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Extraction Technologies For Medicinal And Aromatic Plants - Unido

Extraction Technologies For Medicinal And Aromatic Plants - Unido

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EXTRACTION TECHNOLOGIES FOR MEDICINAL AND AROMATIC PLANTS<br />

a tubular heat exchanger which is heated by steam. The temperature of the<br />

extract in the percolator is controlled by a steam solenoid valve through a<br />

temperature indicator controller. This sort of arrangement can be incorporated<br />

in single percolators or in a battery of percolators as needed.<br />

The percolators that are tall cylindrical towers must be housed<br />

in sheds of relatively great height. Tall towers are diffi cult to operate, especially<br />

when charging material and discharging the marc from the top and bottom<br />

manholes, which are time-consuming and labor-intensive procedures.<br />

Tall towers have been replaced by extractors of smaller height for which the<br />

H/D ratio is not more than 1.5.<br />

These extractors have perforated baskets in which the material to<br />

be extracted is charged. These perforated baskets, when loaded outside, can<br />

be inserted into the extractor with a chain pulley block and, after the extraction,<br />

they can be lifted out from the extractor for discharging the marc. Some extractors<br />

have an electrical hoist for the charging the material and discharging the<br />

marc, which makes the operation less labor-intensive, quick and effi cient.<br />

The other type of instrument for extraction of medicinal ingredients<br />

from plant material is the Soxhlet apparatus, which consists of an<br />

extractor, a distillation still, a tubular condenser for the distillation still, a tubular<br />

condenser for the recovery of solvent from the marc, a receiver for collecting<br />

the condensate from the condenser, and a solvent storage tank. The<br />

plant material is fed into the extractor, and solvent is added until it reaches<br />

the siphon point of the extractor. Then, the extract is siphoned out into the<br />

distillation still, which is heated with steam. The solvent vapors go to the<br />

distillation condenser, get condensed and return to the extractor. The level<br />

of the solvent in the extractor again rises to the siphon point and the extract<br />

is siphoned out into the distillation still. In this way, fresh solvent comes in<br />

contact with the plant material a number of times, until the plant material is<br />

completely extracted. The fi nal extract in the distillation still, which is rich in<br />

active principle, is concentrated and the solvent is recovered.<br />

1.2.2.3.3 Concentration<br />

The enriched extract from percolators or extractors, known as<br />

miscella, is fed into a wiped fi lm evaporator where it is concentrated under<br />

vacuum to produce a thick concentrated extract. The concentrated extract is<br />

further fed into a vacuum chamber dryer to produce a solid mass free from<br />

solvent. The solvent recovered from the wiped fi lm evaporator and vacuum<br />

chamber dryer is recycled back to the percolator or extractor for the next<br />

batch of plant material. The solid mass thus obtained is pulverized and used<br />

directly for the desired pharmaceutical formulations or further processed for<br />

isolation of its phytoconstituents.<br />

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