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Predicts product temperature at the sublimation interface based on pseudo steady-state heat and mass transfer model
Fill volume Solids concentration Shelf heat transfer coefficient Cross sectional area of the product in the vial Vial area calculated based on outside diameter Dry layer mass transfer resistance parameters: Rphat=R0+A1*l/(1+A2*l), where l is thiskness of dry layer at any time Shelf temperature Chamber pressure OUTPUT: Temperature versus time chart
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