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...
Thank you for your reply.
Can you send me more details about the guidelines for
determine these air plant capacity?
Like per unit in the refinery, or per number of
utility stations?
Also if you have and can spare some guidelines for
instrument air and nitrogen.
Thank you very much.
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
