Refinery operations · Commissioning and start-up · Operator competency

Operational readiness doesn’t end at handover.

It ends when the plant runs steadily with its own people. I’m Roger Tablero. For 27 years I have worked on that gap in refineries in Venezuela, Kuwait, Malaysia and Angola, from field operator to Operations Coordinator.

Portrait of Roger Tablero
Valencia, Spain · Cabinda, Angola
years in refining
27
plants I joined before they reached steady operation
4
with units I started up
3

Why start-ups struggle

Refineries rarely struggle at start-up because of equipment. They struggle because three things were built separately.

  1. Procedures

    Written by people who will not execute them.

  2. Training

    It ends on handover day.

  3. Control systems

    The operator meets them for the first time with the plant already running.

The operator is the one who has to make them fit, on shift. Operational readiness means building the three together and staying until the plant runs steadily with its own people.

I know it from both sides

Sincor, a strategic association of Total, Statoil and PDVSA, trained me for two years before its upgrader started: six months of theory, a year in the field at an operating refinery, then the commissioning of my own unit. They called it world-class training. Today we would call it operational readiness. Later I was on the other side: I trained new technicians in the field at Pengerang and, at Cabinda, designed role-based training for around 40 operators.

Four plants, by phase

Each plant shows the phases of its life I worked through.

Operator trainingPre-commissioningCommissioningStart-upSteady operationScheduled turnarounds
Sincor, later PDVSA PetrocedeñoVenezuela · 1999–2018workedworkedworkedworkedworkedworked
Al Zour refineryKuwait · 2018–2021workedworkednot part of my time therenot part of my time therenot part of my time therenot part of my time there
Pengerang refineryMalaysia · 2021–2024workednot part of my time thereworkedworkedworkedworked
Cabinda RefineryAngola · 2024–todayworkednot part of my time thereworkedworkedworkedworked
  1. 01Venezuela · 1999–2018

    Sincor, later PDVSA Petrocedeño

    Extra-heavy crude upgrader

    Field operator to Operations Superintendent

    Two years of training before start-up, then pre-commissioning, commissioning and first start-up of the delayed coker. Every role up to Operations Superintendent. Four major scheduled turnarounds, one of them as operations lead for the coker in 2014.

  2. 02Kuwait · 2018–2021

    Al Zour refinery

    ARDS complex, three units of 110,000 b/d

    Panel and field operator

    A year in the field learning the units (line tracing, systems, tags, manuals and exams), three months of DCS training with Honeywell, then pre-commissioning of the three ARDS units. The pandemic pushed the start-up back, and I left before it.

  3. 03Malaysia · 2021–2024

    Pengerang refinery

    ARDS and hydrogen compression, 300,000 b/d refinery

    Senior field operator

    I joined after the refinery’s first start-up. Re-commissioning and restart of two ARDS units and the hydrogen compression unit, scheduled shutdowns for catalyst change-out on both units, and field training of new technicians.

  4. 04Angola · 2024–today

    Cabinda Refinery

    New 30,000 bpd hydroskimming refinery

    Operations Coordinator

    Coordination of process operations through commissioning and the transition to stable operation, design of role-based training for around 40 operators, operations input to the scope and sequences of scheduled turnarounds, and design of the operations management system.

What I have built

Systems, methods and records that stayed in use after I built them.

A model for running operations

I designed a management model for the operations department of a refinery, built from its real context and meant to evolve with it. One framework holds three components together.

The framework

Steady Operation Model

It ties together the whole management environment of operations: how people are trained, how decisions are made, how information flows, and the documents and programs underneath. Its purpose is that these work as one system, aimed at safety, reliability, quality and efficiency. A certification such as ISO 9001 rests on that maturity.

  • People

    Role-Based Competency

    On-the-job training structured by role: field technician, lead technician and control room technician. Each role has a package with the knowledge and skills the job demands, a diagnostic assessment that shows strengths and gaps, and a certification assessment. It covers about 40 operators. It turns operating experience into verifiable competence and reduces dependence on informal knowledge.

  • Decisions

    Operating Rhythm

    It sets who decides what, with which information and how often, through three cadences: daily coordination, weekly planning and monthly performance review. It relies on indicators, action and risk management, structured problem solving, and authority and responsibility matrices. Its aim is to align the organization at every level and turn each deviation into a decision with an owner and a deadline.

  • Information

    Single Record

    It starts from a conviction: information is one of the most valuable assets an operation has. The Single Record supports the workflow of the shift, from control readings and shift events to work instructions, tank volumes, chemical stock, and daily, monthly and executive reports. It is designed so that each piece of data is captured once and stays traceable.

Document framework and operating programs

Role-Based Competency prepares the people, the Operating Rhythm orders the decisions, the Single Record carries the information and the workflow, and the Steady Operation Model holds them together.

Also built

  • Document framework

    An ISO 9001:2015 framework for operations, designed as my engineering thesis: procedure taxonomy, templates, a writing guide and a workflow to create, track and review each document. More than 200 procedures and work instructions are built on it, along with the operations manual and the KPI manual.

  • Tank capacity and stock control

    Recalculated alarm and trip levels for crude and product tanks, using API 2350 and ISA 18.2 as operating guides. Setpoints came from measured field times: valve travel, system line-up and the operator’s walk to the farthest tank. Working volume rose to about 85% of capacity within safety and mechanical integrity limits, and the refinery’s stock sheet was built on that basis.

  • Technical record

    Commissioning reports, technical specifications for process and control modifications, and root cause analyses delivered as formal reports.

Earlier in my career

  • Delayed coker · method

    5days, against about 20 for the contracted cleaning

    Five days instead of twenty

    As operations engineer I designed an in-house method to clean the cutting water tank, with an unplanned 15-day shutdown window and no time to hire the contractor. The idea came from the coke drums: with a thin jet, the crews clearing the drum bottom only cut the coke at the flange and nothing flowed; with a thick, smooth, abundant stream, the coke broke up and flowed. I reasoned that the contractor’s hydrojet did what the thin jet did, which is why that cleaning took so long. We fluidized the settled coke from the top with a portable fire monitor and pumped it from a bottom nozzle to the coke pit with a rented slurry pump. Our own operations crew finished in five days, with no confined space entry. The contracted cleaning used to take about twenty.

    Pressure cuts, flow carriesWashing out a 5,000 m³ tank holding up to 6.3 m of coke fines
    Diagram of the cutting water tank wash-out: a fire monitor fluidizes the coke fines from the top and a rented diesel pump sends them to the coke pit. 5 days of washing; it used to take 20.Fire monitorwith 1 m of 1" pipeCutting water tank19 m tallSmooth stream:breaks up the bedand sets it runningCoke finesup to 6.3 mRented diesel pump,1,600 GPM, on an8" nozzle6" valve:regulates the flow to the pitFixed scaffold,tied to the tankFire water, 11 barg,two hosesSettlingbasinsCoke pitkeeps the coke and gives the water back
  • Gas recovery unit · root cause

    1lubrication hole instead of 2

    One bearing, found by elimination

    After a major turnaround, the gas recovery compressor kept tripping on vibration during its automatic ramp-up. I was asked to lead a multidisciplinary team to find out why. We evaluated the train as a whole (motor, Voith coupling and compressor), normalized what could be normalized, and ruled out causes one by one with tests, without changing the scenario. The root cause was a bearing in the Voith, on the compressor side, that did not match the specification: one lubrication hole instead of two. With the correct bearing, the compressor started without problems, in automatic and in manual.

    It only tripped in automaticGas recovery compressor · coker unit
    Diagram of the motor, Voith coupling and gas recovery compressor train. The compressor-side bearing had 1 of 2 lubrication holes; in automatic start-up the slow ramp kept the machine in the vibration zone and it tripped.DCSVibration: normalBently Nevada → ESDHigh vibration: tripMotorVoith fluidcouplingSame oil for driveand lubricationCompressor-sidebearingCompressor

    Why only in automatic

    Ruled out one by one, with tests

    1. Instrumentationwith a checklist
    2. Oilanalysed and replaced
    3. Heat exchangersclean
    4. Voithinspected
    5. Uncoupled runfault in the Voith
  • Delayed coker · turnaround

    2014one of four major scheduled turnarounds

    Operations lead for a scheduled turnaround

    In 2014 I led the delayed coker’s turnaround on behalf of operations. Over those years I planned and directed its scheduled shutdowns and start-ups, and delivered improvement projects on slide valves and heavy diesel filters.

  • Distillation and coking · quality

    12years apart: 2013 and 2025

    A quality system, twelve years apart

    In 2013 PDVSA Petrocedeño recognized my contribution to implementing the Quality Management System for the distillation and coking sub-process. In 2025 I designed one from the ground up.

Talks and writing

  • Guest lecture · 2024

    Petroleum Refining: Fundamental Processes and Their Importance in the Petrochemical Industry

    Two-hour online lecture for final-semester Petrochemical Engineering students, Universidad Yacambú.

  • Engineering thesis · 2025

    Quality Management System in the Operations Area of the Cabinda Refinery according to ISO 9001:2015, Section 8.5.1

    Universidad Yacambú. Highest academic index of the graduating class.

  • LinkedIn · 2026

    Hired to operate a plant that did not exist yet

    How Sincor prepared its operators for two years before start-up, and why operational readiness does not end at handover. In Spanish.

    Read the post

Education

  • Industrial Engineer, Universidad Yacambú, 2025. Highest academic index of the class.
  • University Technician in Chemistry, Chemical Processes, IUT José Antonio Anzoátegui, 1998. Merit diploma.

Compare notes

If you work on commissioning, start-up or operator competency, I would like to hear how you do it.

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