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Multicomponent Distillation, Mass transport theories , Principles of adsorption , Principles of humidification , Principles of drying are main topics covered in this Unit Operations course. This lecture covers following points: Humidification Operations, Liquid Phase, Mass Transfer, Heat and Mass Transfer, Design of Cooling Towers, Air,Water Systems, Enthalpy, Psychrometry, Partial Pressure of Water Vapour, Psychrometric Charts
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Humidification operations involve transfer of the material betweena pure liquid phase and fixed gas that is nearly insoluble- Unlike absorption processes only one component is in the liquid phase(thus no concentration gradient in the liquid phase)- Both heat and mass transfer are important
Air contains water vapour. We changethe amount of water vapour in the air (humidify:increase water concentration; or dehumidify)by contacting air with water and evaporating/condensing it.
: H^ -^
humidity E^ -^
enthalpy h^ -^
heat transfer coefficient
:
OH
air
2
H c c c^
OH P airP s^
,^2 ,^
M is molecular weight
(gas)
Dry-bulb and wet-bulb temperatureDry bulb temperature:^ the ordinary temperature youmeasure with e thermometer
wet cloth/wick
Air flow
Evaporation requires energy. The wick and thereforethe thermometer bulb decreases in temperature belowthe dry-bulb temperature until the rate of heat transferfrom the warmer air to the wick is just equal to the rateof heat transfer needed to provide for the evaporationof water from the wick into the air stream.The temperature reached is called the
wet-bulb
temperature
Wet-bulb temperature
wet cloth/wick
Air flow
Evaporation requires energy. The wick and thereforethe thermometer bulb decreases in temperature belowthe dry-bulb temperature until the rate of heat transferfrom the warmer air to the wick is just equal to the rateof heat transfer needed to provide for the evaporationof water from the wick into the air stream.The temperature reached is called the
wet-bulb
temperature
TWick
N^ H
N^ A^
(rate of vaporization):
2 2 2 2
,^
Wick OH P OH OH OH
yWick
y
^
^
^
k y
Ay y k y N
OH
air OH Wick air
Wick
y
Wick y OH
2
2
2
T^ OH air
OH MH M
M H y
2 (^2) / / 1
/^
Remember!
TWick
Wick y^
2 2 2
2
,^
Wick OHp OH OH
air OH Wick air
Wick
Wick y y
T T c M H M
TT k y h
T docsity.com
OH
Wick y Air
Wick
y^
H H k M T T
h^
2 )
(
)
(
OH y Air
y
Wick Wick
k M
h
T T
H
H
2
)
(
)
(
Gives and equation of a straight line H vs TLewis relation
S y y^ air
) for air-water systems
(^
Wick
Wick
T T F
H H^
H^ wick