Fluid Flow and Hydraulics for Facilities Engineers
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Fluid Flow and Hydraulics for Facilities Engineers - SF-FFH-PEA27
| Code | Date | Time | Duration | Location | Currency | Early Bird Fee Per Person |
|---|---|---|---|---|---|---|
| SF-FFH-PEA27 | 19 - 23 Apr 2027 | 10 AM CST | 5 Days - 4 Hours / Day |
Online |
USD |
4000 |
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Fluid Flow and Hydraulics for Facilities Engineers
This training covers the fluid mechanics that facilities engineers use in practice. It works through pressure drop calculation for liquids and gases, multiphase flow behaviour in flowlines and risers, pump and compressor system hydraulics, control valve and choke sizing, and pressure traverse across a full production network. Erosion limits, velocity criteria, surge and transient effects are covered as design and operating constraints.
Description
Hydraulics determines the pressure at every point in a production system, and pressure determines what the system can deliver. Line size, choke setting, separator operating pressure, pump duty, compressor discharge pressure and export pipeline capacity are all hydraulic decisions, and each one propagates back through the system to the wellhead. This training covers the calculation methods behind those decisions and the physical behaviour that limits them, working from single-phase flow fundamentals through to multiphase flow in gathering networks and transient behaviour during upsets.
The treatment is quantitative but applied. Participants work with the Darcy-Weisbach equation and Moody friction factors, equivalent length and resistance coefficient methods for fittings, compressible flow equations used for gas lines including Weymouth and Panhandle correlations, choked flow criteria, and the standard multiphase flow correlations used in production system modelling. Pump system curves, NPSH margin, compressor operating maps, control valve sizing coefficients and choke performance are covered as the interface between hydraulics and equipment. The training closes with network-level analysis, transient hydraulics including surge and water hammer, and the velocity, erosion and vibration criteria that set practical limits on line sizing.
Hydraulic errors are expensive and durable. An undersized flowline permanently reduces field deliverability by imposing backpressure at the wellhead that no amount of downstream optimisation can remove. An oversized line increases capital cost, produces low velocities that allow water and solids to drop out, and can create slugging behaviour the facility was never designed to handle. Both errors survive for the life of the asset because the pipe has been laid.
Multiphase flow is where most upstream hydraulic difficulty concentrates. Oil, gas and water flowing together in a line do not behave as a homogeneous fluid. Flow regime changes with rate, pressure, inclination and fluid properties, liquid holdup varies with regime, and pressure drop can behave counter-intuitively as production rate falls. Terrain-induced slugging in undulating flowlines and severe slugging in risers can deliver liquid volumes far in excess of the average rate, causing separator carryover, compressor trips and facility upsets that appear to have no cause until the hydraulics are understood.
Transient hydraulics adds a further class of problem. Rapid valve closure produces pressure surges that can exceed design pressure. Pump trips generate low pressure waves and column separation. Start-up and shutdown sequences displace liquid inventory in ways steady-state calculations do not predict. These effects damage equipment and lift relief valves, and they are only avoidable if they are anticipated at design and understood in operations.
Finally, hydraulic criteria govern integrity. Erosional velocity limits under API RP 14E and its successors, minimum velocities for solids and liquid transport, flow-induced vibration thresholds and acoustic limits all define an operating window that is narrower than a simple capacity calculation suggests. Working inside that window requires the calculations covered in this training.
By the end of this training, participants will be able to:
- Apply fluid property relationships for oil, gas and water to hydraulic calculations at process conditions
- Calculate single-phase liquid pressure drop using the Darcy-Weisbach equation, friction factor correlations and fitting resistance methods
- Compute compressible gas flow and pressure drop in pipelines using the appropriate flow equations and identify choked flow conditions
- Identify multiphase flow regimes, estimate liquid holdup and evaluate multiphase pressure drop in flowlines and risers
- Construct system curves and determine pump and compressor operating points, including NPSH margin and surge limits
- Size control valves, chokes and restriction orifices for defined process duties
- Build a pressure traverse across a production network from wellhead to export and identify hydraulic bottlenecks
- Evaluate transient events including surge, water hammer, slug arrival and pump trip, and specify appropriate mitigation
- Apply erosional velocity, minimum velocity and vibration criteria to line sizing and operating limit decisions
The training combines derivation of the governing relationships with sustained numerical work, so that participants leave able to perform the calculations rather than only describe them. Each method is introduced with its assumptions and validity limits, applied to worked examples using representative oil and gas fluid properties and geometries, and then tested against field data showing where simple methods succeed and where they fail. Multiphase flow behaviour is presented through flow regime maps, holdup data and field cases of slugging and carryover. The training progresses from individual components to full network analysis, and participants are encouraged to bring line sizing or pressure drop problems from their own assets for group work.
Organisations sending participants to this training will:
- Improve the technical quality of in-house line sizing, hydraulic checks and debottlenecking studies
- Reduce production loss caused by hydraulic bottlenecks that were not identified during design or modification
- Strengthen review of contractor hydraulic deliverables, flow assurance reports and simulation results
- Reduce equipment damage and relief events caused by unanticipated surge, slugging and transient conditions
- Improve facility operating decisions by giving operations staff a quantitative understanding of pressure behaviour across the system
- Support better capital decisions on line sizing, pump and compressor selection and export system capacity
Participants will:
- Perform hydraulic calculations for liquid, gas and multiphase systems with confidence in the assumptions used
- Explain why pressure behaves as it does at any point in a production system
- Recognise slugging, carryover, cavitation, surge and erosion problems from their hydraulic signature
- Size lines, valves, chokes and orifices against correct velocity and pressure criteria
- Interpret and challenge hydraulic simulation results rather than accepting them without scrutiny
- Build quantitative capability that supports movement into facilities engineering, flow assurance or process design roles
- Facilities, process and production engineers
- Pipeline, flow assurance and subsea engineers
- Petroleum and reservoir engineers working on production system performance
- Project and design engineers responsible for piping and equipment sizing
- Operations engineers and supervisors managing facility capacity and constraints
- Mechanical and rotating equipment engineers dealing with pump and compressor systems
- Graduate engineers entering facilities, pipeline or production engineering roles
Module 1 - Fluid Properties and Flow Fundamentals
- Density, viscosity, compressibility and surface tension of produced fluids
- Black oil property correlations: solution gas-oil ratio, formation volume factor, bubble point
- Gas properties: compressibility factor, specific gravity, real gas behaviour
- Water properties, salinity effects and gas solubility
- Conservation of mass, momentum and energy in pipe flow
- Reynolds number, laminar and turbulent flow, velocity profiles
- Pipe roughness, relative roughness and its effect on friction
Module 2 - Single-Phase Liquid Hydraulics
- Darcy-Weisbach equation and friction factor determination
- Moody diagram, Colebrook-White and explicit friction factor correlations
- Pressure drop components: friction, elevation and acceleration
- Fittings and valves: equivalent length and resistance coefficient methods
- Non-Newtonian and viscous crude flow considerations
- Line sizing for liquid service and economic velocity
- Worked pressure drop calculations for oil and water lines
Module 3 - Compressible Gas Flow
- Compressible flow fundamentals and the isothermal flow equation
- Pipeline flow equations: Weymouth, Panhandle A and B, AGA
- Selection of the appropriate equation by pipe size and Reynolds number
- Efficiency factors and their practical application
- Sonic and choked flow: critical pressure ratio and its consequences
- Gas line sizing, velocity limits and noise considerations
- Pressure drop in gas gathering systems and export lines
Module 4 - Multiphase Flow Behaviour
- Superficial velocities, holdup, slip and no-slip conditions
- Flow regimes in horizontal, inclined and vertical pipe
- Flow regime maps and regime transition prediction
- Multiphase pressure drop correlations and mechanistic models
- Liquid holdup prediction and its effect on inventory and pressure drop
- Terrain-induced slugging in undulating flowlines
- Severe slugging in risers and its mitigation
- Slug catcher sizing concepts and slug handling in facilities
- Effect of declining rates on flow regime and pressure drop in ageing fields
Module 5 - Wellbore and Vertical Lift Hydraulics
- Pressure traverse in vertical and deviated wellbores
- Vertical lift performance curves and their construction
- Gradient curves and their interpretation
- Effect of water cut, gas-oil ratio and tubing size on lift performance
- Nodal analysis and the well operating point
- Gas lift injection hydraulics and injection point determination
- Liquid loading in gas wells and critical unloading velocity
Module 6 - Pump Hydraulics
- Pump head, capacity, efficiency and power relationships
- Pump performance curves and affinity laws
- System curve construction and duty point determination
- Effect of throttling, speed variation and impeller trimming
- Net positive suction head available and required
- Cavitation mechanisms, damage and prevention
- Series and parallel pump operation
- Minimum flow, recirculation and pump protection requirements
- Positive displacement pump hydraulics and pulsation
Module 7 - Compressor and Gas System Hydraulics
- Compression ratio, stage selection and discharge temperature calculation
- Centrifugal compressor performance maps and head-flow relationships
- Surge and stonewall limits and anti-surge recycle requirements
- Reciprocating compressor capacity control and pulsation effects
- Suction and discharge system pressure drop and its effect on compressor duty
- Interstage cooling, scrubbing and liquid carryover risk
- Fuel gas and gas lift system distribution hydraulics
Module 8 - Control Valves, Chokes and Restrictions
- Control valve sizing: flow coefficient, pressure recovery and valve characteristic
- Valve authority and controllability in a system
- Cavitation and flashing in control valves and their prevention
- Noise generation, prediction and mitigation
- Wellhead choke performance: critical and subcritical flow
- Multiphase choke correlations
- Restriction orifices and flow limiting devices
- Selection of trim, materials and anti-cavitation designs for severe service
Module 9 - Network Hydraulics and System Analysis
- Building a pressure traverse from reservoir to export point
- Gathering network configuration and its hydraulic consequences
- Backpressure propagation and its effect on well deliverability
- Identifying the controlling hydraulic bottleneck in a production system
- Sensitivity analysis on line size, separator pressure and export pressure
- Debottlenecking options: looping, boosting, pressure reduction, line replacement
- Effect of production profile change on network hydraulics over field life
Module 10 - Transient Hydraulics and Operating Limits
- Sources of hydraulic transients: valve closure, pump trip, compressor trip, start-up
- Water hammer theory, wave speed and surge pressure estimation
- Column separation and cavitation during transients
- Surge protection: relief, accumulators, slow closing valves, control philosophy
- Liquid inventory displacement during rate changes and shutdown
- Erosional velocity criteria and the basis of API RP 14E
- Minimum velocity criteria for solids and liquid transport
- Flow-induced vibration, acoustic-induced vibration and screening methods
- Setting practical operating envelopes from hydraulic limits
Upon successful completion of this training course, delegates will be awarded an official Certificate of Completion issued by the Petroleum Engineers Association (PEA), an ISO 9001:2015 certified training organization. The certificate carries 10 Credits and formally records the total learning hours completed.
Each certificate is signed by the Course Facilitator and the CEO of the Petroleum Engineers Association, and serves as verifiable proof of professional training that delegates can present to employers and professional bodies worldwide.
This course is led by a hydraulics and fluid flow specialist with more than 20 years in the oil and gas industry, built on calculating pressure drop, sizing lines and predicting how fluids behave across a production system.
He currently holds process engineering leadership responsibility with a major operator managing production networks, covering multiphase flow behaviour, pump and compressor hydraulics and network pressure traverse — the disciplines that determine how fluids move safely and efficiently through a facility. Earlier in his career he served as a process engineer on major facility developments, leading line sizing and control valve sizing work across a wide range of single-phase and multiphase flow applications. Across two decades he has applied fluid flow principles to design and troubleshoot production networks handling both liquids and gases.
That operating background shapes how he teaches. Delegates learn not only how fluid flow calculations are performed on paper, but how they play out in real production systems — where single-phase and multiphase flow assumptions break down, why pump and compressor hydraulics get miscalculated, what drives control valve sizing decisions, how transient effects and erosion criteria affect line sizing, and how facilities engineers apply pressure traverse calculations across a full production network. Every module is anchored in real hydraulics data, sizing decisions and lessons from operating production systems.
His subject coverage spans the full hydraulics chain: single-phase liquid and gas flow, multiphase flow behaviour, pump and compressor hydraulics, control valve sizing, network pressure traverse, transient effects and the velocity and erosion criteria that govern line sizing.
He has delivered fluid flow and hydraulics training for many years across the Middle East, North Africa and Southeast Asia, working with mixed groups of facilities engineers, process engineers and technical staff at every level of experience. He is an active contributor to industry forums on hydraulics and fluid flow engineering.
His approach is practical, discussion-led and grounded in real hydraulics experience — not the textbook.
Frequently Asked Questions
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