Refining & CDU Overhead Corrosion Protection

Stop Tramp Amine Corrosion at the Refinery Gate.
Detect Scavenger Carryover in Crude & Desalter Water in <5 Minutes.

Unneutralized triazine scavengers in crude feedstocks thermally degrade into free amines (MEA, MMA), forming aggressive amine hydrochloride salts that destroy crude unit overhead condensers. OndaVia’s Quantitative Raman Spectroscopy (QRS) quantifies tramp amines at ppm levels on-site—before corrosive crude enters your distillation columns.

✓ Measures Free MEA, MMA & Unreacted Triazine
✓ Direct ppm-level Detection in Crude, Desalter & Overhead Water
✓ Results in < 5 Minutes at the Lab Bench or Pipeline Skid

The Corrosion Mechanism: From Wellhead Scavenger to Condenser Leak

How upstream H2S scavenger over-treatment travels hundreds of miles down pipeline networks to attack refinery overhead systems.

1
Upstream Over-Injection
Triazine-based scavengers are over-injected into upstream crude gathering lines. Unreacted triazine remains dissolved in crude oil cargoes.
2
Desalter Wash Water Slip
Triazine and amine salts partition incompletely in the desalter, carrying over directly into the preheat train and atmospheric furnace.
3
Furnace Thermal Cracking
At furnace temperatures (>550°F / 290°C), triazine rapidly cracks into volatile free monoethanolamine (MEA) and monomethylamine (MMA).
4
Overhead Salt Deposition
Volatile amines distill overhead and react with HCl gas to form solid MEA·HCl salts at 220°F–280°F—well above the water dew point.

🔥 The Overhead Corrosion Hazard

  • Under-Deposit Attack: Amine hydrochloride salts are hygroscopic. They absorb trace moisture, generating concentrated acid pockets (pH < 1) that aggressively pit carbon steel and titanium condenser tubes.
  • Dry Salt Point Deposition: Unlike filming neutralizing amines, tramp MEA·HCl precipitates before wash water can dissolve it, causing heavy salting in exchanger bundles.
  • Distillation Tower Salt Plugs: Secondary tramp amines cause tray fouling and differential pressure spikes in top fractionator fractionation trays.

📉 The Financial & Operational Costs

  • $1M+ Unscheduled Turnarounds: An overhead tube rupture forces an emergency crude unit shutdown, costing $500,000 to $2,500,000+ in lost margin and repair.
  • Blind Chemical Treating: Refineries over-inject expensive filming inhibitors and neutralizers trying to combat localized pitting they cannot accurately measure.
  • Opportunity Crude Losses: Plants reject deeply discounted crude blends out of fear, or accept them blindly and suffer catastrophic exchanger corrosion.

The OndaVia Solution: Definitive Identification in < 5 Minutes

OndaVia Quantitative Raman Spectroscopy (QRS) isolates the distinct vibrational fingerprint of each amine species. In under 5 minutes, you can screen incoming crude shipments, monitor desalter wash water partitioning, and measure overhead accumulator water—quantifying exact ppm concentrations of MEA-triazine, MMA-triazine, free MEA, and neutralizer amines.

Why Traditional Tramp Amine Testing Methods Fail

How OndaVia QRS compares directly to manual potentiometric titrations and contract lab chromatography.

Testing Dimension Potentiometric Wet Titrations Contract Testing Lab (IC / GC-MS) OndaVia Raman (QRS)
Turnaround Time 30–45 minutes per test 5 to 10 business days Under 5 minutes on-site
Species Specificity ✕ Blind (measures total base number; cannot separate tramp MEA from added neutralizers) ✓ Speciated identification ✓ Speciated ppm quantification (MEA, MMA, Triazines, Neutralizers)
Gate-Check Feasibility ✕ Impractical for fast custody transfer decisions ✕ Completely useless (crude is already refined before data arrives) ✓ Immediate (accept or treat crude before feeding CDU)
Sample Preparation Complex solvent extractions, acid titrants, hazardous waste Demanding analytical prep & calibration Simple 1-step extraction into sealed microfluidic cartridge
Cost per Test High technician labor overhead $150 to $400 per sample fee Low consumable cartridge cost

Documented Refinery Protection in the Field

Real-world operational results from operating crude distillation units and refinery technical centers.

Gulf Coast Refinery Case History #1
ROI: $1.4M Prevented Condenser Retubing

Catching Tramp MEA in Opportunity Tight Oil Blends

The Problem: A 250,000 bpd refinery began running a discounted light tight oil (LTO) blend. Within weeks, overhead accumulator water pH swung wildly, and electrical resistance corrosion probes indicated severe localized pitting in the carbon steel overhead condenser bundles.

The OndaVia Diagnosis: Gate testing with an OPAL-103 identified 42 ppm unreacted MEA-triazine in the incoming crude delivery. In the desalter, only 60% partitioned into the brine, allowing 16 ppm of triazine to charge directly to the crude furnace where it cracked into volatile MEA.

The Outcome: The refinery established a strict 5 ppm tramp amine gate specification. Armed with 5-minute OPAL testing, they negotiated chemical treater upstream remediation, optimized desalter wash water injection, and prevented an emergency unit shutdown that would have cost over $1.4M in downtime and retubing.

Midwest Refining Center Case History #2
ROI: 28% Chemical Inhibitor Savings

Eliminating Neutralizer Over-Injection in Overhead Systems

The Problem: Because laboratory IC results took a week to arrive, corrosion engineers routinely over-injected expensive neutralizing filming amine chemistry into the CDU overhead vapor line to ensure the water boot stayed buffered above pH 5.8.

The OndaVia Diagnosis: Routine daily testing of overhead accumulator water using OndaVia QRS showed that over-injection was creating a secondary salting hazard from excess unreacted neutralizer amine salts.

The Outcome: By pairing daily OPAL-103 measurements with ionic modeling, the refinery trimmed neutralizer injection rates to match actual acid gas demand, cutting annual specialty chemical spend by 28% while improving overhead cleanliness.

Refinery Deployment Options: Lab Benchtop or In-Line PAT

Engineered for the demands of 24/7 refinery operations and process chemical service teams.

Refinery Lab & Crude Gate Screening

OPAL-103 Portable Analysis System

Engineered for Crude Receiving Labs, Shift Chemist Benches, and Inspection Skids
  • Crude Gate Screening: Test incoming crude oil tanker trucks, rail offloading, and pipeline batches in under 5 minutes.
  • Pushbutton Operation: Pre-calibrated cartridges eliminate standard prep, hazardous acid burettes, and chemist calibration curves.
  • Multi-Matrix Versatility: Analyzes raw crude oil, desalter effluent wash water, and overhead accumulator sour water on the same platform.
  • Speciated Ppm Output: Directly displays ppm MEA, ppm MMA, and unreacted triazine concentration.
Automated In-Line Process PAT

ORCA-303 Continuous Process Analyzer

Engineered for Desalter Effluent Monitoring and Overhead Accumulator Sour Water
  • Autonomous Slipstream Sampling: Continuous automated fluid extraction, optical analysis, and self-cleaning cycles.
  • Refinery DCS / SCADA Integration: 4–20 mA and Modbus TCP/IP outputs provide real-time amine salt alarm feeds.
  • Closed-Loop Trim: Automates chemical injection pump control for wash water acidification and neutralizer amine dosing.
  • Class I, Div 2 / ATEX Certified: Purged explosion-proof enclosures ready for refinery process battery limits.

Analytical Specifications & Detection Limits

Target Amine Analytes Monoethanolamine (MEA), Monomethylamine (MMA), EDA, MDEA, Triazine Scavenger, Morpholine, Proprietary Neutralizing Amines
Detectable Sample Matrices Raw Crude Oil, Desalter Effluent Water, CDU Overhead Accumulator Boot Water, Sour Water Stripper Feed
Measurement Range 0.5 ppm to 500+ ppm (expandable with automated micro-dilution)
Analysis Cycle Time < 5 minutes total (sample prep to final concentration readout)
Sample Volume < 5 mL crude oil or water sample required
Consumable System Factory pre-calibrated microfluidic optical cartridges (Part # OV-OP-B010 / OV-OP-B012)

Eliminate Tramp Amine Overhead Corrosion Risks Today

Whether you need an OPAL-103 to screen incoming crude shipments at the gate or an automated ORCA-303 for continuous desalter brine monitoring, our engineering team can provide application notes, custom proposals, and rapid feasibility testing.