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Handbook of air conditioning and refrigeration / Shan K

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11.30 CHAPTER ELEVEN<br />

Refrigeration Capacity. In reciprocating compressors, the piston only performs compression<br />

work during the upward stroke in a complete rotation <strong>of</strong> the crankshaft. Piston displacement ,<br />

cfm [m3 V˙<br />

p<br />

/(60 s)], can be calculated as<br />

V˙ p �<br />

where Dcy � diameter <strong>of</strong> the cylinder, ft (m)<br />

Lst � stroke <strong>of</strong> cylinder, ft (m)<br />

N � number <strong>of</strong> cylinders<br />

n � rotating speed <strong>of</strong> compressor, rpm<br />

�Dcy 2 LstNn 4<br />

(11.5)<br />

From Eq. (9.72), the mass flow rate <strong>of</strong> the refrigerant m˙ r � V˙ p�v�suc, so from Eq. (9.25), the <strong>refrigeration</strong><br />

capacity Qrc, Btu/h (W), <strong>of</strong> a reciprocating compressor can be calculated as<br />

where � suc � density <strong>of</strong> suction vapor, lb/ft 3 (kg/m 3 )<br />

h 1� � enthalpy <strong>of</strong> superheated vapor leaving evaporator, Btu/lb (J/kg)<br />

h 4 � enthalpy <strong>of</strong> subcooled liquid entering evaporator, Btu/lb (J/kg)<br />

(11.6)<br />

In the eight-cylinder reciprocating compressor using HCFC-22 as refrigerant described above, volumetric<br />

efficiency � v depends mainly on compression ratio p dis/p suc. The smaller the p dis/p suc <strong>and</strong> the<br />

lower the reexpansion <strong>of</strong> clearance volume, cylinder heating, <strong>and</strong> leakages through valves <strong>and</strong> pistons,<br />

the greater the � v. Figure 11.18a shows the � v versus p dis/p suc curve for this compressor. For a<br />

suction temperature <strong>of</strong> 40°F (4.4°C), the absolute saturated pressure is 68.5 � 14.7 � 83.2 psia<br />

(574 kPa abs.). For a condensing temperature <strong>of</strong> 115°F (46.1°C), the absolute condensing pressure<br />

is 243 � 14.7 � 257.7 psia (1777 kPa abs.). The compression ratio is therefore p dis/p suc � (257.7<br />

� 3)/83.2 � 3.13. From Fig. 11.18a, � v � 0.81.<br />

The upper part <strong>of</strong> Fig. 11.18a shows the <strong>refrigeration</strong> capacity versus suction temperature Q rc-<br />

T suc curves. If T con remains constant <strong>and</strong> T suc increases, the <strong>refrigeration</strong> capacity rises accordingly<br />

for the following reasons:<br />

● For a specific compressor rotating at a specific speed, the piston displacement is constant.<br />

● Volumetric efficiency increases as T suc rises.<br />

Q rc � 60V˙ p� v� suc(h 1� � h 4)<br />

● Density <strong>of</strong> the suction vapor refrigerant � suc increases as T suc increases because <strong>of</strong> higher saturated<br />

pressure.<br />

● For a constant T con <strong>and</strong> a fixed amount <strong>of</strong> subcooling, enthalpy h 4 is also constant. Enthalpy <strong>of</strong><br />

superheated refrigerant leaving evaporator at a fixed degree <strong>of</strong> superheat h 1� increases nearly<br />

linearly between 40 <strong>and</strong> 80°F (4.4 <strong>and</strong> 26.7°C) as T suc rises. This also causes an increase <strong>of</strong><br />

<strong>refrigeration</strong> effect Q rf � h 1� � h 4. These factors result in a very slight upward bend in the<br />

Q rc - T suc curve.<br />

If the suction temperature T suc is at a constant value, an increase in condensing temperature T con results<br />

in a decrease in � v <strong>and</strong> a decrease in Q rf because <strong>of</strong> a smaller h 4. Consequently, Q rc decreases<br />

as T con rises, <strong>and</strong> Q rc increases as T con falls, as shown in Fig. 11.18.<br />

Power Input. The <strong>refrigeration</strong> compressor consumes most <strong>of</strong> the energy input to a <strong>refrigeration</strong><br />

system. In a single-stage reciprocating <strong>refrigeration</strong> system, power input P in, kW, to the compressor<br />

can be calculated from Eqs. (9.71) <strong>and</strong> (9.72):<br />

P in � V˙ p� v� suc(h 2 � h 1�)<br />

56.85� com<br />

V˙ p<br />

(11.7)

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