Duwe and ash, thank's for your input. About the expansion coefficients, we already took those in mind. Tha ash experience, might be very usefull for a decision.
Big,
My question is more about - would tracing be enough? So, I'm looking for something like: If process fluid solidifies at 90ºC, for a 3" pipe one tracing line/two tracing line/jacketed line/etc is enough. We have steam available and we also have some electric tracing available, but this last...
Q:Do you require heating on the branch connection?
A:Yes. But it was decided to let it traced.
Q:How was the existing jacket terminated when you cut it for the branch connection?
A:According to the site you mentioned, it was swaged jacketed piping.
Q;Is the branch connection configured...
DSB123,
Yes, I meant jacketted pipe. And its not really a pipe-line, but it's a line with about 100 meters. The problem is that we have cut the pipes to put another entry in the line. In means the outside was cut off and we became without jacket in a small part of the line. So, I'm wondering if...
For heating a pipeline with steam, is there a simple definition/procedure to decide the use of a double-pipe or tracing?
Is there a site where I could read more of these (already tried a few, but didn't found what I'm looking)?
Thanks in advance
I have started this thread in the "Corrosion Engineer" threads. As the answers weren't of my satisfation, I came here searching other opinions.
Find the thread in the "corrosion engineer" threads in the attachment.
The questions:
Hello!
I have a problem with the filtering laterals...
Hello!
I have a problem with the filtering laterals (regeneration screen) inside cationic bed. They worn after 2 years of work. They are half-pipes (half is a common pipe and the other half is a screen with 300 microns openings) which contact with 3 fluids: 1 - Raw Water; 2 – Air; 3 – HCl...
