micjk
Mechanical
- May 20, 2002
- 120
Is it possible to calculate the mean time to failure for a ss tank top with a top mounted agitator. What we have is a tank with top mounted agitator that stirs a viscous solution (not sure of viscosity) at a speed of @ 60 rpm. This solution will "gel" when exposed to the atmosphere. I believe that we have build up on the agitator blades which is causing an imbalance scenario. The nozzle that this agitator is mounted to is not gusseted which inturn allows the agitator to rock in a circular motion flexing the top @ 1/16 - 1/8 in with every revolution, which will eventually, I believe, cause failure of the tank top (which would not be good). The shell is @ 3/16 - 1/4 in thick ss with a reinforcement plate of the same thickness welded to it. The failure is inevitably going to occur at the weld seam between tank top and this reinforcement plate (my opinion).I've told management about this,what will happen and that we need to gusset this nozzle, but this is a very integral part of our process and shutting down is a very rare option. Can I calculate stresses at the flex points and how long before we start to see signs of fatigue. Formulas and or website info would be deeply appreciated. Roy Gariepy
Maintenance and Reliability Dept.
Bayer Corporation Dorlastan Fibers Div.
Goose Creek, South Carolina USA
Maintenance and Reliability Dept.
Bayer Corporation Dorlastan Fibers Div.
Goose Creek, South Carolina USA