Practical Distillation Technology

Topic Process Operations

CPD Hours 23.25


A related course is available online >>

"Henry was excellent and used case-based learning effectively to demonstrate fundamental principles. The content was extremely informative and well presented."

Recognised expert Henry Kister presents this comprehensive course on distillation technology, with particular emphasis on the problems that can occur and how to solve them. He will discuss numerous operating experiences throughout the course to illustrate the key principles and to distinguish good from bad practices.

The course will help you to develop a working knowledge of key techniques that can promote trouble-free operation and reduce distillation cost.

Every delegate will receive a copy of Henry Kister's Distillation Operation and Distillation Troubleshooting text books, together with extensive course materials, providing invaluable reference sources after the course.

Learning outcomes

By the end of the course, you will understand:

  • how to troubleshoot a distillation column and determine what may cause poor performance
  • how to evaluate existing column performance and develop new designs
  • how to avoid common causes of capacity bottlenecks, tray damage, downcomer sealing problems, packed tower distributor malfunctions and many other operating difficulties
  • how to de-bottleneck a column to improve capacity and/or separation
  • how to control and operate a distillation column
  • how to validate your tower simulation.

Who will benefit

Engineering and supervisory personnel who are involved in:

  • operating
  • troubleshooting
  • de-bottlenecking
  • designing
  • starting up distillation processes.

Course outline

NB: Programme is provisional and may be subject to change.

Avoiding fractionation pitfalls

Vapour-liquid equilibrium (VLE): key concepts and simulation traps. Should we believe the simulation? Issues with close-boilers and non-idealities: why some heavy components go up while the simulation thinks they go down. VLE data: to trust or not to trust? Are distillation trays ideal stages? Reflux-stages relationship. Multi-component distillation: composition profiles, side-draws, accumulation, and cycling problems. What you need to watch out for.

Troubleshooting distillation simulations

Does your simulation reflect the real world? How poor simulation leads to incorrect problem diagnosis. What validation checks are needed? How far should we go? Sensitivity analysis and graphics for simulation troubleshooting: useful hints.

Tray hydraulics and limits

Visualisation of vapour-liquid dispersions on trays, flooding, entrainment, weeping, dumping. Flood mechanisms: jet (entrainment), system limit, downcomer backup, downcomer choke. Which one limits your tower capacity? Common tray types: sieve, moving valve, fixed valve, sheds: pros and cons. Which works well in fouling applications? Small holes, valves: benefits and traps. Flood: what causes it, what affects it, and how to predict it. Are the predictions reliable? Tray efficiency: are simulation predictions reliable? Can it be enhanced by tray modification?

Troubleshooting tray towers

Flooding and foaming symptoms: high dPs, reduced bottoms, others. Which can be trusted? Liquid and vapour sensitivity and other field tests: identifying the correct flood mechanism and ruling out incorrect theories. Gamma scans: application for diagnosing flood, missing and damaged trays, foaming, and downcomer flooding. How to combine gamma scans with process checks to get the most out of the scans. Do gamma scans ever lie?

Troubleshooting packed towers

Rules of thumb for flood pressure drop and packing efficiency. Simulation hydraulic calculations: to trust or not to trust? Grid gamma scanning for detecting maldistribution, damage, distributor malfunction. Distributor overflow: death for packed beds, how to diagnose and avoid. Some do’s and don’ts for distributors. Can poor distributor feeding bottleneck towers? Circumferential surface temperature surveys: how to conduct and the hidden secrets they reveal. Neutron backscatter and CAT scans: when useful.


State-of-the-art trays and packings: strengths and weaknesses. Factors that favour trays and factors that favour packings. The pressure drop bonanza: why packings win in non-fouling vacuum services and in compressor suction. Pitfalls unique to structured packings: high pressure application, oxidation, shutdown fires. High-capacity trays (eg Superfrac, VG Plus, MD): principles, tricks, and traps. Do they really give 30% more capacity than conventionals?

Distillation control

Assembling control loops into an overall scheme: what works, which is better, what causes instability, and what impairs efficiency. The three most common causes of control assembly failure: no material balance control, fighting between temperature controllers, and level control on a small stream. Tips for avoiding problems. Best temperature control location: is there a reliable method for finding it? How can a temperature controller be fooled? Reboiler, condenser, and pressure controls: which loops work and which misbehave. How dead pockets in vapour overhead lines interfere with controls. Understanding flooded condensers and hot vapour bypasses: why some work while others don’t. Control systems that did not work.

Avoiding tower malfunctions

The 10 most common causes of distillation malfunctions: what trouble should we look for and prevent? Points of transition (feeds, draws, tower base): why these are some of the worst tower bottlenecks: how diagnosed and remedied. High tower base levels: how they induce premature flood, tray/packing damage and column overfills, and how you can prevent. Instrument issues at the tower base: what to watch out for. Tray/packing damage: pressure surges due to water entering a tower full of hot oil or insoluble organics, other sources of tray damage and ways to avoid. Some commissioning and startup watchouts: pre-startup inspection, blinding and unblinding, reverse flow, steam-water operation, washing, rapid pressuring/depressuring. Chimney trays: do’s, don’ts and how they bottleneck towers. Liquid outlets: choking in sidedraw rundown lines and how it restricts tower capacity. Why must self-venting flow be assured in the presence of entrained vapour? Siphon formation. Kettle and once-through thermosiphon reboilers: how they bottleneck towers.

Case studies

These operating experiences will be scattered throughout to illustrate the key principles and to distinguish good from bad practices.

Previous delegates say

The best thing about the course, according to 2019 delegates:

  • Henry Kister's enthusiasm and engaging delivery 
  • the extensive number of operating examples provided from Henry Kister's real-world experience
  • the practical techniques provided for troubleshooting
  • the breath of information covered
  • the extensive course material and reference books provided.

"Henry was excellent. His enthusiasm and the course content were brilliant. What a pleasure!"
Emily Anderson, Seqens Custom Specialties, UK

"Henry was excellent and used case-based learning effectively to demonstrate fundamental principles. The content was extremely informative and well presented. Henry's tireless energy in presenting the core material, and his willingness to answer any questions on distillation no matter how complex made this course exceptional."
Simon Hayton, Worley, UK

"Henry is an excellent presenter, teacher, and speaker; a terrific course."
Benjamin Floan, Crown Iron Works, USA

"Wonderful. Top class teacher."
Laurent Ferrari, Total, Belgium


IChemE requires that its trainers and training venues follow all local government guidelines with regard to COVID-19 on its training courses. All delegates will also be required to adhere to the guidelines and further communication on this matter will be issued to attendees closer to the course.

Whilst our usual cancellation terms and conditions apply, delegates can transfer to a later face-to-face course date or a related online course at any stage, without incurring a cancellation fee.

In the event of IChemE being unable to deliver the training course as planned, a full refund will be provided.


Discounts are available to companies booking more than one place:

  • 2 places — 5% discount
  • 3 places — 10% discount
  • 4 or more places — 15% discount.

Bookings must be made at the same time to receive the discount.

In-company training

This course is also available as an in-company course where content can be customised to meet your organisation's specific needs and delivered on a date/location that suits your requirements. Contact us for more information.

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