No, these flanges are part of the steel ducting system used to recover off gas from the steel furnace. The dimensions are in the range of 1500x 1700 to 2400 square. The ducting is of 12 mm plate and the proposed flange thickness is 22mm with full face gaskets.
Hi I am looking at finding a standard that could be used for design of an atmospheric process vessel (tank) for SG>1 toxic/corrosive products. The vessel diameter is 3m or less and will be supported on four legs.
I am looking at completing a flange design for a 2400mm square flue gas duct in a steel mill. Since it is not a circular flange type I can not use BPVC Section VIII Appendix 2 design criteria. Can any one shed light on if there is a design standard for such flange design?
Want to find out the best way to establish a stress intensity factor (SIF) for a butt weld join (BW) that was completed with a unfused root face about 1.6mm (1/16").
RMW, The service I am looking for is lime rock feed to the kiln. The rocks or chips are about 10mm x 20mm x 5mm in size (random sizes). So my concern is of they will get jam in the rorary feeder?
Any comments
Can any body help with finding an isolation valve for a lime chip feeder duct attached to the kiln? Issue is to minimize trap air going into the kiln and the loss of vacuum in the kiln.
Tx
llls
Hi Guys, Sorry for not replying. OK the tank I am looking at needs a head room of 1.5m, we are planning to have a 15 deg cone bottom (mainly for self draining requirement). The shell T-T is about 6.5m. Earlier comments by hdw to limit legged tanks to 1m Dia, any idea how this limit came from, as...
Thanks JStephen, I am located in New Zealand. I have copy of API650/620. Also AS1692 is used in NZ for flammable liquid tanks with SG<1. The contents of the product I am looking at is SG>1 and falls in to corrosive product.
Hi I am looking at finding a standard that could be used for design of an atmospheric process vessel (tank) for SG>1 toxic/corrosive products. The vessel diameter is 3m or less and will be supported on four legs.
Hi,
I am after some information on a good engineering practice document that could be used for shipload out system piping system design for the transfer line between the Wharf and storage tank located inland. Any body know about a link to such information site? Or happy to communicate with me on...
Hi,
I am looking at issues with oxygen compressor building. Recently came a across thsi problem:
The issue is the comp building is naturally ventilated via the roof apex opening (600 wide runs along the building roof). The interstage PSV and discharge PSV tail piping vents within the building...
Hi,
I am looking at issues with oxygen compressor building. Recently came a across thsi problem:
The issue is the comp building is naturally ventilated via the roof apex opening (600 wide runs along the building roof). The interstage PSV and discharge PSV tail piping vents within the building...
Hi Deics, Thanks for your feedback. As you know due to process licensor confidentiality issues I haven’t contacted Stamicarbon. By the way our process licensor is not Stamicarbon. Therefore I would appreciate to chat with you or communicate via email. My email address is...
