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Maximum Moisture Content Air

Reference data and engineering information about maximum moisture content air for air psychrometrics applications.

maximummoisturecontentair

Overview

Engineering reference data for Maximum Moisture Content 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

Air Moisture Capacity Data

14 rows
Maximum moisture content in air at saturation vs. temperature
Temperature(°C)
Temperature(°F)
Max. Water Content(g/m³)
Max. Water Content(lb/ft³)
-25-130.640.04
-20-41.050.066
-1551.580.099
-10142.310.14
-5233.370.21
0324.890.31
5416.820.43
10509.390.59
155912.80.8
206817.31.07
308630.41.9
4010451.13.2
50122835.2
601401308.1

Source: engineeringtoolbox.com

Moisture Carrying Capacity Increase

The percentage increase in moisture carrying capacity when air is heated can be calculated as:

Δ%=ρw,T2ρw,T1ρw,T1×100%\Delta\% = \frac{\rho_{w,T_2} - \rho_{w,T_1}}{\rho_{w,T_1}} \times 100\%

where ρw,T1\rho_{w,T_1} and ρw,T2\rho_{w,T_2} are the maximum water content (g/m³) at the initial and final temperatures respectively.

Example: Heated Air for Drying

When air is heated from 20°C to 50°C:

  • At 20°C: ρw,20=17.3 g/m3\rho_{w,20} = 17.3 \text{ g/m}^3
  • At 50°C: ρw,50=83.0 g/m3\rho_{w,50} = 83.0 \text{ g/m}^3

Δ%=83.017.317.3×100%=380%\Delta\% = \frac{83.0 - 17.3}{17.3} \times 100\% = 380\%

This dramatic increase in moisture holding capacity explains why heated air is significantly more effective than cold air in industrial drying processes.

Interactive Charts

Air - moisture carrying capacity vs. temperature

References