In this review article, recently developed continuous biotransformation processes are discussed. The processes are used to carry out resolution, redox reactions, hydrolysis/esterification, C-C bond formation, and other reactions. Examples of continuous downstream processing are also included.
Subtilisin Carlsberg (SC) was lyophilized from an aqueous buffer solution containing different amounts of unmodified commercial fumed silica. The activity of the enzyme/fumed silica preparation in hexane was compared to pure freeze-dried enzyme, and to a freeze-dried preparation reported in the literature with potassium chloride as additive. A sharp increase in enzyme activity was found to correlate with an increasing amount of fumed silica added to the enzyme solution prior to freeze-drying. A weight-ratio of 98.5wt% fumed silica relative to the mass of the final enzyme/fumed silica preparation led to about 130 fold increased activity of SC in hexane (when compared to pure lyophilized SC in hexane). This is about twice the activation effect compared to including potassium chloride in the buffer solution before freeze-drying [1].When freezing at -20ºC instead of in liquid nitrogen, even better activation was observed with fumed silica. We hypothesize that the activation of SC in hexane by immobilization of the enzyme on fumed silica is likely due to the distribution of the enzyme on the large surface area of fumed silica. This alleviates mass transfer limitations.
The application of enantioseparation methods alone can only yield up to 50% of the desired chiral product. Thus enantioseparation becomes more attractive when accompanied by the racemization of the counter-enantiomer. Here we present first results of dynamic kinetic resolution of L-asparagine (L-Asn) via preferential crystallization and enzymatic racemization from a racemic, supersaturated solution on a 20 mL scale. An enzyme lyophilisate (WT amino acid racemase from P. putida KT2440 (E.C. 5.1.1.10), overexpressed in E. coli BL21(DE3)) was used for in situ racemization (enzyme concentrations varying from 0 to 1 mg/mL). When preferential crystallization was applied without any enzyme, a total of 31 mg of L-Asn monohydrate could be crystallized, before crystal formation of d-Asn started. Crystallization experiments accompanied by enzymatic racemization led to a significant increase of crystallized L-Asn (198 mg L-Asn monohydrate; >92%ee) giving the first experimental proof for this new process concept of dynamic kinetic resolution via preferential crystallization and enzymatic racemization. Measurements of the racemase activity before and after the crystallization process showed no significant differences, which would allow for enzyme recovery and recycling.
Enzymatic catalysis in nonaqueous media is considered as an attractive tool for the preparation of a variety of organic compounds of commercial interest. This approach is advantageous for numerous reasons including the enhanced stability of some substrates and products in solvents, sometimes improved selectivity of the enzyme, and reduction of unwanted water-dependent side reactions since little water is present. Due to the poor solubility of enzymes in these media, mass transfer limitations are sometimes present, leading to low apparent catalytic activity. Immobilization on solid supports has been successfully applied to overcome enzyme solubility issues by increasing the accessibility of substrates to the enzymes' active sites. We have developed a simple immobilization protocol that uses fumed silica as support. Fumed silica is an inexpensive nanostructured material with unique properties including large surface area and exceptional adsorptive affinity for organic macromolecules. Our protocol is performed in two main steps. First, the enzyme molecules are physically adsorbed on the surface of the non-porous fumed silica nanoparticles with the participation of silanol groups (Si-OH) and second, water is removed by lyophilization. The protocol has been successfully applied to both s. Carlsberg and Candida antarctica lipase B (CALB). The resulting fumed silica-based nanobiocatalysts of these two enzymes were tested for catalytic activity in hexane. The transesterification of N-acetyl-L: -phenylalanine ethyl ester was the model reaction for s. Carlsberg nanobiocatalysts. The simple esterification of geraniol and the enantioselective transesterification of (RS)-1-phenylethanol were the model reactions for CALB nanobiocatalysts. The observed catalytic activities were remarkably high and even exceeded those of commercially available preparations.
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