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Handbook of air conditioning and refrigeration / Shan K

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2.12 CHAPTER TWO<br />

Thermodynamic Wet-Bulb Temperature<br />

For any state <strong>of</strong> moist <strong>air</strong>, there exists a thermodynamic wet-bulb temperature T* that exactly<br />

equals the saturated temperature <strong>of</strong> the moist <strong>air</strong> at the end <strong>of</strong> the ideal adiabatic saturation process<br />

at constant pressure. Applying a steady flow energy equation, we have<br />

h1 � (w* s � w1)h* w � h* s<br />

(2.38)<br />

where h1, h* s � enthalpy <strong>of</strong> moist <strong>air</strong> at initial state <strong>and</strong> enthalpy <strong>of</strong> saturated <strong>air</strong> at end <strong>of</strong> ideal adiabatic<br />

saturation process, Btu/lb (kJ/kg)<br />

w1,w* s � humidity ratio <strong>of</strong> moist <strong>air</strong> at initial state <strong>and</strong> humidity ratio <strong>of</strong> saturated <strong>air</strong> at end<br />

<strong>of</strong> ideal adiabatic saturation process, lb/lb (kg/kg)<br />

h* w � enthalpy <strong>of</strong> water as it is added to chamber at a temperature T*, Btu/lb (kJ/kg)<br />

The thermodynamic wet-bulb temperature T*, °F (°C), is a unique property <strong>of</strong> a given moist <strong>air</strong><br />

sample that depends only on the initial properties <strong>of</strong> the moist <strong>air</strong>—w 1, h1 <strong>and</strong> p. It is also a fictitious<br />

property that only hypothetically exists at the end <strong>of</strong> an ideal adiabatic saturation process.<br />

Heat Balance <strong>of</strong> an Ideal Adiabatic Saturation Process<br />

Psychrometer<br />

When water is supplied to the insulation chamber at a temperature T* in an ideal adiabatic saturation<br />

process, then the decrease in sensible heat due to the drop in temperature <strong>of</strong> the moist <strong>air</strong> is just<br />

equal to the latent heat required for the evaporation <strong>of</strong> water added to the moist <strong>air</strong>. This relationship<br />

is given by<br />

cpd(T1 � T*) � cpsw1(T1 � T*) � (w* s � w1)h* fg<br />

(2.39)<br />

where T1 � temperature <strong>of</strong> moist <strong>air</strong> at initial state <strong>of</strong> ideal adiabatic saturation process, °F (°C)<br />

h* fg � latent heat <strong>of</strong> vaporization at thermodynamic wet-bulb temperature, Btu/lb (J/kg)<br />

Since cpa � cpd � w1cps, we find, by rearranging the terms in Eq. (2.39),<br />

Also<br />

Wet-Bulb Temperature<br />

w* s � w 1<br />

T 1 � T* � c pa<br />

h* fg<br />

T* � T 1 � (w* s � w 1)h* fg<br />

c pa<br />

(2.40)<br />

(2.41)<br />

A psychrometer is an instrument that permits one to determine the relative humidity <strong>of</strong> a moist <strong>air</strong><br />

sample by measuring its dry-bulb <strong>and</strong> wet-bulb temperatures. Figure 2.4 shows a psychrometer,<br />

which consists <strong>of</strong> two thermometers. The sensing bulb <strong>of</strong> one <strong>of</strong> the thermometers is always kept<br />

dry. The temperature reading <strong>of</strong> the dry bulb is called the dry-bulb temperature. The sensing bulb <strong>of</strong><br />

the other thermometer is wrapped with a piece <strong>of</strong> cotton wick, one end <strong>of</strong> which dips into a cup <strong>of</strong><br />

distilled water. The surface <strong>of</strong> this bulb is always wet; therefore, the temperature that this bulb<br />

measures is called the wet-bulb temperature. The dry bulb is separated from the wet bulb by a radiation-shielding<br />

plate. Both dry <strong>and</strong> wet bulbs are cylindrical.<br />

When unsaturated moist <strong>air</strong> flows over the wet bulb <strong>of</strong> the psychrometer, liquid water on the surface<br />

<strong>of</strong> the cotton wick evaporates, <strong>and</strong> as a result, the temperature <strong>of</strong> the cotton wick <strong>and</strong> the wet bulb

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