Skid-Mounted Modular

Desalting & Heating-Separation Integration Module

Electric desalting and three-phase separation in one engineered module -- from water-cut wellstream to export-specification crude oil, integrated and factory-tested as a single system.

Desalting and separation integration module
Integration Scope Electric desalter + Heating + 3-phase separator
Crude Oil Target BS&W ≤ 0.2-0.5%
Salt ≤ 3 PTB
Key Technology High-voltage electrostatic field coalescence
Reference Project CNOOC Wushi
(2025 First-of-its-Kind)
Application Offshore / onshore terminals / Refinery feed

When Gravity Separation Alone Cannot Meet Export Specification

A three-phase separator removes bulk water and gas from crude oil -- achieving BS&W in the range of 1-5%. For pipeline export, tanker loading, or refinery feedstock, the specification is typically BS&W ≤ 0.2-0.5% and salt content ≤ 3-10 PTB. Electrostatic desalting achieves this by applying a high-voltage electric field to break tight emulsions. Our integration module combines these steps into a single engineered system.

Offshore Production

Offshore Production: Export Crude Quality

Offshore facilities must typically produce export-specification crude directly before transfer. An integrated desalting and separation module -- designed with a defined footprint and performance guarantee -- is the most space and weight-efficient solution, minimising offshore commissioning time.

Onshore Export Terminal

Onshore Export Terminal Crude Conditioning

Terminals condition wellstream production to meet pipeline entry or tanker loading specifications. An integrated desalting module performs the final dehydration and desalting step, conditioning commingled production to export specification before storage or metering.

Offshore-to-Onshore Terminal

Offshore-to-Onshore Terminal Processing

Crude arriving via submarine pipeline may have significant water content and dissolved salts. LINSON OIL's 2025 First-of-its-Kind Equipment for CNOOC's Wushi Oilfield was awarded for this exact duty: conditioning offshore crude at an onshore terminal with integrated dehydration.

Upstream Field-Scale Desalting

Upstream Desalting for Refinery Feedstock

Upstream desalting reduces a refinery's own desalter load, saving energy and chemical costs. For operators under quality-linked pricing contracts, upstream desalting directly improves crude oil value.

Primary Reference: CNOOC Wushi Oilfield Group -- Onshore Terminal

Integrated dehydration, stabilisation, LNG liquefaction, and mercury removal system -- including crude oil dehydration stages -- for an onshore terminal processing production from offshore Wushi oilfield wells. Designated 2025 Shandong Province First-of-its-Kind Equipment.

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From Wellstream to Export-Grade Crude

The Integrated Process Sequence

Process flow diagram

Why Electric Desalting Works

Crude oil emulsions are stabilised by naturally occurring surfactants that prevent water droplets from coalescing. For droplets below ~100 μm, gravity settling is too slow. An electrostatic desalter applies a high-voltage AC or DC electric field (15,000-33,000 V) across the crude oil layer. This field causes dipole polarisation and electrophoresis, forcing water droplets to migrate, collide, and coalesce into larger droplets that settle rapidly under gravity.

The Integrated Process Sequence

Stage 1 -- Crude Oil Heating

The incoming wellstream is heated to 60-120°C to reduce oil viscosity, weaken emulsion films, and increase settling velocity. Heating is provided by the integrated water bath, vacuum phase-change heater, or heat exchanger.

Stage 2 -- Bulk Three-Phase Separation

Heated crude passes through a bulk separator to remove free water and gas, reducing water-cut to 10-15% -- the optimal range for electrostatic desalting.

Stage 3 -- Wash Water Injection

Fresh water (3-10% of crude volume) is injected to dilute the salt concentration of the dispersed water phase before entering the desalter.

Stage 4 & 5 -- Electrostatic Desalting & Outlets

The washed crude enters the desalter vessel containing electrode grids. The electric field coalesces water droplets into a water pad at the bottom. Desalted crude exits the top, meeting BS&W and salt specifications.

Performance Targets

  • BS&W (Inlet) 1-10%
  • BS&W (Outlet) ≤ 0.2-0.5%
  • Salt (Inlet) 20-200 PTB
  • Salt (Outlet) ≤ 3-10 PTB
  • Droplet Size 10-100μm → >200μm
  • Inlet Temp 60-120°C

The Integration Advantage

When procured separately, the desalter guarantee depends on separator and heater performance -- leaving interface risks to the EPC.

LINSON OIL designs the complete sequence as a single engineering system. Our performance guarantee covers the integrated module output, not just individual stages.

Engineering Specifications

Detailed technical parameters for standard integrated modules.

Electrostatic desalter vessel detail
Parameter Standard Range Notes
Crude Oil Throughput 500 - 50,000+ m³/d Multiple vessels in parallel for larger throughputs
Inlet Crude BS&W Up to 40% Higher requires upstream bulk separation
Outlet Crude BS&W ≤ 0.2-0.5% Per client export or pipeline specification
Outlet Salt Content ≤ 3-10 PTB Per refinery or pipeline specification
Desalter Type Single-stage / Two-stage Two-stage for salt < 3 PTB
Operating Voltage 15,000 - 33,000 V AC / DC / Combined per crude properties
Transformer/Rectifier Auto voltage control T-class safe area or Ex-rated hazardous area
Design Pressure 0.4 - 4.0 MPa (g) Per crude oil operating pressure
Design Code -- Vessels GB 150 / ASME VIII Div.1 ASME U-stamp for export
High-Voltage Safety Interlocked isolation Per IEC 61936 high-voltage installations
FAT Full system firing test Voltage ramp test; level control; interlocks

Standard Supply & Customization Options

Standard Module Supply

Process Design

  • Crude characterisation & performance prediction
  • Process simulation (heating, sizing, wash water)
  • P&ID development for integrated module
  • Performance guarantee basis (BS&W and salt)

Mechanical Supply

  • Bulk three-phase separator & Heating stage
  • Electrostatic desalter vessel with internal grids
  • High-voltage T/R unit with auto control
  • Inter-stage pipe spools (GC2 / ASME B31.3)
  • Wash water injection system & Instruments

Control & Integration

  • PLC with HMI touchscreen & SCADA outputs
  • High-voltage safety interlocks
  • Common structural skid frame
  • Full FAT (high-voltage, level, safety)

OEM / ODM Options

  • Two-stage / DC Field: For salt < 3 PTB, tight emulsions, or heavy crude.
  • Offshore Optimisation: Compact multi-stage vessel design for FPSO weight budgets.
  • Heat & Water Integration: Crude-to-crude heat exchangers; integrated produced water treatment.
  • Chemical Injection & Sampling: Integrated dosing, auto sampling, online BS&W analyser.
  • Certifications: ASME U-stamp, DNV/BV/ABS, ATEX/IECEx (Zone 1/2).

First-of-Its-Kind. Certified.

Delivering export-grade crude to international standards.

CNOOC Wushi onshore terminal

CNOOC Wushi Oilfield -- Onshore Terminal

2025 First-of-its-Kind Equipment

Integrated crude oil dehydration, stabilisation, LNG liquefaction, LPG recovery, and mercury removal system for the onshore terminal processing production from offshore Wushi oilfield wells. This demonstrates LINSON OIL's integrated crude oil processing capability at scale.

Key Certifications

A2 + High-Pressure Vessel GC2 Piping ASME U-stamp IEC 61936 CNAS Lab ISO 9001/3834-2

Congo (Brazzaville) -- Jiarou Oilfield

Integrated associated gas and crude handling system. Included crude oil conditioning and dehydration stages alongside gas recovery. Cross-border delivery and field commissioning support fully managed by LINSON OIL.

Industry-Leading Warranty

Standard: 2 years from commissioning (vs. industry 1 year). Long-term partners: up to 2.5 years. Covers system performance, not just component integrity, verified by our rigorous FAT process before shipment.

Crude Assay. Throughput. Export Spec.
We'll Design the System.

Integrated module design begins with your crude oil characterisation. Send us your parameters, and our process engineering team will assess the required process sequence, preliminary sizing, and performance guarantee basis.

Free Engineering Resource

Submit your assay and specification to receive:

  • Preliminary process route assessment
  • Performance feasibility confirmation
  • Relevant project reference match

Response typically within 1-2 business days.

LINSON OIL -- 2025 First-of-its-Kind: CNOOC Wushi Dehydration System | A2 + GC2 + High-Voltage System Integration | ASME U-stamp | Classification Society Certification Available