Lancea
Structural
- Apr 8, 2011
- 2
Hi everyone,
I have a seismic calculation question.
A tube (19.48 ft, 2 ft diameter) stands in the middle of a 40 diameter 26 ft tall tank, in which the max operating water height is 23 ft.
When calculation the sloshing force on the TUBE, I did the impulsive & convective period of the tank mass (Ti & Tc), the impulsive & convective acceleration of the mass (Ai & Ac), then 0.5*Ti*Ai & 0.5*Tc*Ac are the max imulsive & convective velocity of the mass particles (Vi & Vc). After this, I used the "P = 0.5*density*velocity(square)*A*Cd" to calculate the force acting on the tube ,where the A = diameter of the tube * H (tube height in impulsive / convective mass region).
OK, the above precedure turned out the forces are pretty fractional.
Is this the good way to calculate the sloshing force on the tube??
Please let me know what you are going to do on this real problem.
Anyone's comments will help!
Thanks a lot!!
--Lancea
I have a seismic calculation question.
A tube (19.48 ft, 2 ft diameter) stands in the middle of a 40 diameter 26 ft tall tank, in which the max operating water height is 23 ft.
When calculation the sloshing force on the TUBE, I did the impulsive & convective period of the tank mass (Ti & Tc), the impulsive & convective acceleration of the mass (Ai & Ac), then 0.5*Ti*Ai & 0.5*Tc*Ac are the max imulsive & convective velocity of the mass particles (Vi & Vc). After this, I used the "P = 0.5*density*velocity(square)*A*Cd" to calculate the force acting on the tube ,where the A = diameter of the tube * H (tube height in impulsive / convective mass region).
OK, the above precedure turned out the forces are pretty fractional.
Is this the good way to calculate the sloshing force on the tube??
Please let me know what you are going to do on this real problem.
Anyone's comments will help!
Thanks a lot!!
--Lancea