Review: Biocatalytic transformations of ferulic acid: An abundant aromatic natural product

In this review we examine the fascinating array of microbial and enzymatic transformations of ferulic acid. Ferulic acid is an extremely abundant, preformed phenolic aromatic chemical found widely in nature. Ferulic acid is viewed as a commodity scale, renewable chemical feedstock for biocatalytic conversion to other useful aromatic chemicals. Most attention is focused on bioconversions of ferulic acid itself. Topics covered include cinnamoyl side-chain cleavage; nonoxidative decarboxylation; mechanistic details of styrene formation; purification and characterization of ferulic acid decarboxylase; conversion of ferulic acid to vanillin;O-demethylation; and reduction reactions. Biotransformations of vinylgualacol are discussed, and selected biotransformations of vanillic acid including oxidative and nonoxidative decarboxylation are surveyed. Finally, enzymatic oxidative dimerization and polymerization reactions are reviewed.     

Prediction of the Reaction Equilibrium of Biocatalytic Reactions in Aqueous-Organic Two-Phase Systems

Biocatalytic reactions can be carried out in aqueous-organic two-phase systems. Several models to describe the thermodynamically-determined equilibrium position in such systems have appeared in the literature. Some of these models are only valid for dilute systems, whereas others can also be used for nondilute systems. In this paper, these models are described and compared. It is explained in what way the equilibrium constants of each model can be used to predict the product concentration in different organic solvents.     

酶法生产L-高苯丙氨酸的研究进展

L-高苯丙氨酸(L-homophenylalanine,L-HPA)作为一种重要的非天然氨基酸,是合成治疗高血压的普利类药物等的关键中间体,具有广阔的市场前景。目前L-高苯丙氨酸的合成主要依赖于化学法,但化学合成L-高苯丙氨酸具有原料昂贵、步骤繁琐和污染严重等缺点,限制了广泛应用。因此,国内外研究者对L-高苯丙氨酸的酶法生产进行了深入的研究。本文就目前酶法合成L-高苯丙氨酸的工艺,包括脱氢酶法、转氨酶法、海因酶法和脱羧酶法的研究进展进行了综述,为酶法合成L-高苯丙氨酸提供一定的借鉴,为最终实现L-高苯丙氨酸的酶法工业化生产奠定基础。     

Mutant Escherichia coli penicillin acylase with enhanced stability at alkaline pH

Increased stability at alkaline pH should be a valuable attribute for the utilization of penicillin acylase in bioreactors employed to convert penicillins into 6-aminopenicillanic acid, a precursor of semisynthetic penicillins. In these systems, base is added for pH control, which results in local alkaline conditions that promote enzyme inactivation. Hydrolysis and synthesis reactions are also pH dependent. Here, we report work in which the gene coding for Escherichia coli penicillin acylase was subjected to oligonucleotide-directed random mutagenesis at regions coding for amino acids predicted to be at the surface of the enzyme. The resulting mutant library, cloned in E. coli, was screened by a filter paper assay of the colonies for the presence of penicillin acylase activity with enhanced stability at alkaline pH. Characterization of one of the selected clones revealed the presence of a mutation, Trp431-Arg, which would presumably alter the surface charge of the protein. In vitro experiments demonstrated a near twofold increase in the half-life of the mutant enzyme when stored at pH 8.5 as compared with the wild-type enzyme, with a comparable specific activity at several pH values. In general, the mutant displayed increased stability toward the basic side in the pH-stability profile. (c) 1995 John Wiley & Sons, Inc.     

Solvent effects on biocatalysis in organic systems: equilibrium position and rates of lipase catalyzed esterification

Porcine pancreatic lipase immobilized on celite particles has been employed as a catalyst for the esterification of dodecanol and decanoic acid in a predominantly organic system. Solvent influence on the equilibrium position and on the catalyst activity has been studied using 20 solvents, including aliphatic and aromatic hydrocarbons, ethers, ketones, nitro- and halogenated hydrocarbons, and esters. The equilibrium constant for esterification correlates well with the solubility of water in the organic solvent, which in turn shows a good relationship with a function of Guttman's donor number and the electron pair acceptance index number of the solvent. This may be rationalized in terms of the requirements for solvation of water and of the reactants. The catalyst activity, measured as the initial rate of the esterification reaction, is best correlated as a function of both n-octanol-water partition coefficient (log P) and either the electron pair acceptance index or the polarizability.     

Harnessing and engineering amide bond forming ligases for the synthesis of amides

The amide functional group is ubiquitous in nature and one of the most important motifs in pharmaceuticals, agrochemicals, and other valuable products. While coupling amides and carboxylic acids is a trivial synthetic transformation, it often requires protective group manipulation, along with stoichiometric quantities of expensive and deleterious coupling reagents. Nature has evolved a range of enzymes to construct amide bonds, the vast majority of which utilize adenosine triphosphate to activate the carboxylic acid substrate for amine coupling. Despite the fact that these enzymes operate under mild conditions, as well as possessing chemoselectivity and regioselectivity that obviates the need for protecting groups, their synthetic potential has been largely unexplored. In this review, we discuss recent research into the discovery, characterization, and development of amide bond forming enzymes, with an emphasis on stand-alone ligase enzymes that can generate amides directly from simple carboxylic acid and amine substrates.     

Optimization of factors influencing enzyme activity and product selectivity and the role of proton transfer in the catalytic mechanism of patchoulol synthase

The patchoulol synthase (PTS) from Pogostemon cablin is a versatile sesquiterpene synthase and produces more than 20 valuable sesquiterpenes by conversion of the natural substrate farnesyl pyrophosphate (FPP). PTS has the potential to be used as a biocatalyst for the production of valuable sesquiterpenes such as (−)-patchoulol. The objective of the present study is to develop an efficient biotransformation and to characterize the biocatalytic mechanism of the PTS in detail. For this purpose, soluble PTS was prepared using an optimized cultivation protocol and continuous downstream process with a purity of 98%. The PTS biotransformation was then optimized regarding buffer composition, pH-value, and temperature for biotransformation as well as functional and kinetic properties to improve productivity. For the bioconversion of FPP, the highest enzyme activity was reached with the 2-(N-morphlino)ethanesulfonic acid (MES) buffer containing 10% (v/v) glycerol and 10 mM MgCl₂ at pH 6.4 and 34°C. The PTS showed an unusual substrate inhibition for sesquiterpene synthases indicating an intermediate sesquiterpene formed in the active center. Deuteration experiments were used to gain further insights into the biocatalytic mechanism described in literature. Thus it could be shown that a second substrate binding site must be responsible for substrate inhibition and that further protonation and deprotonation steps are involved in the reaction mechanism.     

Preparation and properties of an immobilized cellulase on the reversibly soluble matrix Eudragit L-100

Abstract

To prepare a smart biocatalyst, cellulase was immobilized on the reversibly soluble matrix Eudragit L-100 by non-covalent and covalent methods. Covalent immobilization using carbodiimide coupling exhibited superior enzyme loading and reusability compared with non-covalent immobilization, and the covalent loading was increased by almost 20% through the addition of N-hydroxysuccinimide. The temperature optimum of the cellulase was not improved apparently by immobilization but the pH optimum increased from 4.75 to 5.25. Immobilized cellulase was more active than free cellulase above pH 5.0. Immobilized cellulase was more stable than free cellulase during storage at 4°C, room temperature and 50°C. K_m values of immobilized and free cellulase were 85.55 and 73.84 g L^?1, respectively. About 50% productivity was retained after five cycles for hydrolysis of steam-exploded straw.     

Effect of yeast cell disruption on ADH activity for redox reactions with in situ cofactor regeneration in a continuous solid/gas bioreactor

It has recently been demonstrated that dried cells of Saccharomyces cerevisiae were able to produce alcohols and aldehydes in a solid/gas reactor with in situ cofactor regeneration. Since diffusion of gaseous substrates may be limited by the membrane and cell wall, cell disruption by sonication was used to improve oxidoreduction with ethanol and butyraldehyde as substrates. Results showed that partial cell disruption enhances the maximum conversion yield with the best results obtained after 2 min of sonication. Beyond this time, the ADH activity decreased. Better stability was observed in the pellet obtained after centrifugation indicating the importance of cell environment for enzyme stability. Tests on purified mitochondria showed that the ADH activity in cells was mainly cytoplasmic. The addition of oxidized cofactor did not change either the activity or the stability of the catalyst in a gaseous medium. The effect of water activity was studied on material obtained after 2 min of disruption and a reduction of critical water activity needed for revealing enzymatic activity was observed. With increasing a_w, the enzyme was active at a_w=0.3 while a water activity of 0.4 was required before disruption. Nevertheless, the best compromise between activity and stability was obtained in both cases for a water activity of 0.57.     

Benzoic acid production via cascade biotransformation and coupled fermentation-biotransformation

As an important bulk chemical, benzoic acid is currently manufactured from nonrenewable feedstocks under harsh conditions. Although there are natural pathways for biosynthesis of benzoic acid, they are often inefficient and subjected to complex regulation. Here we develop a nonnatural enzyme cascade to efficiently produce benzoic acid from styrene or biogenic L -phenylalanine under mild conditions. By using a modular approach, two whole-cell catalysts Escherichia coli LZ305 and LZ325 are engineered for coexpressing seven and nine enzymes for production of 133–146 mM benzoic acid (16.2–17.8 g/L_aq) with 88–97% conversion via seven- and nine-step cascade biotransformation of styrene and L -phenylalanine, respectively. The seven-step cascade represents a formal high-yielding biocatalytic oxidative cleavage of styrene, and the nine-step cascade showcases the high efficiency of extended nonnatural enzyme cascades. Moreover, to achieve benzoic acid production directly from low-cost renewable glycerol, a novel coupled fermentation-biotransformation process was developed by integration of fermentative production of L -phenylalanine with in situ biotransformation to give 63–70 mM benzoic acid (7.6–8.6 g/L_aq), which is around 20 times higher than the reported value via a natural pathway. The coupled fermentation-biotransformation process could be generally applicable to microbial production of growth-inhibitory or toxic chemicals in high concentrations.