What Mr. GK Sharma has replied is vey correct.
1. Gradually increase the Grinding pressure to the maximum design level.2. Nitorgen Presure of accumulator also to be increased as per the Mill supplier guide line. 3. Gradually increae the water spray on the Mill table from 1 Cubic Meter to 3 Cubic meter.
4. Reduction of Mill table speed upto 10% will help Pet coke to sustain on the table. 5. Reduce Coal Mill fan speed by 10 to 12%. 6. To maintain the Pet coke residue 1.5 to 2% on 90 Micron sieve, it almost 40 to 50% Production loss is oberved and subsequently
power consumption also will increase. Hard Grove Index (HGI) is less than 38 will further reduce the production. Damring height may reduce to minimum level. I think, Mill optimization can be done on the base of trial. Mill outlet temperature also can increase
up to 75 to 78 C, it will help to reduce the Mill main drive load.
As per my experience in Pfeffier Mill, Grinding Pressure may increased up to 150 Bar, and accumulator pressure can increase up to 65 to 70 Bar. Mill table speed 92% and Mill Fan speed is 85 to 88% 35 tph capacity Mill production fall down to 20 to 22 tph
and Product residue is 1.5% on 90 Micro sieve.