Pressure Vessel Volume Calculator
Calculate internal volume of horizontal/vertical pressure vessels including cylindrical shell and 2:1 elliptical heads.
Introduction
Calculate the total internal volume of a pressure vessel including the cylindrical shell and two 2:1 elliptical ASME heads. Enter the vessel diameter and shell length (tangent-to-tangent) to get volume in liters, cubic meters, and gallons. This calculator follows ASME BPVC Section VIII practice for 2:1 elliptical head volume (V_head = pi x D^3 / 24) and is used for vessel sizing, capacity planning, reactor volume estimation, and separator design. Shell volume uses V = pi x (D/2)^2 x L with the straight tangent-to-tangent length; head volume is added automatically.
How This Calculator Works
Shell volume = π(D/2)² × L. Two 2:1 elliptical heads ≈ 2 × (πD³/24) = πD³/12. ×1000 converts m³ to liters.
Total vessel volume = Shell Volume + 2 x Head Volume. Shell Volume = pi x (D/2)^2 x L. Each 2:1 Elliptical Head Volume = pi x D^3 / 24. The calculator uses D and L in meters and converts to liters (x1000). For other head types (hemispherical, torispherical), use the Pressure Vessel Engineering Hub reference tables.
Step-by-step process:
- Enter your input values in the calculator above
- The engine converts all inputs to SI base units (meters, kg, Pa)
- The formula is evaluated:
pi * (diameter/2)^2 * height * 1000 + pi * diameter^3 / 12 * 1000 - Result is formatted with the appropriate unit and precision
Calculation Example
Head Types and Volume Formulas
2:1 Elliptical (ASME standard, most common): V = pi x D^3 / 24 per head. Head depth = D/4.
Hemispherical: V = pi x D^3 / 12 per head. Head depth = D/2.
Torispherical (ASME F&D): V ≈ 0.10 x D^3 per head (approximate, depends on knuckle radius).
The engine uses the 2:1 elliptical head volume. For hemispherical heads multiply the head allowance by 2; for torispherical heads use about 0.10 x D^3 per head for preliminary estimates.
Worked Example: 3 m x 8 m Horizontal Vessel
Inputs: D = 3 m, shell length L = 8 m (tangent-to-tangent), 2:1 elliptical heads.
Shell volume = pi x (1.5)^2 x 8 = 56.55 m3.
Two heads = pi x 27 / 12 = 7.07 m3. Total = 63.62 m3 = 63,620 liters = 16,805 US gallons.
The two 2:1 heads add about 12.5% to the shell volume at L/D = 2.67.
Unit Conversion Reference
Volume: 1 m3 = 1,000 liters = 264.17 US gallons = 35.315 ft3 = 220.0 UK gallons.
To convert liters to US gallons multiply by 0.2642. A 17,802 L vessel = 4,702 US gallons.
1 US gallon = 3.785 liters; 1 ft3 = 28.32 liters.
Vessel Sizing Considerations
Common pressure vessel proportions: L/D (tangent-to-tangent) from 2.5 to 5 for horizontal separators; vertical vessels often sized by required liquid hold-up time.
Operating fill is typically 80-90% of total volume for liquid service; gas service uses the remaining vapor space.
Nozzle and internal volumes are normally ignored (less than 1% of total). The 2:1 elliptical head depth is D/4, so overall length = T/T length + D/2.
Shell Volume Per Meter Reference
For quick capacity checks, remember the shell volume per meter of length for common diameters (shell only, V/m = pi x (D/2)^2):
D = 1.0 m: 0.785 m3/m (785 L/m).
D = 1.5 m: 1.767 m3/m (1,767 L/m).
D = 2.0 m: 3.142 m3/m (3,142 L/m).
D = 2.5 m: 4.909 m3/m (4,909 L/m).
D = 3.0 m: 7.069 m3/m (7,069 L/m).
D = 4.0 m: 12.566 m3/m (12,566 L/m).
To include 2:1 elliptical heads, add pi x D^3 / 12 for the pair (about 0.21 x D^2 per meter at L/D = 1). A 3 m diameter vessel with 6 m shell: 7.069 x 6 + 7.07 = 49.48 m3, matching the worked example above.
Engineering Applications
- •ASME pressure vessel sizing and capacity
- •Chemical reactor volume estimation
- •Compressed gas storage vessel design
- •Separator and scrubber capacity planning
- •Process vessel sizing for plant design
- •Liquid hold-up time and operating volume checks
Frequently Asked Questions
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