Psychrometric Chart Analyzer

m
101.3 kPa

Dry bulb (Tdb)

--

Relative humidity (RH)

--

Humidity ratio (W)

--

Wet bulb (Twb)

--

Dew point (Tdp)

--

Enthalpy (h)

--

Specific volume (v)

--

Click to highlight chart lines:

Process mode:
Calculate via:
°C
%
⚠ Calculated inputs lie outside standard operating limits or saturation curve. Properties clamped.

Calculated state properties

Dry bulb temperature --
Wet bulb temperature --
Dew point temperature --
Relative humidity --
Humidity ratio (W) --
Enthalpy (h) --
Specific volume (v) --

Directions

This simulator plots real-time air states on a psychrometric chart and lets you model common HVAC air-conditioning processes.

1. Set your conditions

2. Define State 1 and State 2

3. Explore the chart

Use the Details button for the governing equations and symbol definitions, and Guided inquiry to download a companion worksheet.

Details: equations & symbols

All properties are computed at the local total pressure \(P\), determined from elevation \(z\) (m) using the barometric formula:

\[ P(z) = 101.325\left(1 - 2.25577\times10^{-5}\,z\right)^{5.25588} \ \text{kPa} \]

Saturation vapor pressure

A Tetens-type correlation is used for dry-bulb temperature \(T\) in \(^{\circ}\text{C}\):

\[ p_{sat}(T) = 0.61078\,\exp\!\left(\dfrac{17.27\,T}{T+237.3}\right)\ \text{kPa}, \quad T \ge 0^{\circ}\text{C} \]

\[ p_{sat}(T) = 0.61078\,\exp\!\left(\dfrac{21.875\,T}{T+265.5}\right)\ \text{kPa}, \quad T < 0^{\circ}\text{C (over ice)} \]

Humidity ratio and vapor pressure

\[ W = 0.62198\,\dfrac{p_w}{P-p_w} \qquad\Longleftrightarrow\qquad p_w = \dfrac{P\,W}{0.62198+W} \]

Relative humidity

\[ \text{RH} = \dfrac{p_w}{p_{sat}(T_{db})}\times 100\% \]

Dew point temperature

Found by inverting the Tetens correlation for the vapor pressure \(p_w\):

\[ T_{dp} = \dfrac{237.3\,\ln\!\left(p_w/0.61078\right)}{17.27-\ln\!\left(p_w/0.61078\right)} \]

Enthalpy of moist air

\[ h = 1.006\,T_{db} + W\left(2501.0+1.86\,T_{db}\right)\ \text{kJ/kg dry air} \]

Specific volume

\[ v = \dfrac{R_{da}\,(T_{db}+273.15)\,(1+1.6078\,W)}{P}, \qquad R_{da}=0.287055\ \text{kJ/(kg}\cdot\text{K)} \]

Thermodynamic wet-bulb temperature

\(T_{wb}\) is solved iteratively (bisection) from the adiabatic-saturation energy balance:

\[ h(T_{db},W) = h_{sat}(T_{wb}) - \left(W_{s}(T_{wb})-W\right)c_{p,w}\,T_{wb} \]

where \(W_s(T_{wb})\) is the saturation humidity ratio at \(T_{wb}\) and \(c_{p,w}=4.186\ \text{kJ/(kg}\cdot\text{K)}\) is the specific heat of liquid water.

Adiabatic mixing of two streams

Conservation of dry-air mass and energy for streams 1 and 2 combining into stream 3 (with mass fractions \(r_1+r_2=1\)):

\[ T_{db,3}=r_1T_{db,1}+r_2T_{db,2}, \qquad W_3=r_1W_1+r_2W_2 \]

Symbols

SymbolMeaningUnits (SI)
\(T_{db}\)Dry-bulb temperature°C
\(T_{wb}\)Thermodynamic wet-bulb temperature°C
\(T_{dp}\)Dew-point temperature°C
RHRelative humidity%
\(W\)Humidity ratiokg water / kg dry air
\(h\)Specific enthalpy (per kg dry air)kJ/kg
\(v\)Specific volume (per kg dry air)m³/kg
\(P\)Total (atmospheric) pressurekPa
\(p_{sat}\)Saturation vapor pressure at \(T_{db}\)kPa
\(p_w\)Partial (vapor) pressure of waterkPa
\(z\)Elevation above sea levelm
\(r_1, r_2\)Mass fraction of mixing stream 1, 2—

About

This simulation was generated by Professor David L. Silverstein and Dr. Loyal Murphy of the University of Mississippi using Google Gemini. It was modified for LearnChemE using Claude AI.