Recent content by wms

You could consider a recirculating system, being fed in excess of 90TPH, and reclaiming at 90TPH.

Mycom is the way to go. However, unless you can sell your product for $ 10/Ton or more you will not be able to justify the expense of so small a plant. What is the purity of the CO2 stream, and source?

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.

BradStone Touched on the best method of avoiding your impending catastrophe. Nitrogen or other inert shielding also some sort of mixer mounted strainer would be a good idea. Along with your God-Given common sense you will find some reference in NFPA 36 or 26 with regard to working...

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.

Ethanol industry sop is vapor phase w/ pressure swing. Also regeneration via etoh vapor.

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

Thanks for the reply. We have to drop the CO2 out prior to the vacuum distillation as it causes beer stone to plate out in distillation.

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.

Thanks TIGREK, but that didn't do it.

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

Do you mean the acidulation process?

US Dept of EPA has a tank program, "TANKS 3.1" Also determine if a floating roof is required. Vapor pressure of 200 proof is 1.22 psia. 190 proof is 1.16 psia