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Torque · Quick Engineering Unit Converter

Seven categories: pressure, dimension, temperature, flow, torque, weight, and velocity. Also available from the floating Quick Unit dock.SI conversion
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Engineering Reference & ASME Code Basis

1. Core Formula & Variable Definitions

ISO 80000-1 (Quantities and Units - General) · NIST SP 811 (Guide for the Use of the International System of Units) · ASME B31.3 (2022 Edition) · / B16.5 (Engineering Units and Conversion Conventions) · ASTM E380 / IEEE SI 10 (American National Standard for Metric Practice)

Ppsi = Pbar × 14.5037738  ·  T°F = T°C × 1.8 + 32  ·  Lmm = Lin × 25.4

1 ft·lb = 1.355817948 N·m  ·  1 m³/h = 4.402867655 GPM  ·  = Q × ρ

ISO 80000-1 Quantities and Units & NIST Special Publication 811 Guide for SI

1 bar 14.5037738 psi (10⁵ Pa)1 inch 25.4 mm (Exact)1 ft·lb 1.355818 N·m1 m³/h 4.402868 US GPM

Precision engineering conversions follow ISO 80000-1 and NIST SP 811 authoritative standards. 1 bar is defined as exactly 100,000 Pa (100 kPa / 0.1 MPa). Exact standard inch-millimetre relationship is defined as 1 in = 25.4 mm (International Yard and Pound Agreement of 1959). Fluid volumetric and mass flow conversions use fluid density ρ at flowing reference temperature (default 1,000 kg/m³ for water).

  • P (Pressure Conversion)1 bar = 14.5037738 psi = 0.10 MPa = 100 kPa = 1.019716 kgf/cm².
  • T (Temperature Conversion)T(°F) = 1.8·T(°C) + 32; T(K) = T(°C) + 273.15; T(°R) = T(°F) + 459.67.
  • L (Length / Dimension)1 inch = 25.4 mm (exact); 1 foot = 0.3048 m; 1 meter = 39.3700787 inches.
  • τ (Torque Conversion)1 ft·lb = 1.355817948 N·m; 1 N·m = 0.737562149 ft·lb; 1 kgf·m = 9.80665 N·m.
  • Q / ṁ (Volumetric & Mass Flow)1 m³/h = 4.402867655 US GPM; Mass flow ṁ (kg/h) = Q (m³/h) × ρ (kg/m³).
  • ρ (Fluid Reference Density)Density used for mass-to-volumetric flow rate translation (kg/m³ or lb/ft³).

2. Allowances, Tolerances & Standards

Field engineering calculations require strict differentiation between gauge and absolute pressures, standard vs normal gas volumes, and preservation of significant digits.

Gauge vs Absolute Pressure (barg vs bara)P_abs = P_gauge + P_atm (1.01325 bar / 14.696 psi)

Pressure gauges read zero at atmospheric ambient. Thermodynamic gas calculations (ideal gas law, compressor sizing) require absolute pressure (bara / psia); hydraulic piping calculations use gauge pressure (barg / psig).

Gas Flow Standard Reference ConditionsNormal (Nm³/h @ 0 °C) vs Standard (Sm³/h / SCFM @ 15 °C or 60 °F)

Normal m³/h (Nm³/h) is referenced to 0 °C (273.15 K) and 1.01325 bar abs per DIN/ISO. Standard m³/h (Sm³/h) is referenced to 15 °C (288.15 K) per ISO 13443. Standard Cubic Feet per Minute (SCFM) uses 60 °F and 14.696 psia.

US Gallon vs UK Imperial Gallon1 US Gallon = 3.7854 L vs 1 UK Gal = 4.5461 L (+20.1%)

American plant nameplates (GPM) refer to US gallons (231 in³ / 3.7854 L). UK / Commonwealth legacy documentation often cites Imperial gallons (4.5461 L); confusing the two leads to a 20.1% flow sizing error.

Rounding & Significant Digit PracticeMaintain 6 Digits in Engines, 2–3 in Reports

All internal conversion arithmetic must use double-precision IEEE-754 factors. Final engineering deliverable reports round pressure to 1 decimal place (bar) or whole number (psi), and thickness to 2 decimal places (mm).

Quick Reference Lookup Table

Pressure quick reference — bar to psi, MPa, and kgf/cm²
InputpsiMPakgf/cm²
1 bar14.5040.101.0197
5 bar72.5190.505.0986
10 bar145.0381.0010.1972
20 bar290.0752.0020.3943
50 bar725.1895.0050.9858
100 bar1450.37710.00101.9716

1 bar = 14.5037738 psi = 0.1 MPa = 1.019716 kgf/cm². Screening values; use the live converter for other magnitudes.

3. Material & Code Limitations

Unit conversions involving material properties (thermal expansion, elasticity, density) depend on physical temperature baselines and reference states.

Material GroupTemperature RangeAllowable Stress / LimitEngineering Notes
Stress & Elastic Modulus Units1 MPa = 1 N/mm² = 10 bar = 145.0377 psi = 0.145038 ksiStandard ASME Section II-D ConversionSI structural stress is expressed in MPa (N/mm²); US customary is ksi (1,000 psi).
Thermal Expansion Coefficient (α)1 × 10⁻⁶ /°C = 0.555556 × 10⁻⁶ /°F (Factor 5/9)Linear Thermal Strain RateConverting thermal expansion coefficients between °C and °F requires multiplying by 5/9 (1.8 inverse).
Liquid Density vs Specific GravitySG = ρ_fluid / ρ_water @ 4 °C (1,000 kg/m³ / 62.428 lb/ft³)Dimensionless Density RatioIn pump hydraulic calculations, water density shifts from 1,000 kg/m³ at 4 °C to 998 kg/m³ at 20 °C and 958 kg/m³ at 100 °C.
Energy, Power & Heat Rate1 kW = 1.341022 HP = 3,412.142 BTU/hr = 859.845 kcal/hrEquipment Mechanical PowerPump brake horsepower (BHP) and heat exchanger duty conversions across international project consortiums.

Code Applicability & Safety Boundaries

  • Prohibition of Dual-Unit Mixing in Governing Formulas: Never mix metric and imperial units within a single empirical code formula (e.g. ASME B31.3 wall thickness or API RP 14E erosion); convert all inputs to the formula's native unit system before evaluation.
  • Absolute Zero Temperature Conversion: When performing thermodynamic gas volume or expansion calculations, always convert to absolute Rankine (°R = °F + 459.67) or Kelvin (K = °C + 273.15).
  • Torque Wrench Scaling Verification: When calibrating pneumatic or hydraulic torque tools, verify whether torque charts cite N·m, ft·lb, or kgf·m to prevent over-torquing flange studs by 35% (1 ft·lb ≈ 1.356 N·m).

4. Step-by-Step Worked Example

Field Verification

Convert an overseas piping data sheet for a high-pressure pump system: internal design pressure P = 35.0 bar gauge, design temperature T = 180.0 °C, volumetric flow rate Q = 150.0 m³/h (water at 180 °C, density ρ = 887.0 kg/m³), and stud bolt tightening torque τ = 450 N·m into US Customary engineering units (psig, °F, US GPM, lb/hr mass flow, and ft·lb torque).

Gauge Pressure (P):35.0 bar gauge (barg)Design Temperature (T):180.0 °CVolumetric Flow (Q):150.0 m³/hFluid Density (ρ @ 180 °C):887.0 kg/m³ (Hot Boiler Feedwater)Bolt Assembly Torque (τ):450.0 N·m
1

Convert Pressure from bar to psig

Formula: P_{\text{psig}} = P_{\text{bar}} · 14.5037738
P_psig = 35.0 × 14.5037738 = 507.632 psi gauge.
Result:P = 507.6\text{ psig} (3.50\text{ MPa / 35.7 kgf/cm}^2)

Standard Class 300 pressure range.

2

Convert Temperature from °C to °F

Formula: T_{^{\circ}\text{F}} = T_{^{\circ}\text{C}} · 1.8 + 32
T_°F = (180.0 × 1.8) + 32 = 324.0 + 32 = 356.0 °F (Absolute T = 453.15 K / 815.67 °R).
Result:T = 356.0\text{ }^{\circ}\text{F}

Exact conversion without rounding errors.

3

Convert Volumetric Flow Rate from m³/h to US GPM

Formula: Q_{\text{GPM}} = Q_{\text{m}^3/\text{h}} · 4.402867655
Q_GPM = 150.0 × 4.402867655 = 660.430 US gpm.
Result:Q = 660.4\text{ US GPM} (41.67\text{ L/s})

Based on 1 US gallon = 3.785411784 L.

4

Calculate Mass Flow Rate in kg/h and Convert to lb/hr

Formula: \dot{m}_{\text{kg/h}} = Q · \rho,\quad \dot{m}_{\text{lb/hr}} = \dot{m}_{\text{kg/h}} · 2.20462262
Mass flow = 150.0 m³/h × 887.0 kg/m³ = 133,050 kg/h. In US pounds: 133,050 × 2.20462262 = 293,325.04 lb/hr.
Result:\dot{m} = 133,050\text{ kg/h} = 293,325\text{ lb/hr}

Density at 180 °C (887 kg/m³) accounts for thermal liquid expansion.

5

Convert Bolt Assembly Torque from N·m to ft·lb

Formula: \tau_{\text{ft}\cdot\text{lb}} = \tau_{\text{N}\cdot\text{m}} · 0.737562149
τ_ft·lb = 450.0 × 0.737562149 = 331.903 ft·lb (or 450 / 1.355817948 = 331.903 ft·lb).
Result:\tau = 331.9\text{ ft}\cdot\text{lb} (45.89\text{ kgf}\cdot\text{m})

Directly dial into torque wrench calibration certificate.

Conclusion: The converted process operating conditions are 507.6 psig design pressure, 356.0 °F design temperature, 660.4 US GPM volumetric flow (293,325 lb/hr mass flow), and 331.9 ft·lb stud bolt makeup torque, fully verified against ISO 80000-1 and NIST standards.

5. Code Limitations & FAQ

barg (bar gauge) is the pressure relative to local atmospheric pressure (gauges read 0.0 at sea level). bara (bar absolute) is the total pressure relative to a perfect absolute vacuum (\(P_{\text{abs}} = P_{\text{gauge}} + 1.01325\text{ bar}\) at sea level). Process piping design pressures on P&IDs and datasheets are almost universally gauge pressures (barg / psig), while thermodynamic thermodynamic gas expansion formulas require absolute pressures (bara / psia).

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