Production of (R)-3-quinuclidinol by a whole-cell biocatalyst with high efficiency

Optically pure (R)-3-quinuclidinol [(R)-3-Qui] is widely used as a chiral building block for producing various antimuscarinic agents. An asymmetric bioreduction approach using 3-quinuclidinone reductases is an effective way to produce (R)-3-Qui. In this study, a biocatalyst for producing (R)-3-Qui was developed by using Escherichia coli that coexpressed Kaistia granuli (KgQR) and mutant glucose dehydrogenase (GDH). KgQR catalyses the synthesis of (R)-3-Qui through the efficient reduction of 3-quinuclidinone. The specific activity of recombinant KgQR was 254?U/mg, and the Michaelis–Menten constant (K_m) for 3-quinuclidinone was 0.51?mM. The thermal stability of KgQR was relatively high compared with ArQR. Approximately 73% of the residual activity remained after incubation in 0.2 M potassium phosphate buffer (KPB) (pH 7.0) for 8?h at 30?°C. In addition, 80% residual activity remained for the double-mutant GDH (Q252L and E170K) after incubation in a buffer (pH 7.0) for 8?h at 30 and 40?°C. 3-Quinuclidinone (242?g/L) can be reduced to (R)-3-Qui in 3?h by coexpressing KgQR and mutant GDH in E. coli. The conversion rate reached 80.6?g/L/h, which is the highest reported to date. The results demonstrates that this whole-cell biocatalyst will have a great potential in industrial manufacturing.     

Acrylamide synthesis using agar entrapped cells of <Emphasis Type="Italic">Rhodococcus rhodochrous</Emphasis> PA-34 in a partitioned fed batch reactor

The nitrile hydratase (Nhase) induced cells of Rhodococcus rhodochrous PA-34 catalyzed the conversion of acrylonitrile to acrylamide. The cells of R. rhodochrous PA-34 immobilized in 2% (w/v) agar (1.76 mg dcw/ml agar matrix) exhibited maximum Nhase activity (8.25 U/mg dcw) for conversion of acrylonitrile to acrylamide at 10°C in the reaction mixture containing 0.1 M potassium phosphate buffer (pH 7.5), 8% (w/v) acrylonitrile and immobilized cells equivalent to 1.12 mg dcw (dry cell weight) per ml. In a partitioned fed batch reaction at 10°C, using 1.12 g dcw immobilized cells in a final volume of 1 l, a total of 372 g of acrylonitrile was completely hydrated to acrylamide (498 g) in 24 h. From the above reaction mixture 87% acrylamide (432 g) was recovered through crystallization at 4°C. By recycling the immobilized biocatalyst (six times), a total of 2,115 g acrylamide was produced.     

Tris–sucrose buffer system: a new specially designed medium for extracellular invertase production by immobilized cells of isolated yeast Cryptococcus laurentii MT-61

The aims of the present study were to isolate new yeasts with high extracellular (exo) invertase activity and to investigate the usability of buffer systems as invertase production media by immobilized yeast cells. Among 70 yeast isolates, Cryptococcus laurentii MT-61 had the highest exo-invertase activity. Immobilization of yeast cells was performed using sodium alginate. Higher exo-invertase activity for immobilized cells was achieved in tris–sucrose buffer system (TSBS) compared to sodium acetate buffer system and potassium phosphate buffer system. TSBS was prepared by dissolving 30 g of sucrose in 1 L of tris buffer solution. The optimum pH, temperature, and incubation time for invertase production with immobilized cells were determined as 8.0, 35 °C and 36 h in TSBS, respectively. Under optimized conditions, maximum exo-invertase activity was found to be 28.4 U/mL in sterile and nonsterile TSBS. Immobilized cells could be reused in 14 and 12 successive cycles in sterile and nonsterile TSBS without any loss in the maximum invertase activity, respectively. This is the first report which showed that immobilized microbial cells could be used as a biocatalyst for exo-invertase production in buffer system. As an additional contribution, a new yeast strain with high invertase activity was isolated.     

Studies on the accumulation of heavy metal elements in biological systems

Summary Cells of a Daucus carota suspension culture were entrapped in a matrix of calcium alginate. The immobilised cells, incubated in a buffer mixture of sucrose, nitrate, KCl, CaCl₂, 2-(N-morpholino)-ethane sulphonic acid at pH 5.5, hydroxylated digitoxigenin. When compared under the same incubation conditions, freely suspended cells biotransformed digitoxigenin at a faster rate. Periplogenin formation was maximal at pH 5.3 and temperatures of 26°–34°C. The hydroxylase activity of the entrapped cells adapted to the presence of 20 mM CaCl₂ over a 12 day incubation. The diffusion barrier established on entrapment of the cells could not be overcome by addition of detergents or methanol. Controlled addition of chloroform (at 1/4 and 1/2 saturation) did stimulate hydroxylation of digitoxigenin without adversely affecting cell viability. The rate of hydroxylation of digitoxigenin was linear over an immobilised cell concentration of 0–7 mg dry weight and a digitoxigenin concentration of 0–20 mg/L. Five consecutive batch bioconversions at a rate greater than 60% could be achieved before the biocatalyst was inactivated. The results are discussed in relation to improving the hydroxylation reaction by immobilised D. carota and other reactions performed by immobilised plant cells.     

Production of l-lactic acid with immobilized Lactobacillus delbrueckii

Summary Living Lactobacillus delbrueckii cells were entrapped in calcium alginate gel beads and employed both in recycle batch and continuous column reactors to produce l-lactic acid from glucose. The substrate contained l% (w/v) yeast extract as nutrient and 4.8% (w/v) solid calcium carbonate as buffer. The maxiumum lactic acid yield obtained was 97%, of which more than 90% was l-lactic acid. The biocatalyst activity half-life in continuous operation was about 100 d, and only about 10% of the activity was lost during intermittent storage of the bioreactor at +7°C for about 5 months.     

An approach for the improved immobilization of penicillin G acylase onto macroporous poly(glycidyl methacrylate‐co‐ethylene glycol dimethacrylate) as a potential industrial biocatalyst

The use of penicillin G acylase (PGA) covalently linked to insoluble carrier is expected to produce major advances in pharmaceutical processing industry and the enzyme stability enhancement is still a significant challenge. The objective of this study was to improve catalytic performance of the covalently immobilized PGA on a potential industrial carrier, macroporous poly(glycidyl methacrylate‐co‐ethylene glycol dimethacrylate) [poly(GMA‐co‐EGDMA)], by optimizing the copolymerization process and the enzyme attachment procedure. This synthetic copolymer could be a very promising alternative for the development of low‐cost, easy‐to‐prepare, and stable biocatalyst compared to expensive commercially available epoxy carriers such as Eupergit or Sepabeads. The PGA immobilized on poly(GMA‐co‐EGDMA) in the shape of microbeads obtained by suspension copolymerization appeared to have higher activity yield compared to copolymerization in a cast. Optimal conditions for the immobilization of PGA on poly(GMA‐co‐EGDMA) microbeads were 1 mg/mL of PGA in 0.75 mol/L phosphate buffer pH 6.0 at 25°C for 24 h, leading to the active biocatalyst with the specific activity of 252.7 U/g dry beads. Chemical amination of the immobilized PGA could contribute to the enhanced stability of the biocatalyst by inducing secondary interactions between the enzyme and the carrier, ensuring multipoint attachment. The best balance between the activity yield (51.5%), enzyme loading (25.6 mg/g), and stability (stabilization factor 22.2) was achieved for the partially modified PGA. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 32:43–53, 2016     

Characterization of a novel immobilized biocatalyst obtained by matrix-assisted refolding of recombinant polyhydroxyoctanoate depolymerase from <Emphasis Type="Italic">Pseudomonas putida</Emphasis> KT2442 isolated from inclusion bodies

Purification and matrix-assisted refolding of recombinant His-tagged polyhydroxyalkanoate (PhaZ) depolymerase from Pseudomonas putida KT2442 was carried out. His-tagged enzyme was overproduced as inclusion bodies in recombinant E. coli M15 (pREP4, pPAZ3), which were denatured by 8 M urea, immobilized on Ni²⁺-nitrilotriacetate-agarose matrix, and refolded by gradual removal of the chaotropic agent. The refolded enzyme could not be eluted with 1 M imidazole buffer, leading to an immobilized biocatalyst where PhaZ depolymerase was homogeneously distributed in the agarose support as shown by confocal scanning microscopy. Polyhydroxyoctanoate could not be hydrolyzed by this novel immobilized biocatalyst, whereas the attached enzyme was active in the hydrolysis of p-nitrophenyl alkanoate esters, which differed in their alkyl chain length. Taking advantage of the observed esterase activity on p-nitrophenylacetate, functional characterization of immobilized PhaZ depolymerase was carried out. The immobilized enzyme was more stable than its soluble counterpart and showed optimal hydrolytic activity at 37°C and 50 mM phosphate buffer pH 8.0. Kinetic parameters were obtained with both p-nitrophenylacetate and p-nitrophenyloctanoate, which had not been described so far for the soluble enzyme, representing an attractive and alternative chromogenic assay for the study of this paradigmatic enzyme.     

Hydrogen peroxide degradation by immobilized cells of alkaliphilic Bacillus halodurans

Whole cells of Bacillus halodurans LBK 261 were used as a source of catalase for degradation of hydrogen peroxide. The organism, B. halodurans grown at 55°C and pH 10, yielded a maximum catalase activity of 275 U g^-1 (wet wt.) cells. The catalase in the whole cells was active over a broad range of pH with a maximum at pH 8-9. The enzyme was optimally active at 55°C, but had low stability above 40°C. The whole cell biocatalyst exhibited a K_m of 6.6 mM for H₂O₂ and V_max of 707 mM H₂O₂ min^-1 g^-1 wet wt. cells, and showed saturation kinetics at 50 mM H₂O₂. The cells were entrapped in calcium alginate and used for H₂O₂ degradation at pH 9 in batch and continuous mode. In the batch process, the immobilized preparation containing 1.5 g (wet wt.) cells could be recycled at least four times for complete degradation of the peroxide in 50 mL solution at 25°C. An excess of immobilized biocatalyst could be used in a continuous stirred tank reactor for an average of 9 days at temperatures upto 55°C, and in a packed bed reactor (PBR) for 5 days before the beads started to deform.     

<Emphasis Type="Italic">Burkholderia cenocepacia</Emphasis>: a new biocatalyst for efficient bioreduction of ezetimibe intermediate

Ezetimibe is a selective acyl-coenzyme A: cholesterol acyltransferase (ACAT) inhibitor used in hypercholesterolemia. Synthesis of ezetimibe requires enantiopure 3-[5-(4-fluorophenyl)-5(S)-hydroxypentanoyl]-4(S)-4-phenyl-1,3-oxazolidin-2-one (FOP alcohol) as a crucial intermediate which is produced by reduction of the corresponding prochiral ketone (FOP dione). A new biocatalyst from acclimatized soil was screened for bioreduction of the above prochiral ketone. The microorganism was identified by 16S mRNA sequencing, as Burkholderia cenocepacia. Various physicochemical conditions were optimized to increase cellmass and enzyme activity. The overall increase in cellmass concentration and enzyme activity was 2.06 and 1.85-fold, respectively. Various reaction conditions, for example pH, temperature, agitation, and cellmass concentration, were optimized for maximum product yield (chiral alcohol) with excellent enantioselectivity. Best reduction was achieved in phosphate buffer (50 mM, pH 8.0) at 40°C (200 rpm) and the yield of enantiopure alcohol from the corresponding prochiral ketone was 54%. This biocatalyst was also used for the reduction of various other prochiral ketones.     

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.     

Increasing the Catalytic Performance of a Whole Cell Biocatalyst Harboring a Cytochrome P450cam System by Stabilization of an Electron Transfer Component

Catalytic activity of a recombinant Escherichia coli whole cell biocatalyst harboring a cytochrome P450cam monooxygenase system from Pseudomonas putida coupled with enzymatic co-factor regeneration was investigated. About 0.7 μmol camphor was hydroxylated per mg dry cells at 4°C in 50 mM Tris/HCl buffer (pH 7.4) when utilizing a stable putidaredoxin (Pdx) mutant, C73S/C85S-Pdx (Cys73Ser, Cys85Ser double mutant), instead of wild-type Pdx, which was about two-fold improvement in the substrate conversion. Ten-micromole camphor was completely hydroxylated at 20°C in 6 h by 15 mg dry cell weight of whole cell biocatalyst including C73S/C85S-Pdx. Thus, modulation of protein-protein interaction in multicomponent enzymatic catalysis in whole cells is important.     

One‐step magnetic modification of yeast cells by microwave‐synthesized iron oxide microparticles

Baker's yeast (Saccharomyces cerevisiae) cells were magnetically modified with magnetic iron oxide particles prepared by microwave irradiation of iron(II) sulfate at high pH. The modification procedure was very simple and fast. Both non‐cross‐linked and glutaraldehyde cross‐linked magnetic cells enabled efficient sucrose conversion into glucose and fructose, due to the presence of active intracellular invertase. The prepared magnetic whole‐cell biocatalyst was stable; almost the same catalytic activity was observed after 1‐month storage at 4°C. Simple magnetic separation and stability of the developed biocatalyst enabled its reusability without significant loss of enzyme activity.

Significance and Impact of the Study

Magnetic whole yeast cell biocatalyst containing intracellular invertase in its natural environment has been prepared. Magnetic properties enable its easy separation from reaction mixture. Magnetically modified Saccharomyces cerevisiae cells have been used for invert sugar production, hydrolysing sucrose into glucose and fructose. The described magnetization procedure employing microwave‐synthesized iron oxide microparticles is a low‐cost and easy‐to‐perform alternative to already existing magnetization techniques.     

Increase of electrical properties using a novel mixed buffer system in an enzyme fuel cell

Environment-friendly biocatalytic energy is considered to represent an attractive alternative to chemical catalystbased cells due to its renewability and better operation at low temperature. However, electrical biocatalysts have a low activity and electrical power. For increasing electrical properties of biocatalyst, a novel mixed buffer (phosphate and 3-morpholinopropanesulfonic acid (MOPS)) system was applied to an enzyme-based biofuel cell with microperoxidase (MP-11)-modified Au electrode. The cathodic electrical properties were increased by the phosphate and MOPS-mixed buffer solution. It was identified that the novel mixed buffer system obtained stronger ionic strength from phosphate buffer and better enzyme activity from MOPS buffer. The highest results of cyclic voltammetry were obtained when the proportion of phosphate to MOPS was nearly 1:1 and the pH was 7.0∼7.3. In addition, the novel mixed buffer led to the maximum power density (ca. 62.7 μW/cm²) in a basic enzymatic fuel cell (EFC).     

Kinetic and microstructural characterization of immobilized penicillin acylase from Streptomyces lavendulae on Sepabeads EC-EP

Recombinant penicillin acylase from Streptomyces lavendulae was covalently bound to epoxy-activated Sepabeads EC-EP303®. Optimization of the immobilization process led to a homogeneous distribution of the enzyme on the support surface avoiding the attachment of enzyme aggregates, as shown by confocal electron microscopy. The optimal immobilized biocatalyst had a specific enzymatic activity of 26.2IUgwetcarrier^?1 in the hydrolysis of penicillin V at pH 8.0 and 40°C. This biocatalyst showed the highest activity at pH 8.5 and 65°C, 1.5 pH units lower and 5°C higher than its soluble counterpart. Substrate specificity of the derivative also showed its ability to efficiently hydrolyze other natural aliphatic penicillins such as penicillins K, F and dihydroF. The immobilized enzyme was highly stable at 40°C and pH 8.0 (t_1/2=625 h vs. t_1/2=397 h for the soluble enzyme), and it could be recycled for at least 30 consecutive batch reactions without loss of catalytic activity.     

Covalent immobilization of recombinant Citrobacter koseri transaminase onto epoxy resins for consecutive asymmetric synthesis of L-phosphinothricin

Transaminase responsible for alienating prochiral ketone compound is applicable to asymmetric synthesis of herbicide L-phosphinothricin (L-PPT). In this work, the covalent immobilization of recombinant transaminase from Citrobacter koseri (CkTA) was investigated on different epoxy resins. Using optimum ES-105 support, a higher immobilized activity was obtained via optimizing immobilization process in terms of enzyme loading, coupling time and initial PLP concentration. Crucially, due to blocking unreacted epoxy groups on support surface with amino acids, the reaction temperature of blocked immobilized biocatalyst was enhanced from 37 to 57 °C. Its thermostability at 57 °C was also found to be superior to that of free CkTA. The K_m value was shifted from 36.75 mM of free CkTA to 39.87 mM of blocked immobilized biocatalyst, demonstrating that the affinity of enzyme to the substrate has not been apparently altered. Accordingly, the biocatalyst performed the consecutive synthesis of L-PPT for 11 cycles (yields>91%) with retaining more than 91.13% of the initial activity. The seemingly the highest reusability demonstrates this biocatalyst has prospective for reducing the costs of consecutive synthesis of L-PPT with high conversion.

     

Oxidative biotransformation of thioanisole by <Emphasis Type="Italic">Rhodococcus rhodochrous</Emphasis> IEGM 66 cells

Comparative study of sulfoxidation activity of free and immobilized Rhodococcus rhodochrous IEGM 66 cells was performed. Free Rhodococcus cells (in the presence of 0.1 vol % n-hexadecane) displayed maximal oxidative activity towards thioanisole (0.5 g/l), a prochiral organic sulfide, added after 48-h cultivation of bacterial cells. Higher sulfide concentrations inhibited sulfoxidation activity of Rhodococcus. Use of immobilized cells allowed the 2-day preparatory stage to be omitted and a complete thioanisole bioconversion to be achieved in 24 h in the case that biocatalyst and 0.5 g/l thioanisole were added simultaneously. The biocatalyst immobilized on gel provides for complete thioanisole transformation into (S)-thioanisole sulfoxide (optical purity of 82.1%) at high (1.0–1.5 g/l) concentrations of sulfide substrate.     

Production of high fructose syrup from <Emphasis Type="Italic">Asparagus</Emphasis> inulin using immobilized exoinulinase from <Emphasis Type="Italic">Kluyveromyces marxianus</Emphasis> YS-1

Extracellular exoinulinase from Kluyveromyces marxianus YS-1, which hydrolyzes inulin into fructose, was immobilized on Duolite A568 after partial purification by ethanol precipitation and gel exclusion chromatography on Sephadex G-100. Optimum temperature of immobilized enzyme was 55 °C, which was 5 °C higher than the free enzyme and optimal pH was 5.5. Immobilized biocatalyst retained more than 90% of its original activity after incubation at 60 °C for 3 h, whereas in free form its activity was reduced to 10% under same conditions, showing a significant improvement in the thermal stability of the biocatalyst after immobilization. Apparent K _m values for inulin, raffinose and sucrose were found to be 3.75, 28.5 and 30.7 mM, respectively. Activation energy (E _a) of the immobilized biocatalyst was found to be 46.8 kJ/mol. Metal ions like Co²⁺ and Mn²⁺ enhanced the activity, whereas Hg²⁺ and Ag²⁺ were found to be potent inhibitors even at lower concentrations of 1 mM. Immobilized biocatalyst was effectively used in batch preparation of high fructose syrup from Asparagus racemosus raw inulin and pure inulin, which yielded 39.2 and 40.2 g/L of fructose in 4 h; it was 85.5 and 92.6% of total reducing sugars produced, respectively.     

Kinetic aspects of glucose oxidation by Gluconobacter oxydans cells immobilized in calcium alginate

Summary Gluconobacter oxydans subspecies suboxydans (ATCC 621 H), when growing at high glucose concentrations, oxidizes this substrate incompletely and gluconic acid accumulates in the medium in almost stoichiometric amounts. Such cells were harvested and entrapped in various alginate gels. The preparation with the highest retention of glucose oxidizing activity was used in further studies with the aim of developing an efficient process for continuous gluconic acid production.The retention of activity increases (up to 95%) as the alginate concentration in the gel decreases or the cell/alginate weight ratio is enhanced. In the latter case, however, transport of oxygen to and inside the biocatalyst beads rapidly becomes rate-limiting and thus lowers the efficiency of the biocatalyst. Similarly, the efficiency decreases as the size of the biocatalyst beads increases. In no case rate-limitation by transport of glucose was found. Thus, biocatalyst activity per unit volume of support, diameter of the biocatalyst beads, and aeration efficiency are important parameters for reactor design.     

Improvement of the enzymatic synthesis of ethyl valerate by esterification reaction in a solvent system

The present study reports the improved enzymatic synthesis of ethyl valerate (green apple flavor) by esterification reaction of ethanol and valeric acid in heptane medium. Lipase from Thermomyces lanuginosus (TLL) was immobilized by physical adsorption on polyhydroxybutyrate (PHB) particles and used as a potential biocatalyst. The effect of certain parameters that influence the ester synthesis was evaluated by factorial design. The experimental conditions that maximized the synthesis of ethyl valerate were 30.5°C, 18% m/v of biocatalyst (TLL–PHB), absence of molecular sieves, agitation of 234?rpm, and 1,000?mM of each reactant (ethanol and valeric acid). Under these conditions, conversion percentage ≈92% after 105?min of reaction was observed. Soluble TLL was also used as biocatalyst and the highest conversion was of 82% after 120?min of reaction. Esterification reaction performed in a solvent-free system exhibited conversion of 13% after 45?min of reaction catalyzed by immobilized lipase, while the soluble lipase did not exhibit catalytic activity. The synthesis of the ester was confirmed by Fourier transform infrared spectroscopy and gas chromatography–mass spectrometry analyses. After six consecutive cycles of ethyl valerate synthesis, the prepared biocatalyst retained ≈86% of its original activity.     

Enhancement of phase separation by the addition of de-emulsifiers to three-phase (diesel oil/biocatalyst/aqueous phase) emulsion in diesel biodesulfurization

Ethanol, added as a de-emulsifier to separate oil and biocatalyst (or bacterial cells) from a three-phase (oil/biocatalyst/aqueous phase) emulsion, formed in diesel biodesulfurization employing Gordonia nitida, improved oil recovery by centrifugation from about 50% in its absence to almost 100% at 3% (v/v). The biocatalyst recovered with ethanol addition showed similar specific growth rates (0.03 h^–1) and dibenzothiophene desulfurization rates (6–7.2 mol l^–1 h^–1) to those (0.03 h^–1 and 7.1 mol l^–1, respectively) of the biocatalyst recovered with no ethanol addition. The desulfurization activity significantly increased as the number of the repeated recovery and reuse of the biocatalyst.