Field Reference / Introduction
Overview

The fired heater — what it is,
where it sits, and why it matters.

This page gives you the foundations. You'll find what a fired heater actually does in a refinery, the main types you're likely to work with, the hazards that make careful operation non-negotiable, and how to get the most from this reference.

What is a fired heater?

A fired heater — also called a process heater, furnace, or charge heater depending on the application — is a direct-fired heat exchanger. Fuel is burned inside an insulated enclosure, and the heat released transfers through steel tubes to a process fluid flowing inside them.

Unlike shell-and-tube or plate heat exchangers, which move heat from one process stream to another, a fired heater introduces new heat energy into the process from combustion. This makes it both the most powerful and the most hazardous heat transfer device in a refinery.

Heat duties range from a few million BTU/hr for small treater feed heaters up to several hundred million BTU/hr for CDU charge heaters. Despite this range in size, the fundamental operating principles are the same.

Graphic · Fired Heater Zones Overview
Insert labelled cross-section showing radiant section, convection section, burners, process coil, stack, and air registers. Replace this block when graphic is available.

Role in the refinery

Fired heaters appear throughout a refinery wherever a process stream needs to reach a temperature that cannot be achieved by heat integration alone. The most common duties are listed below.

Common Fired Heater Duties in Refinery Service
Unit / Service Common Name Typical Duty Typical Outlet Temp.
Crude Distillation Unit CDU charge heater / atmospheric heater Partially vaporise crude feed for the atmospheric column 340–370°C
Vacuum Distillation Unit VDU charge heater Heat atmospheric residue to near-cracking temperature under tight control 390–420°C
Catalytic Reformer Reformer charge heater / inter-heaters Heat naphtha feed and reheat between reactor beds 490–530°C
Hydrocracker / Hydrotreater Charge heater / reactor feed heater Heat feed to reactor inlet temperature 300–430°C
Delayed Coker Coker heater Rapidly heat vacuum residue to cracking temperature — shortest residence time possible 480–510°C
Visbreaker Visbreaker heater / soaker heater Controlled thermal cracking of heavy residue 440–490°C

In most of these services, the fired heater is the rate-limiting piece of equipment for the entire unit. If the heater trips, the unit stops. This is why fired heater reliability — and the operator's ability to recognise and respond to problems early — directly determines plant throughput and safety.

Main heater types

Fired heaters come in several configurations. The type you work with affects layout, burner arrangement, draft system, and inspection access — but the combustion and process principles are the same across all of them. Module 01 covers each type in depth; the brief summary below gives you a working picture.

Box / Cabin Heater
Most common type
Rectangular firebox with burners on the floor or walls. Separate convection section above. Used across most refinery services. Good tube access for inspection.
Cylindrical Heater
Compact duty
Vertical cylinder with a central burner firing upward and process tubes arranged around the inside wall. Compact footprint. Common in smaller duties and older installations.
Arbor / Wicket Heater
High flux duty
Tubes arranged in a U-shape ("wicket") in the radiant section. Used where a large number of parallel passes is needed, such as reformer inter-heaters.
Cabin Heater (Double-fired)
Large CDU / VDU
Two radiant sections sharing a common convection section. Allows very large heat duties with balanced firing across both cells.
Note
The heater type affects where you stand, what you inspect, and how air registers and dampers are arranged — but it does not change the fundamental operating principles covered in this reference. Procedures in this library are written to be applicable across heater types, with notes where a specific configuration creates a meaningful difference.

Key zones inside a fired heater

Understanding the two main sections of a fired heater is essential before working through any procedure. All temperature, pressure, and flow references in this library use these terms.

Radiant section

The firebox itself. Burners fire here, and heat is transferred to the process tubes primarily by radiation from the hot flame and from the refractory-lined walls. This is where the highest heat flux occurs — and where tube overheating and coking problems develop. Typical radiant section temperatures range from 750°C to over 1000°C in the gas space.

Convection section

Flue gas leaving the radiant section passes upward through the convection section, where it gives up remaining heat to process tubes and, in most modern heaters, to a preheat coil or steam generation coil. Heat transfer here is primarily by convection — hence the name. Stack temperatures leaving the convection section typically range from 150°C to 350°C depending on heater efficiency and design.

The stack

The vertical flue that carries combustion gases to atmosphere. Stack height creates the natural draft that draws air into the burners. Stack dampers control draft and therefore airflow. The stack is also the source of the most visible indicator of combustion quality — smoke colour and density.

Graphic · Radiant & Convection Section Detail
Insert labelled diagram showing radiant section, convection section, bridgewall, shock tubes, stack, and process tube arrangement. Replace this block when graphic is available.

Key hazards

Fired heaters sit at the intersection of flammable process fluids, high temperatures, and a live flame. The hazards below are covered in depth in Modules 03 and 04. Every operator working on a fired heater should be able to describe each of them without prompting.

Firebox explosion
Unburned fuel accumulating in the firebox can ignite explosively when an ignition source is introduced. Most commonly associated with improper light-off procedure or failure to re-purge after a flame-out. Potentially fatal.
Tube rupture
Overheated or corroded process tubes can fail, releasing hot hydrocarbons directly into the firebox. Can escalate rapidly to a major fire. Early recognition of tube hot spots is a critical operator skill.
Flame-out
Loss of flame — from low fuel pressure, air ingress, or excessive draft — allows unburned fuel to enter the firebox. Hazardous if not detected and responded to immediately. Requires controlled shutdown and re-purge before re-ignition.
Tube coking
Carbon deposits building on the inside of process tubes reduce heat transfer, causing tube wall temperatures to rise progressively. Left unaddressed, leads to tube overheating and failure. Monitored through coil outlet temperature trends.
Refractory failure
Damaged or fallen refractory exposes the heater shell to radiant heat, causing hot spots and shell distortion. Can also disrupt draft and flame pattern. Visible on external shell inspections and infrared surveys.
Bridgewall overtemperature
High flue gas temperature at the exit of the radiant section indicates either over-firing, poor combustion distribution, or loss of convection section duty. Left uncorrected, damages convection tubes and reduces overall heater life.
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Danger — firebox explosion risk
Never attempt to ignite a burner without confirming a full firebox purge. This is the single rule that prevents the most catastrophic fired heater incidents. It applies every time, without exception — after a flame-out, after maintenance, after any period with fuel in the box.

How to use this reference

This library is organised to support two modes of use: working through it as a structured learning resource, or jumping directly to a specific topic when you need it.

Site-specific limits
Operating limits — temperatures, pressures, flow rates, alarm setpoints — vary between heaters and between sites. The Quick Reference section of this library provides typical ranges as a guide. Always confirm limits against your site-specific documentation before use.