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Biomedical subjects

S L Nail

Publications and source records attributed to S L Nail.

At least 19 recordsLinked to original sources

Design and application of a low-temperature Peltier-cooling microscope stage.

A light microscopy system has been designed for freezing and lyophilization studies of protein pharmaceuticals. The system consists of a cascade of four Peltier thermoelectric modules in the lyophilization cell to freeze samples to -60 degrees C, controllers to regulate temperature and pressure conditions, and a video camera to record the events under study. Specific demonstration of the system was conducted using recombinant CD4-IgG and human growth hormone (hGH) as model proteins. Observations of recrystallization during warming of frozen CD4-IgG solution and lyophilization of hGH solution are discussed. These examples demonstrate that the system is a useful tool for the fundamental understanding of freezing and lyophilization of protein pharmaceuticals.

CD4 Antigens

Glycine crystallization during freezing: the effects of salt form, pH, and ionic strength.

PURPOSE: The purpose of the study is to characterize glycine crystallization during freezing of aqueous solutions as a function of the glycine salt form (i.e., neutral glycine, glycine hydrochloride, and sodium glycinate), pH, and ionic strength. METHODS: Crystallization was studied by thermal analysis, microscopy, x-ray diffraction, and pulsed Fourier transform nmr spectroscopy. RESULTS: A solution of neutral glycine with no additives undergoes rapid secondary crystallization during freezing, forming the beta polymorph, with a eutectic melting temperature of -3.4 degrees C. Glycine hydrochloride solutions undergo secondary crystallization relatively slowly, and the eutectic melting temperature is -28 degrees C. Sodium glycinate crystallizes from frozen solution at an intermediate rate, forming a eutectic mixture with a melting temperature of -17.8 degrees C. Where secondary crystallization does not occur rapidly, a complex glass transition is observed in the -70 degrees to -85 degrees C temperature range in the DSC thermograms of all systems studied. Rates of secondary crystallization and the type of crystal formed are influenced by solution pH relative the the pKs of glycine, and also by the change in ionic strength caused by adjustment of pH. Increased ionic strength significantly slows the crystallization of neutral glycine and promotes formation of the gamma polymorph. Thermal treatment or extended holding times during the freezing process may be necessary in order to promote secondary crystallization and prevent collapse during freeze drying. CONCLUSIONS: The results underscore the importance of recognizing that seemingly minor changes in formulation conditions can have profound effects on the physical chemistry of freezing and freeze drying.

Calorimetry, Differential Scanning

Electrolyte-induced changes in glass transition temperatures of freeze-concentrated solutes.

Addition of electrolytes to solutions of non-crystallizing solutes can cause a significant decrease in the glass transition temperature (Tg') of the maximally freeze-concentrated solution. For example, addition of 2% sodium chloride to 10% solutions of dextran, PVP, lactose, and sucrose causes a decrease in Tg' of 14 degrees to 18 degrees C. Sodium phosphate has a smaller effect on Tg' and is unusual in that 1% to 2% sodium phosphate in 10% PVP causes a second glass transition to be observed in the low-temperature thermogram, indicating a phase separation in the freeze concentrate. Comparison of DSC thermograms of fast-frozen solutions of sucrose with and without added sodium chloride shows that electrolyte-induced reduction of Tg' is not caused by a direct plasticizing effect of the electrolyte on the freeze concentrate. Measurement of unfrozen water content as a function of temperature by a pulsed nmr method shows that the most likely mechanism for electrolyte-induced changes in Tg' is by increasing the quantity of unfrozen water in the freeze concentrate, where the unfrozen water acts as a plasticizer and decreases Tg'. The correlation time (tau c) of water in the freeze concentrate is in the range of 10(-7) to 10(-8) seconds. The results underscore the importance of minimizing the amount of added salts to formulations intended for freeze drying.

Calorimetry, Differential Scanning

The effect of bulking agent on the solid-state stability of freeze-dried methylprednisolone sodium succinate.

The rate of hydrolysis of methylprednisolone sodium succinate in the freeze dried solid state at 40 degrees C was determined in the presence of two common bulking agents--mannitol and lactose--at two different ratios of drug to excipient. Residual moisture levels were less than 1% in all samples tested, with no significant difference in residual moisture among different formulations. Rate of hydrolysis was significantly higher in mannitol-containing formulations versus lactose-containing formulations, and the rate of hydrolysis increases with increasing ratio of mannitol to drug. Thermal analysis and x-ray diffraction data are consistent with a composition-dependent rate of crystallization of mannitol in the formulation and its subsequent effect on distribution of water in the freeze-dried matrix. Increased water in the microenvironment of the drug decreases the glass transition temperature of the amorphous phase, resulting in an increased rate of reaction. The physical state of lactose remained constant throughout the duration of the study, and the rate of hydrolysis was not significantly different from the control formulation containing no excipient. Thermal analysis and x-ray diffraction data are consistent with formation of a liquid crystal phase in freeze-concentrated solutions of methylprednisolone sodium succinate containing no excipient.

Calorimetry, Differential Scanning

An improved microscope stage for direct observation of freezing and freeze drying.

A microscope stage for observation of freezing and freeze drying is described. The stage uses thermoelectric (Peltier) heaters configured in two stages, with circulating fluid as a heat sink on the high temperature side. Lowest attainable sample temperature is about -47 degrees C. Principal advantages of this system are closed-loop control of stage temperature, rapid response to changes in temperature set point, and improved documentation of experiments by use of a video recorder system with a character generator which allows display of sample identity and temperature. Accuracy of measuring the sample temperature in the field of view was validated by comparing observed values of eutectic melting with published values for a series of solutes with eutectic temperatures in the range from -2 degrees C to -32 degrees C. Good agreement was obtained throughout this range.

Freeze Drying

Measurement of glass transition temperatures of freeze-concentrated solutes by differential scanning calorimetry.

Thermal analysis of aqueous solutions in which the solute does not crystallize immediately upon freezing was carried out to define the effects of experimental parameters on thermograms in the glass transition region. The intensity of enthalpy relaxations in the glass transition region is related to both the rate of cooling and the rate of heating through the glass transition region--slow cooling or slow heating increases the extent of structural relaxation in the glassy state and increases the intensity of the endotherm. Plots of the logarithm of heating rate versus 1/Tg' are linear, and activation enthalpies for structural relaxation are in the range of 210-350 kJ/mol. For polymeric solutes, both the activation enthalpies for structural relaxation and the heat capacity change accompanying the glass transition increase with increasing molecular weight of the solute. Molecular weight dependence of the observed midpoint of the glass transition agrees with the Fox-Flory relationship. Results are compared and contrasted with glass transitions in solid polymers and with the glass transition of hyperquenched water. Practical implications for characterization of formulations intended for freeze-drying are discussed.

Calorimetry, Differential Scanning

Measurement of glass transition temperatures in freeze concentrated solutions of non-electrolytes by electrical thermal analysis.

The electrical resistance (R) of frozen aqueous solutions was measured as a function of temperature in order to determine whether this technique can be applied for determination of glass transition temperatures of maximally freeze concentrated solutions (Tg') of non-electrolytes which do not crystallize during freezing. Electrical thermal analysis (ETA) thermograms of frozen solutions containing the solute alone show a gradual change in slope over the temperature range of interest, with no inflection point which corresponds to Tg'. However, addition of low levels (about 0.1%) of electrolyte changes the shape of the thermogram into a biexponential function where the intersection of the two linear portions of the log (R) vs. T plot corresponds to the glass transition region. The total change in log (R) over the temperature range studied increases as the ionic radius of the reporter ion increases. The sharpest inflection points in the log (R) vs T curves, and the best correlation with DSC results, were obtained with ammonium salts. Tg' values measured by ETA were compared with values measured by DSC. DSC thermograms of solutes with and without electrolyte (0.1%) show that the electrolyte decreases Tg' by about 0.5 to 1.0 degrees C. However, Tg' values measured by ETA are somewhat higher than those measured by DSC, and difference between the two methods seems to increase as Tg' decreases. Tg' as measured by ETA is less heating rate dependent than DSC analysis, and ETA is a more sensitive method than DSC at low solute concentrations and at low heating rates.(ABSTRACT TRUNCATED AT 250 WORDS)

Calorimetry, Differential Scanning

Protein purification process engineering. Freeze drying: A practical overview.

Freeze drying provides a valuable tool to the formulation scientist by permitting dehydration of heat-sensitive drugs and biologicals at low temperature. The final product is quickly and easily reconstituted, and the process is compatible with aseptic operations. Freezing is a critical step, since the microstructure established by the freezing process usually represents the microstructure of the dried product. The product must be frozen to a low enough temperature to be completely solidified. If the solute crystallizes during freezing, this temperature is the eutectic temperature. If the solute remains substantially amorphous with freezing, the relevant temperature is the collapse temperature. Understanding the physical form of the solute--crystalline or amorphous--after freezing can be important from the standpoint of drying characteristics, appearance of the final product, and even product stability during storage. Supercooling is a significant factor in freezing of formulations intended for freeze drying--prior to both primary and secondary (eutectic) crystallization. The driving force for freeze drying is the difference in vapor pressure of ice between the sublimation zone and the condenser. Because the vapor pressure of ice increases sharply with increased product temperature, it is important from the standpoint of process efficiency to maintain product temperature as high as possible during primary drying without damaging the product. The upper limit of product temperature during primary drying again depends on the physical form of the solute. Exceeding either the eutectic temperature (crystalline solute) or the collapse temperature (amorphous solute) results in loss of the desirable properties of a freeze dried product. Freeze drying is a coupled heat and mass transfer process, where either heat transfer or mass transfer may be rate limiting with respect to the overall drying rate. Heat transfer is often the rate-limiting transfer operation because of the high heat of sublimation of ice and the inefficiency of heat transfer. Conduction is the primary mechanism of heat transfer, as opposed to convection or thermal radiation. The rate-limiting resistance to heat transfer is usually the interfacial, or contact, resistance caused by poor contact between materials--the heated shelf, metal trays, and the bottom surface of glass vials. Since the thermal conductivity of a gas is directly proportional to pressure in the free molecular flow regime, the chamber pressure during primary drying is an important determinant of the overall heat transfer rate. As a result, the drying rate for a heat transfer-limited process increases sharply with chamber pressure up to a pressure where free molecular flow conditions no longer apply.(ABSTRACT TRUNCATED AT 400 WORDS)

Biotechnology

Methodology for in-process determination of residual water in freeze-dried products.

The integrity of freeze-dried biological products after reconstitution, as well as their stability during storage, is often more sensitive to small variations in residual moisture level than traditional low molecular weight drugs. Susceptibility to over-drying has also been documented for biological products. This places additional demands on the quality of in-process monitoring to achieve the desired level of residual water. This discussion is a critical overview of methodology for in-process moisture determination, including product temperature measurement, comparative pressure measurement, pressure rise, and residual gas analysis. Advantages and limitations of these methods are discussed.

Biological Products

Strategies in the design of solution-stable, water-soluble prodrugs II: properties of micellar prodrugs of methylprednisolone.

In a previous study, a physical-organic approach to the design of solution-stable, water-soluble prodrugs of the corticosteroid methylprednisolone was outlined, and several 21-esters were synthesized to test the approach. Compounds exhibiting dilute solution stabilities approaching 2 years at 25 degrees C were reported. A complicating factor in more concentrated aqueous solutions of water-soluble prodrugs, however, is the limited extent to which hydrolysis can occur before the solution becomes saturated with respect to the relatively insoluble parent drug. In this study the advantages of micellar prodrugs as water-soluble delivery systems for parenteral administration of relatively insoluble parent drugs are explored. Micellar prodrugs, besides being highly water soluble, have additional advantages in that their micelles solubilize poorly soluble degradation products which may otherwise precipitate and may act as a self-stabilizing influence due to protection of the hydrolytically labile prodrug linkage within the micelle interior. Two 21-esters of methylprednisolone previously identified as having promising dilute solution stability have now been shown to self-associate in aqueous solution at higher concentrations, as determined by solubility, kinetic, and light-scattering measurements. One consequence of self-association is that free methylprednisolone, the product of prodrug hydrolysis, is solubilized in concentrated prodrug formulations. In addition, acid- and base-catalyzed hydrolysis rate constants are altered in the micelles, resulting in further prolongation of shelf life in concentrated solutions. Due to the added benefits of self-micellization, the water-soluble 21-esters investigated exhibit shelf lives exceeding 2 years at 30 degrees C, the upper limit of the controlled room temperature range.

Chemistry, Pharmaceutical

Stability of methylprednisolone sodium succinate in small volumes of 5% dextrose and 0.9% sodium chloride injections.

The stability of methylprednisolone sodium succinate in small volumes of 5% dextrose and 0.9% sodium chloride injections was studied. Vials of methylprednisolone sodium succinate (125-3000 mg) were reconstituted and added to 50- and 100-ml volumes of the two diluents. These piggyback solutions were visually inspected for the development of haze over a 24-hour period. A nephelometer was used to quantitate the development of turbidity with time. The effect of pH on haze formation was investigated, and infrared spectroscopy was used to identify the haze. Nephelometer readings were found to correlate well with visual inspections. The haze was identified as being formed by the precipitation of free methylprednisolone. The rate of change of turbidity was directly related to the pH. A 1.4-3.2 percentage-point increase in the free methylprednisolone concentration secondary to hydrolysis over the 24-hour period was noted. The duration of stability was variable among the investigated lots and concentrations. Nineteen of the 24 admixtures stored at room temperature remained stable and free of visible haze for at least 12 hours after preparation. For all dosage strengths of methylprednisolone sodium succinate studied, these data indicate that solutions can be made stable for at least 12 hours by selecting the appropriate volume of diluent.

Drug Packaging

IR studies of development of order in aluminum hydroxide gels.

The usefulness of deuteration in detecting the development of order in aluminum hydroxide gel by IR spectra is demonstrated. By treatment of gel samples with deuterium oxide vapor at room temperature, the relative ease with which deuteroxyl-hydroxyl exchange takes place is determined as a function of the age of the gel. The use of scale expansion in conjunction with deuteration allows detection of IR absorbance characteristic of gibbsitic material long before such detection is possible by conventional IR analysis or X-ray diffraction.

Aluminum Hydroxide

Structure of aluminum hydroxide gel I: initial precipitate.

The initial aluminum hydroxide gel precipitate resulting from the reaction of aluminum chloride or aluminum sulfate with ammonium hydroxide is shown by potentiometric titration, chemical analysis, and the ratio of bound hydroxide to aluminum to fit a polymer model described previously. The formation of polynuclear hydroxyaluminum particles is treated as a stepwise process involving a deprotonation-dehydration mechanism, which results in the formation of six-membered rings; these rings may further coalesce by the same mechanism. The aluminum hydroxide gel precipitated from aluminum chloride can be represented by the formula Al(OH)2.55(Cl)0.45 and probably exists as a polymer of 10 fused six-membered rings. The aluminum hydroxide gel precipitated from aluminum sulfate can be represented by the formula Al(OH)2.30(SO4)0.35. This species probably exists as a polymer of three fused six-membered rings.

Aluminum

Structure of aluminum hydroxide gel II: aging mechanism.

The aging of aluminum hydroxide gel prepared by the reaction of aluminum chloride and ammonium hydroxide was studied by measurement of pH, acid-consuming capacity, hydroxide to aluminum ratio, chloride activity, and X-ray line broadening. The results were consistent with a polymer model involving particle growth by a deprotonation-dehydration mechanism. Anions inhibit this reaction by binding to the positively charged edges of the hydroxyaluminum polymers.

Aluminum Hydroxide

Structure of aluminum hydroxide gel III: mechanism of stabilization by sorbitol.

The effect of sorbitol on the aging of aluminum hydroxide gel, prepared by the reaction of aluminum chloride solution with strong ammonia solution to a final pH of 7.0, was studied by potentiometric titration, acid-consuming capacity, pH, hydroxide to aluminum ratio, chloride activity, X-ray diffraction, and IR spectroscopy. Gels containing sorbitol lost less than 10% of their acid-consuming capacity during a 6-month aging period compared with a loss of more than 60% for an identical gel without sorbitol. The mechanism by which sorbitol stabilizes the gel appears to be inhibition of the secondary polymerization reaction which takes place upon aging. Another polyhydroxy compound, quercetin, also stabilizes aluminum hydroxide gel.

Aluminum Hydroxide

Kinetics of acid neutralization by aluminum hydroxide gel.

The rate of acid neutralization by an aluminum hydroxide gel prepared by the reaction of aluminum chloride solution and strong ammonia solution was studied. The decrease in acid-consuming capacity during aging as measured by the USP test is due to a decrease in the rate of reaction rather than to a decrease in equilibrium reactivity. The reactivity profile has three phases, which are shown to be related to the structure of the gel. The rate of loss of reactivity is directly related to the extent of washing.

Aluminum Hydroxide

Differential thermal analysis of aluminum hydroxide gel.

The development of order during the aging of aluminum hydroxide gel prepared by the reaction of aluminum chloride and ammonium hydroxide to a final pH of 7.0 can be monitored by differential thermal analysis. The loss of acid reactivity upon aging is accompanied by an increase in the temperature and intensity of the dehydroxylation endotherm and an accompanying decrease in the intensity of the water of hydration endotherm. With continued aging, the thermogram develops the characteristics of a crystalline aluminum hydroxide.

Aluminum Hydroxide