Abstract
An earlier one-dimensional frictionless perfect-gas analysis of jet ejectors is generalized to account for phase changes during the expansion process and is used to evaluate the performance of vapour-jet compressors operating with initially saturated freon-12 or n-butane. The results, obtained by numerical solution of the non-linear equations, show better agreement with experimental data than the predictions based on perfect-gas relations and indicate that the performance depends upon several variables which are not accounted for by the perfect-gas model.
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