WO2005113167A1 - Compositions and methods for drying patterned wafers during manufacture of integrated circuitry products - Google Patents

Compositions and methods for drying patterned wafers during manufacture of integrated circuitry products Download PDF

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Publication number
WO2005113167A1
WO2005113167A1 PCT/US2004/014353 US2004014353W WO2005113167A1 WO 2005113167 A1 WO2005113167 A1 WO 2005113167A1 US 2004014353 W US2004014353 W US 2004014353W WO 2005113167 A1 WO2005113167 A1 WO 2005113167A1
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WIPO (PCT)
Prior art keywords
composition
water
contacting
supercritical fluid
carried out
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PCT/US2004/014353
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French (fr)
Inventor
Chongying Xu
Michael Korzenski
Thomas H. Baum
Alexander Borovik
Eliodor G. Ghenciu
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Advanced Technology Materials, Inc.
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Application filed by Advanced Technology Materials, Inc. filed Critical Advanced Technology Materials, Inc.
Priority to CNA2004800432546A priority Critical patent/CN1960813A/en
Priority to JP2007511332A priority patent/JP2007536730A/en
Priority to EP04751653A priority patent/EP1765526A4/en
Priority to PCT/US2004/014353 priority patent/WO2005113167A1/en
Publication of WO2005113167A1 publication Critical patent/WO2005113167A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B08CLEANING
    • B08BCLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B7/00Cleaning by methods not provided for in a single other subclass or a single group in this subclass
    • B08B7/0021Cleaning by methods not provided for in a single other subclass or a single group in this subclass by liquid gases or supercritical fluids

Definitions

  • the present invention relates to compositions and methodology for drying patterned wafers during the manufacture of integrated circuitry products.
  • patterned images are often dried with hexanes and nitrogen, or with isopropanol and nitrogen.
  • These conventional drying methods do not work well for images having a critical dimension width ⁇ 100nm and aspect ratio greater than 1.
  • the surface tension of isopropanol or hexane pulls the images together, leading to collapse of the lithographic resist and loss of the patterned image, or to degradation of the polymeric resist.
  • the art therefore is in need of improved techniques for drying of patterned wafers which effect complete removal of water, alcohols, etc., without causing collapse of the pattern features or other adverse effects on the patterned wafers.
  • the present invention relates to compositions and methodology for drying of patterned wafers to remove water, alcohols, etc. from the wafer, without causing collapse of the pattern or other adverse effect on the wafer article.
  • the present invention relates to a composition for drying a patterned wafer to remove water therefrom, such composition comprising supercritical fluid, and at least one water-reactive agent that chemically reacts with water to form reaction product(s) more soluble in the supercritical fluid than water.
  • the invention relates to a method of drying a patterned wafer to remove water therefrom, such method comprising contacting said patterned wafer with a composition comprising supercritical fluid, and at least one water-reactive agent that chemically reacts with water to form reaction product(s) more soluble in the supercritical fluid than water.
  • a still further aspect of the invention relates to a method of drying a patterned wafer to remove water therefrom, such method comprising contacting the patterned wafer with a first composition comprising liquid C0 2 , and thereafter contacting the patterned substrate with a second composition comprising SCC02, thereby effecting drying of the patterned substrate without damage to the pattern thereof.
  • Yet another aspect of the invention relates to a method of drying a patterned wafer to remove water therefrom, such method comprising (a) contacting the patterned wafer with a first composition comprising alcohol at pressure above about 1000 psi and temperature below 32°C,
  • FIG. 1 is a scanning electron microscope (SEM) photograph of a patterned wafer showing the details of the pattern structure, utilized as a control sample, relative to FIGS. 2-4.
  • FIG. 2 is an SEM photograph of a patterned wafer of the type shown in FIG. 1 , after air-drying of the wafer.
  • FIG. 3 is an SEM photograph of a patterned wafer of the type shown in FIG. 1 , after drying of the wafer with liquid C0 2 .
  • FIG. 4 is an SEM photograph of a patterned wafer of the type shown in FIG. 1 , after drying of the wafer, first with liquid C0 2 and then with supercritical C0 2 .
  • the present invention is based on the use of supercritical fluid (SCF) as a cleaning medium for drying of patterned wafers, in various approaches that avoid the problems incident to the use of supercritical fluids per se.
  • SCF supercritical fluid
  • supercritical fluids might on first consideration be regarded as potentially useful media for drying of patterned wafers, since supercritical fluids have high diffusivity, low viscosity, near-zero surface tension, and superior penetrating ability, supercritical fluids such as supercritical C0 2 (SCC02) are non-polar and therefore are not useful for drying of patterned wafers.
  • supercritical C0 2 SCC02
  • the solubility of water in supercritical C0 2 is ⁇ 0.1% by weight, making supercritical C0 2 unsuitable for removing residual water on the patterned wafer.
  • the present invention overcomes the problems incident to the use of supercritical fluids as drying media.
  • Supercritical fluids are formed under conditions at which the density of the liquid phase equals the density of the gaseous phase of the substance.
  • C0 2 carbon dioxide
  • the density of the SCF can be varied from liquid-like to gaseous-like, yielding different solvation abilities, by varying the pressure and temperature.
  • Supercritical fluids have a density/solubility and diffusibility approaching that of the liquid and gaseous phase, respectively. Additionally, the surface tension of SCFs is negligible.
  • supercritical C0 2 is a preferred SCF in the broad practice of the present invention, although the invention may be practiced with any suitable SCF species, with the choice of a particular SCF depending on the specific application involved.
  • Other preferred SCF species useful in the practice of the invention include oxygen, argon, krypton, xenon, and ammonia.
  • supercritical fluids are used as drying media for patterned wafers in drying compositions that include one or more water-reactive agents that chemically react with water on the patterned- wafer to form reaction product species that are more soluble in the supercritical fluid than water.
  • HFA hexafluoroacetone
  • the product diol, CH 3 C(OH) 2 CF 3 is highly soluble in SCC02 and is readily dissolved by the supercritical fluid, thereby effectively removing water from the patterned wafer substrate with which the supercritical fluid composition, comprising SCC02 and HFA, is contacted.
  • the water-reactive agent in the supercritical fluid-based wafer drying composition can be of any suitable type, including for example, other halogenated aldehydes and ketones; halogenated diketones, e.g., l,l,l,5,5,5-hexafluoro-2,4-pentanedione, alternatively denoted as (hfac)H; halogenated esters; carboxylic anhydrides, e.g., (CH 3 CO) 2 0; siloxanes, halogenated silanes; and any other compounds and materials that easily react with water and form derivatives soluble in supercritical C0 2 or other supercritical fluid species.
  • halogenated aldehydes and ketones e.g., l,l,l,5,5,5-hexafluoro-2,4-pentanedione, alternatively denoted as (hfac)H
  • halogenated esters e.g., (CH 3 CO)
  • the water-reactive agent can be formulated in the supercritical fluid composition at any suitable concentration that is effective for water removal from the patterned wafer substrate.
  • the concentration of the water-reactive agent can be a concentration in a range of from about 0.01 to about 10.0 % by weight, based on the total weight of the supercritical fluid and the water-reactive agent, with concentrations of from about 0.1 to about 7.5 % by weight, on the same total weight basis being more preferred, and from about 0.1 to about 5.0 % by weight, on the same total weight basis being most preferred.
  • the supercritical fluid drying composition in addition to the supercritical fluid and the water- reactive agent, can contain other components, e.g., co-solvent(s) for removal of components other than water from the patterned substrate, active agent(s) other than the water-reactive agent, surfactant(s), chelating agent(s), etc., as necessary or desirable in a given application of the drying composition.
  • co-solvent(s) for removal of components other than water from the patterned substrate
  • active agent(s) other than the water-reactive agent e.g., surfactant(s), chelating agent(s), etc.
  • an “active agent” is a material that induces chemical reaction and/or physical enhancement of solubility, either in the cleaning composition, or at the surface of the patterned substrate structure, to enhance the cleaning and/or removal action of the composition, relative to a corresponding composition lacking such material.
  • Illustrative co-solvent species can include, but are not limited to, xylene, methanol, ethanol, and higher alcohols, N-alkylpyrrolidiones, such as N-methyl-, N-octyl-, or N-phenyl-pyrrolidones, dimethylsulfoxide, sulfolane, catechol, ethyl lactate, acetone, methyl ethyl ketone, butyl carbitol, monoethanolamine, butyrol lactone, diglycol amine, alkyl ammonium fluoride T- butyrolactone butylene carbonate, ethylene carbonate, propylene carbonate, etc.
  • the co-solvent species may be a single component co-solvent or two or more solvent components.
  • the co-solvent may be present in the supercritical fluid-based drying composition at any suitable concentration, consistent with solubility of the co-solvent in the supercritical fluid.
  • active agents include, without limitation, acids, bases, reducing agents, and oxidizing agents.
  • the reducing agent may require activation, e.g., by an activation process involving thermal, optical, and/or sonic activation.
  • Surfactants useful in the drying compositions of the present invention may likewise be of any suitable type, including anionic, neutral cationic, and zwitterionic types.
  • Illustrative surfactant species include, without limitation, acetylenic alcohols and diols, and long alkyl chain secondary and tertiary amines.
  • Chelating agents useful in the drying compositions of the invention may be of any suitable type including, for example, polycarboxylic acids such as iminodiacetic acid and lauryl ethylenediamine triacetic acid, j8-diketones such as: 2,4-pentanedione; l,l,l-trifluoro-2,4- pentandione; and l,l,l,5,5,5-hexafluoro-2,4-pentanedion, substituted dithiocharbanates, malonic acid esters, and polyethylene glycols.
  • polycarboxylic acids such as iminodiacetic acid and lauryl ethylenediamine triacetic acid
  • j8-diketones such as: 2,4-pentanedione; l,l,l-trifluoro-2,4- pentandione; and l,l,l,l,5,5,5-hexafluoro-2,4-pentanedion, substitute
  • Illustrative species of acids useful in drying compositions of the invention include, without limitation, perfluorocarboxyic acids, and alkyl or aryl sulfonic acids.
  • Illustrative species of bases useful in drying compositions of the invention include, but are not limited to, amines, such as alkyl amines.
  • Oxidizing agents useful in the broad practice of the invention include, without limitation, oxygen, ozone and nitrous oxide.
  • Reducing agents usefully employed in the drying compositions of the invention include, without limitation, hydrogen, ammonia, xylenes, hydrides, silane, alkylsilanes, hydrazine hydrate or alkyl hydrazine.
  • compositions can be employed within the scope of the present invention, and such compositions can alternatively comprise, consist or consist essentially of specific identified component(s) described herein, as desired in a given application of the invention.
  • the contacting of the patterned substrate with the drying composition is carried out for a suitable period of time, which in a specific embodiment can for example be on the order of from about 20 to about 60 seconds, although other (longer or shorter) periods of contacting may be usefully employed depending on the nature and amount of the water to be removed from the patterned substrate, and the process conditions employed for drying.
  • the contacting vessel in which the supercritical fluid-based composition is contacted with the patterned substrate can be rapidly decompressed to separate the supercritical fluid composition from the patterned substrate and exhaust the regasified supercritical fluid from the contacting vessel, so that the non-supercritical component(s), such as the soluble water reaction product(s), can be entrained in the regasified supercritical fluid and likewise be removed from the drying locus.
  • the non-supercritical component(s) such as the soluble water reaction product(s)
  • Such decompression step may be conducted for a suitable period of time, e.g., on the order of
  • composition and method can be usefully employed to clean residual water from small dimensions on semiconductor substrates subsequent to photolithographic image patterning processes without the occurrence of pattern collapse.
  • the present invention contemplates use of supercritical fluid-based drying compositions as part of a two-step process for obtaining efficient drying without the collapse of the pattern features.
  • an initial drying step is carried out by contacting the patterned substrate with liquid C0 2 , followed by a second drying step including contacting the patterned substrate with SCC02, to achieve drying of the patterned substrate without accompanying damage to the patterned wafer.
  • the liquid phase C0 2 in the first step has a higher density than
  • FIG. 1 is a scanning electron microscope (SEM) photograph of a patterned wafer showing the details of the pattern structure, utilized as a control sample, relative to FIGS. 2-4.
  • SEM scanning electron microscope
  • FIG. 2 is an SEM photograph of a patterned wafer of the type shown in FIG. 1 , after such air-drying of the wafer. As shown in FIG. 2, the water and alcohol were not completely removed, and the residual amounts of these contaminants caused collapsing of the pattern structure to occur.
  • FIG. 3 is an SEM photograph of a patterned wafer of the type shown in FIG. 1, after such drying of the wafer with liquid C0 2 . As shown in FIG. 3, the water and alcohol were not completely removed, and the residual amounts of these contaminants caused a high level of collapse of the pattern structure to take place.
  • a third test wafer was dried in a two-step process as described hereinabove, including a first step of contacting the patterned wafer with liquid C0 2 and a second step of contacting the patterned wafer, after the first contacting step, with supercritical C0 2 .
  • FIG. 4 is an SEM photograph of a patterned wafer of the type shown in FIG.
  • the two-step process described above can be carried out at any suitable process conditions and for any suitable durations in the respective first and second steps.
  • the first liquid C0 2 contacting step can be carried out at temperature in a range of from about 20°C to about 30°C for a time in a range of from about 0.5 to about 20 minutes
  • the second SCC02 contacting step can be carried out at temperature in a range of from about 32°C to about 75°C for a duration in a range of from about 0.5 to about 20 minutes.
  • the present invention contemplates use of supercritical fluid-based drying compositions as part of a three-step process for obtaining efficient drying without the collapse of the pattern features.
  • an initial drying step is carried out in which the patterned substrate is contacted with alcohol at a pressure above about 1000 psi and temperature below the critical temperature of C0 2 , 32°C, for a suitable period of time, e.g. from about 1 minute to about 15 minutes.
  • the alcohol can be a single component alcohol, or it can be a mixture of alcohol species, and the alcohol can be recirculated in contact with the patterned substrate, or it can be contacted in a batch or a semibatch mode.
  • the second step is carried out after the alcohol contacting step, and involves contacting the patterned substrate with an alcohol C0 2 solution to remove alcohol from the first contacting step.
  • This second step preferably is carried out with recirculation of the alcohol/C0 2 solution through the contacting chamber containing the patterned substrate, although the contacting may be carried out in a single-pass manner, or in a batch or semi-batch mode of operation.
  • the second step contacting can be carried out at a temperature in a range of from about 22°C to about 31°C for a duration in a range of from about 0.5 to about 20 minutes.
  • the alcohol can be a single component alcohol, or it can be a mixture of alcohol species.
  • the alcohol utilized in the first and second contacting steps can be the same as or different from each other.
  • the alcohol can be of any suitable type.
  • such alcohol comprises a C 1 -C 4 alcohol (i.e., methanol, ethanol, propanol, or butanol), or a mixture of two or more of such alcohol species.
  • the third step is carried out after the alcohol/C0 2 solution contacting step, and involves rinsing the patterned substrate with SCC02.
  • Such supercritical fluid rinse step can be carried out at a temperature in a range of from about 32°C to about 75°C and pressure in a range of from about 80 to about 300 atm., for a duration in a range of from about 0.5 to about 30 minutes.
  • Each of the first, second and third steps can be carried out in a same process vessel, suitably valved, piped and manifolded for delivery, and, if desired, recirculation, of the successive drying compositions.
  • the alcohol/C0 2 solution can be formulated with the alcohol at any suitable concentration.
  • the concentration of the alcohol in the alcohol/C0 2 solution is from about 1 to about 15% by weight, based on the total weight of the alcohol and C0 2 components in the alcohol/C0 2 solution.
  • the alcohol/C0 2 solution can also be formulated with other components as desired, such as those (e.g., co-solvents, active agent(s), surfactant(s) and/or chelating agent(s)) illustratively described hereinabove.

Abstract

Drying of patterned wafers is achieved in a manner effecting removal of water from the patterned wafers without collapse or deterioration of the pattern structures thereof. The drying is carried out in one aspect of the invention with a composition containing supercritical fluid, and at least one water-reactive agent that chemically reacts with water to form reaction product(s) more soluble in the supercritical fluid than water. Various methodologies are described for use of supercritical fluids to dry patterned wafers, which avoid the (low water solubility) deficiency of supercritical fluids such as supercritical CO2.

Description

COMPOSITIONS AND METHODS FOR DRYING PATTERNED WAFERS DURING MANUFACTURE OF INTEGRATED CIRCUITRY PRODUCTS
BACKGROUND
The present invention relates to compositions and methodology for drying patterned wafers during the manufacture of integrated circuitry products.
BACKGROUND OF THE RELATED ART
During the manufacture of integrated circuit (IC) products, residual liquids such as water, alcohols, and the like must be completely removed from patterned wafers by drying operations. However, when critical dimensions are smaller than about 100 nanometers (nm), it is difficult to remove residual water from the patterned wafers with high aspect ratio trenches and vias without causing collapse of the lithographic pattern features.
For example, in the development of photo-exposed lithographic resists, patterned images are often dried with hexanes and nitrogen, or with isopropanol and nitrogen. These conventional drying methods do not work well for images having a critical dimension width <100nm and aspect ratio greater than 1. At such feature dimensions, the surface tension of isopropanol or hexane pulls the images together, leading to collapse of the lithographic resist and loss of the patterned image, or to degradation of the polymeric resist.
The art therefore is in need of improved techniques for drying of patterned wafers which effect complete removal of water, alcohols, etc., without causing collapse of the pattern features or other adverse effects on the patterned wafers.
SUMMARY OF THE INVENTION
The present invention relates to compositions and methodology for drying of patterned wafers to remove water, alcohols, etc. from the wafer, without causing collapse of the pattern or other adverse effect on the wafer article. In one aspect, the present invention relates to a composition for drying a patterned wafer to remove water therefrom, such composition comprising supercritical fluid, and at least one water-reactive agent that chemically reacts with water to form reaction product(s) more soluble in the supercritical fluid than water.
In a further aspect, the invention relates to a method of drying a patterned wafer to remove water therefrom, such method comprising contacting said patterned wafer with a composition comprising supercritical fluid, and at least one water-reactive agent that chemically reacts with water to form reaction product(s) more soluble in the supercritical fluid than water.
A still further aspect of the invention relates to a method of drying a patterned wafer to remove water therefrom, such method comprising contacting the patterned wafer with a first composition comprising liquid C02, and thereafter contacting the patterned substrate with a second composition comprising SCC02, thereby effecting drying of the patterned substrate without damage to the pattern thereof.
Yet another aspect of the invention relates to a method of drying a patterned wafer to remove water therefrom, such method comprising (a) contacting the patterned wafer with a first composition comprising alcohol at pressure above about 1000 psi and temperature below 32°C,
(b) contacting the patterned wafer with a second composition comprising an alcohol/C02 solution, and (c) contacting the patterned substrate with a third composition comprising
SCC02, thereby effecting drying of the patterned substrate without damage to the pattern thereof.
Other aspects, features and embodiments of the invention will be more fully apparent from the ensuing disclosure and appended claims.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1 is a scanning electron microscope (SEM) photograph of a patterned wafer showing the details of the pattern structure, utilized as a control sample, relative to FIGS. 2-4. FIG. 2 is an SEM photograph of a patterned wafer of the type shown in FIG. 1 , after air-drying of the wafer. FIG. 3 is an SEM photograph of a patterned wafer of the type shown in FIG. 1 , after drying of the wafer with liquid C02.
FIG. 4 is an SEM photograph of a patterned wafer of the type shown in FIG. 1 , after drying of the wafer, first with liquid C02 and then with supercritical C02.
DETAILED DESCRIPTION OF THE INVENTION AND PREFERRED EMBODIMENTS THEREOF
The present invention is based on the use of supercritical fluid (SCF) as a cleaning medium for drying of patterned wafers, in various approaches that avoid the problems incident to the use of supercritical fluids per se.
While supercritical fluids might on first consideration be regarded as potentially useful media for drying of patterned wafers, since supercritical fluids have high diffusivity, low viscosity, near-zero surface tension, and superior penetrating ability, supercritical fluids such as supercritical C02 (SCC02) are non-polar and therefore are not useful for drying of patterned wafers. For example, the solubility of water in supercritical C02 is < 0.1% by weight, making supercritical C02 unsuitable for removing residual water on the patterned wafer. The present invention overcomes the problems incident to the use of supercritical fluids as drying media.
While the invention is hereinafter described with specific reference to C02 as an illustrative supercritical fluid species, it will be recognized that the utility of the invention is not thus limited, and that the supercritical fluid in the practice of the present invention can be of any suitable type. Supercritical fluids are formed under conditions at which the density of the liquid phase equals the density of the gaseous phase of the substance. For example, carbon dioxide (C02), which is a gas at standard temperature and pressure, undergoes a transition from liquid to SCF above a critical point, corresponding to Tc > 31.TC and pc > 72.8 atm. Once formed, the density of the SCF can be varied from liquid-like to gaseous-like, yielding different solvation abilities, by varying the pressure and temperature. Supercritical fluids have a density/solubility and diffusibility approaching that of the liquid and gaseous phase, respectively. Additionally, the surface tension of SCFs is negligible.
Because of its readily manufactured character, lack of toxicity and negligible environmental effects, supercritical C02 is a preferred SCF in the broad practice of the present invention, although the invention may be practiced with any suitable SCF species, with the choice of a particular SCF depending on the specific application involved. Other preferred SCF species useful in the practice of the invention include oxygen, argon, krypton, xenon, and ammonia.
In a first embodiment, supercritical fluids are used as drying media for patterned wafers in drying compositions that include one or more water-reactive agents that chemically react with water on the patterned- wafer to form reaction product species that are more soluble in the supercritical fluid than water.
As an illustrative example, hexafluoroacetone (HFA) is usefully employed as a water-reactive agent in SCC02 to provide a highly effective supercritical fluid composition for drying of patterned wafers. In such composition, HFA reacts instantly with water and quantitatively forms a soluble and volatile diol as depicted in the following reaction:
H20 + CF3COCF3 → CH3C(OH)2CF3
The product diol, CH3C(OH)2CF3, is highly soluble in SCC02 and is readily dissolved by the supercritical fluid, thereby effectively removing water from the patterned wafer substrate with which the supercritical fluid composition, comprising SCC02 and HFA, is contacted.
More generally, the water-reactive agent in the supercritical fluid-based wafer drying composition can be of any suitable type, including for example, other halogenated aldehydes and ketones; halogenated diketones, e.g., l,l,l,5,5,5-hexafluoro-2,4-pentanedione, alternatively denoted as (hfac)H; halogenated esters; carboxylic anhydrides, e.g., (CH3CO)20; siloxanes, halogenated silanes; and any other compounds and materials that easily react with water and form derivatives soluble in supercritical C02 or other supercritical fluid species.
Generally, the water-reactive agent can be formulated in the supercritical fluid composition at any suitable concentration that is effective for water removal from the patterned wafer substrate. In various embodiments, depending on the particular supercritical fluid species employed, the concentration of the water-reactive agent can be a concentration in a range of from about 0.01 to about 10.0 % by weight, based on the total weight of the supercritical fluid and the water-reactive agent, with concentrations of from about 0.1 to about 7.5 % by weight, on the same total weight basis being more preferred, and from about 0.1 to about 5.0 % by weight, on the same total weight basis being most preferred.
The supercritical fluid drying composition in addition to the supercritical fluid and the water- reactive agent, can contain other components, e.g., co-solvent(s) for removal of components other than water from the patterned substrate, active agent(s) other than the water-reactive agent, surfactant(s), chelating agent(s), etc., as necessary or desirable in a given application of the drying composition.
As used in such context, an "active agent" is a material that induces chemical reaction and/or physical enhancement of solubility, either in the cleaning composition, or at the surface of the patterned substrate structure, to enhance the cleaning and/or removal action of the composition, relative to a corresponding composition lacking such material.
Illustrative co-solvent species can include, but are not limited to, xylene, methanol, ethanol, and higher alcohols, N-alkylpyrrolidiones, such as N-methyl-, N-octyl-, or N-phenyl-pyrrolidones, dimethylsulfoxide, sulfolane, catechol, ethyl lactate, acetone, methyl ethyl ketone, butyl carbitol, monoethanolamine, butyrol lactone, diglycol amine, alkyl ammonium fluoride T- butyrolactone butylene carbonate, ethylene carbonate, propylene carbonate, etc. The co-solvent species may be a single component co-solvent or two or more solvent components. The co-solvent may be present in the supercritical fluid-based drying composition at any suitable concentration, consistent with solubility of the co-solvent in the supercritical fluid.
Examples of active agents include, without limitation, acids, bases, reducing agents, and oxidizing agents. When a reducing agent is solubilized in the supercritical fluid, the reducing agent may require activation, e.g., by an activation process involving thermal, optical, and/or sonic activation. Surfactants useful in the drying compositions of the present invention may likewise be of any suitable type, including anionic, neutral cationic, and zwitterionic types. Illustrative surfactant species include, without limitation, acetylenic alcohols and diols, and long alkyl chain secondary and tertiary amines.
Chelating agents useful in the drying compositions of the invention may be of any suitable type including, for example, polycarboxylic acids such as iminodiacetic acid and lauryl ethylenediamine triacetic acid, j8-diketones such as: 2,4-pentanedione; l,l,l-trifluoro-2,4- pentandione; and l,l,l,5,5,5-hexafluoro-2,4-pentanedion, substituted dithiocharbanates, malonic acid esters, and polyethylene glycols.
Illustrative species of acids useful in drying compositions of the invention include, without limitation, perfluorocarboxyic acids, and alkyl or aryl sulfonic acids. Illustrative species of bases useful in drying compositions of the invention include, but are not limited to, amines, such as alkyl amines. Oxidizing agents useful in the broad practice of the invention include, without limitation, oxygen, ozone and nitrous oxide. Reducing agents usefully employed in the drying compositions of the invention include, without limitation, hydrogen, ammonia, xylenes, hydrides, silane, alkylsilanes, hydrazine hydrate or alkyl hydrazine.
Various compositions can be employed within the scope of the present invention, and such compositions can alternatively comprise, consist or consist essentially of specific identified component(s) described herein, as desired in a given application of the invention. The contacting of the patterned substrate with the drying composition is carried out for a suitable period of time, which in a specific embodiment can for example be on the order of from about 20 to about 60 seconds, although other (longer or shorter) periods of contacting may be usefully employed depending on the nature and amount of the water to be removed from the patterned substrate, and the process conditions employed for drying.
Following drying of the patterned substrate, the contacting vessel in which the supercritical fluid-based composition is contacted with the patterned substrate can be rapidly decompressed to separate the supercritical fluid composition from the patterned substrate and exhaust the regasified supercritical fluid from the contacting vessel, so that the non-supercritical component(s), such as the soluble water reaction product(s), can be entrained in the regasified supercritical fluid and likewise be removed from the drying locus.
Such decompression step may be conducted for a suitable period of time, e.g., on the order of
10-40 seconds, although longer or shorter times may be desirable depending on the character of the material to be removed from the patterned substrate and the specifics of the process. If necessary, repeated cycles of contacting and decompression may be utilized, to achieve substantially complete removal of the water from the patterned substrate article.
The above-described composition and method can be usefully employed to clean residual water from small dimensions on semiconductor substrates subsequent to photolithographic image patterning processes without the occurrence of pattern collapse.
In another aspect, the present invention contemplates use of supercritical fluid-based drying compositions as part of a two-step process for obtaining efficient drying without the collapse of the pattern features. In this drying process, an initial drying step is carried out by contacting the patterned substrate with liquid C02, followed by a second drying step including contacting the patterned substrate with SCC02, to achieve drying of the patterned substrate without accompanying damage to the patterned wafer.
In this two-step drying process, the liquid phase C02 in the first step has a higher density than
SCC02, so that it can solvate water and/or alcohol on the patterned substrate, but such contacting alone is not sufficient to complete the drying of the patterned substrate, and therefore the second step of rinsing the patterned substrate is employed to effect complete removal of the water and/or alcohol on the substrate.
The advantages of the two-step drying process described above were demonstrated using patterned wafers of the type shown in FIG. 1
FIG. 1 is a scanning electron microscope (SEM) photograph of a patterned wafer showing the details of the pattern structure, utilized as a control sample, relative to FIGS. 2-4.
In the drying tests, the test wafers were immersed in water and then in pure alcohol for several minutes each, and the wafers were then placed in the cleaning chamber for drying. A first test wafer was air-dried. FIG. 2 is an SEM photograph of a patterned wafer of the type shown in FIG. 1 , after such air-drying of the wafer. As shown in FIG. 2, the water and alcohol were not completely removed, and the residual amounts of these contaminants caused collapsing of the pattern structure to occur.
A second test wafer was dried with liquid C02. FIG. 3 is an SEM photograph of a patterned wafer of the type shown in FIG. 1, after such drying of the wafer with liquid C02. As shown in FIG. 3, the water and alcohol were not completely removed, and the residual amounts of these contaminants caused a high level of collapse of the pattern structure to take place. A third test wafer was dried in a two-step process as described hereinabove, including a first step of contacting the patterned wafer with liquid C02 and a second step of contacting the patterned wafer, after the first contacting step, with supercritical C02. FIG. 4 is an SEM photograph of a patterned wafer of the type shown in FIG. 1 , after such drying of the wafer, first with liquid C02 and then with supercritical C02. The pattern structure of the wafer was not altered by this two-step drying operation, and the pattern was retained in a manner consistent with the control wafer (compare FIGS. 1 and 4).
The two-step process described above can be carried out at any suitable process conditions and for any suitable durations in the respective first and second steps. In one embodiment, the first liquid C02 contacting step can be carried out at temperature in a range of from about 20°C to about 30°C for a time in a range of from about 0.5 to about 20 minutes, and the second SCC02 contacting step can be carried out at temperature in a range of from about 32°C to about 75°C for a duration in a range of from about 0.5 to about 20 minutes.
In yet another aspect, the present invention contemplates use of supercritical fluid-based drying compositions as part of a three-step process for obtaining efficient drying without the collapse of the pattern features.
In this drying process, an initial drying step is carried out in which the patterned substrate is contacted with alcohol at a pressure above about 1000 psi and temperature below the critical temperature of C02, 32°C, for a suitable period of time, e.g. from about 1 minute to about 15 minutes. The alcohol can be a single component alcohol, or it can be a mixture of alcohol species, and the alcohol can be recirculated in contact with the patterned substrate, or it can be contacted in a batch or a semibatch mode.
The second step is carried out after the alcohol contacting step, and involves contacting the patterned substrate with an alcohol C02 solution to remove alcohol from the first contacting step. This second step preferably is carried out with recirculation of the alcohol/C02 solution through the contacting chamber containing the patterned substrate, although the contacting may be carried out in a single-pass manner, or in a batch or semi-batch mode of operation. The second step contacting can be carried out at a temperature in a range of from about 22°C to about 31°C for a duration in a range of from about 0.5 to about 20 minutes. As in the first step, the alcohol can be a single component alcohol, or it can be a mixture of alcohol species. The alcohol utilized in the first and second contacting steps can be the same as or different from each other. The alcohol can be of any suitable type. In one embodiment of the invention, such alcohol comprises a C1-C4 alcohol (i.e., methanol, ethanol, propanol, or butanol), or a mixture of two or more of such alcohol species.
The third step is carried out after the alcohol/C02 solution contacting step, and involves rinsing the patterned substrate with SCC02. Such supercritical fluid rinse step can be carried out at a temperature in a range of from about 32°C to about 75°C and pressure in a range of from about 80 to about 300 atm., for a duration in a range of from about 0.5 to about 30 minutes. Each of the first, second and third steps can be carried out in a same process vessel, suitably valved, piped and manifolded for delivery, and, if desired, recirculation, of the successive drying compositions.
The alcohol/C02 solution can be formulated with the alcohol at any suitable concentration. In one embodiment, the concentration of the alcohol in the alcohol/C02 solution is from about 1 to about 15% by weight, based on the total weight of the alcohol and C02 components in the alcohol/C02 solution. The alcohol/C02 solution can also be formulated with other components as desired, such as those (e.g., co-solvents, active agent(s), surfactant(s) and/or chelating agent(s)) illustratively described hereinabove. Although the invention has been described herein with reference to various specific aspects, features and embodiments, it will be appreciated that the invention is not thus limited, but rather extends to and encompasses other variations, modifications and embodiments, such as will suggest themselves to those of ordinary skill in the art, based on the disclosure herein. Accordingly, the invention is intended to be broadly interpreted and construed, as including all such other variations, modifications and embodiments, within the spirit and scope of the invention as hereinafter claimed.

Claims

THE CLAIMS What is claimed is:
1. A composition for drying a patterned wafer to remove water therefrom, said composition comprising supercritical fluid, and at least one water-reactive agent that chemically reacts with water to form reaction product(s) that is more soluble in the supercritical fluid than water.
2. The composition of claim 1, wherein said supercritical fluid comprises a supercritical fluid species selected from the group consisting of carbon dioxide, oxygen, argon, krypton, xenon, and ammonia.
3. The composition of claim 1, wherein said supercritical fluid comprises carbon dioxide.
4. The composition of claim 1 , wherein said at least one water-reactive agent comprises an agent selected from the group consisting of: halogenated aldehydes and ketones; halogenated diketones; halogenated esters; carboxylic anhydrides; siloxanes; and halogenated silanes.
5. The composition of claim 1, wherein said at least one water-reactive agent comprises an agent selected from the group consisting of: hexafluoroacetone; (CH3CO)20; and 1,1,1,5,5,5- hexafluoro-2,4-pentanedione.
6. The composition of claim 1, wherein said at least one water-reactive agent comprises hexafluoroacetone.
7. The composition of claim 1, wherein said at least one water-reactive agent comprises 1 , 1 , 1 ,5 ,5 ,5-hexafluoro-2 ,4-pentanedione.
8. The composition of claim 1, wherein said at least one water-reactive agent is at a concentration in a range of from about 0.01 to about 10 % by weight, based on the total weight of the supercritical fluid and the water-reactive agent.
9. The composition of claim 1, wherein said supercritical fluid comprises SCC02 and said water-reactive agent comprises hexafluoroacetone.
10. A method of drying a pattemed wafer to remove water therefrom, said method comprising contacting said patterned wafer with a composition comprising supercritical fluid, and at least one water-reactive agent that chemically reacts with water to form reaction product(s) more soluble in the supercritical fluid than water.
11. The method of claim 10, wherein said supercritical fluid comprises a supercritical fluid species selected from the group consisting of carbon dioxide, oxygen, argon, krypton, xenon, and ammonia.
12. The composition of claim 10, wherein said supercritical fluid comprises carbon dioxide.
13. The method of claim 10, wherein said at least one water-reactive agent comprises an agent selected from the group consisting of: halogenated aldehydes and ketones; halogenated diketones; halogenated esters; carboxylic anhydrides; siloxanes; and halogenated silanes.
14. The method of claim 10, wherein said at least one water-reactive agent comprises an agent selected from the group consisting of: hexafluoroacetone; (CH3CO)20; and 1,1,1,5,5,5- hexafluoro-2,4-pentanedione.
15. The method of claim 10, wherein said at least one water-reactive agent comprises hexafluoroacetone.
16. The method of claim 10, wherein said at least one water-reactive agent comprises l,l,l,5,5,5-hexafluoro-2,4-pentanedione.
17. The method of claim 10, wherein said at least one water-reactive agent is at a concentration in a range of from about 0.01 to about 10.0 % by weight, based on the total weight of the supercritical fluid and the water-reactive agent.
18. The method of claim 10, wherein said supercritical fluid comprises SCC02 and said water- reactive agent comprises hexafluoroacetone.
19. The method of claim 10, wherein said contacting is carried out for a period of from about 20 to about 60 seconds.
20. The method of claim 10, wherein said contacting is carried out in a contacting zone to which said composition is introduced.
21. The method of claim 20, wherein the composition is flowed through said contacting zone.
22. The method of claim 21, wherein the composition is recirculated through said contacting zone.
23. The method of claim 20, wherein after a predetermined period of contacting, the contacting zone is depressurized to exhaust the composition therefrom.
24. The method of claim 23, wherein the contacting zone is depressurized for a period of time in a range of from about 10 to about 40 seconds to exhaust the composition and removed water from the contacting zone.
25. The method of claim 10, wherein the contacting is carried out without collapse of the pattern of the patterned wafer.
26. A method of drying a patterned wafer to remove water therefrom, said method comprising contacting said patterned wafer with a first composition comprising liquid C0 , and thereafter contacting the patterned substrate with a second composition comprising SCC02, thereby effecting drying of the patterned substrate without damage to the pattern thereof.
27. The method of claim 26, wherein the first composition contacting step is carried out at temperature in a range of from about 20 to about 30°C.
28. The method of claim 27, wherein the first composition contacting step is carried out for a time in a range of from about 0.5 to about 20 minutes.
29. The method of claim 26, wherein the second composition contacting step is carried out at temperature in a range of from about 32 to about 75°C.
30. The method of claim 29, wherein the second composition contacting step is carried out for a time in a range of from about 0.5 to about 20 minutes.
31. The method of claim 26, wherein the first composition contacting step is carried out at temperature in a range of from about 20 to about 30°C for a time in a range of from about 0.5 to about 20 minutes, and the second composition contacting step is carried out at temperature in a range of from about 32 to about 75°C for a time in a range of from about 0.5 to about 20 minutes.
32. A method of drying a patterned wafer to remove water therefrom, said method comprising (a) contacting said patterned wafer with a first composition comprising alcohol at pressure above about 1000 psi and temperature below 32°C, (b) contacting said patterned wafer with a second composition comprising an alcohol C02 solution, and (c) contacting the patterned substrate with a third composition comprising SCC02, thereby effecting drying of the patterned substrate without damage to the pattern thereof.
33. The method of claim 32, wherein said contacting (a) is carried out for a period of from about 1 minute to about 15 minutes.
34. The method of claim 32, wherein said alcohol of said first composition comprises at least one Cι-C4 alcohol.
35. The method of claim 32, wherein said alcohol of said first composition comprises methanol.
36. The method of claim 32, wherein said alcohol of said first composition is the same as alcohol of the second composition.
37. The method of claim 32, wherein said first composition is recirculated in contact with the patterned wafer.
38. The method of claim 32, wherein the second composition is recirculated in contact with the patterned wafer.
39. The method of claim 32, wherein the third composition is recirculated in contact with the patterned wafer.
40. The method of claim 32, wherein said contacting (b) is carried out at temperature in a range of from about 22 to about 31°C.
41. The method of claim 32, wherein said contacting (b) is carried out for a period of from about 0.5 to about 20 minutes.
42. The method of claim 32, wherein said contacting (c) is carried out at temperature in a range of from about 32 to about 75°C.
43. The method of claim 32, wherein said contacting (c) is carried out for a time of from about 0.5 to about 20 minutes.
44. The method of claim 32, wherein concentration of said alcohol in said second composition is in a range of from about 1 to about 15% by weight, based on total weight of said alcohol and said C02 therein.
45. The method of claim 32, wherein the contacting steps (a), (b) and (c) are carried out in a same chamber.
PCT/US2004/014353 2004-05-07 2004-05-07 Compositions and methods for drying patterned wafers during manufacture of integrated circuitry products WO2005113167A1 (en)

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EP04751653A EP1765526A4 (en) 2004-05-07 2004-05-07 Compositions and methods for drying patterned wafers during manufacture of integrated circuitry products
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Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8440573B2 (en) * 2010-01-26 2013-05-14 Lam Research Corporation Method and apparatus for pattern collapse free wet processing of semiconductor devices
TWI826650B (en) * 2012-11-26 2023-12-21 美商應用材料股份有限公司 Stiction-free drying process with contaminant removal for high-aspect-ratio semiconductor device structures
US10283344B2 (en) 2014-07-11 2019-05-07 Applied Materials, Inc. Supercritical carbon dioxide process for low-k thin films
US10026629B2 (en) * 2014-10-17 2018-07-17 Tokyo Electron Limited Substrate liquid processing apparatus, substrate liquid processing method, and computer-readable storage medium storing substrate liquid processing program
JP6644881B2 (en) 2015-10-04 2020-02-12 アプライド マテリアルズ インコーポレイテッドApplied Materials,Incorporated Drying process for high aspect ratio features
CN116207033A (en) 2015-10-04 2023-06-02 应用材料公司 Substrate support and baffle plate apparatus
KR102189211B1 (en) 2015-10-04 2020-12-09 어플라이드 머티어리얼스, 인코포레이티드 Small thermal mass pressurized chamber
CN116206947A (en) 2015-10-04 2023-06-02 应用材料公司 Reduced space processing chamber

Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5730874A (en) * 1991-06-12 1998-03-24 Idaho Research Foundation, Inc. Extraction of metals using supercritical fluid and chelate forming legand
US6187911B1 (en) * 1998-05-08 2001-02-13 Idaho Research Foundation, Inc. Method for separating metal chelates from other materials based on solubilities in supercritical fluids
US6398875B1 (en) * 2001-06-27 2002-06-04 International Business Machines Corporation Process of drying semiconductor wafers using liquid or supercritical carbon dioxide
US20030047195A1 (en) * 2001-09-13 2003-03-13 Deyoung James Methods and apparatus for cleaning and/or treating a substrate using CO2
US6558475B1 (en) * 2000-04-10 2003-05-06 International Business Machines Corporation Process for cleaning a workpiece using supercritical carbon dioxide
US6576066B1 (en) * 1999-12-06 2003-06-10 Nippon Telegraph And Telephone Corporation Supercritical drying method and supercritical drying apparatus
US20030125225A1 (en) * 2001-12-31 2003-07-03 Chongying Xu Supercritical fluid cleaning of semiconductor substrates
US6602351B2 (en) * 2001-02-15 2003-08-05 Micell Technologies, Inc. Methods for the control of contaminants following carbon dioxide cleaning of microelectronic structures
US6684525B2 (en) * 2000-09-26 2004-02-03 University Of North Carolina At Chapel Hill Phosphate fluorosurfactants for use in carbon dioxide
US6764552B1 (en) * 2002-04-18 2004-07-20 Novellus Systems, Inc. Supercritical solutions for cleaning photoresist and post-etch residue from low-k materials
US6804900B2 (en) * 2002-08-22 2004-10-19 Kabushiki Kaisha Kobe Seiko Sho Method for drying microstructure member

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20030075185A (en) * 2001-02-15 2003-09-22 미셀 테크놀로지즈, 인코포레이티드 Methods for cleaning microelectronic structures
US6846380B2 (en) * 2002-06-13 2005-01-25 The Boc Group, Inc. Substrate processing apparatus and related systems and methods

Patent Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5730874A (en) * 1991-06-12 1998-03-24 Idaho Research Foundation, Inc. Extraction of metals using supercritical fluid and chelate forming legand
US6187911B1 (en) * 1998-05-08 2001-02-13 Idaho Research Foundation, Inc. Method for separating metal chelates from other materials based on solubilities in supercritical fluids
US6576066B1 (en) * 1999-12-06 2003-06-10 Nippon Telegraph And Telephone Corporation Supercritical drying method and supercritical drying apparatus
US6558475B1 (en) * 2000-04-10 2003-05-06 International Business Machines Corporation Process for cleaning a workpiece using supercritical carbon dioxide
US6684525B2 (en) * 2000-09-26 2004-02-03 University Of North Carolina At Chapel Hill Phosphate fluorosurfactants for use in carbon dioxide
US6602351B2 (en) * 2001-02-15 2003-08-05 Micell Technologies, Inc. Methods for the control of contaminants following carbon dioxide cleaning of microelectronic structures
US6398875B1 (en) * 2001-06-27 2002-06-04 International Business Machines Corporation Process of drying semiconductor wafers using liquid or supercritical carbon dioxide
US20030047195A1 (en) * 2001-09-13 2003-03-13 Deyoung James Methods and apparatus for cleaning and/or treating a substrate using CO2
US20030125225A1 (en) * 2001-12-31 2003-07-03 Chongying Xu Supercritical fluid cleaning of semiconductor substrates
US6764552B1 (en) * 2002-04-18 2004-07-20 Novellus Systems, Inc. Supercritical solutions for cleaning photoresist and post-etch residue from low-k materials
US6804900B2 (en) * 2002-08-22 2004-10-19 Kabushiki Kaisha Kobe Seiko Sho Method for drying microstructure member

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP1765526A4 *

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CN1960813A (en) 2007-05-09

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