RESUMEN
The feed frame system is one of the key elements of a rotary tablet press. The powder in the funnel flows through the feed frame system, which ensures a uniform powder flow to the die disc. The objective of the present study was to investigate the effect of different feed frame designs of a production-scale rotary tablet press on the residence time distribution of two microcrystalline cellulose blends, one of them serving as a tracer blend and the other serving as a filling material. With these powder blends, the effect of a reduction of the filling volume of a three chamber feed frame on the powder residence time was investigated. It was shown, that the volume reduction of the three chamber feed frame equipped with three modified large hub wheels led to a decrease of the powder residence time as well as to low intermixing of the powder particles. Furthermore, the residence time distribution within the three chamber feed frame was compared to that within a single chamber cone-shaped feed frame. Both feed frame designs had a similar filling volume but different powder paths through the respective feed frame chambers. The results showed that the single chamber feed frame led to a narrower distribution of the powder residence time and a lower intermixing than the three chamber feed frame. An interesting output of the study was that the variation of the feed frame design had a more pronounced effect on the powder behavior than the variation of the filling volume.
Asunto(s)
Polvos/química , Tecnología Farmacéutica , Celulosa/química , Comprimidos/química , Factores de TiempoRESUMEN
The present study focused on the effect of different feed frame components on the residence time distribution of a three-chamber feed frame system (Fill-O-Matic). A production-scale rotary tablet press was used to simulate the industrial manufacture of tablets. The powder residence time distribution was used to characterize the powder behavior in the Fill-O-Matic. Therefore, two powder blends based on microcrystalline cellulose, one of them serving as a plain powder blend (MCC blend) and the other blend (tracer blend) spray colored with an indigo carmine solution by a fluid bed granulator, were used. With these powder blends, the effect of the reduction of the Fill-O-Matic volume with a perspex disc on the residence time distribution was compared with the standard configuration of the Fill-O-Matic. Furthermore, the filling wheel design with regard to the rod shape and different gap size configurations between the feed frame and the die disc were investigated. Interestingly, the reduction of the feed frame volume led to a remarkable decrease of the mean residence time and the mean centered variance. Moreover, the results of the filling wheel design showed that the rod shape of the filling wheels had a high influence on the intermixing of the powder particles in the filling chamber, whereas the corresponding tablet weights and their relative standard deviation were not affected. The gap size between the feed frame and the die disc had low influence on the residence time distribution but an effect on the tablet weights and their standard deviation.
Asunto(s)
Celulosa/química , Composición de Medicamentos/métodos , Excipientes/química , Tecnología Farmacéutica/métodos , Química Farmacéutica/métodos , Polvos , Comprimidos , Factores de TiempoRESUMEN
This study focuses on the behavior of powder particles in a rotary tablet press with special focus on the feed frame system. To obtain a better knowledge of the continuous manufacturing of tablets, the experimental setup was carried out with a production scale rotary tablet press. The behavior of the powder particles at different flow rates through the tablet press, residual moisture contents, particle sizes, and amounts of tracer was investigated. The residence time distribution was evaluated using the tracer indigo carmine, which was sprayed onto microcrystalline cellulose particle as solution with fluidized bed spray granulator to obtain a tracer blend. The residence time distribution was increased by increasing the amount of tracer blend, and a transition from a plain MCC blend to the tracer blend with regard to continuous manufacturing was shown. Furthermore, it was found that an increase in the flow rates of the powder particles through the tablet press led to a decrease of the residence time distribution (Et). The variation of the flow rate had no influence on the mechanically applied strain at high throughputs, which was confirmed by a constant number of paddle passes (Npp). At the lowest flow rate, the Npp appears to be higher than the constant Npp values at higher flow rates. The residual moisture content did not shown any significant influence on the residence time distribution. The examination of the effect of different tracer blend particle sizes led to an interesting result: It was shown that the particle size segregation only had a low influence on Et. However, a comparably higher influence of the particle size segregation on the particle distribution in the produced tablets was demonstrated. Large particles were deposited at the top of the tablet surface whereas small particles were deposited at their bottom.
Asunto(s)
Polvos/química , Comprimidos/química , Celulosa/química , Composición de Medicamentos , Excipientes/química , Tamaño de la Partícula , Dióxido de Silicio/química , Factores de TiempoRESUMEN
We present herein a study on the adsorption of anionic (SDS), cationic (CTAB), and nonionic (C(12)E(5)) surfactants onto anionic silica nanoparticles. The effects of this adsorption are studied by means of the static structure factor, S(q), and the collective diffusion coefficient, D(c), obtained from small-angle X-ray scattering and dynamic light scattering measurements, respectively. The effective charge on the particles was determined also from classical electrophoresis and electroacoustic sonic-amplitude measurements. The surface tension of the sample was also investigated. Of particular note is the adsorption of SDS onto the silica nanoparticles, which leads to supercharging of the interface. This has interesting repercussions for structures obtained by the layer-by-layer (LbL) technique, because emulsions stabilized with supercharged and hydrophobized silica are perfect candidates for use in a multilayer system.