Hi.
For you process folks I have the following question: If you run a long pipe with 2 phase fluid to catch up the condensate in a trap and you want to release the condensated water to atmospheric pressure to generate steam which you want to lead away using a "chimney".
Would this chimney be a...
I have discussed the high velocity and brought up that it will be a big problem and we came to a conclution that the nominal pipe size could be increased to lower the rate of erosion.
This is produced water, I was allowed to reduce the velocity by increasing the nominal pipe size. As DSB...
SJones are correct, im sorry for not provoiding the fluid details here in this post.
The fluid contains following in mg/kg:
CO2: 56,7
H2S: 85,3
SiO2: 694,8
Na: 152,2
SO4: 18,9
SJones Thank you very much for your specific informative answer.
Maybe you have some references or some materials to investigate. To me it seems like the temperature is won't let me chose a non metallic material.
Regards
Hello.
What is the basic steps of estimating rate of corrosion for piping runs?
Assuming uniform corrosion and erosion.
The fluid contains following in mg/kg:
CO2: 56,7
H2S: 85,3
SiO2: 694,8
Na: 152,2
SO4: 18,9
other parameters:
Temp: 210 degree Cecius
Velocity: 40m/s
Is there a way I can...
Hello.
Currently I´m working on a piping design that will transport highly corrosive fluid with low pH at 210 degrees Celsius. I have been trying to determine what kind of material will be suitable for such applications.
The velocity of the fluid can be assumed to be 48 m/s. From my research...
