Extraction Technologies for Medicinal and Aromatic ... - Capacity4Dev
Extraction Technologies for Medicinal and Aromatic ... - Capacity4Dev Extraction Technologies for Medicinal and Aromatic ... - Capacity4Dev
8 MICRODISTILLATION,THERMOMICRODISTILLATION AND MOLECULAR DISTILLATION TECHNIQUES Table 1: Relative effi ciencies of common heating devices Appliance Temperature, °C Rating, W Time Energy used, kWh Energy cost, US$ Electric oven 177 2000 1 h 2 0.17 Convection oven 163 1853 45 min 1.39 0.12 Gas oven 177 36 1 h 3.57 0.07 Microwave oven High 1440 15 min 0.36 0.03 A B Figure 1: Mint gland: (A) before and (B) after microwave irradiation (Microphotographs courtesy of Radient Technologies Inc.) It is evident then that the main resistance to solid-liquid mass transfer, the transport of the solute through cell membrane, is eliminated because of the rupture of the cells. Besides cell breakage, the other advantages of microwave heating are: 1. Improved “existing” products 2. Increased marker recovery 3. Increased purity of the extract 4. Reduced heat degradation 5. Reduced processing costs 6. Signifi cantly faster extraction 7. Much lower energy usage 8. Much lower (order of magnitude) solvent usage 9. Potential for “new” products 134
EXTRACTION TECHNOLOGIES FOR MEDICINAL AND AROMATIC PLANTS 8.3.3.3 Literature on MAE Some interesting results on MAE have recently been published. For example, the extraction of vanillin from V. planifolia pods using MAE and ultrasound-assisted extraction has been described. Using absolute ethanol as the solvent at room temperature, the yield of vanillin was 1.25 wt% at each of 3 conventional extractions performed over 24 h. Using ultrasound-assisted extraction, the yield was 0.99 wt%, while it was 1.86 wt% using MAE. These investigations clearly showed that vanillin extraction by MAE is superior to other techniques in terms of yield, purity of vanillin, and the time taken to extract the same percentage of the vanillin from the pods. The extraction of vanillin and p-hydroxy benzaldehyde (PHB) from vanilla beans using MAE has also been studied: MAE was superior to the conventional, official method of extraction in Mexico, which involves maceration of the beans with ethanol for 12 h. Specifically, extraction time decreased 62-fold and vanillin and PHB concentrations increased between 40% and 50% with respect to the Mexican extraction method. This study also showed that extraction of commercial samples was superior to extraction of dried and lyophilized beans. This observation illustrates the role played by moisture in aiding extraction, as discussed in Section 8.3.3.2. Several other investigations have shown that MAE has gained acceptance as a mild and controllable processing tool. MAE is a simple, rapid and low-solvent-consuming process. 8.3.3.4 Industrial-scale MAE As mentioned earlier, microwave radiation decays exponentially inside a solid matrix. This aspect must be carefully weighed while designing industrial-scale MAE. The major requirements that must be met are: 1. Free distribution of particles allows uniform heating of all the particles in the solid bed. This criterion also enhances the extent and probability of proximity of the substrate to the wall of the sample holder where the microwave exposure is highest. Most comminuted samples of MAPs which are used for commercial extraction are not of the same shape and size. Therefore, there is a strong tendency to “segregate”, which must be curbed by regular renewal of the layer. 2. Thin and uniform spreading of the substrate layers. This permits complete and uniform penetration of microwave radiation even at large water contents. 3. Low depth of the layers. Since microwaves have low penetration depth (~1.5 cm in H 2 O at 2.45 GHz), the layers should be
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EXTRACTION TECHNOLOGIES FOR MEDICINAL AND AROMATIC PLANTS<br />
8.3.3.3 Literature on MAE<br />
Some interesting results on MAE have recently been published.<br />
For example, the extraction of vanillin from V. planifolia pods using MAE <strong>and</strong><br />
ultrasound-assisted extraction has been described. Using absolute ethanol<br />
as the solvent at room temperature, the yield of vanillin was 1.25 wt% at each<br />
of 3 conventional extractions per<strong>for</strong>med over 24 h. Using ultrasound-assisted<br />
extraction, the yield was 0.99 wt%, while it was 1.86 wt% using MAE. These investigations<br />
clearly showed that vanillin extraction by MAE is superior to other<br />
techniques in terms of yield, purity of vanillin, <strong>and</strong> the time taken to extract<br />
the same percentage of the vanillin from the pods. The extraction of vanillin<br />
<strong>and</strong> p-hydroxy benzaldehyde (PHB) from vanilla beans using MAE has also<br />
been studied: MAE was superior to the conventional, official method of extraction<br />
in Mexico, which involves maceration of the beans with ethanol <strong>for</strong> 12 h.<br />
Specifically, extraction time decreased 62-fold <strong>and</strong> vanillin <strong>and</strong> PHB concentrations<br />
increased between 40% <strong>and</strong> 50% with respect to the Mexican extraction<br />
method. This study also showed that extraction of commercial samples was<br />
superior to extraction of dried <strong>and</strong> lyophilized beans. This observation illustrates<br />
the role played by moisture in aiding extraction, as discussed in Section<br />
8.3.3.2. Several other investigations have shown that MAE has gained<br />
acceptance as a mild <strong>and</strong> controllable processing tool. MAE is a simple, rapid<br />
<strong>and</strong> low-solvent-consuming process.<br />
8.3.3.4 Industrial-scale MAE<br />
As mentioned earlier, microwave radiation decays exponentially<br />
inside a solid matrix. This aspect must be carefully weighed while designing<br />
industrial-scale MAE. The major requirements that must be met are:<br />
1. Free distribution of particles allows uni<strong>for</strong>m heating of all the<br />
particles in the solid bed. This criterion also enhances the<br />
extent <strong>and</strong> probability of proximity of the substrate to the wall<br />
of the sample holder where the microwave exposure is highest.<br />
Most comminuted samples of MAPs which are used <strong>for</strong><br />
commercial extraction are not of the same shape <strong>and</strong> size.<br />
There<strong>for</strong>e, there is a strong tendency to “segregate”, which<br />
must be curbed by regular renewal of the layer.<br />
2. Thin <strong>and</strong> uni<strong>for</strong>m spreading of the substrate layers. This permits<br />
complete <strong>and</strong> uni<strong>for</strong>m penetration of microwave radiation<br />
even at large water contents.<br />
3. Low depth of the layers. Since microwaves have low penetration<br />
depth (~1.5 cm in H 2 O at 2.45 GHz), the layers should be<br />