Monday, February 25, 2008

Béla Lipták has presented 7 Part Series on Distillation Control and Optimization in brief. Who is Béla Lipták ? Click to see who is Béla Lipták.
- editor of the Instrument Engineer’s Handbook
- former chief instrument engineer at C&R (later John Brown)
- recipient of ISA’s Life Achievement Award (2005)
- member of the CONTROL Process Automation Hall of Fame (2001).
His 7 series on Distillation Control and Optimization includes
If you are operating or designing control system for a distillation, you should take this opportunity for quick view of these series.
Related Topic
- Distillation Pilot Plant Design, Operating Parameters and Scale-up Considerations
- Operation and Control of Azeotropic Distillation Column Sequences
- OGT - Others FREE articles related to Amine & CO2...
- Optimized Gas Treating, Inc. (OGT) - Experts in CO2-Amine
- KG-TOWER® - FREE Column hydraulic rating software from Koch-Glitsh...
Labels: Distillation
Tuesday, December 4, 2007
Designing a distillation column with high liquid loading at high pressure system generally will encounter challenges due to
- High Liquid flowrate
- Low density difference
- Low Surface tension
- Low Separation efficiency
Downcomer design will be critical in High pressure - high liquid loading system. SULZER has presented special design considerations for above mentioned system in the AICHE annual meeting.
Except for a few odd services, high liquid rate applications are typically the domain of either trays or random packings. Aside from the distributors, random packing designs are rather straightforward with the designer choosing the proper size to accommodate the fluid flow rates and achieve the desired efficiency. Trays, on the other hand, have a large variety of adjustable parameters and can be especially complex, especially when designed for high liquid rate applications...
If you designing or operating a high pressure high liquid loading system, this paper may provides you some ideas.
Related Topic
- HOMEBREW
- Jaeger Inc., many of us may already aware of this packing & column internal manufacturer
- Distillation Pilot Plant Design, Operating Parameters and Scale-up Considerations
- TAC - High Temperature Simulated Distillation (HTSD) and Petroleum Characterization...
- Operation and Control of Azeotropic Distillation Column Sequences
Labels: Column, Distillation
Wednesday, September 12, 2007

Labels: Distillation
Thursday, June 7, 2007

Jaedger Inc., many of us may already aware of this packing & column internal manufacturer, particularly it's innovative product, Jaeger Tri-Packs®. Besides, Jaeger also manufacture others packing such as Jaeger Metal Max-Pak, Raschig Super-Ring® , Jaeger Low Profile Rings, etc...
Jaeger offered some white papers for public information...
Gas Scrubbing
Stream Stripping
Air Stripping
Problems with Fouling
JP-7 Chelating Agents
Handling/Installation/Operation Instruction
Nevertheless, some of Jaeger's webpage are still under-devlopment...
Come on...let see what jaeger offered....
Continue receive FREE stuff & Update.......Subscribe by Email
Labels: Column, Design, Distillation, Fractionation, Packed Column, Packing, Scrubber
Wednesday, June 6, 2007

This articles was written by T. Daniel Koshy and Frank Rukovena, formerly from Norton Chemical, submitted to CheResources website.
Labels: Column, Design, Distillation, Education, Packed Column, Packing, Pilot Plant
Monday, June 4, 2007

Through some of the visitor, i found this site...This site have some interesting articles particular for Refinery engineer...
Triton Analytics Coporation (TAC) was founded in 1991 by Dan C. Villalanti, Ph.D. to serve the growing needs of the petroleum industry. TAC now services over 150 oil, gas and petroleum companies worldwide seeking high precision, reliable analytical results. Since the inception of the company, TAC has set industry standards for gas analysis, exact structure determination of hydrocarbons (NOISE), and High Temperature Simulated Distillation (HTSD). Sample matrices include crudes and feedstocks, distillates, motor oils and heavy residuals up to vacuum tower bottoms. Since that time, TAC capabilities have continued to expand to also include titrimetry with the highest precision available, detailed hydrocarbon analysis (DHA), and Vapor Pressure determination of petroleum mixtures.
FREE articles available in this site....FREE download
HTSD
Yield Correlations between Crude Assay Distillation and High Temperature Simulated Distillation (HTSD)
Refinery Analytical techniques optimize unit performance
Feed Characterization and Deepcut Vacuum Columns: Simulation and Design
NOISE frequently asked questions brochure
Glossary of NOISE terms used in reports
NOISE flyer
Brief technical description of NOISE
Continue receive FREE stuff & Update.......Subscribe by Email
Any comments / advices ?..........Drop it in comment field (below) or sent a private email to me...
Labels: Chromatography, Column, Design, Distillation, Fractionation, Process simulation
Wednesday, May 30, 2007
This document bring us something relates to
Operation and Control of Azeotropic Distillation Column Sequences
A doctoral thesis from the Automatic Control Laboratory (IfA), Swiss Federal Institute of Technology (ETH) Z¨urich.
Jan Ulrich
Labels: Air Pollution Control, Column, Distillation, Operation
Saturday, May 26, 2007

By the way, if you know some good site related to Chemical & Process Engineering, (as you know, i am focusing on distillation recently) do recommend to me...i will crawl the website thoroughly...and let inform our lovely Chemical & Process Engineers...
- ProMax from BR&E - Renowed Process Simulator in Gas Treating Industry
- Optimized Gas Treating, Inc. (OGT) - Experts in CO2-Amine
- Air Pollution Control & Tail Gas Treatment
Labels: Absorption, Air Pollution Control, Amine, Column, Design, Distillation, Global warming, Modelling, Packed Column, Packing, Process simulation, Tail Gas Treatment, Technology, Tower internals
Friday, May 25, 2007

Above efforts will reduce CO2 release into atmosphere. However, recycling CO2 will increase quantity of CO2 in oil and result serious corrosion problem. Hence it needs to be removed from the flashed gas (from unstabilised oil). CO2 removal technology using amine absorption has been used for many years. Recently i found a website (OGT) where the founders, Ralph Weiland and Jack Dingman are those experts in this technology.
Optimized Gas Treating, Inc. (OGT) was established in 1992 by Ralph Weiland and Jack Dingman for the single purpose of providing a commercial version of a Windows-based software package for simulating acid gas removal with aqueous alkanolamines that uses a fundamental mass and heat transfer rate approach to column modeling. ProTreat™ is the culmination of more than 30 years of research in gas treating supported by government and industry in both academic and commercial environments. ProTreat is our sole product. Consequently, it receives our undivided attention in maintaining and enhancing its capabilities so that it remains the premier software package for gas treating with amines. OGT’s principals are recognized world experts in most aspects of gas treating — they offer a total of nearly 60 years of relevant experience.
Some FREE articles offered by OGT :
Labels: Absorption, Amine, Column, Distillation, Equilibrium, Extraction, Global warming, Modelling, Packed Column, Packing, Process simulation, Software, Technology, Tower internals
Tuesday, May 22, 2007

GTC is a proprietary licensed technology to processing industries from naphtha processing to terephthalic acid purification. Success built around production of chemicals and the refining of petroleum worldwide. Notion applied to production of dimethyl terephthalate (DMT), aromatics recovery, replacing LLE with ED, technologies for paraxylene production and fuel gas desulphurization.
GTC offers some FREE articles for download...
Labels: Column, Debottlenecking, Desulphurization, Distillation, Extraction, Technology
Saturday, May 19, 2007

KG-TOWER® has ability to import loading data from simulation output files of Aspen Technology's and SimSci-Esscor's software. Utility required for PRO/II Simulation Software...
Labels: Column, Design, Distillation, Fractionation, Hydraulic, Packed Column, Tower internals
Friday, May 18, 2007

Technical Bulletins (Amistco)
WebWorm
Labels: Column, Design, Distillation, Mist Eliminator, Packed Column, Packing, Separation, Souders-Brown, Tower internals
Thursday, May 17, 2007

WebWorm
Labels: Column, Design, Distillation, Mist Eliminator, Packed Column, Packing, Separation, Souders-Brown, Tower internals
Wednesday, May 16, 2007

I have introduced a very good site for making liquor...Home Distillation of Alcohol. Today another excellence site for home distillation...
This site provides information on the history of making liquor, step-by-step, the best part is application of process engineering knowledge...
All information has been compiled into Microsoft Word® (doc) and Adobe® Portable Data Format (PDF) for those who would prefer to browse through this guide off line...
Resources
Pot Stills
Reflux Stills
Distillation Purity
Boiler Selection
Top End Considerations
and Techniques
Internal Reflux Condenser
Internal Reflux Cooling
Internal Reflux Condenser Core
Internal Reflux Condenser Jacket
Internal Reflux Column
Valved Reflux Still-head
Valved Reflux Column
Attaching the Column and Boiler
Column Packing
Heating
Cooling
Still Operation
Tuning
Final Words
Appendix 1 - Construction Costs
Appendix 2 - Resources
WebWorm
Labels: Alcohol, Column, Distillation
Tuesday, May 15, 2007

Koch-Otto York® Separations Technology), a business group of Koch-Glitsch, LP, provides mist elimination equipment for gas-liquid separation, liquid-liquid separation, as well as vapor flow conditioning devices, for a broad base of industries including chlor-alkali, gas transmission, indoor air quality, petrochemical, power generation, pulp & paper, refining, and sulfuric acid.
FREE articles relates to Mist Eliminator
Demystifying the Selection of Mist Eliminators
Chem. Eng. Nov-Dec 1993, Overview of Mist Eliminator Engineering, Selection, and Sizing
Mist eliminators for sulphuric acid plant duty
British Sulphur 1982 - Overview of Mist Eliminators for Sulphuric Acid Plants
Laser-based Instrument Measures Mist Elminator Carryover
Brochure...
DEMISTER® Mist Eliminator Installation Manual
GOODLOE® Tower Packing
Following articles are available from KGLP site upon request...
Performance of Commercial Chevron Mist Eliminators
Accurate Evaluation of Chevron Mist Eliminators
Lubrication Oil Reservoir Mist Elimination
New methods for fighting sulfuric acid mist emissions
A New Concept “Plant in a Pipe” SX Design (Liquid-liquid extraction)
Metals Solvent Extraction Plants (Liquid-liquid extraction)
Labels: Coalescer, Column, Distillation, Fractionation, Mist Eliminator, Packed Column, Packing, Tower internals
Monday, May 14, 2007

MONTZ is a distillation column and internal manufacturer (under Neuman group). The speciaties about MONTZ are :
- MONTZ packing
- DIVING WALL COLUMN
- Liquid Distributor
- Column Internals
- Reflux splitter
- Mass Transfer tray
- Falling film evaporator
Column layout...
Interesting FREE articles from MONTZ :
- "Performance characteristics of a new high capacity structured packing"
Z. Olujic, A.F. Seibert, B. Kaibel, H. Jansen, T. Rietfort, E. Zich, Chem. Eng. and Proc. 42 (2003), 55-60
- "Distillation column internals - Configurations for process intensification"
Z. Olujic, B. Kaibel, H. Jansen, T. Rietfort, E. Zich, G. Frey, Chem. Biochem. Eng. 17 (2003), 301-309
- "Influence of corrugation geometry on the performance of structured packings"
Z. Olujic, A.F. Seibert, J.R. Fair, Chem. Eng. and Proc. 40 (2000), 335-342
Labels: Column, Distillation, Fractionation, Hydraulic, Packed Column, Packing, Tower internals
Sunday, May 13, 2007

Fractionation Research, Inc. (FRI)
is an organization that researches the mass transfer and hydraulics of distillation or fractionation.Researched devices include sieve trays, valve trays, random packings and structured packings, dualflow trays, bubble cap trays, baffle trays and proprietary devices
FRI is a nonprofit but member supported corporation to provide information to its members enabling them to become more efficient in the design and operation of distillation columns. FRI also act as independent testing facility, provides unbiased technical performance data on mass transfer devices to the industry.
All articles are available to its MEMBERS only...

Labels: Column, Design, Distillation, Fractionation, Hydraulic, Packed Column, Tower internals
Friday, May 11, 2007

A Treatise of the Choicest Spagyrical Preparations Performed by Way o£ Distillation, Being Partly Taken Out of the Most Select Chemical Authors of the Diverse I,anguages and Partly Out of the Author's Manual Experience together with, The Description of the Chiefest Furnaces and Vessels Used by Ancient and Modern Chemists also A Discourse on Diverse Spagyrical Experiments and Curiosities, and of the Anatomy of Gold and Silver, with The Chiefest Preparations and Curiosities Thereof, and Virtues of Them All. All Which Are Contained In Six Books Composed By John French, Dr. of PhysickLondon. Printed by Richard Cotes and are to sold by Thomas Williams at the Bible in Little-Britain without Aldersgate, 1651.
The Art of Distillation from UNIVERSITY OF PENNSYLVANIA LIBRARY
Labels: Distillation, History
Wednesday, May 9, 2007

CONTINUE...
FREE BROCHURES
High Performance and Conventional Trays
SUPERFRAC® High Performance Trays
ULTRA-FRAC® High Performance Trays
TRITON® High Capacity Fractionation Trays
PROVALVE® Valve Trays
FLEXITRAY® Conventional Valve Trays
Tray Technologies
OMNI-FIT® Technology
SPEED-WAY® Manways
SATURN® Technology
Structured Packing
Packing and Internals for Severe Services
Random Packing
Plastic Random Packing
Metal Random Packing
FLEXIMAX® Random Packing
Packed Tower Internals
Metal Packed Tower Internals
Tower Internals Hardware and Services
1. Q: How do you calculate tray capacity? 2. Q: What about flexibility?
3. Q: How do you cost trays?
4. Q: How many flow paths should be specified?
5. Q: How do you calculate diameter?
6. Q: What if existing columns are too small for new operating conditions?
7. Q: Are there considerations of distribution independent of trays?
8. Q: Does top tray feed demand special care?
9. Q: Will all liquid feed streams contain vapor?
10. Q: How do you orient seal pans and nozzles?
11. Q: Are there special considerations for the bottom tray?
12. Q: Should I use reboiler baffles?
13. Q: Are sumps always needed?
14. Q: Should chimney trays be used?
15. Q: What accommodations must be made for flow path changes?
16. Q: Do crude towers require special treatment?
17. Q: Is special attention needed during start-up?
Other Questions
1. Q: What is flooding?
2. Q: What causes flooding?
3. Q: What is jet flood?
4. Q: What causes downcomer flooding?
5. Q: Why does Koch-Glitsch recommend a maximum percent of flood of 80%?
6. Q: Why are so many downcomer sizes used?
7. Q: What is the purpose of recessed inlet sumps under the downcomer?
8. Q: What is the purpose of anti-jump baffles?
9. Q: Why do some tray manufacturers not use downcomer baffles?
10. Q: What is the difference between splash baffles and downcomer anti- jump baffles?
11. Q: When are picket fence weirs used?
12. Q: When are notched weirs useful?
13. Q: What about inlet weirs?
14. Q: When is tray leakage detrimental to the operation of the tray?
15. Q: What is the meaning of unit reference?
16. Q: How is unit reference used?
17. Q: Some manufacturers use 14 and 16 gauge units on alternating rows. Why does Koch-Glitsch use 16 and 12 gauge units, since this is more expensive ?
18. Q: What determines the flexibility of a tray?
19. Q: Which Koch-Glitsch tray has the greatest flexibility?
20. Q: Which has the highest capacity, a valve or sieve tray?
21. Q: If a sieve and valve tray have the same capacity, why are sieve trays not better?
22. Q: Why or when should a bubble cap tray be used?
23. Q: What size bubble cap should be used?
24. Q: What about a tea-cup cap?
25. Q: What about the Koch-Glitsch V-O tray?
26. Q: Why does Koch-Glitsch specify rectangular or square stacks on chimney trays?
27. Q: Why does Koch-Glitsch insist on draw sumps instead of permitting the draw nozzle to be flush with the chimney tray floor?
28. Q: Will liquid flow down the risers of chimney trays in the event of upset conditions?
29. Q: What vapor feed entry is recommended for atmospheric and vacuum crude towers and FCC fractionators?
30. Q: What about mist eliminators?
31. Q: Should mist eliminators have top holddown grids?
32. Q: What is tray efficiency?
33. Q: Under what circumstances are packings chosen over trays?
34. Q: How do Koch-Glitsch packed column design procedures differ from those 01 other manufacturers?
35. Q: What is KGA ?
36. Q: What is the maximum allowable bed depth for a single metal packed bed?
37. Q: What is the maximum allowable bed depth for a single plastic packed bed?
38. Q: Can grid-style support plates be used with plastic packings?
39. Q: Why are tangential entrances recommended for certain tower feeds?
40. Q: How is a flashing feed distributor different?
41. Q: Are packed tower internals less expensive than trays?
42. Q: What is the difference between bed limiters and bed hold-downs?
43. Q: Why don't other manufacturers recommend the use of bed limiters and bed hold-downs?
44. Q: What is the best liquid distributor for a packed tower?
Labels: Column, Distillation, Fractionation, Mist Eliminator, Packed Column, Packing, Tower internals
Monday, May 7, 2007

Products including
FREE ARTICLES
Labels: Column, Distillation, Fractionation, Mist Eliminator, Packed Column, Packing, Tower internals