Dear sirs,
I'm presently working on a new installation in Africa dedicated to treat (de-oiling) the process water coming from the oil production.
After having been treated (in order to reach a residual 15 ppm oil concentration) this water is directly discarded into the sea (maximum water...
Hi sirs,
I'm trying to find some data about the corrosion rate (expressed in micrometer by year) for carbon steel pipelines in a natural gas plant (gas saturated in water at 80°C). Where can I found this data ? Does everyone have this data ?
Hi everybody !
I hope you're all fine. I'm trying to find some data about the corrosion rate (expressed in micrometer by year) for carbon steel pipelines in a natural gas plant (gas saturated in water at 80°C). Where can I found this data ? Maybe somebody has it ?
Thanks a lot.
Silverstone
Dear all,
I have a 'fast to answer' question related to PHAST (DNV software).
In order to simulate the line rupture of an infinite length gas pipeline, we used PHAST with the 3 following main settings (values are given for information but are not important for answer):
- Type of vessel ...
One of our customer company bought a glass reinforced plastic tank and want to use it as a oil/water storage capacity. BSW is about 95% (95 %vol in water and 5 %vol in oil). Do you know if this kind of material is convenient for a such application ?
Moreover, i heard that this material can lead...
One of our customer company bought a glass reinforced plastic tank and want to use it as a oil/water storage capacity. BSW is about 95% (95 %vol in water and 5 %vol in oil). Do you know if this kind of material is really recommended for a such application ?
Moreover, i heard that this material...
Dear sirs,
I'm trying to establish a model computing temperature profiles (as function of distance and time)reached by materials during a blowdown.
Is there some previous references and/or web-links which could help me in this task ?
Best regards,
I've to design an Emergency Depressurization System (blowdown valve + orifice + tubing) for a methane tank (80 bar a. at 35°C). A study seems to show that very low temperatures can be reached by the tubing steel (from -40°C to -100°C).
I want to use some low temperature resisting materials but...
Hi everybody,
I have to design a slug catcher device to protect a screw compressor.
These compressors being able to work even if gas is mist containing, I'm interested by the cheapest solution : using a 16" pipe as slug catcher. To design it i need to know the volume of slugs wich could occur...
