Gas Dehydration and Sweetening (Glycol, Mol Sieve, Amine)
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Gas Dehydration and Sweetening (Glycol, Mol Sieve, Amine) - SF-GDS-PEA27
| Code | Date | Time | Duration | Location | Currency | Early Bird Fee Per Person |
|---|---|---|---|---|---|---|
| SF-GDS-PEA27 | 14 - 18 Jun 2027 | 10 AM CST | 5 Days - 4 Hours / Day |
Online |
USD |
4000 |
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Gas Dehydration and Sweetening (Glycol, Mol Sieve, Amine)
This training covers gas dehydration and sweetening in technical depth. It works through glycol absorption and regeneration, molecular sieve adsorption cycles, and amine acid gas removal, covering process chemistry, unit configuration, equipment sizing, solvent management and operating limits. Systematic troubleshooting of off-specification gas, solvent loss, foaming, corrosion and fouling is covered throughout.
Description
Gas leaving a production separator is saturated with water and, in many fields, contains hydrogen sulphide and carbon dioxide. Neither condition is acceptable downstream. Water forms hydrates, causes corrosion in the presence of acid gas, and condenses in pipelines. Hydrogen sulphide is toxic and corrosive and is limited to a few parts per million in sales gas. Carbon dioxide reduces heating value, causes corrosion when wet, and freezes in cryogenic plants. Dehydration and sweetening are the units that resolve these problems, and both are chemically driven processes that behave badly when operated outside their design envelope.
The training covers the three principal technologies in full. Glycol dehydration is developed from water content prediction and dew point depression requirements through contactor design, circulation rate calculation, regeneration temperature limits, stripping gas and enhanced regeneration methods. Molecular sieve adsorption is covered for the deep dehydration duties that glycol cannot meet, including bed sizing, cycle design, regeneration heating and cooling, and bed life management. Amine sweetening is developed through solvent chemistry and selectivity, covering primary, secondary, tertiary and hindered amines and formulated solvents, with contactor and regenerator design, circulation and reboiler duty calculation, and acid gas handling. Operating problems across all three units are addressed systematically, since dehydration and sweetening units account for a disproportionate share of gas plant reliability loss.
Water dew point is the specification that keeps a gas pipeline operable. Free water in a pipeline carrying carbon dioxide or hydrogen sulphide creates an aggressive corrosion environment that consumes wall thickness quickly, and at the pressures and temperatures common in gas transmission it forms hydrates that block lines and damage equipment. Dehydration to specification is therefore not a quality nicety but a condition for continued operation of the transport system.
Glycol dehydration handles most upstream duty, but it has a hard limit. Dew point depression achievable with triethylene glycol is constrained by the lean glycol concentration, which is constrained by the reboiler temperature at which glycol begins to degrade thermally. Achieving concentrations beyond that requires stripping gas, azeotropic stripping or vacuum regeneration. When the duty requires water content in the low parts per million, as it does upstream of cryogenic recovery, adsorption on molecular sieve is the only practical route, and that brings a different set of engineering problems in cycle design, bed support, regeneration energy and adsorbent life.
Amine sweetening is chemically more complex and operationally less forgiving. Solvent selection is a trade-off between acid gas pickup, selectivity between hydrogen sulphide and carbon dioxide, regeneration energy, corrosivity and degradation resistance. The circulating solvent accumulates heat stable salts, degradation products and particulates that drive foaming, fouling and corrosion. Most amine unit problems, including the majority of off-specification events, originate in solvent condition rather than in equipment design.
Both units also sit at the boundary of process safety. Amine regenerator overhead systems carry concentrated hydrogen sulphide. Acid gas disposal requires either sulphur recovery, incineration or reinjection, each with its own hazards. Glycol regenerator still columns vent hydrocarbon and benzene, toluene, ethylbenzene and xylene compounds with emissions and exposure consequences. Competent operation requires understanding these exposures alongside the process chemistry.
By the end of this training, participants will be able to:
- Determine water content of natural gas at process conditions and calculate the dew point depression required to meet specification
- Design a glycol dehydration unit including contactor sizing, circulation rate, stage requirement and regeneration conditions
- Evaluate enhanced regeneration methods and select the appropriate technique for a required lean glycol concentration
- Design molecular sieve dehydration including bed sizing, cycle time, regeneration heating and cooling requirements
- Explain amine chemistry and select an appropriate solvent for a defined acid gas removal and selectivity requirement
- Size amine contactors and regenerators and calculate circulation rate, acid gas loading and reboiler duty
- Manage solvent condition including heat stable salts, degradation products, filtration and reclaiming
- Diagnose off-specification gas, solvent loss, foaming, fouling and corrosion problems in treating units
- Assess acid gas disposal options including sulphur recovery, incineration and acid gas reinjection
The training addresses each technology as a complete unit, developing the underlying chemistry and equilibrium behaviour before moving to design calculation and then to operating practice. Water content charts, dew point depression calculations, glycol circulation rate determination, adsorption bed sizing, amine loading and reboiler duty calculations are worked through numerically using representative gas compositions. Units are presented with process flow diagrams, equipment drawings and operating data from installed plants. The troubleshooting content is built on documented failures in glycol, molecular sieve and amine service, and participants are encouraged to bring treating unit problems from their own plants for group analysis.
Organisations sending participants to this training will:
- Improve sales gas specification compliance and reduce off-specification events and associated deferment
- Reduce solvent and glycol losses and the operating cost associated with them
- Extend molecular sieve and amine solvent life through better operating and management practice
- Reduce corrosion and fouling damage in treating units and their associated equipment
- Improve the technical quality of treating unit design review, vendor evaluation and modification assessment
- Strengthen process safety management around acid gas handling and hydrogen sulphide exposure
Participants will:
- Design and check dehydration and sweetening units against defined process specifications
- Understand why a treating unit is failing to meet specification and what corrective action will work
- Manage solvent condition proactively rather than reacting to foaming and corrosion events
- Interpret laboratory solvent analysis and translate it into operating action
- Review vendor treating unit proposals critically against process requirements
- Build specialist capability in units that are central to gas plant reliability
- Gas plant process and facilities engineers
- Operations engineers and supervisors responsible for treating units
- Production chemists and solvent management specialists
- Design engineers specifying dehydration and sweetening units
- Maintenance and integrity engineers supporting treating equipment
- Laboratory and technical support staff analysing solvent and product quality
- Process safety practitioners working on facilities handling acid gas
Module 1 - Gas Treating Requirements and Water Content
- Sales gas and plant feed specifications: water dew point, hydrogen sulphide, carbon dioxide, hydrocarbon dew point
- Water content of natural gas: charts, correlations and equations of state
- Effect of pressure, temperature, gas composition and salinity on water content
- Hydrate formation conditions and prediction
- Corrosion consequences of water in acid gas service
- Selection of treating technology against duty and specification
- Sequencing of dehydration and sweetening within a gas processing scheme
Module 2 - Glycol Dehydration: Process and Design
- Glycol types: monoethylene, diethylene, triethylene and tetraethylene glycol
- Absorption principle and equilibrium water content over glycol solutions
- Dew point depression as a function of lean glycol concentration and contact temperature
- Contactor design: trayed and packed columns, stage requirement, sizing
- Glycol circulation rate calculation and its optimisation
- Inlet scrubbing, gas cooling and feed conditioning
- Rich and lean glycol heat exchange
- Flash vessel operation and hydrocarbon removal
- Filtration: particulate and carbon filtration
- Complete unit configuration and control philosophy
Module 3 - Glycol Regeneration and Enhancement
- Reboiler operation, temperature limits and thermal degradation of glycol
- Still column design, reflux and overhead losses
- Achievable lean glycol concentration and its limits
- Stripping gas regeneration and stripping column design
- Azeotropic regeneration processes
- Vacuum regeneration
- Emissions from the still column: hydrocarbons, BTEX and their control
- Glycol losses: vaporisation, entrainment, mechanical, degradation
- Glycol analysis: concentration, pH, chlorides, iron, hydrocarbons, solids
- Glycol reclaiming and replacement decisions
Module 4 - Glycol Unit Operating Problems
- Off-specification dew point: systematic diagnosis
- Foaming in the contactor: causes and control
- High glycol losses and their identification
- Glycol degradation, acidity and corrosion
- Salt contamination and its consequences
- Fouling of exchangers, filters and the still column
- Reboiler fire tube failure and hot spots
- Contactor flooding and carryover
- Pump failures and circulation problems
- Cold weather and start-up problems
Module 5 - Molecular Sieve Dehydration
- Adsorption principles and adsorbent types: molecular sieve, silica gel, activated alumina
- Molecular sieve grades and selection
- Mass transfer zone, equilibrium capacity and useful capacity
- Bed sizing: diameter from velocity limits, length from capacity requirement
- Adsorption cycle design: two bed, three bed and multi-bed arrangements
- Cycle time selection and switching valve arrangements
- Regeneration: heating, cooling, gas source, temperature profile
- Regeneration gas heating and cooling equipment
- Bed support, hold-down, and flow distribution
- Water and hydrocarbon breakthrough detection
Module 6 - Molecular Sieve Operating Problems and Bed Life
- Adsorbent ageing, capacity decline and bed life prediction
- Liquid carryover damage to beds
- Coking, carbon deposition and hydrocarbon fouling
- Sulphur compound and amine carryover damage
- Bed pressure drop increase, dusting and attrition
- Switching valve leakage and its consequences
- Regeneration inadequacy: temperature, flow and time
- Bed changeout planning, loading practice and commissioning
- Monitoring programme for adsorption units
Module 7 - Amine Sweetening: Chemistry and Solvent Selection
- Acid gas removal requirements and specification drivers
- Amine classification: primary, secondary, tertiary and sterically hindered
- MEA, DEA, MDEA, DGA and formulated solvents
- Reaction chemistry with hydrogen sulphide and carbon dioxide
- Selectivity and its exploitation for hydrogen sulphide removal
- Acid gas loading limits and their basis
- Physical solvents and hybrid solvents
- Solvent selection against feed composition, specification and energy cost
- Alternative technologies: hot potassium carbonate, scavengers, membranes
Module 8 - Amine Unit Design and Operation
- Contactor design: trays, packing, stage requirement, sizing
- Circulation rate calculation from acid gas load and loading limits
- Rich amine flashing and hydrocarbon removal
- Lean and rich amine heat exchange
- Regenerator design, stripping steam and reflux
- Reboiler duty calculation and heat source selection
- Reboiler temperature limits and thermal degradation
- Acid gas overhead system and condensing
- Filtration: mechanical and activated carbon
- Unit control philosophy and specification control
Module 9 - Amine Solvent Management and Unit Problems
- Heat stable salt formation, measurement and effects
- Amine degradation products and their consequences
- Solvent analysis programme and interpretation
- Reclaiming: thermal, ion exchange, electrodialysis
- Foaming: causes, detection, antifoam use and its risks
- Corrosion mechanisms in amine service and their locations
- Erosion-corrosion at high velocity points
- Amine losses: vaporisation, entrainment, degradation, mechanical
- Off-specification treated gas: systematic diagnosis
- Contactor flooding, carryover and hydrocarbon contamination
Module 10 - Acid Gas Handling and Disposal
- Acid gas stream characteristics and handling hazards
- Sulphur recovery by the Claus process in outline
- Tail gas treating and sulphur recovery efficiency
- Acid gas incineration and emissions requirements
- Acid gas compression and reinjection
- Sulphur handling, storage and product quality
- Hydrogen sulphide safety: exposure limits, detection, personal protection, emergency response
- Emissions regulation and sulphur dioxide limits
- Selection between disposal routes on technical and economic grounds
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 gas treating specialist with more than 20 years in the oil and gas industry, built on removing water and acid gas to meet pipeline and plant specification.
He currently holds gas treating engineering leadership responsibility with a major operator managing gas processing facilities, covering glycol and molecular sieve dehydration, amine-based acid gas removal and unit design and sizing — the disciplines that keep treated gas within pipeline and plant specification. Earlier in his career he served as a process engineer on major gas treating plant developments, leading solvent selection and unit sizing work on some of the industry's most technically demanding gas treating trains. Across two decades he has diagnosed and resolved numerous off-specification treated gas problems across operating facilities.
That operating background shapes how he teaches. Delegates learn not only how gas dehydration and sweetening units are designed to work, but how they perform in practice — where water dew point control by glycol or molecular sieve actually falls short, why amine absorption systems underperform, what drives solvent selection and unit sizing decisions, how operating problems develop over time, and how engineering and operations teams diagnose off-specification treated gas together. Every module is anchored in real plant data, design decisions and lessons from operating gas treating facilities.
His subject coverage spans the full gas treating chain: water dew point control by glycol absorption and molecular sieve adsorption, acid gas removal by amine absorption, solvent selection, unit design and sizing, operating problems and the diagnosis of off-specification treated gas.
He has delivered gas dehydration and sweetening training for many years across the Middle East, North Africa and Southeast Asia, working with mixed groups of process engineers, gas treating specialists and technical management at every level of experience. He is an active contributor to industry forums on gas treating and processing.
His approach is practical, discussion-led and grounded in real gas treating plant experience — not the textbook.
Frequently Asked Questions
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