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Corrosion & Materials for Desalination Intakes

Selecting alloys and non-metallics that survive warm, high-chloride seawater for the design life of a desalination intake — super-duplex, super-austenitic, titanium, GRP and HDPE, matched to duty, temperature and galvanic compatibility.

Warm Chloride Seawater Is the Toughest Corrosion Duty

Desalination intakes handle warm, fully-aerated, high-chloride seawater — the classic environment for pitting and crevice corrosion of stainless steels and for galvanic attack between dissimilar metals. The wrong material does not fail gracefully: it pits, perforates and contaminates the feed, and a leak in a buried intake line is expensive to find and fix. Reynolds & Bauhm selects wetted materials on pitting resistance (PREN), temperature, mechanical duty and lifecycle cost, and engineers the galvanic and cathodic-protection details so the whole intake reaches its design life.

Alloys & Non-Metallics for Seawater

MaterialPREN / classWhere used
Super-duplex (S32750)PREN > 40Pump casings, valves, high-duty pipework
Super-austenitic 6Mo (254 SMO)PREN ~43Warm seawater, fasteners, heat-exchange
Titanium (Gr.2)Effectively immuneHeat-exchanger plates, critical wetted parts
Cu-Ni 90/10Inherently anti-foulingPipework where biofouling resistance helps
GRP / GRENon-metallicLarge-bore intake pipe, tanks, sumps
HDPENon-metallicBuried/marine intake pipelines
316/316L stainlessPREN ~24 — avoidPits & crevice-corrodes in warm seawater

Beyond the Alloy: Getting the System Right

Galvanic Compatibility

Dissimilar metals in seawater drive galvanic corrosion of the less-noble part. We map the galvanic series across the system and isolate, match or protect accordingly.

Cathodic Protection

Sacrificial anodes or impressed-current CP protect buried and submerged steel intake structures, screens and pump bowls where coatings alone are not enough.

Coatings & Linings

Glass-flake epoxy and rubber linings protect carbon-steel structures cost-effectively, with detailing to avoid holidays and crevices at welds and flanges.

Temperature Margin

Critical pitting/crevice temperatures fall with chloride and rise with PREN. We select with margin above the warmest expected seawater, not the average.

Biofouling Interaction

Material choice and biofouling control are linked — Cu-Ni resists settlement, while smooth non-metallics ease cleaning. We design them together.

Biofouling Control

Lifecycle Cost

The cheapest alloy is rarely the cheapest intake. We balance capital, maintenance and the cost of failure across the asset’s design life.

Specifying materials for a desalination intake?

Give us the seawater temperature, chloride and the duty — we’ll produce a wetted-materials schedule and the galvanic/CP strategy for a full-design-life intake.

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