Centrifugal pump design involves optimizing hydraulic performance, mechanical strength, and material selection to meet specific flow, pressure, and efficiency requirements. Below is a structured breakdown of the design process.
The impeller is the heart of the centrifugal pump, responsible for energy transfer.
| Type | Description | Application |
|---|---|---|
| Closed Impeller | Vanes enclosed between two shrouds | High-efficiency, clean liquids |
| Semi-Open Impeller | One shroud, open on one side | Slurries, mildly abrasive fluids |
| Open Impeller | No shrouds, vanes fully exposed | Slurries, sewage, high solids |
Diameter (D₁, D₂) – Affects head & flow
Vane Angle (β₁, β₂) – Impacts efficiency & pressure
Number of Vanes – Typically 5–9 (fewer vanes = better for solids)
Specific Speed (Nₛ) – Determines impeller shape:
Radial (Low Nₛ, high head)
Mixed Flow (Medium Nₛ)
Axial Flow (High Nₛ, low head, high flow)
Spiral-shaped to convert kinetic energy → pressure.
Cutwater (Tongue) – Minimizes recirculation & vibration.
Diffuser Casings (Used in multistage pumps for higher efficiency).
Suction Nozzle Diameter – Must avoid cavitation (NPSHₐ > NPSHᵣ).
Discharge Nozzle – Sized for desired flow rate.
Shaft Diameter – Calculated based on torque & deflection limits.
Bearings – Usually ball bearings (small pumps) or sleeve bearings (large pumps).
Mechanical Seals (most common for high-pressure)
Gland Packing (low-cost, maintenance-heavy)
| Component | Common Materials | Selection Criteria |
|---|---|---|
| Impeller | Stainless steel (SS316), Bronze, Cast Iron | Corrosion & wear resistance |
| Casing | Cast Iron, Ductile Iron, SS304/316 | Pressure & fluid compatibility |
| Shaft | Carbon Steel, SS420 | Fatigue & torsional strength |
Head vs. Flow Curve – Shows pump performance.
Best Efficiency Point (BEP) – Target operating range.
Avoid Running at Low Flow – Risk of recirculation & overheating.
| Law | Formula | Application |
|---|---|---|
| Flow (Q) ∝ Speed (N) | Q₂/Q₁ = N₂/N₁ | Changing RPM affects flow |
| Head (H) ∝ N² | H₂/H₁ = (N₂/N₁)² | Speed impacts pressure |
| Power (P) ∝ N³ | P₂/P₁ = (N₂/N₁)³ | Higher speed = much more power |
NPSHₐ (Available) = Suction pressure – Vapor pressure
NPSHᵣ (Required) – Must be NPSHₐ > NPSHᵣ to prevent cavitation.
Multiple impellers for high-pressure applications (e.g., boiler feedwater).
Design Tip: Balance axial thrust using opposed impellers or balance drums.
Built-in reservoir to retain liquid for priming.
Used where suction lift is required.
Motor & pump sealed in a single unit for underwater use (e.g., sewage, wells).
CFD (Computational Fluid Dynamics) – Optimizes flow paths.
FEA (Finite Element Analysis) – Checks structural stress.
Pump Sizing Software (e.g., ANSYS, SolidWorks Flow Simulation).
Centrifugal pump design balances hydraulic efficiency, mechanical durability, and material compatibility. Key steps include:
Impeller & casing design for optimal flow & pressure.
Mechanical strength checks (shaft, bearings, seals).
Material selection based on fluid & environment.
Performance validation using affinity laws & NPSH.
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