Wet Bulb Temperature Calculator

Calculate

Relative humidity of the air (0–100%)

Overview

Wet-bulb temperature is the lowest temperature that air can reach through evaporative cooling alone — the equilibrium temperature of a water-wetted surface freely evaporating into the surrounding air. It is one of the three fundamental psychrometric temperatures (along with dry-bulb and dew point) and is essential for cooling tower sizing, evaporative cooler performance, outdoor heat stress assessment, and HVAC coil entering-air conditions.

Unlike dew point, which depends only on moisture content, wet-bulb temperature depends on both the moisture content and the dry-bulb temperature of the air. It always lies between the dry-bulb and the dew point: at 100% relative humidity all three temperatures converge; as humidity decreases, the wet-bulb depression (T_db − T_wb) increases, indicating greater evaporative cooling potential.

This calculator derives wet-bulb temperature from any of three common input combinations — dry-bulb with relative humidity, dry-bulb with dew point temperature, or dry-bulb with humidity ratio — using an iterative Newton-Raphson solver on the Sprung psychrometric equation. It outputs wet-bulb temperature alongside wet-bulb depression, relative humidity, humidity ratio, dew point, vapor pressure, and enthalpy, and classifies the result against ASHRAE comfort thresholds and cooling effectiveness benchmarks.

Both Imperial (°F, gr/lb, psi) and Metric (°C, g/kg, kPa) unit systems are fully supported. All formulas use the Magnus approximation with constants 17.625 and 243.04, and the corrected Imperial saturation pressure constant 0.08855 = 0.61078 × 0.1450377.

How to Use This Calculator

  1. Select input combination — choose from Dry-Bulb + Relative Humidity, Dry-Bulb + Dew Point Temperature, or Dry-Bulb + Humidity Ratio.

  2. Enter dry-bulb temperature — in °C or °F.

  3. Enter the second input based on your selected combination — relative humidity (%), dew point temperature (°C/°F), or humidity ratio (g/kg or gr/lb).

  4. Click "Calculate" — get wet-bulb temperature, wet-bulb depression (ΔT), relative humidity, humidity ratio, dew point, vapor pressure, and enthalpy.

Use the entering wet-bulb for cooling tower / evaporative cooler sizing and coil total-load selection; size to the ASHRAE 0.4%/1% design wet-bulb for the location.

Inputs & Outputs

Inputs

  • Input Combination — Options: Dry-Bulb + Relative Humidity, Dry-Bulb + Dew Point Temperature, Dry-Bulb + Humidity Ratio
  • Dry-Bulb Temperature (°C / °F)
  • Relative Humidity (%)
  • Dew Point Temperature (°C / °F)
  • Humidity Ratio (g/kg / gr/lb)

Outputs

  • Wet-Bulb Temperature (°C / °F)
  • Wet-Bulb Depression (ΔT) (°C / °F)
  • Relative Humidity (%)
  • Humidity Ratio (W) (g/kg / gr/lb)
  • Dew Point Temperature (°C / °F)
  • Vapor Pressure (kPa / psi)
  • Specific Enthalpy (kJ/kg / BTU/lb)

Formula

Calculator Formulas

All calculations assume standard atmospheric pressure:

  • Imperial: P_atm = 14.696 psi
  • Metric: P_atm = 101.325 kPa

Saturation Vapor Pressure (Magnus Approximation)

Metric:   P_sat(T) = 0.61078 × exp(17.625 × T / (243.04 + T))   [kPa]
Imperial: P_sat(T) = 0.08855 × exp(17.625 × Tc / (243.04 + Tc)) [psi]
          where Tc = (T_°F − 32) / 1.8

Note: 0.08855 = 0.61078 × 0.1450377 (base Magnus constant × kPa-to-psi conversion)


Sprung Psychrometric Equation (Forward Direction)

Given dry-bulb T_db and wet-bulb T_wb, the humidity ratio is:

Metric:
  W_sat_wb = 621.945 × P_sat(T_wb) / (P_atm − P_sat(T_wb))   [g/kg]
  W = W_sat_wb − 0.000799 × (T_db − T_wb) × (1000 + W_sat_wb) [g/kg]

Imperial:
  W_sat_wb = 4350 × P_sat(T_wb) / (P_atm − P_sat(T_wb))       [gr/lb]
  W = W_sat_wb − 0.000437 × (T_db − T_wb) × 7000              [gr/lb]

Wet-Bulb from Known Humidity Ratio (Iterative Solver)

When the humidity ratio W is known (from RH, dew point, or direct input), wet-bulb temperature is found by solving the Sprung equation iteratively:

Find T_wb such that:

f(T_wb) = W_sat(T_wb) − A × (T_db − T_wb) × K − W_actual = 0

where:

  • Metric: A = 0.000799, K = (1000 + W_sat(T_wb))
  • Imperial: A = 0.000437, K = 7000

This calculator uses Newton-Raphson iteration with numerical derivative:

T_wb[n+1] = T_wb[n] − f(T_wb[n]) / f'(T_wb[n])

Convergence criterion: |ΔT_wb| < 0.001°C (0.002°F)


Combination A: Dry-Bulb + Relative Humidity

Step 1: P_sat_db = Magnus formula at T_db Step 2: P_v = (RH / 100) × P_sat_db Step 3: W from vapor pressure

Metric:   W = 621.945 × P_v / (P_atm − P_v)   [g/kg]
Imperial: W = 4350 × P_v / (P_atm − P_v)       [gr/lb]

Step 4: T_wb by iterative Sprung solver Step 5: Dew point by inverse Magnus on P_v Step 6: Depression = T_db − T_wb


Combination B: Dry-Bulb + Dew Point

Step 1: P_v = P_sat(T_dp) (Magnus formula at dew point) Step 2: W from vapor pressure (same as Combo A Step 3) Step 3: RH = (P_v / P_sat(T_db)) × 100 Step 4: T_wb by iterative Sprung solver Step 5: Depression = T_db − T_wb


Combination C: Dry-Bulb + Humidity Ratio

Step 1: P_v from humidity ratio

Metric:   P_v = P_atm × W / (621.945 + W)   [kPa]
Imperial: P_v = P_atm × W / (4350 + W)       [psi]

Step 2: RH = (P_v / P_sat(T_db)) × 100 Step 3: T_wb by iterative Sprung solver Step 4: Dew point by inverse Magnus on P_v Step 5: Depression = T_db − T_wb


Dew Point (Inverse Magnus)

Metric:
  α = ln(P_v / 0.61078)
  T_dp = 243.04 × α / (17.625 − α)   [°C]

Imperial:
  P_v_kPa = P_v_psi × 6.8948
  α = ln(P_v_kPa / 0.61078)
  T_dp(°C) = 243.04 × α / (17.625 − α)
  T_dp(°F) = 32 + 1.8 × T_dp(°C)

Enthalpy

Imperial: h = 0.240 × T_db + (W / 7000) × (1061 + 0.444 × T_db)   [BTU/lb]
Metric:   h = 1.006 × T_db + (W / 1000) × (2501 + 1.86 × T_db)    [kJ/kg]

Verification

  • At RH = 100%: T_wb = T_db = T_dp, depression = 0
  • At RH = 0%: T_wb → T_dp → minimum, depression → maximum
  • T_dp ≤ T_wb ≤ T_db always holds
  • Wet-bulb depression increases as RH decreases (more evaporative cooling potential)

Variable Reference

Variable Meaning Units
T_db Dry-bulb temperature °F / °C
T_wb Wet-bulb temperature °F / °C
T_dp Dew point temperature °F / °C
RH Relative humidity %
W Humidity ratio gr/lb / g/kg
P_v Partial vapor pressure psi / kPa
P_sat Saturation vapor pressure psi / kPa
ΔT Wet-bulb depression (T_db − T_wb) °F / °C
h Specific enthalpy BTU/lb / kJ/kg
P_atm Standard atmospheric pressure 14.696 psi / 101.325 kPa

What Is Wet-Bulb Temperature?

Wet-bulb temperature is the temperature reading from a thermometer whose sensing bulb is wrapped in a water-saturated wick and exposed to moving air. As water evaporates from the wick, it absorbs latent heat from the thermometer, cooling it below the dry-bulb (ambient) temperature. The equilibrium temperature reached — where the rate of heat gained from the warmer surrounding air equals the rate of latent heat lost through evaporation — is the wet-bulb temperature.

The wet-bulb depression (T_db − T_wb) is a direct measure of the air's evaporative cooling potential. In dry air (low RH), evaporation is rapid and the depression is large — the wet bulb reads well below the dry bulb. In humid air (high RH), evaporation is slow and the depression is small. At 100% relative humidity, no evaporation occurs and the wet-bulb equals the dry-bulb temperature.

Why Wet-Bulb Temperature Matters in HVAC

Wet-bulb temperature is the single most important parameter for sizing cooling towers and evaporative condensers. A cooling tower's capacity is fundamentally limited by the entering wet-bulb temperature — it cannot cool water below this temperature regardless of tower size. The difference between the leaving cold water temperature and the entering wet-bulb temperature (the "approach") is the primary performance metric for tower selection.

In evaporative cooling (swamp cooler) design, wet-bulb temperature determines the lowest achievable supply air temperature. The wet-bulb effectiveness of the cooler, typically 70–90%, defines how close the leaving air temperature approaches the entering wet-bulb temperature.

For HVAC cooling coil design, the entering wet-bulb temperature determines the total (sensible + latent) cooling load on the coil. Two air streams with the same dry-bulb temperature but different wet-bulb temperatures have different total heat content (enthalpy), and the coil must be sized for the higher wet-bulb condition.

Wet-bulb temperature is also the basis for outdoor heat stress indices. The Wet Bulb Globe Temperature (WBGT) index used by OSHA, military, and athletic organizations for heat safety guidelines is dominated by the wet-bulb component, which captures the combined effect of temperature and humidity on the human body's ability to cool itself through perspiration.

Key Facts

  • Wet-bulb temperature always lies between dry-bulb and dew point temperatures: T_dp ≤ T_wb ≤ T_db. At 100% RH, all three temperatures are equal. As humidity decreases, the spread between them increases.
  • Cooling towers cannot cool water below the entering wet-bulb temperature. The approach (leaving water temperature minus wet-bulb) is the primary performance metric — typical design approaches range from 5–10°F (3–6°C) for HVAC towers.
  • The ASHRAE design wet-bulb temperature for a location is the 0.4% or 1% annual exceedance value from ASHRAE Climatic Design Conditions. Equipment sized to the 0.4% design wet-bulb will meet load for 99.6% of annual hours.
  • Wet-bulb depression (T_db − T_wb) directly indicates evaporative cooling potential. A depression of 20°F (11°C) or more indicates conditions favorable for evaporative cooling. A depression below 5°F (3°C) means evaporative cooling is ineffective.
  • The Sprung psychrometric constant used in this calculator (A = 0.000799 °C⁻¹ metric, A = 0.000437 °F⁻¹ imperial) applies to mechanically ventilated (aspirated) wet-bulb thermometers with air velocity ≥ 3 m/s (600 fpm).
  • A wet-bulb temperature of 35°C (95°F) is considered the theoretical upper limit of human survivability — above this temperature, the human body cannot cool itself through perspiration regardless of shade, wind, or hydration.

Applications

  • Cooling tower sizing and performance evaluation — entering wet-bulb temperature determines the theoretical minimum cold water temperature and tower approach
  • Evaporative cooler (swamp cooler) design — wet-bulb temperature sets the lowest achievable supply air temperature; wet-bulb depression indicates cooling potential
  • HVAC cooling coil entering-air conditions — wet-bulb temperature determines total enthalpy and latent load on the coil
  • Outdoor heat stress assessment — wet-bulb temperature is the dominant component of WBGT (Wet Bulb Globe Temperature) used for occupational and athletic heat safety
  • Psychrometric analysis and field measurement — convert sling psychrometer readings (dry-bulb + wet-bulb) to full psychrometric state
  • ASHRAE climate data interpretation — design wet-bulb temperatures from ASHRAE Climatic Design Conditions are used for equipment sizing in every HVAC project

Example Calculation

Imperial Example

Given: Combination A — Dry-Bulb + Relative Humidity

  • T_db = 95°F, RH = 40%
  • P_atm = 14.696 psi

Step 1 — Saturation pressure at 95°F:

Tc = (95 − 32) / 1.8 = 35.00°C
P_sat = 0.08855 × exp(17.625 × 35.00 / (243.04 + 35.00))
P_sat = 0.08855 × exp(2.2188) = 0.08855 × 9.197 = 0.8144 psi

Step 2 — Vapor pressure:

P_v = 0.40 × 0.8144 = 0.3258 psi

Step 3 — Humidity ratio:

W = 4350 × 0.3258 / (14.696 − 0.3258) = 1417.2 / 14.370 = 98.6 gr/lb

Step 4 — Wet-bulb (iterative Sprung solver):

Initial guess: T_wb = (95 + T_dp) / 2 ≈ 78°F

Iteration 1: T_wb = 78°F
  Tc_wb = (78 − 32)/1.8 = 25.56°C
  P_sat_wb = 0.08855 × exp(17.625×25.56/(243.04+25.56)) = 0.4721 psi
  W_sat_wb = 4350 × 0.4721 / (14.696 − 0.4721) = 144.3 gr/lb
  W_calc = 144.3 − 0.000437 × (95 − 78) × 7000 = 144.3 − 52.0 = 92.3 gr/lb
  Error = 92.3 − 98.6 = −6.3 → T_wb too low

Iteration 2: T_wb = 79.2°F
  ... (Newton-Raphson converges)

Final: T_wb ≈ 79.6°F

Step 5 — Dew point:

P_v_kPa = 0.3258 × 6.8948 = 2.246 kPa
α = ln(2.246 / 0.61078) = 1.302
T_dp(°C) = 243.04 × 1.302 / (17.625 − 1.302) = 316.4 / 16.323 = 19.4°C
T_dp(°F) = 32 + 1.8 × 19.4 = 66.9°F

Step 6 — Wet-bulb depression:

ΔT = 95 − 79.6 = 15.4°F

Step 7 — Enthalpy:

h = 0.240 × 95 + (98.6/7000) × (1061 + 0.444 × 95)
h = 22.80 + 0.01409 × 1103.2 = 22.80 + 15.54 = 38.34 BTU/lb

Result summary:

  • Wet-Bulb Temperature: 79.6°F
  • Wet-Bulb Depression: 15.4°F
  • Relative Humidity: 40.0%
  • Humidity Ratio: 98.6 gr/lb
  • Dew Point: 66.9°F
  • Vapor Pressure: 0.3258 psi
  • Enthalpy: 38.34 BTU/lb
  • Status: MODERATE DEPRESSION — GOOD EVAPORATIVE COOLING POTENTIAL

Metric Example

Given: Combination B — Dry-Bulb + Dew Point

  • T_db = 30°C, T_dp = 18°C
  • P_atm = 101.325 kPa

Step 1 — Vapor pressure from dew point:

P_v = 0.61078 × exp(17.625 × 18 / (243.04 + 18))
P_v = 0.61078 × exp(1.2152) = 0.61078 × 3.371 = 2.059 kPa

Step 2 — Humidity ratio:

W = 621.945 × 2.059 / (101.325 − 2.059) = 1280.4 / 99.266 = 12.90 g/kg

Step 3 — Saturation pressure at T_db = 30°C:

P_sat_db = 0.61078 × exp(17.625 × 30 / (243.04 + 30))
P_sat_db = 0.61078 × exp(1.9364) = 0.61078 × 6.933 = 4.234 kPa

Step 4 — Relative humidity:

RH = (2.059 / 4.234) × 100 = 48.6%

Step 5 — Wet-bulb (iterative Sprung solver):

Initial guess: T_wb = (30 + 18) / 2 = 24°C

Iteration 1: T_wb = 24°C
  P_sat_wb = 0.61078 × exp(17.625×24/(243.04+24)) = 2.985 kPa
  W_sat_wb = 621.945 × 2.985 / (101.325 − 2.985) = 18.88 g/kg
  W_calc = 18.88 − 0.000799 × (30 − 24) × (1000 + 18.88)
  W_calc = 18.88 − 0.000799 × 6 × 1018.88 = 18.88 − 4.885 = 13.99 g/kg
  Error = 13.99 − 12.90 = +1.09 → T_wb too high

Iteration 2: T_wb = 22.8°C
  ... (Newton-Raphson converges)

Final: T_wb ≈ 22.5°C

Step 6 — Wet-bulb depression:

ΔT = 30 − 22.5 = 7.5°C

Step 7 — Enthalpy:

h = 1.006 × 30 + (12.90/1000) × (2501 + 1.86 × 30)
h = 30.18 + 0.01290 × 2556.8 = 30.18 + 32.98 = 63.16 kJ/kg

Result summary:

  • Wet-Bulb Temperature: 22.5°C
  • Wet-Bulb Depression: 7.5°C
  • Relative Humidity: 48.6%
  • Humidity Ratio: 12.90 g/kg
  • Dew Point: 18.0°C
  • Vapor Pressure: 2.059 kPa
  • Enthalpy: 63.16 kJ/kg
  • Status: MODERATE DEPRESSION — GOOD EVAPORATIVE COOLING POTENTIAL

Standards & References

  • ASHRAE Handbook — Fundamentals (2021), Ch. 1 Psychrometrics (Sprung wet-bulb equation) — Primary reference for wet-bulb temperature formulations, the Sprung psychrometric equation, and the relationship between wet-bulb and other psychrometric properties.
  • ASHRAE Standard 55-2020 — Thermal Environmental Conditions for Human Occupancy — References wet-bulb temperature indirectly through humidity limits and the psychrometric comfort envelope.
  • ASHRAE Climatic Design Conditions — Provides design wet-bulb temperatures (0.4%, 1%, 2% annual exceedance) for equipment sizing at locations worldwide.
  • Magnus Formula (Alduchov-Eskridge, 1996) — Used for saturation pressure calculation. Constants 17.625 and 243.04 are optimized for the temperature range −40°C to +60°C.
  • Sprung Psychrometric Equation — Constants A = 0.000437 °F⁻¹ (Imperial) and A = 0.000799 °C⁻¹ (Metric) apply to mechanically ventilated wet-bulb sensors with air velocity ≥ 3 m/s.
  • CTI Standard STD-201 — Thermal Performance Testing of Cooling Towers — Defines wet-bulb measurement requirements for cooling tower acceptance testing.

Limitations

  • All calculations assume standard atmospheric pressure of 14.696 psi (101.325 kPa). At elevations above approximately 1,000 ft (300 m), lower atmospheric pressure increases evaporation rate and lowers the wet-bulb temperature for the same moisture content.
  • The Magnus approximation loses accuracy below approximately −40°F (−40°C) and above approximately 150°F (65°C). For extreme temperature applications, use ASHRAE full-range saturation pressure equations.
  • The Sprung psychrometric constant applies to mechanically aspirated wet-bulb sensors with air velocity ≥ 3 m/s (600 fpm). Naturally ventilated or screen-shielded sensors use a different constant and may produce results that differ by 1–2°F (0.5–1°C).
  • The iterative solver converges to within 0.001°C (0.002°F) of the true psychrometric wet-bulb temperature. This precision exceeds the accuracy of field wet-bulb measurements, which are typically ±0.5°F (±0.3°C).
  • Wet-bulb temperature calculated here is the thermodynamic (psychrometric) wet-bulb, which differs slightly from the natural wet-bulb temperature used in WBGT heat stress calculations. Natural wet-bulb is measured without forced aspiration and is typically 1–3°F higher.

Common Mistakes to Avoid

  • Confusing wet-bulb with dew point temperature. Both are lower than dry-bulb, but they measure different things. Dew point depends only on moisture content and is the condensation threshold. Wet-bulb depends on both moisture content and dry-bulb temperature and represents the evaporative cooling limit. They are equal only at 100% RH.
  • Using dry-bulb temperature instead of wet-bulb for cooling tower sizing. Cooling tower capacity is governed by the entering wet-bulb temperature, not the dry-bulb. Using dry-bulb leads to oversized towers in humid climates and undersized towers in dry climates.
  • Assuming wet-bulb temperature is constant when dry-bulb changes. Unlike dew point, wet-bulb temperature changes with dry-bulb temperature even at constant moisture content. Heating air at constant humidity ratio raises the wet-bulb temperature (though less than the dry-bulb rise).
  • Applying the wrong Sprung constant for the sensor type. The psychrometric constant A = 0.000799 °C⁻¹ (0.000437 °F⁻¹) applies to mechanically aspirated wet-bulb sensors. Naturally ventilated sensors use a larger constant (approximately 0.0012 °C⁻¹), producing a lower computed humidity ratio.
  • Neglecting altitude correction for wet-bulb calculations. At higher altitudes, lower atmospheric pressure increases evaporation rate, lowering the wet-bulb temperature for the same moisture content. The standard formulas assume sea-level pressure (101.325 kPa / 14.696 psi).
  • Using wet-bulb temperature for condensation risk assessment. Condensation occurs when a surface falls below the dew point, not the wet-bulb temperature. Use the Dew Point Temperature Calculator for condensation analysis.

Frequently Asked Questions

What is wet-bulb temperature and why does it matter in HVAC?
Wet-bulb temperature is the lowest temperature air can reach through evaporative cooling alone. It matters in HVAC because it determines cooling tower capacity (towers cannot cool water below the entering wet-bulb), evaporative cooler performance, and the total heat content (enthalpy) of air entering cooling coils. It is also the basis for outdoor heat stress assessment.
What is the difference between wet-bulb and dew point temperature?
Both are lower than dry-bulb temperature, but they measure different things. Dew point is the temperature at which condensation begins — it depends only on moisture content and does not change with dry-bulb temperature. Wet-bulb is the evaporative cooling limit — it depends on both moisture content and dry-bulb temperature. Dew point is always ≤ wet-bulb, and they are equal only at 100% RH.
How is wet-bulb temperature used in cooling tower design?
Cooling tower capacity is fundamentally limited by the entering wet-bulb temperature — the tower cannot cool water below this temperature. The approach (leaving cold water temperature minus entering wet-bulb) is the primary performance metric. Typical HVAC cooling towers are designed for 5–10°F (3–6°C) approach at the ASHRAE 0.4% or 1% design wet-bulb temperature for the project location.
What is wet-bulb depression and what does it indicate?
Wet-bulb depression is the difference between dry-bulb and wet-bulb temperature: ΔT = T_db − T_wb. It directly indicates evaporative cooling potential. A large depression (>20°F / 11°C) means dry air with excellent evaporative cooling potential — ideal for swamp coolers. A small depression (<5°F / 3°C) means humid air where evaporative cooling is ineffective.
Why can't I just use a simple formula to calculate wet-bulb from dry-bulb and RH?
The Sprung psychrometric equation that defines wet-bulb temperature is implicit — wet-bulb appears on both sides of the equation through the saturation humidity ratio at the wet-bulb temperature. There is no closed-form algebraic solution. This calculator uses Newton-Raphson iteration to solve the equation numerically, converging to within 0.001°C of the true value.
Is this calculator valid for outdoor weather conditions?
Yes. This calculator accepts any valid psychrometric input combination and works equally well for outdoor conditions. Use Combination A (dry-bulb + RH) with weather station data, or Combination C (dry-bulb + humidity ratio) if you have moisture content data. The results are valid for the standard HVAC temperature range of −40°F to 150°F (−40°C to 65°C).
What is the relationship between wet-bulb temperature and human heat stress?
Wet-bulb temperature is the dominant factor in heat stress because it captures the combined effect of temperature and humidity on the body's ability to cool through perspiration. A wet-bulb temperature of 35°C (95°F) is considered the theoretical upper limit of human survivability — above this, the body cannot shed metabolic heat through evaporation regardless of shade, wind, or hydration.
How does altitude affect wet-bulb temperature?
At higher altitudes, lower atmospheric pressure increases the evaporation rate, which lowers the wet-bulb temperature for the same moisture content. This calculator assumes standard sea-level pressure (101.325 kPa / 14.696 psi). For locations above approximately 1,000 ft (300 m), altitude-corrected atmospheric pressure should be used for precise results.

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Engineers often use these calculators in combination for complete project workflows:

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