Coking Furnace for Refinery Heavy Oil Processing

A coking furnace is crucial for refinery heavy oil upgrading. It is designed to heat heavy oil and vacuum residue to the required temperature before the coking process.

At Gelan, we design and manufacture refinery coking furnaces to improve heat distribution, reduce premature cracking inside the furnace, and support longer run length under severe operating conditions.

  • ≤ ±10–15°C tube wall temperature deviation
  • Up to 6–12 months continuous run length
  • Optimized heat flux distribution for improved temperature uniformity
  • Designed and fabricated to ASME and API 560 standards
refinery coking furnace hero

What Does a Coking Furnace Do in Heavy Oil Processing

In a refinery, crude oil is first separated through atmospheric and vacuum distillation. The remaining heavy residue cannot be economically upgraded by distillation alone.

A coking furnace heats this residue to the required temperature before the coking stage, helping convert it into lighter, higher-value products such as gas, naphtha, and diesel.

Convert low-value residue into higher-value saleable products

Improve overall yield from the same crude input

Reduce heavy residue sent to low-margin fuel use

Support more efficient downstream residue upgrading

Where the Coking Furnace Fits in the Refinery Process

After atmospheric and vacuum distillation, heavy residue is routed to the coking section for further upgrading.
The coking furnace is positioned before the coking drums. It heats the residue to the required temperature so it can enter the coking stage under stable conditions.

coking furnace in refinery process flow
Learn More

Typical Technical Specifications of a Coking Furnace

Parameter Gelan Typical Range Importance
Operating Temperature 480–520°C Affects cracking conditions and material selection
Feedstock Vacuum residue / heavy oil Determines fouling tendency and furnace design complexity
Tube Wall Temperature Deviation ≤ ±10–15°C Lower deviation helps reduce hotspot risk
Continuous Run Length 6–12 months Longer cycles mean fewer shutdowns
Heat Flux Customized by design Impacts heat distribution and cracking stability
Tube Material Alloy steel (e.g. HK, HP) Selected based on temperature and corrosion resistance
Design Standard ASME / API 560 Can be supplemented to meet project specifications and client requirements

*These parameters are not fixed. In real projects, furnace design must be adjusted based on feed quality, fouling tendency, and required operating cycle.

How Gelan Coking Furnace Design Solves Heavy Oil Challenges

01

Reducing Coke Build-Up in Heavy Residue Service

Heavy residue feeds tend to form coke rapidly on tube surfaces. Once coke builds up, heat transfer drops and the furnace needs to be shut down for decoking.

Gelan approach:

  • Heat flux distribution designed to avoid local high-temperature zones
  • Tube surface temperature controlled to slow down coke formation

Typical performance:

heavy oil coking furnace coke control for mobile
heavy oil coking furnace coke control
reduce premature cracking in coking furnace for mobile
reduce premature cracking in coking furnace
02

Residence Time Control to Prevent Early Cracking

If the feed stays too long in the furnace tubes, cracking can start inside the furnace instead of in the coking stage, leading to unstable operation.

Gelan approach:

  • Tube length and flow path designed to control residence time
  • Heat input balanced to avoid overexposure of feed inside tubes

Typical performance:

03

Stable and Uniform Temperature Control

Uneven temperature distribution can create hotspots, damage tubes, and accelerate coke formation.

Gelan approach:

  • Burner layout optimized for even radiant heat distribution
  • Tube arrangement designed to improve temperature uniformity

Typical performance:

coking furnace temperature control for mobile
coking furnace temperature control
coking furnace energy efficiency design for mobile
coking furnace energy efficiency design
04

Heat Load Distribution and Energy Efficiency

Poor heat load distribution not only affects operation stability but also increases fuel consumption.

Gelan approach:

  • Heat duty and heat intensity balanced across the furnace
  • Combustion system designed for stable and efficient operation

Typical performance:

05

Tube Life Under High Temperature and Fouling Conditions

Furnace tubes operate under high temperature and fouling conditions, which directly affect maintenance cost and shutdown frequency.

Gelan approach:

  • Tube material selected based on temperature and corrosion conditions
  • Design optimized to reduce thermal stress and local overheating

Typical performance:

high temperature coking furnace tube life for mobile
high temperature coking furnace tube life
industrial coking furnace process capacity for mobile
industrial coking furnace process capacity
06

Processing Capacity and Operational Stability

For large-scale refinery projects, the furnace must handle required throughput without sacrificing stability.

Gelan approach:

  • Furnace size and configuration designed based on project capacity
  • Flow distribution optimized to maintain stable operation at scale

Typical performance:

Where Delayed Coking Furnaces Are Used

Typically used in industries where heavy oil and residue require further upgrading.

Applied in crude oil refining to process heavy fractions and improve overall product value from residual feedstock

Oil Refining

Used in large-scale processing environments where stable handling of heavy hydrocarbons is required

Petrochemical Industry

Residue Coking Furnace Projects Delivered by Gelan

Related Equipment in the Delayed Coking Process

A coking furnace works together with other key equipment to support stable residue processing and product conversion.

FAQs About Coking Furnace

What is a coking furnace used for in a refinery?

A coking furnace is used to heat heavy residue to the required temperature before the coking stage.

It prepares the feed for further cracking and helps convert low-value residue into lighter products and petroleum coke.
Most coking furnaces process vacuum residue or heavy atmospheric residue.

These feeds usually contain high asphaltene content and have a strong tendency to form coke during heating.

Common challenges include:

  • Coke formation inside furnace tubes
  • Uneven heat distribution and local hotspots
  • Premature cracking before the coking stage
  • Short run length due to fouling

These issues directly affect stability, maintenance frequency, and operating cost.

Residence time controls when cracking starts.

If the feed stays too long in the furnace, cracking may begin too early, leading to fouling and unstable operation.

Run length mainly depends on:

  • Feed quality and fouling tendency
  • Heat distribution inside the furnace
  • Tube temperature control

In most cases, coke buildup inside the tubes is the main limiting factor.

Typical operating temperatures are around 480–510°C, depending on feedstock and process conditions.

Coke formation can be reduced by:

  • Controlling tube wall temperature
  • Improving heat distribution
  • Managing residence time
  • Optimizing feed conditions

These measures help extend operating cycles and reduce shutdown frequency.

The right furnace depends on your feed characteristics, fouling tendency, operating cycle, and required throughput.
For projects with heavy residue or severe operating conditions, working with an experienced manufacturer like Gelan can help you better match furnace design with your actual process requirements.

Furnace performance directly impacts:

  • Unit run length
  • Throughput stability
  • Frequency of shutdowns
  • Overall refinery profitability

Even small improvements in operation stability can significantly affect long-term performance.

faqs

Get a Coking Furnace Designed for Your Project

Talk to our engineers to discuss your process and get a coking furnace solution tailored to your project.


Leave a message

Let's have a chat