Selection Procedure
Step 4.
Determine the pressure drop at 6.53 GPM. Pressure drops are cataloged for both standard wall (SWT) and heavy wall. (HWT) tube coils. In this example, if a SWT coil is selected the pressure drop, by interpolation is 2.38 feet of water.
Step 5.
Calculate the final air temperature
F.T. = E.A.T. + | Btu/hr | |
CFM x 1.085 | ||
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= 70 + 96000 = 70 + 53.2 = 123.2° 1661 x 1.085
Example 2
Determine the capacity of a Model 336P unit heater operating at 180° (EWT), 100° (EAT) and 15° (WTD).
Step 1.
Find conversion factor (inTable
Step 2.
Adjust the water temperature drop
Adj. WTD = 15 = 27.5°
.546
Step 3.
Multiply the MBH (interpolated) at
27.5° WTD, 200° EWT and 60° EAT by the factor to obtain the MBH at desired conditions.
0.546 x 224.9 = 123.0 MBH
Step 4.
WTD = 27.5 x 0.546 = 15°
Step 5.
GPM = | Btu/hr | = 123,000 = 16.9 | |
485xWTD | |||
| (485)(15) |
Step 6.
Pressure drop interpolated at 27.5°WTD for a SWT coil is 1.82 feet of water.
Step 7.
Calculate final temperature
F.T. = E.A.T. + |
| Btu/hr |
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CFM x 1.085 | |||||||
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= 100° + |
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| 123,000 | = 121.8° | ||
| 5210 x 1.085 |
Note:
If a constant water temperature drop is desired, apply the conversion factor to the WTD and to the desired MBH and enter 200° EWT column at these conditions. Select the unit which will provide the equivalent MBH at the adjusted WTD. The GPM can then be interpolated from the table at the adjusted WTD. To determine the actual capacity at operating conditions proceed as outlined in example #2.
If a constant GPM is desired, enter the 200° EWT column at the given or calculated GPM. Select the unit which will provide the equivalent MBH at this GPM. To determine the actual capacity at operating conditions in this case proceed as outlined in example #1.
Table
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Air |
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| Entering WaterTemperature |
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Temp. |
| 160 | 170 | 180 | 190 | 200 | 210 | 220 | 230 | 240 | 250 | 260 | 270 | 280 | 290 | 300 | 310 | 320 | 330 | 340 | 350 | 360 | 370 | 380 | 390 | 400 |
30 | .962 | 1.036 | 1.110 | 1.182 | 1.259 | 1.331 | 1.408 | 1.482 | 1.554 | 1.627 | 1.702 | 1.780 | 1.850 | 1.925 | 2.000 | 2.070 | 2.142 | 2.220 | 2.295 | 2.370 | 2.440 | 2.515 | 2.590 | 2.660 | 2.735 | |
40 | .880 | .954 1.024 1.100 1.171 1.249 | 1.318 1.391 1.468 | 1.539 | 1.612 1.686 | 1.759 | 1.831 | 1.909 | 1.976 | 2.048 | 2.120 2.193 | 2.268 2.348 | 2.417 | 2.488 2.560 2.632 | ||||||||||||
50 | .795 | .869 | .940 | 1.011 | 1.085 | 1.158 | 1.230 | 1.301 | 1.374 | 1.448 | 1.520 | 1.590 | 1.664 | 1.735 | 1.809 | 1.882 | 1.953 | 2.024 | 2.095 | 2.168 | 2.242 | 2.312 | 2.388 | 2.459 | 2.530 | |
60 | .715 | .785 | .859 | .929 1.000 1.071 | 1.141 1.215 1.285 | 1.359 | 1.429 | 1.500 | 1.571 | 1.642 | 1.715 | 1.785 | 1.858 | 1.930 2.000 | 2.070 2.140 2.215 2.285 2.360 2.430 | |||||||||||
70 | .634 | .704 | .774 | .845 | .917 | .988 1.058 1.129 1.200 | 1.270 | 1.340 | 1.410 | 1.482 | 1.552 | 1.622 | 1.694 | 1.764 | 1.838 1.907 1.976 2.045 2.116 2.188 2.258 2.332 | |||||||||||
80 | .568 | .628 | .698 | .768 | .838 | .908 | .978 | 1.048 | 1.118 | 1.188 | 1.258 | 1.328 | 1.398 | 1.468 | 1.538 | 1.604 | 1.674 | 1.742 | 1.815 | 1.884 | 1.952 | 2.020 | 2.091 | 2.162 | 2.230 | |
90 | .484 | .552 | .622 | .690 | .760 | .829 | .898 | .967 1.036 1.106 1.173 | 1.244 | 1.311 | 1.380 | 1.450 | 1.515 | 1.585 | 1.655 | 1.723 | 1.795 | 1.862 | 1.930 | 1.998 | 2.067 | 2.137 | ||||
100 | .410 | .478 | .546 | .615 | .684 | .753 | .820 | .889 | .957 | 1.025 | 1.095 | 1.161 | 1.230 | 1.300 | 1.368 | 1.433 | 1.499 | 1.569 | 1.638 | 1.705 | 1.776 | 1.843 | 1.910 | 1.977 | 2.046 |
Apply to the 200 F entering water capacities only.
Correction Factors for Propylene Glycol/Water
When sizing equipment for systems that will utilize a propylene glycol solution, consider the following factors:
1.Heat transfer @180F with no increase in flow rate
Propylene
Glycol
20% solution | .97* |
50% solution | .90* |
Table
Abbreviations | Definitions |
MBH | 1000 BTU Per Hour |
GPM | Gallons Per Minute |
FT | FinalTemperature °F |
Feet Of Water Pressure Drop - Standard WallTubes. | |
Feet Of Water Pressure Drop - Heavy WallTubes |
| Propylene |
| Propylene | |
2. GPM required @180F, | Glycol |
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| Glycol |
20°D (no correction to |
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pump curve) | 1.10% | 7. pH@50% by volume. | 9.5 | |
3. Pump head required |
| 8. Freezing Point | 55% by volume — | |
@180F w/increase in |
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| 50% | |
GPM | 1.23%* |
| 40% | |
4. Specific gravity |
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| 30% | +28F |
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| 20% | +17F | |
(water = 1.0) | **Compared to water |
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5. Pounds/Gallons@60F |
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(water = 8.3453 |
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Pounds/Gallons) | 8.77 |
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20 |