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Handbook of air conditioning and refrigeration / Shan K

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To save energy, most AHU <strong>and</strong> PU manufacturers also <strong>of</strong>fer <strong>air</strong> economizers for single-zone<br />

constant-volume systems when the supply volume flow rate <strong>of</strong> the <strong>air</strong> system is 2000 cfm (1000<br />

L/s) <strong>and</strong> greater. Most single-zone constant-volume systems employ zone temperature control,<br />

night setback, diagnostics, emergency stop, <strong>and</strong> safety controls. Air economizer <strong>and</strong> <strong>air</strong> system controls<br />

are discussed in the chapters that follow.<br />

Energy per Unit Volume Flow<br />

As specified in ASHRAE/IESNA St<strong>and</strong>ard 90.1-1999 <strong>and</strong> discussed in Sec. 17.2, the fan power<br />

input to the fan motors per unit volume flow Psy / V˙ sd in hp/cfm (W·s/L), for constant-volume <strong>air</strong><br />

systems as calculated by Eq. (17.24a):<br />

(20.29)<br />

For variable-<strong>air</strong>-volume (VAV) systems, the fan power input per unit volume flow can be calculated<br />

by Eq. (17.24b) as:<br />

20.11 AIR CONDITIONING PROCESSES<br />

Sensible Heat Ratio<br />

P sy<br />

V˙ sd<br />

P sy<br />

V˙ sd<br />

P sy<br />

V˙ sd<br />

P sy<br />

V˙ sd<br />

AIR SYSTEMS: BASICS AND CONSTANT-VOLUME SYSTEMS 20.41<br />

� 0.0012 hp / cfm (0.0019 W�s / L) when V˙ sd � 20,000 cfm (9440 L / s)<br />

� 0.0011 hp / cfm (0.00174 W�s / L) when V˙ sd � 20,000 cfm<br />

� 0.0017 hp / cfm (0.0027 W�s / L) when V˙ sd � 20,000 cfm<br />

� 0.0015 hp / cfm (0.0024 W�s / L) when V˙ sd � 20,000 cfm<br />

An <strong>air</strong> <strong>conditioning</strong> process determines the change in thermodynamic properties <strong>of</strong> moist <strong>air</strong> between<br />

the initial <strong>and</strong> final states <strong>of</strong> <strong>conditioning</strong> <strong>and</strong> also the corresponding energy <strong>and</strong> mass transfer<br />

between the moist <strong>air</strong> <strong>and</strong> a medium, such as water, refrigerant, or moist <strong>air</strong> itself during this<br />

change. The energy balance <strong>and</strong> the conservation <strong>of</strong> mass in nonnuclear processes are the two principles<br />

most <strong>of</strong>ten used in the analysis <strong>and</strong> calculation <strong>of</strong> the change <strong>of</strong> thermodynamic properties in<br />

<strong>air</strong> <strong>conditioning</strong> processes.<br />

In general, for a single <strong>air</strong> <strong>conditioning</strong> process, heat transfer or mass transfer is positive. However,<br />

for calculations that involve several <strong>air</strong> <strong>conditioning</strong> processes, the heat supplied to the moist<br />

<strong>air</strong> is taken to be positive, <strong>and</strong> the heat rejected from the moist <strong>air</strong> is taken to be negative.<br />

The sensible heat ratio (SHR) <strong>of</strong> an <strong>air</strong> <strong>conditioning</strong> process is defined as the ratio <strong>of</strong> the absolute<br />

value <strong>of</strong> sensible heat to the absolute value <strong>of</strong> total heat, or<br />

SHR �<br />

In Eq. (20.30), total heat, in Btu/h (W), is given as<br />

� qsen �<br />

� qtotal � �<br />

� qsen �<br />

� qsen � � � ql �<br />

q total � � q sen � � � q l �<br />

(20.30)

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