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Oil and gas pump component application example using corrosion-resistant powder metallurgy stainless steel
Case Study

Corrosion-Resistant PM Pump Components for Oil & Gas

How powder metallurgy 17-4PH stainless steel replaced cast parts for offshore oil pump, reducing failures by 85% and maintenance costs by 60%.

Note: This page summarizes a representative application example. Results are specific to the described design, validation scope, and production conditions.

Executive Summary

Client: Offshore pumping equipment manufacturer Challenge: Cast pump impellers failing in corrosive saltwater/oil mixture Solution: 17-4PH stainless steel PM impellers with H900 heat treatment Results:

  • Failure rate reduced from 18% to 2.5%
  • Service life increased from 8 months to 48+ months
  • Maintenance costs reduced by 60%
  • Pump efficiency improved 12% (tighter tolerances)

Customer Background

Industry: Offshore oil & gas production Application: High-pressure saltwater injection pumps Environment:

  • 150 bar (2,175 psi) operating pressure
  • Seawater + crude oil mixture
  • Chloride content: 35,000 ppm
  • Temperature: 40-80 deg C
  • Abrasive particles present

Original Design: Investment cast 316 stainless steel impeller


The Challenge

Problem 1: Premature Corrosion Failure

  • Issue: Pitting corrosion on impeller vanes within 6-8 months
  • Root Cause: Cast 316 SS had carbide segregation and micro-porosity
  • Impact: $12,000 per pump failure (replacement + downtime)
  • Frequency: 18% annual failure rate across 200-pump fleet

Problem 2: Dimensional Inconsistency

  • Issue: Cast parts had +/-0.5mm tolerance variation
  • Impact: Reduced pump efficiency, vibration issues
  • Cost: 8-12% efficiency loss = higher energy costs

Problem 3: Long Lead Times

  • Issue: Investment casting required 12-16 weeks
  • Impact: Expensive inventory of spare parts needed

SinterWorks PM Solution

Material Selection: 17-4PH Stainless Steel

Why 17-4PH instead of 316L?

  • Higher strength: 1100 MPa vs 650 MPa
  • Better pitting resistance in chlorides
  • Precipitation hardenable (H900 condition = 40-44 HRC)
  • Excellent corrosion-fatigue resistance

Manufacturing Process

  1. Powder Compaction: High-density compaction (7.2 g/cm3 green density)
  2. Sintering: 1350 deg C in high-vacuum furnace
  3. Solution Treatment: 1040 deg C to rapid cool
  4. Aging (H900): 480 deg C for 4 hours to 42 HRC hardness
  5. Precision Sizing: Achieve +/-0.05mm tolerance
  6. Surface Polishing: Ra 0.8 um (reduce flow turbulence)

Design Optimizations

  • Vane thickness increased 20% (PM enables complex geometry)
  • Flow channels optimized via CFD simulation
  • Mounting holes sized to +/-0.03mm (tighter than cast)

Testing & Validation

Laboratory Corrosion Testing

Test Method: ASTM G48 (Pitting resistance) Results:

  • 17-4PH PM: 45 CPT (Critical Pitting Temperature)
  • Cast 316 SS: 28 CPT
  • Conclusion: 17-4PH 60% more resistant to pitting

Salt Spray Testing (ASTM B117)

  • 2000 hours exposure
  • PM parts: No visible pitting
  • Cast 316 parts: Pitting depth 0.3-0.8mm

Mechanical Testing

PropertyPM 17-4PH H900Cast 316 SSImprovement
Tensile Strength1150 MPa620 MPa+85%
Yield Strength1050 MPa350 MPa+200%
Hardness42 HRC88 HRB (~18 HRC)+133%
Impact Resistance35 J80 J-56% (trade-off)

Production Implementation

Pilot Trial (50 Units)

  • Duration: 12 months field testing
  • Failure Rate: 0% (vs 18% baseline)
  • Average Service Life: 24 months (still running at trial end)

Full Production Rollout

  • Volume: 200 impellers/year
  • Lead Time: 6-8 weeks (50% faster than casting)
  • Quality Consistency: Cpk 1.67 (tight dimensional control)

Results Achieved

Performance Improvements

MetricBefore (Cast 316)After (PM 17-4PH)Improvement
Service Life8 months avg48+ months+500%
Failure Rate18% annual2.5% annual-86%
Pump Efficiency72%84%+12%
Dimensional Accuracy+/-0.5mm+/-0.05mm10x better
Surface FinishRa 3.2 umRa 0.8 um4x smoother

Cost Savings

  • Maintenance Cost Reduction: $432,000/year (200-pump fleet)
    • Fewer replacements: $240,000/year saved
    • Reduced downtime: $192,000/year saved
  • Energy Savings: $85,000/year (improved efficiency)
  • Inventory Reduction: $120,000 (fewer spare parts needed)

Total Annual Savings: $637,000 PM Part Cost Premium: 35% higher per unit ROI: 14 months


Get Corrosion-Resistant PM Components

SinterWorks specializes in PM parts for oil & gas applications:

  • 17-4PH, 316L, and custom stainless alloys
  • Full-density sintering + heat treatment
  • Corrosion testing capabilities (salt spray, ASTM G48)
  • Small to medium production volumes

Request a quote: Upload your pump component drawings for free evaluation.


Frequently Asked Questions

Why not use 316L stainless instead of 17-4PH?

316L has better overall corrosion resistance, but lower strength (650 vs 1150 MPa). For high-pressure pumps with chloride exposure, 17-4PH offers the best balance.

Can PM match the size of investment castings?

Typically up to 300mm diameter. For larger parts, casting may still be necessary, or multiple PM parts can be joined.

How do you ensure no porosity in PM parts?

High-density compaction (>7.0 g/cm3), vacuum sintering at 1350 deg C, and optional HIP (Hot Isostatic Pressing) for critical applications.

Need Help Reviewing a Corrosion-Sensitive Pump Component?

We can review pressure load, chloride exposure, tolerance needs, and material options to judge whether a PM route fits your pump hardware.

  • DFM review support
  • Material and process guidance
  • Quotation feedback within 24-48 hours