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|Material:||Stainless Steel 304||Column Size:||DN100*1000-2000mm|
|Internals:||10-20 Sieve Tray Columns.||Reboiler:||50L-100L|
|Receiver Size&quantity:||20L*2 Or 30L*2||Floor Area:||Length*width*height=1000*800*2700-3500 (mm)|
flute distillation column,
multicomponent distillation column
10 mbar Vacuity Fractional Distillation Column for CBD / THC / Hemp oil
Feed liquid is admitted into still under high vacuum, immediately spread into a very thin film and forced quickly down the evaporation surface. Heated walls and high vacuum drive the more volatile components (distillate) to the external condenser as the less volatile components (residue) continue down the cylinder. The resulting fractions, thus separated, exit through individual discharge outlets. Depending on application, the desired product is either the distillate or the residue fraction. Small amounts of condensable low MW compounds collect in cold trap upstream of vacuum system. For high solvent loads, an optional external condenser may be installed immediately downstream of the still.
|Material||stainless steel 304|
|Temperature||Room temp~200/300 ℃(depend on the oil heater)|
|Internals||10-20 Sieve tray columns.|
|Condenser HTA||0.86 (m2)|
|Vacuity||MIN:10mbar(depend on the nature of material and vacuum pump&vacuum pump not included)|
|Floor area||length*width*height=1000*800*2700-3500 (mm)|
In industrial uses, sometimes a packing material is used in the Fractional Distillation Column instead of trays, especially when low pressure drops across the column are required, as when operating under vacuum. This packing material can either be random dumped packing (1-3" wide) such as Raschig rings or structured sheet metal. Typical manufacturers are Koch, Sulzer and other companies. Liquids tend to wet the surface of the packing and the vapors pass across this wetted surface, where mass transfer takes place. Unlike conventional tray distillation in which every tray represents a separate point of vapor liquid equilibrium the vapor liquid equilibrium curve in a packed column is continuous. However, when modeling packed columns it is useful to compute a number of "theoretical plates" to denote the separation efficiency of the packed column with respect to more traditional trays. Differently shaped packings have different surface areas and void space between packings. Both of these factors affect packing performance.
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