HUMIDIFICATION AND DRYING Flashcards

1
Q

Involves removal of moisture, usually water from a solid by allowing a composite material to come in contact with a drying medium that supplies the heat needed by moisture to evaporate.

A

Drying

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2
Q

Moisture remove is the unbound/free moisture, capable of generating partial pressure equivalent to vapor pressure time of drying.

A

Drying Rate Period

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3
Q

Moisture remove is bound moisture, water evaporates after capillary action/diffusion to the solids’ surface time of drying.

A

Falling Rate Period

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4
Q

Drying medium conditions subjecting the solids are changing.

A

Variable Drying Conditions

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5
Q
  • tsolid and residual moisture = constant
  • wet bulb temperature of air is constant
A

Adiabatic Dryers

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6
Q

Rf is assumed linear and passing through origin, Rf independent of ΔH

A

Drying is not Adiabatic

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7
Q

x > xc

A

Drying Rate Period

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8
Q

x < xc

A

Falling Rate Period

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9
Q

qL and qD = 0

A

Adiabatic Dryers

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10
Q

Involves the transfer of material between a pure liquid phase and a fixed gas phase that is nearly insoluble in the liquid

A

Humidification

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11
Q
  • These operations are somewhat similar but simpler than absorption and stripping.
A

Humidification

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12
Q
  • The liquid contains only one component, there are no concentration
    gradients and no resistance to mass transfer in the liquid phase.
A

Humidification

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13
Q

the gaseous form of the component that is also present
as liquid (liquid that can become gas)

A
  • Vapor
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14
Q

component present only in gaseous form (does not
condense)

A

Gas

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15
Q
  • Sometimes also called as Absolute Humidity
  • This refers to the ratio of the mass of vapor per unit mass of vapor-free gas. This may be determined from the partial pressure exerted by the vapor (A) in the gas (B).
A

HUMIDITY

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16
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. The partial pressure of the vapor is in effect equal to the vapor pressure.
A

Saturation Humidity, HS.

17
Q
  • This refers to the ratio of the partial pressure to the vapor pressure at a specified temperature of the gas-vapor mixture.
A

Relative Humidity, RH or HR

18
Q
  • This refers to the ratio of the partial pressure to the vapor pressure at
    a specified temperature of the gas-vapor mixture.
A

Percentage Saturation or Percentage Humidity, HA

19
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, VH

20
Q

The specific volume if the gas is saturated with the vapor

A

Saturated volume, Vs

21
Q

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

A

Humid Heat, Cs

22
Q

This refers to the total enthalpy content of 1 lb gas and its vapor at a given temperature

A

Enthalpy of Mixture, Hy

23
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, Ts

24
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, Tw

25
Q
  • This is the steady temperature attained when a vapor-gas mixture becomes saturated when cooled at constant humidity, that is pA= pA
A

Dew Point, Td

26
Q

Adiabatic Humidification

A

In order for humidification to be considered adiabatic, the following conditions must be met:
1. Tx1 =Tx2 =Tx =constant
2. TW1=TW2= Tx= constant
That is, the temperature of the water is constant and equal to the wet-bulb temperature of the gas which is also constant. This, of course, is a simplification which may not be achieved in reality.

27
Q

the air undergoes a non-adiabatic humidification process. Thus, the integrated design equations used are similar to that of dehumidification except that the limits are reversed.

A

Water Cooling

28
Q

Due to the approximate nature of the mass and heat transfer equations generated for water cooling and dehumidification, it is necessary to use a more accurate working design equation. If the system is limited to air-water, the design may be based on the enthalpy driving force as given by the ________

A

Merkel’s Equation.

29
Q

Presents Physical and thermal properties of moist air in a graphical form

A

Psychrometric Chart

30
Q

Actual temperature of air-vapor mixture

A

Dry Bulb Temperature

31
Q

lowest temperature at which air can be cooled by the evaporation of water into the air at a constant pressure

A

Wet Bulb Temperature

32
Q

Temperature at which H = Hs

A

Dew point