Open, wind-driven areas
On naturally ventilated decks a release disperses before it reaches a point detector. Placement has to follow prevailing wind and dispersion behaviour, not the geometry of the plot plan.
Fire and gas detection across the full hydrocarbon chain — wellhead and offshore production, pipelines and terminals, refining and processing.
No single detection philosophy covers the whole hydrocarbon chain. A wellhead platform, a pipeline compressor station and a refinery process unit share an industry and almost nothing else — the gases differ, the ventilation differs, the manning levels differ, and so does what a missed detection actually costs. A layout copied from one segment into another will pass a drawing review and fail in service.
ZE-Tronics engineers, supplies, installs, commissions and calibrates fire and gas safety systems across all three segments, and treats each one on its own terms. We have worked in Azerbaijan’s oil and gas sector since 2012, as an authorised partner of the manufacturers whose equipment the specifications name, with our own engineering, installation and calibration capability in country.
Open, naturally ventilated installations where gas disperses quickly and detector placement is governed by wind behaviour rather than by plot geometry. Point detectors alone under-perform here: a release that never crosses a sensor is a release that is never seen. The combination that works is open-path infrared across the likely dispersion corridors, backed by ultrasonic leak detection for high-pressure releases that vent to atmosphere before they can form a measurable cloud.
Offshore and near-shore installations add salt, vibration and constant weather to the specification. Enclosure ratings, cable gland selection and mounting design matter as much as the sensor technology; a correctly chosen detector on a poorly engineered bracket is a maintenance problem waiting to happen.
Long, thinly manned assets where the first responder is often a control room hundreds of kilometres away. Detection has to remain reliable without frequent attention, and the system has to communicate meaningfully rather than simply raise an alarm. Digital detector diagnostics, drift trending and historical logging turn a maintenance visit from a fixed calendar event into a decision based on evidence.
Dense process units, many simultaneous hazards, and consequences that escalate quickly from one unit to the next. Coverage assessment matters more here than anywhere else. A detector layout that looks complete on a plot plan can leave real gaps at grade level, under structures and behind large equipment — the places where a heavy hydrocarbon vapour actually collects.
NFPA 72, NORSOK and UK HSE guidance all point the same way: the fire and gas system should not depend on the process control system for its safety function. It must act on what it detects and then inform the control system of what it has done. What none of them prescribe is how that interface should be built. That is an engineering decision, and it is where a lot of otherwise well-specified systems become fragile.
We design the interface deliberately — hardwired for the actions that must never depend on a communication link, serial or fieldbus for the status, diagnostics and trending that make the system maintainable. The result is a safety layer that survives a control system fault and still gives operations a single, coherent picture.
Most oil and gas work is brownfield, and the constraint is rarely technical. It is permits, isolations and the discipline of impairment planning. Every hour a detection loop is out of service is an hour of reduced protection that has to be recorded, time-bounded and compensated for by other means. We plan modifications around turnaround windows wherever the schedule allows, and we say clearly when it does not.
A gas detector that has not been calibrated is an assumption, not a measurement. Catalytic sensors drift and can be poisoned; infrared sensors need their optics verified; electrochemical cells age. Our in-house laboratory is accredited to AZS ISO/IEC 17025:2020 for both fixed and portable gas detection, so calibration is traceable rather than nominal. Our electronics repair bench handles flame, gas and smoke detectors and their controllers in country, which removes weeks of shipping from every fault.
Fire and gas systems fail at the handover points between vendors. A detector specified correctly at FEED, procured against the wrong certification, mounted where a dispersion study says it will never see a release, and calibrated on a schedule that ignores its own drift history is a detector that protects nobody. Owning the whole chain — design, certified supply, installation, commissioning, accredited calibration and lifecycle support — removes those seams, and with them most of the ways the system can quietly stop working.
See our full service range, or send us a plot plan and talk to our engineers.
On naturally ventilated decks a release disperses before it reaches a point detector. Placement has to follow prevailing wind and dispersion behaviour, not the geometry of the plot plan.
A jet release from a high-pressure line can vent to atmosphere without ever building a concentration at a sensor. Ultrasonic leak detection hears the release itself.
On pipelines and compressor stations the first responder is a control room hundreds of kilometres away. The system has to be dependable without frequent attention and communicate meaningfully, not just alarm.
In refining, a fire in one unit becomes a fire in the next. Coverage that looks complete on a drawing can leave real gaps at grade level and beneath structures.
Fire and gas systems fail at the handover points between vendors. We own every step, so there are none.
Yes. Most oil and gas work is brownfield. We plan around permit-to-work discipline, isolation management and formal impairment planning, so every hour a detection loop is offline is recorded, time-bounded and compensated for. Where the schedule allows, modifications are aligned to turnaround windows.
Not by spacing rules alone. We use fire and gas mapping in line with ISA TR84.00.07, which produces a stated coverage percentage for a defined release size and a defined fire size. That gives the operator a number to accept or challenge, rather than an opinion.
Yes. The fire and gas system stays independent of the process control system, as NFPA 72, NORSOK and HSE guidance all require, while communicating status and required actions to it. We build the interface — hardwired, serial or fieldbus — to suit the existing architecture.
Both. We are an authorised partner of international fire and gas manufacturers and supply original, certified equipment against the project specification, with stock staged in Baku and London to shorten lead times.
We do, in our own AZS ISO/IEC 17025:2020 accredited laboratory, for both fixed and portable gas detection. We also run an electronics repair bench for flame, gas and smoke detectors and their controllers, which avoids sending units abroad.
Send us a plot plan, an equipment list or a scope of work. Our engineers reply within one business day.
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