Payment & Shipping Terms:
|Material:||Stainless Steel 304/S316L||Column Size:||DN50*800-1600mm|
|Distillation Column Type:||Packed Tower||Floor Area:||Length*width*height=1000*800*2700-3500 (mm)|
30L-50L Reboiler Distillation Column for CBD / THC / Hemp oil / Cannabissativa
Continuous distillation process.
Low operating pressures (100~10000Pa ,100Pa=1mbar).
Short residence time.
High evaporation rates.
Processing of high-boiling, high-viscosity or crystallizing products is possible.
Can be used as a reboiler for column.
Low fouling on evaporator wall.
|Material||stainless steel 304/S316L|
Distillation column type
|Temperature||Room temp~200/300 ℃(depend on the oil heater)|
|Condenser HTA||1.5 (m2)|
|Vacuity||MIN:1mbar(depend on the nature of material and vacuum pump&vacuum pump not included)|
|Floor area||length*width*height=1000*800*2700-3500 (mm)|
Basic Operation and Terminology
The liquid mixture that is to be processed is known as the feed and this is introduced usually somewhere near the middle of the Distillation column to a tray known as the feed tray. The feed tray divides the column into a top (enriching or rectification) section and a bottom (stripping) section. The feed flows down the column where it is collected at the bottom in the reboiler.
Bottom sectionHeat is supplied to the reboiler to generate vapour. The source of heat input can be any suitable fluid, although in most chemical plants this is normally steam. In refineries, the heating source may be the output streams of other columns. The vapour raised in the reboiler is re-introduced into the unit at the bottom of the column. The liquid removed from the reboiler is known as the bottoms product or simply, bottoms.
Top sectionThe vapour moves up the column, and as it exits the top of the unit, it is cooled by a condenser. The condensed liquid is stored in a holding vessel known as the reflux drum. Some of this liquid is recycled back to the top of the column and this is called the reflux. The condensed liquid that is removed from the system is known as the distillate or top product.
Thus, there are internal flows of vapour and liquid within the Distillation column as well as external flows of feeds and product streams, into and out of the Distillation column.
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