The brain is protected and isolated from the general circulation by a highly efficient blood-brain barrier. This is characterised by relatively impermeable endothelial cells with tight junctions, enzymatic activity and active efflux transport systems. Consequently the blood-brain barrier is designed to permit selective transport of molecules that are essential for brain function. This creates a considerable challenge for the treatment of central nervous system diseases requiring therapeutic levels of drug to enter the brain. Some small lipophilic drugs diffuse across the blood-brain barrier- sufficiently well to be efficacious. However, many potentially useful drugs are excluded. This review provides an insight into the current research into technologies to target small molecules, peptides and proteins to the brain. A brief review of the nature of the blood-brain barrier and its transport mechanisms is provided. Strategies to target and improve transport across the blood-brain barrier include the prodrug-lipidisation approach, sequential metabolism chemical delivery systems, drug-vectors, liposomes and nanoparticles. Included is the discussion of techniques to minimise clearance from the circulation by the reticuloendothelial system in order to extend circulation residence time and optimise the opportunity for interaction between the drug delivery system and the blood-brain barrier.
The TFF, in concentration mode at TMP of 10 psi, is a relatively quick, efficient, and cost-effective technique for purification and concentration of a large nanoparticle batch (>or=200 ml). The DCD technique can be an alternative purification method for nanoparticle dispersions of small volumes.
The purpose of this work was to probe the rate and mechanism of rapid decarboxylation of pyruvic acid in the presence of hydrogen peroxide (H2O2) to acetic acid and carbon dioxide over the pH range 2 – 9 at 25°C, utilizing UV spectrophotometry, high performance liquid chromatography (HPLC), and proton and carbon nuclear magnetic resonance spectrometry (1H, 13C-NMR). Changes in UV absorbance at 220 nm were used to determine the kinetics since the reaction was too fast to follow by HPLC or NMR in much of the pH range. The rate constants for the reaction were determined in the presence of molar excess of H2O2 resulting in pseudo first order kinetics. No buffer catalysis was observed. The calculated second order rate constants for the reaction followed a sigmoidal shape with pH independent regions below pH 3 and above pH 7 but increased between pH 4 and 6. Between pH 4 and 9, the results were in agreement with a change from rate determining nucleophilic attack of the deprotonated peroxide species, HOO−, on the α-carbonyl group followed by rapid decarboxylation at pH values below 6 to rate-determining decarboxylation above pH 7. The addition of H2O2 to ethyl pyruvate was also characterized.
A tangential flow filtration system was evaluated to purify PEGylated nanoparticles. Two widely used surfactants, PVA and sodium cholate were efficiently removed from an empty nanoparticles suspension using the proposed system. During drug loading, surfactant (PVA) was observed to be entrapped within the core of the nanoparticle to a higher extent, hence was purified at a comparatively slower rate. The presence of dextran sulfate enhanced the drug loading but also resulted in reduced purification rate; this was described by the hypothesis of PVA inclusion within the core of the nanoparticles. Practically, it was possible to correlate the slow purification rate of PVA to its reduced filtration flow during the purification of the empty and loaded nanoparticles containing dextran sulfate. Indirectly, this system was capable of revealing the influence of an excipient and drug on the nanoparticle surface.
This article describes drug loading validation of nanoparticles. Ultracentrifugation was avoided because of problems arising from small-sized particles. Ultrafiltration was adopted in two different modes followed by monitoring of polyvinyl alcohol (PVA), dextran sulfate (DS), and loperamide HCl contents. Diafiltration centrifugation removed all PVA at the fourth cycle and provided significantly (p = .000, .017) higher drug loading values compared with tangential flow filtration (TFF). This was due to residual PVA associated with the nanoparticles. TFF enabled satisfactory dry weight recovery (101.66 ± 4.45%, n = 3) of nanoparticles during extended purification. Indirect drug loading (from the purification curve) was not significantly different (p = .450, .487) to the direct drug loading values. Encapsulation parameters were obtained from the purification curve once quantitative estimation of the all formulation components was established.
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