Welcome To Know Our Products, We Can Offer You High Quality Products!
WhatsApp / WeChat:
Email:
Welcome To Know Our Products, We Can Offer You High Quality Products!
WhatsApp / WeChat:
Email:
Effect of Impeller Inlet Edge Thinning on Efficiency of 6/4D-AH Slurry Pump: CFD Simulation and Field Validation
Release time:
2026-05-12
Author:
Source:
Abstract
Effect of Impeller Inlet Edge Thinning on Efficiency of 6/4D-AH Slurry Pump: CFD Simulation and Field Validation
Subtitle: Thinning the inlet edge by 2-4mm during impeller repair can increase efficiency by 1.5%-3%, but excessive thinning (>6mm) induces cavitation – optimal thinning amount and measured data
Introduction
The 6/4D-AH is a classic AH series slurry pump (150mm discharge, 100mm inlet), widely used in mill discharge, cyclone feed, and tailings transport. After prolonged operation, the impeller inlet edge often becomes blunt or develops notches due to cavitation or wear. During field repair, maintenance personnel typically grind the inlet edge to restore a streamlined profile. This seemingly simple operation significantly affects pump performance: moderate thinning reduces inlet shock losses and improves efficiency; excessive thinning reduces inlet area, increases velocity, induces cavitation, reduces efficiency, and shortens life.
Hebei Xingou Machinery Equipment Co., Ltd. has quantified the effects of different thinning amounts on 6/4D-AH impeller efficiency, head, and NPSHr through CFD simulation and field testing. This article presents simulation data, the optimal thinning range (2-4mm), and repair guidelines.
1. Purpose and Risks of Inlet Edge Thinning
1.1 Why Thin the Inlet Edge?
| Reason | Description |
|---|---|
| Restore streamlined shape | Cavitation or wear makes the edge blunt; thinning restores smooth transition |
| Reduce inlet shock | Optimized inlet angle reduces hydraulic losses |
| Improve suction performance | Moderate thinning increases inlet area, reduces velocity |
1.2 Risks of Excessive Thinning
| Risk | Mechanism |
|---|---|
| Increased cavitation | Higher velocity lowers local pressure below vapor pressure |
| Reduced efficiency | Flow separation and vortex losses increase |
| Reduced blade strength | Thinned edge is prone to fatigue fracture |
| Head drop | Deteriorated inlet conditions affect overall performance |
2. CFD Simulation Setup
2.1 Model and Conditions
| Parameter | Value |
|---|---|
| Pump model | 6/4D-AH |
| Impeller diameter | 380 mm |
| Number of blades | 5 |
| Rated speed | 1450 rpm |
| Design flow | 180 m³/h |
| Medium | Clean water (to exclude particle effects) |
| Turbulence model | SST k-ω |
2.2 Thinning Scenarios
Thinning was applied to the pressure side of the inlet edge. Five scenarios were compared:
| Case | Thinning amount Δt (mm) | Note |
|---|---|---|
| A | 0 (original) | Baseline |
| B | 2 | Mild |
| C | 4 | Moderate (recommended) |
| D | 6 | Severe |
| E | 8 | Excessive |
3. Simulation Results
3.1 Efficiency Change
| Case | Δt (mm) | Efficiency (%) | Change vs. baseline | NPSHr (m) | Change |
|---|---|---|---|---|---|
| A | 0 | 68.5 | Baseline | 5.2 | Baseline |
| B | 2 | 69.3 | +0.8% | 5.3 | +0.1 |
| C | 4 | 70.1 | +1.6% | 5.5 | +0.3 |
| D | 6 | 69.5 | +1.0% | 6.0 | +0.8 |
| E | 8 | 67.8 | -0.7% | 7.2 | +2.0 |
Conclusions:
Moderate thinning (2-4 mm) improves efficiency by 0.8%-1.6%.
Optimal thinning is 4 mm, giving the highest efficiency gain (+1.6%).
Thinning beyond 6 mm reduces efficiency and significantly increases NPSHr (cavitation risk).
3.2 Flow Field Analysis
| Δt (mm) | Inlet flow characteristics |
|---|---|
| 0 | Blunt edge, minor flow separation |
| 4 | Smooth streamlines, minimal inlet shock, uniform velocity |
| 8 | Very sharp edge, high local velocity, low‑pressure zone, incipient cavitation |
4. Field Validation Case
Background: A 6/4D-AH pump at an iron ore concentrator had an impeller with notches on the inlet edge due to cavitation. Hebei Xingou Machinery recommended thinning the inlet edge to 4mm during repair, and performance was tested before and after.
Field test data (same duty: flow 180 m³/h, speed 1450 rpm):
| Parameter | Before repair (notched) | After repair (thinned 4mm) | Change |
|---|---|---|---|
| Pump efficiency | 66.2% | 68.5% | +2.3% |
| Motor current (A) | 212 | 198 | -6.6% |
| Vibration (mm/s) | 3.8 | 3.2 | -16% |
| NPSHa (field estimate) | 5.8 m | 6.0 m | Acceptable |
Conclusion: Thinning by 4mm improved efficiency by 2.3 percentage points, reduced current by 6.6%, and caused no cavitation. Results align with CFD trends.
5. Thinning Procedure
5.1 Tools
| Tool | Purpose |
|---|---|
| Angle grinder (with grinding disc) | Rough shaping |
| Rotary burr (conical) | Fine profiling |
| Sandpaper (120#, 240#, 400#) | Polishing |
| Template or profilometer | Check blade profile |
5.2 Steps
| Step | Action | Key points |
|---|---|---|
| ① Mark | Mark thinning zone on inlet edge (10-15mm inward) | Maintain symmetry |
| ② Rough grind | Use angle grinder to reach target thickness (2-4mm) | Leave 0.5mm stock |
| ③ Fine shape | Use rotary burr to create smooth rounded contour | Avoid sharp corners |
| ④ Polish | Sand progressively to Ra ≤1.6 μm | Reduce flow resistance |
| ⑤ Inspect | Compare blade profiles; ensure thinning amount consistent | Variation ≤0.5mm |
| ⑥ Balance | Perform static balance after thinning | Prevent vibration |
5.3 Precautions
| Point | Note |
|---|---|
| Thinning ≤4mm | >6mm increases cavitation risk significantly |
| Maintain inlet angle | Do not change blade inlet angle |
| Symmetrical grinding | All blades must be thinned equally; otherwise imbalance |
| Check NPSHr after thinning | If cavitation occurs, reduce speed or increase suction pressure |
6. Summary of Thinning Effects
| Δt (mm) | Efficiency change | NPSHr change | Recommendation |
|---|---|---|---|
| 0 | Baseline | Baseline | Factory condition |
| 2 | +0.8% | +0.1 m | Safe, acceptable |
| 4 | +1.6% | +0.3 m | Optimal |
| 6 | +1.0% | +0.8 m | Diminishing gain, higher cavitation risk |
| 8 | -0.7% | +2.0 m | Not recommended |
Conclusion
Thinning the impeller inlet edge during repair of a 6/4D-AH slurry pump can improve efficiency. CFD simulation and field validation show that thinning by 2-4 mm increases efficiency by 0.8%-1.6%, with 4 mm being optimal. Thinning beyond 6 mm reduces efficiency and significantly increases cavitation risk. Repair should follow proper procedures, maintain symmetry, and include static balancing. Hebei Xingou Machinery Equipment Co., Ltd. offers impeller repair guidance and CFD support. Please contact us.
Key words:
6/4D-AH slurry pump, impeller inlet thinning, pump efficiency improvement, CFD simulation, cavitation prevention, impeller repair, streamlined profile, Hebei Xingou Machinery, slurry pump impeller, thinning procedure
Recommend Reading
The New Option for your Old Warman Slurry Pump
2026-03-23
Performance Benefits of Ceramic Wet Parts in High-Abrasion Slurry Pumps
2026-01-23
How to Choose the Right Slurry Pump Parts for Industrial Applications
2025-12-25






