In order to achieve process control systems in semiconductor manufacturing that are able to maximize yield at minimum cost, an integrated approach that combines advanced control techniques and mathematical modeling with available on-line measurements is necessary. We have utilized a model predictive control approach for multivariate run-to-run control of chemical mechanical planarization (CMP), lithography, and rapid thermal processing reactors. Improvements due to advanced control have been quantified in actual fab operations.
Many steps in the manufacturing ofsemiconductors offer no opportunity for real-time measurement ofthe wafer state, necessitating the use of pre-and post-process measurements of the wafer state in a run-to-run control algorithm. The predominant algorithm in the industry is an extended form of SPC using an EWMA filter' to adjust a model parameter vector using the available measurements. This paper evaluates the merits of using an optimal discrete controller relying on a discrete-time constrained state-space process model that incorporates feedforward action using the pre-process measurement and feedback using the post-process measurement, accounts for the process statistics using a noise model and optimal filtering theory, and ensures integral action in the controller by estimating unmeasured disturbances. Comparisons to the EWMA algorithm are presented using simulations based on actual. plant data from a chemical-mechanical polishing application. The polish process is particularly suitable for the application of such a controller because of the natural method the controller provides for incorporating unmeasured disturbances, like pad and slurry changes, in the control action.
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