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Distillation still bottoms, 85% moisture, discharge at a ph of 4.6-4.8. Can they be adjusted to a level that will allow them to be processed by a mild steel centrifuge and mild steel dryer.

I KNOW THIS IS VERY BASIC, BUT THE ANSWER ELUDES ME. IN COPYING FILES FROM WIN XPLORER TO C-D THE WRITE PROTECT ENABLES.I HAVE TRIPLE CHECKED THE FILES I AM COPYING AND THEY ARE NOT WRITE PROTECTED.

Need advice on eliminating siloxane from land gas recovery.

Will the vacuum created by condensing overhead vapors be sufficient to provide motivation through columns or is a vacuum pump required.

Would appreciate any tips on removal of dissolved CO2 from beer stream prior to distillation.

FEEDING A COOK TUBE 12"id x 450 FT. WITH A GROUND CORN WATER SLURRY OF 35% SOLIDS. FEED IS VIA A HYDRO THERMAL STEAM HEATER/MIXER.SLURRY FEED RATE IS 2000 LBS/MIN. STEAM TO H-T UNIT IS 120 LBS/MIN. OF 150PSIG.DELTA IS 40PSIG. NEED SUGGESTION FOR VAPOR SOLIDS SEPARATION ON DISCHARGE END.

On importing from another drawing, unable to manipulate text or treat the import as anything but single entity.

Would appreciate suggestion of stripper section design for ethanol/water/solids. Height is limiting, diameter is variable. Input 125,000 lbs/hour 8.38lb/gal beer. Output Corn solids>20mesh grind, 15,000 lbs/hr. Ethanol, 14,000 lbs/hr. Water, 96,000 lbs/hr.