Gents,
We're facing an issue with the centrifugal compressor as the production is declining and the flowrate to the compressor is much less now than originally designed for.
One solution to that is to construct a larger anti-surge line that would recycle -in our case- about 40% of the production so that the compressor's minimum flow is achieved.
My question is that; is the prescribed solution more economical (I'm sure there would be Capex for constructing the recycle line, the FCV, probably new larger PSV for the suction scrubber, and of course the energy loss) than purchasing a new smaller compressor that provide better performance with the current production, knowing that the compressor is required to compress about 150MMSCFD of light gas (mainly C1, MW of 17) from 25barg to 70barg?
Thanks for your feedback,
Cheers