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Thermodynamics in Chip Processing II Terry A. Ring
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CVD
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Materials Deposited Dielectrics –SiO2, BSG Metals –W, Cu, Al Semiconductors –Poly silicon (doped) Barrier Layers –Nitrides (TaN, TiN), Silicides (WSi 2, TaSi 2, CoSi, MoSi 2 )
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Deposition Methods Growth of an oxidation layer Spin on Layer Chemical Vapor Deposition (CVD) –Heat = decomposition T of gasses –Plasma enhanced CVD (lower T process) Physical Deposition –Vapor Deposition –Sputtering
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Critical Issues Adherence of the layer Chemical Compatibility –Electro Migration –Inter diffusion during subsequent processing Strong function of Processing Even Deposition at all wafer locations
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CVD of Si 3 N 4 - Implantation mask 3 SiH 2 Cl 2 + 4 NH 3 Si 3 N 4 + 6 HCl + 6 H 2 –780C, vacuum –Carrier gas with NH 3 / SiH 2 Cl 2 >>1 Stack of wafer into furnace –Higher temperature at exit to compensate for gas conversion losses Add gases Stop after layer is thick enough
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CVD of Poly Si – Gate conductor SiH 4 Si + 2 H 2 –620C, vacuum –N 2 Carrier gas with SiH 4 and dopant precursor Stack of wafer into furnace –Higher temperature at exit to compensate for gas conversion losses Add gases Stop after layer is thick enough
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CVD of SiO 2 – Dielectric Si0C 2 H 5 +O 2 SiO 2 + 2 H 2 –400C, vacuum –He carrier gas with vaporized(or atomized) Si0C 2 H 5 and O 2 and B(CH 3 ) 3 and/or P(CH 3 ) 3 dopants for BSG and BPSG Stack of wafer into furnace –Higher temperature at exit to compensate for gas conversion losses Add gases Stop after layer is thick enough
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CVD of W – Metal plugs 3H 2 +WF 6 W + 6HF –T>800C, vacuum –He carrier gas with WF 6 –Side Reactions at lower temperatures Oxide etching reactions 2H 2 +2WF 6 +3SiO 2 3SiF 4 + 2WO 2 + 2H 2 O SiO 2 + 4HF 2H 2 O +SiF 4 Stack of wafer into furnace –Higher temperature at exit to compensate for gas conversion losses Add gases Stop after layer is thick enough
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Chemical Equilibrium
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CVD Reactor Wafers in Carriage (Quartz) Gasses enter Pumped out via vacuum system Plug Flow Reactor Vacuum
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CVD Reactor Macroscopic Analysis –Plug flow reactor Microscopic Analysis –Surface Reaction Film Growth Rate
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Macroscopic Analysis Plug Flow Reactor (PFR) –Like a Catalytic PFR Reactor –F Ao = Reactant Molar Flow Rate –X = conversion –r A =Reaction rate = f(C A )=kC A –C i =Concentration of Species, i. –Θ i = Initial molar ratio for species i to reactant, A. –ν i = stoichiometeric coefficient –ε = change in number of moles
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Combined Effects Contours = Concentration
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Reactor Length Effects SiH 2 Cl 2 (g) + 2 N 2 O(g) SiO 2 (s)+ 2 N 2 (g)+2 HCl(g) How to solve? Higher T at exit!
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Deposition Rate over the Radius r C As Thiele Modulus Φ 1 =(2kR w /D AB x) 1/2
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Radial Effects This is bad!!!
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Combined Length and Radial Effects Wafer 20 Wafer 10
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CVD Reactor External Convective Diffusion –Either reactants or products Internal Diffusion in Wafer Stack –Either reactants or products Adsorption Surface Reaction Desorption
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Microscopic Analysis -Reaction Steps Adsorption –A(g)+S A*S –r AD =k AD (P A C v -C A*S /K AD ) Surface Reaction-1 –A*S+S S*S + C*S –r S =k S (C v C A*S - C v C C*S /K S ) Surface Reaction-2 – A*S+B*S S*S+C*S+P(g) –r S =k S (C A*S C B*S - C v C C*S P P /K S ) Desorption: C*S C(g) +S –r D =k D (C C*S -P C C v /K D ) Any can be rate determining! Others in Equilib. Write in terms of gas pressures, total site conc.
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CMP
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What is CMP? Polishing of Layer to Remove a Specific Material, e.g. Metal, dielectric Planarization of IC Surface Topology
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Scratching Cases Rolling Indenter Line Scratches –Copper Only –Copper & ILD Chatter Scratches Uncovery of Pores
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CMP Tooling Rotating Multi-head Wafer Carriage Rotating Pad Wafer Rests on Film of Slurry Velocity= - (Wt Rcc)–[Rh (Wh –Wt)] when Wh=Wt Velocity = const.
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Slurry Aqueous Chemical Mixture –Material to be removed is soluble in liquid –Material to be removed reacts to form an oxide layer which is abraded by abrasive Abrasive –5-20% wgt of ~200±50nm particles Narrow PSD, high purity(<100ppm) Fumed particle = fractal aggregates of spherical primary particles (15-30nm)
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Pad Properties Rodel Suba IV Polyurethane –tough polymer Hardness = 55 –Fiber Pile Specific Gravity = 0.3 Compressibility=16% rms Roughness = 30μm –Conditioned
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Heuristic Understanding of CMP Preston Equation(Preston, F., J. Soc. Glass Technol., 11,247,(1927). –Removal Rate = K p *V*P V = Velocity, P = pressure and K p is the proportionality constant.
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CMP Pad Modeling Pad Mechanical Model - Planar Pad Warnock,J.,J. Electrochemical Soc.138(8)2398-402(1991). Does not account for Pad Microstructure
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CMP Modeling Numerical Model of Flow under Wafer –3D -Runnels, S.R. and Eyman, L.M., J. Electrochemical Soc. 141,1698(1994). –2-D -Sundararajan, S., Thakurta, D.G., Schwendeman, D.W., Muraraka, S.P. and Gill, W.N., J. Electrochemical Soc. 146(2),761-766(1999).
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Copper Dissolution Solution Chemistry –Must Dissolve Surface Slowly without Pitting Supersaturation
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Oxidation of Metal Causes Stress Stress, i = E i (P-B i – 1)/(1 - i ) P-B i is the Pilling-Bedworth ratio for the oxide
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