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                                                 CHEMICAL VAPOR DEPOSITION

                   14.4  WAFER PROCESSING

                                 Does it matter if the process is kinetically controlled or mass-transfer limited? Yes. When mass-
                               transfer limited, the surface is starved for at least one of the reactants. That means the sticking coef-
                               ficient for that reactant will be high. As we will see later in the chapter, high sticking coefficients
                               result in poor step coverage. On the other hand, in the kinetic regime, the surface is saturated with
                               reactants. Under these conditions, by-products can become trapped in the film, reducing its purity.
                               In the case of the tungsten reaction, the level of fluorine incorporated into the film is much higher
                               when the process is kinetically controlled.
                               Gas Utilization.  For many CVD processes, reactants are expensive and so we want to use them
                               most efficiently. Unfortunately, the most efficient operating conditions are those that produce the
                               lowest deposition rate, i.e., flow the gases into the chamber very slowly, to allow lots of time for the
                               reactants to diffuse to the wafer.
                                 Mass-transfer limited processes will be more efficient than kinetically controlled ones. The low
                               sticking probabilities of kinetically controlled processes mean that some molecules will hit the
                               wafer, bounce off, and be pumped out. The utilization can be easily calculated if you know the flow
                               and deposition rates.
                               Transport Mechanisms: Diffusion, Convection, Thermal Diffusion, E Fields, Pe Number.
                               Reactants are transported from the inlet to the wafer primarily by convection and diffusion. Several
                               secondary mechanisms may also be present. In convection, the reactants are transported by the gas
                               velocity. In diffusive transport, the reactants migrate from areas of high concentration to low. The
                               rate of convective transport is given by

                                                                j = Y ρu
                                                                   i
                               where Y is the mass fraction of species i, r is the density of the gas, and u is the velocity. The dif-
                                     i
                               fusive flux is given by
                                                               j =− Dρ∇Y
                                                                       i
                               where D is the diffusion coefficient of species i in the mixture. The relative importance of convec-
                               tion and diffusion is determined by the dimensionless Peclet number

                                                                Pe =  ud
                                                                    D
                               where d is the characteristic length of the chamber (typically the distance from showerhead to wafer).
                               If Pe << 1, the transport is primarily by diffusion. If Pe >> 1, it is by convection. For most CVD reac-
                               tors, Pe is between 1 and 10, indicating that convection is somewhat stronger, but both mechanisms
                               are important. This can have implications for process development. For instance, if a process engi-
                               neer changes a carrier gas from helium to argon, as a cost-saving measure, there will likely be the
                               unintended consequence of lowering the deposition rate because of the lower diffusivity of argon.
                               Diffusive transport can also lead to nonuniformities when there are purge flows near the wafer sur-
                               face. The reactants diffuse out of the reaction zone, following the concentration gradient, leading to
                               a thin deposition at the wafer edge.
                                 The Pe number can be used to estimate the gas utilization of a process, at least for the rate-limiting
                               reactant. Figure 14.3 shows the gas utilization versus Pe number for a mass transfer limited reac-
                               tion in a showerhead reactor like Fig. 14.1. In the typical range of 1 to 10, the efficiency is between
                               25 and 68 percent.
                                 Additional transport mechanisms may also be important. In plasma processes, electron and ion
                               transport are governed by the electric fields in the chamber. The chamber surfaces are typically
                               somewhat negative due to higher electron mobilities. This leads to ion bombardment of those sur-
                               faces, including the wafer.
                                 Thermal diffusion is a weak transport phenomenon that only becomes important where there is a
                               large difference in the molecular weights of the gases and large temperature gradients. For instance,


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