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Steam Humid Air

Reference data and engineering information about steam humid air for air psychrometrics applications.

steamhumidair

Overview

Engineering reference data for Steam Humid Air in air psychrometrics.

Key Formulas

Humidity Ratio

ω=0.622PvPa\omega = 0.622 \frac{P_v}{P_a}

Mass of water vapor per mass of dry air.

Relative Humidity

ϕ=PvPvs×100%\phi = \frac{P_v}{P_{vs}} \times 100\%

Ratio of actual to saturation vapor pressure.

Wet Bulb Temperature

Twb=TdbPvsPvγT_{wb} = T_{db} - \frac{P_{vs} - P_v}{\gamma}

Temperature measured by wet-bulb thermometer.

Enthalpy of Moist Air

h=cpT+ωhgh = c_p T + \omega h_g

Sensible + latent heat per unit mass of dry air.

Variables

SymbolDescriptionUnit
ω\omegaHumidity ratiokg/kg
ϕ\phiRelative humidity%
PvP_vVapor pressurePa
PvsP_{vs}Saturation vapor pressurePa
TdbT_{db}Dry bulb temperature°C
TwbT_{wb}Wet bulb temperature°C

Water Vapor in Air Reference Data

21 rows
Water vapor content in air (kg per 100 m³) at various dry bulb temperatures and relative humidities
Dry Bulb Temperature(°C)
100% RH(kg/100 m³)
85% RH(kg/100 m³)
80% RH(kg/100 m³)
75% RH(kg/100 m³)
70% RH(kg/100 m³)
65% RH(kg/100 m³)
60% RH(kg/100 m³)
55% RH(kg/100 m³)
50% RH(kg/100 m³)
45% RH(kg/100 m³)
40% RH(kg/100 m³)
35% RH(kg/100 m³)
30% RH(kg/100 m³)
323.392.892.722.552.382.192.041.931.71.531.361.191.02
313.222.732.572.412.252.11.931.771.611.451.291.130.97
303.052.592.442.292.131.971.831.671.521.371.221.070.91
292.892.452.312.172.021.881.731.591.451.31.161.010.87
282.732.322.192.051.911.781.641.51.371.231.10.960.82
272.592.22.071.941.811.681.551.421.291.161.030.910.78
262.452.081.961.831.711.591.471.341.221.10.970.860.73
252.311.971.851.731.621.51.391.271.161.040.930.810.69
242.191.861.751.641.531.421.311.21.090.980.870.770.66
232.061.761.631.551.451.341.241.141.030.930.830.720.62
221.951.661.561.461.361.271.171.070.980.880.780.680.59
211.841.561.471.381.291.21.11.020.920.830.740.670.55
201.741.481.391.31.221.131.040.980.870.780.690.610.52
191.631.391.311.231.151.060.980.90.820.740.650.570.49
181.541.311.241.161.0810.930.850.770.690.620.540.46
171.451.241.161.091.020.940.870.80.730.650.590.510.44
151.291.11.030.970.90.840.770.710.660.580.520.450.39
100.940.80.760.710.660.610.570.520.470.430.380.330.28
00.490.410.390.370.340.320.290.270.240.220.20.170.15
-50.330.280.260.250.230.210.20.180.160.150.130.110.1
-100.220.180.170.160.150.140.130.120.110.10.090.080.06

Source: engineeringtoolbox.com

Humidification Calculation

The required amount of steam or water to humidify air can be calculated from the difference in vapor content:

Δw=wfinalwinitial\Delta w = w_{final} - w_{initial}

Where:

  • Δw\Delta w = Amount of water vapor required (kg per 100 m³)
  • wfinalw_{final} = Final vapor content at target temperature and humidity (kg per 100 m³)
  • winitialw_{initial} = Initial vapor content at starting conditions (kg per 100 m³)

Unit Conversion Note

The table values represent vapor content in kg per 100 m3\text{kg per 100 m}^3 air volume. For calculations using humidity ratio xx (mass of water vapor per mass of dry air), convert using:

x=wρair(kg/kg dry air)x = \frac{w}{\rho_{air}} \quad \text{(kg/kg dry air)}

Where ρair\rho_{air} is the air density at the actual temperature.

Interactive Charts

Water Vapor in air vs. dry bulb temperature and relative humidity

References