Hi toothless,
I respectfully disagree that using the isentropic efficiency of the compressor alone would be sufficient to optimise the compressor wash.
Knowing only the isentropic efficiency is not sufficient as this efficiency can decrease if the load conditions are such that the compressor operates at a low efficiency part of the characteristic. We need to compare it with the expected isentropic efficiency at any operating condition.
The loss in isentropic efficiency of the compressor is quite small due to fouling. It is the loss in flow capacity that is significant. For example, after about 500 hours of operation after a compressor wash, the isentropic efficiency decreases by about 1% where as flow capacity decreases by about 3%. Furthermore, we need the change in both flow and efficiency characteristic due to fouling before we can determine the loss in power and increased heat rate due to compressor flowing before we can properly optimise the wash frequency. Other engine faults such as hot end damage will also affect the wash frequency. Also, as stated above, we need to know the downtime for wash, unit price (i.e. revenue), fuel cost, engine load, any standby availability to determine the wash frequency so that the lost revenue due to washing is minimised.
Your comments on this will be very much appreciated thanks.
Regards,
gtsim