How Does a Crude Distillation Unit (CDU) Work? A Complete Technical Guide
A Crude Distillation Unit (CDU) is the foundation and first major processing step of every oil refinery. It is the primary unit responsible for separating crude oil into distinct hydrocarbon fractions based on their boiling points. These fractions—gases, naphtha, kerosene, diesel, gas oil, and atmospheric residue— become feedstocks for downstream units where they are further upgraded into fuels, petrochemical feedstocks, and specialty products.
Without the CDU, no refinery can operate. It performs the essential task of transforming untreated crude oil— containing a mix of thousands of hydrocarbons—into organised, usable streams. Understanding how a crude distillation unit works reveals why refining begins with physical separation: it prepares the raw material for conversion, treating, and blending processes across the refinery.
This article provides a complete explanation of the architecture, operating principles, equipment, process flow, and safety considerations of the CDU, with a brief contextual mention of the role of the fluid catalytic cracker (FCC) in a refinery as a downstream consumer of CDU products. ➡️Oil & Gas Training Courses
What Is a Crude Distillation Unit (CDU)?
A Crude Distillation Unit is a large processing unit that separates crude oil into components through atmospheric distillation. It uses the principle that different hydrocarbons have different boiling points. By heating crude oil and sending it into a tall fractionation column, the CDU allows lighter vapours to rise and heavier compounds to fall, enabling controlled separation.
The CDU typically consists of two major sections:
- Preheat and desalting system
- Atmospheric distillation column with side strippers and heat recovery network
Many refineries follow the CDU with a Vacuum Distillation Unit (VDU) to process heavier fractions further and extract additional valuable products.
Why the CDU Is the Starting Point of Refining
Crude oil arrives at the refinery as a single, contaminated, chemically diverse mixture. Before any chemical conversion or upgrading can occur:
- Water, salts, and sediments must be removed
- The crude must be heated to the appropriate temperature
- The hydrocarbon mixture must be separated into defined cuts
Every downstream processing unit—hydrotreaters, catalytic reformers, hydrocrackers, isomerisation units, and even the fluid catalytic cracker (FCC)—depends on the CDU to deliver clean, properly segregated feedstocks.
The Crude Oil Journey Through a CDU: Step-by-Step
The CDU process can be divided into several major stages. Each step ensures efficient, safe, and accurate distillation of crude oil into valuable fractions.
1. Crude Oil Storage and Feed Preparation
Crude oil is delivered to the refinery by pipelines, ships, or rail and stored in large tanks. Before entering the CDU, the crude typically undergoes basic preparation steps:
- Crude types may be blended to achieve the desired feed quality
- Temperature, density, and basic properties are checked
- Any free water is allowed to settle naturally in storage tanks
Proper feed preparation helps ensure stable CDU operation and avoids sudden variations that may disrupt temperature and pressure control within the unit.
2. Desalting – Removing Salts, Sediments, and Water
Raw crude contains impurities such as:
- Sodium, magnesium, and calcium salts
- Suspended solids and minerals
- Free and emulsified water
- Organic chlorides
- Metal contaminants
If not removed, these impurities cause corrosion, fouling, and catalyst poisoning in downstream equipment. The desalter is therefore a critical component of the CDU.
How the Desalter Works
In the desalter:
- Crude oil is mixed with a controlled amount of wash water.
- High-voltage electrostatic fields cause water droplets to coalesce.
- Coalesced water settles at the bottom carrying salts and solids.
- Desalted crude leaves the top with significantly reduced salt content (typically < 3–5 ppm).
This step protects the furnace, distillation column, and downstream units from aggressive corrosion and scaling.
3. Heat Exchanger Train – Energy Recovery and Preheating
Before crude enters the furnace, it passes through a network of heat exchangers where it is heated by recovering heat from:
- Product streams leaving the CDU
- Pump-around circuits within the column
- Column bottom streams and other hot process flows
This “heat integration” greatly improves refinery energy efficiency and reduces fuel consumption in the furnace.
Typically, the crude temperature rises from ambient (around 20–40°C) to about 120–250°C in the exchanger train, before final heating in the furnace.
4. Crude Furnace – Reaching Vaporisation Temperature
The furnace (or fired heater) is the final heating stage before the distillation column. It takes the preheated crude to its target temperature necessary for effective vaporisation.
Typical furnace outlet temperatures are:
- Light to medium crude: approximately 320–360°C
- Heavy crude: approximately 360–380°C
The objective is to vaporise as much of the crude as practical without causing thermal cracking and coke formation.
Key furnace considerations include:
- Controlled heating to minimise coking and tube damage
- Even heat distribution across the coil passes
- Use of fuel gas, fuel oil, or refinery gas as furnace fuel
- Continuous monitoring of emissions and combustion efficiency
5. Atmospheric Distillation Column – The Heart of the CDU
Once heated, the crude oil flows into the atmospheric distillation column—a tall, insulated tower containing trays or structured packing. This is where fractionation occurs.
Core Principle: Fractionation
The operation of the column is based on the fact that different hydrocarbons condense at different temperatures:
- Hot vapours from the furnace enter the column and rise upwards.
- Temperature decreases from the bottom to the top of the column.
- Heavier molecules condense on lower trays, while lighter molecules condense higher up.
- Non-condensable gases exit the column overhead.
The column operates slightly above atmospheric pressure, providing stable separation and maintaining control over boiling conditions.
Typical Cuts Drawn from the Column
The CDU draws several product streams at different levels:
- Overhead vapours: LPG and light naphtha
- Heavy naphtha: further processed for gasoline or petrochemicals
- Kerosene: jet fuel and heating kerosene feed
- Diesel (light gas oil): mid-distillate fuel feed
- Atmospheric gas oil: feedstock for downstream conversion units
- Atmospheric residue: the heaviest fraction removed from the column bottom
Each of these streams may undergo further stabilisation or side stripping to tighten its boiling range.
6. Side Strippers – Purifying Each Fraction
Side strippers are small associated columns connected to the main column side draws. Their purpose is to improve product quality by removing lighter components from each side stream.
For example:
- The kerosene side stripper removes dissolved light naphtha from the kerosene cut.
- The diesel side stripper removes lighter vapours to ensure the proper diesel boiling range.
Steam is commonly injected as a stripping medium. This lowers partial pressures and aids the removal of light components without excessive temperature increase.
7. Overhead Condenser and Reflux System
The overhead vapours from the column are cooled in an overhead condenser. This cooling step produces:
- Liquid reflux, returned to the column to enhance separation efficiency
- Off-gas (LPG and light hydrocarbons), sent to gas recovery units
A reflux drum separates the condensed liquid and vapour phases, allowing controlled overhead pressure and temperature. Proper reflux management is essential for stabilising naphtha quality and controlling the column’s top-end cut point.
8. Pump-Around Systems – Controlling Temperature Profiles
Pump-around circuits are intermediate withdrawal and return loops that help control the internal temperature profile of the column and recover heat for other refinery services.
In a typical pump-around system:
- Liquid is withdrawn from a specific tray level.
- It is cooled in external heat exchangers to recover heat.
- The cooled liquid is then returned to a higher tray in the column.
Pump-arounds increase separation efficiency, support energy integration, and help stabilise column operation.
9. Bottoms Handling – Atmospheric Residue
The heaviest material in the column, atmospheric residue, exits at the bottom. It cannot be distilled further at atmospheric pressure without thermal cracking.
Atmospheric residue is typically routed to:
- Vacuum Distillation Units (VDU)
- Coking units
- Visbreakers
- Residue hydrocrackers
These downstream units convert heavy residue into lighter, higher-value products such as gas oils, naphtha, and petroleum coke.
Understanding CDU Products and Their Refinery Pathways
Each CDU product stream serves as feedstock for specific downstream processes:
- Naphtha: sent to catalytic reforming or petrochemical crackers for gasoline components and aromatics.
- Kerosene: treated and blended to form jet fuel and kerosene products.
- Diesel: hydrotreated for sulfur removal and blended as diesel fuel.
- Atmospheric gas oil: key feedstock for catalytic cracking and hydrocracking units.
- Atmospheric residue: processed in vacuum distillation and residue upgrading units.
Why Accurate CDU Operation Is Critical
Because every downstream unit depends on its cuts, inefficient CDU operation has serious consequences:
- Improper product boiling ranges and off-spec feeds
- Reduced throughput in units like the FCC and reformer
- Higher fouling and maintenance requirements
- Energy inefficiency and increased fuel consumption
- Higher risk of corrosion and equipment failure
To prevent these issues, refiners use:
- Advanced process control (APC) systems
- Real-time analysers and online quality monitoring
- Heat integration studies to optimise energy use
- Predictive maintenance strategies for critical equipment
Operational Challenges in a CDU
Operating a CDU presents several technical and operational challenges, including:
1. Fouling in Heat Exchangers
Heavy crudes, asphaltene instability, and salt deposition can cause fouling in the exchanger train, reducing heat transfer efficiency and increasing energy consumption.
2. Overheating or Coking in the Furnace
Poor temperature control or rapid changes in feed quality can lead to overheating and coke formation inside furnace tubes, requiring costly shutdowns and decoking operations.
3. Corrosion
Overhead systems are particularly vulnerable to corrosion due to the presence of water, chlorides, and acidic compounds. Proper dosing of corrosion inhibitors and control of overhead temperatures are essential.
4. Poor Fractionation
Tray damage, flooding, excessive vapour loads, or inadequate reflux can lead to poor fractionation and off-spec product cuts.
5. Feed Variability
Modern refineries often process a wide range of crude types. Variability in crude quality challenges operators to maintain consistent product quality and stable unit performance.
Safety Considerations in CDU Operation
The CDU handles high temperatures, flammable materials, and pressurised equipment. Key safety measures include:
- Continuous flame monitoring and safe burner management in the furnace
- Pressure relief valves and overpressure protection systems
- Continuous gas detection around critical equipment areas
- Proper drainage and slop management for hydrocarbons and water
- Emergency shutdown (ESD) systems and defined operating procedures
- Firefighting systems, fireproofing, and effective insulation
Robust process safety management is essential due to the high-risk nature of crude oil handling and the large energy loads in the CDU.
Environmental Controls in a CDU
Refineries implement various environmental controls around CDU operation to minimise emissions and resource use:
- Heat integration to reduce fuel consumption and CO2 emissions
- Low-NOx burners and optimised combustion control in the furnace
- Treatment of desalter effluent and oily wastewater
- Flare gas recovery and vapour recovery units (VRU)
- Energy monitoring and continuous improvement programmes
Environmental performance is both a regulatory requirement and a driver of operational efficiency.
Conclusion: The CDU as the Backbone of Refinery Operations
The Crude Distillation Unit is the first and most essential step in refining. It transforms crude oil from a raw, unprocessed fluid into the core fractions needed for all downstream fuel and chemical production. By separating hydrocarbons according to boiling range, the CDU sets the foundation for conversion units such as the reformer, hydrocracker, and the fluid catalytic cracker (FCC) to produce gasoline, diesel, aviation fuel, and petrochemical feedstocks.
Understanding how the crude distillation unit works provides valuable insight into how refineries transform natural resources into the fuels and materials that power modern economies. As global energy systems evolve, the CDU will continue to play a central role in enabling flexible, efficient, and high-quality refining operations.
Also Read: What Is Oil Refining and How Does It Work?
Also Read: Upstream, Midstream, and Downstream in the Petroleum Industry?
Explore Our: Oil & Gas Training Courses in Dubai – Oil & Gas Training Courses in Amsterdam – Training Courses in Dubai
