Turn temperature shifts into usable pressure results instantly. Pick gas, bulk, or restrained-solid mode today. Download tables, review formulas, and validate with examples here.
| Scenario | Inputs | Expected behavior |
|---|---|---|
| Gas in sealed cylinder | Ideal CV; P1=101.325kPa; T1=20°C; T2=80°C | Pressure rises roughly with absolute temperature. |
| High-pressure real gas | Real CV; P1=10MPa; T1=25°C; T2=100°C; Z1=0.90; Z2=0.95 | Z factors adjust pressure beyond ideal behavior. |
| Heated liquid in rigid container | Bulk; K=2200MPa; αv=2.1e-4; T1=20°C; T2=60°C | Thermal pressure depends on K, αv, and ΔT. |
| Restrained steel component | Solid; E=200000MPa; αL=1.2e-5; ν=0.30; ΔT≈100K | Restraint condition can amplify thermal stress. |
When volume and gas amount stay constant, pressure follows absolute temperature:
P₂ = P₁ · (T₂/T₁) and ΔP = P₂ − P₁
A simple compressibility-factor correction uses Z values at each state:
P₂ = P₁ · (T₂/T₁) · (Z₂/Z₁)
For a material prevented from changing volume, a common estimate is:
Pth = K · αv · ΔT and P₂ = P₁ + Pth
A basic restrained estimate uses a constraint factor C:
σ = C · E · αL · ΔT
This tool also supports an optional relaxation percentage to reduce σ when assemblies are not perfectly rigid.
Thermal pressure is the pressure (or stress) change caused by a temperature change when expansion is restricted. In a sealed gas volume, temperature raises molecular energy, increasing pressure. In a rigid liquid-filled container, thermal expansion fights compressibility. In restrained solids, thermal strain becomes mechanical stress.
Use the constant‑volume gas models for sealed vessels where volume does not change. Use the bulk model for fluids or materials in near‑rigid volumes (pipe segments with closed valves, filled cavities, test cells). Use the restrained solid model for components bolted, welded, or captured so free expansion is prevented.
Order‑of‑magnitude values help with quick checks: steel E ≈ 200 GPa, aluminum E ≈ 69 GPa; metals often have αL ≈ 10–25×10−6 1/K. Many liquids have αv around 10−4–10−3 1/K, while bulk modulus K can be hundreds of MPa to a few GPa.
Gas pressure ratios require absolute temperature. For example, heating from 20 °C to 80 °C changes temperature from 293.15 K to 353.15 K, so P₂/P₁ ≈ 1.205. That is about a 20.5% pressure rise at constant volume, before any real‑gas correction.
At elevated pressures or near condensation, ideal behavior can drift. The Z‑factor correction provides a simple improvement when Z data is available: P₂ = P₁·(T₂/T₁)·(Z₂/Z₁). If you do not have Z, setting Z₁ = Z₂ = 1 keeps results consistent with the ideal model.
Thermal stress estimates are sensitive to restraint. This calculator offers uniaxial, biaxial, and triaxial approximations using Poisson ratio ν. A relaxation percentage lets you model partial stress relief from slip, creep, or yielding. Treat these results as screening values, then validate with design standards where needed.
Engineering teams often mix kPa, MPa, bar, atm, and psi. The multi‑unit table helps prevent conversion mistakes and supports documentation. The history log captures timestamped inputs and outputs so you can reproduce results, compare scenarios, and export clean CSV or PDF summaries.
Thermal pressure can exceed component ratings quickly in confined systems. Always compare predicted pressures with allowable limits, include safety margins, and consider relief devices where applicable. If the temperature rise is uncertain, run worst‑case values and record the assumptions for traceability.
Choose the constant‑volume gas model. Use the Z‑factor option if the gas is at high pressure or you have compressibility data. Always enter temperatures in the selected unit; the tool converts to Kelvin internally.
Set Z1 and Z2 to 1.0. That reproduces ideal‑gas behavior. If you later obtain Z values from a chart or dataset, you can rerun the case and compare the difference in P2 and ΔP.
It estimates pressure rise when a material wants to expand with temperature but is confined by a nearly rigid volume. The calculation uses Pth = K·αv·ΔT, where K captures compressibility and αv captures thermal expansion.
Yes. Switch bulk input mode to β, then provide β and its unit. The tool converts β to K using K = 1/β, then applies the same thermal‑pressure relation to compute Pth and the final pressure.
Perfect restraint converts thermal strain directly into stress. Real parts often relieve stress through slip, creep, or yielding. Use the relaxation setting for partial relief and treat the output as a conservative estimate unless validated by detailed analysis.
For bulk and solid modes, the calculator will report the thermal contribution as the primary result. For gas models, P1 is required because the method computes a final pressure from an initial state and a temperature ratio.
Presets are typical values intended for quick checks and learning. Materials vary by grade, temperature, and state. For engineering decisions, replace presets with verified datasheet values and record the source in your report exports.
Important Note: All the Calculators listed in this site are for educational purpose only and we do not guarentee the accuracy of results. Please do consult with other sources as well.