Real-time image-based investigation of spheronization and drying phenomena using different pellet formulations

Extrusion-spheronization (ES) is a frequently used agglomeration process in the pharmaceutical industry to manufacture spherical solid units or pellets with a narrow size and shape distribution. In this study, photometric stereo imaging was applied in real-time during the final steps of the ES process, being spheronization and drying. In addition to the pellet size distribution of undispersed (wet) samples, the imaging technique captures visual information on pellet shape and surface brightness. Pellet samples were taken at 20 time points during spheronization and were imaged at-line (during spheronization) and off-line (after spheronization). Particle size distributions and visual image information were both used to characterise the spheronization behaviour of different formulations. Next, particle size distributions and surface brightness values calculated from the at-line obtained images during fluid bed drying of pellets were analysed. The particle size distribution and brightness value changes occurring during pellet drying were explained both by the reduction in residual moisture content and drug solid-state transition. Due to the rapidness of the technique with regard to sample preparation, sample measurement and the acquisition of results in combination with the possibility to measure undispersed (wet) samples, valuable information on spheronization and drying characteristics of different formulations was obtained in real-time.

Determination of tackiness of chitosan film-coated pellets exploiting minimum fluidization velocity

The tackiness of aqueous chitosan film coatings and effects of anti-sticking agents on sticking tendency, were evaluated. A novel rapid method exploiting minimum fluidization velocity to determine tackiness was introduced and tested. The pressure difference over the miniaturized fluidized-bed was precisely recorded as a function of velocity of fluidization air. High molecular weight chitosan plasticized with glycerol was used as a film-forming agent. Magnesium stearate, titanium dioxide, colloidal silicon dioxide and glyceryl-1-monostearate (GMS) were studied as anti-sticking agents. Film coatings were performed in a miniaturized top-spray coater. The incorporation of anti-sticking agents led to a clear decrease in tackiness of the chitosan films, and magnesium stearate and GMS were shown the most effective. Film-coated pellets containing magnesium stearate and GMS as an anti-sticking agent were very easily fluidized (showing very low values of minimum fluidization velocity) and were thus classified as the best flowing and the least sticking samples. Both these additives were found anti-sticking agents of choice for aqueous chitosan film coatings. Determination of the experimental minimum fluidization velocity in a fluidized bed, is a useful and sensitive method of measuring the tackiness tendency of film-coated pellets.

Development and characterization of aqueous amylose-rich maize starch dispersion for film formation

Development and characterization of amylose-rich starch dispersion for film forming was performed. The influence of dispersion preparation temperature on amylose-rich maize starch (Hylon VII) film formation, and the physical properties of the films were investigated. The film-forming ability of the dispersions was evaluated with free films plasticized with glycerol and sorbitol, and the films were prepared at an elevated temperature (70 degrees C) by a casting technique. The solid-state and particle properties of dispersions were investigated by means of X-ray diffraction (XRD), Fourier transform near infrared (FT-NIR) spectroscopy and laser diffraction particle size analysis. Free films were characterized with respect to their appearance, by FT-NIR spectroscopy, and by XRD. Mechanical stress-strain properties were also studied. Increasing the temperature of dispersion preparation results in higher crystallinity, thus affecting the film forming ability. Mechanically strong and elastic films can be formed from amylose-rich starch dispersion formed at 40 degrees C. The more crystalline precipitate complex (obtained at 80 degrees C) and the entirely amorphous gel (obtained at 10 degrees C) formed non-continuous and cloudy films. The better film-forming properties of the dispersion formed at 40 degrees C are probably due to the highly amorphous structure and smaller particle size. The study shows the possibility of using ambient tempered amylose-starch dispersion for film forming.

Effect of beta-sitosterol on precipitation of cholesterol from non-aqueous and aqueous solutions

The aim of the present work was to study the solubility and phase behaviour of the beta-sitosterol-cholesterol mixed crystals in the presence and absence of water. Cholesterol, beta-sitosterol and 3:1, 1:1 and 1:3 mixtures of these were co-precipitated from acetone and acetone-water solutions. Precipitated crystals were analysed using powder X-ray diffraction (PXRD), differential scanning calorimetry (DSC), optical microscopy and Karl-Fischer titrimetry. The quantification of the sterols in solutions was preformed using GC-MS. The solubility of the sterols was mutually limiting. In the aqueous system, the solubility of both the sterols were significantly lower than in the absence of water, but the decrease in the solubility was considerably greater with the more hydrophobic beta-sitosterol. In the aqueous system, the total sterol solubility decreased with the increasing proportion of beta-sitosterol. The formation of new crystal structures, solid solutions of cholesterol and beta-sitosterol, was observed in non-aqueous as well as in aqueous environments except with the lowest cholesterol proportion in the system, in which case mixed crystals with eutectic behaviour were formed.

Development of indomethacin Carbopol ETD 2001 gels and the influence of storage time and temperature on their stability

We investigated the development of a topical indomethacin gel formulation of suitable consistency using Carbopol ETD 2001 as the gelling agent. Topical gel formulations containing 1% w/w indomethacin (IND), 1% w/w Carbopol ETD 2001 (C2001), 1% of trethanolamine (TEA), 30% hexylene glycol (HG) and 10% polyethylene glycol (PEG 300) were prepared with excipients Tween 80, PVP 25, both Tween 80 and PVP 25 or neither agent. These four gel formulations were tested after a period of 1 and 4 weeks at storage temperature of 6 degrees C, 20 +/- 2 degrees C and 45 degrees C. Physical evaluation of the stability of these gels was carried out by microscopic and rheological tests, measurement of pH and by visual inspection. Rheological properties were studied using the cone and plate method at shear rates of 600 to 6000 1/s. Viscosities corresponding to shear rates were also calculated. Our results indicated that C2001 could be used as a gelling agent for IND in topical preparations. IND-C2001 gels were clear and exhibited an acceptable appearance; gel behaviour was non-Newtonian and pseudoplastic. The addition of either Tween 80 or PVP 25 to the base gel formulation significantly increased the shear stresses and viscosity of the gels. These novel formulations exhibited good physical stability throughout the 4-week examination periods as inferred from pH measurements and microscopic examination. Additionally, the non-Newtonian pseudoplastic behaviour of the gels was maintained throughout storage, with only a minimal decrease in gel viscosity after 4 weeks. Differences in consistencies of the four formulations, although initially apparent, were no longer evident after 4 weeks of storage for all temperature conditions examined. Gels stored at high temperature (45 degrees C) developed a dark yellow color and decreased in viscosity compared to other storage temperature.

Enhanced stability of rubbery amylose-rich maize starch films plasticized with a combination of sorbitol and glycerol

Well known aging problems with rubbery starch films are the migration of plasticizer and increased crystallinity leading to embrittlement. The effects of a combination of sorbitol and glycerol used as plasticizers on mechanical, moisture permeability and solid-state properties of rubbery amylose maize starch (Hylon VII) films were studied. The films were prepared by casting and were exposed to conditions of 25 degrees C/60% relative humidity (RH) and 40 degrees C/75% RH for 9 months. The starch films plasticized with a combination of sorbitol and glycerol (1:1) at equal amount to the polymer weight, were shown to be the most stable alternative of the studied films during the 9 months storage period. The water vapor transmission (WVTR) of the films did not change during the period of storage and neither did the elongation at break, but the tensile strength increased. X-ray diffraction (XRD) results showed that during storage no crystallization had occurred. The combination of sorbitol and glycerol prevented the migration of the plasticizer molecules out of the film.

Influence of storage time and temperature on the stability of indomethacin Pluronic F-127 gels

The stability of 20 topical gel formulations containing drug, 1% w/w indomethacin (IND), and 20% w/w Pluronic (PF-127) as a gel-forming agent, hexylene glycol (HG) and polyethylene glycol 300 (PEG) in different amounts (16, 20 and 24% w/w) as solvents and 1% w/w polyvinyl pyrrolidone (PVP, K-25) and Tween as excipients was determined by appearance and consistency of the gels, microscopy, pH and rheological measurements after 1 and 4 weeks storage, at 6 degrees C, 20 +/- 2 degrees C and 45 degrees C. Viscosity values were determined from rheograms by a Haake Rotovisco sensor at shear rates of 1000 to 10,000 l/s. The relationship between effectors (temperature and storage time) and response (viscosity) was determined using multiple regression analysis. All formulations were stable at room temperature (20 +/- 2 degrees C). The consistency of the gels containing HG and PEG decreased during storage at 6 degrees C. Storing the gels at 6 degrees C resulted in the precipitation of IND, but when PVP was incorporated into the IND-PF-127 gels, the stability of the gels was improved. All IND gels sustained their pseudoplastic flow behaviour. The viscosity decreased as storage time increased. A statistically significant model was obtained, showing that the effect of storage temperatures on the viscosity was much less than the effect of storage time.

Diffusion of a freely water-soluble drug in aqueous enteric-coated pellets

The effects of filler used in the pellet cores (ie, waxy cornstarch or lactose) and the enteric film coat thickness on the diffusion and dissolution of a freely soluble drug were studied. Two kinds of pellet cores containing riboflavin sodium phosphate as a model drug, microcrystalline cellulose (MCC) as a basic filler, and waxy cornstarch or lactose as a cofiller were film coated (theoretically weight increase 20% or 30%) with an aqueous dispersion of cellulose acetate phthalate (CAP). The diffusion of riboflavin sodium phosphate in aqueous enteric-coated pellets was investigated using noninvasive confocal laser scanning microscopy (CLSM). The in vitro release tests were performed using a USP apparatus I (basket method). Diffusion of drug from the core to the film coat was found to be greater with lactose-containing pellets than with waxy cornstarch-containing pellets. The dissolution test showed that 30% enteric-coated waxy cornstarch pellets had a good acidic resistance in 0.1 N HCl solution for at least 1 hour, while the other enteric pellet formulations failed the test. The waxy cornstarch-containing enteric pellets dissolved at SIF in less than 10 minutes. Confocal images of film-coated pellets showed that waxy cornstarch-containing pellets had less drug dissolved than respective lactose-containing pellets. The observations were further confirmed by measurement of fluorescence intensity of riboflavin sodium phosphate in the film coat. The dissolution test was consistent with the confocal microscopy results. In conclusion, waxy cornstarch as a cofiller in the pellet cores minimizes premature drug diffusion from the core into the film coat layer.

Amylopectin as a subcoating material improves the acidic resistance of enteric-coated pellets containing a freely soluble drug

The effect of an aqueous amylopectin subcoating on the acidic resistance and dissolution behaviour of enteric-coated pellets was studied. Freely water-soluble riboflavin sodium phosphate (RSP) was used as a model drug, and microcrystalline cellulose (MCC) and lactose as fillers in the pellet cores. The pellets were subcoated with 5% aqueous amylopectin solution or with 5% hydroxypropyl methylcellulose (HPMC) solution, and subsequently film-coated with aqueous dispersion of cellulose acetate phthalate (CAP). Drug release of enteric-coated pellets was investigated by confocal laser scanning microscopy (CLSM). Dissolution tests showed that amylopectin subcoating improved the acidic resistance of the enteric-coated pellets in 0.1 N hydrochloric acid (HCl) compared with HPMC subcoating. As the amylopectin subcoating load was increased to 4% and the aqueous CAP coating load to 35%, the coated pellets resisted in 0.1 N HCl solution for approximately 1 h (the amount of drug released was below 10%), and they dissolved in the SIF without enzymes in less than 10 min. Confocal microscopy images and profiles of mean fluorescence intensities of RSP (obtained in the range of the interface of the pellet core and the film and the film coating surface) showed consistent results with dissolution tests. It seems that amylopectin subcoating can prevent the influx of the dissolution medium into the pellet core, and thus decrease the premature dissolution and release of the drug from the enteric-coated pellets in 0.1 N HCl solution. The drug release mechanism appeared to be osmotically driven release, and followed by diffusion through the polymer film.

Pluronic F-127 gels as a vehicle for topical formulations of indomethacin and rheological behaviour of these formulations

Topical gel formulations containing a non-steroidal anti-inflammatory drug, indomethacin (IND), were prepared using 20% w/w Lutrol PF-127 as a gel-forming agent, and 16, 20 and 24% w/w Hexylene glycol (HG) or polyethylene glycol 300 (PEG) as solvents. 1% w/w Tween 80 and 1% w/w PVP 25 were added as excipients. The effects of the amounts of solvent and excipients on the physical characteristics of IND gel such as consistency, appearance, crystallization, pH and viscosity were studied. The results indicated that 1% w/w IND is able to form a structural gel. The viscosity values were calculated from the rheograms which were determined by a Haake Rotovisco sensor at a shear rate of 10,000 l/s. Viscosities corresponding to shear rates of 1000, 3000, 6000 and 9000 l/s were also calculated. Yield points were approximated from the rheograms. Although all IND gels maintained their pseudoplastic flow behaviour, their viscosities decreased markedly with increasing shear rates. Furthermore, increasing the amount of HG or PEG gave a more viscous gel except for the 24 w/w% HG gels which turned a jelly with or without either Tween or PVP. The difference in viscosities was explained by the changes in the gel compositions. 20% of PEG-1% PVP ranked first in viscosity followed by 16% PEG-1% PVP, 16% PEG-1% Tween, 24% PEG, 20% PEG-1% Tween and 16% HG-1% PVP. The results indicate that the excipients influence the physical characteristics of the gels. The optimum concentration for gels manifesting as strength of gel was 20% PEG in combination with 1% PVP which had the highest viscosity and yield value at a low shear rate.

Microcrystalline cellulose-water interaction--a novel approach using thermoporosimetry

PURPOSE

To study the physical state of water in microcrystalline cellulose (MCC) and in silicified microcrystalline cellulose wet masses and the effect of granulation on different water fractions.

METHODS

Thermoporosimetry, together with the solute exclusion technique, was used to measure different water fractions and pore size distributions of wet granules. To understand the effect of granulation on the physical state of water, both ungranulated and granulated wet masses were studied. In addition, dynamic and isothermal step melting procedures were compared.

RESULTS

Four distinct fractions of water (nonfreezing, freezing bound, free, and bulk water) could be detected in MCC wet masses. Granulation decreased the volume of bulk water and increased the volume of freezing bound and free water. Consequently, granulated wet masses were able to hold more water inside the particles compared to ungranulated wet masses. Thus, granulation had a similar effect on MCC as beating has on cellulose fibers in the papermaking proces

CONCLUSIONS

Thermoporosimetry and solute exclusion increased the understanding of MCC-water interaction and showed how the physical state of water in MCC wet masses changes during granulation.

Process analysis of fluidized bed granulation

This study assesses the fluidized bed granulation process for the optimization of a model formulation using in-line near-infrared (NIR) spectroscopy for moisture determination. The granulation process was analyzed using an automated granulator and optimization of the verapamil hydrochloride formulation was performed using a mixture design. The NIR setup with a fixed wavelength detector was applied for moisture measurement. Information from other process measurements, temperature difference between process inlet air and granules (T(diff)), and water content of process air (AH), was also analyzed. The application of in-line NIR provided information related to the amount of water throughout the whole granulation process. This information combined with trend charts of T(diff) and AH enabled the analysis of the different process phases. By this means, we can obtain in-line documentation from all the steps of the processing. The choice of the excipient affected the nature of the solid-water interactions; this resulted in varying process times. NIR moisture measurement combined with temperature and humidity measurements provides a tool for the control of water during fluid bed granulation.

Process analysis of fluidized bed granulation

This study assesses the fluidized bed granulation process for the optimization of a model formulation using in-line near-infrared (NIR) spectroscopy for moisture determination. The granulation process was analyzed using an automated granulator and optimization of the verapamil hydrochloride formulation was performed using a mixture design. The NIR setup with a fixed wavelength detector was applied for moisture measurement. Information from other process measurements, temperature difference between process inlet air and granules (T(diff)), and water content of process air (AH), was also analyzed. The application of in-line NIR provided information related to the amount of water throughout the whole granulation process. This information combined with trend charts of T(diff) and AH enabled the analysis of the different process phases. By this means, we can obtain in-line documentation from all the steps of the processing. The choice of the excipient affected the nature of the solid-water interactions; this resulted in varying process times. NIR moisture measurement combined with temperature and humidity measurements provides a tool for the control of water during fluid bed granulation.

Corn starches as film formers in aqueous-based film coating

The purpose of this study was to evaluate the film formation ability and mechanical stress-strain properties of aqueous native corn starches, using free films and film coatings applied to tablets. Free films were prepared from high-amylose corn (Hylon VII), corn and waxy corn starches, using sorbitol and glycerol as plasticizers. The tablets and pellets were film-coated using an air-suspension coater, and characterized with respect to the film coating surface topography, cross-sectional structure and thickness (SEM), and dissolution in vitro. The amylose content of the starch film formers affected both the tensile strength and the elongation. The elongations were under 5% for even the plasticized starches, and in most cases, no plasticization effect was seen by either of the plasticizers. Dissolution of native corn starch film-coated tablets (weight gain 1%) did not differ from uncoated ones. A notable delay in dissolution of the drug was found by increasing Hylon VII film coating thickness, suggesting controlled-release characteristics.

Rheological properties of creams with four different surfactant combinations - effect of storage time and conditions

Changes in the rheological properties of four o/w cream formulations differing in the combination of surfactants were studied. The non-ionic surfactants used were soybean derivatives, polyethylene glycol 10 and 25 soya sterol, and sorbitol derivatives, sorbitan monooleate and trioleate. Combinations of the soybean and sorbitol derivatives were used. The rheological properties were tested during a 28-day storage period at three different storage conditions (cold, room temperature and accelerated conditions). In addition to dynamic and static rheological tests, droplet size distributions and conductivities of the creams were also determined. The consistency of the creams containing polyethylene glycol 10 soya sterol decreased during storage. Despite the greatest decreases in consistency, the creams containing polyethylene glycol 10 soya sterol exhibited the most viscoelastic structures with linear viscoelastic behaviour. Storing the creams for 28 days in the three different storage conditions made the differences in the consistency of the formulations smaller. All three storage conditions were involved when the conditions of the most viscoelastic cream of each formulation was specified. In the case of linearly viscoelastically behaving creams containing polyethylene glycol 10 soya sterol, all the rheological tests correlated with the droplet size distributions and the conductivity tests.

Characterization of wet massing behavior of silicified microcrystalline cellulose and alpha-lactose monohydrate using near-infrared spectroscopy

The purpose of this study was to investigate the energetic state of water in silicified microcrystalline cellulose (SMCC) and alpha-lactose monohydrate wet masses using near-infrared (NIR) spectroscopy. The applicability of NIR spectroscopy to studying pharmaceutical wet masses at a wide moisture range was evaluated in comparison with mixer torque rheometry (MTR). With increasing moisture content changes in the physical properties of the samples resulted in an apparent increase in log (1/R) throughout the whole spectrum. The upward displacement of baseline and the relative height of water bands were greatest with materials that had a poor liquid-retention capacity. In the case of SMCC and 1:1 mixture of SMCC and alpha-lactose monohydrate, the height of the baseline-corrected water bands increased linearly at low moisture contents, thereafter achieving a plateau stage. According to the MTR results, the plateau stage of the band heights indicated a capillary state of liquid saturation. The second derivative spectrum was capable of distinguishing monohydrate, absorbed, and adsorbed water, which overlapped in the absorbance spectrum. When water was absorbed to the internal structure of the material (SMCC), the water bands were first seen at higher wavelengths, then followed by a shift to lower wavelengths. When water was only adsorbed onto the surface of the particles (glass ballotini), the water bands were seen directly in the region of bulk water.

Influence of the centrifugal granulating process on the properties of layered pellets

Drug-layered pellets based on microcrystalline cellulose (MCC) beads as substrates were prepared using a laboratory-scale centrifugal granulator. The effect of three independent process parameters (rotor rotation speed, slit air flow rate, and spray air rate) on responses describing the amount of drug loss during the process, amount of agglomerates, bulk density, flowability, friability, shape, and surface roughness were studied using a 3(3) full factorial experimental design. The variables studied were found to have a significant influence on the responses evaluated. Rotor rotation speed and slit air flow rate had a significant positive influence on the amount of drug loss during the process and the amount of agglomerates, whereas rotor rotation speed and spray air rate had the same effect on the bulk density, flowability, and the roundness of the pellets. The amount of agglomerates and the roundness value of the pellets were negatively affected by the spray air rate while the slit air flow rate showed the same effect on the bulk density and flow rate of the pellets. In addition to the main effects, there were some significant paired interactions between slit air flow rate and spray air rate as well as rotor rotation speed and slit air flow rate. Based on the results, the significance of these three parameters should be considered carefully for quality pellet preparation by the centrifugal granulating technique using MCC beads as substrates.

Characterization of microcrystalline cellulose and silicified microcrystalline cellulose wet masses using a powder rheometer

A powder rheometer has been used to study the properties of wet powder masses and the results have been compared to the mixer torque rheometer (MTR). Two different microcrystalline cellulose (MCC) grades (Avicel and Emcocel) and silicified microcrystalline cellulose (SMCC, Prosolv) were used as model powders. The wet massing behaviour of one material (Prosolv) was studied by the powder rheometer using liquid addition experiments, while the rheological properties of wet granules were studied using both the powder rheometer and the MTR. In water addition measurements the torque behaved in a similar way to MTR measurements and the maximum value of ZTL (zero torque limit) was achieved at the capillary state of wet mass. The wet granules exhibited different behaviour in the powder rheometer and the MTR experiments, which indicates that these rheometers involve different shear forces or they measure different properties of the wet granules. Emcocel wet masses achieved the capillary state at lower liquid amount than Avicel and Prosolv masses, which indicates that Emcocel is not able to hold as much water in the internal structure as Avicel and Prosolv. The powder rheometer proved to be a sensitive piece of equipment, which can be used to study both dry and wet powder masses. It was able to distinguish wet granules from wet powder masses after liquid addition, whereas the MTR could not. However, before the powder rheometer can be properly utilised in wet powder mass studies, the problem of torque overload requires resolution.

Use of a capillary rheometer to evaluate the rheological properties of microcrystalline cellulose and silicified microcrystalline cellulose wet masses

The influence of microcrystalline cellulose (MCC) type and water content on the rheological properties of the wet powder masses were studied using two different MCC grades (Avicel and Emcocel) and silicified microcrystalline cellulose (SMCC, Prosolv). A ram extruder was used as a capillary rheometer and unique flow curves for each cellulose grade and moisture content were derived. In addition, the elastic parameters of recoverable shear and compliance were determined. From different flow curve models evaluated, it was not possible to obtain clear evidence, which model best described the rheological properties of each cellulose grade at each water level. Furthermore, the residuals were shear rate dependent, which indicates that the models do not perfectly agree with physical properties of the wet masses. The elastic properties of wet masses increased with increasing water content and decreased with increasing shear stresses. SMCC grade proved to be more elastic than the simple MCC grades at each moisture content. Thus, the rheological properties of MCC and SMCC wet masses were different and changed with water content. Consequently, it was not possible to achieve similar rheological properties between different grades of cellulose by altering the water content of the wet mass.

Novel identification of pseudopolymorphic changes of theophylline during wet granulation using near infrared spectroscopy

The purpose of this study was to demonstrate the efficiency of near infrared (NIR) spectroscopy in studying the pseudopolymorphic changes and the state of water during the wet granulation process. Anhydrous theophylline was granulated in a planetary mixer using water as granulation liquid. NIR spectra and differential scanning calorimetric (DSC) and wide-angle X-ray scattering (WAXS) patterns of theophylline granules, anhydrous theophylline, and theophylline monohydrate were measured. At a low level of granulation liquid (0.3 mol of water per mole of anhydrous theophylline), water absorption maxima in the NIR region occurred first at around 1475 and 1970 nm. These absorption maxima were identical to those of theophylline monohydrate. At higher levels of granulation liquid (1.3-2.7 mol of water per mole of anhydrous theophylline), the increasing absorption maxima occurred at 1410 and 1905 nm due to OH vibrations of free water molecules. X-ray diffraction patterns confirmed the transformation of anhydrous theophylline to theophylline monohydrate during wet granulation. NIR spectroscopy was able to detect different states of water molecules during the wet granulation process faster and in a more flexible manner than conventional methods.

Effect of compression force on the crystal properties of erythromycin acistrate tablets

The crystal properties of compressed and powdered erythromycin acistrate tablets were studied by the X-ray powder diffraction (XRPD) method. Detailed analysis of X-ray powder diffraction line profiles was performed. Diffraction peak intensities and full width at half maximum (FWHM) values of the peaks corresponding to three different crystal lattice directions were determined. Crystallite size was calculated by Scherrer's equation using the data of integral breadth of the peaks. The preferred orientation of the crystallites is also discussed. According to the results, the crystallite size increased on the tablet surface after a small compression force (4 kN) in all crystal lattice directions studied. Even small compression forces caused recrystallization. With higher compression forces (8-18 kN) the crystallite size and the FWHM values remained rather constant. After the compression force of 18 kN the peaks in different crystal lattice directions behaved differently. In the lattice directions of diffraction maxima 2 and 3, the effect was the same with the small (4 kN) and the high compression force (22 kN). Further recrystallization occurred with 22 kN. However, in the crystal lattice direction of diffraction maximum 1 at the compression force of 8 kN the crystallite broke and crystallinity decreased. These were not seen in the powdered tablet samples. It could be concluded that the effect of compression force on the crystal properties of erythromycin acistrate tablets was seen on the tablet surface but not in the powdered tablets. Compression force also affected the preferred orientation of crystallites on the tablet surface and especially in the lattice direction of diffraction maximum 3. This was not seen in the powdered tablets.

In-line moisture measurement during granulation with a four-wavelength near infrared sensor: an evaluation of particle size and binder effects

Factors affecting in-line near infrared (NIR) moisture measurement with a four-wavelength sensor were evaluated (choice of binder used in granulation liquid and the increase in particle size). An entire NIR spectrum is not necessary for the measurement of water, and often the use of only a few NIR wavelengths around the water band enables reliable and high-speed detection of moisture. Glass ballotini and microcrystalline cellulose (MCC) were used as model test materials. The binders studied were poly[1-(2-oxo-1-pyrrolidinyl)ethylene] (PVP) and gelatin. Full off-line NIR spectra of test materials at different levels of binder solutions were measured. The major spectral features for both the binders were bands around 1700 nm (first overtones CH related stretches) and 2200 nm (combination bands). Gelatin also had an NH band around 1500 nm (first overtones of NH stretches) and combination bands at about 2050 nm. Particle size effects were observed as an increase in spectra baseline. All these factors should be considered when choosing NIR wavelengths used for detection of water with a fixed wavelength set-up. A robust calibration model enables the development of in-process control of wet granulation processes.

Content-based image retrieval: a new promising technique in powder technology

The aim of the present study was to introduce a new technique for analyzing powders by examining the content information of images of pharmaceutical powder systems. Texture features of images of microcrystalline cellulose were compared by using a content-based image retrieval system (CBIR), QBIC (Query-by-Image-Content). The rank order and image similarities were compared to particle sizes and appearances of different mixtures. The image order of the similarity values was in close agreement with the appearance and particle size of the mixtures. When the image of pure Avicel PH 101 was used as a query image, the most similar images were always from images of mixtures with a large number of particles with smaller particle mean sizes. When images of pure Avicel PH 200 were used as a query image, the closest matches of image similarity were from images of mixtures with a larger amount of larger particles. The results show that the CBIR system extracts applicable content information on images of powders, but the texture features used were not totally adequate for analysis of the powders used. In general, content-based image retrieval seems to be a promising approach to efficiently use the vast image information that is available from pharmaceutical powders. Nevertheless, to achieve an efficient CBIR tool for powder technology requires development of substantial algorithms for feature extraction.

Use of the near-infrared reflectance method for measurement of moisture content during granulation

The purpose of this study was to demonstrate the use of a near-infrared (NIR) method for in-process control of a placebo formulation. An NIR setup with a multichannel detector was applied in the measurement of water during fluidized bed granulation. The effects of two critical granulation parameters were studied using the central composite design. The present NIR setup with three wavelengths proved applicable for in-line moisture measurement. The 1990 nm signal was used for measurement of water and the 1745 and 2145 nm signals were used to correct the change in spectra baseline during granulation. Variations in inlet air conditions proved to be critical factors, explaining differences in the granule size distributions. Differences in granule moistening and drying rates resulting from varying inlet air conditions could be measured with the NIR setup. The moisture content of granules at the end of the spraying phase explained part of the differences in granule size distributions. The moisture content of granules at the end of the drying phase affected the tableting behavior of granules. The results suggested that direct measurement of granule moisture content facilitates the in-process control of the granulation.

Mercury porosimetry of mannitol tablets: effect of scanning speed and moisture

Purpose of the work was to study the effect of the scanning speed of mercury porosimetry and moisture content of the sample on the mercury porosimetry result for mannitol tablets. Tablets were compressed at three different compression pressures from nonhygroscopic mannitol powder and granules. Pore structure of tablets was determined with three different scanning speeds of a high-pressure mercury porosimeter after storage in three different moisture conditions. With low scanning speed, smallest pores of tablets were determined more accurately. Small amounts of moisture, even as low as 1%, before evacuation in nonhygroscopic mannitol tablets decrease the porosity. Decrease in porosity was observed at a pore diameter range of 50-1000 nm, not at the smallest determined pores. Thus, the role of water in pharmaceutical samples appears to be complicated. Reasonably slow scanning is recommended in high-pressure mercury porosimetry. If total pore volume is the only parameter of interest, fast scanning can be used. Pretreatment of the samples by proper drying before mercury porosimetry is important.

Surface Pressure, Hysteresis, Interfacial Tension, and CMC of Four Sorbitan Monoesters at Water-Air, Water-Hexane, and Hexane-Air Interfaces

The purpose of this study was to investigate the interfacial properties of sorbitan monoesters (Span 20, 40, 60, and 80). The surface pressure was investigated at the water-air interface using a Langmuir-Blodgett apparatus. Interfacial tensions at n-hexane-air and water-n-hexane interfaces were measured by a du Nouy tensiometer. The effects of different surface-active agents and their concentrations on the interfacial properties of surfactant films were determined. With saturated sorbitan monoesters the lengthening of the hydrocarbon chain increases the collapse pressure and molecular area at the water-air interface. Unsaturated Span 80 had a lower collapse pressure and a larger molecular area than its saturated counterpart Span 60. Under compression-expansion cycles, all sorbitan monoesters showed hysteresis effects. At the n-hexane-air interface there were no differences in the interfacial tension between different sorbitan monoesters. At the water-n-hexane interface, differences in CMCs were small, but the surface excess of Span 80 was markedly smaller and the molecular area larger than the corresponding values of other sorbitan monoesters. Copyright 2000 Academic Press.

Next generation fluidized bed granulator automation

A system for fluidized bed granulator automation with in-line multichannel near infrared (NIR) moisture measurement and a unique air flow rate measurement design was assembled, and the information gained was investigated. The multivariate process data collected was analyzed using principal component analysis (PCA). The test materials (theophylline and microcrystalline cellulose) were granulated and the calibration behavior of the multichannel NIR set-up was evaluated against full Fourier Transform (FT) NIR spectra. Accurate and reliable process air flow rate measurement proved critical in controlling the granulation process. The process data describing the state of the process was projected in two dimensions, and the information from various trend charts was outlined simultaneously. The absorbence of test material at correction wavelengths (NIR region) and the nature of material-water interactions affected the detected in-line NIR water signal. This resulted in different calibration models for the test materials. Development of process analytical methods together with new data visualization algorithms creates new tools for in-process control of the fluidized bed granulation.

Extrusion-spheronization of pH-sensitive polymeric matrix pellets for possible colonic drug delivery

The aim of this study was to investigate extrusion-spheronization pelletization for preparing pH-sensitive matrix pellets for colon-specific drug delivery. The effects of three independent variables (amounts of Eudragit S, citric acid and spheronizing time) on pellet size, shape (roundness and aspect ratio), and drug release were studied with central composite design. The pellets contained ibuprofen as a model drug, citric acid as a pH-adjusting agent, Eudragit S as a pH-sensitive binder and microcrystalline cellulose (MCC). The pellets were prepared with Nica extrusion-spheronizing equipment and subsequently enteric-coated using an air-suspension technique. Eudragit S as a pH-sensitive matrix former in pellets increased the pellet size and influenced pellet roundness. In small amounts Eudragit S increased pellet roundness but in larger amounts pellet roundness was reduced. Citric acid promoted the pelletization process resulting in a narrower area distribution. The pH-sensitive matrix pellet failed to delay the drug release. The combination of citric acid and enteric coating, however, delayed the drug release for 15 min in a pH 7.4 phosphate buffer.

Controlled release injectable liposomal gel of ibuprofen for epidural analgesia

The epidural administration is used commonly in the treatment of pain. Nonsteroidal anti-inflammatory drugs, especially ibuprofen, would have potential in epidural use. Like many epidurally useful drugs it, however, has a short duration of action, which is a limiting factor. To improve epidural pain treatment, a long-acting, single-dose gel injection is being developed. In the present study, the possibility of using liposomal systems to control the release and dural permeation of ibuprofen was investigated in vitro. Liposomal solutions of ibuprofen.Na (20 mg/ml) were prepared by high-pressure homogenization from egg phosphatidylcholine. The liposomal gel consisted of poloxamer 407 and the liposomal solution. No signs in the 1H-NMR spectroscopy of line broadenings or chemical shifts were observed. The liposomal formulations were reproducible and stable. Ibuprofen release in phosphate buffer, pH 7.4, at 37 degrees C from the liposomal solution and the liposomal gel were prolonged significantly compared with their respective solution and gel controls. The liposomal gel controlled ibuprofen release and dural permeation in vitro and showed a permeation pattern favourable for maintaining constant drug levels. The liposomal poloxamer gel represents a new formulation approach to increase the local epidural availability of ibuprofen. It appeared to be a promising injectable controlled-release drug delivery system.

Determination of optimal combination of surfactants in creams using rheology measurements

The effect of surfactant on the rheological properties of some cream formulations was studied. Two surfactants from two different series were combined to determine the combination which yielded the most viscoelastic structure for creams. The surfactants were the soybean derivatives soya sterol, polyethylene glycol 10 soya sterol and polyethylene glycol 25 soya sterol and the sorbitol derivatives sorbitan monooleate and sorbitan trioleate. The rheological properties of the creams were studied using oscillation stress sweep, oscillation frequency sweep and viscosity tests. Droplet size distribution and conductivity of the creams were also determined. The combination polyethylene glycol 10 soya sterol and sorbitan trioleate yielded the most viscoelastic structure with linearly viscoelastic behaviour.

Waxy corn starch: a potent cofiller in pellets produced by extrusion-spheronization

The purpose of this study was to assess the usefulness of waxy corn (maize) starch as a cofiller and diluent in pellets produced by aqueous extrusion-spheronization. Waxy corn starch was combined with microcrystalline cellulose (MCC) in the range of 20-50% of the entire composition. Pellets containing ordinary corn starch or lactose with MCC were used as reference. The shape of pellets was characterized using an optical microscopic image analysis system. The surface and cross-sectional structure were investigated by means of scanning electron microscopy (SEM). The replacement of ordinary corn starch by waxy corn starch made it possible to increase the amount of starch from 20 to 40%. The pellets containing 50% waxy corn starch were of poorer quality but superior to those containing 30% corn starch. The surface structure became slightly more irregular with respect to the amount of either starch, and a cavity was formed inside the pellet during the spheronization. The origin of starch did not affect the surface structure of the pellets. Waxy corn starch is a potential cofiller: the amount of MCC can be reduced in pellets produced by extrusion-spheronization by using waxy corn starch as a cofiller. This enables the reduction of the manufacturing cost of pellets with low drug load.

Microcrystalline cellulose and its microstructure in pharmaceutical processing

Mercury porosimetry and nitrogen adsorption methods were used in pore structure and pore surface area characterisation of microcrystalline cellulose powder, granules and tablets. The effect of compression on pore structure and surface area of tablets compressed with three different compression pressures of powder and granules was determined. Densification of MCC in wet granulation led to decreased compactibility in tableting. Effects of granulation on the microstructure of microcrystalline cellulose and plastic deformation of powder during compression were detected with nitrogen adsorption, at the diameter range 3-200 nm. Structure of granules was destroyed during tableting when compression pressures of 196 MPa were used. Fragmentation and deformation of granules were observed from the results determined using both methods. Due to different measurement ranges, different theoretical basis of the methods and behaviour of the samples during analysis, results obtained with mercury porosimetry and nitrogen adsorption methods are not strictly comparable. Results obtained with mercury porosimetry give information on the behaviour of powder and granule particles in granulation or compression, whereas nitrogen adsorption brings out the changes in intraparticular structure of particles. The results obtained using these methods together can be used in the characterisation of behaviour of materials in granulation and tableting.

Rheological characterization of microcrystalline cellulose and silicified microcrystalline cellulose wet masses using a mixer torque rheometer

The rheological properties of silicified microcrystalline cellulose (Prosolv 50) were compared with those of standard grades of microcrystalline cellulose (Emcocel 50 and Avicel PH 101). Cellulose samples were analyzed using nitrogen adsorption together with particle size, flowability, density and swelling volume studies. The rheological behaviour of the wet powder masses was studied as a function of mixing time using a mixer torque rheometer (MTR). Silicified microcrystalline cellulose exhibited improved flow characteristics and increased specific surface area compared to standard microcrystalline cellulose grades. Although the silicification process affected the swelling properties and, furthermore, the mixing kinetics of microcrystalline cellulose, the source of the microcrystalline cellulose had a stronger influence than silicification on the liquid requirement at peak torque.

Characterization of particle deformation during compression measured by confocal laser scanning microscopy

Direct compression of riboflavin sodium phosphate tablets was studied by confocal laser scanning microscopy (CLSM). The technique is non-invasive and generates three-dimensional (3D) images. Tablets of 1% riboflavin sodium phosphate with two grades of microcrystalline cellulose (MCC) were individually compressed at compression forces of 1.0 and 26.8 kN. The behaviour and deformation of drug particles on the upper and lower surfaces of the tablets were studied under compression forces. Even at the lower compression force, distinct recrystallized areas in the riboflavin sodium phosphate particles were observed in both Avicel PH-101 and Avicel PH-102 tablets. At the higher compression force, the recrystallization of riboflavin sodium phosphate was more extensive on the upper surface of the Avicel PH-102 tablet than the Avicel PH-101 tablet. The plastic deformation properties of both MCC grades reduced the fragmentation of riboflavin sodium phosphate particles. When compressed with MCC, riboflavin sodium phosphate behaved as a plastic material. The riboflavin sodium phosphate particles were more tightly bound on the upper surface of the tablet than on the lower surface, and this could also be clearly distinguished by CLSM. Drug deformation could not be visualized by other techniques. Confocal laser scanning microscopy provides valuable information on the internal mechanisms of direct compression of tablets.

Effects of process variables on the size, shape, and surface characteristics of microcrystalline cellulose beads prepared in a centrifugal granulator

Preparation of microcrystalline cellulose (MCC) beads with a laboratory-scale centrifugal granulating apparatus was studied, and the pharmaceutical quality of the beads was characterized with respect to the subsequent drug layering. Five process parameters of potential importance, including rotor rotation speed X1, slit air X2, spray air pressure X3, spray air rate X4, and height of nozzle setting X5, were evaluated using a fractional factorial design (FFD 2(5-2)) as the experimental design. The responses evaluated were expected yield, mean size, size distribution, shape characteristics (including roundness, circularity, elongation, rectangularity, and modelx), and friability. All five process parameters studied were found to have an influence on the selected properties of the beads, but the effects of rotor rotation speed, slit air flow rate, and spray air rate were statistically significant (p < .05). The effect of the rotor rotation speed was found to be the most potent on all the responses studied. The results also show some significant interactions between the parameters tested. The most significant interactions were between rotor rotation speed and slit air, rotor rotation speed and spray air, and slit air and spray air.

The effect of compression force on surface structure, crushing strength, friability and disintegration time of erythromycin acistrate tablets

The surface roughness of erythromycin acistrate tablets was studied by non-contact laser profilometry. Seven roughness parameters and 3D fractal dimension were examined. The mechanical properties (including crushing strength, friability and disintegration time) were determined, and SEM data were taken from the tablets. According to the results, the crushing strength and the disintegration time of the tablets increased with increasing compression force. At higher compression forces the crushing strength reached a constant level. The friability of the tablets behaved quite unexpectedly and minimum friability was observed at a compression force of 14 kN. Except for fractal dimension, the roughness parameters behaved very much in the same way as the friability of the tablets. The SEM data supported the friability and surface roughness data of the tablets.

Dependence between dissolution rate and porosity of compressed erythromycin acistrate tablets

The correlation between dissolution rate and porosity of compressed erythromycin acistrate tablets was studied. The total porosity of the tablets, the pore size distribution and the specific surface area of the pores were determined using high-pressure mercury porosimetry. The particle size and specific surface area of the raw material and of the dry granulated mass of the tablets were also determined. The results show that the pore size distribution, showing the differences in pore structure, is more informative than total intruded volume of mercury. However, it is very difficult to explain the dissolution behaviour of erythromycin acistrate tablets only by porosity results of the tablets, and more work is still needed in this field.

Pore structure and surface area of mannitol powder, granules and tablets determined with mercury porosimetry and nitrogen adsorption

Two methods used in pore structure characterisation, mercury porosimetry and nitrogen adsorption, were compared. Pore structure and surface area of mannitol powder, granules produced in wet granulation and tablets compressed with three compression pressures were studied. Greater surface area, more porous structure and greater number of small pores in granules, when compared with powder, increased the compactibility of mannitol granules in tableting. Plastic deformation and fragmentation of powder and granules in compression were observed in volume pore size distributions and surface areas measured with these methods. Pore volume and volume pore size distribution obtained with mercury porosimetry describe densification of mass better than those obtained with nitrogen adsorption. In spite of differences between the methods, the volume pore size distribution curves of samples in the overlapping pore size range had the same shape. The specific surface area of tablets, measured by the nitrogen gas adsorption method described well the deformation under compression. Fragmentation increased the surface area of powder, and plastic deformation decreased the surface area of granules in the pore size range determined. Surface area values measured with mercury porosimetry were larger than those determined with nitrogen adsorption.

Controlled release and dura mater permeability of lidocaine and ibuprofen from injectable poloxamer-based gels

Epidural administration of drugs is becoming more common in the treatment of severe forms of pain. To improve present therapies, a long-acting single-dose gel injection would be beneficial. The present study investigated the use of three different polymers as additives in injectable poloxamer gel in controlling the drug release. The release of lidocaine.HCl and ibuprofen.NA from 25% poloxamer (PO) gel and poloxamer gel with hydroxypropylmethylcellulose (HPMC), sodium carboxymethylcellulose (CMC), or dextran (DE) was studied in vitro. Cellulose additives significantly prolonged ibuprofen release, whereas additives were found to have a slight release-increasing effect on lidocaine as compared with the PO gel. The structural differences of the gels, more than the macroviscosity, seem to regulate the release of drugs. The drug permeation-prolonging effect of the respective gels, along with the control solutions, was evaluated in vitro using porcine dura mater membrane. The compact gel depot acted as the rate-limiting step, and significantly prolonged the dural permeation of both drugs in comparison with control solutions. The difference in the drug release and permeation-reducing effects of the gels demonstrated the possibility for interactions between dural membrane and the gel. The findings are promising for further experimental in vivo animal testing of these injectable poloxamer-based gels.

Controlled release gel of ibuprofen and lidocaine in epidural use--analgesia and systemic absorption in pigs

PURPOSE

Reduction of the frequency of injections and localization of the absorption of drug molecules to the injection site would be of great advantage in epidural pain treatment. The epidural use of a controlled release gel of lidocaine and ibuprofen was studied.

METHODS

The effect of a poloxamer gel (25%) containing 2% lidocaine.HCl and 2% ibuprofen.Na on the duration of analgesia after epidural administration to pigs was compared with drug in solution. Analgesia was assessed by observing the motor function and the nociceptive reflex-withdrawal response to painful pressure stimulation on the feet. Pharmacokinetic and histological examinations were performed.

RESULTS

Analgesia lasted significantly longer after epidural lidocaine gel injection in comparison with the solution. The gel prolonged the systemic absorption, thereby increasing the epidural availability of lidocaine for spinal analgesia. Although the absorption of ibuprofen was prolonged after epidural gel injection, the duration of analgesia as compared with the solution was not prolonged. After epidural injection, only slight inflammatory changes were observed in the tissue structures of the epidural space, but none in the spinal cord.

CONCLUSIONS

These results demonstrate poloxamer gel to be a promising controlled-release, injectable epidural formulation for the management of pain.

Optimization of aqueous-based film coating of tablets performed by a side-vented pan-coating system

The purpose of this research was to characterize the aqueous-based hydroxypropylmethylcellulose (HPMC) film coating of tablets utilizing a laboratory-scale side-vented pan-coating apparatus (Thai coater). The process and apparatus parameters of potential importance with respect to the final film quality were evaluated by using fractional factorial design (2(6-2)IV) and the process was optimized using response surface methodology (central composite design). Rotating speed of the pan was identified as a major parameter with respect to film thickness (weight increase; p < 0.05) and breaking strength (p < 0.05) of the aqueous HPMC film-coated tablets. Increasing the rotating speed from 5 rpm to 10 rpm resulted in a mean relative change of -43.9% and 2.4% of film thickness (weight increase) and breaking strength, respectively. As expected, inlet air temperature significantly affected the moisture content of the final film-coated tablets (p < 0.01) and the film thickness (weight increase; p < 0.05), but the effects on the other responses studied were minimal or negligible. Pneumatic spraying pressure and position of the spray gun (excluding angle of the gun) did not affect the responses studied. The process parameters relevant to a side-vented pan-coating process can be identified (by fractional factorial design) and, consequently, optimized (by central composite design) by using the factorial design approach.