Suppose that at some point the vented dry returns feed into a vented wet return, which drops 3 ft into a condensate return tank. The estimated total equivalent length (pipe plus fittings) is 120 ft. If the mass flow rate of the condensate is 9800 lbm/hr, what size pipe should be used?
Table 10-7 applies to this situation. In this case the pressure drop is equal to the difference in elevation head between the condensate tank and the entrance to the wet return: 3 ft of head. Then the lost head per 100 ft is
∆P/L = 3(100/120) = 2.5 ft/100 ft
Referring to Table 10-7 at ∆P/L = 2.5 ft/100 ft, a 2\frac{1}{2} in. pipe can handle 9890 lbm/hr, which is close to the specified 9800 lbm/hr. Therefore, use 2\frac{1}{2} in. pipe.
Table 10-7a Vented Wet Condensate Return for Gravity Flow Based on Darcy–Weisbach Equation | ||||||||
Nominal
Diameter, in. IPS |
Condensate Flow, lb/hr,^{a} at Condensate Head, ft per 100 ft |
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0.5 | 1 | 1.5 | 2 | 2.5 | 3 | 3.5 | 4 | |
\frac{1}{2} | 105 | 154 | 192 | 224 | 252 | 278 | 302 | 324 |
\frac{3}{4} | 225 | 328 | 408 | 476 | 536 | 590 | 640 | 687 |
1 | 432 | 628 | 779 | 908 | 1020 | 1120 | 1220 | 1310 |
1 \frac{1}{4} | 901 | 1310 | 1620 | 1890 | 2120 | 2330 | 2530 | 2710 |
1 \frac{1}{2} | 1360 | 1970 | 2440 | 2840 | 3190 | 3510 | 3800 | 4080 |
2 | 2650 | 3830 | 4740 | 5510 | 6180 | 6800 | 7360 | 7890 |
2 \frac{1}{2} | 4260 | 6140 | 7580 | 8810 | 9890 | 10900 | 11,800 | 12,600 |
3 | 7570 | 10,900 | 13,500 | 15,600 | 17,500 | 19,300 | 20,900 | 22,300 |
4 | 15,500 | 22,300 | 27,600 | 32,000 | 35,900 | 39,400 | 42,600 | 45,600 |
5 | 28,200 | 40,500 | 49,900 | 57,900 | 64,900 | 71,300 | 77,100 | 82,600 |
6 | 45,800 | 65,600 | 80,900 | 93,800 | 105,000 | 115,000 | 125,000 | 134,000 |
^{a}Flow is in lb/hr of 180 F water for schedule 40 steel pipes.
Source: Reprinted by permission from ASHRAE Handbook, Fundamentals Volume, 1997. |
Table 10-7b Vented Wet Condensate Return for Gravity Flow Based on Darcy–Weisbach Equation |
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Nominal Diameter, mm |
Condensate Flow, g/s,^a |
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50 | 100 | 150 | 200 | 250 | 300 | 350 | 400 | |
15 | 13 | 19 | 24 | 28 | 32 | 35 | 38 | 41 |
20 | 28 | 41 | 51 | 60 | 68 | 74 | 81 | 87 |
25 | 54 | 79 | 98 | 114 | 129 | 142 | 154 | 165 |
32 | 114 | 165 | 204 | 238 | 267 | 294 | 318 | 341 |
40 | 172 | 248 | 308 | 358 | 402 | 442 | 479 | 513 |
50 | 334 | 482 | 597 | 694 | 779 | 857 | 928 | 994 |
65 | 536 | 773 | 956 | 1110 | 1250 | 1370 | 1480 | 1590 |
80 | 954 | 1370 | 1700 | 1970 | 2210 | 2430 | 2630 | 2810 |
100 | 1960 | 2810 | 3470 | 4030 | 4520 | 4960 | 5379 | 5750 |
125 | 3560 | 5100 | 6290 | 7290 | 8180 | 8980 | 9720 | 10,400 |
150 | 5770 | 8270 | 10,200 | 11,800 | 13,200 | 14,500 | 15,700 | 16,800 |
^{a} Flow is in g/s of 82 C water for Schedule 40 steel pipes. | ||||||||
Source: Reprinted by permission from ASHRAE Handbook. Fundamentals Volume, 1997. |