etrobal
Mechanical
- May 27, 2008
- 39
we have had problems with solids in our pressure vessels ranging in sizes 0.625mm max with specific gravity of 4.58 to 5.30. the fluid is dry steam with max mass flow of 13.23 kg/sec, design pressure at 14.06 kg/cm2g, design temperature at 197.7degC, separation pressure of 11.72 kg/cm2g, separation temperature of 190degC with the solids at 84ppm at the nozzle inlet. the top ellipsoidal head is the first to leak due to the suspended solids.
we've had also leaks in our pipe elbows and other change in directions fittings in our pipelines upstream of the pressure vessel.
if we will line our carbon steel pipes with another material, or similarly with our pressure vessel of sa515 gr70 lined with another material, how will this affect our stress calculations, or stress runs? will we use the original material's allowable stresses or use the liners? will expansion affect the vessel nozzles, connections and other endpoints of the piping system?
we are bidding the design of the pressure vessel, where, if after installation, the designed vessel can provide a maximum 5ppm suspended solids at the steam outlet, the company is prepared to purchase several for its various wellheads. we've had bids ranging from usd52,000 to usd80,000. while we will be able to arrest, hopefully, the deterioration of the vessel heads, our problem will be on the upstream piping system. wil it be cheaper instead to have a lined system than a vessel designed to outsmart the solids?
we've had also leaks in our pipe elbows and other change in directions fittings in our pipelines upstream of the pressure vessel.
if we will line our carbon steel pipes with another material, or similarly with our pressure vessel of sa515 gr70 lined with another material, how will this affect our stress calculations, or stress runs? will we use the original material's allowable stresses or use the liners? will expansion affect the vessel nozzles, connections and other endpoints of the piping system?
we are bidding the design of the pressure vessel, where, if after installation, the designed vessel can provide a maximum 5ppm suspended solids at the steam outlet, the company is prepared to purchase several for its various wellheads. we've had bids ranging from usd52,000 to usd80,000. while we will be able to arrest, hopefully, the deterioration of the vessel heads, our problem will be on the upstream piping system. wil it be cheaper instead to have a lined system than a vessel designed to outsmart the solids?