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Effect of Impeller Inlet Edge Thinning on Efficiency of 6/4D-AH Slurry Pump: CFD Simulation and Field Validation

Release time:

2026-05-12

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Abstract

Effect of 6/4D-AH slurry pump impeller inlet edge thinning on efficiency: CFD simulation and field validation show 4mm thinning improves efficiency by 1.6%; exceeding 6mm induces cavitation. Optimal thinning amount and repair procedure.

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.

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1. Purpose and Risks of Inlet Edge Thinning

1.1 Why Thin the Inlet Edge?

ReasonDescription
Restore streamlined shapeCavitation or wear makes the edge blunt; thinning restores smooth transition
Reduce inlet shockOptimized inlet angle reduces hydraulic losses
Improve suction performanceModerate thinning increases inlet area, reduces velocity

1.2 Risks of Excessive Thinning

RiskMechanism
Increased cavitationHigher velocity lowers local pressure below vapor pressure
Reduced efficiencyFlow separation and vortex losses increase
Reduced blade strengthThinned edge is prone to fatigue fracture
Head dropDeteriorated inlet conditions affect overall performance


2. CFD Simulation Setup

2.1 Model and Conditions

ParameterValue
Pump model6/4D-AH
Impeller diameter380 mm
Number of blades5
Rated speed1450 rpm
Design flow180 m³/h
MediumClean water (to exclude particle effects)
Turbulence modelSST k-ω

2.2 Thinning Scenarios

Thinning was applied to the pressure side of the inlet edge. Five scenarios were compared:

CaseThinning amount Δt (mm)Note
A0 (original)Baseline
B2Mild
C4Moderate (recommended)
D6Severe
E8Excessive


3. Simulation Results

3.1 Efficiency Change

CaseΔt (mm)Efficiency (%)Change vs. baselineNPSHr (m)Change
A068.5Baseline5.2Baseline
B269.3+0.8%5.3+0.1
C470.1+1.6%5.5+0.3
D669.5+1.0%6.0+0.8
E867.8-0.7%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
0Blunt edge, minor flow separation
4Smooth streamlines, minimal inlet shock, uniform velocity
8Very 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):

ParameterBefore repair (notched)After repair (thinned 4mm)Change
Pump efficiency66.2%68.5%+2.3%
Motor current (A)212198-6.6%
Vibration (mm/s)3.83.2-16%
NPSHa (field estimate)5.8 m6.0 mAcceptable

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

ToolPurpose
Angle grinder (with grinding disc)Rough shaping
Rotary burr (conical)Fine profiling
Sandpaper (120#, 240#, 400#)Polishing
Template or profilometerCheck blade profile

5.2 Steps

StepActionKey points
① MarkMark thinning zone on inlet edge (10-15mm inward)Maintain symmetry
② Rough grindUse angle grinder to reach target thickness (2-4mm)Leave 0.5mm stock
③ Fine shapeUse rotary burr to create smooth rounded contourAvoid sharp corners
④ PolishSand progressively to Ra ≤1.6 μmReduce flow resistance
⑤ InspectCompare blade profiles; ensure thinning amount consistentVariation ≤0.5mm
⑥ BalancePerform static balance after thinningPrevent vibration

5.3 Precautions

PointNote
Thinning ≤4mm>6mm increases cavitation risk significantly
Maintain inlet angleDo not change blade inlet angle
Symmetrical grindingAll blades must be thinned equally; otherwise imbalance
Check NPSHr after thinningIf cavitation occurs, reduce speed or increase suction pressure


6. Summary of Thinning Effects

Δt (mm)Efficiency changeNPSHr changeRecommendation
0BaselineBaselineFactory condition
2+0.8%+0.1 mSafe, acceptable
4+1.6%+0.3 mOptimal
6+1.0%+0.8 mDiminishing gain, higher cavitation risk
8-0.7%+2.0 mNot 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.

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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

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