3) A granular material containing 40 per cent moisture is fed to a countercurrent rotary dryer at a temperature of 295 K and is withdrawn at 305 K. containing 5 per cent moisture. The air supplied which contains 0 006 kg water vapor/kg dry air, enters at 385 K and leaves at 310 K. The dryer handles 0.125 kg/s wet stock. Assuming that radiation losses amount to 20 kJ/kg dry air used, the latent heat of water vapor at 295 K = 2449 kJ/kg, specific heat capacity of dried material =088 kJ/kg K, the specific heat capacity of dry air 1.00 kJ/kg K, and the specific heat capacity of water vapor 2.01 kJ/kg K Determine the mass flowrate of dry air supplied to the dryer and the humidity of the exit air leaving it.

Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
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3) A granular material containing 40 per
cent moisture is fed to a countercurrent
rotary dryer at a
temperature of 295 K and is withdrawn
at 305 K. containing 5 per cent moisture.
The air
supplied which contains 0 006 kg water
vapor/kg dry air, enters at 385 K and
leaves at 310 K.
The dryer handles 0.125 kg/s wet stock.
Assuming that radiation losses amount
to 20 kJ/kg dry
air used, the latent heat of water vapor
at 295 K = 2449 kJ/kg, specific heat
capacity of dried
material =088 kJ/kg K, the specific heat
capacity of dry air 1.00 kJ/kg K, and the
specific heat
capacity of water vapor 2.01 kJ/kg K
Determine the mass flowrate of dry air
supplied to the dryer and the humidity of
the exit air
leaving it.
Transcribed Image Text:3) A granular material containing 40 per cent moisture is fed to a countercurrent rotary dryer at a temperature of 295 K and is withdrawn at 305 K. containing 5 per cent moisture. The air supplied which contains 0 006 kg water vapor/kg dry air, enters at 385 K and leaves at 310 K. The dryer handles 0.125 kg/s wet stock. Assuming that radiation losses amount to 20 kJ/kg dry air used, the latent heat of water vapor at 295 K = 2449 kJ/kg, specific heat capacity of dried material =088 kJ/kg K, the specific heat capacity of dry air 1.00 kJ/kg K, and the specific heat capacity of water vapor 2.01 kJ/kg K Determine the mass flowrate of dry air supplied to the dryer and the humidity of the exit air leaving it.
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