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   Hastings Industries Inc.  Vari-Cool Evaporative  

Vari-Cool Evaporative - Page 6

 

 

 

THE FOLLOWING TABLE SHOWS EFFICIENCY AND PRESSURE DROP AT VARIOUS AIR QUANTITIES
I/D Model S.A.CFM Indirect Unit  % Efficiency S.P H2O Direct Unit  % Efficiency S.P H2O Face Velocity
2S(1600) 2000

2500

3000

60%

55%

50%

.2"

.3"

.44"

90%

88%

86%

.13"

.19"

.28"

400 FPM

500 FPM

600 FPM

3S(2400) 3000

3750

4500

60%

55%

50%

.2"

.3"

.44"

90%

88%

86%

.13"

.19"

.28"

400 FPM

500 FPM

600 FPM

4S(3200) 4000

5000

6000

60%

55%

50%

.2"

.3"

.44"

90%

88%

86%

.13"

.19"

.28"

400 FPM

500 FPM

600 FPM

5S (4000) 5000

6250

7500

60%

55%

50%

.2"

.3"

.44"

90%

88%

86%

.13"

.19"

.28"

400 FPM

500 FPM

600 FPM

6S(4800) 6000

7500

9000

60%

55%

50%

.2"

.3"

.44"

90%

88%

86%

.13"

.19"

.28"

400 FPM

500 FPM

600 FPM

* 7S(5600) 6000

8750

10,500

60%

55%

50%

.2"

.3"

.44"

90%

88%

86%

.13"

.19"

.28"

400 FPM

500 FPM

600 FPM

* 8S(6400) 8000

10,000

12,000

60%

55%

50%

.2"

.3"

.44"

90%

88%

86%

.13"

.19"

.22"

400 FPM

500 FPM

600 FPM

* (CFM) = Recommended secondary air quantity - indirect unit @ .17" H2O

 

Step #4 -

Using the appropriate altitude psychrometric chart, chart the performance of the indirect and direct evaporative cycles.

(a) Plot the entering condition (DB & WB) to the indirect unit. Calculate the temperature drop (cooling effect) of the unit :

[Ent.Air - (WB depression)(5 efficiency) = DB Lvg. Air

Moving horizontally from the entering air point, plot the leaving air temperature on the chart. the indirect unit provides total sensible cooling.   this point represents the leaving air from the indirect unit and the entering air condition to the direct unit.

(b) Using the entering DB & WB conditions tot he direct unit calculate the temperature drop using the direct unit efficiency.

[Ent Air - (WB depression)(%efficiency) + DB Lvg. Air

Moving diagonally up the wet-bulb line (from the entering condition to the direct unit) plot the leaving air temperature on the chart.

This point is the leaving air temperature from the two stage evaporative system at the design entering air condition.

If this supply air temperature is satisfactory, third stage booster refrigeration may not be required.

 

Step #5 - If a lower supply air temperature is required, than can be provided by the two evaporative stages, calculate the booster (conventional refrigeration) capacity by plotting the desired supply air temperature on the chart and determine the enthalpy (BTU Per Pound of Dry Air) change required :
(60) (h2 - h1)(SA cfm) = Btuh

Sp.volume dry air

h2 = leaving air temperature I/d evaporative unit

h1=leaving supply air temperature required

From this calculation the booster refrigeration capacity can be determined and cooling coil selection made.  The coil may be located either ahead of, or on the leaving air side of the direct unit.  Appropriate coil surface area and temperature must be determined based on the location of the coil and the entering air conditions.

Note that it may be advisable in some cases to increase the system supply air quantity which will reduce the refrigeration load and increase the effective capacity of the two evaporative stages.  Keep in mind that the booster refrigeration will only operate at high outdoor wet bulb conditions which comprise a small portion of the total system operating hours the two stage evaporative system will provide the total cooling effect during the majority of cooling hours.

* Note : WB depression is the difference between the dry-bulb and wet-bulb temperatures or DB° F - WB° F.

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