DriSteem Vaporstream Specifikace Strana 14

  • Stažení
  • Přidat do mých příruček
  • Tisk
  • Strana
    / 84
  • Tabulka s obsahem
  • KNIHY
  • Hodnocené. / 5. Na základě hodnocení zákazníků
Zobrazit stránku 13
P a g e 1 0 D R I - S T E E M D e s i g n G u i d e
D R I - S T E E M D e s i g n G u i d e P a g e 1 1
Sample Problem 4
Determine the maximum humidification load for an economizer
system located in Minneapolis where:
The desired conditions in the space are 70 °F and 35% RH.
The mixed air is 55 °F.
The total air is 12,000 cfm.
Solution to Sample Problem 4 using
the economizer cycle method
1. Find the moisture content of your desired conditions by
referring to Table 6-1 on Page 6. Read across the 70 °F line to the
35% column, and find 2.40 lbs/hr/100 cfm.
2. Determine the moisture to be added at each 10 °F increment by
using:
Table 11-1 to find entering RH
Table 6-1 to find moisture content of entering conditions
Table 9-1 to find the percentage of outside air
Create a new table with your results by using the following
formula (where H = lbs/hr/cfm):
[H (space) H (outside air)] × % outside air
× [cfm (total air)/100 cfm] = lbs/hr (load)
Table 12-1 shows data created from the above formula for this
sample problem.
3. Find the maximum humidification load from your created table.
The maximum load for this system is 70.68 lbs/hr and occurs
when the outdoor temperature is 40 °F as shown in Table 12-1.
Notes about economizer cycle method
Economizer “free cooling,” provided
by using outside air, is not always cost
effective. The operating cost advantage of
ambient cooling may be lost when certain
operating conditions prevail, such as:
The indoor relative humidity requirements
are in a fairly high range (40% RH or
greater).
Electricity is used to heat water into
steam for humidification.
A crossover point occurs where the
economizer cycle’s increased humidification
energy costs (due to increased air volume
requiring humidification) are more than the
savings derived by outside air cooling.
Zobrazit stránku 13
1 2 ... 9 10 11 12 13 14 15 16 17 18 19 ... 83 84

Komentáře k této Příručce

Žádné komentáře