On the importance of the support material for bioorganic synthesis. Influence of water partition between solvent, enzyme and solid support in water-poor reaction media

alpha-Chymotrypsin was adsorbed on solid support materials and the catalytic activity of the preparations in organic solvents was studied. The activity was highly dependent on the nature of the support material and on the amount of water present in the reaction mixture. There appears to be competition for the water in the system between the enzyme, the support material and the solvent. The support materials were characterized by measuring their ability to absorb water from water-saturated diisopropyl ether. For the quotient: (amount of water on the support)/(amount of water in the solvent) in the model system the term aquaphilicity was proposed. The activity of adsorbed chymotrypsin in diisopropyl ether decreased with increasing aquaphilicity of the support material. The same trend was observed when the activity of horse liver alcohol dehydrogenase adsorbed on different supports was measured in diisopropyl ether.     

A water activity control system for enzymatic reactions in organic media

A water activity control system for enzymatic synthesis in organic media, for litre-scale reactors has been constructed. Water activity, a(w), is a key factor when using enzymes in non-conventional media and the optimum value varies for different enzymes. The control system consists of a water activity sensor in the headspace of a jacketed glass reactor (equipped with narrow steel tubes to introduce air), gas-washing bottles containing blue silica gel (a(w)=0) and water (a(w)=1), a PC to monitor water activity and a programmable logic controller (PLC) to control the water activity. The system was evaluated by adjusting water activity in the medium, with a deviation from the set point of less than +/-0.05. Synthesis of cetyl palmitate, under controlled water activity and catalysed by two different lipase preparations, namely, Novozym 435 (immobilised Candida antarctica lipase B) and immobilised Candida rugosa lipase, were also performed. Novozym 435 catalyses reactions very well at extremely low water activity while C. rugosa lipase shows low activity for a(w)<0.5.     

Designing enzymatic kyotorphin synthesis in organic media with low water content

Design of enzymatic kyotorphin synthesis in low water media has been carried out as a function of enzyme nature, the immobilization support material and the reaction medium, by using N-benzoyl-L-tyrosine ethyl ester and L-argininamide as substrates. Native and chemically-glycated alpha-chymotrypsin deposited on supports with different degrees of aquaphilicity (celite, polypropylene PP, and polyamide PA6) were used as catalysts. Binary organic solvent systems of ethanol and different water-immiscible organic cosolvents (ethylacetate, tert-butanol, chloroform, toluene, n-hexane, and n-octane) were studied as reaction media at constant water content (3% v/v). The greater the water binding affinity of the support the lower the synthetic activity of deposited enzymes: the activity of the celite derivative was 4x greater than the polyamide derivative. The enzyme glycation process hardly modified the catalytic ability of the celite derivative, but resulted in a moderate increase in operational stability. The presence of hydrophobic organic cosolvents in the water/ethanol reaction medium significantly increased enzyme activity, whereas the selectivity of the reaction remained high. Hexane was shown to be the best cosolvent, the synthetic activity of the celite derivative in hexane-ethanol (77 : 20%, v/v) being 130x greater than that in 97% (v/v) ethanol.     

Efficient enzymatic acrylation through transesterification at controlled water activity

Enzymatic acrylation is a process of potentially strong interest to the chemical industry. Direct esterification involving acrylic acid is unfortunately rather slow, with inhibition phenomena appearing at high acid concentrations. In the present study the acrylation of 1-octanol catalyzed by immobilized Candida antarctica lipase B (Novozym 435) was shown to be as much as an order of magnitude faster when ethyl acrylate served as the donor of the acrylic group. Water activity is a key parameter for optimizing the rate of ester synthesis. The optimum water activity for the esterification of octanol by acrylic acid was found to be 0.75, that for its esterification by propionic acid to be 0.45 and the transesterification involving ethyl acrylate to be fastest at a water activity of 0.3. The reasons for these differences in optimum water activity are discussed in terms of enzyme specificity, substrate solvation, and mass transfer effects.     

Process design for enzymatic peptide synthesis in near-anhydrous organic media

This work is a case study on a process design for enzymatic peptide synthesis, which is based on and inspired by previously established data about the Alcalase-catalyzed coupling of an amino acid amide and a chemically synthesized activated N-protected amino acid carbamoylmethyl ester in near-anhydrous tetrahydrofuran. The choices with regard to Alcalase formulation, the type of reactor, method of controlling the water content, and whether or not to recycle the enzyme, are discussed. In addition, an estimate is given for the reactor size, volumes of solvent, amount of substrate, enzyme and molecular sieves, needed in order to meet a specific demand for peptides. We believe that this case study gives a good indication of the various choices that have to be made when designing a process for enzymatic peptide synthesis and the implications of these choices.     

A simple approach for the selective enzymatic synthesis of dilauroyl maltose in organic media

A selective synthesis of dilauroyl maltose was developed using lipase-catalyzed condensation of lauric acid and maltose in two-solvent mixtures. The characteristics of different solvent combination were tested and it was found that the combination of acetone with n-hexane has a good selectivity for the synthesis of dilauroyl maltose. The highest diester conversion of 69% (i.e. 36.5 g/L of dilauroyl maltose) was obtained under optimal conditions: 25.65 g/L maltose, 60 g/L lauric acid, 60 g/L molecular sieve and 10 g/L lipase at 150 rpm and 50 °C for 72 h in 10 mL of mixed solvent of acetone:n-hexane (60:40, v/v).     

On-line water removal during enzymatic asymmetric esterification in organic media

Summary Enantioselective esterification of 2-bromopropionic acid with n-butanol using Candida cylindracea lipase was carried out in n-pentane at various initial water contents. Reaction rate as well as enantioselectivity decreased at high water content. A heteroazeotropic distillation method was applicable to remove the excess water continuously and to work at the optimum reaction conditions.     

Salt hydrates for water activity control with biocatalysts in organic media

Addition of solid salt hydrate(s) to the reaction mixture is a convenient method of water activity control. This article discusses the theoretical background to their use, and gives a compilation of data on the water activity values produced by 48 hydrate pairs of possible use in this application.     

Comparative study of the enzymatic synthesis of cephalexin at high substrate concentration in aqueous and organic media using statistical model

Synthesis of cephalexin with immobilized penicillin acylase at high substrates concentration at an acyl donor to nucleophile molar ratio of 3 was comparatively evaluated in aqueous and ethylene glycol media using a statistical model. Variables under study were temperature, pH and enzyme to substrate ratio and their effects were evaluated on cephalexin yield, ratio of initial rates of cephalexin synthesis to phenylglycine methyl ester hydrolysis, volumetric and specific productivity of cephalexin synthesis, that were used as response parameters. Results obtained in both reaction media were modeled using surface of response methodology and optimal operation conditions were determined in terms of an objective function based on the above parameters. At very high substrates concentrations the use of organic co-solvents was not required to attain high yields and actually almost stoichiometric yields were obtained in a fully aqueous media with the advantages of higher productivities than in an organic co-solvent media and compliance with the principles of green chemistry.     

Effect of water activity on enzymatic synthesis of alkylglycosides

Water activity (a_w) was studied during biocatalyzed alkylglycoside synthesis using defated raw almond meal displaying a good glucosidasic activity. Optimum a_w were determined for several alcohols used for the alkylation of the sugar. Above and below optimum a_w, yield decreased rapidly.     

Effect of water activity on enzymatic synthesis of cephalexin

Summary In enzymatic synthesis of cephalexin (CEX) from 7-amino-3-deacetoxycephalosporanic acid (7-ADCA) and D--phenylglycine methyl ester (PGM) using an acylase fromXanthomonas citri, it was found that the synthetic activity and conversion yield were enhanced markedly by depressing the water activity (a _w ) of reaction system. This enhancement was probably resulted from the change of thermodynamic equilibrium and maximized at a range ofa _w from 0.96 to 0.97.     

Effect of immobilization support, water activity, and enzyme ionization state on cutinase activity and enantioselectivity in organic media

We studied the reaction between vinyl butyrate and 2-phenyl-1-propanol in acetonitrile catalyzed by Fusarium solani pisi cutinase immobilized on zeolites NaA and NaY and on Accurel PA-6. The choice of 2-phenyl-1-propanol was based on modeling studies that suggested moderate cutinase enantioselectivity towards this substrate. With all the supports, initial rates of transesterification were higher at a water activity (a(w)) of 0.2 than at a(w) = 0.7, and the reverse was true for initial rates of hydrolysis. By providing acid-base control in the medium through the use of solid-state buffers that control the parameter pH-pNa, which we monitored using an organo-soluble chromoionophoric indicator, we were able, in some cases, to completely eliminate dissolved butyric acid. However, none of the buffers used were able to improve the rates of transesterification relative to the blanks (no added buffer) when the enzyme was immobilized at an optimum pH of 8.5. When the enzyme was immobilized at pH 5 and exhibited only marginal activity, however, even a relatively acidic buffer with a pK(a) of 4.3 was able to restore catalytic activity to about 20% of that displayed for a pH of immobilization of 8.5, at otherwise identical conditions. As a(w) was increased from 0.2 to 0.7, rates of transesterification first increased slightly and then decreased. Rates of hydrolysis showed a steady increase in that a(w) range, and so did total initial reaction rates. The presence or absence of the buffers did not impact on the competition between transesterification and hydrolysis, regardless of whether the butyric acid formed remained as such in the reaction medium or was eliminated from the microenvironment of the enzyme through conversion into an insoluble salt. Cutinase enantioselectivity towards 2-phenyl-1-propanol was indeed low and was not affected by differences in immobilization support, enzyme protonation state, or a(w).     

Continuous control of water activity during biocatalysis in organic media

Summary This paper describes a newly developed technique to adjust and control the water activity in enzymatic reactions in organic media. A saturated salt solution of known water activity is circulated inside a silicone tube, submerged into the reaction medium. The circulating solution can both absorb and release water. Water activity control during lipase catalyzed esterification was demonstrated with diisopropyl ether as solvent.     

Water activity dependence of performance of surface-displayed lipase in yeast cells: a unique water requirement for enzymatic synthetic reaction in organic media

Water activity (a(w)) is a crucial parameter affecting enzymatic synthetic reactions in organic media. In this paper, we report on the a(w) dependence of surface-displayed lipases, genetically immobilized on yeast cells via fusion with cell wall proteins. When Saccharomyces cerevisiae displaying Rhizopus oryzae lipase was used for esterification in n-hexane, equilibrating the dried cells with water prior to the reaction markedly increased the reaction rate. An equilibration of the cells with various saturated salt solutions showed that the reaction rate increased with increasing a(w) of the salt solution, to give the best performance at a(w) of 1.0. Interestingly, this trend was extremely different from those of lipases in powder or resin-immobilized form. To determine whether the cell surface is responsible for the unique a(w) profiles, an investigation was carried out similarly using other lipase sources and yeast strains, which indicated that, in all the cells examined, a higher a(w) resulted in a higher reaction rate. Moreover, increasing a(w) was found to increase the cell surface hydrophobicity determined by an aqueous-hydrocarbon biphasic partitioning assay. These results indicate that lipases displayed on yeast cells show a unique a(w) dependence probably because of the variation in cell surface characteristics.     

Enhancement effect of water activity on enzymatic synthesis of cephalexin

The effect of water activity (a(w)) of the reaction medium on the enzymatic synthesis of cephalexin (CEX) from 7-amino-3-deacetoxycephalosporanic acid (7-ADCA) and D-alpha-phenylglycine methyl ester (PGM) was investigated using the alpha-amino acid ester hydrolase enzyme from Xanthomonas citri. It was found that the synthetic activity of the enzyme and the conversion yield were markedly improved when the a(w) of the reaction medium was lowered to about 0.97. The water activity depressing agents evaluated were glycerol, sucrose, and sorbitol, and the conversion yields were improved up to 170% with 15% glycerol, 230% with 30% sucrose, and 270% with 20% sorbitol, respectively. The extent of favorable effect of a(w) on the conversion yield was not the same among the a(w) depressors, probably due to other unknown interactions between the enzyme and depressors. However, optimal a(w) values corresponding to the maximum conversion yield coincided for all a(w) depressors used. The conversion yield of CEX showed an increasing trend with increasing a(w) up to the optimal a(w) value (0.96-0.97) which corresponds to the maximum conversion yield and a decreasing trend beyond the optimal a(w). There appears to be a delicate balance between the hydrolytic reaction of PGM and synthetic reaction of CEX. The increasing a(w)-[E . PGM] complex and the branched reaction pathway fluxes from [E . PGM] to PG (D-alpha-phenyl glycine) and CEX are balanced in such a way that the maximum CEX conversion yield is obtained at a(w) value of 0.96-0.97. The a(w) depressors stabilized the enzyme somewhat, but this positive effect was considered to be only a minor contribution to the substantial yield enhancement. The a(w) depressor effect on viscosity and in turn the mass transfer rate limitation was ruled out since the change in conversion due to the viscosity change was found to be insignificant. (c) 1993 John Wiley & Sons, Inc.     

Influence of solvent and water activity on kinetically controlled peptide synthesis.

alpha-Chymotrypsin deposited on Celite was used to catalyse peptide synthesis reactions between N-protected amino acid esters and leucine amide in organic media with low water content. The influence of the solvent and the thermodynamic water activity on the reaction kinetics was studied. The substrate specificity in the reactions was shown to be a combination of the substrate specificity of the enzyme in aqueous media and the influence of the solvents. The magnitude of the solvent effects differed greatly depending on the substrates used. In hydrophobic solvents high reaction rates were observed and the competing hydrolysis of the ester substrate occurred to only a minor extent. Reactions occurred at water activities as low as 0.11, but the rate constants increased with increasing water activity and were about two orders of magnitude higher at the highest water activity tested (0.97).     

Chemical modification of alpha-chymotrypsin for obtaining high transesterification activity in low water organic media

Alpha-chymotrypsin was made more hydrophilic by modifying 11 (out of 16) ε-amino groups with pyromellitic dianhydride. The hydrophilic preparation was precipitated with n-propanol. This preparation gave significantly higher initial rates at the optimum a_w (127.51 nmol mg^?1 min^?1 in n-octane and 21.30 nmol mg^?1 min^?1 in acetonitrile at a_w=0.33) compared with the lyophilized preparation (53.50 nmol mg^?1 min^?1 in n-octane and 0.26 nmol mg^?1 min^?1 in acetonitrile at a_w=0.97). FT-IR showed that the precipitate of modified alpha-chymotrypsin has a higher content of alpha-helices and beta-sheets compared to the lyophilized powder.     

On enzymatic activity in organic solvents as a function of enzyme history

Catalytic activities of alpha-chymotrypsin and subtilisin Carlsberg in various hydrous organic solvents were measured as a function of how the enzyme suspension had been prepared. In one method, lyophilized enzyme was directly suspended in the solvent containing 1% water. In another, the enzyme was precipitated from its aqueous solution by a 100-fold dilution with an anhydrous solvent. In most cases, the reaction rate in a given nonaqueous enzymatic system strongly (up to an order of magnitude) depended on the mode of enzyme preparation. The magnitude of this dependence was markedly affected by the nature of the solvent and enzyme. A mechanistic hypothesis proposed to explain the observed dependencies was verified in additional experiments in which the water contents and enzyme history were further varied.     

The importance of the surface charge on support media for microbial adhesion

Using cristobalites treated at various temperatures, methane fermentation tests were carried out in an anaerobic fluidized-bed reactor (AFBR). Cristobalites treated below 1,000°C had almost the same qualities in terms of components, physical properties, and surface structures. However, points of zero charge were different between cristobalites treated below 600°C and those treated above 800°C. Points of zero charge on the former numbered about 5 and their surfaces were positively charged in the fermentor controlled pH at 7, while points of zero charge of the latter numbered above 8 and surfaces were negatively charged. In the methane fermentation tests, a TOC removal efficiency of 78% was obtained using positively charged cristobalite at a TOC loading rate of 8 g/l-h, but with negatively charged cristobalite, the efficiency was only 63% under the same conditions. This result confirms the importance of the surface charge on the support medium for the anaerobic digestion in an AFBR.