[go: up one dir, main page]
More Web Proxy on the site http://driver.im/

US20010001949A1 - Chemical vapor deposition apparatus with liquid feed - Google Patents

Chemical vapor deposition apparatus with liquid feed Download PDF

Info

Publication number
US20010001949A1
US20010001949A1 US09/097,489 US9748998A US2001001949A1 US 20010001949 A1 US20010001949 A1 US 20010001949A1 US 9748998 A US9748998 A US 9748998A US 2001001949 A1 US2001001949 A1 US 2001001949A1
Authority
US
United States
Prior art keywords
liquid
specified
solution
precursor
temperature
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
US09/097,489
Other versions
US6428623B2 (en
Inventor
Donald L. Westmoreland
Gurtej S. Sandhu
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from US08/236,946 external-priority patent/US5393564A/en
Application filed by Individual filed Critical Individual
Priority to US09/097,489 priority Critical patent/US6428623B2/en
Publication of US20010001949A1 publication Critical patent/US20010001949A1/en
Priority to US10/213,030 priority patent/US7182979B2/en
Application granted granted Critical
Publication of US6428623B2 publication Critical patent/US6428623B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/44Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
    • C23C16/448Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for generating reactive gas streams, e.g. by evaporation or sublimation of precursor materials
    • C23C16/4485Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for generating reactive gas streams, e.g. by evaporation or sublimation of precursor materials by evaporation without using carrier gas in contact with the source material

Definitions

  • the invention relates to the manufacture of semiconductor circuits on semiconductor wafers, and more particularly to chemical vapor depositions of materials on the wafer.
  • a large number of nonvolatile metal organic precursors which are suitable in microelectronics applications for chemical vapor deposition (CVD) of thin films are solids at temperatures at or below 1500 Kelvin and at pressures at or above 10 ⁇ 10 Torr.
  • a majority of metal-organic compounds with attributes desirable for CVD are solids. These compounds have chemical stability, molecular structures, and reactivity which make them ideally suited for CVD application.
  • vapor transport is difficult to perform under temperatures and pressures typically utilized in semiconductor manufacture. Thus, vapor transport of these precursors is a major hinderance to the implementation of the precursors in a production environment.
  • the precursor has a sufficient vapor pressure, then sublimation of the precursor for transportation of its vapor is the only option available, however this is difficult to control in a manufacturing environment. Solid precursors have been dissolved, transported, and delivered in organic solution, but these solutions usually leave a large carbon residue.
  • CVD chemical vapor deposition
  • the invention features dissolving a nonvolatile precursor, either solid or liquid, in a solution and delivering the precursor in the solution to a CVD chamber.
  • the invention is a very efficient method for transporting a nonvolatile precursor for CVD in the manufacturing environment and incorporates a minimum amount of unwanted by-product in the desired film.
  • the method entails a process which is easily controlled and therefore predictable with repeatable results.
  • the invention is a method directed to the use of a nonvolatile precursor, either solid or liquid, in a chemical vapor deposition (CVD) process.
  • a solid precursor as referenced herein, is a precursor which is in a solid state at a temperature at or below 1500 Kelvin and at a pressure at or above 10 ⁇ 10 Torr
  • a liquid precursor as referenced herein, is a precursor which is in a liquid state at a temperature at or below 1500 Kelvin and at a pressure at or above 10 ⁇ 10 Torr.
  • the nonvolatile precursor is dissolved in a solvent to form a solution.
  • the nonvolatile precursor is then transported in the solution at a pressure and a temperature necessary to maintain it as a liquid to the CVD chamber.
  • the solution is transported in a continuous liquid stream to the CVD chamber.
  • a continuous liquid stream is an unbroken non-nebulized stream of liquid which may be passed to the chamber without interruption or may be passed to the chamber in a pulse or batch. The pulse or batch can be thought of as a portion of the solution.
  • the solution becomes a gas during rapid evaporation of the solution at a high temperature and at a low pressure.
  • the gaseous form of the precursor reacts with a reactant at the heated surface of the wafer.
  • the method of the invention can be used in liquid source chemical vapor deposition where the solution is applied to the wafer before being evaporated.
  • FIG. 1 is a cross section of a simplified representation of the equipment used to perform a chemical vapor deposition on a semiconductor wafer.
  • the invention is a method directed to the use of a nonvolatile precursor suitable for chemical vapor deposition (CVD).
  • the nonvolatile precursor may be a solid or a liquid.
  • the solid precursor as referenced herein, is a precursor which is in a solid state at a temperature at or below 1500 Kelvin and at a pressure at or above 10 ⁇ 10 Torr
  • the liquid precursor as referenced herein, is in a liquid state at a temperature at or below 1500 degrees Kelvin and at a pressure at or above 10 ⁇ 10 Torr.
  • the method can be understood by studying FIG. 1 in conjunction with the following description.
  • the nonvolatile precursor is dissolved in a solvent to form a solution 1 of the precursor and the solvent. It is important that the precursor and the solvent do not react with each other in liquid form.
  • the solvent can be either a reactive component which makes up a part of the film or it can be simply a nonreactive inert carrier.
  • the solution 1 is formed in a chamber 2 .
  • the solution 1 is then transported in liquid form at elevated pressures and/or reduced temperatures to a chamber 3 through a transport device 4 .
  • the liquid is transported as a continuous liquid stream to the chamber 3 .
  • a continuous liquid stream is an unbroken non-nebulized stream of liquid which may be passed to the chamber without interruption or may be passed to the chamber in a pulse or batch.
  • the pulse or batch can be thought of as a portion of the solution.
  • the solution 1 becomes a gas upon entry to the chamber 3 .
  • the chamber 3 is held at a high enough temperature and a low enough pressure to effect rapid evaporation of the solution 1 .
  • the precursor remains in the gas phase until it reacts with a reactant at a heated surface of the wafer 5 .
  • the reactant may be either the solvent in its gaseous state or may be another gas injected into the chamber 3 . In either case a material is produced during the reaction and deposited as a film on the wafer 5 . Typically, a gaseous by-product is also produced in the reaction.
  • One example of the first embodiment comprises a solid precursor of bis(cyclopentadienly)titanium diazide (Tiaz) dissolved in liquid ammonia (LNH 3 ) to form a solution 1 of Tiaz in LNH 3 in chamber 2 when the temperature of chamber 2 is 20° C. or less and the pressure is 120 psi or greater.
  • the Tiaz in LNH 3 is then transported to the chamber 3 through the transport device 4 .
  • the temperature and pressure of the transport device 4 are regulated in order to keep the solution in it liquid form. In this example the temperature is 20° or less and the pressure is 120 psi or greater.
  • the solution 1 immediately vaporizes upon entry into chamber 3 .
  • the rapid evaporation occurs because the chamber 3 is held at a temperature of 100° C. and a pressure of 500 millitorr and the water surface is held at 550° C. Hydrogen is injected into the chamber and combines with the vaporized Tiaz to form titanium nitride which is deposited on the wafer as a thin film. A by-product cyclopentadiene remains and is pumped from the chamber with the ammonia vapor.
  • the temperatures and pressures may be varied as long as the temperature and pressure of the chamber and transport device allow the precursor to remain dissolved in the solution.
  • the temperature and pressure of the chamber may vary as long as the solution is vaporized.
  • the solution 1 is applied to the wafer 5 before being evaporated.
  • This is typically referred to as liquid source chemical vapor deposition.
  • the solution is delivered through a nebulizer which delivers a very fine mist that settles evenly over the entire wafer.
  • the temperature of the wafer 5 may be either higher, or lower, or the same as the temperature of the solution 1 .
  • the wafer temperature and chamber 3 pressure must be maintained so that the solvent evaporates upon contact with the wafer surface and so that the precursor reacts immediately with the reactant gas, which is either injected into the chamber or formed during evaporation of the solution, to deposit a film.
  • the solution remains on the wafer until the wafer temperature is increased to evaporate the solvent.
  • the gaseous state of the precursor reacts with a gas reactant thereby producing a material deposited as a film on the wafer surface.
  • the reaction typically produces a gaseous by-product in addition to the deposited film.
  • the by-product and the solvent vapor in the case where the vapor doesn't react with the precursor to form the film, are then removed from the chamber 3 .
  • An example of the process of the second embodiment comprises a precursor, zirconium tetrachloride, dissolved in a solvent, silicon tetrachloride, to form a solution in chamber 2 when the temperature of the chamber 2 is between 60° and 10° C. and the pressure is 60 psi or greater.
  • the solution is then transported to the chamber 3 through the transport device 4 .
  • the temperature and pressure of the transport device 4 are regulated in order to maintain the solution in its liquid form.
  • the temperature and pressure of the transport device 4 are the same as the temperature and pressure of chamber 2 .
  • Chamber 3 is held at a pressure of 10 torr in order to help facilitate the vaporization of the solution on the wafer.
  • the wafer temperature is 600° C.
  • the zirconium tetrachloride in silicon tetrachloride solution is injected into the chamber 3 and reacts at the wafer surface to form a vapor and combines with hydrogen to form zirconium silicide which is deposited on the wafer to form a thin film.
  • a by-product, hydrogen chloride, is formed and is pumped from the chamber with the excess silicon tetrachloride.
  • Ideal solvents for this application are inorganic liquids such as: liquid ammonia (NH 3 ), liquid NO 2 , liquid SO 2 , liquid TiCl 4 , liquid TaCl 5 , liquid WF 6 , liquid SiCl 4 , borazine, dimethyl hydrazine, liquid xenonflourides, liquid phosphine, liquid arsine, diethylzinc, BCl 3 , BF 3 , SF 6 , H 2 S, SiF 4 , CBrF 3 , CCl 2 F 2 , CCl 3 F, CClF 3 , CCl 4 , SiH 2 Cl 2 .
  • Many of these solvents are gases at room temperature but are easily maintained as liquids with elevated pressure and reduced temperature. For example, ammonia boils at ⁇ 33° C. and is an excellent solvent. It is a further advantage that these gases are easily available at a low cost at the present time.
  • the following gases may be selected as reactant gases for forming the deposited film: hydrogen, ammonia, or silane.
  • nonvolatile liquid precursors suitable for forming films on semiconductor wafers by the method of the invention indenyltris(dimethylamido)zirconium, cyclopentadienyltris(diethylamido)titanium, and bis(cyclopentadienyl)bis(dimethylamido)titanium.
  • the invention provides an efficient method for transporting nonvolatile precursors for CVD in the manufacturing environment.

Landscapes

  • Chemical & Material Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Electrodes Of Semiconductors (AREA)
  • Chemical Vapour Deposition (AREA)

Abstract

The invention is a method directed to the use of a nonvolatile precursor, either a solid precursor or a liquid precursor, suitable for chemical vapor deposition (CVD), including liquid source CVD (LSCVD), of a semiconductor film. Using the method of the invention the nonvolatile precursor is dissolved in a solvent. The choice of solvent is typically an inorganic compound that has a moderate to high vapor pressure at room temperature and that can be liquified by a combination of pressure and cooling. The solution thus formed is then transported at an elevated pressure and/or a reduced temperature to the CVD chamber. In CVD the solution evaporates at a higher temperature and a lower pressure upon entry to the CVD chamber, and the nonvolatile precursor, in its gaseous state, along with a gas reactant, produces a product which is deposited as a thin film on a semiconductor wafer. In LSCVD the liquid enters the chamber, contacts the wafer, evaporates, produces a product which is deposited as a thin film on the wafer surface.

Description

    FIELD OF THE INVENTION
  • The invention relates to the manufacture of semiconductor circuits on semiconductor wafers, and more particularly to chemical vapor depositions of materials on the wafer. [0001]
  • BACKGROUND OF THE INVENTION
  • A large number of nonvolatile metal organic precursors which are suitable in microelectronics applications for chemical vapor deposition (CVD) of thin films are solids at temperatures at or below 1500 Kelvin and at pressures at or above 10[0002] −10 Torr. In fact, a majority of metal-organic compounds with attributes desirable for CVD are solids. These compounds have chemical stability, molecular structures, and reactivity which make them ideally suited for CVD application. However, vapor transport is difficult to perform under temperatures and pressures typically utilized in semiconductor manufacture. Thus, vapor transport of these precursors is a major hinderance to the implementation of the precursors in a production environment. If the precursor has a sufficient vapor pressure, then sublimation of the precursor for transportation of its vapor is the only option available, however this is difficult to control in a manufacturing environment. Solid precursors have been dissolved, transported, and delivered in organic solution, but these solutions usually leave a large carbon residue.
  • OBJECTS OF THE INVENTION
  • It is an object of the invention to provide reliable production worthy methods for fast delivery of nonvolatile precursors to the chemical vapor deposition (CVD) chamber. [0003]
  • The invention features dissolving a nonvolatile precursor, either solid or liquid, in a solution and delivering the precursor in the solution to a CVD chamber. [0004]
  • The invention is a very efficient method for transporting a nonvolatile precursor for CVD in the manufacturing environment and incorporates a minimum amount of unwanted by-product in the desired film. The method entails a process which is easily controlled and therefore predictable with repeatable results. [0005]
  • SUMMARY OF THE INVENTION
  • The invention is a method directed to the use of a nonvolatile precursor, either solid or liquid, in a chemical vapor deposition (CVD) process. A solid precursor, as referenced herein, is a precursor which is in a solid state at a temperature at or below 1500 Kelvin and at a pressure at or above 10[0006] −10 Torr, and a liquid precursor, as referenced herein, is a precursor which is in a liquid state at a temperature at or below 1500 Kelvin and at a pressure at or above 10−10 Torr. Using the method of the invention the nonvolatile precursor is dissolved in a solvent to form a solution. The nonvolatile precursor is then transported in the solution at a pressure and a temperature necessary to maintain it as a liquid to the CVD chamber. The solution is transported in a continuous liquid stream to the CVD chamber. A continuous liquid stream is an unbroken non-nebulized stream of liquid which may be passed to the chamber without interruption or may be passed to the chamber in a pulse or batch. The pulse or batch can be thought of as a portion of the solution.
  • In a first embodiment the solution becomes a gas during rapid evaporation of the solution at a high temperature and at a low pressure. The gaseous form of the precursor reacts with a reactant at the heated surface of the wafer. [0007]
  • In a second embodiment the method of the invention can be used in liquid source chemical vapor deposition where the solution is applied to the wafer before being evaporated. [0008]
  • BRIEF DESCRIPTION OF THE DRAWING
  • FIG. 1 is a cross section of a simplified representation of the equipment used to perform a chemical vapor deposition on a semiconductor wafer. [0009]
  • DETAILED DESCRIPTION OF THE INVENTION
  • The invention is a method directed to the use of a nonvolatile precursor suitable for chemical vapor deposition (CVD). The nonvolatile precursor may be a solid or a liquid. The solid precursor, as referenced herein, is a precursor which is in a solid state at a temperature at or below 1500 Kelvin and at a pressure at or above 10[0010] −10 Torr, and the liquid precursor, as referenced herein, is in a liquid state at a temperature at or below 1500 degrees Kelvin and at a pressure at or above 10−10 Torr. The method can be understood by studying FIG. 1 in conjunction with the following description. Using the method of the invention, the nonvolatile precursor is dissolved in a solvent to form a solution 1 of the precursor and the solvent. It is important that the precursor and the solvent do not react with each other in liquid form. The solvent can be either a reactive component which makes up a part of the film or it can be simply a nonreactive inert carrier.
  • The [0011] solution 1 is formed in a chamber 2. The solution 1 is then transported in liquid form at elevated pressures and/or reduced temperatures to a chamber 3 through a transport device 4. The liquid is transported as a continuous liquid stream to the chamber 3. A continuous liquid stream is an unbroken non-nebulized stream of liquid which may be passed to the chamber without interruption or may be passed to the chamber in a pulse or batch. The pulse or batch can be thought of as a portion of the solution. When the solution 1 reaches the chamber 3, at least two options are available.
  • In a first embodiment the [0012] solution 1 becomes a gas upon entry to the chamber 3. The chamber 3 is held at a high enough temperature and a low enough pressure to effect rapid evaporation of the solution 1. The precursor remains in the gas phase until it reacts with a reactant at a heated surface of the wafer 5. The reactant may be either the solvent in its gaseous state or may be another gas injected into the chamber 3. In either case a material is produced during the reaction and deposited as a film on the wafer 5. Typically, a gaseous by-product is also produced in the reaction.
  • One example of the first embodiment comprises a solid precursor of bis(cyclopentadienly)titanium diazide (Tiaz) dissolved in liquid ammonia (LNH[0013] 3) to form a solution 1 of Tiaz in LNH3 in chamber 2 when the temperature of chamber 2 is 20° C. or less and the pressure is 120 psi or greater. The Tiaz in LNH3 is then transported to the chamber 3 through the transport device 4. The temperature and pressure of the transport device 4 are regulated in order to keep the solution in it liquid form. In this example the temperature is 20° or less and the pressure is 120 psi or greater. The solution 1 immediately vaporizes upon entry into chamber 3. The rapid evaporation occurs because the chamber 3 is held at a temperature of 100° C. and a pressure of 500 millitorr and the water surface is held at 550° C. Hydrogen is injected into the chamber and combines with the vaporized Tiaz to form titanium nitride which is deposited on the wafer as a thin film. A by-product cyclopentadiene remains and is pumped from the chamber with the ammonia vapor.
  • The temperatures and pressures may be varied as long as the temperature and pressure of the chamber and transport device allow the precursor to remain dissolved in the solution. In addition the temperature and pressure of the chamber may vary as long as the solution is vaporized. [0014]
  • In a second embodiment, the [0015] solution 1 is applied to the wafer 5 before being evaporated. This is typically referred to as liquid source chemical vapor deposition. The solution is delivered through a nebulizer which delivers a very fine mist that settles evenly over the entire wafer. When the solution first contacts the wafer the temperature of the wafer 5 may be either higher, or lower, or the same as the temperature of the solution 1. In the first case the wafer temperature and chamber 3 pressure must be maintained so that the solvent evaporates upon contact with the wafer surface and so that the precursor reacts immediately with the reactant gas, which is either injected into the chamber or formed during evaporation of the solution, to deposit a film. In the latter two cases, the solution remains on the wafer until the wafer temperature is increased to evaporate the solvent. As in the case of the first embodiment the gaseous state of the precursor reacts with a gas reactant thereby producing a material deposited as a film on the wafer surface. The reaction typically produces a gaseous by-product in addition to the deposited film. The by-product and the solvent vapor, in the case where the vapor doesn't react with the precursor to form the film, are then removed from the chamber 3.
  • An example of the process of the second embodiment comprises a precursor, zirconium tetrachloride, dissolved in a solvent, silicon tetrachloride, to form a solution in [0016] chamber 2 when the temperature of the chamber 2 is between 60° and 10° C. and the pressure is 60 psi or greater. The solution is then transported to the chamber 3 through the transport device 4. The temperature and pressure of the transport device 4 are regulated in order to maintain the solution in its liquid form. In this example the temperature and pressure of the transport device 4 are the same as the temperature and pressure of chamber 2. Chamber 3 is held at a pressure of 10 torr in order to help facilitate the vaporization of the solution on the wafer. The wafer temperature is 600° C. The zirconium tetrachloride in silicon tetrachloride solution is injected into the chamber 3 and reacts at the wafer surface to form a vapor and combines with hydrogen to form zirconium silicide which is deposited on the wafer to form a thin film. A by-product, hydrogen chloride, is formed and is pumped from the chamber with the excess silicon tetrachloride.
  • It is important to use the correct solvent when performing the method of the invention. The solvent must be able to evaporate quickly and leave no contaminates in the product film. Therefore common hydrocarbon solvents are unacceptable because they leave carbon residue incorporated in the wafer film, dependent on the wafer. Ideal solvents for this application are inorganic liquids such as: liquid ammonia (NH[0017] 3), liquid NO2, liquid SO2, liquid TiCl4, liquid TaCl5, liquid WF6, liquid SiCl4, borazine, dimethyl hydrazine, liquid xenonflourides, liquid phosphine, liquid arsine, diethylzinc, BCl3, BF3, SF6, H2S, SiF4, CBrF3, CCl2F2, CCl3F, CClF3, CCl4, SiH2Cl2. Many of these solvents are gases at room temperature but are easily maintained as liquids with elevated pressure and reduced temperature. For example, ammonia boils at −33° C. and is an excellent solvent. It is a further advantage that these gases are easily available at a low cost at the present time.
  • The following gases may be selected as reactant gases for forming the deposited film: hydrogen, ammonia, or silane. [0018]
  • The following are some of the solid precursors suitable for forming films on semiconductor wafers by the method of the invention: bis(cyclopentadienyl) titanium dichloride, ZrCl4, and tungsten carbonyl. [0019]
  • The following are some of the nonvolatile liquid precursors suitable for forming films on semiconductor wafers by the method of the invention: indenyltris(dimethylamido)zirconium, cyclopentadienyltris(diethylamido)titanium, and bis(cyclopentadienyl)bis(dimethylamido)titanium. [0020]
  • There are various combinations of nonvolatile precursors, solvents and reactants that may be used in the process of the invention. [0021]
  • It has been shown that the invention provides an efficient method for transporting nonvolatile precursors for CVD in the manufacturing environment. [0022]
  • Although the invention has been described in terms of a depositing materials on semiconductor wafers during chemical vapor depositions, the circuit and method have utility in other processes where a chemical vapor deposition is desired. Accordingly the invention should be read as limited only by the claims. [0023]

Claims (18)

What is claimed is:
1. A method for performing a chemical vapor deposition of a film on a surface of a wafer, comprising the following steps:
a) solubilizing a nonvolatile precursor in an inorganic solvent to form a liquid solution;
b) transporting said liquid solution as a continuous liquid stream to a control chamber, said transporting performed at a temperature and a pressure to ensure a state of said nonvolatile precursor remains liquid;
c) evaporating said liquid solution in said control chamber to change said state of said nonvolatile precursor to a vapor;
d) creating a reaction between said vapor of said nonvolatile precursor and a reactant vapor; and
e) depositing the film on the surface of the wafer in response to said reaction.
2. The method as specified in
claim 1
, further comprising the step of eliminating contaminates during the depositing of the film by selecting said inorganic solvent and said nonvolatile precursor to ensure non-reaction of said inorganic solvent and said nonvolatile precursor in said solution.
3. The method as specified in
claim 1
, further comprising the following steps:
a) creating a by-product during said step of depositing; and
b) removing said by-product from said chamber.
4. The method as specified in
claim 1
, further comprising the following steps:
a) injecting said liquid solution into said control chamber; and
b) controlling the temperature and pressure of said control chamber such that the temperature is high enough and the pressure is low enough to rapidly effect said step of evaporating said liquid solution when said liquid solution enters said control chamber.
5. The method as specified in
claim 4
, further comprising the step of heating said wafer to a temperature greater than said vapor of said nonvolatile precursor thereby precipitating said step of depositing.
6. The method as specified in
claim 1
, wherein said step of evaporating comprises the steps of:
a) heating said wafer to a temperature capable of evaporating said liquid solution;
b) applying said liquid solution to the surface of the wafer; and
c) increasing a temperature of said liquid solution to said temperature capable of evaporating said liquid solution in response to said step of applying and said step of heating thereby effecting said step of evaporating.
7. The method as specified in
claim 6
, further comprising the following steps:
a) nebulizing said liquid solution at said control chamber in order to create a mist of said liquid solution prior to said step of applying; and
b) uniformly covering the surface of the wafer with said mist during said step of applying.
8. The method as specified in
claim 6
, further comprising the following steps:
a) heating the wafer to a temperature greater than a temperature of said liquid solution prior to said step of applying; and
b) controlling a temperature and a pressure of said control chamber in order to effect said step of evaporating.
9. The method as specified in
claim 1
, further comprising the step of creating said reactant vapor during said step of evaporating.
10. The method as specified in
claim 1
, further comprising the step of injecting said reactant vapor into said control chamber.
11. The method as specified in
claim 1
, wherein said nonvolatile precursor is a nonvolatile solid at a temperature at or above 1500 degrees Kelvin and at a pressure at or below 10−10 Torr.
12. The method as specified in
claim 11
, wherein said nonvolatile solid is selected from the group consisting of Tiaz, ZrCl4, and biscyclopentadienyltitanium diclhoride.
13. The method as specified in
claim 1
, wherein said nonvolatile precursor is a nonvolatile liquid at a normal temperature and pressure.
14. The method as specified in
claim 13
, wherein said nonvolatile liquid is selected from the group consisting of indenyltris(dimethylamido)zirconium, cyclopentadienyltris(diethylamido)titanium, and bis(cyclopentadienyl)bis(dimethylamido)titanium.
15. The method as specified in
claim 1
, wherein said inorganic solvent is selected from the group consisting of liquid ammonia (NH3), liquid NO2, liquid SO2, liquid TiCl4, liquid TaCl5, liquid WF6, liquid SiCl4, borazine, hydrazine, liquid xenonfluorides, liquid phosphine, liquid arsine, diethylzinc, BCl3, BF3, SF6, H2S, SiF4, CBrF3, CCl2F2, CCl3F, CClF3, CCl4, SiH2Cl2.
16. The method as specified in
claim 1
, wherein said reactant vapor is selected from the group consisting of hydrogen, ammonia, and silane.
17. The method as specified in
claim 1
, wherein said step of transporting further comprises transporting said liquid solution in pulses.
18. A method for depositing a film on a surface, comprising the following steps:
a) combining a nonvolatile precursor and an inorganic solvent to form a solution;
b) adjusting a temperature and a pressure in order to maintain said solution in a liquid state;
c) transporting said solution as a liquid stream to a chamber;
d) vaporizing the solution at said chamber to form a precursor vapor;
e) creating a reaction with a reactant vapor and said precursor vapor; and
f) depositing the film on the surface in response to said step of creating.
US09/097,489 1993-05-14 1998-06-15 Chemical vapor deposition apparatus with liquid feed Expired - Fee Related US6428623B2 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
US09/097,489 US6428623B2 (en) 1993-05-14 1998-06-15 Chemical vapor deposition apparatus with liquid feed
US10/213,030 US7182979B2 (en) 1993-05-14 2002-08-05 High efficiency method for performing a chemical vapordeposition utilizing a nonvolatile precursor

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
US6220393A 1993-05-14 1993-05-14
US08/236,946 US5393564A (en) 1993-05-14 1994-05-02 High efficiency method for performing a chemical vapor deposition utilizing a nonvolatile precursor
US39594295A 1995-02-28 1995-02-28
US90969597A 1997-08-12 1997-08-12
US09/097,489 US6428623B2 (en) 1993-05-14 1998-06-15 Chemical vapor deposition apparatus with liquid feed

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
US90969597A Continuation 1993-05-14 1997-08-12

Related Child Applications (1)

Application Number Title Priority Date Filing Date
US10/213,030 Division US7182979B2 (en) 1993-05-14 2002-08-05 High efficiency method for performing a chemical vapordeposition utilizing a nonvolatile precursor

Publications (2)

Publication Number Publication Date
US20010001949A1 true US20010001949A1 (en) 2001-05-31
US6428623B2 US6428623B2 (en) 2002-08-06

Family

ID=27490264

Family Applications (2)

Application Number Title Priority Date Filing Date
US09/097,489 Expired - Fee Related US6428623B2 (en) 1993-05-14 1998-06-15 Chemical vapor deposition apparatus with liquid feed
US10/213,030 Expired - Fee Related US7182979B2 (en) 1993-05-14 2002-08-05 High efficiency method for performing a chemical vapordeposition utilizing a nonvolatile precursor

Family Applications After (1)

Application Number Title Priority Date Filing Date
US10/213,030 Expired - Fee Related US7182979B2 (en) 1993-05-14 2002-08-05 High efficiency method for performing a chemical vapordeposition utilizing a nonvolatile precursor

Country Status (1)

Country Link
US (2) US6428623B2 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20070199509A1 (en) * 2003-09-05 2007-08-30 Moffatt William A Apparatus for the efficient coating of substrates
US20080102205A1 (en) * 2006-10-27 2008-05-01 Barry Sean T ALD of metal-containing films using cyclopentadienyl compounds
US20090311879A1 (en) * 2006-06-02 2009-12-17 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Method of forming high-k dielectric films based on novel titanium, zirconium, and hafnium precursors and their use for semiconductor manufacturing
US9499571B2 (en) 2014-12-23 2016-11-22 L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude Germanium- and zirconium-containing compositions for vapor deposition of zirconium-containing films
US9663547B2 (en) 2014-12-23 2017-05-30 L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude Silicon- and Zirconium-containing compositions for vapor deposition of Zirconium-containing films
US10106568B2 (en) 2016-10-28 2018-10-23 L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude Hafnium-containing film forming compositions for vapor deposition of hafnium-containing films

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3065041B2 (en) * 1998-10-29 2000-07-12 アプライド マテリアルズ インコーポレイテッド Semiconductor device film forming method and film forming apparatus
US7253084B2 (en) * 2004-09-03 2007-08-07 Asm America, Inc. Deposition from liquid sources
US8197898B2 (en) * 2005-03-29 2012-06-12 Tokyo Electron Limited Method and system for depositing a layer from light-induced vaporization of a solid precursor
US7345184B2 (en) * 2005-03-31 2008-03-18 Tokyo Electron Limited Method and system for refurbishing a metal carbonyl precursor
US7485338B2 (en) * 2005-03-31 2009-02-03 Tokyo Electron Limited Method for precursor delivery
US20060222777A1 (en) * 2005-04-05 2006-10-05 General Electric Company Method for applying a plasma sprayed coating using liquid injection
US7459395B2 (en) * 2005-09-28 2008-12-02 Tokyo Electron Limited Method for purifying a metal carbonyl precursor
US7297719B2 (en) * 2006-03-29 2007-11-20 Tokyo Electron Limited Method and integrated system for purifying and delivering a metal carbonyl precursor
US8012876B2 (en) * 2008-12-02 2011-09-06 Asm International N.V. Delivery of vapor precursor from solid source
EP4215649A1 (en) 2022-01-24 2023-07-26 Ivan Timokhin Preparation of shaped crystalline layers by use of the inner shape/surface of the ampule as a shape forming surface

Family Cites Families (36)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3008447A (en) * 1958-11-15 1961-11-14 Electronique & Automatisme Sa Apparatus for the production of electrically conductive film layers of controlled resistivity
US4176209A (en) 1978-01-09 1979-11-27 Raytheon Corporation Process for forming polymeric paraxylylene coatings and films possessing improved oxidation resistance
US4349498A (en) * 1981-01-16 1982-09-14 Carbomedics, Inc. Radio-opaque markers for pyrolytic carbon prosthetic members
US4670350A (en) * 1984-05-30 1987-06-02 Ppg Industries, Inc. Cyanoethylacrylate/acrylic acid copolymer
US4553677A (en) 1984-06-08 1985-11-19 Aseptic Technologies, Inc. Dilution bottle
JPS6169962A (en) * 1984-09-13 1986-04-10 Agency Of Ind Science & Technol Device for forming fogged thin film
US4571350A (en) * 1984-09-24 1986-02-18 Corning Glass Works Method for depositing thin, transparent metal oxide films
US4906493A (en) 1985-04-26 1990-03-06 Sri International Method of preparing coatings of metal carbides and the like
US4689247A (en) 1986-05-15 1987-08-25 Ametek, Inc. Process and apparatus for forming thin films
EP0252755A1 (en) 1986-07-11 1988-01-13 Unvala Limited Chemical vapour deposition
US4746501A (en) * 1986-12-09 1988-05-24 United States Department Of Energy Process for preparing transition metal nitrides and transition metal carbonitrides and their reaction intermediates
JPH0280303A (en) * 1987-06-04 1990-03-20 Tonen Corp Process and apparatus for forming thin superconducting film
US5688565A (en) 1988-12-27 1997-11-18 Symetrix Corporation Misted deposition method of fabricating layered superlattice materials
US5090985A (en) * 1989-10-17 1992-02-25 Libbey-Owens-Ford Co. Method for preparing vaporized reactants for chemical vapor deposition
US4970093A (en) * 1990-04-12 1990-11-13 University Of Colorado Foundation Chemical deposition methods using supercritical fluid solutions
US5278138A (en) 1990-04-16 1994-01-11 Ott Kevin C Aerosol chemical vapor deposition of metal oxide films
US5120703A (en) 1990-04-17 1992-06-09 Alfred University Process for preparing oxide superconducting films by radio-frequency generated aerosol-plasma deposition in atmosphere
US5362328A (en) * 1990-07-06 1994-11-08 Advanced Technology Materials, Inc. Apparatus and method for delivering reagents in vapor form to a CVD reactor, incorporating a cleaning subsystem
US5171734A (en) * 1991-04-22 1992-12-15 Sri International Coating a substrate in a fluidized bed maintained at a temperature below the vaporization temperature of the resulting coating composition
US5381755A (en) 1991-08-20 1995-01-17 The United States Of America As Represented By The Secretary Of The Navy Method of synthesizing high quality, doped diamond and diamonds and devices obtained therefrom
JP3222518B2 (en) * 1991-12-26 2001-10-29 キヤノン株式会社 Liquid source vaporizer and thin film forming device
JPH05311445A (en) 1992-05-12 1993-11-22 Kawasaki Steel Corp Production of tin film
US5271957A (en) 1992-06-18 1993-12-21 Eastman Kodak Company Chemical vapor deposition of niobium and tantalum oxide films
US5258204A (en) 1992-06-18 1993-11-02 Eastman Kodak Company Chemical vapor deposition of metal oxide films from reaction product precursors
US5270248A (en) * 1992-08-07 1993-12-14 Mobil Solar Energy Corporation Method for forming diffusion junctions in solar cell substrates
JP2870719B2 (en) * 1993-01-29 1999-03-17 東京エレクトロン株式会社 Processing equipment
US5344792A (en) 1993-03-04 1994-09-06 Micron Technology, Inc. Pulsed plasma enhanced CVD of metal silicide conductive films such as TiSi2
US5393564A (en) 1993-05-14 1995-02-28 Micron Semiconductor, Inc. High efficiency method for performing a chemical vapor deposition utilizing a nonvolatile precursor
FR2707671B1 (en) 1993-07-12 1995-09-15 Centre Nat Rech Scient Method and device for introducing precursors into a chemical vapor deposition chamber.
CA2107692A1 (en) * 1993-10-05 1995-04-06 Philip Sylvester Esmond Farrell Anti-g suit with pressure regulator
US5451260A (en) * 1994-04-15 1995-09-19 Cornell Research Foundation, Inc. Method and apparatus for CVD using liquid delivery system with an ultrasonic nozzle
US5478610A (en) * 1994-09-02 1995-12-26 Ceram Incorporated Metalorganic chemical vapor deposition of layered structure oxides
US5968594A (en) * 1996-06-28 1999-10-19 Lam Research Corporation Direct liquid injection of liquid ammonia solutions in chemical vapor deposition
US5916640A (en) 1996-09-06 1999-06-29 Msp Corporation Method and apparatus for controlled particle deposition on surfaces
US5924012A (en) 1996-10-02 1999-07-13 Micron Technology, Inc. Methods, complexes, and system for forming metal-containing films
US6010969A (en) 1996-10-02 2000-01-04 Micron Technology, Inc. Method of depositing films on semiconductor devices by using carboxylate complexes

Cited By (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20070199509A1 (en) * 2003-09-05 2007-08-30 Moffatt William A Apparatus for the efficient coating of substrates
US9583335B2 (en) 2006-06-02 2017-02-28 L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude Method of forming dielectric films, new precursors and their use in semiconductor manufacturing
US10217629B2 (en) 2006-06-02 2019-02-26 L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude Method of forming dielectric films, new precursors and their use in semiconductor manufacturing
US20110207337A1 (en) * 2006-06-02 2011-08-25 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Geroges Claude Method of forming dielectric films, new precursors and their use in semiconductor manufacturing
US8399056B2 (en) 2006-06-02 2013-03-19 L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude Method of forming high-k dielectric films based on novel titanium, zirconium, and hafnium precursors and their use for semiconductor manufacturing
US8470402B2 (en) 2006-06-02 2013-06-25 L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude Method of depositing a metal-containing dielectric film
US8668957B2 (en) 2006-06-02 2014-03-11 L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude Method of forming dielectric films, new precursors and their use in semiconductor manufacturing
US9911590B2 (en) 2006-06-02 2018-03-06 L'Air Liquide Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude Methods of forming dielectric films, new precursors and their use in semiconductor manufacturing
US20090311879A1 (en) * 2006-06-02 2009-12-17 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Method of forming high-k dielectric films based on novel titanium, zirconium, and hafnium precursors and their use for semiconductor manufacturing
US11155919B2 (en) 2006-10-27 2021-10-26 Asm Ip Holding B.V. ALD of metal-containing films using cyclopentadienyl compounds
US9273391B2 (en) 2006-10-27 2016-03-01 Asm Ip Holding B.V. ALD of zirconium-containing films using cyclopentadienyl compounds
US9670582B2 (en) 2006-10-27 2017-06-06 Asm Ip Holding B.V. ALD of metal-containing films using cyclopentadienyl compounds
US9677175B2 (en) 2006-10-27 2017-06-13 ASM IP Holding, B.V. ALD of metal-containing films using cyclopentadienyl compounds
US9850575B1 (en) 2006-10-27 2017-12-26 Asm Ip Holding B.V. ALD of metal-containing films using cyclopentadienly compounds
US8795771B2 (en) * 2006-10-27 2014-08-05 Sean T. Barry ALD of metal-containing films using cyclopentadienyl compounds
US20080102205A1 (en) * 2006-10-27 2008-05-01 Barry Sean T ALD of metal-containing films using cyclopentadienyl compounds
US10294563B2 (en) 2006-10-27 2019-05-21 Asm Ip Holding B.V. ALD of hafnium-containing films using cyclopentadienyl compounds
US9663547B2 (en) 2014-12-23 2017-05-30 L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude Silicon- and Zirconium-containing compositions for vapor deposition of Zirconium-containing films
US9868753B2 (en) 2014-12-23 2018-01-16 L'Air Liquide, Société Anonyme our l'Etude et l'Exploitation des Procédés Georges Claude Germanium- and zirconium-containing composition for vapor deposition of zirconium-containing films
US9499571B2 (en) 2014-12-23 2016-11-22 L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude Germanium- and zirconium-containing compositions for vapor deposition of zirconium-containing films
US10106568B2 (en) 2016-10-28 2018-10-23 L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude Hafnium-containing film forming compositions for vapor deposition of hafnium-containing films

Also Published As

Publication number Publication date
US7182979B2 (en) 2007-02-27
US6428623B2 (en) 2002-08-06
US20020192376A1 (en) 2002-12-19

Similar Documents

Publication Publication Date Title
US5393564A (en) High efficiency method for performing a chemical vapor deposition utilizing a nonvolatile precursor
US6428623B2 (en) Chemical vapor deposition apparatus with liquid feed
USRE35785E (en) Low-pressure chemical vapor deposition process for depositing high-density highly-conformal, titanium nitride films of low bulk resistivity
US6008143A (en) Metal organic chemical vapor deposition apparatus and deposition method
US5376409A (en) Process and apparatus for the use of solid precursor sources in liquid form for vapor deposition of materials
US6432205B1 (en) Gas feeding system for chemical vapor deposition reactor and method of controlling the same
US6800542B2 (en) Method for fabricating ruthenium thin layer
US5399379A (en) Low-pressure chemical vapor deposition process for depositing high-density, highly-conformal titanium nitride films of low bulk resistivity
US6797337B2 (en) Method for delivering precursors
JP2019510877A (en) Deposition of molybdenum thin films using molybdenum carbonyl precursors
US20100227476A1 (en) Atomic layer deposition processes
EP0174743A2 (en) Process for transition metal nitrides thin film deposition
US6531192B2 (en) Chemical vapor deposition process for depositing titanium nitride films from an organo-metallic compound
US5741547A (en) Method for depositing a film of titanium nitride
KR20110041498A (en) Method of forming a tantalum-containing layer on a substrate
KR100326744B1 (en) Chemical Vapor Deposition Utilizing a Precursor
KR100300038B1 (en) Metal organic chenical vapour deposition method and apparatus therefor
WO2006009872A1 (en) Direct injection chemical vapor deposition method
KR100428877B1 (en) Method of manufacturing insulating layer of semiconductor device using en solution
CN114341396A (en) Method for forming metal nitride film
KR19980071092A (en) Method for manufacturing layer on surface
KR20030011403A (en) Method of manufacturing film on substrate by using tantalum source solution
KR20020052465A (en) Method for chemical vapor deposition
JPH11186244A (en) Method of forming film and manufacturing semiconductor device
JPH08218169A (en) Formation of tin film

Legal Events

Date Code Title Description
FPAY Fee payment

Year of fee payment: 4

FPAY Fee payment

Year of fee payment: 8

REMI Maintenance fee reminder mailed
LAPS Lapse for failure to pay maintenance fees
STCH Information on status: patent discontinuation

Free format text: PATENT EXPIRED DUE TO NONPAYMENT OF MAINTENANCE FEES UNDER 37 CFR 1.362

FP Lapsed due to failure to pay maintenance fee

Effective date: 20140806