A Tower separates the mixture into 2 or more desired parts. It also transfers material from one phase to another. The towers are classified based on:
Length to Diameter ratio of a Tower normally ranges from
3: 1 to 20:1
They are perforated trays with small round holes. Vapor enters vertically through these holes and bubbles through the liquid, providing high efficiency at a low cost. The perforations on active Deck are typically ½” holes. The hole size may vary from 0.18” to 1” depending upon the application. Sieve Trays are conventional Trays with lower capacity than valve trays with similar efficiency. Sieve trays depend on vapor velocity to hinder liquid from falling through the perforations on the tray deck. Lower vapor velocity than design lets liquid flow through the perforations rather than into the downcomer. This condition is known as weeping. Where weeping is severe, the equilibrium efficiency will be very low. For this reason, sieve trays have a very small turndown ratio. Their standard operating range is 2:1 which can be extended to 2.5:1 with slightly higher pressure drop. At the other extreme, a very high vapour velocity leads to excessive entrainment of the upper tray and loss of tray efficiency. Sieve Tray design factors include the hole arrangement, quantity, and size. The number of holes and their size depends upon the vapor flow rate in the tower. Sieve trays are not too good in terms of Capacity, Flexibility and Fouling resistance.
These are the Oldest Type of Trays for fractionation Columns. These Trays have Caps covering the risers on every hole on the active deck of the Tray. Each bubble cap assembly consists of a riser and a cap. The Vapor moving up the column passes through the riser on the tray floor and then is directed downward to bubble into the liquid surrounding the cap. Because of their design, bubble cap trays should not weep. However, bubble cap trays are more expensive because of the more metal and labor required to make such trays. These Trays have a lower capacity and higher pressure drop compared to sieve trays or other valve trays. They have a high Turn down ratio though (8:1 or even more). Bubble Cap Trays can manage very low liquid rates. They are therefore useful for low reflux ratio operations. Bubble Cap Trays are a good choice for Glycol dehydration Columns—absorption process
Perforated plates with vertically moveable valves on the perforations. Some of the stagnant liquid section areas of the tray may have small directional fixed valves as well. These Trays have higher Turn Down than Sieve Trays. Since valves of different weights can be put on the perforations, these Trays have a bigger operating range with reduced tendency to weep. They offer more operational flexibility compared to fixed valve trays. By simple turn up or turn down of the vapor flow rate within a certain range, one may operate moving valve trays over a wide operating range. Their nominal turn down is 4:1.The Turndown performance of moving valve tray can be improved by installing valves in rows with alternating valve thickness. For eg one can put 14 ga and 16ga valves in alternate rows to improve Tray Turn Down performance. They have acceptability for varied applications as they can be constructed with valves with different lifts (leg lengths). The moving valves can be circular or rectangular or circular caged valves, depending upon the need. These Trays are more prone to fouling than fixed valve trays because they have more surface area available for the deposition of contaminants.
Offer greater reliability and fouling resistance. Fixed valves are permanently open. Fixed Valves are more robust compared to moving valves so they can better withstand operational upsets. The vapor deflection by Valves , increases the vapor velocity on the tray deck around fixed or moving valves, which helps prevent zones of stagnation where solids can deposit, polymerization can begin, or corrosion can occur. Thus, valve trays offer more fouling resistance than small-hole sieve trays.
Mesh Pad is a great Tower Internal device for Mist elimination. We can provide various kinds of Mist Removers, depending upon the application.
Structured Packing is one of the three main devices used in Mass Transfer applications. The other two devices are Trays and Random Packing. Depending upon the requirements , different Structured packings can be provided for various Bed heights and Column Diameters. The structured packing we provide; employs a smooth transition to vertical axis from the bottom of upper layer to the top portion of each layer ,allowing much lower resistance to vapour and liquid flow across the packing at the interphase. This structured packing provides additional 20%~30% more capacity and significant lower pressure drop when compared to conventional structured packing of same surface area. This is so because in the conventional Structured Packing the maximum resistance to fluid flow is through packing channels at the interphase of two packing layers, limiting maximum usable capacity for standard structured packing for a given surface area. The directional change at the interphase of consecutive packing layer leads to additional resistance to vapour flow ,leading to liquid build-up thus causing additional pressure drop and consequently capacity loss. Packed towers are low pressure drop devices,
therefore, they are often used for vacuum distillations. The Packed Columns normally have a narrower operating range than trayed Columns. A packed Column may need a larger diameter than a tray column to handle the same feed rate.
Liquid Distributors play a very important role as a Tower Internal. Depending upon the application, a pipe OR gravity Distributor may be provided in various materials. The Figure here shows a Trough Baffle Distributor with side orifice in troughs. This is most suitable for a very low specific liquid rate. This distributor is equipped with integrated hold down grid. This distributor is equipped with high open area to minimize pressure drop. The distributor design consists of several troughs equipped with enhanced baffle plate. The trough walls are equipped with elevated distribution holes that feed onto a special liquid spreading baffle that is attached to it. The baffle spreads the liquid from each distribution hole into several streams feeding them in a controlled way onto the top of the packed bed. This drip point multiplier effect allows the use of larger holes within individual troughs, providing greater fouling resistance while achieving optimum liquid distribution quality even at very low liquid rates. The proposed distributor is equipped with pre-distributor parting box that receives the incoming liquid, reduces its momentum and feeds into individual troughs in proportion to area they are covering ensuring optimum distribution quality across entire operating range of liquid distributor.
This has spray Nozzles attached at the bottom of pipe-lets to ensure proper, even distribution of the liquid. There could be many branch pipes attached to the main pipe of the liquid distributor.
The packed bed will be equipped with GT-S101 Packing Support Grid.
Feed device @ Nozzle N1 (12”): We are quoting our GT-V101 Vane Inlet feed device in line with requisition documents with features as noted below.GT-V101 feed device is used for both vapour and mixed feed. The design consists of banks of vanes with curved design introducing feed laterally into column. The vanes split the incoming high velocity feed into multiple streams reducing the inlet momentum and distributing the fluid across entire cross section of the vessel. This ensures good disengagement between vapour and liquid and proper gas distribution to equipment above the feed section.
We are quoting our GT-A10 deck type collector tray to collect the Rich TEG solution and transfer it to column boot in line with requisition documents.
Liquid Distributors are very critical for the performance of a packed Column. Selection of appropriate Liquid distributor depends upon various factors like the type of application, type of packing, fouling tendency and the column diameter , liquid flow rates, requirement of the open area, requirement for a re-distributor to name a few.
Random Packing is normally cheaper for Columns less than 2 FEET diameter.
For corrosive fluids, random packing is often advantageous because it can be made of Plastic, Carbon, Ceramic or other highly resistant metallic or non-metallic material.
This is generally used in absorption and distillation columns to facilitate mass transfer between the Gas and Liquid Phases. Traditionally , Engineers preferred Random packing for small diameter columns ( <20”). Random packing is far cheaper than Trays or Structured Packing but Column Beds packed with Random Packing may experience channeling. They also have lower Turndown ratios compared to Trays. Random Packing can be supplied in Metal, Plastic or Ceramic. They are used in Columns for distillation, absorption as well as stripping. Random packing comes in various sizes. The bigger the size of Random Packing, the higher would be its capacity but lower would be the efficiency and cost. Similarly , for smaller sized Random Packing, the efficiency is higher but the Capacity gets compromised . Smaller sized Random Packing also costs more, generally.
They have an aspect ratio of 1:1. Pa rings are Cylindrical with slots punched on the ring wall and fingers inside the ring to offer more surface area. They have 50% - 80% higher capacity and efficiency than the Ra Rings of the same size. They are more commonly used in Columns providing service for Distillation, absorption or stripping.
They are the first generation Random Packing. They are plain hollow Cylinders like pipe pieces with an aspect ratio of 1:1. They can be provided in Metal, Ceramic or Plastic as per the application requirement. They have lower capacity and lower efficiency. They are generally used for corrosive or high temperature applications.
Sa Rings are Like Saddles. They have a low aspect ratio and offer good Mass Transfer between Liquid and gas Phases as the saddles mostly settle with their flat portion parallel to vapor and Liquid . They thus offer good capacity. They can be supplied in Metal, Plastic as well as Ceramic depending upon the need from the Customer. The Sa Rings may be used for De-methanizers, De-ethanizers, Quench Towers in general
CM Rings developed as the random packing evolved. They have an aspect ratio ( height : Diameter) of 1:3 which aids lower pressure drop and higher capacity. They are good in fouling media and may be used for such applications. They come in various sizes and can be provided in Metal or Plastic
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