1. Chemical Vapor Deposition This presentation is partially animated. Only use the control panel at the bottom of screen to review what you have seen. When using your mouse, make sure you click only when it is within the light blue frame that surrounds each slide.

2. Introduction to Chemical Vapor Deposition A) Chemical Vapor Deposition CVD Types CVD Uses CVD Process General CVD Reactor Concept General CVD Process Advantages General CVD Process Applications B) Dealing with Engineering Science of CVD Reactions Transport Processes Laminar Flow Boundary Layer Concept Other Susceptor to Flow Axis Options Thermodynamics Reaction Kinetics C) Operational Overview Polycrystaline Silicon Silicon Dioxide Nitride Films

3. LPCVD APCVD PECVD Chemical Vapor Deposition Current Options Atmospheric Pressure CVD Plasma Enhanced CVD Low Pressure CVD

4. CVD Silicon Nitride Silicon dioxidePolycrystalline Silicon Epitaxial Layers Customized Surfaces InsulatorConductors Barriers Chemical Vapor Deposition CVD Applications

5. Arrival Flow Rate Substrate Input Flow Rate r = Growth Rate of Film g r g Surface Reaction Rate Growth Rate Film Chemical Vapor Deposition CVD Process Surface Reaction

6. CVD Reactor Concept Reaction Chamber Susceptor Controlled Thermal Environment Controlled Pressure Environment

7. General CVD Process Advantages Excellent Step Coverage Large Throughput (100 A/min film growth) Low Temperature Processing (450 to 1000 C) Applicable to any Vaporization Source Technology (Laser CVD for direct Writing) General CVD Process Applications Epitaxial Films Enhance performance of Discreet and Integrated Bipolar Devices Allow Fabrication of RAM’s and CMOS in Bulk Substrate Dielectrics Insulation between Conducting Layers Diffusion and Ion Implant Masks Capping Dopant Films Extracting Impurities Passivation to Protect Structures from Impurities Moisture Scratches Polysilicon Conductors Gate Electrodes Conductors for Multilevel Metalizations Contacts for Shallow Junction Devices

8. B) Dealing with Engineering Science of CVD Reactions Transport Processes Thermodynamics Reaction Kinetics Transport Processes Turbulent FlowNo, to Many Particles. Molecular FlowNo, to Low a Throughput Laminar Flow ( Only One Left, Make Do) Set Conditions For Laminar Flow ( Low Reynolds Number Value)

9. R = D V ( ) Reynolds Number Linear Velocity Tube Diameter # D µ Gas Density Gas Viscosity

10. Laminar Flow Conditions Diameter and velocity in tens of cm and cm/s will give Reynolds numbers in laminar flow regime R = 1.76 x 10 5 Growth ( D /R) (1/ T ) 1.67 ( T/ y ) (Z) P) Boundary Layer Thickness Reagent Partial Pressure $ Reagent’s Gas Phase Coefficient of Thermal Diffusion $ ' " % 0.33

11. Susceptor Input Reactant Gas Flow Boundary layer develops along susceptor flow axis X 1 X 2 X 3 X 4 Graphic Exaggerated for Visual Effect Distance Above Susceptor

12. Trends in Gradients Velocity Values Increase Along Susceptor Increase Above Susceptor Temperature Values Increase Along Susceptor Decrease Above Susceptor Reactant Concentration Value Decrease Along Susceptor Increase Above Susceptor

13. Other Susceptor to Flow Axis Options Design Factors Include Flow Direction and Wafer Angle A) Input gas flow B) Input gas flow C) Input gas flow D) Input gas flow E) Input gas flow

14. Thermodynamics CVD Phase Diagram Give range of input conditions for CVD that could produce specific condensed phases. Presented as Function of Temperature or Pressure vs Mole Fraction. Boron codeposit only in High Boron Mole Fractions in input stream Boron codeposition favored at higher pressures. 1200 o C 1000 o C 1400 o C Reactant Gas Mole Fraction B/(Ti + B) 0.01 Atm 1.0 Atm 0.6 TiB 2 Phase H/HCl = 0.95 Use Graphic for Educational Value Only 7 th Conference on CVD 1979 K.E. Spear Electrochemical Society Vol 79 TiB 2 & B Phase

15. BCl 3 /CH 4 = 4 Use Graphic for Educational Value Only J. Electrochem. Soc.123,136, 1976 Bernard Ducarroir 10 -4 10 -3 10 -2 10 10 -0 10 -4 10 -3 10 -2 10 Partial Pressure for Methane B 4 C + C B 4 C B 4 C + B B Carbon Vapor 1600 0 C 1.0 Atm Boron-Carbon CVD Phase Diagrams

16. Vanadium-Silicon-Hydrogen-Chloride CVD Phase Diagrams

18. Reaction Kinetics Use Graphic for Educational Value Only 124, 790 (1979) Besmann,J. Electrochem. Soc. 1/T (x 10 / K) 5.0 6.0 7.0 8.09.0 1.0 10.0 Titanium Diboron Deposition Arrhenius Plot P = 0.263 Atm. Input flow Rate = 462 cc /min B/(B + Ti) = 0.66 Cl/(Cl + H) = 0.33 Input Gases TiCl 4 BCl 3 H 2 Reaction Temperatures (2000K to 1000K)

19. Use Graphic for Educational Value Only Arrhenius Rate Profiles

20. Use Graphic for Educational Value Only Partial Pressure Reactant Gas 1.0 10.0 Arrhenius Isotherms (a) (f) Surface Reaction Limiting Growth Rate

21. ln(r g2 /r g1 ) ' (q + act /k)(T 2 & T 1 /T 2 T 1 )

22. C) OperationalOverviews Polycrystalline Silicon (Polysilicon) Four popular ways to alter pressure. Change gas flow rate but keep pumping speed constant. Change pumping speed with constant flow rate Change reacting gas or carrier gas with other held constant Change both gases but keep there ratio constant. Considerations Temperature Pressure (LPCVD) Si H HH H 25 PA to 130 PA 100% Silane 25 PA to 130 PA 20% to 30% Silane At high temperatures get gas phase reactions that produce rough, loosely adhering deposits and poor uniformity. At low temperatures deposition rates are to slow for industrial situations. Zone heating rear of furnace up to 15C hotter. (Better film uniformity) o Si APCVD 575 to 650 Toxic( 1 Atm but 90% N 2 ) Pyrophoric High Exposure Limit C o LPCVD 575 to 650C o

23. Silicon dioxide Low Temperature Loose adhering deposits on side walls of reactor. ( Particles that can contaminate the film. At high silane pressures allows for gas phase reactions. ( Promotes particle contamination and hazy films) Fair step coverage Low film density ( 2. 0 g/cm 3 ) Deposition rate complex function of Oxygen concentration Easy chemical reaction. ( Low activation energy, 0.4 ev (10 kcal/mole) ) Film depends on gas phase transport of material to surface Low temperature allows production of films that will serve as insulation between aluminum levels in device.

24. Si H H H H SiO 2 NO 650 to 750C Si O C C H H H H O O C H H C H H OCH 2 CH 3 2 3 SilaneTetraethoxysilane TEOS SiO 2 650 to 750C (LPCVD) 30 PA to 250 PA 100 to 1000 std. cc / min Medium Temperature

25. High Temperature Nonlinear pressure dependence that is function of wafer position. Small amounts of Chlorine in films that tends to cause cracking in a poly layer) Reagent depletion problems Phosphorus doping is difficult. ( The phosphorus oxides are volatile at high deposition temperatures.) Excellent Uniformity

26. Except for epi and parallel plate processes both sides of wafer are coated. Equipment Furnace with or without vacuum capability Plasma Chamber CVD is Crucial to Fabrication of IC's, Especially MOSFETS (The Bottom Line) Pad Silicon Dioxide First Monolayer of Silicon Nitride Si Cl N H H Precursor NHSiCl H H H H N H H H Si Cl H H Si Cl H H