vesselguy
Petroleum
- Feb 25, 2002
- 386
The largest API620 tanks I have designed in the past were around 30ft and had self supporting cone or dome roofs. For API650 tanks, I have designed them to 120ft with supporting roof. No problem. However, I now have to consider the possiblility of changing several 100ft diameter API650 tanks (with Appendix F)into full blown API-620 design because process engineers want to increase the pressure!
I don't have experience with this large diameter API620 design. Can the more experienced tank engineers confirm for me if I can still have a supported roof (ie. internal rafters & columns) and still be an API-620 design? I think it is possible as long as I meet the top shell course's compression area requirements and the roof and shell thickness is sufficient to resist the internal pressure.
Would the fabrication cost of an API-620 design be much more than an API-650 design? Thanks.
I don't have experience with this large diameter API620 design. Can the more experienced tank engineers confirm for me if I can still have a supported roof (ie. internal rafters & columns) and still be an API-620 design? I think it is possible as long as I meet the top shell course's compression area requirements and the roof and shell thickness is sufficient to resist the internal pressure.
Would the fabrication cost of an API-620 design be much more than an API-650 design? Thanks.