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Extraction Technologies for Medicinal and Aromatic ... - Capacity4Dev

Extraction Technologies for Medicinal and Aromatic ... - Capacity4Dev

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7 DISTILLATION TECHNOLOGY FOR ESSENTIAL OILS<br />

Considering the previously mentioned demerits of FDUs, designs<br />

of economical <strong>and</strong> improved units with capacities 500-2000 kg per<br />

batch are now being preferred (Figure 3). The units are fabricated with high<br />

quality mild stainless steel, keeping in view the plant materials to be distilled.<br />

The improved distillation unit consists of a cylindrical distillation tank<br />

fi tted on a square inbuilt boiler (cal<strong>and</strong>ria) having smoke pipes which reduces<br />

the heating time of the water, resulting in a high rate of steam generation<br />

<strong>and</strong> lower fuel consumption (20%-30%). Hot fl ue gasses of the furnace are<br />

led through the smoke tubes where they impart heat to the water, thus raising<br />

additional steam. The tank is fi tted on a specially designed furnace having<br />

fi re grate, fl ue ducts <strong>and</strong> fi re door <strong>for</strong> proper controlling of the fi ring <strong>and</strong><br />

draft. The furnace is connected to a chimney of optimum height to maximize<br />

the air draft <strong>and</strong> control the pollution by smoke in the workplace. A similarly<br />

designed stainless steel shell <strong>and</strong> tube-type condenser having higher condensation<br />

capacity are used <strong>for</strong> cooling the vapors. It prevents loss of oil<br />

due to improper condensation. The condensed oil-water mixture is then allowed<br />

to pass through a specially designed stainless steel oil separator. The<br />

separator has an inbuilt baffl e to maximize the retention time of the mixture,<br />

thereby resulting in no loss of oil with the outgoing water from the separator.<br />

The unit also has a chain pulley hoist system with a support structure that<br />

makes work easier <strong>and</strong> saves time during discharge of the distillation waste<br />

material from the tank. CIMAP has designed, fabricated <strong>and</strong> supplied these<br />

improved units to entrepreneurs <strong>and</strong> farmers in different parts of India.<br />

7.3.3 Direct Steam Distillation<br />

In direct steam distillation, plant material is distilled with steam<br />

generated outside the tank in a steam generator or boiler. As in water <strong>and</strong><br />

steam distillation, the plant material is supported on a per<strong>for</strong>ated grid above<br />

the steam inlet. As already noted, the steam in an FDU is at atmospheric<br />

pressure <strong>and</strong> hence its maximum temperature is 100° C. But, steam in a<br />

modern pressure boiler operating at, <strong>for</strong> example, 50 psi pressure will have<br />

a temperature correspondingly higher. Moreover, there is no limitation to the<br />

steam generation when an external boiler is used as a source of steam. The<br />

use of high-pressure steam in modern steam distillation units permits much<br />

more rapid <strong>and</strong> complete distillation of essential oils.<br />

Steam distillation is preferred when a lot of area is under cultivation<br />

<strong>and</strong> more than one unit is to be installed. Also, <strong>for</strong> distillation of high boiling<br />

oils <strong>and</strong> hardy materials such as roots <strong>and</strong> woods like s<strong>and</strong>alwood, cedar wood<br />

<strong>and</strong> nagarmotha, steam distillation is more efficient. Steam distillation also<br />

reduces the time required <strong>for</strong> the extraction of oils. A charge of Java citronella,<br />

which takes up to 5 h in an FDU, is processed within two to 3 h in a steam<br />

distillation still. In this method of distillation, steam is generated separately in<br />

a steam boiler <strong>and</strong> is passed through the distillation tank through a steam coil<br />

(Figure 4). The plant material is tightly packed above the per<strong>for</strong>ated grid. Steam,<br />

containing the oil vapor, is condensed in a tube condenser <strong>and</strong> is separated in<br />

120

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