16.01.2013 Views

Handbook of air conditioning and refrigeration / Shan K

Handbook of air conditioning and refrigeration / Shan K

Handbook of air conditioning and refrigeration / Shan K

SHOW MORE
SHOW LESS

Create successful ePaper yourself

Turn your PDF publications into a flip-book with our unique Google optimized e-Paper software.

11.22 CHAPTER ELEVEN<br />

If a receiver is installed after the condenser, the liquid line between the condenser <strong>and</strong> receiver<br />

should be sized so that liquid flows from the condenser to the receiver <strong>and</strong> gas flows in the opposite<br />

direction. This section <strong>of</strong> liquid line is usually sized based on a liquid velocity <strong>of</strong> 100 fpm (0.5 m/s).<br />

In the design <strong>and</strong> planning <strong>of</strong> the liquid line layout, the following factors must be considered:<br />

● If a receiver is placed after the subcooling section <strong>of</strong> the condenser, subcooling will occur at the<br />

outlet <strong>of</strong> the receiver only when a surge-type liquid receiver is used or if an additinal subcooling<br />

setup is added after the receiver.<br />

● Static pressure due to the liquid refrigerant column must be taken into account. At 105°F<br />

(40.6°C), the density <strong>of</strong> liquid HCFC-22 is 70.3 lb/ft 3 (1125 kg/m 3 ). For each foot <strong>of</strong> liquid column,<br />

the increase <strong>of</strong> static pressure is therefore �p s � 70.3/144 � 0.488 psi (3.4 kPa), or roughly<br />

0.5 psi (3.5 kPa) for each foot <strong>of</strong> liquid column. At the top <strong>of</strong> a 10-ft (3-m) riser, the pressure is<br />

about 10 � 0.5 � 5 psi (35 kPa) less than at the bottom <strong>of</strong> the riser.<br />

Figure 11.12 is a Q rl-L eq chart for a liquid line with HCFC-22 at 40°F (4.4°C) suction temperature<br />

<strong>and</strong> 105°F (40.6°C) condensing temperature with a pressure drop corresponding to a change <strong>of</strong> 1°F<br />

(0.56°C) saturation temperature.<br />

For suction temperature other than 40°F (4.4°C) <strong>and</strong> condensing temperature other than 105°F<br />

(40.6°C), the corrected <strong>refrigeration</strong> load is calculated as<br />

Q rl,c �<br />

Qrl Fliq, s Fliq,c (11.4)<br />

Correction factor Fliq,s takes into account the effect <strong>of</strong> enthalpy difference hlv-hen on m˙ r.<br />

Correction<br />

factor Fliq,c also takes into account the effect <strong>of</strong> enthalpy difference on m˙ r.<br />

Its values are listed in<br />

Table 11.1. When Tcon � 105°F (40.6°C), Fliq,c � 1, <strong>and</strong> Qrl,c � Qrl. FIGURE 11.12 Liquid line sizing Q rl--L eq chart for HCFC-22 at 40°F suction temperature <strong>and</strong> 105°F condensing<br />

temperature (type L copper tube, outside diameter, 1°F change in saturated temperature).

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!