Direct pelletization in a rotary processor controlled by torque measurements. I. Influence of process variables

The aim of this study was to elucidate the feasibility of using torque measurement to control the end point of a wet pelletization process in a rotary processor at varying levels of friction plate rotation speed, air gap pressure difference, and batch size. A 1:1 mixture of lactose monohydrate (200 mesh) and microcrystalline cellulose (PH-101) was granulated into pellets in an instrumented laboratory scale rotary processor using water as aqueous binder liquid. A full factorial designed study was performed to investigate the influence of the friction plate rotation speed (600 and 1200 rpm), the air gap pressure difference (1 and 3 kPa), the torque increase (0.4 and 0.8 N.m) and the batch size (500 and 1000 g) on the pellet properties. All pellets produced were round and showed a narrow size distribution. The geometric mean diameter varied from 400 to 1900 microns with a good reproducibility. Increasing the batch size and the rotation speed led to smaller pellets, whereas a higher torque produced larger pellets. This study showed that the process can be controlled by means of the torque increase because it was possible to produce pellets of a reproducible size by stopping the liquid addition at a certain torque level.     

Agglomerate formation and growth mechanisms during melt agglomeration in a rotary processor

The purpose of this study was to investigate the effect of the binder particle size and the binder addition method on the mechanisms of agglomerate formation and growth during melt agglomeration in a laboratory scale rotary processor. Lactose monohydrate was agglomerated with molten polyethylene glycol (PEG) 3000 by adding the PEG either as solid particles from the size fraction 0-250, 250-500, or 500-750 microm or as droplets with a median size of 25, 48, or 69 microm. It was found that the PEG particle size, the PEG droplet size, and the massing time significantly influenced the agglomerate size and size distribution. Agglomerate formation and growth were found to occur primarily by distribution and coalescence for the PEG size fraction 0-250 microm and mainly by the immersion mechanism for the PEG size fractions 250-500 and 500-750 microm. When the PEG was sprayed upon the lactose, the mechanism of agglomerate formation was supposed to be a mixture of immersion and distribution, and the agglomerate growth was found to occur by coalescence regardless of the PEG mean droplet size. Compared to high shear mixers and conventional fluid bed granulators, the mechanisms of agglomerate formation and growth in the rotary processor resembled mostly those seen in the fluid bed granulator.     

Melt pelletisation of a hygroscopic drug in a high shear mixer. Part 2. Mutual compensation of influence variables.

The process of melt pelletisation in a Diosna P10 high shear mixer was examined for sodium valproate and glycerol monostearate. The effects of binder concentration, impeller speed and massing time on mean granule size, size distribution and liquid saturation were investigated. Spherical pellets of almost similar size and size distribution were obtained after 20 min of massing time, with a binder content from 3.1 to 14.1% w/w by adjusting the impeller speed. Granule growth was observed at low levels of binder concentration and liquid saturation (<80%) which is untypical for melt granulation. The liquid saturation seemed to have no major influence on the final pellet size. Additional, mutually compensating effects on granule growth were found to be impeller speed and massing time for a fixed binder concentration. Low levels of both, binder concentration and impeller speed, allowed for good control of the process. The amount of water adsorbed by the hygroscopic drug was found to accelerate granule growth.     

Effects of binder rheology on melt agglomeration in a high shear mixer

Lactose monohydrate was melt agglomerated in an 8-l high shear mixer using Gelucire 50/13, Stearate 6000 WL 1644, or polyethylene glycol (PEG) 3000 as meltable binder. The impeller speed was varied at two levels, and massing time was varied at six levels. In order to obtain a similar agglomerate growth, a larger binder volume had to be used with Gelucire 50/13 than with Stearate 6000 WL 1644 and PEG 3000. The lower viscosity of Gelucire 50/13 gave rise to agglomerates of a wider size distribution and a higher porosity as well as more adhesion of mass to the bowl. A lower binder viscosity resulted in more spherical agglomerates at the low impeller speed.     

Effect of a melt agglomeration process on agglomerates containing solid dispersions

The purpose was to produce solid dispersions of a poorly water-soluble drug, Lu-X, by melt agglomeration in a laboratory scale rotary processor. The effect of binder type and method of manufacturing on the dissolution profile of Lu-X was investigated. Lactose monohydrate and Lu-X were melt agglomerated with Rylo MG12, Gelucire 50/13, PEG 3000, or poloxamer 188. Either a mixture of binder, drug, and excipient was heated to a temperature above the melting point of the binder (melt-in procedure) or a dispersion of drug in molten binder was sprayed on the heated excipient (spray-on procedure). The agglomerates were characterized by DSC, XRPD, SEM, and EDX-SEM. The study showed that the agglomerates containing solid dispersions had improved dissolution rates compared to physical mixtures and pure drug. The melt-in procedure gave a higher dissolution rate than the spray-on procedure with PEG 3000, poloxamer 188, and Gelucire 50/13, whereas the opposite was found with Rylo MG12. This was explained by differences in mechanisms of agglomerate formation and growth, which were dominated by immersion with PEG 3000, poloxamer 188, and Gelucire 50/13, and by distribution and coalescence with Rylo MG12. The spray-on procedure resulted in a higher content of Lu-X in the core of the agglomerates when immersion was the dominating mechanism, and in a higher content in the agglomerate surface when distribution was dominating. The melt-in procedure resulted generally in a homogeneous distribution of Lu-X in the agglomerates. The compounds in the agglomerates were found primarily to be crystalline, and the dissolution profiles were unchanged after 12 weeks storage at 25 degrees C at 50% RH.     

Impact of a non-meltable additive on melt agglomeration with a hydrophobic meltable binder in high-shear mixer

The present study aims to investigate the behavior of melt agglomeration with a low-viscosity hydrophobic meltable binder by using a non-meltable additive. The size, crushing strength, and pore size distribution of resultant agglomerates, the rheological, surface tension, and wetting properties of the molten binder, as well as, the flow characteristics of preagglomeration powder blend were determined. The use of additive showed contradictory agglomerate growth-promoting and -retarding effects on the molten binder surface tension and the interparticulate frictional forces. Critical concentration effects of additive corresponded to threshold transition of agglomeration-promoting to -retarding behavior were discussed.     

Impact of a Non-meltable Additive on Melt Agglomeration with a Hydrophobic Meltable Binder in High-Shear Mixer

The present study aims to investigate the behavior of melt agglomeration with a low-viscosity hydrophobic meltable binder by using a non-meltable additive. The size, crushing strength, and pore size distribution of resultant agglomerates, the rheological, surface tension, and wetting properties of the molten binder, as well as, the flow characteristics of preagglomeration powder blend were determined. The use of additive showed contradictory agglomerate growth-promoting and -retarding effects on the molten binder surface tension and the interparticulate frictional forces. Critical concentration effects of additive corresponded to threshold transition of agglomeration-promoting to -retarding behavior were discussed.     

Melt pelletization in high shear mixer using a hydrophobic melt binder: influence of some apparatus and process variables.

The effects of process conditions and the apparatus variables on the granulometric characteristics of a formulation containing a hydrophobic binder (stearic acid), lactose and paracetamol prepared by melt pelletization process were investigated in a 10-litre high shear mixer. The factors under investigation were: impeller speed, massing time, type of impeller blades and presence of the deflector and their reciprocal interactions. Two granule characteristics were analysed: the percentage of aggregates larger than 3000 microm (Y(1)) and the yield of the 2000-microm pellet size fraction (Y(2)). In order to estimate simultaneously the above-mentioned factors, a particular experimental design was adopted, that allowed the reduction of the number of trials from 378 to 35 and took into consideration other uncontrolled factors with the aid of a block variable. Using the postulated model, we found the optimal operating conditions to minimize Y(1) and increase Y(2) by selecting the type of impeller, and by using an impeller speed lower than 300 rpm, a massing time of 8-9 min and by not using the deflector. Finally, the validity of the adopted strategy has been proved with an additional check point.     

Effects of interactions between powder particle size and binder viscosity on agglomerate growth mechanisms in a high shear mixer.

A study was performed in order to elucidate the effects of the interactions between powder particle size and binder viscosity on the mechanisms involved in agglomerate formation and growth. Calcium carbonates having mean particle sizes in the range of 5-214 microm and polyethylene glycols having viscosities in the range of approximately 50-100000 mPas were melt agglomerated in a high shear mixer. Agglomerate growth by nucleation and coalescence was found to dominate when agglomerating small powder particles and binders with a low viscosity. Increasing the binder viscosity increased the formation of agglomerates by immersion of powder particles in the surface of the binder droplets. With a larger powder particle size, an increasing binder viscosity was necessary in order to obtain an agglomerate strength being sufficient to avoid breakage. Due to a low agglomerate strength, a satisfying agglomeration of very large particles (214 microm) could not be obtained, even with very viscous binders. The study demonstrated that the optimum agglomerate growth occurred when the agglomerates were of an intermediate strength causing an intermediate deformability of the agglomerates. In order to produce spherical agglomerates (pellets), a low viscosity binder has to be chosen when agglomerating a powder with a small particle size, and a high viscosity binder must be applied in agglomeration of powders with large particles.     

Melt pelletisation of a hygroscopic drug in a high shear mixer. Part 1. Influence of process variables.

The applicability of a high shear mixer for melt pelletisation of binary mixtures of sodium valproate and glycerol monostearate was investigated. The effects of binder concentration, impeller speed, jacket temperature and massing time on mean pellet size and size distribution were examined in a 2(4)-factorial design. Binder concentration and impeller speed were found to be the most important variables influencing the mean granule size and size distribution. An increase in each of those accelerated the granule growth. Due to the solubility of the drug in the molten binder very low amounts of binder were necessary for the formation of pellets. The modified high shear mixer was found to be suitable for batch sizes of 1-4 kg; granule growth was delayed with increasing load. A common pellet growth pattern, which can be divided into three phases, was derived and confirmed from all trials. The process was monitored by means of a torque measuring system. The torque-time curve can be used to detect the beginning of the destruction phase.     

Melt agglomeration with polyethylene glycol beads at a low impeller speed in a high shear mixer.

This study was performed in order to evaluate the possibility of obtaining spherical agglomerates with a high content of meltable binder by a melt agglomeration process in a high shear mixer. Lactose monohydrate was melt agglomerated with polyethylene glycol (PEG) 1500 or 6000 in a 10-l high shear mixer at an impeller speed of 400 rpm. The PEG 1500 was used as a size fraction of beads, and the PEG 6000 as a fine powder, a powder, unfractionated beads, and size fractions of beads. It was found to be possible to incorporate a high amount of PEG (28% m/m of the amount of lactose), because the rather low impeller speed applied in the present experiments caused less densification of the agglomerates. The fine powder of the PEG 6000 caused a complete adhesion of the mass to the bowl shortly after melting. A rapid agglomerate growth by coalescence was found to be the dominant growth mechanism when agglomeration was performed with the PEG 6000 powder. The PEG beads resulted in a slow and more controllable agglomerate growth, because the growth occurred primarily by an immersion of the lactose particles in the surface of the molten binder droplets. The initial shape of the agglomerates produced with the PEG beads was similar to the spherical shape of the beads. This shape could not be maintained during the process due to a breakage of the agglomerates caused by a hollow structure of the PEG beads.     

Investigation of melt agglomeration process with a hydrophobic binder in combination with sucrose stearate

The melt agglomeration process of lactose powder with hydrogenated cottonseed oil (HCO) as the hydrophobic meltable binder was investigated by studying the physicochemical properties of molten HCO modified by sucrose stearates S170, S770 and S1570. The size, size distribution, micromeritic and adhesion properties of agglomerates as well as surface tension, contact angle, viscosity and specific volume of molten HCO, with and without sucrose stearates, were examined. The viscosity, specific volume and surface tension of molten HCO were found to be modified to varying extents by sucrose stearates which are available in different HLB values and melt properties. The growth of melt agglomerates was promoted predominantly by an increase in viscosity, an increase in specific volume or a decrease in surface tension of the molten binding liquid. The agglomerate growth propensity was higher with an increase in inter-particulate binding strength, agglomerate surface wetness and extent of agglomerate consolidation which enhanced the liquid migration from agglomerate core to periphery leading to an increased surface plasticity for coalescence. The inclusion of high concentrations of completely meltable sucrose stearate S170 greatly induced the growth of agglomerates through increased specific volume and viscosity of the molten binding liquid. On the other hand, the inclusion of incompletely meltable sucrose stearates S770 and S1570 promoted the agglomeration mainly via the reduction in surface tension of the molten binding liquid with declining agglomerate growth propensity at high sucrose stearate concentrations. In addition to being an agglomeration modifier, sucrose stearate demonstrated anti-adherent property in melt agglomeration process. The properties of molten HCO and melt agglomerates were dependent on the type and concentration of sucrose stearate added.     

Relationship between inhomogeneity phenomena and granule growth mechanisms in a high-shear mixer

This study was performed in order to evaluate the possibility of obtaining prolonged release matrix pellets by a melt pelletization process in a laboratory high shear mixer (Mi-Pro, Pro-C-epT). Phenylephrine hydrochloride pellet formulations based on lactose 450 mesh and a mixture of Compritol 888 and Precirol ATO 5 as melting binders were evaluated. The fatty binder content of pellets was substantially increased (from 18 to 80% w/w). The effects of jacket temperature, massing time (MT) and impeller speed (IS) on the pellet characteristics were investigated. It was shown that pellets of narrow size distribution can be produced by using an IS of 800 rpm, a chopper speed of 4000 rpm and a MT of 8 min. On the other hand, the applicability of this technique for the production of sustained-release pellets using ciprofloxacin hydrochloride, ketoprofen and theophylline as less water soluble model drugs than phenylephrine hydrochloride was also studied. This study demonstrated that formulations based on an appropriate mixture of Precirol and Compritol can be used to produce in a short time prolonged release pellets for very hydrosoluble drugs like phenylephrine hydrochloride as well as for the other drugs tested.     

Effects of physical properties of powder particles on binder liquid requirement and agglomerate growth mechanisms in a high shear mixer.

A study was performed in order to elucidate the effects of the physical properties of small powder particles on binder liquid requirement and agglomerate growth mechanisms. Three grades of calcium carbonate having different particle size distribution, surface area, and particle shape but approximately the same median particle size (4-5 microm), were melt agglomerated with polyethylene glycol (PEG) 3000 or 20,000 in an 8-l high shear mixer at three impeller speeds. The binder liquid requirement was found to be very dependent on the packing properties of the powder, a denser packing resulting in a lower binder liquid requirement. The densification of the agglomerates in the high shear mixer could be approximately predicted by compressing a powder sample in a compaction simulator. With the PEG having the highest viscosity (PEG 20,000), the agglomerate formation and growth occurred primarily by the immersion mechanism, whereas PEG 3000 gave rise to agglomerate growth by coalescence. Powder particles with a rounded shape and a narrow size distribution resulted in breakage of agglomerates with PEG 3000, whereas no breakage was seen with PEG 20,000. Powder particles having an irregular shape and surface structure could be agglomerated with PEG 20,000, whereas agglomerate growth became uncontrollable with PEG 3000. When PEG 20,000 was added as a powder instead of flakes, the resultant agglomerates became rounder and the size distribution narrower.     

Optimization of melt pelletization in a high shear mixer

The effects of process conditions and binder content on the process yield and pellet characteristics of two formulations prepared by melt pelletization in a laboratory-type high shear mixer were investigated. The formulations were prepared using Gelucire^® 50/13 and Lutrol^® F68 as meltable binders. The factors under investigation were impeller speed, mixing time, mixer load, binder concentration, and their reciprocal interactions. Analysis of variance (ANOVA) was used in order to study the significance of above mentioned process variables on the useful yield. Twenty-seven experiments were required for the response surface methodology based on Box–Behnken experimental design (24 combinations with three replications of the centre point) for each formulation.The control over the process and the quality of the resulting pellets were found to depend on the rheological properties of the binders used. In the case of a low viscosity binder (Gelucire^® 50/13), the process was easily controllable whereas in the case of a high viscosity binder (Lutrol^® F68), the process was more difficult to control.The useful yield of the formulation in the case of the low viscosity binder was found to be mostly influenced by the concentration of the binder. On the other hand, different binder concentrations did not affect the useful yield of the formulation prepared by use of the high viscosity binder. In the latter case, mixing time was identified as the variable that mostly influenced the pelletization process.Finally response surface methodology was applied to find the optimum values of the process variables.     

熔融高速搅拌法制备氢氯噻嗪缓释微丸

通过对处方和工艺进行优化和筛选 ,采用熔融高速搅拌法制备了利尿药氢氯噻嗪的缓释微丸。结果表明 :以固体石蜡和单硬脂酸甘油酯为粘合剂 ,在 6 4℃、70 0r/min条件下操作 ,成粒子后再加入少量固体石蜡和钙盐 ,继续搅拌 ,降温整粒 8min可得圆整的缓释微丸。验证了应用熔融高速搅拌法制备氢氯噻嗪缓释微丸的适用性和技术特殊性 ,为工业生产奠定了基础。     

Effects of droplet size and type of binder on the agglomerate growth mechanisms by melt agglomeration in a fluidised bed.

This study was performed in order to evaluate the effects of binder droplet size and type of binder on the agglomerate growth mechanisms by melt agglomeration in a fluidised bed granulator. Lactose monohydrate was agglomerated with melted polyethylene glycol (PEG) 3000 or Gelucire 50/13 (esters of polyethylene glycol and glycerol), which was atomised at different nozzle air flow rates giving rise to median droplet sizes of 40, 60, and 80 microm. Different product temperatures were investigated, below the melting range, in the middle of the melting range, and above the melting range for each binder. The agglomerates were found to be formed by initial nucleation of lactose particles immersed in the melted binder droplets. Agglomerate growth occurred by coalescence between nuclei followed by coalescence between agglomerates. Complex effects of binder droplet size and type of binder were seen at low product temperatures. Low product temperatures resulted in smaller agglomerate sizes, because the agglomerate growth was counteracted by very high binder viscosity or solidification of the binder. At higher product temperatures, neither the binder droplet size nor the type of binder had a clear effect on the final agglomerate size.     

Effect of off-bottom clearance on properties of pellets produced by melt pelletization

This study examines the influence of off-bottom clearance on size and size distribution of pellets produced during melt pelletization at different postmelt impeller speeds and binder concentrations using lactose and polyethylene glycol. Melt pelletization of lactose powder 450 M in an 8-liter highshear mixer, the floor of which was made of polytetrafluoroethylene (PTFE), was carried out with polyethylene glycol 3000 as the meltable binder. Erosion of the PTFE floor of the mixer occurred with time of use and this caused a change in the off-bottom clearance. The findings showed that with a wider clearance, the size distribution of pellets was wider and pellets were much larger. These changes were the results of changes in the mixing intensity and impact frequency of the mass in relation to the eddies formed within the off-bottom clearance. The changes were not associated with the reduction in the circulating material load by entrapment into the off-bottom clearance. In the melt pelletization process, the quality of product was higher if the clearance was kept to a minimum. The off-bottom clearance was best measured at the beginning of each pelletization run because the PTFE floor of the mixer was prone to erosion.     

Effects of physical properties of PEG 6000 on pellets produced by melt pelletization.

This study examined the effects of polyethylene glycol (PEG) binders of different physical forms and from different commercial sources on size and size distribution of pellets produced. The meltable binders used were PEG 6000 in the form of flakes, and coarse and fine powders, and melt pelletization using lactose 450 M was carried out in an 8-liter high-shear mixer. Binder particle size, molecular weight, tack, and viscosity were determined. The results showed that the size and size distribution of the pellets obtained could not be explained by the binder particle size. The size and size distribution of the pellets were related to the tack and viscosity of the molten binders. PEGs used were labeled as the same nominal molecular weight grade, although their determined molecular weights could be quite different. Differences in tack and viscosity of the molten binders were associated with determined molecular weight of the binders. The melt pelletization process is sensitive to tack and viscosity of the molten binders. When different PEG brands of the same nominal molecular weight or different batches of the same brand are used in melt pelletization, it is important to characterize the tack and viscosity of the binders used. The effects of the physical form of binders on the pellet quality appear to be less important when compared to the influences of tack and viscosity of the molten binder.     

A priori performance prediction in pharmaceutical wet granulation: testing the applicability of the nucleation regime map to a formulation with a broad size distribution and dry binder addition

In this study, Hapgood's nucleation regime map (Hapgood et al., 2003) was tested for a formulation that consists of an active pharmaceutical ingredient (API) of broad size distribution and a fine dry binder. Gabapentin was used as the API and hydroxypropyl cellulose (HPC) as the dry binder with deionized water as the liquid binder. The formulation was granulated in a 6 l Diosna high shear granulator. The effect of liquid addition method (spray, dripping), liquid addition rate (29-245 g/min), total liquid content (2, 4 and 10%), and impeller speed (250 and 500 rpm) on the granule size distribution and lump formation were investigated. Standard methods were successfully used to characterize the process parameters (spray drop size, spray geometry and powder surface velocity) for calculating the dimensionless spray flux. However, the addition of dry binder had a very strong effect on drop penetration time that could not be predicted from simple capillary flow considerations. This is most likely due to preferential liquid penetration into the fine pores related to the dry binder particles and subsequent partial softening and dissolution of the binder. For systems containing a dry binder or other amorphous powders, it is recommended that drop penetration time be measured directly for the blended formulation and then scaled to the drop size during spraying.Using these approaches to characterize the key dimensionless groups (dimensionless spray flux and drop penetration time), Hapgood's nucleation regime map was successfully used to predict a priori the effect of process conditions on the quality of the granule size distribution as measured by lump formation and the span of the size distribution, both before and after wet massing for range of conditions studied. Wider granule size distributions and higher amount of lumps were obtained moving from intermediate to mechanical dispersion regime. Addition of the liquid in the dripping mode gave the broadest size distribution with ungranulated fines and highest percentage of lumps compared to spraying mode. Addition of the liquid by spraying in the intermediate regime gave the narrowest size distribution with the lowest amount of lumps. The effects of impeller speed and wet massing time on granule size distribution were complex. At 2% liquid content, increasing the impeller speed and adding wet massing time caused some breakage of lumps and the production of fines. At higher liquid contents, the effects were less clear, likely due to a balance between increased breakage and increased granule consolidation and growth. Nevertheless, this work has demonstrated that for complex formulations with dry binder addition, the final granule size distribution still depends strongly on the homogeneity of the initial liquid distribution which is well predicted by the nucleation regime map analysis.