325
9
300
7 8
Water Pressure Drop (Kpa)
275
250
225
200
175
150
125
10
11 & 12
100
75
50
25
0
0 | 5 | 10 | 15 | 20 | 25 |
|
|
| Liters/second | LEGEND | |
|
|
| 7 — 30RAP035 | 10 — 30RAP050 | |
|
|
|
| ||
|
|
|
| 8 — 30RAP040 | 11 — 30RAP055 |
|
|
|
| 9 — 30RAP045 | 12 — 30RAP060 |
Fig. 17B — Heat Exchanger Pressure Drop —
BADGOOD
BADGOOD
Fig. 18 — Tank Baffling
Table 7 — Maximum Loop Volume Limits
CONCENTRATION | |||||
GAL | L | GAL | L | ||
| |||||
PURE WATER | 310 | 1173 | 725 | 2744 | |
10% EG | 180 | 681 | 425 | 1609 | |
20% EG | 175 | 662 | 410 | 1552 | |
30% EG | 155 | 587 | 370 | 1401 | |
40% EG | 150 | 568 | 350 | 1325 | |
10% PG | 175 | 662 | 410 | 1552 | |
20% PG | 150 | 568 | 350 | 1325 | |
30% PG | 128 | 485 | 300 | 1136 | |
40% PG | 118 | 447 | 275 | 1041 | |
LEGEND |
|
|
|
|
EG — Ethlyene Glycol
PG — Propylene Glycol
NOTE: Max loop volume is based on typical system of 12 psig and 30 psig of min/max pressures, and 100 F mean temperature. If the volume in the system is greater than the limits listed, then extra expansion tank volume must be added to the system.
Table 6 — Minimum Fluid Volume In Circulation | |||||||||
|
|
|
|
|
|
|
| ||
|
| NORMAL AIR | PROCESS COOLING OR | ||||||
|
|
| LOW AMBIENT | ||||||
30RAP |
| CONDITIONING |
| ||||||
|
| OPERATION |
| ||||||
UNIT |
| APPLICATION |
|
| |||||
| APPLICATION gal/ton | ||||||||
SIZE |
| gal/ton (L per kW) | |||||||
|
| (L per kW) |
| ||||||
|
|
|
|
|
|
| |||
| Std Unit | HGBP | Digital | Std Unit | HGBP |
| Digital | ||
010,015 | 12 | (13.0) | N/A | 3 (3.3) | 12 | (13.0) | N/A |
| 3 (3.3) |
6 | (6.5) | 4 (4.3) | 3 (3.3) | 10 | (10.8) | 7 (7.6) |
| 3 (3.3) | |
3 | (3.3) | 3 (3.3) | 3 (3.3) | 6 | (6.5) | 5 (5.4) |
| 3 (3.3) |
LEGEND
HGBP — Hot Gas Bypass
Pump Modification/Trimming (Units with
the only way to obtain greater flow with a given pump/impeller is to decrease system head. This will allow the pump to “ride” its curve to the right, resulting in increased flow. If greater flow is necessary, look at opening the balance valve. Also, verify that the strainer is clean, and that no unnecessary system resis- tance is present, such as partially closed isolation valves.
Increasing system resistance by closing the balancing valve will force the pump to “ride” its curve to the left, resulting in less flow. Although this does reduce power consumption slightly, it may not be the desirable method of reducing the flow, especially if a rather large reduction is needed.
19