I’ve heard that the KDT-6 Dual stage can do about 4L/Hr (input).
I’m going to do the math for my own sake, not to argue with you! Please let me know if any of my numbers look funny…
Also do you have any tips on separating the terps from the residual solvent on the initial strip?
If I were able to process 4L Crude (input)/Hr then at a ~70% Yield on 2 passes I would be getting about 2.8Kg of 2nd pass distillate/hr.
Let’s say I have all of the diffusion/discharge/feeding pumps necessary to have it be mostly continuous and let’s account for 45min every 8hr (for easier maths sake) and let’s also say I’m operating 16hr per day. That means I have an actual operation time of 16-(0.75x2)=14.5Hr
14.5Hr x 2.8L 2nd pass output/Hr = 40L 2nd pass output/day
Now let’s say that we’re running our rotachrom with ~600g/run @20min/run
That’s 1.8kg (input)/Hr @ 80% yield = 1.44Kg output T-free per hour
Let’s say we did this for 12 days
12 days x (4L/Hr x 14.5Hr) = 696Kg input crude in 12 Days
12 days x (2.8kg output/hr x 14.5hr) = 487kg 2nd pass distillate output/12 Days
Now let’s say the rotachrom does 1.8Kg input/Hr at 15 hours per day (1hr for sample prep and other downtime)
1.8Kg x 15hr = 27Kg input per day
@80% yield = 21.6Kg T-free output per day
Now let’s run that for 12 days
27kg/day x 12 days = 324Kg Input distillate/12 days
324Kg @ 80% Yield = 259Kg T-free output/12 days
487Kg 2nd pass output/12 days - 324Kg input to rotachrom = 163Kg surplus
The only questions is will I have enough time to repolish my T-free to get that nice golden color at the end of the month.
The numbers I am asking for are representing 24Hr/day 24 Days/month model so they are really trueing to maximize the equipment.