Introduction
Efficient gas absorption depends on the following:
- Intimate contact
- Efficient Heat Transfer
This is achieved in a Falling Film Absorber which is essentially a shell & tube heat exchanger in which both gas to be absorbed and absorbing liquid flow co-currently downward with extraction of heat by circulation of coolant in the shell. The abssorbing liquid is circulated through a tank till desired concentration is achieved. The liquid flows at such a rate that the tubes do not flow full of the liquid but instead, descends by gravity along the inner walls of the tubes as a thin film. Obviously, this produces a much greater linear velocity for a giver rate flow than could be obtained if the tube flowed full.
The equipment works as a number of water cooled-wall columns in parallel and each tube is provided with distribution system on top to effect uniform distribution of both liquid and gas and also formation of a thin liquid film on the inner surface of the tube.
Salient Features
- The heat of absorption is continuously removed. This ensures better absorption and product concentration as compared with conventional packed tower.
- Low residence time and operating temperature ideally suited to heat sensitive materials.
- Borosilicate glass and PTFE contact parts ensure corrosion/ contamination free operation.
- Both standard and custom built units are available.
- Capable of operating from zero to maximum gas flow rate.
- Ease of installation due to light weight.
- Trouble free and consistent performance with minimal attention.
- Wide application e.g. HCl, HBr, NH3, SO2, H2S, Br2 etc.
- Less cost.
- Negligible pressure drop compared to conventional columns.
- Compact design Sleek and slender.
- Both heat and mass transfer operations are incorporated in a single equipment.
- Very high heat transfer coefficient as the liquid falls instead of flowing.
- Scaling of process fluid is minimal due to high velocity and ease of cleaning by simple acid circulation.
- Hot conditions are eliminated at all stages namely pipe, tanks and pumps etc.
Limitations
- Not recommended for gases containing high proportion of inert (insoluble).
- Not applicable if the gases are not highly soluble.
Sr. No. | Nominal Size (mm) | Absorber Area (m2) | No. Of Tubes/Tube OD (mm) | Max. Gas Absorption Rate (Pure HCL)* (Kg/hr) | Max. Acid Prod. Rate (As 30% HCL)( Kg/hr) | Height (m) |
---|---|---|---|---|---|---|
1 | 80 | 1.00 | 4/20 | 30 | 100 | 4400 |
2 | 100 | 1.76 | 7/20 | 60 | 200 | 4500 |
3 | 150 | 4.80 | 19/20 | 150 | 500 | 4600 |
4 | 225 | 7.80 | 31/20 | 250 | 833 | 4920 |
5 | 300 | 15.30 | 61/20 | 500 | 1667 | 5050 |
6 | 400 | 36.00 | 143/20 | 1175 | 3917 | 5300 |
7 | 450 | 47.00 | 187/20 | 1500 | 5000 | 5700 |
8 | 600 | 84.00 | 333/20 | 2700 | 9000 | 5800 |