Effect of additives on gas-phase catalysis with immobilised Thermoanaerobacter species alcohol dehydrogenase (ADH T)

This paper presents a strategy for preparing an efficient immobilised alcohol dehydrogenase preparation for a gas-phase reaction. The effects of additives such as buffers and sucrose on the immobilisation efficiency (residual activity and protein loading) and on the gas-phase reaction efficiency (initial reaction rate and half-life) of Thermoanaerobacter sp. alcohol dehydrogenase were studied. The reduction of acetophenone to 1-phenylethanol under in situ cofactor regeneration using isopropanol as co-substrate was used as a model reaction at fixed reaction conditions (temperature and thermodynamic activities). A strongly enhanced thermostability of the enzyme in the gas-phase reaction was achieved when the enzyme was immobilised with 50 mM phosphate buffer (pH 7) containing sucrose five times the protein amount (on weight/weight basis). This resulted in a remarkable productivity of 200 g L(-1) day(-1) even at non-optimised reaction conditions. The interaction of additives with the enzyme and water affects the immobilisation and gas-phase efficiencies of the enzyme. However, it was not possible to predict the effect of additives on the gas-phase reaction efficiency even after knowing their effect on the immobilisation efficiency.

Synthesis of enantiopure (5R)-hydroxyhexane-2-one with immobilised whole cells of Lactobacillus kefiri

Whole-cell reduction of (2,5)-hexanedione to yield highly enantiopure (5R)-hydroxyhexane-2-one (enantiomeric excess >99%) with Lactobacillus kefiri DSM 20587 was investigated. Cell immobilisation with sodium cellulose sulphate was chosen as the most suitable encapsulation matrix, giving an immobilisation yield of 40%. Despite the lowered biocatalytic activity from cell immobilisation, the bioreduction process was vastly improved with the help of reaction engineering techniques (batch to a plug flow reactor set-up). High selectivity (95%) and space-time yield (87 g L(-1) day(-1)) were achieved in the plug flow reactor. The biocatalyst remained active (68% residual activity) after 6 days of operation.

Purification and characterization of an alcohol:N,N-dimethyl-4-nitrosoaniline oxidoreductase from the methanogen Methanosarcina barkeri DSM 804 strain Fusaro

Cell-free extracts of Methanosarcina barkeri DSM 804 showed alcohol dehydrogenase activity under aerobic conditions when N,N-dimethyl-4-nitrosoaniline (NDMA) was used as an artificial electron acceptor. The NDMA-dependent alcohol dehydrogenase (NDMA-ADH) was purified to approximate homogeneity by column chromatography. It is most probably a homodimeric enzyme consisting of subunits of 45 kDa, the native molecular mass estimated by gel filtration being about 87 kDa. The purified protein had an isoelectric point of 4.3. It possesses a tightly but noncovalently bound NADP(H) cofactor. Each subunit contains 1 mol NADP(H)/mol, about 2 mol Zn2+/mol and significant amounts of magnesium. The purified enzyme preferably oxidized primary alcohols (including benzyl alcohol). NDMA-ADH from M. barkeri also catalyzed the stoichiometric dismutation of aldehydes, especially higher aliphatic aldehydes, to form equimolar amounts of the corresponding alcohol and acid without addition of an electron carrier. The enzyme did not catalyze the dehydrogenation of methanol or the disproportionation of formaldehyde and therefore is not directly involved in methanogenesis. An alignment of the N-terminal amino acid sequence of the enzyme with the sequences of other alcohol dehydrogenases from methanogenic and nonmethanogenic bacteria indicated no significant identity. Nevertheless there was a quite interesting sequence similarity in the first 30 N-terminal amino acids to plant cinnamyl alcohol dehydrogenase. NDMA-ADH from M. barkeri is a novel type of alcohol dehydrogenase in methanogenic bacteria.