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ANSI Process Pump Metallurgy Guide: Selecting the Right Alloy from 316SS to Titanium

Material Selection: Where Pump Reliability Begins

In chemical process pumping, the material of construction is not just one factor among many — it is the single most important decision you make. Specify the wrong alloy and the pump fails within months — or weeks — regardless of how well it’s designed, manufactured, and installed.

This guide covers every standard and exotic alloy available for ANSI B73.1 process pumps, with practical guidance on when to use each one, what they cost, and what specific chemicals each grade handles best.

Material Grade Quick Reference

Material ASTM/ACI Grade Relative Cost Best For Avoid For
Cast Iron Class 30 0.3× Water, neutral pH Any acid or corrosive service
316 Stainless Steel CF8M 1.0× General chemical, organic acids Strong reducing acids, hot chlorides
CD4MCuN (Duplex) A890 Gr 1B 1.5× Chloride SCC resistance, high strength Strong reducing acids
Alloy 20 CN7M 2.5× Sulfuric acid, mixed acids Hydrochloric acid
Nickel CZ100 3.0× Caustic soda, hot alkaline Acids (except HF)
Titanium B367 Gr C-3 3.5× Chlorides, seawater, bleach Strong reducing acids
Hastelloy C-276 CW2M 4.5× Mixed acids, severe corrosion Hot concentrated HNO₃
Hastelloy B N-12MV 5.0× Hydrochloric acid (all conc.) Oxidizing environments

Service Condition Guide

Chemical / Service Concentration Temperature Recommended Material Alternative
Sulfuric Acid 0-20% Up to 150°F Alloy 20 316SS (very dilute)
Sulfuric Acid 20-70% Up to 200°F Alloy 20 or Hastelloy C High-Si Cast Iron
Hydrochloric Acid Any Up to 150°F Hastelloy B Zirconium
Nitric Acid 0-65% Up to 200°F 304L or 316L Titanium
Caustic Soda 0-50% Up to 250°F Nickel (CZ100) 316SS (low temp only)
Sodium Hypochlorite 0-15% Up to 150°F Titanium Hastelloy C
Seawater / Brine N/A Any Titanium or CD4MCuN Super duplex
Ferric Chloride Any Any Titanium Hastelloy C (moderate temp)

Common Material Selection Mistakes

Mistake 1: Using 316SS for Sulfuric Acid Above 10%

At concentrations above 10% H₂SO₄ and temperatures above 100°F, the passive layer on 316SS breaks down. Use Alloy 20.

Mistake 2: Using 316SS for Hot Chloride Service

Above 140°F, even 50 ppm chlorides can cause catastrophic Cl-SCC in 316SS. Switch to CD4MCuN or Titanium.

Mistake 3: Assuming Hastelloy C Handles Everything

Hastelloy C-276 performs poorly in hot concentrated HNO₃ (use Titanium) and is attacked by HCl above 15% at elevated temperature (use Hastelloy B).

Mistake 4: Overlooking Galvanic Corrosion

A Titanium impeller on a 316SS shaft in seawater will cause rapid shaft corrosion. Always specify compatible material pairs.

Not Sure Which Alloy Your Application Requires?

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