Granulation, dry

The encapsulation of herbicides has received much attention. Encapsulated alachlor is a high volume herbicide product generally sold as a Hquid formulation, although a dry granule version is also available. The capsules, produced by interfacial polymeri2ation (11), are reported to be spherical with a diameter of 2—15 p.m (75). Two thiocarbamate herbicides, EPTC and vemolate [1929-77-7], were encapsulated by interfacial polymeri2ation because they are volatile compounds. When appHed in unencapsulated form, they must be incorporated in the soil within two hours in order to provide effective weed control. When appHed as a microencapsulated formulation, the rate of volatili2ation is lower and soil incorporation can be delayed 24 hours (76). 

If the feed flows countercurrent to the air, as is the case when drying granulated sugar, exhaust temperature does not respond to variations in product moisture. For these diyers, product moisture can better be regulated by controlhng its temperature at the point of discharge. Conveyor-type diyers are usually divided into a number of zones, each separately heated with recirculation of air which raises its wet-bulb temperature. Only the last two zones may require indexing of exhaust-air temperature as a function of AT... 

For successful tableting, a material must have suitable flow properties to allow it to be fed to the tableting machine. Wet or dry granulation is used to improve the flow properties of materials. In the case of wet granulation, agitative granulation techniques such as fluidized beds or mixer granulators as discussed above are often employed. 

The particular features of the nylons should also be taken into account in extrusion. Dry granules must be used unless a devolatilising extruder is employed. Because of the sharp melting point it is found appropriate to use a screw with a very short compression zone. Polymers of the lowest melt viscosity are to be avoided since they are difficult to handle. Provision should be made to initiate cooling immediately the extrudate leaves the die. 

Dried granules may be injection moulded, blow moulded and extruded without undue difficulty with melt temperatures of 220-260°C. The moulding shrinkage (0.003-0.004 cm/cm) is very low and a somewhat greater than normal draft may be required in deep draw moulds. 

The main purpose of pesticide formulation is to manufacture a product that has optimum biological efficiency, is convenient to use, and minimizes environmental impacts. The active ingredients are mixed with solvents, adjuvants (boosters), and fillers as necessary to achieve the desired formulation. The types of formulations include wettable powders, soluble concentrates, emulsion concentrates, oil-in-water emulsions, suspension concentrates, suspoemulsions, water-dispersible granules, dry granules, and controlled release, in which the active ingredient is released into the environment from a polymeric carrier, binder, absorbent, or encapsulant at a slow and effective rate. The formulation steps may generate air emissions, liquid effluents, and solid wastes. 

Polymorphs are different crystal forms of the same compound [55], They are usually prepared by crystallization of the drug from different solvents under diverse conditions. However, exposure to changes in temperature, pressure, relative humidity, and comminution which are encountered in processes such as drying, granulation, milling, and compression may also lead to polymorphic transformations. 

Flavoring agents proper are commonly volatile oils that have been dissolved in alcohol and sprayed onto the dried granules or have simply been adsorbed onto another excipient (e.g., talc). They are added immediately prior to compression to avoid loss through volatilization. In some cases they may even have some lubricating activity. If the oil normally contains ter-penes, a low terpene grade is better so as to avoid possible deterioration in taste due to terpene oxidation... 

Brown, R. L. Nature 191. No. 4787 (1961) 458. Minimum energy theorem for flow of dry granules through apertures. 

Hancock, B.C., Colvin, J.T., Mullarney, M.P., and Zinchuk, A.V., The relative densities of pharmaceutical powders, blends dry granulation, and immediate release tablets, Pharm. Technol., 4, 64, 2003. 

Within the pharmaceutical industry, granulation is a widely used process to prepare drug substance and excipient particles for compression. " There are wet and dry granulation procedures herein high shear wet grannlation, fluid bed granulation and roller compaction will be discussed. 

Figure 7.26 Compaction behavior of KBr powder and spray-dried granules of alumina and clay tile as a function of punch pressure. From J. S. Reed, Principles of Ceramics Processing, 2nd ed. Copyright 1995 by John Wiley Sons, Inc. This material is used by permission of John Wiley Sons, Inc.

Gereg and Capolla developed process parameters determined by a model laboratory bench scale Carver press, model C (Carver Inc. Savannah, Georgia, U.S.A.), which were translated to production scale compactor parameters (6). Their study provided a method to predict whether a material is suitable for roller compaction. Their study objectives were to characterize properties of the material to identify process parameters suitable to achieve the necessary particle size and density using the dry granulation process and then translate laboratory information to a production scale roller compactor. Actually, information developed from a Carver press was correlated and scaled-up to a production scale Fitzpatrick roller compactor. Model IR 520 (Fitzpatrick Co., Elmhurst, Illinois, U.S.A.) The compactor produced very similar powder granule characteristics as the Carver press. Various lactose materials, available as lactose monohydrate or spray dried lactose monohydrate, were used as the model compounds. Results indicated that a parametric correlation could be made between the laboratory bench Carver press and the production scale compactor, and that many process parameters can be transferred directly. 

Dry granulation is a process which consists of granulating a powder by compression, avoiding the wetting and drying steps. The advantages and drawbacks of this process were described by Sheth et al. [1]. The two methods used for dry granulation are compaction and double compression [2,3]. 

Two polymers were incorporated in the inert matrix system ethylcellulose and polyvinyl chloride. The processes used to prepare tablets containing such polymers often include direct compression [4-6], wet granulation [7,8], coating [9-11] and, rarely, dry granulation [12]. 

When using dry granulation, it is highly desirable to add a binder to the mixture in order to ensure an acceptable cohesion between particles. Therefore, in this present study, ethylcellulose was incorporated in two parts before precompression as a binder, and before the final compression as an independent variable in the experimental design. 

When compared with direct compression results, the dry granulation processes enhance the flow of the powder and decrease the variability of the AUC, the major response. Nevertheless, this variability and the variability of the drug dissolved at 8 h (T7) are greater than the fixed optimal values, particularly for the compaction processes. From the results it is seen that the wet granulation process gave a powder presenting an adequate or better result than the other processes ... 

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