Hello,
We intend to compress H2S gas from 0.8 to 45 barg with a reciprocating compressor, 90% mol H2S, 3% water and 7% hydrocarbons.
The water are in the gas phase.
What are the options for the MOC for the parts in contact with the H2S gas stream? is SS316 suitable (e.g. the cylinders etc.) ...
Hello,
On the outlet line from the seal leg (the line is self draining, traced and insulated) we intend to install a valve,
it seems better to install it near the seal leg but it is inconvenient since it is at a high point with no space to operate or maintain,
on the other hand we can install it...
Hello,
A long (50 km) petroleum underground pipe is designed to have a flow metering station every 2 km.
How can I draw a P&ID to show one typical metering station which will be repeated 25 times ?
A simple sketch will be helpful.
regards
Hello,
when installing two 100% PSV's in parallel, one open and the second closed, what will be recommended
and good engineering practice from the mechanical point of view (reaction force in operation) and from
piping design as pressure drop (3% of set pressure in inlet piping):
to use 3-way...
Hello all,
A compressor with a total of 4 stages, the first two with a common motor and the last two stages also with a common separate motor. Can I use another stand by compressor with two stages to operate as the two first stages and if needed also to operate as the last stages?
Regards...
Hello,
In oeder to improve economics and enviromental aspects of a/m subject,
does a continuous treatment exists so there is no down time of the metal processing machine?
What are the main features of such a system? a process flow diagram or block diagram can be helpful.
Regards...
Hello,
According to API 521 a relief valve is not required in the case of tube rupture if the design pressure of the low side pressure is 10/13 of the high pressure design pressure.
For example: if the high pressure side design pressure is 26 barg we set the design pressure of the low side...
