Psychrometric Chart & Moist Air Properties Calculator
Analyze moist air thermodynamics, HVAC conditioning processes, and atmospheric state points. Computes dry-bulb, wet-bulb, dew point temperature, relative humidity, humidity ratio, specific enthalpy, and specific volume with real-time psychrometric chart visualization.
Psychrometric Chart & Moist Air Properties Calculator: Free Psychrometric Chart & Moist Air Properties Calculator tool: interactive Psychrometric Chart and Moist Air Properties Calculator. Compute dry-bulb.
Thermodynamic State Inputs
Moist Air State Vector
Engineering Fundamentals of Psychrometrics and Moist Air Thermodynamics
Psychrometrics is the branch of atmospheric thermodynamics and chemical engineering dedicated to the physical, thermal, and vapor-equilibrium properties of gas-vapor mixtures—most notably atmospheric air mixed with water vapor. In building services engineering, HVAC design, industrial food dehydration, cleanroom manufacturing, and meteorology, precise quantification of moist air properties is foundational to sizing cooling coils, chillers, evaporative cooling towers, humidifiers, and ventilation air-handling units (AHUs).
Dry atmospheric air is a multi-component mixture primarily comprised of diatomic nitrogen (78.084% by volume), diatomic oxygen (20.947%), argon (0.934%), carbon dioxide (~0.042%), and trace noble gases, exhibiting an apparent average molecular weight of $M_a = 28.966 ext{ g/mol}$. In contrast, pure water vapor has a molecular weight of $M_w = 18.01528 ext{ g/mol}$. Because moist air represents a binary mixture of non-condensable dry air and condensable steam (water vapor), its thermodynamic behavior conforms rigorously to Dalton's Law of Partial Pressures and Gibbs-Dalton mixture idealizations within moderate ambient temperature and pressure regimes.
Dalton's Law and Fundamental Thermodynamic Relations
By Dalton's Law, the barometric atmospheric pressure $P$ measured by a barometer is the sum of the partial pressure exerted by dry air molecules ($P_a$) and the partial pressure exerted by water vapor molecules ($P_v$):
Applying the ideal gas law to each individual constituent gas occupying the identical mixture volume $V$ at absolute temperature $T$ (in Kelvin):
where $R_a = ar{R} / M_a = 8.31446 / 28.966 = 0.287042 ext{ kJ/(kg}cdot ext{K)}$ is the specific gas constant of dry air, and $R_w = ar{R} / M_w = 8.31446 / 18.01528 = 0.46152 ext{ kJ/(kg}cdot ext{K)}$ is the specific gas constant of water vapor. The ratio of molecular weights is given by the fundamental psychrometric constant:
Saturation Vapor Pressure: The Magnus-Tetens and ASHRAE Formulations
The maximum amount of moisture that dry air can carry at thermodynamic equilibrium without liquid condensation depends strictly on temperature. The saturation vapor pressure of water over liquid water ($P_{ws}$) is governed fundamentally by the Clausius-Clapeyron relation. Over standard HVAC ambient temperatures (-20 °C to 60 °C), the widely recognized Magnus-Tetens formulation yields excellent accuracy within 0.1% of Goff-Gratch and ASHRAE tables:
For temperatures below the freezing point ($T < 0^circ ext{C}$) over ice sublimation:
Definition of Psychrometric State Variables
- Relative Humidity ($phi$ or RH): The dimensionless ratio of actual water vapor partial pressure $P_v$ to the saturation vapor pressure $P_{ws}$ at the identical dry-bulb temperature: $$phi = rac{P_v}{P_{ws}(T_{db})} imes 100%$$
- Humidity Ratio ($W$ or Moisture Content): The mass of water vapor per unit mass of bone-dry air: $$W = rac{m_w}{m_a} = rac{M_w cdot P_v}{M_a cdot P_a} = 0.62198 cdot rac{P_v}{P - P_v} quad [ ext{kg } ext{H}_2 ext{O / kg dry air}]$$ Often expressed in engineering practice in grams per kilogram dry air ($g/kg = 1000 cdot W$).
- Dew Point Temperature ($T_{dp}$): The temperature to which moist air must be cooled isobarically ($P = ext{const}$) at constant moisture ratio ($W = ext{const}$) to reach saturation ($phi = 100%$). Inverting the Magnus relation yields: $$alpha(T_{db}, phi) = rac{17.27 cdot T_{db}}{237.3 + T_{db}} + lnleft(rac{phi}{100} ight)$$ $$T_{dp} = rac{237.3 cdot alpha}{17.27 - alpha} quad [^circ ext{C}]$$
- Wet-Bulb Temperature ($T_{wb}$) and Carrier's Psychrometric Formula: The adiabatic saturation temperature achieved when air passes over a wet thermometer bulb with high convective velocity ($> 3 ext{ m/s}$). Water evaporates into the unsaturated air, absorbing its latent heat of vaporization from the air stream until convective heat transfer balances mass evaporative cooling. Carrier's equation relates $P_v$, $T_{db}$, and $T_{wb}$: $$P_v = P_{ws}(T_{wb}) - rac{(P - P_{ws}(T_{wb})) cdot (T_{db} - T_{wb})}{1532 - 1.3 cdot T_{wb}}$$
- Specific Enthalpy of Moist Air ($h$): The total thermal energy contained in moist air per kilogram of dry air, relative to a reference state of dry air and saturated liquid water at 0 °C: $$h = c_{pa} cdot T_{db} + W cdot left( h_{we} + c_{pw} cdot T_{db} ight)$$ Using empirical specific heat capacities $c_{pa} = 1.006 ext{ kJ/(kg}cdot ext{K)}$, latent heat $h_{we} = 2501.0 ext{ kJ/kg}$, and superheated water vapor specific heat $c_{pw} = 1.86 ext{ kJ/(kg}cdot ext{K)}$: $$h = 1.006 cdot T_{db} + W cdot (2501.0 + 1.86 cdot T_{db}) quad [ ext{kJ / kg dry air}]$$
- Specific Volume of Moist Air ($v$): The volume occupied by the moist air mixture containing exactly 1.0 kilogram of dry air: $$v = rac{R_a cdot (T_{db} + 273.15)}{P_a} = rac{R_a cdot (T_{db} + 273.15) cdot (1 + 1.6078 cdot W)}{P} quad [ ext{m}^3 ext{ / kg dry air}]$$ Moist air density $ ho$ is the reciprocal of specific volume per unit total mass: $ ho = rac{1 + W}{v} ext{ kg/m}^3$.
Step-by-Step Worked Numerical Examples
Example 1: Baseline Room Air at Sea Level
Given: A standard indoor office conditioned to $T_{db} = 24.0^circ ext{C}$ and $phi = 50.0%$ relative humidity at standard sea level barometric pressure $P = 101.325 ext{ kPa}$.
Step 1: Compute saturation vapor pressure at 24 °C:
$$P_{ws}(24) = 0.61078 cdot expleft( rac{17.27 imes 24}{24 + 237.3} ight) = 0.61078 cdot exp(1.5878) = 2.986 ext{ kPa}$$Step 2: Compute actual water vapor pressure:
$$P_v = phi imes P_{ws} = 0.50 imes 2.986 = 1.493 ext{ kPa}$$Step 3: Compute humidity ratio $W$:
$$W = 0.62198 cdot rac{1.493}{101.325 - 1.493} = 0.62198 cdot rac{1.493}{99.832} = 0.009304 ext{ kg/kg} = 9.304 ext{ g / kg dry air}$$Step 4: Compute dew point temperature:
$$alpha = rac{17.27 imes 24}{261.3} + ln(0.50) = 1.5878 - 0.6931 = 0.8947$$ $$T_{dp} = rac{237.3 imes 0.8947}{17.27 - 0.8947} = rac{212.31}{16.375} = 12.97^circ ext{C} approx 13.0^circ ext{C}$$Step 5: Compute specific enthalpy:
$$h = 1.006 imes 24.0 + 0.009304 imes (2501.0 + 1.86 imes 24.0) = 24.144 + 0.009304 imes 2545.64 = 24.144 + 23.684 = 47.83 ext{ kJ/kg}$$Step 6: Compute specific volume:
$$v = rac{0.287042 imes (24 + 273.15) imes (1 + 1.6078 imes 0.009304)}{101.325} = rac{85.304 imes 1.01496}{101.325} = 0.8546 ext{ m}^3 ext{/kg}$$Example 2: Cooling and Dehumidification Coil Sizing
Scenario: An air handling unit receives outside ventilation air at $T_{db,1} = 34.0^circ ext{C}$ and $phi_1 = 65%$ ($W_1 = 22.18 ext{ g/kg}$, $h_1 = 90.9 ext{ kJ/kg}$) at an airflow rate of $dot{V} = 5,000 ext{ L/s}$ ($5.0 ext{ m}^3 ext{/s}$). The air passes across a chilled water cooling coil and discharges at $T_{db,2} = 12.5^circ ext{C}$ saturated ($phi_2 = 95%$, $W_2 = 8.52 ext{ g/kg}$, $h_2 = 33.9 ext{ kJ/kg}$).
Calculations:
1. Mass flow rate of dry air: With inlet specific volume $v_1 = 0.895 ext{ m}^3 ext{/kg}$, $dot{m}_a = 5.0 / 0.895 = 5.587 ext{ kg dry air / s}$.
2. Total cooling capacity required:
$$dot{Q}_{ ext{total}} = dot{m}_a cdot (h_1 - h_2) = 5.587 cdot (90.9 - 33.9) = 5.587 imes 57.0 = 318.5 ext{ kW} quad (90.6 ext{ Tons of Refrigeration})$$
3. Rate of water condensed from air stream:
$$dot{m}_{ ext{cond}} = dot{m}_a cdot (W_1 - W_2) = 5.587 cdot (0.02218 - 0.00852) = 5.587 imes 0.01366 = 0.0763 ext{ kg/s} = 274.7 ext{ kg / hr of condensate}$$
4. Sensible heat component:
$$dot{Q}_{ ext{sensible}} approx dot{m}_a cdot c_{pa} cdot (T_{db,1} - T_{db,2}) = 5.587 imes 1.006 imes (34.0 - 12.5) = 120.8 ext{ kW}$$
5. Latent heat component:
$$dot{Q}_{ ext{latent}} = dot{Q}_{ ext{total}} - dot{Q}_{ ext{sensible}} = 318.5 - 120.8 = 197.7 ext{ kW}$$
6. Sensible Heat Ratio: $ ext{SHR} = 120.8 / 318.5 = 0.379$ (indicates a heavily moisture-dominated tropical latent load).
Comparative Analysis of Psychrometric Air Conditioning Processes
| Psychrometric Process | Vector Direction on Chart | Dry-Bulb ($T_{db}$) | Humidity Ratio ($W$) | Relative Humidity ($phi$) | Enthalpy ($h$) | Typical Equipment Application |
|---|---|---|---|---|---|---|
| Sensible Heating | Horizontal to the Right | Increases ↑ | Constant — | Decreases ↓ | Increases ↑ | Electric duct heater, hot water reheat coil, furnace |
| Sensible Cooling | Horizontal to the Left | Decreases ↓ | Constant — | Increases ↑ | Decreases ↓ | Dry cooling coil above dew point, sensible economizer |
| Cooling & Dehumidification | Down & Left towards Saturation | Decreases ↓ | Decreases ↓ | Increases ↑ (approaches 90-95%) | Decreases ↓ | Direct expansion (DX) evaporator, chilled water coil |
| Evaporative Cooling (Adiabatic) | Up & Left along Constant Wet-Bulb | Decreases ↓ | Increases ↑ | Increases ↑ | Constant — | Direct evaporative cooler (swamp cooler), cooling tower |
| Chemical / Desiccant Dehumidification | Down & Right along Constant Enthalpy | Increases ↑ | Decreases ↓ | Decreases ↓ | Approx. Constant — | Silica gel wheel, lithium chloride rotary desiccant |
| Steam Humidification | Vertically Upward | Approx. Constant — | Increases ↑ | Increases ↑ | Increases ↑ | Electrode boiler steam canister in cleanrooms / hospitals |
ASHRAE Standard 55 Thermal Comfort Criteria
ASHRAE Standard 55 ("Thermal Environmental Conditions for Human Occupancy") defines acceptable thermal indoor environments where at least 80% of occupants express satisfaction. The primary factors include metabolic rate (met), clothing insulation (clo), air temperature, mean radiant temperature, air velocity, and humidity.
On the psychrometric chart, the thermal comfort envelope is bounded by:
- Operative Temperature: Typically between 20.0 °C and 24.0 °C in winter heating conditions (1.0 clo clothing insulation) and between 23.5 °C and 27.0 °C in summer cooling conditions (0.5 clo light clothing).
- Upper Humidity Limit: Capped at a maximum dew point of 16.8 °C or maximum humidity ratio of $W le 12.0 ext{ g/kg dry air}$ (corresponding to approximately 65% RH at 24 °C) to prevent mold growth, dust mite proliferation, and indoor air quality degradation.
- Lower Humidity Limit: Recommended minimum relative humidity $ge 30%$ (dew point $ge 2.0^circ ext{C}$ to $4.0^circ ext{C}$) to prevent dry eye irritation, mucous membrane desiccation, static electricity shocks, and respiratory discomfort.
Engineering FAQs
Why does relative humidity drop when air is heated with no water added?
Relative humidity is the ratio $P_v / P_{ws}$. When air undergoes sensible heating, the actual water vapor content $W$ and partial pressure $P_v$ remain strictly constant. However, as temperature increases, the saturation vapor pressure $P_{ws}$ increases exponentially according to the Clausius-Clapeyron equation. Because the denominator expands while the numerator stays constant, $phi$ drops precipitously. This explains why cold winter outdoor air (e.g., 0 °C, 80% RH) becomes extremely dry indoor air (e.g., 22 °C, ~22% RH) after being heated by a building furnace without dedicated humidification.
What is the Apparatus Dew Point (ADP) and Coil Bypass Factor (BF)?
In a real cooling coil, not all air molecules make direct physical contact with the cold finned tube surfaces. The effective surface temperature of the coil is termed the Apparatus Dew Point (ADP). The fraction of total air that passes through the coil uninterrupted without contacting the fins is defined as the Bypass Factor ($BF$, typically 0.05 to 0.15 for commercial coils). The off-coil state point lies along the straight condition line connecting the on-coil air state and the ADP point on the saturation curve, divided according to the Contact Factor ($CF = 1 - BF$).
How does high elevation alter cooling coil design?
At high elevations (such as Denver, Bogotá, or Mexico City), total atmospheric pressure is lower (80 to 85 kPa vs 101.325 kPa). Air density is reduced proportionally by 15% to 25%. Because heat transfer depends on the mass flow rate $dot{m} = ho dot{V}$, an air handler operating at high altitude requires a higher volumetric flow rate (CFM or $ ext{m}^3/ ext{s}$) to deliver the identical mass of air and sensible cooling capacity. Furthermore, psychrometric curves shift because the humidity ratio $W$ is higher for any given partial vapor pressure.
Frequently Asked Questions
Relative humidity is the ratio $P_v / P_{ws}$. When air undergoes sensible heating, the actual water vapor content $W$ and partial pressure $P_v$ remain strictly constant. However, as temperature increases, the saturation vapor pressure $P_{ws}$ increases exponentially according to the Clausius-Clapeyron equation. Because the denominator expands while the numerator stays constant, $phi$ drops precipitously. This explains why cold winter outdoor air (e.g., 0 °C, 80% RH) becomes extremely dry indoor air (e.g., 22 °C, ~22% RH) after being heated by a building furnace without dedicated humidification.
In a real cooling coil, not all air molecules make direct physical contact with the cold finned tube surfaces. The effective surface temperature of the coil is termed the Apparatus Dew Point (ADP). The fraction of total air that passes through the coil uninterrupted without contacting the fins is defined as the Bypass Factor ($BF$, typically 0.05 to 0.15 for commercial coils). The off-coil state point lies along the straight condition line connecting the on-coil air state and the ADP point on the saturation curve, divided according to the Contact Factor ($CF = 1 - BF$).
At high elevations (such as Denver, Bogotá, or Mexico City), total atmospheric pressure is lower (80 to 85 kPa vs 101.325 kPa). Air density is reduced proportionally by 15% to 25%. Because heat transfer depends on the mass flow rate $dot{m} = ho dot{V}$, an air handler operating at high altitude requires a higher volumetric flow rate (CFM or $ ext{m}^3/ ext{s}$) to deliver the identical mass of air and sensible cooling capacity. Furthermore, psychrometric curves shift because the humidity ratio $W$ is higher for any given partial vapor pressure.