Todd

Thank you for the instruction.  

I would like to know what the potential yield of pure glycerin is if you did 
an acid - base transesterification - esterification of the WVO, then seperated 
the FAA and boiled off the methanol?  

I realize that the "coctail" is not pure glycerin.  Do you know what that % 
of 97% glycerin is of the original gal. of WVO.

I believe it was you who suggested in an earlier post that a thin film 
processor would do the job at a cost.  I assumed you were referring not only 
the 
cost of the equipment but also the expense of the electricity to operate the 
Processor.

I apologize for my inability to explain myself more clearly.

Again, thank you for all your help.  It's much appreciated.

Sincerely,
Dave Hannah


[Non-text portions of this message have been removed]




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