Andreas Buthe

pH-optima in lipase-catalysed esterification

Though lipases are frequently applied in ester synthesis, fundamental information on optimal pH or substrate concentration, can almost only be found for the reverse reaction – hydrolysis. This study demonstrates that the pH-optima of lipase-catalysed esterifications differ significantly from the optima of the hydrolysis reaction. In the esterification of n-butanol and propionic acid with lipases of Candida rugosa (CRL) and Thermomyces lanuginosa (TLL) pH-optima of 3.5 and 4.25, respectively, were found. This is about 3–4 units (CRL) and 7 units (TLL) in pH lower than optimum for hydrolysis. Enzyme activity increased with increasing concentrations of protonated acid indicating that the protonated acid rather than the deprotonated form is substrate for esterification. The rate of esterification can be drastically increased by ensuring acid concentrations up to 1000 mmol L−1 for CRL and 600 mmol L−1 for TLL in the reaction system.

Novel solvent-based method for preparation of alginate beads with improved roundness and predictable size.

Attempts to determine conditions or processes within alginate gel beads often suffer from inaccuracies due to an improper roundness of the analysed beads. Therefore, a novel solvent-based method for the preparation of alginate beads with improved shape was developed: An aqueous solution of 2% (w/v) alginate in water was injected into a solvent layering consisting of hexane, n-butanol, n-butanol with 1% (w/v) CaCl2 and finally 2% (w/v) CaCl2 in water. Beads of up to 3.5 mm in diameter obtained with this method had a roundness which was ∼5% better than comparable beads prepared by dropping an alginate solution into a CaCl2-hardening bath. This was determined by a software supported quantitative analysis of bead size and shape. Additionally, the novel solvent-based method allows for highly reproducible preparation of alginate beads with exactly predictable sizes. The biggest beads obtained with this method were 9 mm in diameter. Thus, with the solvent-based preparation of alginate beads it is now possible to easily obtain beads of exactly the type needed for a specific analytical purpose.

Encapsulation of synthetically valuable biocatalysts into polyelectrolyte multilayer systems.

Layer-by-Layer (LbL) technology recently turned out to be a versatile tool for the encapsulation of bioactive entities. In this study, the factual potential of this technology to encapsulate synthetically valuable biocatalysts, that is enzymes and whole cells expressing a specific catalytic activity, was investigated. The biocatalysts were embedded into a polyelectrolyte multilayer system involving poly(allylamine) hydrochloride (PAH) and poly(styrene sulfonate) sodium salt (PSS). The enzymes were adsorbed to CaCO3 or DEAE-cellulose previous to encapsulation. A slight increase (32%) of the catalytic performance was observed for lipase B from Candida antarctica when four layers of polyelectrolytes were applied. On the whole, however, the residual activity of the investigated enzymes after encapsulation was rather low. Similar results were obtained with whole-cell biocatalysts. It was found that the activity decrease can be attributed to mass transfer restrictions as well as direct interactions between polyelectrolytes and catalytically active molecules. Both effects need to be understood in more detail before LbL technology can be advanced to technically efficient biocatalysis.

Lipase-catalysed synthesis of ester oils from biodiesel by-products

Ester oils obtained from natural long-chain fatty acids and alcohols are versatile substitutes for many petroleum-based products. Their efficient synthesis with the solvent-free esterification of free fatty acids (FFA) from by-products of biodiesel fabrication and 2-ethyl-1-hexanol with immobilised lipase from Thermomyces lanuginosa was investigated. The immobilisation of the biocatalyst in static emulsion yielded a specific esterification activity that was higher by a factor of 4.9–9.4 than the activity of the native enzyme. Favourable properties of the silicone-based immobilisation matrix in terms of stability and immobilisation yield were observed. In biodiesel by-products, the immobilised lipase catalysed the esterification of FFA as well as the transesterification of residual fatty acid methyl esters (FAME) to the desired ester oils. A conversion of 90% FFA and 35% FAME gave a total yield of 60%. The inactivation coefficients during repeated use in a stirred-tank reactor with intermittent pressure reduction were exceptionally low.