Humidification Operations - Unit Operations - Lecture Slides, Slides of Engineering Chemistry

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
Humidification operations involve transfer of the material between
a 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 change
the amount of water vapour in the air (humidify:
increase water concentration; or dehumidify)
by contacting air with water and evaporating/
condensing it.
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Humidification operations

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.

Design of cooling towers

Design of cooling towers

  • forced draft- natural draft(nuclear powers)

Air/water systems^ Psychrometry: science of measuring water vapour content in the air^ Notation

: H^ -^

humidity E^ -^

enthalpy h^ -^

heat transfer coefficient

Air/water systemsHumidity: example^ Partial pressure of water vapour^ If the total pressure of moist air is 100 kPa (approximatelyatmospheric) and the humidity is measured as 0.03 kg kg-1,calculate the partial pressure of the water vapour.- If the air is at 60°C, calculate the relative humidity

Air/water systems^ Psychrometry: science of measuring water vapour content in the air^ Some useful definitions

:

  1. Humidity is related to the mole fraction of water in the gas as:

OH

air

OH M

H

M

M

H

y

2

/^ 

  1. Humid heat is the energy necessary to increase the temperatureof a mixture of 1g of dry air + whatever amount of vapour by 1C:

H c c c^

OH P airP s^

,^2 ,^

 

M is molecular weight

(gas)

Air/water systemsProperties of air water systems are summarized inpsychrometric charts:

Air/water systemsRelative humidity from wet-bulb and dry-bulb temperatures

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

Air/water systems

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

Air/water systems^ Wet bulb temperature isa function of:a) Temperature of airb) HumidityIs used in analysis ofair humidity

Wet bulb temperature theory

TWick

N^ H

  1. The rate of heat requiredto evaporate

N^ A^

(rate of vaporization):

(^

2 2 2 2

,^

Wick OH P OH OH OH

T

T

c

N

M

q^

  1. At the same time the mass transferrate can be expressed through concentrationgradients

yWick

y

^

^

^

A
M
H
M
H
M
H
M
H

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!

Wet bulb temperature theory

TWick

  1. Finally, rate of heat suppliedby the air to the surface

A

T

Th

q^

Wick y^

(^ 

4) Combine 1,2,3 

^

^

2 2 2

2

,^

Wick OHp OH OH

air OH Wick air

Wick

Wick y y

T T c M H M

H
M
H
M
H

TT k y h

T docsity.com

Wet bulb temperature theory

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

c

k

h M

^

) for air-water systems

(^

Wick

Wick

T T F

H H^

 

Air/water systemsRelative humidity from wet-bulb and dry-bulb temperatures

H^ wick