on the outermost side. For this reason, the number of anode electrodes 11 is one more than that of the cathode electrodes 12.
- FIG. 15 shows an example in which the number of cathode electrodes 12 is three, it goes without saying that the number of cathode electrodes 12 is not limited to three.
- the number of plasma regions formed in the anode electrode 11 and the cathode electrode 12 can be increased. Thereby, the processing capability of the plasma processing apparatus 10 improves.
- the plasma processing apparatus 10 shown in FIG. 1 can be applied to a plasma chemical vapor deposition (CVD) apparatus, a plasma etching apparatus, a plasma ashing apparatus, and the like.
- CVD plasma chemical vapor deposition
- FIG. 16 shows an example in which the plasma processing apparatus 10 shown in FIG. 1 is used in a plasma CVD apparatus.
- the anode electrode 11 and the cathode electrode 12 are disposed in the chamber 20, and the substrate 1 to be deposited is disposed on the anode electrode 11.
- the anode electrode 11 is grounded.
- a gas containing a raw material gas for film formation is used as the process gas 100, and the process gas 100 is introduced from the gas supply device 13 into the chamber 20 through the gas supply nozzle 130.
- the pressure in the chamber 20 is measured by a pressure measuring device 16 such as a capacitance gauge, and the pressure in the chamber 20 is adjusted by an exhaust speed controller (APC) 15 that is an exhaust pump that evacuates the chamber 20 and adjusts the exhaust speed.
- APC exhaust speed controller
- a desired thin film mainly composed of the raw material contained in the raw material gas is formed on the exposed surface of the substrate 1.
- the temperature of the substrate 1 during the film forming process may be set by the substrate heater 21 shown in FIG.
- the film formation speed can be increased and the film quality can be improved.
- the plasma processing apparatus 10 shown in FIG. 1 uniform high-density plasma is generated on the surface of the cathode electrode 12. Therefore, according to the plasma CVD apparatus shown in FIG. 16, the source gas is efficiently decomposed, and a thin film is uniformly formed on the substrate 1 in a large area at a high speed. Therefore, the film thickness and film quality uniformity of the formed film are improved, and the film forming speed is improved.
- a desired thin film can be formed by appropriately selecting a source gas by a plasma CVD apparatus employing the plasma processing apparatus 10.
- a silicon semiconductor thin film, a silicon nitride thin film, a silicon oxide thin film, a silicon oxynitride thin film, a carbon thin film, or the like can be formed on the substrate 1.
- a silicon nitride (SiN) film is formed on the substrate 1 using a mixed gas of ammonia (NH 3 ) gas and monosilane (SiH 4 ) gas.
- a silicon oxide (SiO x) film is formed on the substrate 1 using a mixed gas of monosilane (SiH 4 ) gas and N 2 O gas, or TEOS gas and oxygen gas.
- FIG. 17 shows an example in which the AC power supply 17 is attached to the anode electrode 11 separately from the AC power supply 14 attached to the cathode electrode 12.
- the frequency of the AC power supplied from the AC power supply 17 may be equal to or lower than the frequency of the AC power supplied from the AC power supply 14.
- the frequency of the AC power supplied from the AC power supply 17 is set to about 60 Hz to 27 MHz.
- the anode electrode 11 can be cleaned by supplying AC power only from the AC power supply 17 without supplying AC power from the AC power supply 14. Specifically, a sputtering gas is introduced into the chamber 20, and the anode electrode 11 is cleaned by sputter etching while supplying AC power from the AC power supply 17.
- the plasma processing apparatus 10 shown in FIG. 18 in which the AC power supplies 14 and 17 are respectively attached to the cathode electrode 12 and the anode electrode 11 is used for the plasma CVD apparatus. May be.
- the distance k from the surface of the cathode electrode 12 that does not excite the plasma to the cathode back plate 121 is set so that k ⁇ b.
- the plasma processing apparatus 10 having the plurality of cathode electrodes 12 as shown in FIG. 15 to the plasma CVD apparatus, the number of substrates to be formed at a time increases, and the film forming processing capability is improved. Can do.
- the example in which the plasma processing apparatus 10 shown in FIG. 1 is applied to a plasma CVD apparatus has been described above.
- the plasma processing apparatus 10 shown in FIG. 1 can be applied to a plasma etching apparatus or a plasma ashing apparatus by changing the gas type of the process gas 100 with the configuration shown in FIGS.
- a plasma etching apparatus that etches and removes a film formed on the substrate 1 can be realized by introducing a plasma etching gas as the process gas 100 into the chamber 20.
- the plasma etching gas is appropriately selected depending on the material to be etched.
- a fluorine-based gas such as nitrogen trifluoride (NF 3 ) gas or carbon tetrafluoride (CF 4 ) gas can be used.
- a plasma ashing apparatus using the plasma processing apparatus 10 can be realized.
- oxygen and argon gas as the process gas 100, it is possible to ash the carbon film or the photoresist film formed on the substrate 1 as an etching mask.
- the plasma processing apparatus 10 that can stably generate uniform and high-density plasma on both surfaces of the cathode electrode 12, a plasma CVD apparatus, a plasma etching apparatus, a plasma ashing apparatus, etc.
- the processing speed and accuracy can be improved.
- the plasma processing apparatus of the present invention can be used for the purpose of generating uniform and high-density plasma on both sides of the cathode electrode.
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Abstract
Description
本発明の第1の実施形態に係るプラズマ処理装置10は、図1に示すように、処理基板を装着するアノード電極11と、アノード電極11に対向する面に開口部が設けられた貫通孔120を有するカソード電極12と、アノード電極11とカソード電極12間にプロセスガス100を導入するガス供給装置13と、アノード電極11とカソード電極12間に交流電力を供給して、アノード電極11とカソード電極12間においてプロセスガス100をプラズマ状態にする交流電源14とを備える。図1に示したようにアノード電極11とカソード電極12は平板型であり、プラズマ処理装置10は容量結合型プラズマを利用したものである。容量結合方式の電極間の距離は概略均一であることが望ましい。 (First embodiment)
As shown in FIG. 1, the
a=2b+c ・・・(1)
式(1)において、長さcは、貫通孔120内部のシース領域を除いた領域の直径方向の距離である。貫通孔120の直径dは、以下の式(2)で表される:
d=a+2×λd=2b+c+2×λd ・・・(2)
c=0の場合、十分な運動エネルギーを持った電子の移動空間が確保できず、貫通孔120内部に十分なプラズマ生成空間が確保されないことになる。 FIG. 9 shows details of the discharge state in region A of FIG. Electrons repel the
a = 2b + c (1)
In formula (1), the length c is the distance in the diameter direction of the region excluding the sheath region inside the through
d = a + 2 × λd = 2b + c + 2 × λd (2)
When c = 0, an electron moving space having sufficient kinetic energy cannot be secured, and a sufficient plasma generation space cannot be secured inside the through
λd=7.4×103×(Te/ne)1/2 ・・・(3)
図13に、デバイ長λdの計算値の例を示す。ここでは、一般的な高密度グロー放電プラズマの電子温度と電子密度を用いてデバイ長λdを算出した。なお、ガス分子の平均自由工程λgは式(4)、電子の平均自由工程λeは式(5)でそれぞれ表される:
λg=3.11×10-24×T4/(P×D) ・・・(4)
λe=λg×4×21/2 ・・・(5)
式(4)で、Tは雰囲気温度(K)、Pは圧力(Pa)、Dはガス分子の直径(m)である。 The relationship between the Debye length λd, the electron temperature Te, and the electron density ne is expressed by the following formula (3):
λd = 7.4 × 10 3 × (Te / ne) 1/2 (3)
FIG. 13 shows an example of the calculated value of the Debye length λd. Here, the Debye length λd was calculated using the electron temperature and electron density of a general high-density glow discharge plasma. Note that the mean free path λg of gas molecules is expressed by the formula (4), and the mean free process λe of electrons is expressed by the formula (5):
λg = 3.11 × 10 −24 × T 4 / (P × D) (4)
λe = λg × 4 × 2 1/2 (5)
In Equation (4), T is the ambient temperature (K), P is the pressure (Pa), and D is the diameter (m) of the gas molecules.
図14に、アノード電極11が1つの場合におけるプラズマ処理装置10の例を示す。図14に示すようにカソード電極12の片側の表面にのみプラズマを励起する場合には、カソード電極12のプラズマを励起しない面から距離kの位置にカソード背板121を配置する。このとき、カソード電極12とカソード背板121間にプラズマが発生しないように、k<b(b:電子の平均自由工程)であるように距離kを設定する。このとき、カソード電極12とカソード背板121に交流電源14から交流電力が供給される。なお、アノード電極11とカソード電極12間、及びカソード電極12とカソード背板121間に、プロセスガス100が導入される。 <First Modification>
FIG. 14 shows an example of the
プラズマ処理装置10が、複数のカソード電極12を有する例を図15に示す。図15に示したプラズマ処理装置10では、アノード電極11とカソード電極12が交互に配置され、且つ、最も外側にはアノード電極11が配置されている。このため、アノード電極11の枚数はカソード電極12よりも1枚多い。図15ではカソード電極12が3枚である例を示したが、カソード電極12の枚数が3枚に限られないことはもちろんである。 <Second Modification>
An example in which the
図1に示したプラズマ処理装置10は、プラズマ化学気相成長(CVD)装置、プラズマエッチング装置、プラズマアッシング装置などに適用可能である。 (Second Embodiment)
The
Claims (13)
- 基板を装着するアノード電極と、
前記アノード電極に対向するように配置され、対向する面に開口部が設けられた貫通孔を有するカソード電極と、
前記アノード電極と前記カソード電極間にプロセスガスを導入するガス供給装置と、
前記アノード電極と前記カソード電極間に交流電力を供給して、前記アノード電極と前記カソード電極間において前記プロセスガスをプラズマ状態にする交流電源と
を備えることを特徴とするプラズマ処理装置。 An anode electrode for mounting the substrate;
A cathode electrode that is disposed so as to face the anode electrode and has a through-hole provided with an opening on the facing surface;
A gas supply device for introducing a process gas between the anode electrode and the cathode electrode;
An AC power supply that supplies AC power between the anode electrode and the cathode electrode to bring the process gas into a plasma state between the anode electrode and the cathode electrode. - 前記ガス供給装置が、前記プロセスガスを下方から上方に向かって前記アノード電極と前記カソード電極間に導入することを特徴とする請求項1に記載のプラズマ処理装置。 The plasma processing apparatus according to claim 1, wherein the gas supply device introduces the process gas from the lower side to the upper side between the anode electrode and the cathode electrode.
- 前記ガス供給装置が、前記カソード電極の底面に沿って配置されたガス供給ノズルから前記カソード電極の底部に向けて前記プロセスガスを噴き出すことを特徴とする請求項2に記載のプラズマ処理装置。 3. The plasma processing apparatus according to claim 2, wherein the gas supply device ejects the process gas from a gas supply nozzle disposed along the bottom surface of the cathode electrode toward the bottom of the cathode electrode.
- 前記カソード電極の前記開口部が設けられた両面にそれぞれ対向して前記アノード電極が配置されていることを特徴とする請求項1に記載のプラズマ処理装置。 The plasma processing apparatus according to claim 1, wherein the anode electrode is disposed so as to face both surfaces of the cathode electrode where the opening is provided.
- 前記カソード電極を複数備えることを特徴とする請求項1に記載のプラズマ処理装置。 The plasma processing apparatus according to claim 1, comprising a plurality of the cathode electrodes.
- 前記アノード電極及び前記カソード電極の少なくともいずれかがカーボンからなることを特徴とする請求項1に記載のプラズマ処理装置。 2. The plasma processing apparatus according to claim 1, wherein at least one of the anode electrode and the cathode electrode is made of carbon.
- 前記貫通孔の直径が3.8mm以上且つ8.0mm以下であることを特徴とする請求項1に記載のプラズマ処理装置。 The plasma processing apparatus according to claim 1, wherein the diameter of the through hole is 3.8 mm or more and 8.0 mm or less.
- 前記カソード電極の表面に前記開口部が最密に配置されていることを特徴とする請求項1に記載のプラズマ処理装置。 The plasma processing apparatus according to claim 1, wherein the openings are arranged closest to the surface of the cathode electrode.
- 前記カソード電極に、長軸方向に沿った断面形状のサイズ又は形状が互いに異なる複数種類の前記貫通孔が形成されていることを特徴とする請求項1に記載のプラズマ処理装置。 2. The plasma processing apparatus according to claim 1, wherein the cathode electrode is formed with a plurality of types of the through-holes having different cross-sectional sizes or shapes along a major axis direction.
- 前記交流電源が供給する前記交流電力の周波数が、60Hz以上且つ27MHz以下であることを特徴とする請求項1に記載のプラズマ処理装置。 The plasma processing apparatus according to claim 1, wherein the frequency of the AC power supplied by the AC power source is 60 Hz or more and 27 MHz or less.
- 前記プロセスガスとして成膜用の原料ガスを含むガスを使用して、前記アノード電極上に配置された基板に前記原料ガスに含まれる原料を主成分とする膜を形成することを特徴とする請求項1項に記載のプラズマ処理装置。 A film containing a raw material gas contained in the raw material gas as a main component is formed on a substrate disposed on the anode electrode using a gas containing a raw material gas for film formation as the process gas. Item 2. The plasma processing apparatus according to Item 1.
- 前記アノード電極上に配置された基板の表面に形成された膜をエッチングするガスを前記プロセスガスとして使用することを特徴とする請求項1に記載のプラズマ処理装置。 The plasma processing apparatus according to claim 1, wherein a gas for etching a film formed on a surface of a substrate disposed on the anode electrode is used as the process gas.
- 前記プロセスガスとして酸素ガス及びアルゴンガスを含むガスを使用して、前記アノード電極上に配置された基板の表面に形成された膜をアッシングすることを特徴とする請求項1に記載のプラズマ処理装置。 2. The plasma processing apparatus according to claim 1, wherein a gas including oxygen gas and argon gas is used as the process gas to ash the film formed on the surface of the substrate disposed on the anode electrode. .
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JP2016197528A (en) * | 2015-04-03 | 2016-11-24 | 株式会社島津製作所 | Plasma processing apparatus |
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US10756003B2 (en) | 2016-06-29 | 2020-08-25 | Corning Incorporated | Inorganic wafer having through-holes attached to semiconductor wafer |
US11062986B2 (en) | 2017-05-25 | 2021-07-13 | Corning Incorporated | Articles having vias with geometry attributes and methods for fabricating the same |
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FR3115180A1 (en) * | 2020-10-14 | 2022-04-15 | Peter Choi | Plasma generating device |
US11554984B2 (en) | 2018-02-22 | 2023-01-17 | Corning Incorporated | Alkali-free borosilicate glasses with low post-HF etch roughness |
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Publication number | Priority date | Publication date | Assignee | Title |
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CN104498898B (en) | 2008-08-04 | 2017-10-24 | 北美Agc平板玻璃公司 | Pass through the method for the chemical vapor deposition formation coating of plasma enhancing |
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US9721765B2 (en) | 2015-11-16 | 2017-08-01 | Agc Flat Glass North America, Inc. | Plasma device driven by multiple-phase alternating or pulsed electrical current |
US10573499B2 (en) | 2015-12-18 | 2020-02-25 | Agc Flat Glass North America, Inc. | Method of extracting and accelerating ions |
US10242846B2 (en) | 2015-12-18 | 2019-03-26 | Agc Flat Glass North America, Inc. | Hollow cathode ion source |
CN109358237B (en) * | 2018-09-26 | 2020-11-06 | 台州学院 | Experiment platform for influence of plasma collision frequency on electromagnetic propagation and using method |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH02301134A (en) * | 1989-05-16 | 1990-12-13 | Kokusai Electric Co Ltd | Plasma controller for plasma generator |
JP2001155997A (en) * | 1999-11-24 | 2001-06-08 | Kanegafuchi Chem Ind Co Ltd | Plasma cvd system and method for fabricating silicon based thin film photoelectric converter |
JP2001271168A (en) * | 2000-03-24 | 2001-10-02 | Komatsu Ltd | Surface treating device |
JP2002280377A (en) * | 2001-03-19 | 2002-09-27 | Hitachi Kokusai Electric Inc | Substrate treatment apparatus |
JP2006057122A (en) * | 2004-08-18 | 2006-03-02 | Kyoto Institute Of Technology | Plasma chemical vapor deposition system and plasma chemical vapor deposition method |
WO2009069211A1 (en) * | 2007-11-29 | 2009-06-04 | Shimadzu Corporation | Plasma process electrode and plasma process device |
JP2010034532A (en) * | 2008-07-29 | 2010-02-12 | Psk Inc | Method for treating large-area substrate using hollow cathode plasma |
JP2010109157A (en) * | 2008-10-30 | 2010-05-13 | Shibaura Mechatronics Corp | Semiconductor manufacturing apparatus |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1109365A (en) * | 1994-01-20 | 1995-10-04 | 顾恩友 | Cold plasma sterilizing and disinfecting device |
CN201172685Y (en) * | 2008-03-31 | 2008-12-31 | 北京世纪辉光科技发展有限公司 | Vertical producing apparatus for double-face plasma surface treated sheet metal |
WO2009125477A1 (en) * | 2008-04-08 | 2009-10-15 | 株式会社島津製作所 | Cathode electrode for plasma cvd and plasma cvd apparatus |
-
2011
- 2011-09-22 CN CN201180070316.2A patent/CN103493602B/en not_active Expired - Fee Related
- 2011-09-22 KR KR1020137028584A patent/KR101485140B1/en not_active IP Right Cessation
- 2011-09-22 WO PCT/JP2011/071657 patent/WO2013008344A1/en active Application Filing
- 2011-09-22 JP JP2013523764A patent/JP5804059B2/en not_active Expired - Fee Related
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH02301134A (en) * | 1989-05-16 | 1990-12-13 | Kokusai Electric Co Ltd | Plasma controller for plasma generator |
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JPWO2013008344A1 (en) | 2015-02-23 |
CN103493602A (en) | 2014-01-01 |
CN103493602B (en) | 2016-06-08 |
KR101485140B1 (en) | 2015-01-22 |
JP5804059B2 (en) | 2015-11-04 |
KR20130137034A (en) | 2013-12-13 |
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