On the importance of the support material for enzymatic synthesis in organic media. Support effects at controlled water activity

Enzymes were deposited on different porous support materials and these preparations were used to catalyze reactions in organic media. Reactions were carried out at specific water activities, achieved by equilibrating both the enzyme preparation and the substrate solution at the desired water activity before mixing them and thereby starting the reactions. The reaction rates obtained at the same water activity with different supports differed greatly, indicating a direct influence of the support on the enzyme. For horse liver alcohol dehydrogenase, Celite was the best support, and the reaction rate increased with increasing water activity. In the alpha-chymotrypsin-catalyzed alcoholysis of N-acetyl-L-phenylalanine ethyl ester with 1-butanol, high rates were again obtained with Celite, but with this support only about one third of the ethyl ester was converted to butyl ester, the rest was hydrolyzed. With the polyamide support, Accurel PA6, alcoholysis was the dominating reaction, and by using a low water activity (0.33), hydrolysis was completely suppressed while still maintaining a high alcoholysis activity. Controlled pore glass (CPG), derivatized with either hexyl or glucosyl groups, had quite different properties as enzyme supports. For horse liver alcohol dehydrogenase, glucose-CPG was a much better support than hexyl-CPG, and in the alpha-chymotrypsin-catalyzed reactions, glucose-CPG favored hydrolysis, and hexyl-CPG alcoholysis, at water activities exceeding 0.8. The results are discussed considering the absorption of water on the enzymes, on the supports and the solubility of water in the reaction media; all these parameters were measured separately.     

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.     

Reaction Kinetics of Immobilized α-Chymotrypsin in Organic Media 1. Influence at Solvent Polarity

Esterification of N-acetyl phenylalanine with ethanol catalyzed by immobilized α-chymotrypsin (EC 3.4.21.1) was studied in various reaction media. The effect of reaction medium polarity on enzymatic activity as well as equilibrium yield was measured. The reaction rate increased with increasing amounts of added water, reaching an optimum corresponding to water saturation of the reaction medium. Further additions of water resulted in decreased activity. Bell-shaped activity profiles were obtained for all reaction media tested. Reaction media consisting of pure solvents and of mixtures of solvents were used. The enzymatic activity and the equilibrium yield increased with decreased polarity of the medium. Maximum activity was found in a reaction medium consisting of 80% diisopropyl ether and 20% heptane. The enzymatic activity obtained at optimal water additions in the different solvents and solvents mixtures could be correlated to the solubility of water and the log P of the medium. The equilibrium yield of the reaction was much more closely correlated to the solubility of water than the log P. Much lower enzymatic activity was obtained when solvent mixtures producing water-miscible media were created, than in mixtures producing water-immiscible media, such as mixtures of acetonitrile and diisopropyl ether. The equilibrium yield could be increased by decreasing the water content in the reaction medium, which reduced the water activity.     

Enzymatic Synthesis of Hexyl Glycosides from Lactose At Low Water Activity and High Temperature Using Hyperthermostable β-glycosidases

Optimization of hexyl-g-glycoside synthesis from lactose in hexanol at low water activity and high temperature was investigated using g-glycosidases from hyperthermophilic organisms: Sulfolobus solfataricus (LacS) and Pyrococcus furiosus (CelB). The method for water activity adjustment by equilibration with saturated salt solutions was adapted for use at high temperature. The influence of enzyme immobilization (on XAD-4, XAD-16, or Celite), addition of surfactants (AOT or SDS), substrate concentration, water activity, and temperature (60-90°C) on enzymatic activity and hexyl-g-glycoside yield were examined. Compared to other g-glycosidases in lactose conversion into alkyl glycoside, these enzymes showed high activity in a hexanol one-phase system and synthesized high yields of both hexyl-g-galactoside and hexyl-g-glucoside. Using 32 λg/l lactose (93 λmM), LacS synthesized yields of 41% galactoside (38.1 λmM) and 29% glucoside (27.0 λmM), and CelB synthesized yields of 63% galactoside (58.6 λmM) and 28% glucoside (26.1 λmM). With the addition of SDS to the reaction it was possible to increase the initial reaction rate of LacS and hexyl-g-galactoside yield (from 41 to 51%). The activity of the lyophilized enzyme was more influenced by the water content in the reaction than the enzyme on solid support. In addition, it was concluded that for the lyophilized enzyme preparation the enzymatic activity was much more influenced by the temperature when the water activity was increased. A variety of different glycosides were prepared using different alcohols as acceptors.     

From hydrocolloids to high specific surface area porous supports for catalysis

Polysaccharide hydrogels are effective supports for heterogeneous catalysts. Their use in solvents different from water has been hampered by their instability upon drying. While the freeze-drying process or air-drying of hydrocolloid gels led to compact solids with a low surface area, drying the gel in CO2 beyond the critical point provided mesoporous materials with a high specific surface area. Their effectiveness as a support for catalysis was exemplified in the reaction of substitution of an allyl carbonate with morpholine catalyzed by the hydrosoluble Pd(TPPTS)3 complex. The influence of water on the catalytic activity and the properties of the support was evidenced.     

A new test for chorismate mutase activity.

Chorismate mutase (EC 5.4.99.5) catalyzes the conversion of chorismic acid to prephenic acid. A continuous test of the enzymatic activity is based on the decrease of the absorption of the substrate chorismate at 274 nm (1). In a sensitive but discontinuous test, prephenic acid, the product of the enzymatic reaction is converted to phenylpyruvic acid. The absorbance of its enolic form is determined in alkaline solution at 320 nm (2,3). Another discontinuous test makes use of the absorption of the phenylpyruvate enol-borate complex (4,5) at 300 nm. The continuous test cannot be used when aromatic compounds are to be tested as modifiers of the enzymatic activity. Similarly, the tests based on the absorption of the enolic form of phenylpyruvic acid cannot be used when compounds which show a high absorbance in the 300 to 320 nm wavelength region are tested. This paper describes a test for chrismate mutase based on the determination of the 2,4-dinitrophenylhydrazone of the α-keto acid, phenylpyruvic acid. In alkaline solution the 2,4-dinitrophenylhydrazone of phenylpyruvic acid shows an absorption maximum at 440 nm, thus allowing one to test compounds like 3-hydroxybenzoic acid and 5-hydroxyisophthalic acid as potential inhibitors of the enzymatic reaction.     

Formation of C-C bonds by mandelonitrile lyase in organic solvents

Mandelonitrile lyase (EC 4.1.2.10) catalyzes the formation of D-mandelonitrile from HCN and benzaldehyde. Mandelonitrile lyase was immobilized by adsorption to support materials, for example, Celite. The enzyme preparations were used in diisopropyl ether for production of D-mandelonitrile. In order to obtain optically pure D-mandelonitrile it was necessary to use reaction conditions which favor the enzymatic reaction and suppress the competing spontaneous reaction, which yields a racemic mixture of D, L-mandelonitrile. The effects of substrate concentrations, water content, and support materials on both the spontaneous and enzymatic reactions were studied. The enzymatic reaction was carried out under conditions where the importance of the spontaneous reaction was negligible and high enantiomeric purity of D-mandelonitrile was achieved (at least 98% enantiomeric excess). The operational stability of the enzyme preparations was studied in batch as well as in continuous systems. It was vital to control the water content in the system to maintain an active preparation. In a packed bed reactor the enzyme preparations were shown to be active and stable. The reactors were run for 50 h with only a small decrease in product yield.     

Enzymatic Synthesis of Hexyl Glycosides from Lactose At Low Water Activity and High Temperature Using Hyperthermostable β-glycosidases

Optimization of hexyl-&#103-glycoside synthesis from lactose in hexanol at low water activity and high temperature was investigated using &#103-glycosidases from hyperthermophilic organisms: Sulfolobus solfataricus (LacS) and Pyrococcus furiosus (CelB). The method for water activity adjustment by equilibration with saturated salt solutions was adapted for use at high temperature. The influence of enzyme immobilization (on XAD-4, XAD-16, or Celite), addition of surfactants (AOT or SDS), substrate concentration, water activity, and temperature (60-90°C) on enzymatic activity and hexyl-&#103-glycoside yield were examined. Compared to other &#103-glycosidases in lactose conversion into alkyl glycoside, these enzymes showed high activity in a hexanol one-phase system and synthesized high yields of both hexyl-&#103-galactoside and hexyl-&#103-glucoside. Using 32 &#117 g/l lactose (93 &#117 mM), LacS synthesized yields of 41% galactoside (38.1 &#117 mM) and 29% glucoside (27.0 &#117 mM), and CelB synthesized yields of 63% galactoside (58.6 &#117 mM) and 28% glucoside (26.1 &#117 mM). With the addition of SDS to the reaction it was possible to increase the initial reaction rate of LacS and hexyl-&#103-galactoside yield (from 41 to 51%). The activity of the lyophilized enzyme was more influenced by the water content in the reaction than the enzyme on solid support. In addition, it was concluded that for the lyophilized enzyme preparation the enzymatic activity was much more influenced by the temperature when the water activity was increased. A variety of different glycosides were prepared using different alcohols as acceptors.     

Effect of trophic conditions on aspartate transamination in wheat plants

The enzymatic transamination reactions between aspartic and α-ketoglutaric acid and between aspartic and pyruvic acid were studied in fresh dialysed extracts of young wheat plants cultivated under various trophical conditions, in mineral solution (Knop), in the solution of an soil organic substance (potassium humate) and without nutrients (H₂O). Simultaneously, the level of endogenic aspartic acid, glutamic acid and the growth values were determined. The enzymatic reactions were characterized by determining the optimum pH, the time course, and the effect of coenzyme and of inhibitors. The activity of the aspartate-glutamate transaminase from the root system of plants was considerably higher than the activity of the overground organs. The enzymatic activity from both parts of the plant was inversely proportional to the growth rate: intensive growth of the plants from the Knop variant was connected with their low enzymatic activity; the level of endogenic glutamic acid was high. The slow growth of the plants without nutrients was connected with a higher enzymatic activity; the level of endogenic glutamic acid was low. The plants from the potassium humate variant had an intermediate position between these two variants from the point of view of growth as well as from that of enzymatic activity. The plants with insufficient nutrition (slow growth, low level of endogenic glutamic acid) apparently have a low capacity for supplementing the glutamic acid deficit, which is essential for the metabolic processes, by increasing the activity of the reactions leading to glutamic acid synthesis (Asp-Glu) and, on the other hand, by decreasing the reactions utilizing it (Glu-Ala). For wheat plants the active aspartate-glutamate reaction is obviously physiologically more important than the direct reaction glutamate-aspartate and the reaction aspartate-alanine which in all cases had a very low activity.     

Three Systems Used for Biocatalysis in Organic Solvents a Comparative Study

The activity and operational stability of horse liver alcohol dehydrogenase (HLADH) and α-chymotrypsin were investigated in three systems commonly used for biocatalysis in organic solvents:

1. enzyme adsorbed on a solid support (celite) and added to the organic solvent (isooctane)

2. enzyme powder directly added to the organic solvent (isooctane).

3. enzyme dissolved in a microemulsion (AOT/isooctane).

The activity and the operational stability in all systems were strongly dependent on the water content. The initial reaction rate was high in both the microemulsion and the celite system, but was much lower when adding the enzymes directly to the organic solvent. HLADH was observed to be more stable when added directly to the organic solvent or dissolved in the microemulsion than when adsorbed on celite, whereas for α-chymotrypsin stability was higher when adsorbed on celite or added directly to the organic solvent. For a hydrolytic reaction, a microemulsion was preferred due to the high water content. When adding the enzymes directly to the organic solvent both HLADH and chymotrypsin were adsorbed strongly to the glass walls of the reaction vessel. None of the systems were superior in all respects for the two enzymes studied.     

Enzymatic synthesis of arginine-based cationic surfactants

A novel enzymatic approach for the synthesis of arginine N-alkyl amide and ester derivatives is reported. Papain deposited onto solid support materials was used as catalyst for the amide and ester bond formation between Z-Arg-OMe and various long-chain alkyl amines and alcohols (H2N-Cn2, HO-Cn; n = 8-16) in organic media. Changes in enzymatic activity and product yield were studied for the following variables: organic solvent, aqueous buffer content, support for the enzyme deposition, presence of additives, enzyme loading, substrate concentration, and reaction temperature. The best yields (81-89%) of arginine N-alkyl amide derivatives were obtained at 25 degrees C in acetonitrile with an aqueous buffer content ranging from 0 to 1% (v/v) depending on the substrate concentration. The synthesis of arginine alkyl ester derivatives was carried out in solvent-free systems at 50 or 65 degrees C depending on the fatty alcohol chain length. In this case, product yields ranging from 86 to 89% were obtained with a molar ratio Z-Arg-OMe/fatty alcohol of 0.01. Papain deposited onto polyamide gave, in all cases, both the highest enzymatic activities and yields. Under the best reaction conditions the syntheses were scaled up to the production of 2 g of final product. The overall yields, which include reaction, Nalpha-benzyloxycarbonyl group (Z) deprotection and purification, varied from 53 to 77% of pure (99.9% by HPLC) product.     

Design of reactive porous polymer supports for high throughput bioreactors: poly(2-vinyl-4,4-dimethylazlactone-co-acrylamide- co-ethylene dimethacrylate) monoliths

Enzymatic bioreactors with both high flow characteristics and mechanical stability based on macroporous poly(2-vinyl-4, 4-dimethylazlactone-co-acrylamide-co-ethylene dimethacrylate) monoliths have been prepared. Covalent immobilization of trypsin on these support is achieved in a single reaction step using the azlactone functional groups. Optimization of hydrophilic/hydrophobic properties of the monolith affords a support that does not shrink in water and leads to immobilized enzyme that shows high activity in the hydrolysis of both low and high molecular weight substrates such as L-benzoyl arginine ethyl ester and casein. The catalytic activity of the monolithic reactor is maintained even at a flow velocity of 180 cm/min, which substantially exceeds those reported in the literature for packed bed reactors.     

Role of the support surface on the loading and the activity of Pseudomonas fluorescens lipase used for biodiesel synthesis

The present work investigates the influence of the support surface on the loading and the enzymatic activity of the immobilized Pseudomonas fluorescens lipase. Different porous materials, polypropylene (Accurel), polymethacrylate (Sepabeads EC-EP), silica (SBA-15 and surface modified SBA-15), and an organosilicate (MSE), were used as supports. The immobilized biocatalysts were compared towards sunflower oil ethanolysis for the sustainable production of biodiesel. Since the supports have very different structural (ordered hexagonal and disordered) and textural features (surface area, pore size, and total pore volume), in order to consider only the effect of the support surface, experiments were performed at low surface coverage. The different functional groups occurring on the support surface allowed either physical (Accurel, MSE, and SBA-15) or chemical adsorption (Sepabeads EC-EP and SBA-15–R-CHO). The surface-modified SBA-15 (SBA-15–R-CHO) allowed the highest loading. The lipase immobilized on the MSE was the most active biocatalyst. However, in terms of catalytic efficiency (activity/loading) the lipase immobilized on the SBA-15, the support that allowed the lowest loading, was the most efficient.     

Structure-based catalytic optimization of a type III Rubisco from a hyperthermophile

The Calvin-Benson-Bassham cycle is responsible for carbon dioxide fixation in all plants, algae, and cyanobacteria. The enzyme that catalyzes the carbon dioxide-fixing reaction is ribulose-1,5-bisphosphate carboxylase/oxygenase (Rubisco). Rubisco from a hyperthermophilic archaeon Thermococcus kodakarensis (Tk-Rubisco) belongs to the type III group, and shows high activity at high temperatures. We have previously found that replacement of the entire α-helix 6 of Tk-Rubisco with the corresponding region of the spinach enzyme (SP6 mutant) results in an improvement of catalytic performance at mesophilic temperatures, both in vivo and in vitro, whereas the former and latter half-replacements of the α-helix 6 (SP4 and SP5 mutants) do not yield such improvement. We report here the crystal structures of the wild-type Tk-Rubisco and the mutants SP4 and SP6, and discuss the relationships between their structures and enzymatic activities. A comparison among these structures shows the movement and the increase of temperature factors of α-helix 6 induced by four essential factors. We thus supposed that an increase in the flexibility of the α-helix 6 and loop 6 regions was important to increase the catalytic activity of Tk-Rubisco at ambient temperatures. Based on this structural information, we constructed a new mutant, SP5-V330T, which was designed to have significantly greater flexibility in the above region, and it proved to exhibit the highest activity among all mutants examined to date. The thermostability of the SP5-V330T mutant was lower than that of wild-type Tk-Rubisco, providing further support on the relationship between flexibility and activity at ambient temperatures.     

A novel process of cyclodextrin production by the use of specific adsorbents: Part II. A new reactor system for selective production of α-cyclodextrin with specific adsorbent

We have developed a novel process of α-cyclodextrin (α-CD) production by using a new adsorbent that is characterized by its exceedingly powerful selectivity for α-CD compared with other CDs. α-CD production was carried out in a closed reactor system that was composed of a main reactor, wherein liquefied starch was converted to CDs by cyclodextrin glucosyltransferase (CGTase: EC 2.4.1.19), and a column packed with the adsorbent. While the reaction mixture was circulated in the system, α-CD was selectively adsorbed in the column and its concentration in the mixture of the main reactor was kept at a low level. This low concentration of α-CD stimulated the conversion of starch to CDs and as a result, enhanced its yield based on added starch. When 8.3 % (w/v) of liquefied starch was used in the reactor system, the yield of α-CD was 22.2% and α-CD occupied 58.7 % of the reaction mixture of total CDs synthesized. Meanwhile, in a batch system without the adsorbent, the yield of α-CD and its fraction were 10.8% and 45.0%, respectively. After the conversion reaction, and following the preliminary washing with water through the column. α-CD was easily eluted with hot water, resulting in a high purity of about 95%.     

Interesterification of fats and oils by immobilized fungus at constant water concentration

The kinetics of enzymatic interesterification of oils and fats, using acetone-dried cells of Rhizopus chinensis immobilized on biomass support particles as a lipase catalyst, were investigated in batch operations at several constant water concentrations.Even under microaqueous (i.e., low-water-content) conditions, not only interesterification but also hydrolysis occured, and the water content in the reaction system decreased. The reaction rates of interesterification and hydrolysis at constant water concentrations were determined.For the reactions between olive oil and methyl stearate at several water concentrations, the parameters involved in the reaction model were determined by a trial-and-error method so as to make the calculated results correlate with the experimental data. The relationship between the parameters obtained and water concentration were examined.The rate constants involved in the reaction model of both interesterification and hydrolysis increased or decreased monotonically with the increasing water content, while the apparent activity of the lipase catalyst for interesterification had a maximum value at a water concentration of about 50 ppm. This suggests that when the water content is excessive the hydrolysis activity of lipase is accelerated more than its interesterification activity, and that when the water content is too little lipase activity can not be activated for either hydrolysis or interesterification.     

Effect of Different Supports on the Reaction Rate of Rhizomucor Miehei Lipase in Organic Media

Five different aluminas, a silica and a zirconia support were used to adsorb lipase (E.C. 3.1.1.3) from Rhizomucor miehei. The activity of the immobilised lipase was measured by esterification of dodecanol and decanoic acid in hexane. The immobilised lipase and the organic phase were pre-equilibrated separately to known water activities before mixing them to commence the reactions. The aluminas, which varied in pore sizes and surface areas, adsorbed similar amounts of enzyme. However, the esterification activities varied about 10-fold, increasing with increasing surface area. The silica and zirconia supports adsorbed about half as much lipase as the aluminas. The esterification reaction rates per unit quantity of enzyme adsorbed were compared with those for aluminas with similar surface areas; this specific rate was about 2 times higher for the zirconia, but the difference with silica was only small. There was no clear correlation between the esterification rates at fixed water activity and the amount of water adsorbed by the support used.     

Synthesis of well-defined graft copolymers by combination of enzymatic polycondensation and "click" chemistry

Aliphatic polyesters having pendant azide groups were prepared by enzymatic polycondensation in the presence of lipase from Candida antarctica type B (CAL-B). The grafting reaction to the N(3)-functional polyester was carried out quantitatively at room temperature using copper-catalyzed azide-alkyne cycloaddition (CuAAC, "click" reaction) with monoalkyne-functional poly(ethylene oxide) (alkyne-PEO, M(n) = 750 g/mol). Furthermore, both enzymatic polycondensation and "click" reaction were carried out successfully in sequential one-pot reaction. The graft copolymer was surface-active and self-assembled in water. The graft copolymer had a critical aggregation concentration (cac) of 3 × 10(-2) μM in water determined by surface tension measurements. Above cac, the graft copolymer formed single chains and aggregates having a hydrodynamic radius of ～75 nm. Furthermore, the surface activity of the polymers at the air-water interface was studied by Langmuir trough measurements. The Langmuir isotherm of the graft polymer showed a pseudoplateau resulting from desorption of PEO chains into the subphase upon compression.     

Covalent immobilization of pure isoenzymes from lipase of Candida rugosa

Covalent immobilization of pure lipases A and B from Candida rugosa on agarose and silica is described. The immobilization increases the half-life of the biocatalysts ( ) with respect to the native pure lipases ( ). The percentage immobilization of lipases A and B is similar in both supports (33–40%). The remaining activity of the biocatalysts immobilized on agarose (70–75%) is greater than that of the enzymatic derivatives immobilized on SiO₂ (40–50%). The surface area and the hydrophobic/hydrophilic properties of the support control the lipase activity of these derivatives. The thermal stability of the immobilized lipase A derivatives is greater than that of lipase B derivatives. The nature of the support influences the thermal deactivation profile of the immobilized derivatives. The immobilization in agarose (hydrophilic support) gives biocatalysts that show a greater initial specific reaction rate than the biocatalysts immobilized in SiO₂ (hydrophobic support) using the hydrolysis of the esters of (R) or (S) 2-chloropropanoic and of (R,S) 2-phenylpropanoic acids as the reaction test. The enzymatic derivatives are active for at least 196 h under hydrolysis conditions. The stereospecificity of the native and the immobilized enzymes is the same.     

Alternative Oils Tested as Feedstocks for Enzymatic FAMEs Synthesis: Toward a More Sustainable Process

Previously isolated and characterized Pseudomonas lipases were immobilized in a low‐cost MP‐1000 support by a re‐loading procedure that allowed a high activity per weight of support. Immobilized LipA, LipC, and LipCmut lipases, and commercial Novozym® 435 were tested for fatty acid methyl ester (FAMEs) synthesis using conventional and alternative feedstocks. Triolein and degummed soybean oils were used as model substrates, whereas waste cooking oil and M. circinelloides oil were assayed as alternative, low cost feedstocks, whose free fatty acid (FFA), and acylglyceride profile was characterized. The reaction conditions for FAMEs synthesis were initially established using degummed soybean oil, setting up the best water and methanol concentrations for optimum conversion. These conditions were further applied to the alternative feedstocks and the four lipases. The results revealed that Pseudomonas lipases were unable to use the FFAs, displaying a moderate FAMEs synthesis, whereas a 44% FAMEs production was obtained when M. circinelloides oil was used as a substrate in the reaction catalysed by Novozym® 435, used under the conditions established for degummed soybean oil. However, when Novozym® 435 was tested under previously described optimal conditions for this lipase, promising values of 85 and 76% FAMEs synthesis were obtained for waste cooking oil and M. circinelloides oil, respectively, which might result in promising, nonfood, alternative feedstocks for enzymatic biodiesel production. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 33:1209–1217, 2017