Showing posts with label Tower internals. Show all posts
Showing posts with label Tower internals. Show all posts

Monday, December 10, 2007

Minimum Four Factors For Selection of Head Type on a Vessel




There are many head types attached to a vessel, column or drum such as hemispherical, semi-hemispherical, elliptical, flanged, etc. All these have been used in many application and however the selection of the head type is normally not documented in any process nor mechanical document and drawings. The question of application of head type has been raised many time by young engineers and the answer has been repeated many times. There is some incentive behind to list out some common reasons in application of head type.

There are few factors affecting the selection of head type :
  • Allowable stress & Material used
  • Access internals
  • Constructibility / fabrication limitation
  • Cost Saving
Allowable Stress & Material used
From stress and material saving perspective, for a vessel exposing to very high pressure hemispherical head is having highest allowable stress and minimum material. This will be followed by elliptical head and last flanged head (least allowable stress). Generally an elliptical head is in used.

Access Internals
In large vessel with the needs of accessing internals, normally an access hole (normally used manhole) will be provided.

Access_internal

However, in small vessel with internals, a flanged head is preferred. Most of the time a swing davit will be installed on the flanged head to held the flange without assistance of any hoist.

Constructibility / fabrication limitation
Flanged head some time is used due to complexity of fabrication. There are many event where a inline condenser is mounted on top of a column.

condenser_top_mounted

In some event where the column is small diameter (i.e. 1000mm) and a condenser with 800m ND needs to be mounted on top, there will be difficulties to use a elliptical head. those a flanged head with mating concentric reducer will be used. Apart it serve as manhole to access the internals such as demister.

Cost Saving
Sometime process and operation may required a manhole (for any specific reason) on a small vessel. Apart from construction limitation, providing a flanged head will solve the constructibility problem, it also act as manhole. Some cost saving is expected.

MW

Above are some common reasons for selection of head type. I am sure there are others special reason(s) for the selection in Petrochemical & Chemical industry. If you have any example, why not sure with us ? OR if you have any photos for above applications, why not sent to me so that i can upload here ?

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Saturday, May 26, 2007

OGT - Others FREE articles related to Amine & CO2...


Following earlier introduction to <<Optimized Gas Treating, Inc. (OGT) - Experts in CO2-Amine>>, there are some others FREE articles available on this site for download...Refer to below listing and relevant links...ENJOY...
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...
Knowledge does not belongs to any of us but it belongs to ALL of US...Let Share It...I still believe the more you share, the more you will gain...

Post-combustion Capture of CO2
Treating High CO2 Gases with MDEA
Tray Hydraulic Operating Regimes and Selectivity
Upgrading Acid Gas Streams
Acid Gas Enrichment Part I: Maximizing Selectivity
Acid Gas Enrichment Part II: Maximizing Selectivity
Troubleshooting a Tail Gas Treater
Troubleshooting a Refinery Fuel Gas Treater
Troubleshooting Amine Plants
Simulator Provides Guidance for Increasing CO2 Slip in Gas Treating Applications
Eliminating Guess Work
How to Increase CO2 Slip
Effective Amine Technology
Effect of Heat-Stable Salts on Amine Absorber and Regenerator Performance
Are Your Simulation Amines too Clean?
Acid Gas Enrichment - Maximizing Selectivity

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Friday, May 25, 2007

Optimized Gas Treating, Inc. (OGT) - Experts in CO2-Amine


Carbon Dioxide (CO2) is known as one of industrial waste gas causing global warming...there are number of measures are implemented to reduce global warming. CO2 reduction measures are CO2 capturing, reinjection into aquifer, injection into reservior for well maintenance, gas injection for enhanced oil recovery (EOR), etc.



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 :

Column related


- Column Design Using Mass Transfer Rate Simulation (PetroChemical & gas Processing)





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Thursday, May 24, 2007

Generalised model to predict pressure drop and capacity of countercurrent gas/liquid packed column


How to calculate pressure drop and capacity of countercurrent gas/liquid packed column ?



J. Stichlmajr et al has published an article may answer above question :






A generalized model has been developed for the prediction of pressure drop and flooding in packed columns in which gas and liquid flow countercurrently. The model has been validated for a wide variety of packings, both random and structured. A single mathematical expression is used to describe all flow regimes: dry gas, irrigated gas flow below the load point, loading region, and flooding. The approach to the model development is fundamental in character and is an improvement over models published.



The model can be used with

- Structured packing : Montz, Gempack, Sulzer

- Random packing (ceramic) : Raschig, Pall, Reflux, Hiflow, Berl Saddles, Intalox Saddles, Torus Saddles

- Random packing (metal) : Raschig, Pall, Bialecki, Nutter, Cascade Mini, Super Saddles

- Random packing (plastic) : Pall, NSW, Leva



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Saturday, May 19, 2007

KG-TOWER® - FREE Column hydraulic rating software from Koch-Glitsh...



"Version 3.2 of Koch-Glitsch’s hydraulic rating software, KG-TOWER® Equipment Rating Program, is now available for download! This electronic design tool can assist you in the specification of mass transfer equipment, including conventional and high performance valve trays and conventional and high performance random and structured tower packings. "...Registration required for KG TOWER®
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...
Enjoy...

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Thursday, May 17, 2007

AMISTCO (P1) - Extensive info on Mist eliminator & Column Internals

AMISTCO, a mist eliminator, knitted mesh, random & structured packing, distillation inlet distributor, internal support, filter & coalescer manufacturer. Incorporated 26 years ago and located in Alvin Texas, South of Houston...


AMISTCO has published several good articles for Mesh and Vane Mist Eliminators from fundamentals, application, and design aspects.

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Tuesday, May 15, 2007

Koch-Glitsch LP - One of the OSHA site Star !


Koch-Glitsch LP - One of the OSHA site Star !



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
Using the Phase Doppler Particle Analyser (PDPA) Laser Probe for FGD Moisture Carryover Measurements
Brochure...
Overview of Koch-Otto York Product Line and Applications

DEMISTER® Mist Eliminator Installation Manual







FLEXIFIBER mist eliminators with carbon fiber. High Fluroride Applications historically corrosive to glass fibers.



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Monday, May 14, 2007

Dividing WALL Column...A special column design from MONTZ






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


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Sunday, May 13, 2007

FRI - A member supported Fractionation & Distillation research and testing coporation...





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...



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Wednesday, May 9, 2007

KG (Part 2) :- A brand that should not be missed by any Chemical & Process Engineer


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

FLEXILOCK® Tray Construction
OMNI-FIT® Technology
SPEED-WAY® Manways
SATURN® Technology


Structured Packing

Structured Packing
Packing and Internals for Severe Services


Random Packing

IMTP® High Performance Packing
Plastic Random Packing
Metal Random Packing
FLEXIMAX® Random Packing


Packed Tower Internals

Plastic Packed Tower Internals
Metal Packed Tower Internals
Tower Internals Hardware and Services


FAQ

17 Critical Questions
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?


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Monday, May 7, 2007

KG (Part 1) :- A brand that should not be missed by any Chemical & Process Engineer

Koch-Glitsch, a manufacturer of mass transfer products that you should not be missed by any Chemical and Process Engineer... global leader in the design and manufacture of state-of-the-art mass transfer products for the chemical, petrochemical, refining, gas processing, pharmaceutical, and specialty industries.
Products including
- grid, structured and random packing in metal or plastic
- replacement hardware for distillation, absorption, stripping and extraction columns.
- available in a wide range of metals, plastics, thermoplastics, and fiber-reinforced plastics.
FREE ARTICLES

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Sunday, May 6, 2007

ACS - Design manual for Mist Eliminators, Trays, Packing, Internals...All in distillation columns



ACS Separations Technologies

Suppliers for
- custom engineered mist eliminators
- fractionation trays
- random packing
- tower internals
- liquid-liquid coalescer

for E&P, refining and petrochemical industries.









Some good articles shared by ACS Separation Technologies...
Design manual

- Mist Eliminator Design Manual covers both mesh and vane type mist eliminators. Includes material types, design theory, sizing, and application case studies.
- Liquid-Liquid Coalescer Design Manual covers all liquid separation media types down to 1 micron. Includes various element types, design theory, sizing, and application case studies.
- ACS/Montz Packing Design Manual catalog covers all types of structured and random packings made from wire, sheet metal foil, and expanded metals. Includes material types, design theory, sizing and performace curves, and applications.
Technical Papers

-
Improving Gas Dehydrator Efficiency - ACS Optimiztion of mist elimination equipment for Glycol & Amine gas treatment systems
-
Oily Water coalescers for environmental clean up and produced water remediation
-
No welding process vessel upgrades for mist eliminators, coalescers, and inlet diffusers

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Thursday, April 19, 2007

SULCOL: FREE tower internals design package


Sulzer Chemtech Ltd is active in the field of process engineering and is a technology leader in the field of mass transfer and static mixing, with its advanced and economical solutions.
Sulzer Chemtech offers a FREE tower internals design package : SULCOL for Windows. As claimed by Sulzer this program is based on real applications in industrial columns and Sulzer's own experimental data. SULCOL can be downloaded from www.sulzerchemtech.com, under pull-down menu Design Tools. Download required registration...

Some features in SULCOL :

  • structured and random packing hydraulic design and rating
  • tray hydraulic design and rating includes fixed and movable valves, one pass, multipass and conventional downcomer tray design
  • Complete description of Sulzer Chemtech's tray portfolio including Shell tray technology.
  • Imports data from PRO/II, ASPENPLUS and Excel.
  • Export data to RTF or an XML file


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