I am involved in testing hydraulic tubing system (design pressure = 3000psi).
I have tested two sections individually.
I plan to join these two sections with JIC fittings.
Can anyone advise if I may do a "service leak test" of the system with pressure provided by the hydraulic system (ie the...
Thanks for these responses.
We like the v-cone from a space-saving point of view but have concerns about the robustness of the v-cone configuration in slug flow conditions.
We are now looking at the conditioning orifice meter (by Emerson).
Regards,
DJ Wright
Has anyone out there got experience of using the McCrometer v-cone flow meter for metering wet gas at a wellhead?
I have used venturis before but the v-cone flow meter has some apparent advantages (e.g. smaller required space envelope and lower cost).
Regards,
DJ Wright
Thanks for your thoughts.
In my application, gas will be flowing round bends at > 10m/s.
Intuitively, it seems to me that bends will not cause accumulation of hydrate crystals in such circumstances.
For more details, see similar posts in Chemical Process Engineering.
Regards,
djwright
Thanks for your advice.
My original post was I think slighly misleading. A reinterpretation of the expert's view is that turbulent flow regimes can promote hydrate growth.
Typically, a production well has xmas tree, pipework with choke, NRV connected to a manifold by means of a tee.
Our flow...
I am looking at wet natural gas piping system.
An expert has advised that hydrate crystals have a tendency to accumulate at piping bends (radius < 3d).
Intuitively, this does not seem right. Also I have been unable to find any references to the phenomenum on the internet.
Has anyone got any...
I am looking at wet natural gas piping system.
An expert has advised that hydrate crystals have a tendency to accumulate at piping bends (radius < 3d).
Intuitively, this does not seem right. Also I have been unable to find any references to the phenomenum on the internet.
Has anyone got any...
I want to calculate increase in pressure in empty vessel (volume is approx. 2m3) due to gas (methane) flow into the vessel at a known rate (approx. 6 standard m3 per minute).
Could a kind process engineer out there let me know how to do the calculation?
Thanks.
djwright
Thanks for helpful posts.
In our application we have used gas-sheilded process to weld 60ksi structural steel. Welding environment was offshore / windy but full protection and monitoring was provided.
Some "cracking" was reported. Various theories have been put forward (lack of...
Thanks for the responses.
I guess my original post wasn't very clear.
I have some 316L tubing already in place. So far (1 year in service) it looks OK.
I am currently planning to install more. I would prefer to use 316L if its fit for purpose and cheaper than the alternatives suggested...
I want to use 316L stainless steel hydraulic tubing on an offshore platform (field life approx. 10 years) offshore Ireland.
I am advised that 316L will corrode and that I must therefore paint it.
I don't want to paint because I believe it is not necessary in my application and for obvious cost...
Is flux cored arc welding a good process for site welding of structural steel?
Has there been any history of weld cracking associated with this process?
Thoughts and experiences would be appreciated.
Thanks for this.
Based on my investigations so far I believe that it is essential to ensure that overlay welding procedure provides hardness less than 22HRC / 248HV10 as per NACE MR-01-75.
I have contacted ITAG to establish the cause of the problem on Liverpool Bay and await a response.
djwright
Thanks for this.
It was the reported BHP failure(s) which had me worried.
The use of overlays is so common I assume that the BHP failure is specific to BHP rather than a generic problem.
In our sour service application, we have qualified overlay procedures in accordance with ASME IX and NACE...
