Drying - PowerPoint PPT Presentation

1 / 28
About This Presentation
Title:

Drying

Description:

Hot Air. A. L. Qc = Convective heat transfer rate. Qc = hc A ... Hot Air. A. L -dx/dt = rate of moisture loss -dx/dt = Qc/ Hvap = (moles water/hr) ... – PowerPoint PPT presentation

Number of Views:2348
Avg rating:3.0/5.0
Slides: 29
Provided by: univer86
Category:
Tags: air | drying | hot

less

Transcript and Presenter's Notes

Title: Drying


1
  • Drying

R. Gary Hollenbeck
2
(No Transcript)
3
(No Transcript)
4
(No Transcript)
5
  • Thermal Dehydration

y Solid. x H2O y Solid x
H2O
x amount of water y amount of solid WD x/y
moisture content (dry weight) WW x/(xy)
moisture content (wet weight)
6
  • Comparison of Moisture Content Expressions

WW
1
0.8
0.6
0.4
0.2
0
0
1.0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
WD
7
  • Comparison of Moisture Content Expressions

WW
1
0.8
0.6
0.4
0.2
0
0
10
1
2
3
4
5
6
7
8
9
WD
8
  • Comparison of Moisture Content Expressions

WW
WD
9
  • Heat Transfer Mechanisms
  • Convection
  • Conduction
  • Radiation

10
  • Mass Transfer Mechanisms
  • Diffusion
  • vapor
  • liquid
  • Capillary Flow
  • Shrinkage/Pressure Gradients
  • Gravity
  • Vaporization/Condensation

11
  • Tray Drying

Hot Air
Qc Convective heat transfer rate Qc
energy/time cal/hr
12
  • Tray Drying

Hot Air
A
L
Qc Convective heat transfer rate Qc hc A
?T hc convective heat transfer coefficient A
Area ? T Temperature differential
13
  • Drying of Wet Solid

Hot Air
A
L
-dx/dt rate of moisture loss -dx/dt Qc/ ?Hvap
(moles water/hr) ?Hvap heat of vaporization
14
  • Tray Drying

Hot Air
A
L
-dx/dt rate of moisture loss -dx/dt hc A ?T/
?Hvap
15
  • Constant Rate Period

y weight of dry solid y r V r A L r bulk
density V Volume of bed -dx /y -dWD
hc ?T dt dt r ?Hvap
L -dWD/dt Kc


Note terms on rhs are constant as long as free
moisture exists at the bed surface.
16
  • Drying Curve

Wo
Constant Rate Period slope Kc
Wc
WD(t)
time
17
  • Falling Rate Period

When dry areas begin to appear on the surface of
the bed, and mass transfer of water to the
surface becomes rate-limiting.
-dWD/dt KF (WD(t) - We) KF Falling Rate
Constant We Equilibrium Moisture Content
18
  • Drying Curve

Wo
Wc
WD(t)
Falling Rate Period
We
time
19
  • Drying Curve

Wo
Constant Rate Period
KC KF (WC - We)
Wc
WD(t)
Falling Rate Period
We
time
20
  • Classical Bed Dryer

Adjustable Louvers
Exhaust Outlet
Fresh Air Inlet
Fan Screen
Heater
21
  • Vertical Fluid Bed Dryer
  • Fresh Air Inlet Filter
  • Steam or Electric Heater
  • Air Circulating Fan
  • Air Volume Damper
  • Air Diffuser
  • Vessel Containing Material
  • Nylon Filter Bags
  • Air Exhaust

22
  • Conveyor Fluidized Bed Dryer

Exhaust Blower
Surge Hopper
Dust Collector
Exhaust Air Duct
Dry Material
Vibrating Conveyor
Conveying and air distributing surface
23
Spray Dryer
  • Feed Tank
  • Centrifugal Atomizer
  • Drying Chamber
  • Inlet Air Filter
  • Air Supply Fan
  • Air Heater
  • Triple Inlet Duct
  • Adjustable Air Disperser
  • Cooling Air Fan
  • Chamber Product Collector
  • Cyclone Product Collector
  • Exhaust Fan

Hot Air Liquid Feed Dry Powder Hot Air
2
3
8
12
1
7
9
11
6
10
5
4
24
  • Activity 1

In a continuous dryer, should the air flow be
con-current or counter-current?
Con-current
Counter-current
25
  • Activity 2

How will the drying rate curve change if the wet
solid is dried in a fluidized bed dryer instead
of a tray dryer?
26
  • Activity 3

Analyze the stages in drying for a solution being
dried in a spray dryer.
27
  • Activity 4

Predict how the distribution of a water-soluble
drug in a wet granulation would be influenced by
the drying process in a tray dryer.
28
  • Activity 5

Predict how the distribution of a water soluble
drug in a granulation would be influenced by the
drying process in a fluid bed dryer.
Write a Comment
User Comments (0)
About PowerShow.com