Everest has already made many landmarks in offering the solutions to many complicated processes including CNSL.

Everest offers positive displacement vacuum pumps that are basically meant to handle NC load (within permissible limits as per the HEI standards) + saturated vapor load.

According to the invention Natural CNSL contains anacardic acid which is converted in to cardanol by decarboxylation process of anacardic acid. In this Process natural CNSL is heating under vacuum condition up to 170 to 180°C in which anacardic acid get converted into cardanol with release of CO2 and H2. Anacardic acid Contains carboxylic group which is eliminated by heating, this converted components is called cardanol,

After this cardanol is further sent for purification step in which cardanol is separated out from rest components as this process contains highly viscous components so normal distillation is not possible, that’s why Agitated thin film distillation (ATFD) is applied to complete the process.

In CNSL distillation, Cardanol is recovered at top of the column and at the bottom of column a tarry matter, high viscous residue remains called ‘Resorcinol’.

It has been found that there are certain difficulties of operation with regard to single-stage fractional distillation method, as long term exposure of CNSL to heating cause the CNSL self polymerised which affects the Product properties therefore distillation is carried out in short period of time.

When CNSL distillation is done at about 200°C to 240°C under reduced pressure of about 2 to 2.5 mm mercury in short possible time gives distillate containing cardanol and cardol and residue tarry material. To make the purity and color of cardanol of high level, firstly distilled cardanol is then subjected to a second distillation under the same identical conditions of temperature and pressure where the cardanol distils over at a temperature of 230°C to 235°C and other impurities remains which has high boiling point than Cardanol that is why cardanol extraction is high temperature sensitive process, if there is drop in vacuum then temperature will rise suddenly which cause the impurities to carry with distilled cardanol and will cause the discoloration of Cardanol. In practice it has been found that the preliminary decarboxylation of the oil is essential, since there will be excessive frothing, which renders the distillation procedure unproductive and uneconomical.

• Kettle Capacity:- 5000 litres
• Total Loading:- 3500 litres
• Main Product:- 1000 litres
• Total distilled:- 2390 litres
• Working Temperature: 170 -235 °C
• Pump Capacity: – 1670.800.250M3/Hr
• Loss %:- 3 – 4%
• Pre-condenser recovery: – 2930 litres
• Process Time:- 14Hrs 30 Min
• Average distil rate: 140-150 lt/hr

Observed Data During Process: