Complete centrifugal-pump hydraulic design calculations covering rated flow, velocities, friction losses, total differential head, system curve, NPSH, power, motor rating, BEP position, minimum flow, shutoff pressure, affinity laws and specific speed. Every calculator includes browser-local calculation history.
Clickable centrifugal pump workflow
Centrifugal Pump Design Calculation Sequence
Follow the stages in order. Each calculation button opens the existing pump calculator.
Confirm duty, system curve, NPSH, power, motor, minimum-flow protection, shutoff conditions, mechanical configuration and applicable project/API requirements.
Deliverables: calculation note, datasheet, system curve, MR and TBE inputs.
Engineering boundary: this sequence supports calculation planning and preliminary review. Final selection remains subject to project requirements, verified operating cases, manufacturer curves and formal engineering review. Decision cards identify review stages, not automatic acceptance checks.
Interactive performance review
Centrifugal Pump Performance Curves
Enter representative vendor-curve anchors to visualize pump head, system head, efficiency, absorbed power and NPSH required over the operating range. These generated curves are screening approximations and must be replaced by manufacturer-tested curves for final selection.
Curve Inputs
Vendor curve data
Overlay Multiple Pump Curves
Import vendor curves from CSV or type them into a table, compare pump alternatives on the same charts, change each curve's colour, and export the combined dataset as CSV.
CSV columns:pump,flow,head,efficiency,power,npshr,flow_unit,head_unit,power_unit. Required: pump, flow, head. Optional performance columns may be left blank.
Pump headSystem headBEPIllustrative POR: 70–120% BEP
How to use the curves
Confirm the duty point lies on the vendor head curve and near the intended operating region.
Verify normal and rated flow relative to BEP, POR and AOR stated by the manufacturer.
Check absorbed power through runout against the selected motor rating.
Compare system NPSHA with vendor NPSHR plus the project-required margin at every operating case.
Check shutoff head, minimum continuous flow, runout flow and maximum impeller diameter separately.
Centrifugal Pump Preliminary Selection
Preliminary pump configuration and applicable industry standard. Final selection requires vendor confirmation and engineering review.
Preliminary planning only. Confirm suction filling, acceleration head where applicable, pulsation, viscosity effects, starting torque, materials and pressure protection with the manufacturer. Do not operate against a blocked discharge without suitable pressure protection.
Preliminary Pump Selection Tool
Enter the duty and fluid properties to obtain a pump-family shortlist with reasons. This is a transparent qualitative screening tool, not a vendor model selector or design approval.
Selection History
Selection basis and limitations
Rule order: metering objective; dry-running requirement; abrasive/solids duty; hygienic or shear-sensitive service; clean lubricating service; otherwise a multi-family shortlist. No universal pressure, temperature, flow, viscosity or particle-size capability limits are assumed. Numerical values define the duty and review checklist, not certified family capability. Density and viscosity are also used to calculate kinematic viscosity. No confidence percentage or model guarantee is implied.
Important: Results are preliminary and do not replace API, ASME, IEC, ISO, project specifications, vendor guarantees, process simulation or a formal design review. Verify units and use absolute pressure for gas calculations.
Equation and unit references: SI conversion practice follows NIST guidance; pump-assessment context follows the U.S. Department of Energy MEASUR resources; ideal-gas compressor relations follow standard isentropic relations described by NASA Glenn Research Center.