Question

In: Other

how can the diameter and hight and type of packed effect the prcess in scrubber column

how can the diameter and hight and type of packed effect the prcess in scrubber column

Solutions

Expert Solution

Diameter:- The decrease in diameter of the scrubber column increases the scrubbing efficiency as the decrease in diameter results in the increase of droplet concentration per unit volume of the scrubber. But as the decreasing of diameter proceeds, it limits the span of droplets with a large initial release angle which forces the droplets to hit the scrubber wall to form a liquid film, and caused significant liquid coagulation. This phenomenon significantly reduces the liquid surface area which results in the reduction of scrubbing efficiency.

Height:- The increase in the height of the scrubber increase the contact area of the two streams which results in the increase of scrubbing efficiency. But as it is increased further the vapour flow rate might increase and carry out liquid with it which results in inproper operation of scrubber that further results in decrease of scrubber effucency.

Type of packing:- It should be very open in design to minimize pressure drop while still maintaining high surface area. Spiral pac-type packing will accomplish this. Alternate packing is also suitable to enhance this. The type of packing will effect on temperature, pressure drop, scrubbing efficency etc.,


Related Solutions

why is fractionating column packed with glass beds more efficient that a vigreux column of the...
why is fractionating column packed with glass beds more efficient that a vigreux column of the same length and same diameter additionally why does the column need be wrapped with aluminum foil
To obtain a resolution of 1.50, how many theoretical plates must a packed column have for...
To obtain a resolution of 1.50, how many theoretical plates must a packed column have for two peaks which elute at 5.42 and 5.63 minutes, where tm = 1.00 min? With a resolution of 1.50, are these peaks considered to be resolved?
a. What is meant by countercurrent operation? b. Why is a packed bed absorption column column...
a. What is meant by countercurrent operation? b. Why is a packed bed absorption column column operated countercurrently? c. How would the performance change if the column was operated cocurrently?
What are open tubular columns and give some differences between open tubular column and packed column
What are open tubular columns and give some differences between open tubular column and packed column
A packed bed reactor is filled with catalyst material with a diameter of 1.5 mm. The...
A packed bed reactor is filled with catalyst material with a diameter of 1.5 mm. The length of the reactor is 80 cm and the catalyst has a porosity of 0.45. The superficial mass velocity of the inlet gas is 7.5 kg/m2-s with a viscosity of 1.55x10-5 kg/m-s and a density of 2.8 kg/m3. The inlet pressure is 300 kPa. Find the pressure, P, at the end (the exit) of the PBR.
The following conditions were established for a chromatographic separation of multiple hydrocarbons on a packed column...
The following conditions were established for a chromatographic separation of multiple hydrocarbons on a packed column with 1.1 g of liquid stationary phase: inlet pressure 826 torr, room pressure 756 torr, vapor pressure of water at room temperature 17.5 torr; column temperature 110ºC, room temperature 20°C; measured outlet flow rate 20.0 mL/min; retention time for nonretained species 25.3 s, retention time of the first eluting species 1.56 min. Based on these conditions, the pressure drop correction factor j is _______,...
A gas stream containing 3% A is passed through a packed column to remove 99% of...
A gas stream containing 3% A is passed through a packed column to remove 99% of A by absorption in water. The absorber will operate at 25 C and 1 atm, and the gas and liquid rates are to be 20 mole/h ft2 and 100 mole/h ft2 respectively. Mass transfer coefficient and equilibrium data are as follows: y* = 3.1 x at 25 C k_xa = 60 mol/h ft3 unit mol fraction k_ya = 15 mol/h ft3 unit mol fraction...
If one choose to work on a column packed with smaller particle sizes, what might be...
If one choose to work on a column packed with smaller particle sizes, what might be the biggest disadvantage of using smaller particles (in size) as packing material (stationary phase) in column chromotography for separation of mixtures?
Air at 80oC flows through a packed bed of cylinders with effective diameter of 0.015 m...
Air at 80oC flows through a packed bed of cylinders with effective diameter of 0.015 m and length the same as the diameter. The bed void fraction is 0.40 and the length of the packed bed is 2 2 m. The air enters the bed at 1.3 atm abs at the rate of 2.45 kg/m .s. Calculate the pressure drop of air in the bed
Air containing 1.6 vol% sulphur dioxide is scrubbed withpure water in a packed column of 1.5...
Air containing 1.6 vol% sulphur dioxide is scrubbed withpure water in a packed column of 1.5 m2 cross sectional area and 3.5 m heightpacked with no.2 plastic Intalox saddles, at a pressure of 1 atm. Total gasflow rate is 0.062 kmol/s, the liquid flow rate is 2.2 kmol/s, and the outlet gassulphur dioxide concentration is y = 0.004. At the column temperature, theequilibrium relationship is given by y = 40x. (a) What is L/Lmin (b) Calculate NOG. (c) Determine HOG....
ADVERTISEMENT
ADVERTISEMENT
ADVERTISEMENT