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2.3.2 Non-Linear Surface Reactions

In general, the surface velocity (2.25) is not a linear function. As an example, the sticking probability in (2.31) can depend on the local arriving particle flux, if higher order surface kinetics are assumed [21]

$\displaystyle {s}({\vec{x}})\sim{F}({\vec{x}})^{{\eta}-1}.$ (2.32)

Here $ {\eta }$ is the order of the reaction. Obviously, in the case of non-linear reaction kinetics ( $ {\eta}\neq1$ ) the sticking coefficient depends on the flux.

Other examples, where non-linear surface reactions need to be incorporated, are processes with ion-enhanced etching. There physical (ions) and chemical (neutrals) components act in a synergistic manner, so that the etch rate is larger than that obtained by summing up their individual contributions.

The Langmuir adsorption model is able to capture this behavior [91]. The idea is to assume an absorbed state of byproducts. The fraction of surface sites covered by these byproducts is called the surface coverage $ {\Theta}={\Theta}({\vec{x}})$ . The etch rate is then composed of three contributions

$\displaystyle {V}({\vec{x}}) = \underbrace{-\alpha_{\text{ch}}\cdot{\Theta}({\v...
...})\cdot{Y}^{\text{tot}}_{\text{ie}}({\vec{x}})}_{\text{ion-enhanced etching}} .$ (2.33)

The first term corresponds to chemical etching which is proportional to the coverage, the second term represents physical sputtering with the total sputter rate $ {Y}^{\text{tot}}_{\text{ph}}({\vec{x}})$ , and the last term is due to ion-enhanced etching, which is proportional to the coverage and the total ion-enhanced etching rate $ {Y}^{\text{tot}}_{\text{ie}}({\vec{x}})$ . The total yields are both calculated using a weight function similar to that used in (2.27). Two different total yields are introduced, since in the general case the physical sputter yield and the ion-enhanced etching yield are not equal. The constants $ \alpha_{\text{ch}}$ , $ \alpha_{\text{ph}}$ , and $ \alpha_{\text{ie}}$ in (2.33) are model parameters.

For the coverage $ {\Theta}({\vec{x}})$ a balanced equation can be set up as follows

$\displaystyle \frac{{d}{\Theta}}{{d}{t}}({\vec{x}}) = \underbrace{\beta_{\text{...
...}})\cdot{Y}^{\text{tot}}_{\text{ie}}({\vec{x}})}_{\text{ion-enhanced etching}}.$ (2.34)

The first term describes the adsorption of chemical components, which is proportional to the total arriving flux $ {F}({\vec{x}})$ of neutrals and the fraction of empty surface sites $ \left(1-{\Theta}({\vec{x}})\right)$ . The second and the third term are losses due to chemical and ion-enhanced etching, respectively, which are both proportional to the coverage. The constants $ \beta_{\text{ad}}$ , $ \beta_{\text{ch}}$ , and $ \beta_{\text{ie}}$ are again model parameters.

A common approach is to assume that the coverage is always in a steady state $ \frac{\partial{\Theta}}{\partial{t}}({\vec{x}})=0$ . Therefore, the coverage can be explicitly expressed as a function of the rates $ {F}({\vec{x}})$ and $ {Y}^{\text{tot}}_{\text{ie}}({\vec{x}})$ ,

$\displaystyle {\Theta}({\vec{x}})= \frac{ \beta_{\text{ad}}{F}({\vec{x}}) }{ \b...
...)+\beta_{\text{ch}}+\beta_{\text{ie}}{Y}^{\text{tot}}_{\text{ie}}({\vec{x}}) },$ (2.35)

and can be plugged into (2.33). The result is a non-linear function of the rates for the surface velocity.


next up previous contents
Next: 2.3.3 Transport-Independent Surface Reactions Up: 2.3 Surface Kinetics Previous: 2.3.1 Linear Surface Reactions

Otmar Ertl: Numerical Methods for Topography Simulation