molecalculator

Heat, Energy & Rates

Air Enthalpy Calculator: Temperature and Humidity

Calculator No. 08-0811 · Updated · Formula and assumptions shown below

Moist-air enthalpy 50.32 kJ/kg dry air
Humidity ratio
0.0099 kg water/kg dry air
Result, rounded to 4 decimal places
Water-vapor partial pressure
1.584 kPa
Result, rounded to 3 decimal places
Dry-bulb temperature
25 °C
Set in the form below
You enter
Dry-bulb temperature (°C), Relative humidity (%), Air pressure (kPa)
You get
Moist-air enthalpy (kJ/kg dry air), Humidity ratio (kg water/kg dry air), Water-vapor partial pressure (kPa)
Rounding
2 dp · 4 dp · 3 dp

For study and lab planning. The result follows from the numbers you enter and the formula shown. Check it against your method before you weigh, mix or dilute anything, follow the safety data sheet and your supervisor, and do not use it for clinical, dosing or medication work.

An air enthalpy calculator uses dry-bulb temperature, relative humidity, and usually air pressure to estimate the enthalpy of moist air. Enter those conditions to get energy per kilogram of dry air; the result helps compare heating, cooling, and humidification loads.

Formula

The calculator uses the common moist-air psychrometric approximation:

h = 1.006t + w(2501 + 1.86t)

w = 0.62198pv / (p − pv), where pv = (RH/100)pws and pws = 0.61121 exp[(18.678 − t/234.5)(t/(257.14 + t))].

  • h is moist-air enthalpy in kJ per kg of dry air.
  • t is dry-bulb temperature in °C.
  • w is humidity ratio, kg of water vapor per kg of dry air.
  • RH is relative humidity in percent, entered from 0 to 100.
  • p is total air pressure in kPa; the default, 101.325 kPa, is standard atmospheric pressure.
  • pv is water-vapor partial pressure in kPa, and pws is saturation vapor pressure in kPa.

The coefficients are conventional engineering approximations. The enthalpy reference is approximately dry air and liquid water at 0 °C; enthalpy values depend on the chosen reference, so comparisons should use the same convention.

Worked Example

Using the defaults—25 °C, 50% relative humidity, and 101.325 kPa—first estimate saturation vapor pressure:

pws = 0.61121 exp[(18.678 − 25/234.5)(25/(257.14 + 25))] ≈ 3.1685 kPa.

Then calculate vapor pressure: pv = (50/100) × 3.1685 ≈ 1.5843 kPa.

The humidity ratio is w = 0.62198 × 1.5843 / (101.325 − 1.5843) ≈ 0.009881 kg/kg dry air.

Finally, h = 1.006 × 25 + 0.009881 × (2501 + 1.86 × 25) ≈ 50.32 kJ/kg dry air. Rounded to the calculator’s two decimal places, the displayed result is 50.32 kJ/kg dry air.

Assumptions

  • The air is treated as a moist-air mixture at a single, uniform temperature and pressure.
  • The saturation-pressure equation is an engineering approximation, not a high-precision equation for every temperature range or unusual gas mixture.
  • Relative humidity describes water vapor relative to saturation at the entered dry-bulb temperature.
  • The result is per kilogram of dry air, not per kilogram of the combined moist-air mixture and not total energy in a room or duct.

What Temperature and Humidity Tell You

Temperature alone does not describe how much water vapor air contains. At the same dry-bulb temperature, air at higher relative humidity generally has a larger humidity ratio and higher enthalpy. Conversely, relative humidity can change when air is heated or cooled even if its water-vapor content stays constant: warming unsaturated air lowers its relative humidity, while cooling it raises relative humidity.

That distinction matters in comfort and building calculations. A room at 25 °C and 50% RH has about 0.0099 kg of water vapor per kilogram of dry air under the assumptions above. Heating that air without adding moisture changes its relative humidity and enthalpy; adding moisture also changes the latent-energy contribution represented by the humidity-ratio term.

When to Use the Result

Air enthalpy is useful for comparing two air states and estimating the energy change associated with conditioning air. For a process involving a known dry-air mass flow, the approximate heat-transfer rate is often calculated from the enthalpy difference:

Heat-transfer rate ≈ dry-air mass flow rate × (hout − hin)

Use consistent units: if enthalpy is in kJ/kg and dry-air flow is in kg/s, the product is kJ/s, or kW. This is a state comparison, not a complete equipment-sizing calculation. Real systems may also require fan heat, heat losses, condensate removal, changing pressure, and equipment efficiency.

  • Use dry-bulb temperature, not wet-bulb temperature or a temperature measured on a surface.
  • Enter relative humidity as a percentage: enter 50 for 50%, not 0.50.
  • Use the local or process pressure when it differs materially from standard atmospheric pressure, such as at elevation or in a pressurized system.

Reading the Calculator and Common Errors

The first output is enthalpy in kJ/kg of dry air. The humidity-ratio output offers a useful cross-check: a larger value means more water vapor per unit mass of dry air. Water-vapor partial pressure is also reported in kPa. These outputs describe the same air state in different ways; they are not interchangeable units.

A frequent misconception is that relative humidity alone measures the amount of moisture in air. It does not: RH depends on temperature as well as vapor content. Another common mistake is to interpret 50.32 kJ/kg as the energy required to heat an entire room. To estimate total energy, a dry-air mass or flow and a change between initial and final states are needed, along with a defined process boundary.

Results are approximate and rounded. Small differences from a psychrometric chart or another calculator can arise from its saturation-pressure equation, enthalpy reference, pressure setting, and rounding. The equation shown here is most appropriate for ordinary air-conditioning conditions; it should not be treated as a specialist property model for very low temperatures, high pressures, or non-air gas mixtures.

Frequently Asked Questions

What is the formula for air enthalpy from temperature and humidity?
First use temperature, relative humidity, and pressure to estimate water-vapor pressure and humidity ratio. Then use h = 1.006t + w(2501 + 1.86t), with t in °C and h in kJ/kg dry air.

Can I calculate enthalpy with temperature and relative humidity only?
You can make an estimate if you assume a pressure. This calculator defaults to 101.325 kPa, but actual pressure should be entered when known, particularly at elevation or in a pressurized process.

Is moist-air enthalpy measured per kilogram of air or water?
The result is per kilogram of dry air. It includes the sensible and water-vapor contributions, but its denominator is dry-air mass—not the total mass of moist air.

Does higher relative humidity always mean higher enthalpy?
At the same temperature and pressure, higher RH means a higher humidity ratio and generally higher enthalpy. Across different temperatures, RH alone cannot determine which air state has greater enthalpy.

Why does my psychrometric chart show a slightly different value?
Charts and calculators can use different saturation-pressure correlations, reference states, and rounding. Confirm that temperature, RH, pressure, and the dry-air basis match before comparing results.

Related

Formula used
in t | Dry-bulb temperature | °C | 25 | -50 | 100
in rh | Relative humidity | % | 50 | 0 | 100
in p | Air pressure | kPa | 101.325 | 0.01
out h | Moist-air enthalpy | kJ/kg dry air | 1.006 * t + (rh / 100 * 0.61121 * exp((18.678 - t / 234.5) * (t / (257.14 + t))) * 0.62198 / (p - rh / 100 * 0.61121 * exp((18.678 - t / 234.5) * (t / (257.14 + t))))) * (2501 + 1.86 * t) | 2
out w | Humidity ratio | kg water/kg dry air | 0.62198 * (rh / 100 * 0.61121 * exp((18.678 - t / 234.5) * (t / (257.14 + t)))) / (p - rh / 100 * 0.61121 * exp((18.678 - t / 234.5) * (t / (257.14 + t)))) | 4
out pv | Water-vapor partial pressure | kPa | rh / 100 * 0.61121 * exp((18.678 - t / 234.5) * (t / (257.14 + t))) | 3

Each line is one input (in, sel, list) or one result (out: label, unit, formula, decimals). How the calculators work

Method: the standard formula for this calculation with the constants and conversion factors written on the page, rounded as each result states. See method and constants, the disclaimer or report an error.

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