Wazobia
Chemical
- Aug 24, 2006
- 23
Hi.
I'm involved in a project for a fuel storage facility.
We are designing tanks both fixed roof tanks, and internal floating decks, and I am sizing vents for these tanks.
The requirements and calculations for fixed roof tanks are quite detailed in API 2000, however it explicitly states that it doesn't cover floating decks.
After going through API 650, I came across appendix H which mentions circulation vents at the top of the fixed roof (geodesic). It goes into some detail about maximum spacings between vents, minimum total open area of vents as a ratio of tank diameter, and minimum area of an open vent at the centre of the fixed roof.
My question is if there is a definite calculation for the sizes of these vents, as opposed to minimum and maximum values, since I apparently cannot use API 2000? My background over the past few years was in upstream oil & gas design, and I have hardly ever come across relieving a non pressure vessel. It's been a real learning process, however I still need some expert advice
Any help would be greatly appreciated. Thanks.
Some more information - The floating roof tanks are 60,000 m3 capacity, with a diameter of 60 m. The fuels are petrol and naphtha.
I'm involved in a project for a fuel storage facility.
We are designing tanks both fixed roof tanks, and internal floating decks, and I am sizing vents for these tanks.
The requirements and calculations for fixed roof tanks are quite detailed in API 2000, however it explicitly states that it doesn't cover floating decks.
After going through API 650, I came across appendix H which mentions circulation vents at the top of the fixed roof (geodesic). It goes into some detail about maximum spacings between vents, minimum total open area of vents as a ratio of tank diameter, and minimum area of an open vent at the centre of the fixed roof.
My question is if there is a definite calculation for the sizes of these vents, as opposed to minimum and maximum values, since I apparently cannot use API 2000? My background over the past few years was in upstream oil & gas design, and I have hardly ever come across relieving a non pressure vessel. It's been a real learning process, however I still need some expert advice
Any help would be greatly appreciated. Thanks.
Some more information - The floating roof tanks are 60,000 m3 capacity, with a diameter of 60 m. The fuels are petrol and naphtha.