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mass and energy balance for rotary dryer pdf

S dl Thebalanceequations for the solid phase can be derived from Equation 3.12 and Equation 3.14 of theenergy balanceparallel flow: 1 dWB (ig2 ig1 ) ¼ (q wD hAv )aV (3:69) S dl Y2 In the case of an equilibrium method of calculation of dWB ig2 the drying rate the kinetic equations are: dX wD ¼ kY DYm (3:70) WS X+ __ dl WS X dl im q ¼ aDtm ...

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