I need some advice for the following proposed scenario:
HP fuel gas of 40-55bar is sent to a conditioning skid consisting of coalescer, heater and pressure reduction station.
There is a concern that in case of rupture/ puncture in the system (equipment or piping) the resulting released gas...
We are completing the design for a compressing unit;
the fluid is sour gas with about 5% H2S;
We have been chosen screw compressors for our application; small capacity (1000m3/h of gas) at 9barg discharge.
Vendor is proposing double seals with fuel gas in the first seal chamber as purge gas and...
Hello everybody,
Can anybody give me some guidelines or point me to some documentation in order to be able to establish the necessary quantity of utility air/inert air/ nitrogen for a refinery of about 75,000bbl crude/day?
Thanks
Lori
