Dewpoint and Wetbulb Temperature
Air Handling Unit Tonnage Output
Chiller Tonnage Output
Chiller Coefficient of Performance
VAV Box Air Flow Rate (CFM)
Heat Index Calculation
Wind Chill Temperature Calculation
Pressure Measurement
The following equations are used to calculate the wetbulb temperature of air given the drybulb temperature and relative humidity %. The equation assumes that the ambient barometric pressure is constant at a value of 29.15 "Hg since the change in wetbulb temperature is very insignificant with changes in the ambient barometric pressure.
Input Variables | System Variables | Output Variables | |||
RH | Relative Humidity % |
e
| Ambient vapor pressure in kPa |
Td
| Dewpoint temperature in degrees C |
T | Drybulb temperature in degrees C |
GAMMA
| Constant based upon ambient barometric pressure |
Tw
| Wetbulb temperature |
DELTA
| Constant | ||||
Equations | |||||
e | (RH / 100) * 0.611*EXP(17.27*T/(T+237.3)) | ||||
Td | [116.9 + 237.3 ln(e)] / [16.78 – ln(e)] | ||||
GAMMA | 0.00066*P (Use P = 98.642 kPa. This is equal to 29.15 "Hg… about the pressure we normally experience.) | ||||
DELTA | 4098*(e / Td + 237.3)^2 | ||||
Wetbulb Temperature in Degrees F Equals: | |||||
Tw | 1.8 * [[(GAMMA*T) + (DELTA*Td)] / (GAMMA + DELTA)] + 32 | ||||
Dewpoint Temperature in Degrees F Equals: | |||||
Td | 1.8 * [[116.9 + 237.3 ln(e)] / [16.78 – ln(e)]] + 32 |
Air Handling Unit Tonnage Output
The following equation calculates the refrigeration output in Tonns of a coil.
Input Variables | Output Variables | ||
T1
| Entering air temperature of the coil in degrees F |
TONNS
| Dewpoint temperature in degrees F |
T2
| Leaving air temperature of the coil in degrees F | ||
CFM
| Volume of air passing through the coil | ||
Equation | |||
TONNS
| 1.08*(T1 – T2)*CFM |
The following equation calculates the refrigeration output in Tonns of a chiller.
Input Variables | Output Variables | ||
T1
| Chilled water return temperature in degrees F |
TONNS
| Energy output of the chiller |
T2
| Chilled water supply temperature in degrees F | ||
GPM
| Volume of water passing through the chiller | ||
Equation | |||
TONNS
| GPM*(T1 – T2) / 24 |
The following equation calculates the ratio of energy used to the energy output of a chiller.
Input Variables | |
T1 | Chilled water return temperature in degrees F |
T2 | Chilled water supply temperature in degrees F |
GPM | Volume of water passing through the chiller |
KW | Kilowatts |
Output Variables | |
COP | Energy output of the chiller |
Equation | |
COP | (T1 – T2) * GPM * 0.0417 / (0.28433 * KW) |
Input Variables | |
A | Duct area in sq. ft |
Pv | Pressure in inches of H2O from PV3 |
Output Variables | |
V | Velocity of the air |
CFM | Cubic feet of air per minute |
Equation | |
Q | AV |
0.0763 is the density of dry air at 60o F The duct diameter units are in ft. | |
CFM | 1096(Duct Diameter/2)2(√(Pv/.0763)) |
The following equation calculates the heat index of the outside air.
Input Variables | |
Tf | Outside air temperature in degrees F |
RH | Outside air relative humidity % (enter 50 for 50%, etc.) |
Output Variables | |
HI | Heat index |
Equation | |
HI | HI = -42.379 + 2.04901523T + 10.14333127R - 0.22475541TR - 6.83783x10-3T2 - 5.481717x10-2R2 + 1.22874x10-3T2R + 8.5282x10-4TR2 - 1.99x10-6T2R2
where T = ambient dry bulb temperature (°F) R = relative humidity (integer percentage). Because this equation is obtained by multiple regression analysis, the heat index value (HI) has an error of ±1.3°F. Even though temperature and relative humidity are the only two variables in the equation, all the variables on the lists above are implied. |
Wind Chill Temperature Calculation
The following equation calculates the wind chill temperature of the outside air.
Input Variables | |
V | Outside air velocity in Miles per Hour |
T | Outside air temperature in degrees F |
Output Variables | |
WC | Wind chill temperature |
Equation | |
WC | 0.0817(3.71(V)^0.5 + 5.81 - 0.25V)(T - 91.4) + 91.4 |
Velocity Pressure | |
Where V = Air Velocity (FPM) Pv = Velocity Pressure (in. w.g.) |
Equivalent Measures of Pressure | |
1lb. per square inch | = 144lbs. per sq. ft. = 2.036in. Mercury at 32°F = 2.311ft. Water at 70°F = 27.74in. Water at 70°F |
1 inch Water at 70°F | = .03609lb. per sq. in. = .5774oz. per sq. in. = 5774oz. per sq. in. = 5.196lbs. per sq. ft. |
1 ounce per sq. in. | = 1272in. Mercury at 32°F = 1.733in. Water at 70°F |
1ft. Water at 70°F | = .433lbs. per sq. in. = 62.31lbs. sq. ft. |
1 Atmosphere | = 14.696lbs. per sq. in. = 2116.3lbs. per sq. ft. = 33.96ft. Water at 70°F = 29.92in. Mercury at 32°F |
1in. Mercury at 32°F | = .491lbs. per sq. in. = 7.86oz. per sq. in. = 1.136ft. Water at 70°F = 13.63in. Water at 70°F |
Compression Ratio | |
Compression Ratio | = Absolute Discharge Pressure / Absolute Suction Pressure |
Absolute Discharge Pressure | = gauge reading + 15psi |
Absolute Suction Pressure | = gauge reading + 15psi |
Refrigerant Mass Flow Rate | |
Mass Flow Rate (Pounds/Minute) | = Piston Displacement X Refrigerant Density = (Cubic Feet/Minute) X (Pounds/Cubic Feet) |
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