WO2012106600A2 - In situ vapor phase surface activation of sio2 - Google Patents
In situ vapor phase surface activation of sio2 Download PDFInfo
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- WO2012106600A2 WO2012106600A2 PCT/US2012/023778 US2012023778W WO2012106600A2 WO 2012106600 A2 WO2012106600 A2 WO 2012106600A2 US 2012023778 W US2012023778 W US 2012023778W WO 2012106600 A2 WO2012106600 A2 WO 2012106600A2
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- WIPO (PCT)
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- substrate
- thermal oxide
- terminations
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- H—ELECTRICITY
- H10—SEMICONDUCTOR DEVICES; ELECTRIC SOLID-STATE DEVICES NOT OTHERWISE PROVIDED FOR
- H10P—GENERIC PROCESSES OR APPARATUS FOR THE MANUFACTURE OR TREATMENT OF DEVICES COVERED BY CLASS H10
- H10P95/00—Generic processes or apparatus for manufacture or treatments not covered by the other groups of this subclass
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- 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
- C23C16/02—Pretreatment of the material to be coated
- C23C16/0272—Deposition of sub-layers, e.g. to promote the adhesion of the main coating
-
- 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
- C23C16/405—Oxides of refractory metals or yttrium
-
- 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
- C23C16/45523—Pulsed gas flow or change of composition over time
- C23C16/45525—Atomic layer deposition [ALD]
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- H—ELECTRICITY
- H10—SEMICONDUCTOR DEVICES; ELECTRIC SOLID-STATE DEVICES NOT OTHERWISE PROVIDED FOR
- H10P—GENERIC PROCESSES OR APPARATUS FOR THE MANUFACTURE OR TREATMENT OF DEVICES COVERED BY CLASS H10
- H10P14/00—Formation of materials, e.g. in the shape of layers or pillars
- H10P14/60—Formation of materials, e.g. in the shape of layers or pillars of insulating materials
- H10P14/63—Formation of materials, e.g. in the shape of layers or pillars of insulating materials characterised by the formation processes
- H10P14/6326—Deposition processes
- H10P14/6328—Deposition from the gas or vapour phase
- H10P14/6334—Deposition from the gas or vapour phase using decomposition or reaction of gaseous or vapour phase compounds, i.e. chemical vapour deposition
- H10P14/6339—Deposition from the gas or vapour phase using decomposition or reaction of gaseous or vapour phase compounds, i.e. chemical vapour deposition deposition by cyclic CVD, e.g. ALD, ALE or pulsed CVD
-
- H—ELECTRICITY
- H10—SEMICONDUCTOR DEVICES; ELECTRIC SOLID-STATE DEVICES NOT OTHERWISE PROVIDED FOR
- H10P—GENERIC PROCESSES OR APPARATUS FOR THE MANUFACTURE OR TREATMENT OF DEVICES COVERED BY CLASS H10
- H10P14/00—Formation of materials, e.g. in the shape of layers or pillars
- H10P14/60—Formation of materials, e.g. in the shape of layers or pillars of insulating materials
- H10P14/65—Formation of materials, e.g. in the shape of layers or pillars of insulating materials characterised by treatments performed before or after the formation of the materials
- H10P14/6502—Formation of materials, e.g. in the shape of layers or pillars of insulating materials characterised by treatments performed before or after the formation of the materials of treatments performed before formation of the materials
- H10P14/6512—Formation of materials, e.g. in the shape of layers or pillars of insulating materials characterised by treatments performed before or after the formation of the materials of treatments performed before formation of the materials by exposure to a gas or vapour
-
- H—ELECTRICITY
- H10—SEMICONDUCTOR DEVICES; ELECTRIC SOLID-STATE DEVICES NOT OTHERWISE PROVIDED FOR
- H10P—GENERIC PROCESSES OR APPARATUS FOR THE MANUFACTURE OR TREATMENT OF DEVICES COVERED BY CLASS H10
- H10P14/00—Formation of materials, e.g. in the shape of layers or pillars
- H10P14/60—Formation of materials, e.g. in the shape of layers or pillars of insulating materials
- H10P14/69—Inorganic materials
- H10P14/692—Inorganic materials composed of oxides, glassy oxides or oxide-based glasses
- H10P14/6938—Inorganic materials composed of oxides, glassy oxides or oxide-based glasses the material containing at least one metal element, e.g. metal oxides, metal oxynitrides or metal oxycarbides
- H10P14/6939—Inorganic materials composed of oxides, glassy oxides or oxide-based glasses the material containing at least one metal element, e.g. metal oxides, metal oxynitrides or metal oxycarbides characterised by the metal
- H10P14/69392—Inorganic materials composed of oxides, glassy oxides or oxide-based glasses the material containing at least one metal element, e.g. metal oxides, metal oxynitrides or metal oxycarbides characterised by the metal the material containing hafnium, e.g. HfO2
-
- H—ELECTRICITY
- H10—SEMICONDUCTOR DEVICES; ELECTRIC SOLID-STATE DEVICES NOT OTHERWISE PROVIDED FOR
- H10P—GENERIC PROCESSES OR APPARATUS FOR THE MANUFACTURE OR TREATMENT OF DEVICES COVERED BY CLASS H10
- H10P95/00—Generic processes or apparatus for manufacture or treatments not covered by the other groups of this subclass
- H10P95/90—Thermal treatments, e.g. annealing or sintering
-
- H—ELECTRICITY
- H10—SEMICONDUCTOR DEVICES; ELECTRIC SOLID-STATE DEVICES NOT OTHERWISE PROVIDED FOR
- H10P—GENERIC PROCESSES OR APPARATUS FOR THE MANUFACTURE OR TREATMENT OF DEVICES COVERED BY CLASS H10
- H10P14/00—Formation of materials, e.g. in the shape of layers or pillars
- H10P14/60—Formation of materials, e.g. in the shape of layers or pillars of insulating materials
- H10P14/69—Inorganic materials
- H10P14/692—Inorganic materials composed of oxides, glassy oxides or oxide-based glasses
- H10P14/6921—Inorganic materials composed of oxides, glassy oxides or oxide-based glasses containing silicon
- H10P14/69215—Inorganic materials composed of oxides, glassy oxides or oxide-based glasses containing silicon the material being a silicon oxide, e.g. SiO2
Definitions
- Embodiments of the present invention generally relate to the field of integrated circuit fabrication, and more particularly to methods and apparatus for improving chemical vapor deposition, atomic layer deposition and other chemical reaction techniques.
- SiO 2 (silica) surfaces are not very reactive toward many precursors used in chemical reaction techniques to form layer because these surfaces have no reactive site or "chemical handle".
- a surface to make a surface more reactive it must be treated ex situ, that is, outside the process chamber environment, with harsh aqueous solutions such as SC-1 or chemox. These treatments generate surface hydroxyls which provide very good chemical handles for many subsequent precursors.
- SC-1 chemical reaction technique
- One problem with this surface activation strategy is that it requires an air break from the process chamber(s) that are used to deposit subsequent layers, and this air break inherently leads to carbon contamination and poor device performance.
- Other problems may include relatively higher etching rate impacting SiO 2 film thickness, and penetration of SC-1 aqueous solution to local device structure with porous film requirement.
- Embodiments of the invention provide in situ chemical techniques which require no air break that provide uniform surfaces and active sites on dense thermal oxide surfaces such as silica and silica-containing films.
- a process for preparing a substrate having a thermal oxide surface for formation of a film on the thermal oxide surface includes converting a dense thermal oxide with substantially no reactive surface terminations to a surface with reactive surface terminations.
- substantially no reactive surface terminations means that less than about 10% of the surface terminations are reactive.
- substantially no reactive surface terminations means that less than about 5%, 4%, 3%, 2%, 1 % or 0.5% of the surface terminations are reactive.
- the process is performed in situ in a process chamber.
- the surface terminations can include hydroxyls, halides or combinations thereof.
- one or more embodiments may include a process for preparing a substrate without immersion in an aqueous solution.
- the method comprises exposing the thermal oxide surface to a partial pressure of water below the saturated vapor pressure at the temperature of the substrate.
- the vapor pressure of the water is 20% of the saturated vapor pressure at the temperature of the substrate.
- the saturated vapor pressure of the water is 40%, 60% or 80% the saturated vapor pressure at the temperature of the substrate.
- the process includes simultaneously exposing the thermal oxide surface to a catalyst comprising a gaseous Lewis base in the process chamber, for example gaseous ammonia.
- a catalyst comprising a gaseous Lewis base in the process chamber, for example gaseous ammonia.
- the concentration of the Lewis base is greater than the concentration of water in the process chamber.
- the substrate preparation process is performed in situ in a process chamber.
- Subsequent film formation processes such as by chemical vapor deposition and/or atomic layer deposition are performed in the same process chamber as the surface preparation process, or in a process chamber in communication with the chamber used in the surface preparation process.
- the separate chambers, one for surface preparation of the substrate, and one for formation of the film on the surface-terminated thermal oxide can be arranged in cluster tool, and the substrate can be move between the chambers under load lock in which there is no air break which would expose the substrate to contaminants in the ambient atmosphere.
- Figure 1 is a schematic depicting an embodiment of the invention
- Figure 2 illustrates a cluster tool according to an embodiment
- Figure 3 is a graph showing the effect of various in situ surface treatments compared to an ex situ treatment.
- One or more embodiments of the invention involves the in situ chemical treatment of thermally grown oxides layers, for example, silica-containing (e.g., pure silica or SiON) layers with a chemical that will produces a chemical "handle" such as surface hydroxyls or surface halides that can further react with subsequent precursors.
- a chemical "handle" such as surface hydroxyls or surface halides that can further react with subsequent precursors.
- a non-limiting example of a subsequent precursor is HfCI 4
- the chemical treatments provide a Si0 2 /Hf0 2 interface.
- This invention is not limited to the reaction of HfCI with the activated surface, and HfCI 4 is provided as an illustrative example. This can invention can be applied to any film that needs to be grown on thermal Si0 2 .
- Non-limiting examples of other precursors that could be used according to embodiments of the invention include other metal halides (chlorides, bromides, etc), metal amides, metal alkyls, etc.
- other metal chlorides could include TaCI 5 , ZrCI 4 , and LaCI 3 .
- an active surface is provided using gas phase reactants that are chemically strong enough to break the Si-0 bonds and form Si-X and SiO-X bonds where X is some reactive group including but not limited to OH or CI.
- the condensation of two gas phase reactants is used on the surface of the SiO 2 which are much more reactive to the incoming precursor.
- the substrate can be annealed to generate a strong interface between the condensed phase and the SiO 2 .
- Figure 1 shows the reaction of a SiO 2 surface with water with and without an ammonia catalyst.
- the ammonia catalyst aids in performing the surface modification at low temperatures.
- the invention is not limited to the use of a catalyst or a specific ammonia catalyst.
- Figure 1 shows the mechanism of water reacting with a Si0 2 surface to produce two hydroxyl groups.
- the upper pathway of Figure 1 shows that at low temperatures, there is no reaction with water alone.
- the reaction pathway may proceed.
- the lower pathway in Figure 1 shows a mechanism when a Lewis base such as ammonia used as a catalyst.
- a Lewis base such as ammonia used as a catalyst.
- reactants/catalysts could be envisioned in the process.
- hydrogen peroxide combined with ammonia or hydrazine could lead to Si-OH and Si-O-O-H fragments with the Si-O-O-H fragments being easily reduced to Si-O-H.
- the above processes can be performed under conditions when gas or vapor is flowing into a process chamber or under non-flow conditions.
- water vapor the process results in hydroxylation of the surface.
- physisorption of water can take place.
- Aqueous ammonium hydroxide is believed to react with Si-O-Si bonds resulting in the generation of -OH terminations on the substrate surface.
- a surface that simulates an surface treated by an ex situ process such as SC1 can be generated in situ using gas phase reactions. This eliminates the need for an air break between the formation of the base oxide and the gate oxide which should eliminate excess carbon. Excess carbon can produce a large hysteresis capacitance value (CV) in high K dielectric films.
- CV hysteresis capacitance value
- inventions described herein can be performed in situ in a process that is prepared in a process chamber environment, and not outside a process chamber, where contamination of the substrate surface can occur.
- the processes described herein can be performed in a single or stand alone process chamber.
- the processes described herein can be performed in a cluster tool under load locked conditions in which there is no air break to move the substrate to subsequent process chambers.
- Figure 2 shows an example of a cluster tool or multi-chamber processing system 10 that can be used in conjunction with an aspect of the invention.
- the processing system 10 can include one or more load lock chambers 12, 14 for transferring substrates into and out of the system 10.
- a first robot 20 may transfer the substrates between the load lock chambers 12, 14, and a first set of one or more substrate processing chambers 32, 34, 36, 38.
- Each processing chamber 32, 34, 36, 38 may be configured to perform a number of substrate processing operations.
- processing chamber 32 can be an etch processor designed to practice an etch process
- processing chamber 34 can be a deposition reaction chamber for performing ALD or CVD.
- Processing chambers 36, 38 may also be configured to further provide, for example, cyclical layer deposition (CLD), atomic layer deposition (ALD), chemical vapor deposition (CVD), physical vapor deposition (PVD), etch, pre- clean, chemical clean, thermal treatment such as RTP, plasma nitridation, degas, orientation, EUV lithography (e.g. a stepper chamber) and other substrate processes.
- CLD cyclical layer deposition
- ALD atomic layer deposition
- CVD chemical vapor deposition
- PVD physical vapor deposition
- etch pre- clean, chemical clean, thermal treatment such as RTP, plasma nitridation, degas, orientation, EUV lithography (e.g. a stepper chamber) and other substrate processes.
- the first robot 20 can also transfer substrates to/from one or more transfer chambers 42, 44.
- the transfer chambers 42, 44 can be used to maintain ultrahigh vacuum conditions while allowing substrates to be transferred within the system 10.
- a second robot 50 can transfer the substrates between the transfer chambers 42, 44 and a second set of one or more processing chambers 62, 64, 66, 68.
- the processing chambers 62, 64, 66, 68 can be configured to perform a variety of substrate processing operations, including etch processes, in addition to cyclical layer deposition (CLD), atomic layer deposition (ALD), chemical vapor deposition (CVD), physical vapor deposition (PVD), epitaxial deposition, etch, pre-clean, chemical clean, thermal treatment such as RTP, plasma nitridation, degas, EUV lithography (e.g. a stepper chamber) and orientation. Any of the substrate processing chambers 32, 34, 36, 38, 62, 64, 66, 68 may be removed from the system 10 if not needed.
- CLD cyclical layer deposition
- ALD atomic layer deposition
- CVD chemical vapor deposition
- PVD physical vapor deposition
- epitaxial deposition etch
- etch pre-clean
- thermal treatment such as RTP, plasma nitridation, degas, EUV lithography (e.g. a stepper chamber) and orientation.
- FIG. 3 shows the differences in growth rates as a function of different surface treatment conditions.
- Sample Hf0 2 films were grown using an ALD techniques on silicon oxide films.
- Bare-Si wafers were sequentially processed through Steps 1 through Step 4, as shown in Figure 3.
- Steps 2 to Step 4 were processed without air break or exposure to air.
- Hf0 2 films thickness were quantified by X-ray Photoelectron Spectroscopy system. Process condition details are as follows and as summarized in Table 1 :
- Step 1 Each wafer for Samples A-l were etched using dilute HF, followed by SC-1 (NH 4 OH, H 2 0 2 and H 2 0) solution bath treatment at 50 °C for 8 minutes in wet bench system.
- Step 2 Each wafer underwent a 10 Angstrom Dry Thermal Oxidation process at 900 °C, in air O 2 at a pressure of 4 Torr for 15 seconds, as indicated in Figure 3.
- Step 3 Surface treatments were performed on each wafer, as indicated in Figure 3. As shown in Figure 3, Samples C, D and E underwent surface treatment with H 2 O only and Samples F, G, H and I underwent surface treatment with H 2 O in conjunction with NH 3 .
- the H 2 O condition is described as relative humidity, which is a percentile ratio of H 2 O partial pressure over H 2 O saturation pressure at specific temperature.
- NH 3 partial pressure is equivalent to H 2 O partial pressure which is described as relative humidity ("RH").
- RH relative humidity
- Step 4 Each wafer underwent an ALD hafnium oxide (HfO 2 ) process with hafnium tetrachloride (HfCI 4 ) and H 2 O chemistries.
- Sample A in Figure 3 shows the thickness of a film after 5 cycles of ALD of a wafer that has been treated by a wet chemistry ex situ technique.
- Sample B in Figure 3 shows film thickness of a film after 5 cycles of ALD on a dense thermal oxide, silicon oxide.
- the difference in thickness between Sample A and B is attributed to a lack of nucleation sites to start growth on untreated silicon oxide.
- the thickness data for Samples C through I show the different thickness of films obtained after 5 cycles using the different surface treatment conditions listed in Table 1 .
- the differences in thickness demonstrated in Figure 3 between Sample B and Sample H or Sample I show the benefit of this embodiment of the invention.
- a process in which a substrate containing a dense thermal oxide surface having limited or no receptive surface terminations such as hydroxyl surface terminations is treated in a process chamber in situ to provide surface terminations so that a subsequent film formation process (also referred to as a subsequent film deposition process) can be performed on the substrate surface.
- a subsequent film formation process also referred to as a subsequent film deposition process
- surface terminations can by a hydroxyl or halide surface termination.
- a dense thermal oxide surface such as silicon oxide is surface treated to functionalize the surface without substantially changing the thickness of the substrate.
- the term "substantially changing the thickness” means that the thickness does not change by more than 10 angstroms, or by more than 5 angstroms, or by more than 4 angstroms, or by more than 3 angstroms.
- a SiON surface can also be modified in accordance with embodiments of the invention.
- the surface treatments can be performed in situ in a CVD or ALD chamber such as a high K ALD chamber.
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- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
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- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Chemical Vapour Deposition (AREA)
- Formation Of Insulating Films (AREA)
Abstract
Description
Claims
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2013552677A JP2014506013A (en) | 2011-02-04 | 2012-02-03 | In situ vapor phase surface activation of SiO2 |
| CN2012800119147A CN103430286A (en) | 2011-02-04 | 2012-02-03 | In-Situ Vapor-Phase Surface Activation of Silica |
| KR1020137023348A KR20140050581A (en) | 2011-02-04 | 2012-02-03 | In situ vapor phase surface activation of sio2 |
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US201161439686P | 2011-02-04 | 2011-02-04 | |
| US61/439,686 | 2011-02-04 | ||
| US13/192,041 | 2011-07-27 | ||
| US13/192,041 US8778816B2 (en) | 2011-02-04 | 2011-07-27 | In situ vapor phase surface activation of SiO2 |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| WO2012106600A2 true WO2012106600A2 (en) | 2012-08-09 |
| WO2012106600A3 WO2012106600A3 (en) | 2012-11-08 |
| WO2012106600A9 WO2012106600A9 (en) | 2013-01-03 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/US2012/023778 Ceased WO2012106600A2 (en) | 2011-02-04 | 2012-02-03 | In situ vapor phase surface activation of sio2 |
Country Status (6)
| Country | Link |
|---|---|
| US (1) | US8778816B2 (en) |
| JP (1) | JP2014506013A (en) |
| KR (1) | KR20140050581A (en) |
| CN (1) | CN103430286A (en) |
| TW (1) | TW201234425A (en) |
| WO (1) | WO2012106600A2 (en) |
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