Dimerisation of N-acetyl-L-tyrosine ethyl ester and Aß peptides via formation of dityrosine

Alzheimer's disease (AD) is characterised by the formation of amyloid deposits composed primarily of the amyloid β-peptide (Aβ). This peptide has been shown to bind redox active metals ions such as copper and iron, leading to the production of reactive oxygen species (ROS) and formation of hydrogen peroxide (H2O2). The generation of H2O2 has been linked with Aβ neurotoxicity and neurodegeneration in AD. Because of the relative stability of a tyrosyl radical, the tyrosine residue (Tyr-10) is believed to be critical to the neurotoxicity of Aβ. This residue has also been shown to be important to Aβ aggregation and amyloid formation. It is possible that the formation of an Aβ tyrosyl radical leads to increased aggregation via the formation of dityrosine as an early aggregation step, which is supported by the identification of dityrosine in amyloid plaque. The role of dityrosine formation in Aβ aggregation and neurotoxicity is as yet undetermined, partly because there are no facile methods for the synthesis of Aβ dimers containing dityrosine. Here we report the use of horseradish peroxidase and H2O2 to dimerise N-acetyl-l-tyrosine ethyl ester and apply the optimised conditions for dityrosine formation to fully unprotected Aβ peptides. We also report a simple fluorescent plate reader method for monitoring Aβ dimerisation via dityrosine formation.

Transesterification of fish oil to produce fatty acid ethyl esters using ultrasonic energy

This study evaluated the production of fatty acid ethyl esters from fish oil using ultrasonic energy and alkaline catalysts dissolved in ethanol. The feasibility of fatty acid ethyl ester production was determined using an ultrasonic bath and probe, and between 0.5 and 1% KOH (added to the fish oil). Furthermore, factors such as ultrasonic device (bath and probe), catalyst (KOH and C2H5ONa), temperature (20 and 60 °C), and duration of exposure (10–90 min) were assessed. Sodium ethoxide was found to be a more efficient catalyst than KOH when transesterifying fish oil. Ultrasonic energy applied for greater than 30 min at 60 °C using 0.8% of C2H5ONa as a catalyst transesterified over 98% fish oil triglycerides to fatty acid ethyl esters. It is reasonable to conclude that the yield of fatty acid ethyl esters produced by applying ultrasonic energy to fish oil is related to the sonication time. Due to increases in the surface area contact between the reactants and the catalyst, ultrasonic energy has the potential to reduce the production time required by a conventional large-scale commercial transesterification method that uses agitation as a way of mixing.

Weak intermolecular interactions in sulfonamide salts : structure of 1-ethyl-2-methyl-3-benzyl imidazolium bis[(trifluoromethyl)sulfonyl]amide

The crystal structure of a 1,2,3-trisubstituted imidazolium salt of the bis[(trifluoromethyl)sulfonyl)]amide ion is presented; this salt is a prototype for similar, room temperature liquid, imidazolium salts; the structure shows that the anion and cation interact weakly, with little if any hydrogen bonding present.

Synthesis of ethyl acetate employing celite-immobilized lipase of Bacillus cereus MTCC 8372

A wide range of fatty acid esters can be synthesized by esterification and transesterification reactions catalyzed by lipases in non-aqueous systems. In the present study, immobilization of a purified alkaline extra-cellular lipase of Bacillus cereus MTCC 8372 by adsorption on diatomaceous earth (celite) for synthesis of ethyl acetate via transesterification route was investigated. B. cereus lipase was deposited on celite (77% protein binding efficiency) by direct binding from aqueous solution. Immobilized lipase was used to synthesis of ethyl acetate from vinyl acetate and ethanol in n -nonane. Various reaction conditions, such as biocatalyst concentration, substrates concentration, choices of solvents ( n -alkanes), incubation time, temperature, molecular sieves (3Å × 1.5 mm), and water activity(a _w ), were optimized. The immobilized lipase (25 mg/ml) was used to perform transesterification in n -alkane(s) that resulted in approximately 73.7 mM of ethyl acetate at 55 °C in n -nonane under shaking (160 rpm) after 15 h, when vinyl acetate and ethanol were used in a equimolar ratio (100 mM each). Addition of molecular sieves (3Å × 1.5 mm) as well as effect of water activity of saturated salt solutions (KI, KCl and KNO ₃ ) to the transesterification efficiency has inhibitory effect. Batch operational stability tests indicated that immobilized lipase had retained 50% of its original catalytic activity after four consecutive batches of 15 h each.

Synthesis of ethyl oleate employing synthetic hydrogel-immobilized lipase of Bacillus coagulans MTCC-6375

Ten polymeric hydrogels were chemically synthesized by varying the concentrations of copolymer (DMA) and cross-linker (MBAm) molecules. An alkaline lipase of Bacillus coagulans MTCC-6375 was immobilized onto a poly (MAc-co-DMA-cl-MBAm)-hydrogel support at pH 8.5 and temperature 55ºC in 16 h. The bound lipase possessed 7.6 U.g⁻¹ (matrix) lipase activity with a specific activity of 18 U.mg⁻¹ protein. Hydrogel bound-lipase catalyzed esterification of oleic acid and ethanol to synthesize ethyl oleate in n-nonane. Various kinetic parameters were optimized to produce ethyl oleate using immobilized lipase. The optimal parameters were bound enzyme/substrate (E/S) ratio 0.62 mg/mM, ethanol/oleic acid 100 mM:75 mM or 100 mM:100 mM, incubation time 18 h and reaction temperature 55ºC that resulted in approximately 53% conversion of reactants into ethyl oleate in n-nonane. However, addition of a molecular sieve to the reaction mixture promoted the conversion to 58% in 18 h in n-nonane, which was equivalent to 55 mM of ethyl oleate produced.

Synthesis of ethyl laurate by hydrogel immobilized lipase of Bacillus coagulans MTCC-6375

An alkaline thermo-tolerant lipase from Bacillus coagulans MTCC-6375 was purified and efficiently immobilized onto a synthetic hydrophobic poly (MAc-co-DMA-cl-MBAm)-hydrogel at pH 8.5 and temperature 55°C in 16 h. The hydrogel bound matrix possessed 7.6 IU g -1 matrix lipase activity with a specific activity of 18 IU mg -1 protein. Immobilized lipase was used to catalyze the esterification of lauric acid and ethanol to produce ethyl laurate in n-nonane. The reaction conditions that were optimized to produce ethyl laurate in n-nonane included enzyme/substrate (E/S) ratio, substrate concentration, reaction time and reaction temperature. The optimized parameters were E/S ratio of 0.5 mg mM -1, ethanol:lauric acid in ratio of 100 mM:100 mM and reaction time of 15 h at 65°C under continuous shaking (200 rpm). Optimized conditions resulted in 66% conversion of reactants into ethyl laurate in n-nonane in the presence of 300 mg molecular sieve mL -1 reaction mixture.