Petroleum Refining Processes: Refinery Units, Yields and Margin – Dubai, 8–19 Mar 2027
DestinationDubai
Dates8 – 19 March 2027
Reference161_10298
This session
8–19 Mar 2027
This Petroleum Refining Processes: Refinery Units, Yields and Margin session in Dubai runs from Monday 8 March to Friday 19 March 2027 (week 10, Q1 2027). It is the 2nd of 2 dates in Dubai in 2027, at a fee of 35,100 SAR, the same for each of them. Registration is open for this date. It is held in person at Five-star CBD venue.
DatesMonday 8 Mar – Friday 19 Mar 2027
Week10 of 2027
Duration12 days
Fee35,100 SAR
StatusOpen for registration
FormatIn person
VenueFive-star CBD venue
Programme overview
Introduction:
Petroleum refining processes lose value when crude is bought without reading its assay, conversion units run at severities that no longer suit the crude slate and products are blended with costly giveaway. This Core Concept course takes refinery engineers from crude characterisation, configuration and complexity through distillation, reforming, isomerisation, hydrotreating and hydrocracking in week one. Week two moves to fluid catalytic cracking, coking and residue upgrading, alkylation, sulphur recovery, product blending and refinery margin. Participants build a Refinery Process Yield and Margin Assessment for a configuration of their own.
Course Objectives:
Interpret a crude oil assay and predict how a change of crude slate shifts cut yields, sulphur load and downstream unit feed quality
Classify a refinery by configuration and Nelson Complexity Index and explain how each process unit adds conversion and product value
Diagnose yield and product quality problems in crude and vacuum distillation, catalytic reforming, isomerisation, hydrotreating and hydrocracking units
Evaluate fluid catalytic cracking, coking and alkylation operating choices by their effect on conversion, light olefins, coke make and gasoline pool octane
Assess sulphur recovery and amine treating performance and the utilities and emissions burden of a refinery configuration
Build a product blend and a refinery yield and margin estimate using crack spreads and linear programming results to support crude and operating decisions
Target Audience:
Process engineers accountable for the yields, severity and run length of refinery conversion and treating units
Technical services engineers who monitor unit performance, catalyst condition and product quality against targets
Planning and scheduling engineers who evaluate crude slates, run refinery models and set monthly operating plans
Operations supervisors who run distillation, reforming, cracking and treating units on shift
Product blending and oil movement engineers who certify gasoline, diesel and fuel oil batches against specifications
Refinery project and licensing engineers who compare process options for new or revamped units
Course Outline:
Day 1: Crude Oil Characterisation, Assays and Refinery Configurations
Crude Oil Assay Reading: API Gravity, Sulphur, TAN, Metals and Carbon Residue
True Boiling Point Curve and Cut Yield Prediction by Fraction
Hydrocarbon Families: Paraffins, Naphthenes, Aromatics and Their Product Value
Refinery Configuration Types: Topping, Hydroskimming, Cracking and Coking
Nelson Complexity Index Calculation from Unit Capacities and Complexity Factors
Day 2: Atmospheric and Vacuum Distillation
Desalter Operation: Wash Water, Emulsion Breaking and Salt Removal Efficiency
Crude Distillation Unit Flash Zone, Stripping Steam and Overflash Control
Side Draw Cut Point Setting and Fraction Gap and Overlap Assessment
Vacuum Distillation Unit Ejector System, Wash Bed and Gas Oil Recovery
Vacuum Residue Quality: Metals, Asphaltenes and Downstream Feed Suitability
Day 3: Naphtha Upgrading: Catalytic Reforming and Isomerisation
Naphtha Hydrotreater as Reformer Feed Protection Against Sulphur and Nitrogen Poisons
Catalytic Reforming Reactions: Dehydrogenation, Dehydrocyclisation and Hydrocracking Losses
Semi-Regenerative Versus Continuous Catalyst Regeneration Reformer Operation
Reformer Severity, Octane, Hydrogen Yield and Reformate Aromatics Trade-Off
Light Naphtha Isomerisation: Once-Through Versus Recycle Schemes and Octane Gain
Day 4: Hydrotreating and Hydrocracking
Hydrodesulphurisation Chemistry: Sulphur Species Reactivity and Hydrogen Consumption
Distillate Hydrotreater Catalyst Loading, Grading and Pressure Drop Behaviour
Hydrotreater Temperature Programme, Catalyst Deactivation and End-of-Run Criteria
Hydrocracker Flow Schemes: Single-Stage, Once-Through and Two-Stage Recycle
Hydrocracker Conversion, Middle Distillate Selectivity and Refinery Hydrogen Balance
Day 5: Week-One Case: Crude Slate Change and Primary Unit Yields
Case Data Pack: Two Crude Assays and a Hydroskimming Refinery Flowsheet
Cut Yield Comparison for Light Sweet Versus Heavy Sour Crude Feed
Reformer and Isomerisation Response to a Changed Naphtha Composition
Distillate Hydrotreater Sulphur Load and Hydrogen Demand Under the New Slate
Week-One Findings Review and Assessment Scope Setting for Each Participant Refinery
Day 6: Fluid Catalytic Cracking
FCC Riser, Reactor and Regenerator Circuit and Catalyst Circulation
Zeolite Catalyst Formulation, Equilibrium Catalyst Testing and Additives
FCC Heat Balance: Coke Burn, Regenerator Temperature and Catalyst-to-Oil Ratio
FCC Feed Quality Effects: Metals, Carbon Residue and Feed Pretreatment
Delayed Coker Drum Cycle, Furnace Outlet Temperature and Coke Yield
Petroleum Coke Grades: Fuel, Anode and Needle Coke Quality Drivers
Residue Upgrading Options: Visbreaking, Solvent Deasphalting and Residue Hydroprocessing
Alkylation Chemistry: Isobutane to Olefin Ratio and Alkylate Octane
Sulphuric Acid Versus Hydrofluoric Acid Alkylation Operating and Safety Comparison
Day 8: Sulphur Recovery, Amine Treating, Utilities and Environmental Overview
Amine Treating Units: Solvent Selection, Rich Loading and Regenerator Stripping
Sour Water Stripping and Ammonia Handling Ahead of Sulphur Recovery
Claus Process Thermal and Catalytic Stages and Sulphur Recovery Efficiency
Tail Gas Treating Options and Stack Sulphur Dioxide Emissions Overview
Refinery Utilities Overview: Hydrogen Plant, Steam, Fuel Gas and Energy Intensity
Day 9: Product Blending, Specifications, Yields and Refinery Margin
Gasoline Pool Blending: Octane, Vapour Pressure and Blending Index Methods
Diesel and Jet Fuel Specification Control: Sulphur, Cetane, Flash and Cold Flow
Blend Giveaway Measurement and Recipe Adjustment Against Specification Limits
Crack Spread Benchmarks: 3-2-1 Margin and Gross Product Worth per Barrel
Refinery Linear Programming Overview: Crude Valuation and Unit Severity Cases
Day 10: Capstone: Refinery Process Yield and Margin Assessment
Capstone Build: Crude Slate and Configuration Profile for a Participant Refinery
Capstone Build: Unit-by-Unit Yield Map from Distillation to Conversion
Capstone Build: Product Blend Plan and Specification Risk Register
Capstone Build: Margin Estimate and Ranked Crude and Severity Options
Assessment Presentation to a Refinery Technical Review Panel
Skills You Will Gain:
Crude Assay Interpretation
Refinery Complexity Benchmarking
Distillation Cut Point Control
Reformer Severity Management
Hydroprocessing Catalyst Monitoring
FCC Heat Balance Analysis
Sulphur Plant Performance Review
Gasoline and Diesel Blending
Why Attend This Course:
Return with a Refinery Process Yield and Margin Assessment built on the crude slate and units of your own site
Progress from crude, distillation, reforming and hydroprocessing in week one to cracking, coking, alkylation, sulphur recovery, blending and margin in week two
Question crude purchases, catalyst change-outs and severity targets with yield and margin evidence rather than habit
Compare unit practice with refinery engineers working on simple and high-complexity configurations in several markets
Conclusion:
Refinery value depends on how each unit turns a changing crude slate into saleable products. Week one builds that understanding from crude assays and configuration through distillation, reforming, isomerisation, hydrotreating and hydrocracking, closing with a crude slate case. Week two adds fluid catalytic cracking, coking and residue upgrading, alkylation, sulphur recovery and amine treating, product blending, crack spreads and planning models. The final day produces a Refinery Process Yield and Margin Assessment ready for technical review.
Petroleum Refining Processes: Refinery Units, Yields and Margin runs in Dubai over 12 days, with 2 upcoming dates in Dubai. The course fee is 35,100 SAR.
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