It is desired to reduce the 2% CO, in 23 Ib/sec of a natural gas stream using absorption in aqueous diethylamine flowing at 40 lb/sec. Either 1 ½ in. Raschig rings or 1 ½ in. Pall rings are being considered for packing. A pressure drop of 0.25 in H,O/ft is desired to minimize foaming. Under operating conditions, the densities of the gas and the liquid are 2.8 and 63 Ib/ft³, respectively; the liquid viscosity is 2 centistokes. "Determine the flooding velocity and the tower's cross-sectional area using the succeeding procedures
It is desired to reduce the 2% CO, in 23 Ib/sec of a natural gas stream using absorption in aqueous diethylamine flowing at 40 lb/sec. Either 1 ½ in. Raschig rings or 1 ½ in. Pall rings are being considered for packing. A pressure drop of 0.25 in H,O/ft is desired to minimize foaming. Under operating conditions, the densities of the gas and the liquid are 2.8 and 63 Ib/ft³, respectively; the liquid viscosity is 2 centistokes. "Determine the flooding velocity and the tower's cross-sectional area using the succeeding procedures
Elements Of Electromagnetics
7th Edition
ISBN:9780190698614
Author:Sadiku, Matthew N. O.
Publisher:Sadiku, Matthew N. O.
ChapterMA: Math Assessment
Section: Chapter Questions
Problem 1.1MA
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Please answer using the given procedure:
![Determination of Flooding Velocity
Procedure
1. Obtain liquid density (PL) and viscosity(H), gas density(pg) and packing
factor(Fp)
2. Calculate the ratio of flow of entering liquid to entering gas (L/G) from
problem data.
3. Calculate FLG = (L/G)(pg/PL)0.5
4. Obtain CP from Fig. 14-55/14-58 (HB) using FLG and pressure drop of15 in
%3D
5. Solve Up =CP[(PL- PG)/(PLFP)]0.5[PL/4]°.05 using appropriate units in the HB
6. Gp = UF PG
%3D](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2F74c20485-f664-4cf0-af7e-1d10d2425428%2Fbbd96980-5e2a-462c-bf82-ead0f7d3ed6b%2F30srjow_processed.png&w=3840&q=75)
Transcribed Image Text:Determination of Flooding Velocity
Procedure
1. Obtain liquid density (PL) and viscosity(H), gas density(pg) and packing
factor(Fp)
2. Calculate the ratio of flow of entering liquid to entering gas (L/G) from
problem data.
3. Calculate FLG = (L/G)(pg/PL)0.5
4. Obtain CP from Fig. 14-55/14-58 (HB) using FLG and pressure drop of15 in
%3D
5. Solve Up =CP[(PL- PG)/(PLFP)]0.5[PL/4]°.05 using appropriate units in the HB
6. Gp = UF PG
%3D
![It is desired to reduce the 2% CO, in 23 lb/sec of a natural gas stream using
absorption in aqueous diethylamine flowing at 40 lb/sec. Either 1 ½ in.
Raschig rings or 1 ½ in. Pall rings are being considered for packing. A
pressure drop of 0.25 in H2O/ft is desired to minimize foaming. Under
operating conditions, the densities of the gas and the liquid are 2.8 and 63
Ib/ft³, respectively; the liquid viscosity is 2 centistokes.
"Determine the flooding velocity and the tower's cross-sectional area using
the succeeding procedures](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2F74c20485-f664-4cf0-af7e-1d10d2425428%2Fbbd96980-5e2a-462c-bf82-ead0f7d3ed6b%2F2fkx51lc_processed.png&w=3840&q=75)
Transcribed Image Text:It is desired to reduce the 2% CO, in 23 lb/sec of a natural gas stream using
absorption in aqueous diethylamine flowing at 40 lb/sec. Either 1 ½ in.
Raschig rings or 1 ½ in. Pall rings are being considered for packing. A
pressure drop of 0.25 in H2O/ft is desired to minimize foaming. Under
operating conditions, the densities of the gas and the liquid are 2.8 and 63
Ib/ft³, respectively; the liquid viscosity is 2 centistokes.
"Determine the flooding velocity and the tower's cross-sectional area using
the succeeding procedures
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