How much product should there be above a vortex breaker to ensure vortices do not form in a pump suction line?
There are lot of calculations and thumbrules out there for volume needed above an internal pipe in order to avoid using a vortex breaker, but I don't see any guidance if there is...
Do API 650 tanks have center-to-edge settlement allowances following erection/hydrotest?
In API 650 I have found the following:
1) 7.5.2 Plumbness: The maximum out-of-plumbness of the top of the shell relative to the bottom of the shell shall not exceed 1/200 of the total tank height.
2)...
For API 650 tank shell thickness calculation, what are the reasons why someone would use the 1-ft Design Method over the Variable Design Point Method? I know that API 650 5.6.3.1 states that the 1-ft method shall not be used for tanks larger than 61 m (200ft) in diameter. If I have a 50 ft...