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R-134a Properties Calculator

Comprehensive R-134a refrigerant property lookup: enter any two properties to get T, P, v, h, s, u, quality and phase; it reports pairs it cannot resolve

By Christopher FloiedPublished Updated

Enter any two properties to find the thermodynamic state of R-134a refrigerant; for a few pairs the tool reports that the state is ambiguous or cannot be resolved (for example close to the critical point). Values come from the Tillner-Roth & Baehr (1994) reference equation of state, whose stated range is −103.30 to 181.85 °C and up to 70 MPa (critical point 101.06 °C, 4059 kPa).

Absolute h, s and u depend on this choice; Δh and Δs between two states do not.

State: Superheated Vapor, T 20.00 °C, P 400.00 kPa.

State: Superheated Vapor

Complete Thermodynamic State

Temperature T20.00 °C
Pressure P400.00 kPa
Specific Volume v0.054214 m³/kg
Enthalpy h265.86 kJ/kg
Entropy s0.9628 kJ/(kg·K)
Internal Energy u244.18 kJ/kg

R-134a Saturation Dome with State Point (T-s diagram)

Specific entropy s vs temperature T. The two curves trace the saturated-liquid (s_f) and saturated-vapor (s_g) legs of the dome; the marker is your computed state. ● = your computed state point.

Continue your calculation

Use absolute pressure and check the reported phase. Any two independent properties from T, P, v, h, s, u and x, within the model’s range, can be entered, but T and P alone cannot fix a saturated mixture (give the quality there), and for a few pairs the tool reports that the state is ambiguous or cannot be resolved, for example close to the critical point. Absolute h and s follow the reference state you pick; differences between two states do not.

How to Use This Calculator

1

Enter your input values

Fill in all required input fields for the R-134a Properties Calculator. Follow the units and input format printed next to each field. Where a unit selector is available, choose the units that match your data.

2

Review your inputs

Double-check that all values are correct and match the units or format shown for each field. Incorrect units are the most common source of calculation errors and can produce results that are off by factors of 2, 10, or more.

3

Read the results

The R-134a Properties Calculator computes the output in your browser and displays the results, with units clearly labeled, as soon as they are ready — no data sent to a server.

4

Explore parameter sensitivity

Try adjusting individual input values to see how the output changes. This is a quick and effective way to develop intuition about how different parameters influence the result and to identify which inputs have the largest effect.

Formula Reference

Reduced Helmholtz Energy (Tillner-Roth & Baehr 1994 equation of state)

α(τ, δ) = a/(RT) = α⁰(τ, δ) + αʳ(τ, δ) | τ = 374.18 K/T, δ = ρ/(508 kg/m³)

Variables: a = specific Helmholtz energy (J/kg); R = 8.314471 J/(mol·K) / 102.032 g/mol = 81.489 J/(kg·K); T = temperature (K); ρ = density (kg/m³). α⁰ is the ideal-gas part (ln δ, a constant, a term linear in τ, a ln τ term and two power terms in τ); αʳ is the residual part with 21 terms (8 polynomial, 13 exponential). The equation's critical point is 101.06 °C, 4059.28 kPa, 511.95 kg/m³. Coefficients are read from CoolProp 8.0.0's R-134a file. The equation of state's stated range is from the triple point (−103.30 °C) to 181.85 °C and up to 70 MPa; inside it some pairs of inputs still have no state or more than one, and the tool does not check for freezing at high pressure. Source: Tillner-Roth & Baehr, J. Phys. Chem. Ref. Data 23, 657–729 (1994), the international standard formulation for HFC-134a.

Thermodynamic Properties from the Helmholtz Energy

p = ρRT(1 + δαʳ_δ) | u = RTτ(α⁰_τ + αʳ_τ) | h = RT[1 + τ(α⁰_τ + αʳ_τ) + δαʳ_δ] | s = R[τ(α⁰_τ + αʳ_τ) − α⁰ − αʳ]

Variables: p = pressure (Pa); u = specific internal energy (J/kg); h = specific enthalpy (J/kg); s = specific entropy (J/(kg·K)); subscripts δ and τ are partial derivatives of α with respect to δ or τ. From your two known properties the tool finds the state with a bounded numerical search on these relations: density along the isotherm (T with P, v, h, s or u), temperature along the isobar (P with v, h, s or u) or the isochore (v with h, s or u), pressure along the isentrope or the isenthalp (pairs of h, s and u), and the saturation line for pairs with x. When the search cannot give one state it says so instead of guessing: the state is ambiguous (every match is listed), the quality is not fixed (T and P on the saturation line), the liquid and vapour cannot be resolved (too close to the critical point), or the search did not converge. Compressed liquid is computed at its real pressure (h is not replaced by h_f), and superheated vapour at the entered pressure. Source: Span, Multiparameter Equations of State (Springer, 2000), Table 3.1.

Saturation (Phase Equilibrium) and the Lever Rule

p(T, ρ′) = p(T, ρ″) and g(T, ρ′) = g(T, ρ″) | y = y′ + x · (y″ − y′) for y = v, h, s, u

Variables: ρ′, ρ″ = saturated-liquid and saturated-vapour densities (kg/m³); g = specific Gibbs energy (J/kg); x = quality, the vapour mass fraction (0 to 1); y′, y″ = saturated-liquid and saturated-vapour values of v, h, s or u. The two equalities are solved by Newton's method in (δ′, δ″) from the fluid's ancillary equations, stepping in from 0.1 % below the critical temperature when closer than that. Saturation is supported up to a limit about 0.04 mK below the critical temperature; closer than that, the tool reports that the liquid and vapour cannot be resolved. Temperature and pressure exactly on the saturation line do not fix x, so the tool reports that the quality is not fixed instead of assuming saturated liquid; enter x, v, h, s or u with T or P instead. At 0 °C: P_sat = 292.80 kPa, h_fg = 198.60 kJ/kg; at 40 °C: P_sat = 1016.59 kPa, h_fg = 163.02 kJ/kg. Sources: Akasaka, J. Therm. Sci. Technol. 3, 442–451 (2008); Cengel & Boles, Thermodynamics: An Engineering Approach, 8th ed., Ch. 3.

Enthalpy and Entropy Reference States

ASHRAE: h′ = 0, s′ = 0 at −40 °C | IIR: h′ = 200 kJ/kg, s′ = 1 kJ/(kg·K) at 0 °C | NBP: h′ = 0, s′ = 0 at 101.325 kPa

Variables: h′, s′ = saturated-liquid enthalpy and entropy at the stated condition. Choosing a reference state adds one constant to every h and u and another to every s, so Δh, Δs and Δu — the quantities in energy balances — are the same in all three. The tool defaults to ASHRAE, the convention of the R-134a tables in Cengel & Boles. At 0 °C, h′ = 51.86 kJ/kg (ASHRAE), 200.00 kJ/kg (IIR) or 34.19 kJ/kg (NBP). Source: offsets applied as in CoolProp's set_reference_state (Bell et al., Ind. Eng. Chem. Res. 53, 2498–2508, 2014).

When to Use This Calculator

  • •Use the R-134a Properties Calculator to check your hand calculations on homework or exam problems — comparing its result with your own working helps identify arithmetic errors before they propagate.
  • •Use it during the early design phase to rapidly iterate on parameters and narrow down feasible configurations before committing time to detailed finite element simulations or full design packages.
  • •Use it when reviewing a colleague's calculation or checking a vendor's data sheet for plausibility — a quick sanity check can prevent costly downstream errors.
  • •Use it to generate reference data for a technical report or presentation without manual computation, ensuring consistent, reproducible numbers throughout the document.
  • •Use it in the field when a quick estimate is needed and a full engineering software package is not available.

About This Calculator

The R-134a Properties Calculator is a precision engineering calculation tool designed for students, engineers, and technical professionals. Comprehensive R-134a refrigerant property lookup: enter any two properties to get T, P, v, h, s, u, quality and phase; it reports pairs it cannot resolve All calculations are performed using established engineering formulas from the relevant scientific literature and standards. Follow the units printed beside each field. Where a unit selector is provided, the selected unit is converted internally. Results are computed in your browser without sending data to a server, which keeps your inputs private. This calculator is intended as a supplementary tool for learning and design exploration; always verify results against authoritative references for safety-critical applications.

The Theory Behind It

R-134a (1,1,1,2-Tetrafluoroethane, CH₂FCF₃) is a hydrofluorocarbon (HFC) refrigerant that replaced R-12 (CFC) in automotive air conditioning and medium-temperature refrigeration applications following the Montreal Protocol's CFC phaseout. R-134a has zero ozone depletion potential (unlike CFCs) but has a global warming potential (GWP) of 1430, making it a target for replacement under the Kigali Amendment to the Montreal Protocol. Its thermodynamic properties are well-characterized in ASHRAE and NIST databases, with the most accurate formulation being the Tillner-Roth and Baehr (1994) equation of state, adopted by NIST REFPROP. Key properties at standard conditions: normal boiling point −26.1°C (just below the freezing point of water, making it unsuitable for low-temperature refrigeration), critical temperature 101.06°C, critical pressure 4.059 MPa, molecular weight 102.03 g/mol. The vapor pressure curve sets the relationship between evaporator temperature and pressure: at 0°C, P_sat ≈ 293 kPa; at 40°C, P_sat ≈ 1017 kPa. For a vapor-compression refrigeration cycle, these pressures define the low and high pressure sides of the system. The latent heat of vaporization is 198.6 kJ/kg at 0°C, relatively high for an HFC and giving good cooling capacity per unit mass flow. Specific heat of saturated liquid is about 1.34 kJ/(kg·K) and of saturated vapor 0.90 kJ/(kg·K) at 0°C. The saturation dome is wide, allowing substantial superheat and subcooling without crossing saturation. The calculator evaluates the Tillner-Roth and Baehr equation of state directly for any two known properties within its stated range, covering compressed liquid, saturated mixtures, superheated vapor and supercritical states, with a selectable ASHRAE, IIR or NBP enthalpy reference; for a few pairs it reports that the state is ambiguous or cannot be resolved, for example close to the critical point.

Real-World Applications

  • •Automotive air conditioning: R-134a is the standard refrigerant for mobile AC in most vehicles built after 1994, replacing the ozone-depleting R-12. System designers use the property tables to size components and predict cycle performance.
  • •Domestic refrigerators and freezers: medium-temperature refrigeration (0°C evaporator) uses R-134a for refrigerator applications. Freezers typically use R-404A or other low-temperature refrigerants.
  • •Commercial chillers and heat pumps: water-cooled chillers in commercial HVAC historically used R-134a. Current-generation units often use R-1234yf or other low-GWP alternatives due to climate regulations.
  • •Cascade refrigeration systems: R-134a is the high-temperature stage in cascade systems for ultra-low temperature applications, paired with R-23 or CO₂ for the low temperature stage.
  • •Training and education: R-134a is the most common refrigerant used in university HVAC/refrigeration courses, with extensive published property tables and cycle analysis examples.

Frequently Asked Questions

What is R-134a?

R-134a is 1,1,1,2-tetrafluoroethane (CH₂FCF₃), an HFC refrigerant introduced in the 1990s to replace R-12 (CFC-12) after CFCs were banned due to ozone depletion. R-134a has zero ozone depletion but GWP of 1430, making it a greenhouse gas. It is the standard automotive AC refrigerant and has been widely used in residential refrigeration and medium-temperature commercial systems.

What's the boiling point of R-134a?

The normal (atmospheric) boiling point is −26.1°C at 101.325 kPa. In refrigeration systems, R-134a operates at higher pressures: an evaporator at 0°C runs at about 293 kPa, and a condenser at 40°C runs at about 1017 kPa. The pressure ratio (about 3.5) is typical for mobile AC systems. At atmospheric pressure, R-134a is a gas that rapidly evaporates if released.

Why was R-134a chosen to replace R-12?

R-134a has similar thermodynamic properties to R-12 (boiling point, vapor pressures, cooling capacity), making retrofit of existing systems feasible with minimal hardware changes (new oils, slightly larger evaporators). It has zero ozone depletion potential (R-12 had 1.0) and is non-toxic, non-flammable, and chemically stable. The main drawback is its GWP of 1430, which has led to the current transition to lower-GWP refrigerants like R-1234yf (GWP 4).

What's replacing R-134a?

R-1234yf (2,3,3,3-tetrafluoropropene) is the main replacement for automotive AC, with GWP of about 4 (500x lower than R-134a). R-513A, R-450A, and R-515A are blends used in chillers and commercial refrigeration. Each has trade-offs: R-1234yf is mildly flammable (A2L), R-513A has similar flammability characteristics, and performance varies slightly from R-134a in existing systems.

How do I compute cycle performance with R-134a?

Look up saturated properties at the evaporator and condenser pressures, then compute the vapor-compression cycle states: (1) saturated vapor at evaporator pressure (state 1, compressor inlet); (2) superheated vapor at condenser pressure (state 2, compressor outlet, from isentropic compression or with isentropic efficiency); (3) saturated liquid at condenser pressure (state 3, condenser outlet); (4) two-phase at evaporator pressure (state 4, throttle outlet, constant enthalpy from state 3). Compute COP = (h₁ − h₄)/(h₂ − h₁) from these enthalpies.

Related Concepts

Related Calculators

References & Further Reading

Wikipedia

Industry References

Textbooks

  • Tillner-Roth R, Baehr HD. An International Standard Formulation for the Thermodynamic Properties of 1,1,1,2-Tetrafluoroethane (HFC-134a) for Temperatures from 170 K to 455 K and Pressures up to 70 MPa, 1994. J. Phys. Chem. Ref. Data 23(5), 657–729, doi:10.1063/1.555958.

    The reference equation of state the R-134a values are computed from.

  • Bell IH, Wronski J, Quoilin S, Lemort V. Pure and Pseudo-pure Fluid Thermophysical Property Evaluation and the Open-Source Thermophysical Property Library CoolProp, 2014. Ind. Eng. Chem. Res. 53(6), 2498–2508, doi:10.1021/ie4033999.

    Source of the equation-of-state coefficients (MIT licence) and of the reference values the tool is tested against.

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