Extraction Technologies for Medicinal and Aromatic ... - Capacity4Dev
Extraction Technologies for Medicinal and Aromatic ... - Capacity4Dev Extraction Technologies for Medicinal and Aromatic ... - Capacity4Dev
3 MACERATION, PERCOLATION AND INFUSION TECHNIQUES FOR THE EXTRACTION OF MEDICINAL AND AROMATIC PLANTS During maceration of organized drugs, the marc is pressed because a considerable proportion of liquid adheres to it and cannot otherwise be separated. Moreover, the volume is not adjusted because a variable amount of liquid containing soluble matter is left in the marc. If the volume is adjusted, a weak product will result. Omitting adjustment, the volume of liquid expressed infl uences the product yield and the percentage of soluble matter, regardless of the effi ciency with which the marc is pressed in a hand press, screw press or hydraulic press; the strength of the product is not affected. Preparations made by this processes include vinegar of squill (British Pharmaceutical Codex, BPC), oxymel of squill (BPC), tincture of orange (Indian Pharmacopoeia, IP), tincture of capsicum (BPC), compound tincture of gentian, tincture of lemon, and tincture of squill (BPC). In maceration of unorganized drugs, the marc is not pressed because the desirable material is mostly dissolved and the remaining marc is gummy and slimy. Thus, it is neither practicable nor necessary to press it. Moreover, the volume is adjusted because the clear upper layer is easily separated by fi ltration from the lower layer. The solution contains practically all the soluble matter of the drug; the small amount adherent to the gummy matter is recovered when the marc is washed by menstruum in the fi lter. Therefore, adjustment of volume leads to uniformity. Preparations made by this process include compound tincture of benzoin, tincture of myrrh (BPC), and tincture of tolu (BPC). 3.5.3 Modifications to the General Processes of Maceration Repeated maceration may be more effi cient than a single maceration process, as described earlier, because an appreciable amount of active principle may be left behind in the fi rst pressing of the marc. Double maceration is used when the active constituents are particularly valuable and also when the concentrated infusions contain volatile oil. Where the marc cannot be pressed, a process of triple maceration is sometimes employed. The total volume of solvent used is, however, large and the second and third macerates are usually mixed and evaporated before being added to the fi rst macerate. 3.5.4 Large-scale Extraction Procedures For large-scale, industrial extraction, certain modifications are warranted. When the extraction vessel contains a small amount of solvent (500-1000 ml), occasional shaking is no problem. But, for industrial work where a large amount of solvent and huge vessels are involved, shaking the vessels is difficult. Obviously, there are alternative methods of agitation that are just as effective and much simpler to put into practice. In addition, economics become increasingly important and one of the most important objectives is to improve the efficiency of extraction so that less solvent is needed 72
EXTRACTION TECHNOLOGIES FOR MEDICINAL AND AROMATIC PLANTS and evaporation requirements for concentrated products are reduced. Reducing the cost of evaporation has the further advantage of minimizing the heat damage to thermolabile constituents. Some of the modified maceration procedures used for large-scale extraction are described in the next paragraphs. 3.5.4.1 Circulatory Extraction The effi ciency of extraction in a maceration process can be improved by arranging the solvent to be continuously circulated through the drug, as indicated in the Figure 1. Solvent is pumped from the bottom of the vessel (through an outlet) and is distributed by spray nozzles over the surface of the drug. The movement of the solvent reduces boundary layers and the uniform distribution minimizes local concentration in a shorter time. 3.5.4.2 Multistage Extraction Figure 1: Circulatory extraction In the normal maceration process, extraction is incomplete, since mass transfer ceases when equilibrium is reached. This problem can be overcome using a multistage process. The equipment needed for this method is a vessel for the crude drug, a circulating pump, spray distributors and a number of tanks to receive the extracted solution. The extractor and tanks are connected with piping and valves as shown in Figure 2, so that any of the tanks may be connected to the extractor for transfer of the solution. Each batch of drug is treated several times with solvent and, once a cycle is in process, the receivers contain solution with the strongest in receiver 1 and the weakest in receiver 3. 73
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EXTRACTION TECHNOLOGIES FOR MEDICINAL AND AROMATIC PLANTS<br />
<strong>and</strong> evaporation requirements <strong>for</strong> concentrated products are reduced. Reducing<br />
the cost of evaporation has the further advantage of minimizing the heat<br />
damage to thermolabile constituents. Some of the modified maceration procedures<br />
used <strong>for</strong> large-scale extraction are described in the next paragraphs.<br />
3.5.4.1 Circulatory <strong>Extraction</strong><br />
The effi ciency of extraction in a maceration process can be<br />
improved by arranging the solvent to be continuously circulated through the<br />
drug, as indicated in the Figure 1. Solvent is pumped from the bottom of the<br />
vessel (through an outlet) <strong>and</strong> is distributed by spray nozzles over the surface<br />
of the drug. The movement of the solvent reduces boundary layers <strong>and</strong><br />
the uni<strong>for</strong>m distribution minimizes local concentration in a shorter time.<br />
3.5.4.2 Multistage <strong>Extraction</strong><br />
Figure 1: Circulatory extraction<br />
In the normal maceration process, extraction is incomplete,<br />
since mass transfer ceases when equilibrium is reached. This problem can<br />
be overcome using a multistage process. The equipment needed <strong>for</strong> this<br />
method is a vessel <strong>for</strong> the crude drug, a circulating pump, spray distributors<br />
<strong>and</strong> a number of tanks to receive the extracted solution. The extractor <strong>and</strong><br />
tanks are connected with piping <strong>and</strong> valves as shown in Figure 2, so that any<br />
of the tanks may be connected to the extractor <strong>for</strong> transfer of the solution.<br />
Each batch of drug is treated several times with solvent <strong>and</strong>, once a cycle<br />
is in process, the receivers contain solution with the strongest in receiver 1<br />
<strong>and</strong> the weakest in receiver 3.<br />
73