ABSORPTION
Falling Liquid solvent absorbs the gas in the absorption column & is then sent into any one of he following unit:- Distillation, stripping section, removal through precipitation & settling, neutralization, oxidation, reduction & hydrolysis.
Purpose: - Gas purification
- Gas separation
- Product recovery
- Solvent recovery
Solvent Properties:
- Solubility of gas should be high in selected solvent. ( If not, then absorption is a waste!! )
- Low volatility organic liquid ( but water is preferred in many cases, due to easy availability & removal of water soluble gases like, HF, HCl, SiF4 ).
- Low vapor pressure ( to reduce evaporative loss of solvent )
- non-toxic, non-flammable, non- corrosive
- Low viscosity
Internals of Packed tower
- Packing support plate: It must bear the weight of the packings & allow unrestricted flow of down coming liquid. Drawback is that, that the packing blocks some holes, thus reducing the tower capacity.
- Liquid distributor: Placed 6-12 inch above packing for allowing gas disengagement from the bed. Absorption & stripper columns require only one distributor, whereas, Distillation column requires 2 (feed & reflux)
- Liquid re-distributor: Some part of entering liquid flows through the wall without coming in contact with the gas flowing counter currently, thus we need a liquid re-distributor to collect the down coming liquid and distribute it uniformly throughout the bed and thus increase the efficiency of the tower.
- Demisters / Entrainment separators: Generally installed in exit gas streams for arresting the liquid droplets entrained in the gases. If demisters are not installed they can corrode / choke downstream equipments like heat exchangers tubes, damage tube sheets, contaminate products etc.
- Against all acid gases, metal tower, metal plates, metal packing or any other metal internals can have deleterious effect.
- Same is the case with organic liquid and plastic packing.
- Ensure internal cooling facility is available when materials and gases releases high heat of absorption.
Dry & wet random packing:
Packed & plate column:
Good Job,
ReplyDeleteKudos...Keep doing good work. How is your college VNIT, NAGPUR? Is it good for Mech . or Chemical Engg? Please let me know your views aboyour college & it's reputation .
Looking forward to hear from you soon.
Thanks & Regards,
Suresh C.Madhav
(sureshcm24@yahoo.com)
VNIT nagpur is a good college. Mech is old branch here and holds great repuatation, whereas, Chemical is newly opened branched(2006)but has a very huge dept. and facilities and labs are well versed with the latest technologies and is growing fast.
ReplyDeleteHi Raj!
Deletegood work bro.....may i know about your final year project??what was that??kindly send me your final year project report on this E-mail address ad33l_choudhary@hotmail.com OR ad33l_choudhary@yahoo.com
Thanks
Adeel Choudhary
Hi Raj,
ReplyDeleteI was looking at the table of tower packing vs. plates (trays) and saw that it said that packing were used in towers with diameters <0.6m. Packings are routinely used in towers 3m in diameter and many vacuum towers with diameters 7m in diameter. The key to doing this is to properly design the liquid and vapor distributors. Fractionation Research, Inc (www.fri.org) does research and testing of packings and plates in pilot plant towers 1.22m in diameter. If you go to FRI website and click on Publications you will find papers by me and others on the scale-up of packings
I see you have referenced Koch-Glitsch & Sulzer on the pictures used in the write-up. They both have packed chemical, petrochemical, & refining towers 7m dia and larger. Some of these large towers are vacuum EB/STY and refining Vacuum Crude towers.
Best regards, Frank Rukovena
Very Informative Article! It seems you have done lot of research, great job. These Mass Transfer Equipment's are used to enhanced performance of mass transfer operations.
ReplyDelete