Choosing the wrong pump material is the single most expensive mistake in chemical process pump replacement. A Hastelloy C impeller installed in the wrong application can fail in weeks. A 316SS casing in hot sulfuric acid can perforate within days. Understanding material chemistry is not optional, it is the foundation of reliable pump specification.
This guide compares the five most common wet-end materials used in Goulds 3196 and Durco Mark III replacement parts. You will learn which alloy to specify for which chemical service, what each material costs relative to baseline, and how to spot material substitution risks.
Material Overview: The Five Alloys You Will Encounter Most Often
| Material | ASTM Cast Grade | Relative Cost | Best For | Do NOT Use In |
|---|---|---|---|---|
| 316 Stainless Steel | CF8M | 1.0x (baseline) | Water, mild chemicals, dilute acids at ambient temp | Chlorides above 50 ppm, sulfuric acid, HCl |
| CD4MCuN (Duplex SS) | A890 Gr.1B | 2.5-3.5x | Sulfuric acid, phosphoric acid, FGD, erosive slurries | Strong oxidizing acids, hot HNO3 |
| Alloy 20 (Carpenter 20) | CN7M | 4.0-5.5x | Sulfuric acid all concentrations to 75C, nitric acid | Hydrochloric acid, wet chlorine |
| Hastelloy C-276 | CW12MW | 6.0-8.0x | Oxidizing acids, wet chlorine, mixed acid streams | Not needed for mild service, over-specification waste |
| Titanium Gr.2 / Gr.12 | B367 C-2/C-12 | 5.5-7.5x | Chloride service, seawater, chlorine dioxide, hypochlorite | Anhydrous chlorine, fuming nitric acid, fluoride-containing media |
316 Stainless Steel (CF8M): The Workhorse
CF8M is the default material for approximately 60-70% of ANSI chemical process pump applications. It offers adequate corrosion resistance for a broad range of mild chemical services at the lowest cost point.
Chemical Compatibility
- Good: Fresh water, demineralized water, most organic solvents, dilute caustic (NaOH), dilute nitric acid, phosphoric acid (pure, ambient), fatty acids, amines
- Marginal: Sulfuric acid below 5% concentration at ambient temperature, acetic acid, formic acid
- Unacceptable: Hydrochloric acid (any concentration), seawater/brine, sulfuric acid above 10% or elevated temperature, wet chlorine, hypochlorite solutions
The Chloride Problem
316SS is vulnerable to chloride-induced pitting and stress corrosion cracking (SCC). The risk threshold is approximately 50 ppm chlorides at ambient temperature, dropping to near-zero at temperatures above 60C. If your process fluid contains chlorides and operates warm, skip 316SS entirely and move to duplex or titanium.
CD4MCuN (Duplex Stainless): The Sweet Spot for Tough Services
CD4MCuN (ASTM A890 Grade 1B) is a duplex stainless steel that combines the corrosion resistance of high-alloy austenitic grades with the strength and erosion resistance of ferritic grades. For pump maintenance providers, it is often the optimal upgrade from 316SS when the process environment is too aggressive for standard stainless but the cost of Hastelloy is hard to justify.
Why CD4MCuN Works Well in ANSI Pumps
- PREN (Pitting Resistance Equivalent Number): 38-42, compared to 25-28 for 316SS. Significantly better resistance to pitting and crevice corrosion.
- Hardness: 255-290 HB, roughly 30% harder than 316SS (150-180 HB). This means better erosion resistance in slurry and high-velocity services.
- Sulfuric Acid Resistance: Excellent in concentrations up to 80% at temperatures up to 50C, and in concentrations above 95% at higher temperatures.
Best Applications for CD4MCuN
- Flue gas desulfurization (FGD) slurry recirculation
- Phosphoric acid production (wet process, 30-54% P2O5)
- Sulfuric acid dilution and cooling loops
- Pulp and paper black liquor / green liquor services
- Any erosive service where 316SS wears too fast
Alloy 20 (CN7M): The Sulfuric Acid Specialist
Alloy 20 (also known as Carpenter 20) was developed specifically for sulfuric acid service. It handles sulfuric acid across almost the full concentration range at temperatures up to 75C, making it the material of choice for chemical plants with diverse acid handling requirements.
When to Specify Alloy 20
- Sulfuric acid, 0-98% concentration, up to 75C
- Nitric acid, up to 30% at elevated temperatures
- Phosphoric acid with fluoride impurities
- Mixed acid streams common in chemical processing
When NOT to Use Alloy 20
- Hydrochloric acid (HCl) at any concentration above 1%
- Wet chlorine gas or chlorine dioxide bleaching
- Chloride-rich environments at elevated temperatures
Hastelloy C-276 (CW12MW): The Universal Acid Handler
Hastelloy C-276 is the most versatile corrosion-resistant nickel alloy available for chemical pump service. It handles both oxidizing and reducing acids, making it the safest choice when the process chemistry is complex, variable, or not fully characterized.
Capabilities
- Excellent resistance to wet chlorine gas, hypochlorite, and chlorine dioxide
- Handles ferric and cupric chlorides that devastate most stainless steels
- Resists both sulfuric and hydrochloric acids across wide concentration and temperature ranges
- Superior resistance to pitting, crevice corrosion, and stress corrosion cracking
- PREN (Pitting Resistance Equivalent) of 65+, the highest among pump casing alloys
Cost Justification
At 6-8x the cost of 316SS, Hastelloy C-276 is never specified casually. However, in the right application, it is the only material that will survive. For pump maintenance providers, the key decision is: is this a genuine Hastelloy application, or would CD4MCuN or Alloy 20 suffice?
Titanium (B367 Gr.C-2 / C-12): The Chloride Champion
Titanium is virtually immune to chloride-induced corrosion, making it the definitive choice for seawater, brine, and chlorinated process streams. It also offers excellent resistance to oxidizing acids like nitric acid and chlorine dioxide.
Key Properties
- Chloride resistance: Essentially immune at all concentrations and temperatures up to 150C
- Seawater: No pitting, no crevice corrosion, no SCC. Indefinite service life.
- Wet chlorine / chlorine dioxide: Excellent resistance, widely used in pulp bleaching circuits
- Nitric acid: Excellent up to 65% concentration at boiling point
- Density advantage: Titanium is 40% lighter than steel, reducing shaft load and bearing wear
Limitations to Know
- Not for anhydrous chlorine: Titanium reacts violently with dry chlorine gas
- Not for fluoride-containing media: Fluoride ions attack titanium’s protective oxide layer
- Not for fuming nitric acid: Above 70% HNO3 at elevated temperatures, titanium can pyrophorically ignite
- Gall-prone: Titanium on titanium sliding contact galls easily. Shaft sleeves and wear rings require special attention
Material Selection Decision Tree
- Does the fluid contain chlorides above 50 ppm?
- YES and temperature above 60C: Go directly to Titanium or Hastelloy C
- YES but ambient temperature: Consider CD4MCuN
- NO: Continue to step 2
- Does the fluid contain sulfuric acid above 5% concentration?
- YES and above 40C: Alloy 20 or CD4MCuN
- YES and above 75C or unknown: Hastelloy C-276
- NO: Continue to step 3
- Is there any hydrochloric acid present?
- YES at any concentration: Hastelloy C-276
- NO: Continue to step 4
- Is the fluid erosive (slurries, high velocity, solids)?
- YES: CD4MCuN (harder, better erosion resistance than 316SS)
- NO: 316SS (CF8M) is likely adequate
Not Sure Which Material You Need?
Send us your process fluid composition, temperature, and pH. Our application engineers will recommend the optimal alloy, with supporting corrosion data, within 24 hours.
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