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Handbook of air conditioning and refrigeration / Shan K

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Suction Line<br />

REFRIGERATION SYSTEMS: RECIPROCATING, ROTARY, SCROLL, AND SCREW 11.15<br />

5. Find the equivalent length <strong>of</strong> the pipe fittings <strong>and</strong> accessories listed in Tables 11.2 <strong>and</strong> 11.3,<br />

based on the tentative diameter <strong>of</strong> the copper tubing. Recalculate the equivalent length <strong>of</strong> the<br />

<strong>refrigeration</strong> piping including the pipe fittings <strong>and</strong> accessories.<br />

6. Check the size <strong>of</strong> the copper tubing from the Q rl-L eq charts based on the calculated L eq. If it is<br />

equal to the tentative value, the tentative diameter is the required diameter. If not, adjust the<br />

tentative diameter.<br />

7. Determine whether the size <strong>of</strong> the <strong>refrigeration</strong> pipe meets the oil entrainment requirement when<br />

the <strong>refrigeration</strong> load is reduced to its minimum load at part-load operation. If it does not meet<br />

the requirement, add a double riser.<br />

The suction line is the most critical refrigerant line in the piping design. Vapor refrigerant <strong>and</strong> entrained<br />

oil in the evaporator should return to the compressor free <strong>of</strong> liquid slugs.<br />

Oil Trap <strong>and</strong> Piping Pitch. In the suction line, an oil trap should be installed at the bottom <strong>of</strong> a<br />

single riser, as shown in Fig. 11.9a. The sensing bulb <strong>of</strong> the thermostatic expansion valve is <strong>of</strong>ten<br />

TABLE 11.2 Pressure Drop <strong>of</strong> Valves Expressed in Equivalent Length <strong>of</strong> Straight Pipe, in Feet, for Refrigeration Systems<br />

(Screwed, Welded, Flanged, <strong>and</strong> Flared Connections) Losses are for all valves in fully open position.<br />

Nominal pipe or<br />

tube size, in. Globe * 60°-Y 45°-Y Angle * Gate † Swing check ‡ Lift check<br />

17 8 6 6 0.6 5<br />

18 9 7 7 0.7 6 Globe <strong>and</strong><br />

22 11 9 9 0.9 8 vertical lift<br />

1 29 15 12 12 1.0 10 same as<br />

1<br />

1<br />

38<br />

43<br />

20<br />

24<br />

15<br />

18<br />

15<br />

18<br />

1.5<br />

1.8<br />

14<br />

16<br />

globe<br />

valves §<br />

2 55 30 24 24 2.3 20<br />

2 69 35 29 29 2.8 25<br />

3 84 43 35 35 3.2 30<br />

1 3�8 1�2 3�4 1�4 1�2 �2 3 1 � 2<br />

100 50 41 41 4.0 35<br />

4 120 58 47 47 4.5 40<br />

5 140 71 58 58 6 50<br />

6 170 88 70 70 7 60<br />

8 220 115 85 85 9 80<br />

10 280 145 105 105 12 100 Angle lift<br />

12 320 165 130 130 13 120 same as<br />

14 360 185 155 155 15 135 angle<br />

16 410 210 180 180 17 150 valve<br />

18 460 240 200 200 19 165<br />

20 520 275 235 235 22 200<br />

24 610 320 265 265 25 240<br />

* These losses do not apply to valves with needle point type seats.<br />

† Regular <strong>and</strong> short pattern plug cock valves, when fully open, have same loss as gate valve. For valve losses <strong>of</strong> short pattern plug cocks above 6<br />

in. check manufacturer.<br />

‡ Losses also apply to the in-line, ball type check valve.<br />

§ For Y pattern globe lift check valve with seat approximately equal to the nominal pipe diameter, use values <strong>of</strong> 60° � Y valve for loss.<br />

Source: ASHRAE <strong>H<strong>and</strong>book</strong> 1990, Refrigeration Systems <strong>and</strong> Applications. Reprinted with permission.

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