Mass transport in dissolution kinetics. I: Convective diffusion to assess the role of fluid viscosity under forced flow conditions

The quantitative influence of viscosity on dissolution kinetics is assessed under laminar flow conditions by utilizing a convective diffusion model for drug dissolution. Functional dependency of three types of viscosity inducing agents is established with respect to the parameters of fluid flow rate, diffusivity, and solubility. Studies of aqueous solutions of sucrose and of glycerol demonstrate that the decrease in dissolution rate of ethyl p-aminobenzoate is related to the decrease in solute diffusivity in these solutions, whereas the solubility change in the glycerol solutions has an additional independent simultaneous effect. Dissolution in hydroxypropyl cellulose solutions remains constant under fixed fluid flow conditions because of the negligible effect of the polymer upon the drug diffusivity. A change in fluid flow rate, however, alters the dissolution rate and correlates quantitatively with the rate of shear in the convective diffusion model. The interpretation of the effect of viscosity on dissolution kinetics with the convective diffusion model explains these phenomena quantitatively in terms of the fundamental mass transport processes.     

A mechanistic study of danazol dissolution in ionic surfactant solutions

This study examined the dissolution mechanism of the neutral drug danazol into solutions of the ionic surfactant sodium dodecyl sulfate (SDS). The effect of counterion concentration on drug dissolution was also studied by controlling the solution ionic strength (IS). The laminar flow apparatus of Shah and Nelson was chosen to measure in vitro dissolution rates for its simulation of physiological hydrodynamics. A mathematical model was developed to test the proposed mechanism for dissolution. Transport of the dissolved drug away from the tablet surface is the slow step in the process. Two major physicochemical properties, drug solubility in surfactant solutions and the effective diffusion coefficients used in the model, were measured in separate experiments for use in the transport model. Pulsed field proton nuclear magnetic resonance spectroscopy ((1)H NMR) was used to measure the drug diffusion coefficient. Actual drug dissolution rates were determined by multiplying the measured effluent drug concentration in the aqueous medium by its flow rate. The assumption of a transport-controlled dissolution rate was tested by plotting the measured dissolution rates as a function of medium flow rate in a log-log plot. A slope of 1/3 is predicted by the model and slopes of 0.26 to 0.32 were found experimentally, suggesting that the transport controlled mechanism is accurate. The model-predicted dissolution rates were compared with the experimental data. For SDS solutions without IS control, the model calculated data are 20-35% lower than the experimental results, whereas with IS control, the error is only 0.4-4%. We believe that there is significant electrostatic interaction between micelles in processes with low IS or poor IS control. In that situation, the nuclear magnetic resonance (NMR)-measured drug diffusivity would not be its actual value in the dissolution process.     

Controlling the size of alginate gel beads by use of a high electrostatic potential

The effect of several parameters on the size of alginate beads produced by use of an electrostatic potential bead generator was examined. Parameters studied included needle diameter, electrostatic potential, alginate solution flow rate, gelling ion concentration and alginate concentration and viscosity, as well as alginate composition. Bead size was found to decrease with increasing electrostatic potential, but only down to a certain level. Minimum bead size was reached at between 2-4 kV/cm for the needles tested. The smallest alginate beads produced (using a needle with inner diameter 0.18 mm) had a mean diameter of ~300 #181;m. Bead size was also found to be dependent upon the flow rate of the fed alginate solution. Increasing the gelling ion concentration resulted in a moderate decrease in bead size. The concentration and viscosity of the alginate solution also had an effect on bead size as demonstrated by an increased bead diameter when the concentration or viscosity was increased. This effect was primarily an effect of the viscosity properties of the solution, which led to changes in the rate of droplet formation in the bead generator. Lowering the flow rate of the alginate solution could partly compensate for the increase in bead size with increased viscosity. For a constant droplet size, alginates with a low G block content (F GG #44 0.20) resulted in ~30% smaller beads than alginates with a high G block content (F GG #44 0.60). This is explained as a result of differences in the shrinking properties of the beads.     

Controlling the size of alginate gel beads by use of a high electrostatic potential

The effect of several parameters on the size of alginate beads produced by use of an electrostatic potential bead generator was examined. Parameters studied included needle diameter, electrostatic potential, alginate solution flow rate, gelling ion concentration and alginate concentration and viscosity, as well as alginate composition. Bead size was found to decrease with increasing electrostatic potential, but only down to a certain level. Minimum bead size was reached at between 2-4 kV/cm for the needles tested. The smallest alginate beads produced (using a needle with inner diameter 0.18 mm) had a mean diameter of approximately 300 microm. Bead size was also found to be dependent upon the flow rate of the fed alginate solution. Increasing the gelling ion concentration resulted in a moderate decrease in bead size. The concentration and viscosity of the alginate solution also had an effect on bead size as demonstrated by an increased bead diameter when the concentration or viscosity was increased. This effect was primarily an effect of the viscosity properties of the solution, which led to changes in the rate of droplet formation in the bead generator. Lowering the flow rate of the alginate solution could partly compensate for the increase in bead size with increased viscosity. For a constant droplet size, alginates with a low G block content (F(GG) approximately 0.20) resulted in approximately 30% smaller beads than alginates with a high G block content (F(GG) approximately 0.60). This is explained as a result of differences in the shrinking properties of the beads.     

Incorporation of surface-modified dry micronized poorly water-soluble drug powders into polymer strip films

Recent work has established polymer strip films as a robust platform for delivery of poorly water-soluble drugs via slurry casting, in particular using stable drug nanosuspensions. Here, a simpler, robust method to directly incorporate dry micronized poorly water-soluble drug, fenofibrate (FNB), is introduced. As a major novelty, simultaneous surface modification using hydrophilic silica along with micronization was done using fluid energy mill (FEM) in order to reduce FNB hydrophobicity and powder agglomeration. It is hypothesized that silica coating promotes easy, uniform dispersion of micronized and coated FNB (MC-FNB) during direct mixing with aqueous hydroxypropyl methylcellulose (HPMC-E15LV) and glycerin solutions. Uniform dispersion leads to improved film critical quality attributes (CQAs) such as appearance, drug content uniformity and drug dissolution. The impact of polymer solution viscosity (low and high), mixer type (low versus high shear), and FNB surface modification on film CQAs were also assessed. Films with as-received FNB (AR-FNB) and micronized uncoated FNB (MU-FNB) were prepared as control. When MC-FNB powders were used, films exhibited improved appearance (thickness uniformity, visible lumps/agglomerates), better drug content uniformity (expressed as relative standard deviation), fast and immediate drug release, and enhanced mechanical properties (tensile strength, elongation percentage), regardless of the polymer solution viscosity or mixer type. These results compare favorably with those reported using nanosuspensions of FNB, establishing the feasibility of directly incorporating surface modified-micronized poorly water-soluble drug powders in film manufacturing.     

Evaluation of a convective diffusion drug dissolution rate model.

A recently introduced drug dissolution rate model based on convective diffusion was evaluated by experimentally determining dissolution rates. Alkyl p-aminobenzoates were used as the test compounds in a dissolution cell which promoted laminar flow of the liquid past the dissolving surface. The parameters evaluated were diffusivity, solubility, rate of shear, dissolving surface shape, and orientation of the surface relative to flow. The agreement between theory and experiment was quite satisfactory with respect to the functional dependence of the rate on these parameters as well as the actual magnitude of the rates.     

乙酸异丁酸蔗糖酯原位凝胶流变学性质的研究

原位凝胶易于注射,注射后在体内发生相变,迅速转变为药物贮库的传递系统。原位凝胶中一种较好的小分子基质为乙酸异丁酸蔗糖酯(sucroseacetate isobutyrate,SAIB)[1,2],具有良好的生物相容性,在体内可被酶降解并逐渐代谢[3~5],其黏度超过100 Pa·s。与聚合物不同,当浓度高达85%     

Dissolution rate of p-aminobenzoates from solid xylitol dispersions.

Xylitol was studied as a carrier in solid dispersions because of its low melting point and stability up to 180 degrees. It is more stable than sucrose and does not enter into Maillard reactions. Solid dispersions were prepared from esters of p-aminobenzoic acid and xylitol by the melting method and were compressed into tablets. The p-aminobenzoate dissolution rates were determined by a modified beaker method. The increase in the dissolution rates was greatest at the lowest drug levels. When the dispersion drug content exceeded 20-30%, the dissolution rate per unit area remained nearly constant. In the latter case, the increase in the dissolution rate was primarily due to an increase in area. When the carbon chain length was increased in the homologous series, the dissolution rate from the xylitol dispersions showed a nearly linear decrease.     

Quality assessment for sustained release pharmaceutical preparations by dissolution test using microdialysis-HPLC method

Dissolution testing is a core performance test in pharmaceutical development and quality control. The conventional HPLC dissolution method (batch-sampling method) has many steps such as the filtration, collection and replenishment of sample solutions. We previously reported the dissolution test by using microdialysis methods (microdialysis-HPLC method) that can omit many steps. In this study, we investigated whether the microdialysis-HPLC method can be applied to quality assessment for sustained release preparations by a dissolution test. Calcium-channel blockers nifedipine tablets (20 mg) were used, and the test solution used was 0.2 M hydrogen phosphate-citric acid buffer (pH 6.8) with or without 1% sodium lauryl sulfate. In both test solutions, the microdialysis-HPLC method is able to accomplish continuous sampling of sample solutions, and the dissolution behaviors of original nifedipine tablets by the microdialysis-HPLC method were similar to that of the batch-sampling method. In contrast, the dissolution behaviors by the microdialysis-HPLC method were different between original nifedipine tablets and generic products, and the dissolution behaviors in the microdialysis-HPLC method tend to reflect the pharmaceutical design in comparison with the batch-sampling method. In addition, standard deviation in the microdialysis-HPLC method was lower than that of the batch-sampling method. We found that the recovery rate of nifedipine by the microdialysis-HPLC method was increased with the decrease in flow rate through dialysis probe. These findings provide significant information that can be used in pharmaceutical development and quality assessment for original and generic pharmaceutical products, which are sustained release preparations.     

Viscosity of polymer solution phase and other factors controlling the dissolution of theophylline microspheres prepared by the emulsion solvent evaporation method

The objectives of this investigation are to evaluate the effect of the viscosity of polymer solution phase on microsphere properties, especially the drug release characteristics since no studies on this formulation variable have been reported. Also, since it is known that polymer molecular weight affects both the viscosity of the polymer solution and the release properties of microspheres, the interaction of these factors was studied. Microspheres with 33% theoretical drug loading of anhydrous theophylline core material were prepared by the emulsion solvent evaporation method. Two cellulose acetate butyrate polymers, (CAB381-2, CAB381-20), chemically similar but having different molecular weights, were used to prepare different polymer solutions having different apparent viscosities in acetone. A Brookfield viscometer was used to evaluate the viscosities of polymer solutions. Dissolution rates of microspheres prepared from the polymer solutions were inversely related to the initial polymer solution viscosities for both CAB381-2 and CAB381-20. The times for the release of 30 and 50% of the drug from the microspheres have a linear relationship with initial polymer solution viscosity. Initial release was significantly decreased with increasing polymer solution viscosity. Unlike CAB381-2 microspheres which follow Higuchi spherical matrix release kinetics, microspheres prepared from the higher molecular weight polymer (CAB381-20) showed extended release dissolution profiles with near zero order kinetics. It is evident that both the polymer solution viscosity and the molecular weight have an effect on the drug release from microspheres. These results suggest that release rates of matrix microspheres could be predictably optimized by adjusting the viscosity of polymer solutions.     

A comparison of capillary and rotational viscometry of aqueous solutions of hypromellose

A comparison of capillary and rotational viscometry of gentle pseudoplastic solutions of hypromellose (HPMC 4000) by using only single-point value of viscosity is difficult. Single-point comparison becomes topical in consequence to the pharmacopoeial requirement that the apparent viscosity of 2% hypromellose solution should be read at the shear rate of approximately 10 s(-1). This communication is focused on the estimation of the suitable shear rate, D eta, at which the apparent viscosity read using the rotational viscometer is numerically equal to the dynamic viscosity read using a capillary viscometer. For the solutions of HPMC in concentrations up to 2% w/v, the non-linear regression equations generated showed the influencing of the D eta value by the dynamic viscosity and/or by the originally derived linear velocity of the solution flowing through the capillary viscometer tube. To compare the apparent viscosity read using the rotational viscometer with the dynamic viscosity read using capillary viscometer, the exact estimation of the shear rate D eta at which both viscosities are numerically equal is essential since it is markedly affected by the concentration of HPMC solution.     

Evaluation of protein formulation and its viscosity with DSC,DLS, and microviscometer

The viscosity of highly concentrated protein solutions was evaluated using lysozyme as model protein. Viscosity profiles of lysozyme were examined with the effect of buffer and pH-value at various concentrations. The viscosity of lysozyme dissolved in water increased continuously with the concentration as the slope of shear stress against shear rate increased with the concentration. In addition, the viscosity of lysozyme was higher in histidine buffer than in acetate buffer at selected pH ranges. The effect of various excipient concentrations was also investigated in means of unfolding transition temperature (T _m ), viscosity, hydrodynamic size and zeta potential by using differential scanning calorimetry (DSC), microviscometer and dynamic light scattering (DLS). The selected excipients except surfactants increased the viscosity of protein solution with their concentration. Carbohydrates increased the viscosity relatively higher than amino acids and also they increased the conformational stability (T _m ) by enhancing the protein molecule more in compact form. Also amino acids increased the viscosity but decreased the conformational stability since they seemed to be only dispersed in the solution avoiding protein–protein interactions, resulting in a decrease of zeta potential. Consequently, the applied methods—DSC, DLS and microviscometer demonstrated the potential to develop a highly concentrated protein formulation to decrease the high viscosity effect with acceptable conformational stability.     

Influence of physicochemical properties on dissolution of drugs in the gastrointestinal tract

The rate-limiting step to absorption of drugs from the gastrointestinal (GI) tract is often dissolution from the dosage form. Consideration of the Noyes-Whitney dissolution model shows that drug diffusivity, solubility in the gastrointestinal contents, the surface area of the solid wetted by the lumenal fluids and the GI hydrodynamics all play a role in determining the in vivo dissolution rate. Solubility in the GI contents is determined by aqueous solubility, crystalline form, drug lipophilicity, solubilization by native surfactants and co-ingested foodstuffs, and pK(a) in relation to the GI pH profile. Compounds with aqueous solubilities lower than 100 microg/ml often present dissolution limitations to absorption. The dose:solubility ratio of the drug provides an estimate of the volume of fluids required to dissolve an individual dose, and when this volume exceeds 1 l, dissolution is often problematic. The surface area of a drug available for dissolution depends on the particle size of the solid and its ability to be wetted by lumenal fluids. Other physiological factors that can play a role in dissolution include the viscosity of the lumenal contents, through its effect on the diffusivity, and mixing and flow patterns within the gut. In order to better predict in vivo dissolution of drugs, dissolution tests which more adequately simulate the physiological conditions are needed.     

Effect of nicotinamide on the properties of aqueous HPMC solutions

The effect of nicotinamide on the properties of aqueous hydroxypropylmethylcellulose (HPMC) solutions was studied. Rheological studies showed that solutions of HPMC of concentration less than 3.0 w/v.% did not form gels and exhibited Newtonian flow patterns at 25 degrees C. The inclusion of nicotinamide increased the viscosity of HPMC solutions, which indicates that nicotinamide expanded the HPMC coils in aqueous solution. When the temperature of the solutions was raised, they formed gels that were detected by viscometry and oscillation tests as abrupt increases in viscosity, storage modulus and loss modulus and an abrupt decrease in loss angle. Nicotinamide exhibited a salting in effect on the HPMC solutions resulting in an increase in gelation temperatures and cloud points. These effects are considered to be due to the hydrogen-bonding of nicotinamide to HPMC molecules, which was suggested by a shift to a longer wavelength of the UV spectra of aqueous nicotinamide solutions by the addition of HPMC. These results suggested that nicotinamide has affinity with the hydrophilic groups of HPMC.     

Effect of cations and anions on glass transition temperatures in excipient solutions

The purpose of this study was to investigate the effects of cations and anions of various electrolytes on the glass transition temperature (Tg') of frozen solutions of excipients commonly used in freeze-drying. The effect of electrolyte concentration on freezable water content was also investigated by measuring the enthalpy of melting (DeltaH) using Differential Scanning Calorimetry (DSC). Cations and anions induce changes in Tg' of frozen solutions of commonly used parenteral excipients. These changes are dependent on the properties of the excipients used. Tg' values of 5% w/v solutions of maltose, trehalose, sucrose, dextran 40, and polyvinylpyrrolidone (PVP, 17K) were determined as a function of sodium chloride (NaCl) or potassium chloride (KCl) concentrations. In general, a significant decrease in Tg' was observed as a function of increasing the electrolyte concentration. For the disaccharide solutions, the decrease in Tg' due to the addition of NaCl or KCl was similar in magnitude, indicating that changing the cation from K+ to Na+ had no effect on Tg'. However, the decrease in Tg' for the PVP solution due to the addition of KCl was greater than that observed by the addition of NaCl . The differences in the electrolyte-induced changes on Tg' between the disaccharides and PVP may be potentially attributed to the formation of complexes between the cations and the properly oriented hydroxyl groups in the sugars leaving the anions (Cl- ions) to exert their effect on Tg'. While zero cation effect would be consistent with these results for the disaccharides, these results do not mean that the cation effects are zero; they only mean that the cation effects are the same. For the PVP solution, K+ and Na+ ions are not engaged in complex formation with PVP due to the lack of hydroxyl groups. We hypothesize that the structure-breaking K+ ions increase the fluidity of water and exert a greater plasticizing effect on Tg', leading to a more significant decrease in Tg' than the structure-making Na+ ions, which increase the viscosity of water. The decrease in Tg' of frozen solutions of pharmaceutical excipients caused by the addition of electrolytes may be primarily attributed to an increase in the unfrozen plasticizing water surrounding the excipient molecules. Formulation scientists should evaluate the use of electrolytes in the formulation development of lyophilized products containing commonly used excipients. Electrolytes are often needed as stabilizers for protein formulations; however, their selection and use should be properly evaluated. Because electrolytes cause a decrease in Tg' as a function of electrolyte concentration, it is recommended that the minimum electrolyte concentration needed to maintain product stability should be used to minimize the effect of the electrolyte on lowering the Tg'.     

Polysorbate 20 prevents the precipitation of a monoclonal antibody during shear

Monoclonal antibodies (MAbs) are widely used as therapeutic proteins and they are frequently exposed to a high degree of stress during manufacturing or delivery. MAbs shear thin upon increasing shear rates. After undergoing multiple shear cycles, with a cone-and-plate rheometer, the solution viscosity of high concentration antibodies increases due to the formation of insoluble aggregates. These shear-induced insoluble aggregates do not form when polysorbate 20 is present in solution. We hypothesize that monoclonal antibodies form a thin protein layer at the air-water interface. MAbs at the interface expose their hydrophobic core to air leading to unfolding, multiple non-specific intermolecular interactions and, upon continuous high shear, precipitation. Surface tension analysis confirms that monoclonal antibodies are surface active and that polysorbate 20 can prevent their interaction with the air-water interface. In addition, we complement these findings with a viscometer that measures bulk viscosity without the influence of an air-liquid interfacial viscosity and find that the bulk viscosity increases slightly when Mab solutions contained polysorbate 20. These methods of analysis could be used when designing manufacturing systems in which a protein solution is subject to shear forces.     

琼胶流变学性质和胶凝性质的研究

目的研究琼胶的静态流变性质和动态流变性质。方法采用MCR101型流变仪测定流变学性质;质构仪测定胶凝性质。结果与结论琼胶溶液是一种剪切变稀的假塑性流体,其表观粘度随质量分数的增加逐渐增加;温度对琼胶溶液粘度的影响符合Arrhenius模型,琼胶溶液在不同的温度下触变性不同;电解质及蔗糖均会导致溶液的粘度降低。琼胶溶液表现出弱凝胶的特性。琼胶溶液形成的凝胶是一种热可逆的冷致凝胶,其胶凝点远低于熔化点,温差为55℃;凝胶强度在一定的时间区域内,随时间的延长逐渐增大;电解质使琼胶的凝胶强度显著降低,少量蔗糖使琼胶的凝胶强度升高。     

The applicability of sucrose laurate in hot-melt technology

Nowadays, one of the most important task of the pharmaceutical technology is to optimize the dissolution of active ingredients, because most of the drug candidates have a poorly water solubility and hence a slow absorption. According to the latest examinations, the bioavailability of poorly water soluble drugs can be increased significantly by using surfactants or the mixture of surfactants and polymers. Nowadays, surfactants (like polysorbates) are generally used in the production of solid dispersions, so the use of surface-active sucrose esters can be resulted an innovative solution in the pharmaceutical technology. The aim of our investigation was to examine the applicability of sucrose laurate in hot-melt technology in order to influence the crystalline structure and dissolution rate of a poorly water soluble drug (gemfibrosil) having low-melting point. The results of the X-ray powder diffractometry have showed that the sucrose laurate had no significant effect on the crystallization degree of the drug which is important in case of the stability. On the bases of the results of in-vitro dissolution studies, it can be concluded that the sucrose laurate (using minimum 5%) can be well applied in hot-melt technology with carriers having characteristic melting point (e.g. Macrogol) to increase the dissolution rate of poorly soluble drugs.     

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.     

Performance of the vibrating membrane aerosol generation device: Aeroneb Micropump Nebulizer.

The output and particle size distribution of several series of aqueous solutions were measured to define quantitatively the practical limits of the solution properties acceptable for aerosol production by the aeroneb micropump nebulizer. Aerosol output measurements were made gravimetrically and the particle size distributions were obtained by laser diffractometry. Solution properties were obtained from the literature by interpolation of the best-fit curve of the property plotted as a function of composition. For nonionic solutes, addition of sodium chloride dramatically increased the output rate and also decreased the droplet size at low solute concentrations. Increasing viscosity also caused a significant decrease in output. Cesium chloride displayed increased output rate with concentration due to the rising density. Based on calculations with the number of apertures and oscillatory frequency, low output rates appeared to be a consequence of apertures failing to produce a droplet with each oscillation. Overall, ionic strength, density, surface tension, and viscosity affected the output rate in a manner that can be now empirically predicted.