UK HQ Your time

Understanding Refinery Desalter Effluent

Comprehensive treatment approaches for one of the most challenging wastewater streams in petroleum refining.

The Crude Oil Desalting Process

Crude oil desalting is a critical first step in petroleum refining that removes salt, water, solids, and other contaminants from raw crude oil before it enters the atmospheric distillation unit. Salt in crude oil, primarily present as dissolved chlorides of sodium, calcium, and magnesium, can cause severe corrosion, fouling, and catalyst poisoning downstream. The desalting process uses wash water and electrostatic coalescence to separate these impurities from the crude oil stream.

During desalting, crude oil is mixed with 3% to 10% by volume of fresh or recycled wash water. This water dissolves the water-soluble salts and extracts some of the suspended solids. The oil-water mixture then passes through an electrostatic coalescer where high-voltage fields promote droplet growth and separation. The resulting desalted crude oil proceeds to the distillation unit, while the separated aqueous phase becomes the desalter effluent.

Desalter effluent represents one of the most complex and concentrated wastewater streams in a refinery. It contains extremely high salt concentrations, significant oil content, suspended solids, dissolved metals, hydrogen sulphide, ammonia, and phenols. The high salinity, typically 50,000 to 300,000 mg/L TDS, makes advanced biological treatment impossible without substantial dilution or specialised halophilic systems. The combination of corrosive salts, toxic compounds, and variable flow rates creates unique treatment challenges that require specialised engineering solutions.

Effluent Characteristics and Variability

The composition and volume of desalter effluent depend heavily on the crude oil source, desalter design, and operating conditions. Heavy sour crudes from the Middle East, Venezuela, or Canada typically produce effluent with higher oil content, more dissolved hydrogen sulphide, and greater concentrations of naphthenic acids. Light sweet crudes generate lower volumes of effluent with somewhat reduced contaminant loading.

Two-stage desalting, commonly used for heavy or high-salt crudes, produces two distinct effluent streams. The second-stage effluent, being cleaner, can often be recycled as wash water to the first stage. First-stage effluent, containing the bulk of removed contaminants, requires the most intensive treatment. The degree of wash water recycling directly impacts the volume and concentration of effluent requiring final treatment.

Process upsets such as crude switching, emulsion formation, or electrostatic grid failure can dramatically alter effluent quality. During upsets, oil-in-water concentrations may spike from typical values of 200 – 2,000 mg/L to over 10,000 mg/L. Temperature variations between 80°C and 140°C affect oil-water separation efficiency and influent temperature to downstream treatment. These operational realities necessitate robust treatment systems with adequate equalization and surge capacity.

Treatment Challenges

The high total dissolved solids (TDS) content in desalter effluent fundamentally alters the physical chemistry of wastewater treatment. Elevated ionic strength compresses the electrical double layer around colloidal particles, reducing zeta potential and affecting coagulation chemistry. Standard coagulant doses may be insufficient at high salinity, requiring higher chemical addition or specialised formulations adapted to brine conditions.

Oil droplets in desalter effluent are typically small and stabilised by surfactants naturally present in crude oil or added as demulsifiers. The high salt content can either enhance or inhibit demulsification depending on the specific chemistry. Heavy metals including nickel, vanadium, lead, and mercury are present in dissolved or particulate form, requiring precipitation and removal to meet environmental standards.

Brine management represents the ultimate treatment challenge. Once oil and solids are removed, the remaining brine must be disposed of through deep-well injection, evaporation ponds, crystallizers, or discharged to marine environments where permitted. Zero liquid discharge (ZLD) systems using mechanical vapour recompression or multi-effect evaporation can eliminate liquid waste but require significant capital and operating investment. Explore our dewatering solutions for brine handling.

Key Contaminant Challenges

Each contaminant in desalter effluent demands specialised treatment technology and careful process design.

High Salinity

Total dissolved solids in desalter effluent range from 50,000 to 300,000 mg/L, primarily sodium, calcium, and magnesium chlorides. This extreme salinity inhibits conventional advanced biological treatment, alters coagulation chemistry, accelerates equipment corrosion, and creates disposal challenges. Brine management through evaporation, crystallisation, or deep-well injection adds significant requirement and complexity to treatment system design.

  • TDS: 50,000 – 300,000 mg/L
  • Chlorides: 30,000 – 180,000 mg/L
  • Precludes standard advanced biological treatment

Oil & Grease

Desalter effluent contains dispersed crude oil droplets, dissolved hydrocarbons, and emulsified oil stabilised by natural surfactants. Oil content varies with crude type, desalter efficiency, and operational conditions. Free oil can be recovered by gravity separation, but emulsified oil requires chemical demulsification, dissolved air flotation, or membrane separation. Oil recovery is technically attractive as recovered crude can be recycled to the refinery.

  • Oil: 200 – 5,000 mg/L
  • BTEX compounds present
  • Recovery value:

Suspended Solids

Solids in desalter effluent include corrosion products, clay, sand, iron sulphide, and precipitated salts. These solids can abrade pumps, foul heat exchangers, and interfere with oil separation. In two-stage desalters, solids from the second stage are typically cleaner and may be suitable for recycle. First-stage solids carry the highest contaminant burden and require dedicated dewatering and disposal.

  • TSS: 100 – 2,000 mg/L
  • Includes iron sulphide and sand
  • Requires dewatering before disposal

Dissolved Metals

Crude oil contains trace metals that concentrate in desalter effluent, including nickel, vanadium, lead, mercury, and arsenic. These metals pose environmental toxicity concerns and are subject to stringent discharge limits. Chemical precipitation with sulphide, hydroxide, or organosulfide reagents converts dissolved metals to insoluble forms for removal by sedimentation or filtration. Final polishing may require ion exchange or adsorption.

  • Ni, V, Pb, Hg, As present
  • Precipitation pH dependent
  • Tighter limits for surface discharge

Five-Stage Desalter Effluent Treatment

Our integrated approach addresses the unique challenges of high-salinity refinery desalter wastewater through targeted unit operations.

Equalization

Hot desalter effluent is cooled and equalized to buffer flow and concentration fluctuations. Cooling towers or heat exchangers reduce temperature to protect downstream biological units and improve oil separation kinetics. Equalization also provides emergency containment during process upsets.

Oil Separation

API separators, CPI units, or dissolved air flotation systems remove free and dispersed oil. Demulsifying chemicals may be added to break stable emulsions. Recovered crude oil is returned to the refinery crude tank farm. View oil separation systems.

Metals Precipitation

Chemical precipitation converts dissolved heavy metals to insoluble sulphide or hydroxide precipitates. Organosulfide precipitants provide very low residual metal concentrations even at neutral pH. Rapid mixing and flocculation promote particle growth for efficient removal.

Clarification

Lamella clarifiers or dissolved air flotation units remove precipitated metals, residual oil, and suspended solids. Lamella plate packs provide high-rate settling in a compact footprint. Self-cleaning filters or multimedia filters provide final solids polishing before brine management.

Brine Management

Treated brine is managed through deep-well injection, evaporation ponds, crystallizers, or permitted marine discharge. Zero liquid discharge systems use mechanical vapour recompression to produce solids for landfill and distilled water for reuse. Explore dewatering options.

Desalter Effluent Treatment Parameters

Engineering design basis and performance targets for desalter effluent treatment systems.

ParameterTypical RangeTreatment TargetTechnology
Flow Rate (per unit)5 – 150 m³/hrDesign for peak + 20%Hydraulic equalization
Temperature80 – 140°C< 40°C downstreamHeat exchanger / cooling
TDS50,000 – 300,000 mg/LSite-specific brine limitBrine management / ZLD
Oil & Grease200 – 5,000 mg/L< 15 mg/LAPI + DAF
TSS100 – 2,000 mg/L< 30 mg/LSedimentation / DAF
Nickel1 – 50 mg/L< 0.5 mg/LSulphide precipitation
Vanadium2 – 100 mg/L< 0.5 mg/LHydroxide precipitation
Mercury0.01 – 1 mg/L< 0.005 mg/LOrganosulfide + filtration
Hydrogen Sulphide10 – 500 mg/L< 1 mg/LAir stripping / oxidation
Ammonia20 – 300 mg/L< 15 mg/L (if discharged)Steam stripping / biological
Phenols10 – 200 mg/L< 1 mg/LBiological / activated carbon
pH5.5 – 8.56.5 – 8.5Acid / caustic neutralisation
Oil Recovery RateN/A> 90% of separable oilAPI + DAF skimming
Brine Volume ReductionN/A85 – 95% (ZLD systems)MVR / crystallizer

Desalter Configurations We Treat

Treatment systems adapted to different desalter designs, crude types, and refinery configurations worldwide.

Atmospheric Desalters

Single-stage atmospheric desalters processing raw crude before the CDU generate concentrated effluent with high solids and oil loading. Reynolds & Bauhm systems handle the full temperature and flow range with robust metallurgy for corrosive conditions.

Vacuum Desalters

Vacuum unit desalters treating reduced crude operate at higher temperatures and lower pressures. Effluent handling must account for flashing hydrocarbons, higher viscosity, and potential coking tendency in the wastewater stream.

Single-Stage Desalting

Single-stage desalters, common in smaller refineries or with low-salt crudes, produce a single effluent stream with concentrated contaminants. Treatment systems must handle the full contaminant load in one pass.

Two-Stage Desalting

Two-stage desalters enable wash water recycle, reducing overall effluent volume. Our treatment designs integrate with recycle strategies, treating first-stage effluent while managing cleaner second-stage streams.

Heavy Crude Processing

Heavy crude oils with high viscosity, high metals, and high acid numbers generate challenging effluent with elevated solids and emulsified oil. Specialised demulsifiers and higher chemical doses are typically required.

High TAN Crudes

High total acid number (TAN) crudes contain elevated naphthenic acids that create stable emulsions and corrosive conditions. Treatment systems use upgraded metallurgy and specialised chemical programs to handle these aggressive effluents.

Key Benefits of Our Desalter Effluent Systems

Purpose-built solutions that address the unique demands of high-salinity refinery wastewater treatment.

Regulatory Compliance

Meet stringent oil-in-water, metals, and priority pollutant limits for surface water discharge or achieve brine specifications for deep-well injection and marine outfalls.

Maximum Oil Recovery

Recover over 90% of separable crude oil for return to the refinery, directly offsetting treatment costs through product value recovery.

Metals Removal

Achieve very low residual metals concentrations through optimised precipitation chemistry and high-rate solids separation.

Brine Volume Reduction

ZLD and mechanical evaporation systems reduce brine volumes by 85 – 95%, minimising disposal requirements and environmental liability.

High-Temperature Handling

Systems engineered for inlet temperatures up to 140°C with appropriate materials selection, cooling integration, and safety systems.

Upset Tolerance

Equalization and surge capacity buffer the Treatment Process against process upsets, crude switches, and emulsion events.

Corrosion-Resistant Design

Materials selection including duplex stainless steels, titanium, and FRP ensures long equipment life in highly corrosive brine environments.

Process Integration

Systems designed to integrate with existing desalter operations, wash water recycle, and refinery-wide water management strategies.

Related Refinery Treatment Processes

Discover complementary wastewater treatment solutions for comprehensive refinery water management.

Refinery Oil Separation

Primary oil-water separation technologies including API separators, CPI units, and parallel plate separators for refinery service.

Explore Oil Separation

Process Area Runoff

Treatment systems for oily wastewater from crude storage, process units, loading facilities, and maintenance areas.

Explore Process Runoff

Sour Water Stripping

Ammonia and hydrogen sulphide removal from sour water streams in hydrotreating, hydrocracking, and distillation units.

Explore Sour Water

Water Reuse & Recovery

Integrated water reuse strategies including membrane treatment, evaporation, and polishing for cooling tower and boiler feed makeup.

Explore Water Reuse

Refinery Overview

Complete portfolio of refinery wastewater treatment solutions covering all process streams and integrated management strategies.

Explore Oilgas Refinery

Oil & Gas Industry

Comprehensive water treatment solutions for upstream production, midstream terminals, and downstream refining operations.

Oil & Gas Solutions

Related Pages

High Salinity Wastewater

Advanced treatment systems for high salinity wastewater and brine management.

View Page

Oilgas Refinery Coking

Treatment systems for refinery coking unit wastewater including delayed coking and fluid coking effluents with high phenol, COD.

View Page

Oilgas Refinery Process Runoff

Treatment systems for oily process area runoff from petroleum refineries.

View Page

Oilgas Refinery Sour Water Stripper

Treatment systems for stripped sour water from refinery amine and sulphur recovery units.

View Page

Oilgas Refinery Tank Bottoms

Specialised treatment systems for refinery tank cleaning wastewater and tank bottoms containing concentrated oil, sludge and heavy solids.

View Page

Oilgas Refinery Utilities

Treatment systems for refinery utilities wastewater including cooling tower blowdown, boiler blowdown and utility drainage across the refinery.

View Page

Desalter Effluent Water — Design Parameters

Crude oil desalter water is the single largest aqueous outlet from the crude unit and the source of much downstream salt loading.

Stream Characterisation

Flow: 4–10% of crude charge. Salts: 5,000–50,000 mg/L Cl⁻. Oil: 200–2,000 mg/L. TSS: 300–2,000 mg/L. NH₃: 10–100 mg/L from desalting demulsifiers and amines.

API Separator Sizing

Rectangular API to API-421 standard. Surface loading 0.4–0.8 m/h. Skim oil to slop tank; bottom sludge to centrifuge.

DAF / IGF Polishing

Post-API: DAF reduces oil from 50–100 mg/L to 5–15 mg/L. Recycle ratio 30–50%. Saturator pressure 5–6 bar. Polymer often required.

Reuse Potential

High TDS limits reuse to fire water or stream where salt is acceptable. After biological + sand filter, can be used for cooling tower makeup if blended with low-TDS streams.

Corrosion

Chloride + temperature drives pitting of standard SS304/316. Use duplex 2205 or super-duplex in piping & tanks. Cathodic protection on carbon steel underground.

Wash-Water Selection

Desalter wash water quality directly impacts downstream effluent quality. Specify low-TDS, low-NH₃ (<50 mg/L), low-phenol (<5 mg/L) wash water.

API Separators — Engineering Deep-Dive

Stokes’-law sizing, API Publication 421 design methodology, rectangular API / CPI / TPI configurations and refinery-train integration.

Need Desalter Effluent Solutions?

Contact our experts to design a system tailored to your refinery requirements.

Industries We Serve

Our expertise spans multiple industries with sector-specific water treatment solutions.