Humidification Flashcards

1
Q

This topic involves the contact of a pure liquid with a gas for the purpose of changing the vapor content of the gas and/or adding or removing heat from the contacting phase for purposes of heating or cooling.

A

humidification

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2
Q

humidification operation may also be classified as

A

dehumidification, air conditioning and water cooling

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3
Q

The operation involves two components and two phases.

A

phase equilibria

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4
Q

Based on the Gibb’s phase rule, the number of degrees of freedom to define equilibrium conditions is

A

two

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5
Q

This refers to the ratio of the mass of vapor per mass of vapor-free gas.

A

Absolute Humidity

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6
Q

through this, the partial pressure exerted by the vapor A in the gas B can be determined

A

Absolute humidity

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7
Q

This refers to the maximum amount of vapor that a gas can contain which is in equilibrium with the liquid at a given temperature.

A

Relative Humidity

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8
Q

The partial pressure of the vapor is in effect equal to the vapor pressure.

A

Relative Humidity

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9
Q

pressure exerted by a vapor that is in equilibrium with its condensed state

A

Vapor pressure

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10
Q

Ratio of absolute humidity and Saturation humidity is equal to the

A

percentage saturation or percentage humidity

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11
Q

This is the volume occupied by one pound of dry gas plus whatever vapor it contains at a given pressure and temperature.

A

humid volume

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12
Q

The specific volume if the gas is saturated with the vapor.

A

Saturated Volume

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13
Q

This is the heat needed to raise the temperature of one pound of dry gas and the vapor it contains by 1°F.

A

Humid Heat

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14
Q

Total enthalpy content of 1 lb of dry gas and its vapor at a given temperature.

A

Enthalpy of Mixture

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15
Q

This refers to the steady state temperature attained by a gas-vapor mixture when saturated with vapor by spraying under adiabatic conditions.

A

Adiabatic Saturation Temperature

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16
Q

This refers to the steady state temperature attained by a small mass of liquid immersed in a large body of gas.

A

Wet bulb temperature

17
Q

for air-water system the wet bulb temperature becomes identical with the

A

adiabatic saturation temperature

18
Q

steady temperature attained when a vapor-gas mixture becomes saturated when cooled at constant humidity

A

Dew Point

19
Q

Many of the humidification properties for air-water system can be obtained from the ________________ at 1 atm pressure.

A

humidity chart

20
Q

In this operation, the temperature of water is constant and equal to the wet bulb temperature of the gas

A

adiabatic humidification

21
Q

the air undergoes a non-adiabatic humidification

A

water cooling

22
Q

in humidification, if the system is limited to air-water, the design may be based on the enthalpy driving force as given by

A

Merkel’s Equation

23
Q

for water cooling, the Hg is

A

height of a transfer unit (HTU)

24
Q

for water cooling, the Ng is

A

number of transfer units (NTU)

25
Q

consists of the enthalpy of air at saturation based on the temperature of water

A

equilibrium curve

26
Q

equal to the internal energy of the system plus the product of pressure and volume.

A

enthalpy

27
Q

in humidification, ploting of the operating line is generated using the

A

enthalpy balance

28
Q

in humidification, the slope of operating line is

A

L/w

29
Q

obtained by dividing enthalpy transfer equation by the liquid phase heat transfer equation

A

slope of the tie line

30
Q

if the operating line and equilibrium curve are linear, Ng (Number transfer of unit) can be evaluated by

A

logarithmic mean driving force

31
Q

if the resistance to heat transfer in the liq phase can be neglected

A

the slope of tie line becomes infinite

32
Q

for dehumidification and air conditioning

A

in ref to the humidification:

  • similar equation
  • reversed limit
  • operating line is above the equilibrium curve
33
Q

Mickley’s graphical method can be used to determine the

A

temperature profile

34
Q

plotting of the differential equation obtained from the enthalpy transfer equation and the gas phase heat transfer

A

mickley’s equation

35
Q

limiting flow rates of liquid and gas based on the equilibrium conditions may be obtained from

A

slope of operating line when it intersects equilibrium curve at the enthalpy temperature diagram