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                                                    CHEMICAL VAPOR DEPOSITION

                                                                               CHEMICAL VAPOR DEPOSITION  14.3

                                  formed, layers of metal lines separated by dielectric are laid down, forming the interconnect struc-
                                  ture. When aluminum is used as the primary conductor, CVD tungsten provides the conductive medi-
                                  um between metal layers. CVD is also used for the dielectric separating metal layers. This could be
                                  CVD SiO , fluorinated SiO , or carbon-doped SiO (the latter two low-k films being used to reduce
                                         2            2                2
                                  the capacitance of the circuit). For copper metalization, the diffusion barrier between copper and
                                  oxide may be deposited by CVD. Once complete, the wafer is given a scratch protection or passiva-
                                  tion layer, typically silicon nitride or oxynitride, deposited by plasma-enhanced CVD.


                      14.2 THEORY

                                  The theoretical study of CVD focuses on two areas—the transport of gases to and from the wafer,
                                  and the chemical reactions that take place both on the wafer and in transit.

                      14.2.1 Mass Transfer

                                  In order to deposit a CVD film, the reactants must be transported from the inlet to the wafer surface.
                                  For many processes, the deposition rate is limited by how fast this takes place. Additionally, film uni-
                                  formity can be strongly dependent on mass-transfer rates.

                                  Mass Transfer Versus Kinetic Control.  Consider a tungsten CVD process in which hydrogen and
                                  tungsten hexafluoride flow into a chamber and react to form tungsten:
                                                             3H + WF → W + 6HF
                                                               2     6
                                    The volatile HF is pumped away. If the wafer were maintained at room temperature, the reaction
                                  would proceed at near zero rate. As the temperature is increased, the deposition rate would increase
                                  exponentially. At sufficiently high temperature, the rate would slow down and level off, as illustrated
                                  in Fig. 14.2. What is going on? At low temperatures, the reactants are being consumed at a very slow
                                  rate, much slower than they are entering the chamber. Thus the deposition rate is completely gov-
                                  erned by the reaction rate on the wafer surface. This reaction rate is very temperature sensitive, and
                                  so increases rapidly with temperature. Under these conditions, the process is said to be kinetically
                                  controlled. That is, the deposition rate is governed by the chemical kinetics or the reaction rate. As
                                  the temperature is increased further, the reaction rate eventually reaches and then exceeds the rate at
                                  which WF or H arrive at the wafer surface. Once that happens, the process is no longer kinetically
                                          6
                                              2
                                  controlled; it is now mass-transfer controlled or mass-transfer limited. At this point, further increas-
                                  es to the temperature cannot increase the deposition rate because there is not enough material to
                                  react. The only way to increase the rate at this point is to turn up the flow.






                                             Mass transfer
                                          Ln (rate)                      Rate                 Kinetic


                                                    Kinetic
                                                                                 Mass transfer

                                                       1/T                        Reactant flow
                                        FIGURE 14.2  Mass transfer versus kinetic control.


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