Experimental Design: Extruded Granule Formulation Development
Introduction: The development of wettable powder (WP) formulation technology marked the advent of modern agricultural delivery systems in which both liquid and solid technicals could be delivered to a target organism dispersed in water at the time of application. Prior to this time, agricultural products were applied primarily as "dust" formulations; that is, active ingredients were reduced in concentration in the presence of clay diluents to a target assay, processed to a small particle size using high impact equipment, and broadcast as dry powders.
The adverse implications of the above dust applications lie in the areas of uniform distribution of active ingredient and unnecessary exposure to toxic chemicals. Wettable powders were the first delivery system developed for agricultural chemicals to begin to address these concerns by means of formulation dispersion in water at the time of application. The intent of the technology was first to improve the uniform distribution of active ingredient through the development of specific molecules which improved the wetting of the powders into water ("wetting agents") and the physical suspension of the powders once they had been wetted into water ("dispersants"). Inherent with the development of the wettable powder was reduced applicator exposure to the active ingredient once the formulation had been added to water.
However, the applicator was still exposed to the active ingredient at the time the wettable powder was added to water.
Delivery Systems - Granulation: It was therefore desirable to develop "delivery systems" through both packaging and reformulation of WP that did not adversely affect either physical or chemical performance. Efforts to address applicator exposure through packaging involved development of a Unit Dose Delivery System. With this technology, a predetermined weight of WP is heat sealed inside a water-soluble pouch (usually composed of polyvinyl alcohol or similar polymer) and added to the spray tank at the time of application. However, there are limitations to the technology:
In terms of reformulation, controlled addition of water to the processed wettable powder was found to form agglomerates that minimized exposure to airborne dust particles. In this technology, referred to as "Pan Granulation" the powder is fed into a rotating pan while at the same time water is misted onto the powder. The combination of rotation plus water causes agglomerated powder spheres, of variable sizes, to form. The newly formed granules literally roll off the pan as they are displaced with fresh powder to be agglomerated. The resultant granules are then directed toward a fluidized bed dryer where they are dried to predetermined residual moisture by a combination of temperature and residence time in the dryer. The controlled moisture levels in the granule introduce structural integrity while at the same time allowing the granule to disintegrate upon addition to the spray tank. Finished granules are screened to pre-select commercially particle size distribution.
However, limitations to the technology, as a delivery system for Wettable powders, were identified which came to be associated with granule hardness and a tradeoff between disintegration in the spray tank and dust formation upon handling. The harder the granule, the less airborne dust that formed upon handling, but the longer the granule took to disintegrate in water.
Efforts to balance granule dustiness and disintegration were addressed through inert selection and concentration: increased levels of wetting agent/dispersant and incorporation of disintegrants were identified which facilitated the efficient movement of water throughout the granule. Granules processed using Pan Granulation demonstrated variable hardness depending upon technical density, crystalline structure and water solubility; efforts to control granule integrity revolved around incorporation of a densification step prior to granulation and modification of the binder system at the time of agglomeration. Concerns were also expressed with the additional rework costs associated with pan agglomeration since final product is specified as to acceptable granule size distribution. Granules outside these limits had to be reduced in particle size (hammermilled) and mixed with virgin Wettable powder product at a rate that did not then negatively impact granule performance.
In contrast to Pan Granulation, extrusion eliminates the variability of granule integrity associated with technical density and crystalline structure. In this technology, Wettable powders are densified with water in a kneader to the consistency of dough which is key to granule performance prior to extrusion. Too little water and the final granule integrity is affected to the point that dust may form with abrasion; excess water and the granules form stable agglomerates after being extruded which may impact disintegration.
Granule disintegration is a function of choice/concentration of formulation excipients, extrusion screen opening diameter, and surface area/porosity of the granule 'noodle' processed. The first allows for the efficient transport of water throughout the granule. The latter two dictate the granule surface area and the depth to which the water must travel during the disintegration process.
As with Pan Granulation, finished granules are dried to predetermined residual moisture and screened to an acceptable particle size distribution. Also, granules outside this particle size range must be reworked into the initial feedstock in such a manner as to not adversely impact finished granule performance.
Powder and Granule Basics : The basic WP and Extruded Granule formulation contains the following components:
Technical: As with the wettable powder formulations, extruded granule formulations can accommodate both liquid and solid technicals; however, their requirements in terms of diluent and processing are vastly different. The upper concentration limit of solid technicals is related to the melting point of the technical and the heat generated during processing: once the technical begins to be affected by the processing equipment (usually manifesting itself as thermoplastic), you have reached the upper formulation concentration. As a general rule, the higher the melting point of the technical, the higher the concentration at which it can be formulated. Also, processing the formulation using equipment that generates less heat should allow the formulator to increase the product active ingredient concentration.
With liquid technicals, the upper concentration limit is dictated by the amount of diluent powder necessary to isolate the individual liquid droplets. This quantity is a function of the particle size of the diluent: the smaller the particle size, the lower % (w/w) of the diluent that is required to encircle the liquid. "Impregnating a WP" is a term often used to describe the dispersion of a liquid technical into a diluent carrier; however, in many cases this is a misnomer since the liquid never enters the carrier cavities. Rather, the liquid can be viewed under the microscope as liquid spheres surrounded by diluent particles. The exceptions, technicals that can be impregnated, are those which will "wet" onto the diluent surface. Basically, the former technicals can be described as hydrophobic (water insoluble) in character and the latter as hydrophilic (water-soluble).
The water solubility of a technical and the impurities present on its surface are extremely critical to extruded granule disintegration. Hydrophobic technical surfaces require additional concentrations of wetting agent in order to facilitate the movement of water through the compacted granule.
Wetting agent: The wetting agent functions at the water/granule solid interface and aids in the incorporation of water throughout the compacted granule at the time of application. Wetting agents are surfactants, both nonionic and anionic, which orient their water soluble "end" into the water phase and their oil soluble "end" at the organic technical surface; thus serving to reduce the surface tension between the solid surface and water surface. Gravitational forces then allow the powder that is formed during the disintegration process to fall away from the granule surface and expose 'fresh' surface to be wetted. The rate at which the wetting agent aids in the transfer of water into the granule dictates its efficiency: the faster water is incorporated into the extruded granule, the more efficient the wetting agent.
Since a wetting agent functions mainly to disintegrate the extruded granule upon addition to water, its % (w/w) requirement in the formulation is dependent upon the water solubility/dispersibility of the technical and other formulation excipients. Traditionally, to more efficiently distribute the wetting agent into the WP formulation, spray-dried mixtures of wetting agent and dispersant have been developed and are commercially available. However, since a proprietary blend of wetting agent and dispersant is processed at established ratios, it is possible in this case to add an excess of dispersant in order to meet the (generally higher) wetting agent requirement of a hydrophobic technical during extruded granule development. This would unnecessarily increase formulation costs. With extruded granule formulations, fine particle size powders are the preferred wetting agent physical forms since this allows for its optimum concentration and efficient distribution throughout the wettable powder formulation prior to granulation.
Dispersant: Once the powder or granule has been added to the water phase (with the aid of the wetting agent), the dispersant now functions to isolate the individual particles and maintain them in suspension upon agitation. Dispersants useful in powder and granulated products are, for the most part, anionic surfactants which function at the water/particle interface and, by means of surface charge (electrostatic stabilization), prevent the individual particles from forming stable agglomerates.
Dispersant performance is affected by:
Diluent: The role of the clay or silica diluent, whether the technical is solid or liquid, is to reduce the active ingredient assay to a targeted concentration and to isolate the individual organic particles. This isolation serves two purposes:
However, with extruded granules, the diluent serves an additional function: it aids in granule disintegration. Therefore, as the extruded granule active ingredient concentration increases, the choice/concentration of the selected wetting agent becomes increasingly more critical to formulation performance upon application.
In general, the smaller the particle size of the diluent the higher the concentration of a technical that can be formulated. However, with reduced diluent particle size comes reduced formulation bulk density, which may impact commercial packaging and delivery requirement. When considering reduction of the diluent particle size to improve formulation physical suspension upon dilution, it must also be determined whether for wettable powders the same weight of formulated product will still fit into the current commercial container and whether the same volume unit dose applicators (scoops) are still appropriate. Small particle size diluent may also raise the wetting agent requirement in extruded granule formulations, especially with hydrophobic technical surfaces, due to increased surface area and reduction of 'channels' for water penetration throughout the granule.
With liquid technicals, in order to facilitate dispersion in water, it is desirable that the silica be hydrophilic. Although higher concentrations of organic liquid technical active ingredients (through true impregnation) can be formulated using hydrophobic silicas, it is extremely difficult to wet and disperse these formulated powders into water without addition of high concentrations of wetting agent.
Isolation of the individual technical particles is extremely important with those low melting technicals that are solid under normal storage conditions but are melted and processed as liquids. Once processed as wettable powder, the liquid technicals will revert to their preferred physical state, as solids, upon storage. This change in physical states will significantly affect physical performance at the time of application. The wettable powder, which at the time of production was free-flowing and readily dispersed in water to its primary particle size, may have formed physically stable agglomerates upon aging that will adversely affect flowability and physical suspension upon dilution.
Other excipients may be added to the formulation to address concerns associated with chemical stability, odor, surface adhesion, etc. For liquid and low melting point technicals, the issues related to formulation disintegration and suspension performance at higher technical concentrations would likely be exacerbated by conditions encountered in the extrusion process.
Wettable Powder (WP) and Water-Dispersible Granule (WG) Development: To develop a wettable powder involves a series of steps:
Establishment of performance criteria: It is important to establish up front how the formulation is expected to perform since this may dictate choice/concentration of inerts.
Selection of formulation inerts: Formulation inerts should be selected on a cost/performance basis: if you don't get the performance, then it doesn't matter what the cost. Where possible, formula
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