Circulation vent design- API 650 Internal Floating Roof Storage Tank
Circulation vent design- API 650 Internal Floating Roof Storage Tank
(OP)
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.





RE: Circulation vent design- API 650 Internal Floating Roof Storage Tank
In the scope it states "This International Standard does not apply to external floating-roof tanks". If you have internal floating roof tanks, you could use API 2000 in my opinion.
Two inbreathing and outbreathing rates are given, one for low vapor pressure product (basically 1 volume of air for 1 volume of liquid) and for high vapor pressure product which for outbreathing, has a higher allowance because of the vapors being displaced. With an internal floating roof tank, as it rises or falls you simply need to outbreathe or inbreathe the corresponding volume.
Annex E gives a good discussion of the theory behind the standard. In general, I don't see why the same approach wouldn't apply to a fixed roof tank with an internal floating roof. Since a floating roof prevent product loss into the vapor space, I would likely pick the venting requirements for a low vapor pressure product.
Ultimately, you need to move air in and out of the tank to prevent overpressure or vacuum from damaging the tank. I haven't looked at the openings set by API 650 and backcalculated what pressure/vacuum they correspond to. My guess is the pressures are very, very low even relative to atmospheric tank design pressures.
RE: Circulation vent design- API 650 Internal Floating Roof Storage Tank
The version of API 2000 I had looked at was the 5th edition, 1998, which mentions both external floating roof, and free venting internal floating roof tanks. I just looked at the 2009 version and like you say, it excludes only external floating roof tanks, there is no mention of internal floating roof.
API 650 (10th edition) does go on to say if gas blanketing is used in place of circulation vents, then API 2000 should be used for the calculations. The 11th edition makes no mention of this, however I assume it will remain same.
Anyways, the client wants free venting system, which excludes blanketing. I will look further into the Annex E of API 2000 and see what it says.
RE: Circulation vent design- API 650 Internal Floating Roof Storage Tank
RE: Circulation vent design- API 650 Internal Floating Roof Storage Tank
Is there a way to just move the thread and its contents directly, or will I have to start the topic all over?
Regards
RE: Circulation vent design- API 650 Internal Floating Roof Storage Tank
RE: Circulation vent design- API 650 Internal Floating Roof Storage Tank
prevent the development of a combustible gas mixture within the tank is required. Additionally, the tank shall be protected by pressure-vacuum vents in accordance with 5.8.5, based on information provided by the Purchaser.