A food product, having a dry weight of 30 kg is dried in a tunnel dryer. Drying was from top surface only having an area of 2 m2. The following data were obtained during the drying process:   Drying time (hour) Sample weight (kg) 0 50.0 1 48.5 2 47.0 3 45.5 4 44.0 5 42.8 10 36.9 15 33.8 20 32.9   The air used in the dryer is conditioned by first cooling outside air (20 °C, 40% RH) to 0°C and then heating to 50°C before passing through the dryer. Air flows parallel to the product surface through the dryer having cross sectional dimensions of 150 cm X 100 cm.   Calculate: Determine the drying rate in kg H2O/m2.s during the constant rate period.  Humidity ratio, wet bulb temperature and the mass flow rate (kg air/s) of the air entering to the dryer

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
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A food product, having a dry weight of 30 kg is dried in a tunnel dryer. Drying was from top surface only having an area of 2 m2. The following data were obtained during the drying process:

 

Drying time (hour)

Sample weight (kg)

0

50.0

1

48.5

2

47.0

3

45.5

4

44.0

5

42.8

10

36.9

15

33.8

20

32.9

 

The air used in the dryer is conditioned by first cooling outside air (20 °C, 40% RH) to 0°C and then heating to 50°C before passing through the dryer. Air flows parallel to the product surface through the dryer having cross sectional dimensions of 150 cm X 100 cm.

 

Calculate:

  1. Determine the drying rate in kg H2O/m2.s during the constant rate period. 
  2. Humidity ratio, wet bulb temperature and the mass flow rate (kg air/s) of the air entering to the dryer 

 

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