Going back to post #35 & #37, (page 4) that’s really is an impractical idea – pushing moist air thru a stack and expecting the moisture to drop out. Crunching some numbers, and a bit more thought.
I’m thinking I’ll only get about 60-70 lbs of tobacco in my freezer box:
Using 60# at 80% water weight = 48#water & 12#leaf. But I don’t want dry leaf yet (in the yellowing phase), say 20% moisture content is OK. So, 48# less 20%(12#) = 45.6# of water to be removed.
45.6# ÷ 8.34 #/gal = 5.47 gallons of water to remove over a 3 day period.
So, 5.47 gal x 128 oz/gallon ÷ 3(24hrs/day) = 9.7 oz per hour.
That’s over a cup of water per hour.
Then: The supposed air volume for flue-curing is ½ cfm per lbs of tobacco. For 60#, I need 30 cfm of air moving through the chamber. If I push this air through a 4” diameter stack, this figures 5.7 ft/sec velocity through the stack. No way this is going to drop out 9.7 oz of water, unless it is one-really-long stack.
Am now thinking, that if I want a recirculating air system, I am going to need a shell-and-tube heat exchanger, and a cooling system, or equivalent.