Case Studies › Downstream Refining
Case StudyDownstream RefiningGulf CoastIndependent · No Chemistry Sold

Gulf Coast refinery eliminates zinc silicate deposition in critical heat exchangers

A >250,000 BPD Gulf Coast refinery was losing production capacity to deposition in critical heat exchangers — including the crude unit overhead trim cooler — despite a well-controlled zinc-phosphate program. The root cause was a salt the standard prediction tools were not built to see.

Unit Served
Refinery · >250,000 BPD
Key Issue
Zinc silicate deposition
Risk
Production loss · Throughput
ROI on Consulting
< 6 hours
Annual Value Delivered
$38.45M / yr
Challenge — What Was Happening

An open recirculating utility cooling system operating on an alkaline zinc-phosphate inhibitor program was fouling critical heat exchangers — including the crude unit overhead trim cooler — causing measurable production capacity loss.

Calcium phosphate was in control. Zinc phosphate was in control. Polymer dispersant dosages were correct by all standard benchmarks. Yet deposit analysis kept confirming significant zinc deposition, with a strong but unexplained silica component that the operating team and incumbent supplier could not reconcile.

The standard monitoring and prediction tools in use tracked zinc and silica as independent parameters — leading the team to assume they were dealing with two separate problems simultaneously.

Intervention — What We Did

Aligned refinery and service-company data across online and offline datasets. Conducted heat-exchanger modeling with time-series overall heat-transfer coefficient (U-coefficient) analysis to quantify fouling progression and timing.

Applied advanced competing-ion saturation modeling — accounting for all scale-forming and scale-inhibiting species simultaneously, not in isolation. Re-interpreted lab deposit analysis with a fresh lens.

Conducted onsite data collection, system evaluation and structured team interviews. Delivered a full engineering root-cause report and root-cause presentation to refinery operations and engineering leadership.

Root Cause Finding

The tools and training in use tracked zinc and silica separately — so the team assumed silica was a different problem. No standard model accounted for zinc silicate as a compound salt.

At alkaline pH with 3 ppm zinc in solution, a swing of just 0.5 cycles of concentration was sufficient to exceed the zinc silicate saturation index and drive bulk deposition in the highest-temperature exchangers. Adjusting design control limits for zinc concentration, cycles of concentration, polymer dispersant ratio, and operating pH — and incorporating zinc silicate into the saturation prediction tools — eliminated the deposition entirely.

$38.45M
annual value delivered · ROI on consulting engagement < 6 hours
Water Saved
202.3M gal / yr
Energy Reduction
1.5% · ~$2.18M / yr
Production Increase
2.5% · ~$36.27M / yr
Prevented Downtime
Not counted
Refinery water-treatment spend is typically less than 1% of operating expenses — and procurement attention is usually focused on reducing chemical cost. An independent, first-principles review can unlock millions in cost savings and production increases, with ROI measured in hours. Your system deserves a second look.

Does your refinery have unexplained heat exchanger fouling?

Independent cooling water program review for refineries and petrochemical facilities. No chemistry sold. No conflicts of interest. ROI typically measured in hours to days.