Table 5A — Condenser Pressure Drop
50BVC,J,Q Units
FLOW RATE | SIZE 020 | SIZE 024 | SIZE 028 | SIZE 034 |
(gpm) |
| Pressure | Drop (ft wg) |
|
35 | 9.1 | — | — | — |
40 | 11.2 | 6.0 | — | — |
45 | 13.5 | 7.5 | — | — |
50 | 15.9 | 9.1 | 9.1 | — |
55 | 18.4 | 10.9 | 10.9 | — |
60 | 21.1 | 12.8 | 12.8 | 10.8 |
65 | 23.9 | 14.8 | 14.9 | 12.7 |
70 | 27.4 | 17.0 | 17.2 | 14.7 |
75 | — | 19.3 | 19.6 | 16.9 |
80 | — | 21.7 | 22.2 | 19.2 |
85 | — | — | 24.9 | 21.7 |
90 | — | — | 27.8 | 24.3 |
95 | — | — | 30.8 | 27.1 |
100 | — | — | 34.0 | 30.0 |
105 | — | — | — | 33.1 |
110 | — | — | — | 36.3 |
115 | — | — | — | 39.7 |
120 | — | — | — | 43.2 |
LEGEND
GPM — Flow Rate
PD — Pressure Drop (ft wg)
Table 5B — Condenser Pressure Drop
50BVT,V,W Units
FLOW RATE | SIZE 034 | SIZE 044 | SIZE 054 | SIZE 064 |
(gpm) |
| Pressure | Drop (ft wg) |
|
60 | 8.7 | — | — | — |
70 | 11.9 | — | — | — |
80 | 15.5 | 6.3 | — | — |
90 | 19.6 | 8.0 | — | — |
100 | 24.2 | 9.9 | 6.0 | — |
110 | 29.3 | 12.0 | 7.3 | — |
120 | 34.9 | 14.3 | 8.7 | 8.7 |
130 | — | 16.7 | 10.2 | 10.2 |
140 | — | 19.4 | 11.8 | 11.8 |
150 | — | 22.3 | 13.6 | 13.6 |
160 | — | 25.3 | 15.5 | 15.5 |
170 | — | — | 17.4 | 17.4 |
180 | — | — | 19.6 | 19.6 |
190 | — | — | 21.8 | 21.8 |
200 | — | — | 24.2 | 24.2 |
210 | — | — | — | 26.6 |
220 | — | — | — | 29.2 |
230 | — | — | — | 31.9 |
240 | — | — | — | 34.8 |
LEGEND
GPM — Flow Rate
PD — Pressure Drop (ft wg)
Pressure and temperature ports are recommended in both the supply and return lines for system flow balancing. These openings should be 5 to 10 pipe diameters from the unit water connections. For thorough mixing and temperature stabiliza- tion, wells in the water piping should extend at least 1/2 pipe diameter into the pipe. Measuring the condenser waterside pressure drop and referring to Tables 5A and 5B can help to properly set the water flow rate.
Improper fluid flow due to valving, piping, or improper pump operation constitutes abuse that may result in voiding of unit warranty. The manufacturer will not be responsible for damages or failures resulting from improper piping design or piping material selection.
EVAPORATOR CONDENSATE DRAIN — The condensate drain connection is
Drain lines should be pitched away from the unit with a minimum slope of
A trap must be installed in the condensate line to ensure free condensate flow (units are not internally trapped). A vertical air vent is sometimes required to avoid air pockets.
Install a
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P1
1/2 P1
Fig. 20 — Condensate Drain Layout
When calculating trap depth, remember that it is not the total static pressure but the upstream or downstream static resistance that is trapped against. For instance, when calculat- ing the trap depth for a cooling coil condensate pan, trap against the coil pressure drop in that coil section and any other pressure drops upstream of it.
If calculating the trap depth for the cooling coil, use the total static pressure drop (coil plus any other components upstream of it) plus 1 in. (P1 = negative static pressure + 1 in.), as shown in Fig. 21.
Traps must store enough condensate to prevent losing the drain seal at
Drain pans should be cleaned periodically to avoid the
HOT WATER HEATING COIL (Optional) — A
Piping should be in accordance with accepted industry standards and all components rated for the system pressure expected. Pipe the coils so that they will drain, and provide a drain and vent.
Always connect the supply to the top of the coil, and the return to the bottom. Refer to Fig.
Water coils should not be subjected to entering air tempera- tures below 38 F to prevent coil
The return air duct system should be carefully designed to get adequate mixing of the return air and outdoor air streams to prevent cold spots on the coil that could freeze.
A 2 or
22