WO2003087429A1 - Automatic valve control system in plasma chemical vapor deposition system and chemical vapor deposition system for deposition of nano-scale multilayer film - Google Patents

Automatic valve control system in plasma chemical vapor deposition system and chemical vapor deposition system for deposition of nano-scale multilayer film Download PDF

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Publication number
WO2003087429A1
WO2003087429A1 PCT/KR2003/000689 KR0300689W WO03087429A1 WO 2003087429 A1 WO2003087429 A1 WO 2003087429A1 KR 0300689 W KR0300689 W KR 0300689W WO 03087429 A1 WO03087429 A1 WO 03087429A1
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Prior art keywords
chemical vapor
vapor deposition
deposition system
valve control
film
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PCT/KR2003/000689
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French (fr)
Inventor
Jung Joong Lee
Ju Wan Lim
Seung Hoon Lee
Original Assignee
Jung Joong Lee
Ju Wan Lim
Seung Hoon Lee
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Application filed by Jung Joong Lee, Ju Wan Lim, Seung Hoon Lee filed Critical Jung Joong Lee
Priority to DE10392487T priority Critical patent/DE10392487T5/en
Priority to AU2003235486A priority patent/AU2003235486A1/en
Publication of WO2003087429A1 publication Critical patent/WO2003087429A1/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
    • C23C16/455Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for introducing gases into reaction chamber or for modifying gas flows in reaction chamber
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/44Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
    • C23C16/455Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for introducing gases into reaction chamber or for modifying gas flows in reaction chamber
    • C23C16/45523Pulsed gas flow or change of composition over time
    • 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
    • C23C16/22Chemical 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
    • C23C16/30Deposition of compounds, mixtures or solid solutions, e.g. borides, carbides, nitrides
    • C23C16/34Nitrides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B82NANOTECHNOLOGY
    • B82YSPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
    • B82Y40/00Manufacture or treatment of nanostructures

Definitions

  • the present invention relates to an automatic valve control system in a plasma chemical vapor deposition system or a chemical vapor deposition system for deposition of nano-scale multilayer film, and more particularly, to an automatic valve control system in a plasma chemical vapor deposition system or a chemical vapor deposition system for deposition of nano-scale multilayer film having nano-scale ultra-high hardness and multifunction, by using a plasma chemical vapor deposition method or a chemical vapor deposition method.
  • An ultra-lattice thin-film is a basic research model for studying an interfacial property between heterogeneous materials, the terminology of which names a multilayer film in which the thickness of each layer is thin up to a nano-scale degree .
  • heterogeneous materials are adjusted in a film thickness direction with a scale nearly close to an interval between the lattices in a crystal existing in the nature, it is meant that they are shown as an artificial one-dimensional lattice.
  • FIG. 1 A model view of an ideal ultra-lattice is illustrated in FIG. 1.
  • materials A and B have an intrinsic characteristic, respectively, but the whole multilayer film to be expected has a function of a composite material which is obtained by taking an average value or each superior point of the materials A and B.
  • an ultra-lattice thin-film where materials A and B are deposited does not expose inherent properties of the materials A and B, but exhibits a new property as a whole. That is, the ultra-lattice thin-film reveals a new property completely different from the materials A and B.
  • the thickness of each layer should be adjusted up to several nano-meters.
  • the thickness of each layer should not only be adjusted, but also a gradient of concentration should not occur due to a diffusion of the heterogeneous materials in an interface. Because of these limitations , the ultra-lattice thin-filmhas been fabricated up to now, chiefly by using a sputtering device where a substrate is rotatably designed or an evaporation method using two independent evaporation sources.
  • the thickness of each layer can be controlled by controlling a rotational speed of the substrate and an intensity of a bias applied to the targets, byuseofaproperty that a corresponding material is chiefly deposited when the substrate reaches the front of each target.
  • the evaporation method controls evaporation of heterogeneous materials periodically through opening and closing of a shutter installed in front of the two evaporation sources .
  • sputtering and evaporation methods allows fabrication of an ultra-lattice thin-film by a comparatively simple method, and enables the thickness of each layer to be easily controlled, but cannot perform deposition of a thin-film with respect to a substrate of a complicated shape because of limitation of a physical vapor deposition.
  • a chemical vapor deposition (CVD) and a plasma chemical vapor deposition (PECVD) method supplies a reaction material in a gaseous form to perform a deposition process.
  • MFC mass flow meter
  • an object of the present invention to provide an automatic valve control system in a plasma chemical vapor deposition system or chemical vapor deposition system for deposition of a nano-scale multilayer film, in which a supply of a source can be quickly and accurately controlled in order to fabricate an ultra-lattice successfully by using a plasma chemical vapor deposition method or chemical vapor deposition method, and limitation of a substrate shape based on a physical vapor deposition such as a sputtering or evaporation method can be solved in the case that an ultra-lattice thin-film is fabricatedby using a plasma chemical vapor deposition method or chemical vapor deposition method.
  • an automatic valve control system in a plasma chemical vapor deposition system or chemical vapor deposition system for deposition of a nano-scale multilayer film comprising: a chamber in which a multilayer thin-film can be formed of at least two components by using a plasma chemical vapor deposition method or chemical vapor deposition method; at least two source supplies supplying a reaction material including a component constituting any one layer of the multilayer thin-film; at least two paths each whose middle portion is connected to each source supply, whose one end is connected to the chamber, and whose other end is connected to a bypass tube for controlling an amount of flow; a vacuum pump connected to the bypass tube; and at least four valves installed in either side of each path around each connection portion in each source supply, which is opened or closed.
  • the valves comprise a solenoid valve which can be automatically opened or closed, respectively.
  • the present invention further comprises a controller controlling opening or closing of the valves with a predetermined interval of time.
  • the controller controls the valves , and supplies the chamber with materials necessary for forming a thin-film through the at least two paths and source supplies, in a predetermined sequence, in order to form a multilayer thin-film.
  • the present invention further comprises a third source supply in order to smoothly perform a fabrication process, in which a source can be directly supplied to the chamber via the third source supply, in the case of using the source having a component which reacts each other and is hardened during introduction of the source into the chamber among the sources supplied via the at least two source supplies, and a source which forms a plasma continuously stably, among processes is supplied through the third source supply, in the case of the plasma chemical vapor deposition method.
  • the third source supply further comprises a solenoid valve whose opening and closing control can be performed in order to control a source supply.
  • the present invention can control a supply of sources smoothly and quickly, and thus can fabricate a nano-scale multilayer thin-film quickly and accurately by using a plasma chemical vapor deposition method or chemical vapor deposition method.
  • FIG. 1 is an exemplary view for explaining an ultra-lattice thin-film structure
  • FIG. 2 is a configurational view for explaining an automatic valve control system in a plasma chemical vapor deposition system for deposition of a nano-scale multilayer film according to the present invention
  • FIG. 3 is a graphical view showing the hardness of a TiN/AlN ultra-lattice thin-film according to the present invention .
  • FIG. 2 An automatic valve control system used in the present invention is shown in FIG. 2.
  • a reactor of a general plasma chemical vapor deposition system that is, a chamber 10 is used as it is.
  • Reaction gases to be supplied that is, a first source 31 and a second source 32 are designed to be supplied to the chamber 10 via a valve system 20.
  • First to fourth valves 27 to 30 each formed of an air pressure valve are used in the valve system 20.
  • the first to fourth valves 27 to 30 are connected to a solenoid valve (not shown) which can be electrically controlled in order to automatically control an on-and-off operations of the first to fourth valves.
  • the valve system 20 is connected to a first connection tube 21 connected to the chamber 10, and a second tube 24 connected to a second pump 33 to play a role of a bypass tube for bypassing a reaction gas, a first path 22 and a second path 23 connected to the first and second connection tubes 21 and 24 in parallel with each other, respectively, a first source 31 and a second source 32 connected to the middle portions of the first and second paths 22 and 23, receiving a source from first and second sources 31 and 32 , respectively, and transferring the received source, and the first to fourth valves 27 to 30 installed along the first and second paths 22 and 23 around the first and second source supplies 25 and 26.
  • the bypass tube that is, the second connection tube 24 is essentially required for consistently maintaining an amount of gas during fabrication of a multilayer thin-film.
  • connection tube 24 The end of the connection tube 24 is connected to a second pump 33 which operates independently of a first pump 12 which is used in the chamber 10 in order to prevent a back stream of gas to be expected in an entrance portion of the pump.
  • the chamber 10 is fabricated in a cylindrical shape of
  • a plasma generator 17 for generating a plasma is installed in the upper portion of the chamber 10. The plasma generator
  • 17 includes a planar capacitive type electrode, which receives power supplied via a matching unit 40 from a radio frequency
  • the sample piece 16 is formed of resistance wires, and is heated up to a set process temperature by a heater 14 generating heat by power supplied by a power source 15.
  • the chamber 10 and the table 14 except for the plasma generator 17 are electrically grounded.
  • thermocouple gauge the pressure in the chamber 10 is measured by a thermocouple gauge.
  • An ultra-lattice thin-film is fabricated with an automatic valve control system according to the present invention in which TiN and A1N are repeatedly deposited in the thickness of a nano-scale unit, respectively.
  • TiCl , H 2 , or NH 3 are used as a reaction gas for deposition of TiN
  • A1C1 3 , or NH 3 are used as a reaction gas for deposition of AIN.
  • thermodynamic reaction equations are expressed in Reaction Equations 1 and 2, respectively.
  • TiCl 4 and AICI 3 exist in liquid and solid states, respectively, it is introduced into the chamber 10 through a bubbling reaction with a carrier gas in an evaporator.
  • Ar and H 2 are used as a carrier gas, respectively.
  • Ar is additionally supplied in order to help activation of plasma.
  • MFC mass flow meter
  • Equation 1 the following Equations 1 and 2 are established among an amount Qcar of a carrier gas, an amount Qrxn of a reaction gas introduced into a reaction chamber by a bubbling reaction, a pressure Pear of a carrier gas, and a vaporized pressure Prxn of a reaction gas.
  • PT can be confirmed by using a pressure gauge attached to an evaporator. If a pressure of the evaporator is consistently maintained, an amount of a reaction gas introduced into a reaction chamber is a function of an amount of a carrier gas introduced into the evaporator and an evaporation pressure of the reaction gas.
  • the pressure and temperature of TiCl 4 andA1C1 3 are the mercuric evaporation pressure (mmHg) and the absolute temperature ( 0 K)
  • each evaporation pressure P is expressed as the following Equations 3 and 4. ⁇ Equation 3>
  • the evaporat ion pres sure of TiCl 4 and AICI 3 i s a function of only temperature. Accordingly, an amount of the reaction gas can be adjusted by controlling the temperature of the evaporator and the amount of the carrier gas, respectively.
  • NH 3 reacts with a gas of TiCl 4 or A1C1 3 at a low temperature and forms a solid compound such as TiCl 4 -nNH 3 , AlCl 3 -nNH 3 or NH 4 C1, to thus clog an inflow gas tube.
  • the solid compound is made to be uniformly distributed and introduced via a number of small holes 18 formed on an electrode plate formed in the plasma generator 17 installed in the chamber 10.
  • a third source supply tube 35 is connected between a third source 34 such as NH 3 and the chamber 10, and the third source supply tube 35 is opened and closed by a fifth valve 36 formed of a solenoid valve.
  • the plasma generator 17 is formed of a circular plate.
  • the reaction gases supplied from the first and second sources 31 and 32 to the chamber 10, that is, the gases of TiCl 4 and AICI 3 are made to be uniformly introduced by using a ring type gas distributor 19 installed between the plasma generator 17 and the sample piece 16.
  • the first and second pumps 12 and 33 are formed of a mechanical rotary pump, respectively.
  • the RF generator 45 is formed of a radio frequency generator of 13.56MHz.
  • the matching unit 40 is made of an impedance matching box of a capacitive type.
  • the TiN/AlN ultra-lattice thin-film fabricated according to the present invention has been fabricated by the following set of sequences. Sequence 1 .
  • TiCl 4 and A1C1 3 supplied through the evaporator and the reaction gases Ar and H 2 are discharged via the second pump 33 connected to the second connection tube 24, in order to stabilize an amount of gas.
  • NH 3 is made to be introduced into the chamber 10 via a small hole on the upper electrode plate which is the plasma generator 17, to thereby form a plasma.
  • the first valve 27 is opened and the third valve 29 is closed, for deposition of TiN. Accordingly, the reaction materials for deposition of TiN, that is, TiCl 4 , H 2 , and NH 3 are introduced into the chamber 10.
  • the fourth valve 30 is opened, tothereby discharge the reaction material for deposition of AIN, that is, AlCl 3 and NH 3 by the second pump 33 so that the amount of flow does not change.
  • the first valve 27 is closed and the third valve 29 is opened until the reaction material such as TiCl 4 remaining in the chamber 10 is completely discharged (this process is necessary to obtain a clean interface by preventing a Ti concentration gradient in the interface between TiN and AIN which can be expected in advance, in the case that the reaction gas for deposition of AIN is introduced. In the present invention, it takes about 10 seconds . ) .
  • an ultra-lattice TiN/AlN By repeatedly performing the sequences 3 through 6, an ultra-lattice TiN/AlN can be effectively grown.
  • the thickness of each layer is controlled by altering a deposition time (sequences 4 and 6) from a growing speed of a mono-layer thin-film of TiN and AIN obtained through a preliminary experiment.
  • a process of repeating the sequences 3 through 6 by 300—500 times or so.
  • each valve is automatically controlled by supplying an electrical signal to a solenoid valve connected to the first to fourth valves 27 to 30 through a computer program.
  • the ultra-lattice thin-film of TiN/AlN fabricated by the above-described processes is examined into a transmission electronmicroscopy picture .
  • a sample piece observed through an electron microscopy is shown into a pattern shown in FIG.
  • a bright portion represents a TiN layer
  • a dark portion represents an AIN layer
  • a bilayer period means an addition of the thickness of a layer of TiN and that of a layer of AIN .
  • the thickness of the ultra-lattice thin-film fabricated in the present invention is controlled within several nano-meters.
  • TiN/AlN fabricated according to the present invention is examined. As shown in FIG. 3, when the repetition period of a multilayer thin-film is about 5nm, the multilayer thin-film reveals the maximum hardness of 5000 (HKO.Ol) or higher. Considering that the hardness of the TiN and AIN mono-layer thin-films fabricated by the existing plasma chemical vapor deposition method are 2500 (HKO.Ol) and 1200
  • the TiN/AlN multilayer thin-film fabricated according to the present invention reveals the characteristic of an ultra-lattice thin-film.
  • the present invention can fabricate a nano-scale multilayer thin-film representing the characteristic of the ultra-lattice thin-film through a plasma chemical vapor deposition method without causing an amount of the reaction gas to be changed. Also, the present invention can solve the shortcomings of a physical vapor deposition (PVD) method such as a sputtering method, which is a very epoch-making invention in that the present invention provides a new method of fabricating an ultra-lattice thin-film.
  • PVD physical vapor deposition
  • sputtering method which is a very epoch-making invention in that the present invention provides a new method of fabricating an ultra-lattice thin-film.
  • the present invention has been described with respect to particularly preferred embodiments . However, the present invention is not limited to the above embodiments, and it is possible for one who has an ordinary skill in the art to make various modifications and variations, without departing off the spirit of the present invention.

Abstract

An automatic valve control system in PCVD system or CVD system for deposition of nano-scale multilayer film having nano-scale ultra-high hardness and multifunction is provided. The automatic valve control system includes a chamber in which a multilayer thin-film can be formed of at least two components by using PCVD method or CVD method, at least two source supplies supplying a reaction material, at least two paths each whose middle portion is connected to each source supply, whose one end is connected to the chamber, and whose other end is connected to a bypass tube, a vacuum pump connected to the bypass tube, and at least four valves installed in either side of each path around each connection portion in each source supply, which is opened or closed.

Description

AUTOMATIC VALVE CONTROL SYSTEM IN PLASMA CHEMICAL VAPOR DEPOSITION SYSTEM AND CHEMICAL VAPOR DEPOSITION SYSTEM FOR DEPOSITION OF NANO-SCALE MULTILAYER FILM
Technical Field
The present invention relates to an automatic valve control system in a plasma chemical vapor deposition system or a chemical vapor deposition system for deposition of nano-scale multilayer film, and more particularly, to an automatic valve control system in a plasma chemical vapor deposition system or a chemical vapor deposition system for deposition of nano-scale multilayer film having nano-scale ultra-high hardness and multifunction, by using a plasma chemical vapor deposition method or a chemical vapor deposition method.
Background Art
A study on fabrication and commercialization of various vacuum films are being vividly in progress with a help of development of a vacuum technology, one of which is an ultra-lattice or artificial lattice thin-film to be handled in the present invention. An ultra-lattice thin-film is a basic research model for studying an interfacial property between heterogeneous materials, the terminology of which names a multilayer film in which the thickness of each layer is thin up to a nano-scale degree .
If heterogeneous materials are adjusted in a film thickness direction with a scale nearly close to an interval between the lattices in a crystal existing in the nature, it is meant that they are shown as an artificial one-dimensional lattice.
A model view of an ideal ultra-lattice is illustrated in FIG. 1. In a multilayer thin film in which layers of each micron level are deposited, as shown in FIG .1, materials A and B have an intrinsic characteristic, respectively, but the whole multilayer film to be expected has a function of a composite material which is obtained by taking an average value or each superior point of the materials A and B. In contrast, an ultra-lattice thin-film where materials A and B are deposited, does not expose inherent properties of the materials A and B, but exhibits a new property as a whole. That is, the ultra-lattice thin-film reveals a new property completely different from the materials A and B.
Even in the result of a study, a cause that an ultra-lattice thin-film reveals a new property, has not been still thoroughly examined, but reported that it should be due to a lattice distortion effect, an interfacial effect, a stratiform structure effect , an artificial periodic effect , etc., between heterogeneous materials.
In the case that an ultra-lattice is applied to a hard coating, respectively different two metal or ceramic (carbide or nitride) layers are alternately deposited. As a result, movement of the potential in each layer and movement of the potential cross an interlayer interface is suppressed, to accordingly obtain a hardness of 50GPa or more.
Here, in order to effectively suppress movement of the potential, the thickness of each layer should be adjusted up to several nano-meters.
In order to obtain the property of the ultra-lattice thin-film as described above, the thickness of each layer should not only be adjusted, but also a gradient of concentration should not occur due to a diffusion of the heterogeneous materials in an interface. Because of these limitations , the ultra-lattice thin-filmhas been fabricated up to now, chiefly by using a sputtering device where a substrate is rotatably designed or an evaporation method using two independent evaporation sources.
In the case of the sputteringmethod, when two different targets are installed so as to face each other, and a substrate is rotated at a constant speed while sputtering, it has been known that the thickness of each layer can be controlled by controlling a rotational speed of the substrate and an intensity of a bias applied to the targets, byuseofaproperty that a corresponding material is chiefly deposited when the substrate reaches the front of each target.
The evaporation method controls evaporation of heterogeneous materials periodically through opening and closing of a shutter installed in front of the two evaporation sources .
Using the sputtering and evaporation methods allows fabrication of an ultra-lattice thin-film by a comparatively simple method, and enables the thickness of each layer to be easily controlled, but cannot perform deposition of a thin-film with respect to a substrate of a complicated shape because of limitation of a physical vapor deposition.
A chemical vapor deposition (CVD) and a plasma chemical vapor deposition (PECVD) method supplies a reaction material in a gaseous form to perform a deposition process. Taking this into consideration, a study on fabrication of a multilayer thin-film through a control of a mass flow meter
(MFC) of gas has been attempted. For example, in order to obtain a multilayer thin-film of TiN and TiCN, a supply of CH4 gas is controlled through an on/off time control of a mass flow meter (MFC) . However, in this case, since it takes about one minute to stabilize an amount of gas through the mass flow meter (MFC) , it is not possible to adjust the thickness of each layer into several tens of nanometers or less. Further, in the case that a bubbler or evaporator is used in order to supply a liquid or solid reaction material in a gaseous form, it takes much more time to stabilize an amount of flow. As a consequence, it becomes more difficult to control the thickness of each layer through the mass flow meter. Disclosure of the Invention
To solve the above problems, it is an object of the present invention to provide an automatic valve control system in a plasma chemical vapor deposition system or chemical vapor deposition system for deposition of a nano-scale multilayer film, in which a supply of a source can be quickly and accurately controlled in order to fabricate an ultra-lattice successfully by using a plasma chemical vapor deposition method or chemical vapor deposition method, and limitation of a substrate shape based on a physical vapor deposition such as a sputtering or evaporation method can be solved in the case that an ultra-lattice thin-film is fabricatedby using a plasma chemical vapor deposition method or chemical vapor deposition method.
To accomplish the above object of the present invention, there is provided an automatic valve control system in a plasma chemical vapor deposition system or chemical vapor deposition system for deposition of a nano-scale multilayer film, the automatic valve control system comprising: a chamber in which a multilayer thin-film can be formed of at least two components by using a plasma chemical vapor deposition method or chemical vapor deposition method; at least two source supplies supplying a reaction material including a component constituting any one layer of the multilayer thin-film; at least two paths each whose middle portion is connected to each source supply, whose one end is connected to the chamber, and whose other end is connected to a bypass tube for controlling an amount of flow; a vacuum pump connected to the bypass tube; and at least four valves installed in either side of each path around each connection portion in each source supply, which is opened or closed. The valves comprise a solenoid valve which can be automatically opened or closed, respectively. The present invention further comprises a controller controlling opening or closing of the valves with a predetermined interval of time. Thus , the controller controls the valves , and supplies the chamber with materials necessary for forming a thin-film through the at least two paths and source supplies, in a predetermined sequence, in order to form a multilayer thin-film. Also, the present invention further comprises a third source supply in order to smoothly perform a fabrication process, in which a source can be directly supplied to the chamber via the third source supply, in the case of using the source having a component which reacts each other and is hardened during introduction of the source into the chamber among the sources supplied via the at least two source supplies, and a source which forms a plasma continuously stably, among processes is supplied through the third source supply, in the case of the plasma chemical vapor deposition method. The third source supply further comprises a solenoid valve whose opening and closing control can be performed in order to control a source supply. As described above, the present invention can control a supply of sources smoothly and quickly, and thus can fabricate a nano-scale multilayer thin-film quickly and accurately by using a plasma chemical vapor deposition method or chemical vapor deposition method.
Brief Description of the Drawings
The above and other objects and advantages of the present invention will become more apparent by describing the preferred embodiments thereof in more detail with reference to the accompanying drawings in which:
FIG. 1 is an exemplary view for explaining an ultra-lattice thin-film structure; FIG. 2 is a configurational view for explaining an automatic valve control system in a plasma chemical vapor deposition system for deposition of a nano-scale multilayer film according to the present invention; and
FIG. 3 is a graphical view showing the hardness of a TiN/AlN ultra-lattice thin-film according to the present invention .
Best Mode for Carrying out the Invention
Hereinbelow, an automatic valve control system in a plasma chemical vapor deposition system or chemical vapor deposition system for deposition of a nano-scale multilayer film according to the present invention, will be described with reference to the accompanying drawings.
An automatic valve control system used in the present invention is shown in FIG. 2. Here, a reactor of a general plasma chemical vapor deposition system, that is, a chamber 10 is used as it is. Reaction gases to be supplied, that is, a first source 31 and a second source 32 are designed to be supplied to the chamber 10 via a valve system 20. First to fourth valves 27 to 30 each formed of an air pressure valve are used in the valve system 20. The first to fourth valves 27 to 30 are connected to a solenoid valve (not shown) which can be electrically controlled in order to automatically control an on-and-off operations of the first to fourth valves. The valve system 20 is connected to a first connection tube 21 connected to the chamber 10, and a second tube 24 connected to a second pump 33 to play a role of a bypass tube for bypassing a reaction gas, a first path 22 and a second path 23 connected to the first and second connection tubes 21 and 24 in parallel with each other, respectively, a first source 31 and a second source 32 connected to the middle portions of the first and second paths 22 and 23, receiving a source from first and second sources 31 and 32 , respectively, and transferring the received source, and the first to fourth valves 27 to 30 installed along the first and second paths 22 and 23 around the first and second source supplies 25 and 26. Here, the bypass tube, that is, the second connection tube 24 is essentially required for consistently maintaining an amount of gas during fabrication of a multilayer thin-film.
The end of the connection tube 24 is connected to a second pump 33 which operates independently of a first pump 12 which is used in the chamber 10 in order to prevent a back stream of gas to be expected in an entrance portion of the pump.
The chamber 10 is fabricated in a cylindrical shape of
30cm in diameter and 24cm in height, in 304 stainless steel. A plasma generator 17 for generating a plasma is installed in the upper portion of the chamber 10. The plasma generator
17 includes a planar capacitive type electrode, which receives power supplied via a matching unit 40 from a radio frequency
(RF) generator 45 and operates. A sample piece 16 to be tested is installed on a table
13 installed in the lower portion of the chamber 10. The sample piece 16 is formed of resistance wires, and is heated up to a set process temperature by a heater 14 generating heat by power supplied by a power source 15. The chamber 10 and the table 14 except for the plasma generator 17 are electrically grounded.
Also, the pressure in the chamber 10 is measured by a thermocouple gauge.
An ultra-lattice thin-film is fabricated with an automatic valve control system according to the present invention in which TiN and A1N are repeatedly deposited in the thickness of a nano-scale unit, respectively. Here, TiCl , H2, or NH3 are used as a reaction gas for deposition of TiN, and A1C13, or NH3 are used as a reaction gas for deposition of AIN.
The thermodynamic reaction equations are expressed in Reaction Equations 1 and 2, respectively.
<Reaction Equation 1>
2TiCl4(g) + 2NH3(g) + H2(g) = 2TiN(S) + 8HC1 (g)
<Reaction Equation 2>
AlCl3(g) + NH3(g) = AlN(s) + 3HCl(g)
Since TiCl4 and AICI3 exist in liquid and solid states, respectively, it is introduced into the chamber 10 through a bubbling reaction with a carrier gas in an evaporator. Ar and H2 are used as a carrier gas, respectively. Also, when AIN is deposited, Ar is additionally supplied in order to help activation of plasma.
An amount of each gas is consistently maintained by using a mass flow meter (MFC) . The amount of the reaction gas introduced by the bubbling reaction is adjusted by the following principle.
In general, the following Equations 1 and 2 are established among an amount Qcar of a carrier gas, an amount Qrxn of a reaction gas introduced into a reaction chamber by a bubbling reaction, a pressure Pear of a carrier gas, and a vaporized pressure Prxn of a reaction gas. <Equation 1>
Figure imgf000012_0001
<Equation 2>
* r * c-zr * TOM
Here, PT can be confirmed by using a pressure gauge attached to an evaporator. If a pressure of the evaporator is consistently maintained, an amount of a reaction gas introduced into a reaction chamber is a function of an amount of a carrier gas introduced into the evaporator and an evaporation pressure of the reaction gas. When the pressure and temperature of TiCl4 andA1C13 are the mercuric evaporation pressure (mmHg) and the absolute temperature (0 K) , each evaporation pressure P is expressed as the following Equations 3 and 4. <Equation 3>
Pτicι< " ~βγβ° ÷ 9.66logT - 6.12 X IO "3 7
<Equation 4>
- 2919
-+- 25. 129 - 5.7881ogZ
Thus , the evaporat ion pres sure of TiCl 4 and AICI3 i s a function of only temperature. Accordingly, an amount of the reaction gas can be adjusted by controlling the temperature of the evaporator and the amount of the carrier gas, respectively. Meanwhile, NH3 reacts with a gas of TiCl4 or A1C13 at a low temperature and forms a solid compound such as TiCl4-nNH3, AlCl3-nNH3 or NH4C1, to thus clog an inflow gas tube. To prevent this, the solid compound is made to be uniformly distributed and introduced via a number of small holes 18 formed on an electrode plate formed in the plasma generator 17 installed in the chamber 10. A third source supply tube 35 is connected between a third source 34 such as NH3 and the chamber 10, and the third source supply tube 35 is opened and closed by a fifth valve 36 formed of a solenoid valve. The plasma generator 17 is formed of a circular plate. The reaction gases supplied from the first and second sources 31 and 32 to the chamber 10, that is, the gases of TiCl4 and AICI3 are made to be uniformly introduced by using a ring type gas distributor 19 installed between the plasma generator 17 and the sample piece 16.
Based on the above description, the sources 1 and 2 used in the present invention are summarized as follows with reference to FIG. 2.
Source 1: TiCl4, Ar, H2 Source 2: A1C13, Ar, H2 Process conditions of TiN/AlN ultra-lattice thin-film is shown in the following Table 1. [Table 1] Process conditions of TiN/AlN ultra-lattice thin-film
TiN AIN
TiCl4 : 1.4seem A1C13 : 1.9seem
Reaction gas
H2 : lOOsccm H2 : lOOsccm and flow
Ar : 40sccm Ar 40sccm amount
NH3 : 20sccm
Process 530°C temperature
RF power 50W
Total thickness of 2~3 m deposition film
The first and second pumps 12 and 33 are formed of a mechanical rotary pump, respectively. The RF generator 45 is formed of a radio frequency generator of 13.56MHz. The matching unit 40 is made of an impedance matching box of a capacitive type.
The TiN/AlN ultra-lattice thin-film fabricated according to the present invention has been fabricated by the following set of sequences. Sequence 1 .
TiCl4 and A1C13 supplied through the evaporator and the reaction gases Ar and H2 are discharged via the second pump 33 connected to the second connection tube 24, in order to stabilize an amount of gas.
Sequence 2.
If an amount of all reaction gases is stabilized, NH3 is made to be introduced into the chamber 10 via a small hole on the upper electrode plate which is the plasma generator 17, to thereby form a plasma.
Sequence 3.
If the plasma is stabilized, the first valve 27 is opened and the third valve 29 is closed, for deposition of TiN. Accordingly, the reaction materials for deposition of TiN, that is, TiCl4, H2, and NH3 are introduced into the chamber 10. Here, the fourth valve 30 is opened, tothereby discharge the reaction material for deposition of AIN, that is, AlCl3 and NH3 by the second pump 33 so that the amount of flow does not change.
Sequence 4.
If deposition of TiN is completed, the first valve 27 is closed and the third valve 29 is opened until the reaction material such as TiCl4 remaining in the chamber 10 is completely discharged (this process is necessary to obtain a clean interface by preventing a Ti concentration gradient in the interface between TiN and AIN which can be expected in advance, in the case that the reaction gas for deposition of AIN is introduced. In the present invention, it takes about 10 seconds . ) .
Sequence 5.
Then, the second valve 28 is opened and the fourth valve
30 is closed, to make the reaction gases for deposition to be introduced into the chamber 10. Here, the third valve 29 is opened so that an amount of TiCl4 is consistentlymaintained.
Sequence 6.
By repeating the sequence 4, a residual gas such as A1C13 remaining in the chamber 10 is removed.
The on-and-off state of each valve for the above-described sequences is shown in the following Table
2.
[ Table 2 ]
The on-and-off state of each valve for the processing sequences
Figure imgf000017_0001
By repeatedly performing the sequences 3 through 6, an ultra-lattice TiN/AlN can be effectively grown. Here, the thickness of each layer is controlled by altering a deposition time (sequences 4 and 6) from a growing speed of a mono-layer thin-film of TiN and AIN obtained through a preliminary experiment. In order to grow an ultra-lattice thin-film of 2~3 m in thickness necessary for application to a hard thin film, a process of repeating the sequences 3 through 6 by 300—500 times or so.
The opening and closing control of each valve is automatically controlled by supplying an electrical signal to a solenoid valve connected to the first to fourth valves 27 to 30 through a computer program.
The ultra-lattice thin-film of TiN/AlN fabricated by the above-described processes is examined into a transmission electronmicroscopy picture . A sample piece observed through an electron microscopy is shown into a pattern shown in FIG.
1, in which a bilayer period shows up over about 5nm.
That is, a bright portion represents a TiN layer, and a dark portion represents an AIN layer . Here, a bilayer period means an addition of the thickness of a layer of TiN and that of a layer of AIN . The thickness of the ultra-lattice thin-film fabricated in the present invention is controlled within several nano-meters.
Meanwhile, a change in the hardness of a multilayer of
TiN/AlN fabricated according to the present invention is examined. As shown in FIG. 3, when the repetition period of a multilayer thin-film is about 5nm, the multilayer thin-film reveals the maximum hardness of 5000 (HKO.Ol) or higher. Considering that the hardness of the TiN and AIN mono-layer thin-films fabricated by the existing plasma chemical vapor deposition method are 2500 (HKO.Ol) and 1200
(HKO.Ol), respectively, the TiN/AlN multilayer thin-film fabricated according to the present invention reveals the characteristic of an ultra-lattice thin-film.
Industrial Applicability
As described above, the present invention can fabricate a nano-scale multilayer thin-film representing the characteristic of the ultra-lattice thin-film through a plasma chemical vapor deposition method without causing an amount of the reaction gas to be changed. Also, the present invention can solve the shortcomings of a physical vapor deposition (PVD) method such as a sputtering method, which is a very epoch-making invention in that the present invention provides a new method of fabricating an ultra-lattice thin-film. As described above, the present invention has been described with respect to particularly preferred embodiments . However, the present invention is not limited to the above embodiments, and it is possible for one who has an ordinary skill in the art to make various modifications and variations, without departing off the spirit of the present invention.

Claims

What is claimed is:
1. An automatic valve control system in a plasma chemical vapor deposition system or chemical vapor deposition system for deposition of a nano-scale multilayer film, the automatic valve control system comprising: a chamber in which a multilayer thin-film can be formed of at least two components by using a plasma chemical vapor deposition method or chemical vapor deposition method; at least two source supplies supplying a reaction material including a component constituting any one layer of the multilayer thin-film; at least two paths each whose middle portion is connected to each source supply, whose one end is connected to the chamber, and whose other end is connected to a bypass tube for controlling an amount of flow; a vacuum pump connected to the bypass tube; and at least four valves installed in either side of each path around each connection portion in each source supply, which is opened or closed.
2. The automatic valve control system in a plasma chemical vapor deposition system or chemical vapor deposition system of claim 1, wherein said at least four valves comprise a solenoid valve which can be automatically opened or closed, respectively.
3. The automatic valve control system in a plasma chemical vapor deposition system or chemical vapor deposition system of claim 1, further comprising a third source supply for directly supplying the source having a component which reacts each other and is hardened, to the chamber, during introduction of the source into the chamber among the sources supplied v a the at least two source supplies .
4. The automatic valve control system n a plasma chemical vapor deposition system or chemical vapor deposition system of claim 3, wherein said source supply further comprises a solenoid valve which canbe automatically opened or closed.
5. The automatic valve control system m a plasma chemical vapor deposition system or chemical vapor deposition system of any one of claims 1, 2 and 4, further comprising a controller controlling opening or closing of the valves with a predetermined interval of time.
6. The automatic valve control system in a plasma chemical vapor deposition system or chemical vapor deposition system of claim 5, wherein said controller controls the valves , and supplies the chamber with materials necessary for forming a thm-film through the at least two paths and source supplies, m a predetermined sequence, in order to form a multilayer thin-film.
7. The automatic valve control system in a plasma chemical vapor deposition system or chemical vapor deposition system of claim 1, wherein said chamber further comprises a gas distributor connected to one end of the path and installed in the chamber, for uniformly distributing the sources .
PCT/KR2003/000689 2002-04-06 2003-04-07 Automatic valve control system in plasma chemical vapor deposition system and chemical vapor deposition system for deposition of nano-scale multilayer film WO2003087429A1 (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005031032A2 (en) * 2003-09-26 2005-04-07 The Boc Group Plc Apparatus for conveying gases to and from a chamber
EP1550738A1 (en) * 2003-12-31 2005-07-06 The Boc Group, Inc. Method and apparatus for atomic layer deposition
KR20170122778A (en) * 2015-02-25 2017-11-06 코닝 인코포레이티드 Optical structure and article with multi-layer stack with high hardness and method of making same

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* Cited by examiner, † Cited by third party
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KR101925580B1 (en) * 2011-11-15 2019-02-28 주식회사 원익아이피에스 Apparatus for wafer deposition and method for operating the same
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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02243504A (en) * 1989-03-16 1990-09-27 Kobe Steel Ltd Production of high temperature superconductive thin film
US5562776A (en) * 1994-09-19 1996-10-08 Energy Conversion Devices, Inc. Apparatus for microwave plasma enhanced physical/chemical vapor deposition
JPH10190074A (en) * 1996-12-26 1998-07-21 Komatsu Ltd Manufacture of thermoelectric material and manufacture of thermoelectric element using the same
JP2000144429A (en) * 1998-11-13 2000-05-26 Fuji Electric Co Ltd Manufacture of carbonaceous protective film

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2619351B2 (en) * 1984-08-10 1997-06-11 株式会社日立製作所 Gas flow control method
JP3500620B2 (en) * 1994-10-24 2004-02-23 株式会社ニコン Projection exposure method and apparatus
JP3768575B2 (en) * 1995-11-28 2006-04-19 アプライド マテリアルズ インコーポレイテッド CVD apparatus and chamber cleaning method
US6342277B1 (en) * 1996-08-16 2002-01-29 Licensee For Microelectronics: Asm America, Inc. Sequential chemical vapor deposition
KR100671612B1 (en) * 2000-06-30 2007-01-18 주식회사 하이닉스반도체 Apparatus for depositing metal and a method for forming a metal layer using the same

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02243504A (en) * 1989-03-16 1990-09-27 Kobe Steel Ltd Production of high temperature superconductive thin film
US5562776A (en) * 1994-09-19 1996-10-08 Energy Conversion Devices, Inc. Apparatus for microwave plasma enhanced physical/chemical vapor deposition
JPH10190074A (en) * 1996-12-26 1998-07-21 Komatsu Ltd Manufacture of thermoelectric material and manufacture of thermoelectric element using the same
JP2000144429A (en) * 1998-11-13 2000-05-26 Fuji Electric Co Ltd Manufacture of carbonaceous protective film

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005031032A2 (en) * 2003-09-26 2005-04-07 The Boc Group Plc Apparatus for conveying gases to and from a chamber
WO2005031032A3 (en) * 2003-09-26 2005-07-28 Boc Group Plc Apparatus for conveying gases to and from a chamber
US7445023B2 (en) 2003-09-26 2008-11-04 Edwards Limited Apparatus for conveying gases to and from a chamber
EP1550738A1 (en) * 2003-12-31 2005-07-06 The Boc Group, Inc. Method and apparatus for atomic layer deposition
KR20170122778A (en) * 2015-02-25 2017-11-06 코닝 인코포레이티드 Optical structure and article with multi-layer stack with high hardness and method of making same
JP2018509652A (en) * 2015-02-25 2018-04-05 コーニング インコーポレイテッド Optical structure and article provided with high-hardness multilayer laminate, and method for producing the same
US10730790B2 (en) 2015-02-25 2020-08-04 Corning Incorporated Optical structures and articles with multilayer stacks having high hardness and methods for making the same
KR102593891B1 (en) 2015-02-25 2023-10-26 코닝 인코포레이티드 Optical structures and products having multi-layer stacks with high hardness and methods for manufacturing the same

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