Process Utility Systems: Instrument Air, Nitrogen, Steam, Water and Fuel Gas – Paris, 7–18 Dec 2026
DestinationParis
Dates7 – 18 December 2026
Reference763_19640
This session
7–18 Dec 2026
This Process Utility Systems: Instrument Air, Nitrogen, Steam, Water and Fuel Gas session in Paris runs from Monday 7 December to Friday 18 December 2026 (week 50, Q4 2026). It is the only date in Paris in 2026, at a fee of 42,300 SAR, the same for each of them. Registration is open for this date. It is held in person at Right Bank business hotel.
DatesMonday 7 Dec – Friday 18 Dec 2026
Week50 of 2026
Duration12 days
Fee42,300 SAR
StatusOpen for registration
FormatIn person
VenueRight Bank business hotel
Programme overview
Introduction:
Process utility systems keep every unit running, yet a wet instrument air header, a nitrogen shortfall during purging, a collapsed steam header or unstable fuel gas pressure can trip a whole refinery or gas plant within minutes. Many sites still manage each utility in isolation, without a shared balance or a clear view of which units fail first. This Core Concept course trains utility and process staff to map, operate, balance and troubleshoot air, nitrogen, steam, water, fuel gas and flare services as one network. Participants produce a Utility System Reliability and Failure-Impact Study for a case plant.
Course Objectives:
Build a site utility balance and consumer register that shows generation, demand and spare capacity for each utility header
Operate instrument air, plant air and nitrogen generation packages to hold pressure, dew point and purity within the limits consumers need
Control steam, condensate, cooling water, demineralised water and potable water distribution so each header stays stable under load changes
Run fuel gas conditioning and verify flare, relief and closed drain headers are ready to receive loads from process units
Analyse loss-of-utility scenarios and rank their process impact, recovery time and required sparing
Measure utility energy use and reliability with metering and indicators, and diagnose recurring utility faults from header trends
Target Audience:
Utility operators who run compressors, dryers, nitrogen packages, letdown stations and water treatment trains on shift
Process engineers who set utility demand for their units and assess the effect of utility upsets on production
Maintenance and reliability engineers who keep utility rotating and static equipment available and plan sparing
Utility area supervisors who authorise header line-ups, load shedding and standby equipment changeovers
Energy and performance engineers who meter and allocate air, nitrogen, steam and fuel gas consumption
Course Outline:
Day 1: Utility Roles, Site Utility Balance and Header Mapping
Utility Block Diagram: Air, Nitrogen, Steam, Water, Fuel Gas and Flare Interfaces
Site Utility Balance Sheet: Generation, Consumers and Headroom per Header
Utility Consumer Register Built from P&IDs and Line Lists
Header Pressure Levels and Tie-In Points Between Process Units and the Utility Area
Utility Criticality Ranking by Units That Trip on Loss of Each Service
Day 2: Instrument Air and Plant Air Generation
Screw, Centrifugal and Reciprocating Air Compressor Selection and Load-Unload Control
Air Receiver Sizing for Hold-Up Time After a Compressor Trip
Refrigerated Versus Heatless and Heated Desiccant Dryer Selection by Pressure Dew Point
Instrument Air Quality Limits for Particles, Moisture and Oil Content
Instrument Air Priority Valve and Plant Air Shedding Logic
Day 3: Nitrogen Generation, Blanketing and Purging
PSA Nitrogen Generator Cycle with Carbon Molecular Sieve Beds
Hollow Fibre Membrane Nitrogen Units and the Purity Versus Flow Trade-Off
Liquid Nitrogen Storage and Vaporiser Backup for Peak and Emergency Demand
Tank Blanketing Regulators and Breather Valve Settings
Purge Volume Calculation for Equipment Freeing and Oxygen Analyser Verification
Day 4: Steam and Condensate Distribution Networks
High, Medium and Low Pressure Steam Header Control and Letdown Station Design
Desuperheater Sizing and Spray Water Supply at Letdown Stations
Turbine Extraction and Exhaust Steam in the Header Balance
Condensate Collection, Contamination Monitoring and Polishing Before Return
Drip Leg Spacing and Trap Station Layout on Long Steam Mains
Day 5: Week-One Case: Air, Nitrogen and Steam Header Integration
Case Plant Air Demand Profile Versus Installed Compressor Capacity
Dryer Dew Point Excursion Case and Moisture Carryover to Valve Positioners
Nitrogen Header Pressure Decay Case During Simultaneous Purging Jobs
Steam Header Collapse Case After a Letdown Valve Failure
Week-One Utility Balance Update and Header Findings Log
Day 6: Cooling Water, Demineralised Water and Potable Water Distribution
Once-Through, Open Recirculating and Closed Loop Cooling Water Circuits
Cooling Water Supply and Return Header Hydraulics and Exchanger Allocation
Demineralisation Train with Cation, Anion and Mixed-Bed Ion Exchange Regeneration
Demineralised Water Storage with Conductivity and Silica Monitoring
Potable Water Network Segregation, Backflow Prevention and Chlorine Residual Checks
Day 7: Fuel Gas, Flare, Relief and Closed Drain Headers
Fuel Gas Knock-Out, Heating and Margin Above Hydrocarbon Dew Point
Fuel Gas Mixing Drum and Pressure Control to Fired Equipment
Flare Header Back Pressure, Knock-Out Drum and Water Seal Drum Operation
Flare Purge Gas and Pilot Gas Supply Reliability
Closed Drain Header, Drain Drum Pump-Out and Hydrocarbon Routing
Day 8: Utility Failure Cases, Process Impact and Operating Interfaces
Loss of Instrument Air: Valve Fail-Safe Positions and Unit Response
Loss of Cooling Water: Relief Load Generation and Flare Header Impact
Loss of Steam, Power or Nitrogen: Cascading Effects Across Process Units
Failure Mode and Effects Analysis Worksheet for Utility Equipment
Day 9: Reliability, Redundancy, Energy Use and Metering
N+1 and Duty-Standby Sparing Philosophy for Compressors, Pumps and Generators
Reliability Block Diagram and Availability Calculation for a Utility Train
Utility Metering Plan with Flow Meters, Totalisers and Allocation to Units
Specific Energy of Compressed Air, Nitrogen and Steam per Unit Delivered
Utility Indicator Dashboard for Header Stability, Leak Rate and Standby Readiness
Day 10: Capstone: Utility System Reliability and Failure-Impact Study
Utility Troubleshooting Drill Using Header Trends and Operator Logs
Capstone Case Plant Utility Map and Criticality Matrix
Capstone Failure-Impact Scenarios with Recovery Times per Utility
Utility System Reliability and Failure-Impact Study Assembly
Study Presentation to a Mock Plant Technical Review Panel
Skills You Will Gain:
Utility Balance Construction
Compressed Air Dryer Selection
Nitrogen Purity and Purge Control
Steam Header Letdown Control
Fuel Gas Conditioning
Flare Header Readiness Checks
Utility Failure Mode Analysis
Utility Metering and Allocation
Why Attend This Course:
Leave with a Utility System Reliability and Failure-Impact Study for a case plant, reviewed by a mock technical panel
Spot the weak utility header before it trips a unit, using trends, balances and a criticality ranking
Justify spare compressors, nitrogen backup or metering to management with availability and impact figures
Compare utility practice with operators and engineers from refining, petrochemicals, gas processing and power generation
Conclusion:
Utilities fail quietly and then all at once, so plants need a single view of how air, nitrogen, steam, water, fuel gas and flare services support each unit. Week one builds the utility balance and works through instrument air, nitrogen and steam headers in a guided case. Week two adds cooling, demineralised and potable water, fuel gas and flare headers, loss-of-utility cases, sparing, metering and troubleshooting. The final day produces a Utility System Reliability and Failure-Impact Study ready for plant review.
Process Utility Systems: Instrument Air, Nitrogen, Steam, Water and Fuel Gas runs in Paris over 12 days, with 2 upcoming dates in Paris. The course fee is 42,300 SAR.
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