Delayed coker automation · drum switch sequencing · hydraulic cutting control

Decoking Control

Automated drum switching, hydraulic coke cutting, and steam/quench cycle control for delayed coker units, replacing manual and semi-manual processes with a consistent, interlocked, and auditable automated sequence that protects personnel and equipment.
Oil refinery process towers and distillation columns

Control

Delayed coker automation for safe, consistent, and efficient operations

Delayed coking is one of the most hazardous operations in refinery service. The decoking cycle, draining and cooling the coke drum, opening the drum head, hydraulically cutting the coke, closing the drum, and returning to service, involves high-temperature steam, high-pressure water, heavy rotating equipment, and heavy coke handling in an environment that demands precision and discipline at every step. Automating this sequence does more than improve efficiency, it eliminates the human errors that have caused the most serious decoking accidents in refinery history.

 

We design decoking control systems that automate the complete coker operating cycle, from feed switching and drum filling to steam stripping, quench sequencing, drum head removal permissives, hydraulic cutting tool control, and return to service. Every step is interlocked against completion of the preceding step, with verification of valve position, temperature, pressure, and equipment status before the sequence advances. The result is a decoking operation that is consistent from cycle to cycle, fully documented in the control system’s event log, and protected against the sequence errors that cause most decoking incidents, developed to IEC 61131-3 so proven strategies deploy on the platform that best fits your lifecycle, with full logic access.

Oil refinery at dusk representing operational risk

The Problem

Most decoking accidents are sequence errors, not equipment failures

The decoking cycle has specific sequence requirements at every step: feed cannot switch to the new drum until the old drum temperature confirms the coke bed has solidified; the drum cannot be opened for cutting until pressure and temperature are within safe limits; the hydraulic cutting tool cannot be lowered until the top unheading device confirms the drum head is clear; and the drum cannot be returned to service until all cutting tool equipment is clear and the drum is confirmed ready. In a manual or semi-manual operation, each of these verifications depends on operator attention and discipline, and under shift-change pressure, production-schedule pressure, or simple fatigue, they can be rushed or skipped.

 

The consequences are severe. Drum switching before coke solidification can carry liquid over into the fractionator. Opening a drum head before pressure is verified has caused catastrophic hydrocarbon releases and fires. Advancing the cutting cycle before the tool is in position damages the cutting assembly. And thermal cycling from inconsistent quench sequences accelerates coke drum fatigue, the leading cause of drum failure and the multi-million-dollar repairs that follow. Automation does not just prevent accidents; it extends the economic life of the coke drums by delivering consistent thermal cycles every time.

Capabilities

Decoking control capabilities

We automate the complete decoking cycle, from drum switching and steam stripping through hydraulic cutting and return to service, as an integrated, interlocked, and fully auditable control system. Click any capability to expand the full technical detail.

Drum Switching and Feed Transfer Automation

The coke drum switching sequence transfers feed from the full drum to the empty drum through a carefully sequenced operation involving the switch valve, drum inlet valve, steam purge, and fractionator interface. We automate this complete switching sequence with interlocks that verify the receiving drum is pressurized, the inlet and outlet valves are confirmed in position, and the fractionator interface is configured for the new feed path before feed is transferred. Switching time is minimized while all safety verifications are completed.

Drum Head Opening Permissive System

The drum head opening permissive system verifies that the drum is in a safe condition before authorizing unheading device operation. We implement a drum head permissive logic that confirms drum pressure is at or below the safe unheading pressure, drum temperature at the top head is within limits, the drain valve is confirmed open, and steam connections are confirmed isolated. The permissive is implemented as a hardwired interlock with a dedicated permissive status indicator at the operator interface, not as a software advisory that can be acknowledged and bypassed.

Steam Stripping and Cooling Sequence Control

After the drum is full and the feed is switched, the drum is steamed out to strip residual hydrocarbons before water quench begins. We control the steam injection rate, steam temperature, and overhead vapor handling during the stripping phase, with monitoring of drum skin temperature distribution to verify that the drum is stripping uniformly. The transition from steam to water quench is interlocked against completion of the stripping phase criteria, preventing premature water quench that can cause drum shell cracking from differential thermal shock.

Hydraulic Cutting Tool Control

The hydraulic cutting tool (drill bit and water jet cutter) requires precise control of tool rotation speed, vertical travel rate, cutting water pressure, and flow rate for effective coke removal. We design the cutting tool control system, including the hydraulic drive control, winch speed and position control, water pump pressure and flow control, and the cutting sequence logic for initial pilot drilling and full-bore cutting passes. Cutting completion verification uses coke bed level tracking and visual camera integration where provided.

Water Quench Cycle Management

The water quench phase requires careful management of quench water flow rate and drum pressure during the transition from steam to water operation. We control the quench water valve position, drum overhead pressure, and drum drain valve operation through the complete quench cycle, from initial water injection through pressure stabilization and temperature reduction to quench completion. The quench cycle sequence is logged with timestamps and temperature distribution data, providing the cycle-by-cycle record required for drum fatigue life management.

Drum Return to Service Permissive

Before a drum can be returned to service for the next fill cycle, our control system verifies a complete set of return-to-service conditions: cutting tool retracted and secured, drum head confirmed installed, drain valve confirmed closed, steam lines confirmed connected, and drum pressure testing completed if required. All return-to-service permissives are logged with timestamps and operator identification in the event log, providing the auditable record required for process safety management documentation.

Thermal Cycle Monitoring and Drum Life Management

Delayed coke drum thermal cycling fatigue is the primary cause of drum shell cracking and drum replacement. We integrate coke drum skin thermocouple data into the control system and calculate the cumulative thermal cycle history, including the temperature differential between the feed-switch temperature excursion and the quench completion temperature, for comparison against the drum's design fatigue life. This data supports the drum's fitness-for-service assessment and provides the operating record required for insurance and regulatory inspection purposes.

Event Log and Sequence Documentation

Every step in the decoking sequence, valve actuation, permissive verification, operator acknowledgment, sequence hold, and alarm, is logged with timestamp, operator identity, and sequence step number in the control system's event log. This comprehensive documentation provides the real-time operating record required for process safety management, incident investigation, and the cycle data required for drum fatigue analysis. The event log is exportable in standard formats for import into the facility's process historian and safety management system.

Why Innova Technologies

Deep refinery experience applied to the most complex and hazardous process in the unit

Decoking control is not a generic sequence control problem. It requires knowledge of delayed coker operations, drum metallurgy, hydraulic cutting system behavior, and process safety requirements that we bring from real refinery project experience.
Refinery Process Knowledge
Our process control engineers have worked directly with refinery operations teams on delayed coker unit control projects, developing detailed understanding of the operational constraints and safety requirements that govern each step of the decoking sequence. This process knowledge is the foundation for the permissive logic and interlock design: we don’t design the sequence from the procedure document alone; we understand why each step has the requirements it does, and we design the control logic to protect those requirements under all foreseeable operating conditions.
Hydraulic System Engineering Integration
The hydraulic cutting tool is one of the highest-consequence mechanical systems in the decoking operation, improper control can damage the tool, the drum, or the operator platform. Our hydraulic systems engineering capability extends to cutting tool hydraulic drive design, including motor sizing, control valve selection, pressure limiting, and winch speed control, as an integrated scope with the sequence control logic. This ensures the hydraulic system performs correctly within the sequence, and that the sequence logic correctly interprets hydraulic system feedback signals.
Process Safety Management Documentation
Commissioning a decoking control system requires coordination with the operations team, the mechanical completion team, and the process safety group on a timeline often constrained by refinery turnaround scheduling. We provide detailed commissioning procedures, pre-commissioning dry-run testing using simulated valve position signals, and operations training that includes tabletop walkthrough of the complete decoking sequence before the first live cycle. Our commissioning engineers remain on site through the first complete decoking cycle to support the operations team.
Operator Interface Design for Complex Sequence Visualization
A decoking sequence with 40–60 steps requires an operator interface that clearly shows the current step, the pending permissive conditions, and the alarm status for each step, without overwhelming the operator with information not relevant to the current phase of the cycle. We design decoking HMI graphics that track the sequence status through a visual representation of the drum and associated equipment, with clear permissive status indicators that let the operator understand what is holding the sequence and what needs to be verified before advancement.
Commissioning and Training Support
A decoking sequence with 40–60 steps requires an operator interface that clearly shows the current step, the pending permissive conditions, and the alarm status for each step, without overwhelming the operator with information not relevant to the current phase of the cycle. We design decoking HMI graphics that track the sequence status through a visual representation of the drum and associated equipment, with clear permissive status indicators that let the operator understand what is holding the sequence and what needs to be verified before advancement.
Equipment and licensors we integrate

Chevron Lummus

Bechtel

Foster Wheeler

Curtiss-Wright

Z&J / Zimmermann

Flowserve

Emerson

DeltaValve

Technical Resources

Engineering documentation for decoking control

Engineering documentation developed from real delayed coker unit control projects, providing your process safety and operations teams with the technical detail needed for evaluation and specification.

What Happens During Control System Commissioning?

Control Panel Design for Harsh Industrial Environments

The Future of Turbomachinery Control Systems

FAQ

Frequently asked questions

Why should decoking permissive interlocks be hardwired rather than implemented in software?
Safety-critical permissives, particularly the drum head opening permissive, which prevents opening the drum before it is at safe pressure and temperature, should be implemented as hardwired interlocks independent of the control system software, for the same reason that fire and gas trips are hardwired: a control system software failure should not result in the loss of the safety function. A hardwired interlock uses dedicated relay logic that is physically independent of the software sequence controller, so that even a complete control system failure cannot enable the unsafe condition. We implement drum head opening permissives as hardwired relay interlocks with a permissive-enable indicator at the operator interface and in the unheading device control circuit, consistent with process safety management best practices for this type of safety-critical function.
Yes. We design decoking control systems that communicate with the refinery’s existing DCS through standard industrial protocols, OPC-UA, Modbus TCP, or EtherNet/IP. The DCS interface provides operators with real-time visibility into the decoking sequence status, drum temperatures, and alarm status, and allows DCS-level supervisory functions, such as feed rate adjustment during the switching phase, to be coordinated with the decoking sequence. The decoking control logic remains in a dedicated controller (not in the DCS) to maintain independence from the DCS scan rate and response time variability that would be unacceptable for time-critical sequence control.
Coke drum fatigue cracking results from cumulative thermal cycling, specifically, the temperature differential experienced by the drum shell during each cycle and the rate of temperature change during feed switching and quench operations. Automated control improves drum life through two mechanisms: consistency and rate management. Consistency means every cycle follows the same thermal profile, the quench rate is controlled to the same ramp, the steam stripping time is consistent, and the feed switch temperature is controlled within the same range, eliminating the outlier cycles with unusually high thermal gradients that cause disproportionate fatigue damage. Rate management means the quench water injection rate is controlled to a defined ramp profile that limits the rate of temperature change to within the drum’s design thermal shock envelope. Both mechanisms require the precise, repeatable control that an automated system provides and that manual operation cannot consistently achieve.
A complete decoking control system requires: drum skin thermocouples (typically 8–16 locations per drum for thermal monitoring and permissive functions), drum overhead and bottom pressure transmitters, feed inlet temperature and pressure measurements, drum drain valve position feedback, drum overhead vapor flow measurement, quench water flow measurement, cutting tool position transmitter (winch depth indicator), cutting water pressure and flow measurement, and hydraulic drive pressure and flow measurement for the cutting tool. Safety-critical instruments, particularly those providing inputs to hardwired permissive functions, are specified for their reliability and maintained at calibration intervals consistent with the safety function’s required availability.
The decoking control system’s scope typically ends at the drum bottom head, the coke cutting and falling into the pit, and the subsequent coke handling (conveying, dewatering, shipping), are typically managed by a separate coke handling system. The interface between the decoking control and the coke handling system typically includes: coke pit water level status (high-level alarm that can hold the cutting sequence if the pit is full), conveyor running status (required permissive before cutting), and coke cutting completion signal (from cutting tool cycle completion). We design this interface as a discrete input/output connection between the decoking control panel and the coke handling system control, with the required status signals exchanged to ensure that the two systems operate in coordination.

Automate your decoking operation and eliminate the sequence errors that cause incidents

We engineer decoking control systems that make every cycle consistent, every permissive verified, and every step documented, protecting your personnel, your equipment, and your permit.

Featured

Open, documented, maintainable control.

IEC 61131 standardized logic your team can support without OEM lock-in.

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Single-source

One team, drawing to startup.

Engineering, fabrication, installation, and commissioning under one contract.
FORMERLY PETROTECH

A New Name for the Company We've Become.

SAME PEOPLE.
SAME ENGINEERING EXPERTISE.
BROADENED HORIZONS.

A MESSAGE FROM JOHN KAZOUR, CEO

Welcome to Innova Technologies

To our customers and partners,

For more than 50 years, our team has helped customers keep critical operations running. We built our reputation as Petrotech by taking responsibility for control systems on important rotating machinery.

As more industries came to us with similar challenges across power generation, compression, and hydro applications, our engineering team kept finding ways to solve them. Eventually, the business outgrew the Petrotech name.

We are entering our next chapter as Innova Technologies. The new name reflects the full scope of our work as a rotating machinery control systems specialist. We engineer controls around the machine, deliver complete projects from design through commissioning, and provide support that stays with the problem until it is solved.

Our name is changing, but the people, engineering experience, and commitment behind the work continue. Our responsibility to active projects and installed systems carries forward under the Innova Technologies name. Your current contacts remain the right place to start, and we will communicate directly if an administrative record requires an update.

We appreciate the trust you have placed in us over the decades, and we look forward to continuing that work as Innova Technologies.

John Kazour

CEO, Innova Technologies