Dissolving carbon dioxide in high viscous substrates to accelerate biocatalytic reactions.

Solvent free biotransformation of polyglycerol-3 and lauric acid yields polyglycerol-3-laurate and water. This conversion can be catalyzed by Novozym 435. However, the performance is limited by the viscosity of polyglycerol as well as of polyglycerol-3-laurate. A decrease of viscosity by increasing reaction temperature is only possible in a certain temperature range because of the limited stability of the applied enzyme. By dissolving high dense carbon dioxide into the reaction system the viscosity could be reduced, keeping the temperature at an acceptable level at the same time. Thus the reaction rate was increased by a factor of 4 while working at a pressure of 280 bar and 60°C.

Cofactor Generation Cascade for α-Ketoglutarate and Fe(II)-Dependent Dioxygenases.

Fe(II)- and α-ketoglutarate dependent dioxygenases have emerged as important catalysts for the preparation of non-natural amino acids. The stoichiometric supply of the cosubstrate α-ketoglutarate (αKG) is an important cost factor. A combination of the N-succinyl amino acid hydroxylase SadA with an l-glutamate oxidase (LGOX) allowed for coupling in situ production of αKG to stereoselective αKG-dependent dioxygenases in a one-pot/two-step cascade reaction. Both enzymes were used as immobilized enzymes and tested in a preparative scale setup under process-near conditions. Oxygen supply, enzyme, and substrate loading of the oxidation of glutamate were investigated under controlled reaction conditions on a small scale before upscaling to a 1 L stirred tank reactor. LGOX was applied with a substrate concentration of 73.6 g/L (339 mM) and reached a space-time yield of 14.2 g/L/h. Additionally, the enzyme was recycled up to 3 times. The hydroxylase SadA reached a space-time yield of 1.2 g/L/h at a product concentration of 9.3 g/L (40 mM). For both cascade reactions, the supply with oxygen was identified as a critical parameter. The results underline the robustness and suitability of α-ketoglutarate dependent dioxygenases for application outside of living cells.

Optimization of Alcohol Dehydrogenase for Industrial Scale Oxidation of Lactols.

Alcohol dehydrogenases (ADH) are widely used to enantioselectively reduce ketones to chiral alcohols, but their application in industrial scale oxidations is rare. Reasons are the need for an NAD(P)+ cofactor regeneration system, often low performance in oxidative reactions and the limited substrate scope of ADHs. ADHA from Candida magnoliae DSMZ 70638 is identified to efficiently catalyze the regio-selective hydroxy-lactone oxidations to hydroxy-lactones. Hydroxy-lactones are common intermediates in industrial processes to cholesterol lowering (va)statin drugs. A biocatalytic aliphatic hydroxy-lactone oxidation process is developed using pure oxygen as oxidant reaching volumetric productivities of up to 12 g L-1 h-1 , product concentrations of almost 50 g L-1 and 95% reaction yield. For co-factor recycling a previously engineered, water-forming NAD(P)H-oxidase from Streptococcus mutans is used. The process is scaled up to industrial pilot plant scale and it could be demonstrated that ADH catalyzed oxidations can be developed to efficient and safe processes. However, the ADHA wild-type enzyme is not productive enough in chlorolactol oxidation. Therefore, enzyme engineering and multi-parameter screening is successfully applied to optimize the enzyme for the target reaction. The optimized ADHA variant shows a 17-fold higher oxidative activity, a 26°C increased stability and is applied to develop an efficient chlorolactol oxidation process.

Process development for oxidations of hydrophobic compounds applying cytochrome P450 monooxygenases in-vitro.

Cytochrome P450 monooxygenases are a unique family of enzymes that are able to catalyze regio- and stereospecific oxidations for a broad substrate range. However, due to limited enzyme activities and stabilities, hydrophobicity of substrates, as well as the necessity of a continuous electron and oxygen supply the implementation of P450s for industrial processes remains challenging. Aim of this study was to point out key aspects for the development of an efficient synthesis concept for cytochrome P450 catalyzed oxidations. In order to regenerate the natural cofactor NADPH, a glucose dehydrogenase was applied. The low water soluble terpene α-ionone was used as substrate for the model reaction system. The studies reveal that an addition of surfactants in combination with low volumetric amounts of co-solvent can significantly increase substrate availability and reaction rates. Furthermore, these additives facilitated a reliable sampling procedure during the process. Another key factor for the process design was the oxygen supply. Based on various investigations, a bubble-aerated stirred tank reactor in batch mode represents a promising reactor concept for P450 oxidations. Main restriction of the investigated reaction system was the low process stability of the P450 monooxygenase, characterized by maximum total turnover numbers of ∼4100molα-ionone/molP450.