High-yield production of pure tagatose from fructose by a three-step enzymatic cascade reaction

Objective

To produce tagatose from fructose with a high conversion rate and to establish a high-yield purification method of tagatose from the reaction mixture.

Results

Fructose at 1 M (180 g l^?1) was converted to 0.8 M (144 g l^?1) tagatose by a three-step enzymatic cascade reaction, involving hexokinase, plus ATP, fructose-1,6-biphosphate aldolase, phytase, over 16 h with a productivity of 9 g l^?1 h^?1. No byproducts were detected. Tagatose was recrystallized from ethanol to a purity of 99.9% and a yield of 96.3%. Overall, tagatose at 99.9% purity was obtained from fructose with a yield of 77%.

Conclusion

This is the first biotechnological production of tagatose from fructose and the first application of solvent recrystallization for the purification of rare sugars.

     

Production of δ-decalactone from linoleic acid via 13-hydroxy-9(Z)-octadecenoic acid intermediate by one-pot reaction using linoleate 13-hydratase and whole <Emphasis Type="Italic">Yarrowia lipolytica</Emphasis> cells

Objective

To produce δ-decalactone from linoleic acid by one-pot reaction using linoleate 13-hydratase with supplementation with whole Yarrowia lipolytica cells.

Results

Whole Y. lipolytica cells at 25 g l^?1 produced1.9 g l^?1 δ-decalactone from 7.5 g 13-hydroxy-9(Z)-octadecenoic acid l^?1 at pH 7.5 and 30 °C for 21 h. Linoleate 13-hydratase from Lactobacillus acidophilus at 3.5 g l^?1 with supplementation with 25 g Y. lipolytica cells l^?1 in one pot at 3 h produced 1.9 g l^?1 δ-decalactone from 10 g linoleic acid l^?1 via 13-hydroxy-9(Z)-octadecenoic acid intermediate at pH 7.5 and 30°C after 18 h, with a molar conversion yield of 31 % and productivity of 106 mg l^?1 h^?1.

Conclusion

To the best of our knowledge, this is the first production of δ-decalactone using unsaturated fatty acid.

     

Influence of diligent disintegration on anaerobic biomass and performance of microbial fuel cell

Objectives

To enhance the performance of microbial fuel cells (MFC) by increasing the surface area of cathode and diligent mechanical disintegration of anaerobic biomass.

Results

Tannery effluent and anaerobic biomass were used. The increase in surface area of the cathode resulted in 78% COD removal, with the potential, current density, power density and coulombic efficiency of 675 mV, 147 mA m^?2, 33 mW m^?2 and 3.5%, respectively. The work coupled with increased surface area of the cathode with diligent mechanical disintegration of the biomass, led to a further increase in COD removal of 82% with the potential, current density, power density and coulombic efficiency of 748 mV, 229 mA m^?2, 78 mW m^?2 and 6% respectively.

Conclusions

Mechanical disintegration of the biomass along with increased surface area of cathode enhances power generation in vertical MFC reactors using tannery effluent as fuel.

     

Enhancing substrate utilization and power production of a microbial fuel cell with nitrogen-doped carbon aerogel as cathode catalyst

Objectives

Catalytic efficiency of a nitrogen-doped, mesoporous carbon aerogel cathode catalyst was investigated in a two-chambered microbial fuel cell (MFC) applying graphite felt as base material for cathode and anode, utilizing peptone as carbon source.

Results

This mesoporous carbon aerogel containing catalyst layer on the cathode increased the maximum power density normalized to the anode volume to 2.7 times higher compared to the maximum power density obtained applying graphite felt cathode without the catalyst layer. At high (2 and 3) cathode/anode volume ratios, maximum power density exceeded 40 W m^?3. At the same time, current density and specific substrate utilization rate increased by 58% resulting in 31.9 A m^?3 and 18.8 g COD m^?3 h^?1, respectively (normalized to anode volume). Besides the increase of the power and the rate of biodegradation, the investigated catalyst decreased the internal resistance from the range of 450–600 to 350–370 Ω.

Conclusions

Although Pt/C catalyst proved to be more efficient, a considerable decrease in the material costs might be achieved by substituting it with nitrogen-doped carbon aerogel in MFCs. Such cathode still displays enhanced catalytic effect.

     

Engineering the intracellular metabolism of <Emphasis Type="Italic">Escherichia coli</Emphasis> to produce gamma-aminobutyric acid by co-localization of GABA shunt enzymes

Objectives

To direct the carbon flux from Krebs cycle into the gamma-aminobutyric acid (GABA) shunt pathway for the production of GABA by protein scaffold introduction in Escherichia coli.

Results

Escherichia coli was engineered to produce GABA from glucose by the co-localization of enzymes succinate semialdehyde dehydrogenase (GadD), GABA aminotransferase (PuuE) and GABA transporter (GadC) by protein scaffold. 0.7 g GABA l^?1 was produced from 10 g glucose l^?1 while no GABA was produced in wild type E. coli. pH 6 and 30 °C were optimum for GABA production, and GABA concentration increased to 1.12 g GABA l^?1 when 20 g glucose l^?1 was used. When competing metabolic networks were inactivated, GABA increased by 24 % (0.87 g GABA l^?1).

Conclusions

The novel GABA production system was constructed by co-localization of GABA shunt enzymes.

     

Characterization of rhamnolipid biosurfactants produced by recombinant <Emphasis Type="Italic">Pseudomonas aeruginosa</Emphasis> strain DAB with removal of crude oil

Objectives

To improve rhamnolipid production and its potential application in removal of crude oil, the recombinant Pseudomonas aeruginosa strain DAB was constructed to enhance yield of rhamnolipids.

Results

Strain DAB had a higher yield of 17.3 g rhamnolipids l^?1 in the removal process with crude oil as the sole carbon source than 10 g rhamnolipids l^?1 of wild-type strain DN1, where 1% crude oil was degraded more than 95% after 14 days cultivation. These rhamnolipids reduced the surface tension of water from 72.92 to 26.15 mN m^?1 with CMC of 90 mg l^?1. The predominant rhamnolipid congeners were Rha–C₁₀–C₁₀ and Rha–Rha–C₁₀–C₁₀ detected by MALDI-TOF MS analysis with approx. 70% relative abundance, although a total of 21 rhamnolipid congeners were accumulated.

Conclusion

Increasing the copy number of rhlAB genes efficiently enhanced the production of rhamnolipids by the recombinant P. aeruginosa DAB and thus presents a promising application for the bioremediation process.

     

Characterization of a flavin-containing monooxygenase from <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> and its application to production of indigo and indirubin

Objective

To examine the role of a gene encoding flavin-containing monooxygenase (cFMO) from Corynebacterium glutamicum ATCC13032 when cloned and expressed in Escherichia coli for the production of indigo pigments.

Results

The blue pigments produced by recombinant E. coli were identified as indigo and indirubin. The cFMO was purified as a fused form with maltose-binding protein (MBP). The enzyme was optimal at 25 °C and pH 8. From absorption spectrum analysis, the cFMO was classified as a flavoprotein. FMO activity was strongly inhibited by 1 mM Cu²⁺ and recovered by adding 1–10 mM EDTA. The enzyme catalyzed the oxidation of TMA, thiourea, and cysteamine, but not glutathione or cysteine. MBP-cFMO had an indole oxygenase activity through oxygenation of indole to indoxyl. The recombinant E. coli produced 685 mg indigo l^?1 and 103 mg indirubin l^?1 from 2.5 g l-tryptophan l^?1.

Conclusion

The results suggest the cFMO can be used for the microbial production of both indigo and indirubin.

     

CaCO<Subscript>3</Subscript> supplementation alleviates the inhibition of formic acid on acetone/butanol/ethanol fermentation by <Emphasis Type="Italic">Clostridium acetobutylicum</Emphasis>

Objective

To investigate the inhibiting effect of formic acid on acetone/butanol/ethanol (ABE) fermentation and explain the mechanism of the alleviation in the inhibiting effect under CaCO₃ supplementation condition.

Results

From the medium containing 50 g sugars l^?1 and 0.5 g formic acid l^?1, only 0.75 g ABE l^?1 was produced when pH was adjusted by KOH and fermentation ended prematurely before the transformation from acidogenesis to solventogenesis. In contrast, 11.4 g ABE l^?1 was produced when pH was adjusted by 4 g CaCO₃ l^?1. The beneficial effect can be ascribed to the buffering capacity of CaCO₃. Comparative analysis results showed that the undissociated formic acid concentration and acid production coupled with ATP and NADH was affected by the pH buffering capacity of CaCO₃. Four millimole undissociated formic acid was the threshold at which the transformation to solventogenesis occurred.

Conclusion

The inhibiting effect of formic acid on ABE fermentation can be alleviated by CaCO₃ supplementation due to its buffering capacity.

     

Uptake and biotransformation of pure commercial microcystin-LR versus microcystin-LR from a natural cyanobacterial bloom extract in the aquatic fungus <Emphasis Type="Italic">Mucor hiemalis</Emphasis>

Objectives

To evaluate the remediation efficiency of Mucor hiemalis by comparing media elimination, uptake, and biotransformation of microcystin-LR with exposure to pure toxin versus a crude bloom extract.

Results

With exposure to the extract, the elimination rate of microcystin-LR from the media, which was 0.28 ng MC-LR l^?1 h^?1, was significantly higher compared to that achieved with exposure to the pure toxin (0.16 ng MC-LR l^?1 h^?1) after 24 h. However, intracellular breakdown of microcystin-LR was significantly lower in the extract exposed pellets compared to the pure toxin treated fungal pellets over time. This coincided with reduced intracellular glutathione S-transferase activity with crude extract exposure which could be responsible for the detection of only the glutathione conjugate of microcystin-LR.

Conclusion

This paper signifies the importance of using laboratory exposure scenarios which resemble conditions in nature to fully understand and evaluate remediation efficiency. There is merit in using M. hiemalis for mycoremediation of cyanotoxins in surface waters.

     

Rapid evolution of hyaluronan synthase to improve hyaluronan production and molecular mass in <Emphasis Type="Italic">Bacillus subtilis</Emphasis>

Objectives

To improve the production and molecular mass of the glycosaminoglycan hyaluronan (HA) in Bacillus subtilis by engineering hyaluronan synthase (HAS) from Streptococcus zooepidemicus.

Results

By mutating regions within HAS intracellular domains, five positive variants exhibiting higher HA production (from 1.22 to 2.24 g l^?1) and molecular mass values (from 1.20 to 1.36 × 10⁶ Da) were constructed and characterized. Overexpression of the V5 variant and the genes tuaD and glmU increased HA production and molecular mass to 2.8 g l^?1 and 2.4 × 10⁶ Da, respectively.

Conclusions

This study provides a novel strategy for improving HA production and its molecular mass.

     

Conversion of glycerol to 1,3-dihydroxyacetone by glycerol dehydrogenase co-expressed with an NADH oxidase for cofactor regeneration

Objectives

To investigate the efficiency of a cofactor regeneration enzyme co-expressed with a glycerol dehydrogenase for the production of 1,3-dihydroxyacetone (DHA).

Results

In vitro biotransformation of glycerol was achieved with the cell-free extracts containing recombinant GlyDH (glycerol dehydrogenase from Escherichia coli), LDH (lactate dehydrogenase form Bacillus subtilis) or LpNox1 (NADH oxidase from Lactobacillus pentosus), giving DHA at 1.3 g l^?1 (GlyDH/LDH) and 2.2 g l^?1 (GlyDH/LpNox1) with total turnover number (TTN) of NAD⁺ recycling of 6039 and 11100, respectively. Whole cells of E. coli (GlyDH–LpNox1) co-expressing both GlyDH and LpNox1 were constructed and converted 10 g glycerol l^?1 to DHA at 0.2–0.5 g l^?1 in the presence of zero to 2 mM exogenous NAD⁺. The cell free extract of E. coli (GlyDH–LpNox) converted glycerol (2–50 g l^?1) to DHA from 0.5 to 4.0 g l^?1 (8–25 % conversion) without exogenous NAD⁺.

Conclusions

The disadvantage of the expensive consumption of NAD⁺ for the production of DHA has been overcome.

     

Maximizing power generation from dark fermentation effluents in microbial fuel cell by selective enrichment of exoelectrogens and optimization of anodic operational parameters

Objective

To selectively enrich an electrogenic mixed consortium capable of utilizing dark fermentative effluents as substrates in microbial fuel cells and to further enhance the power outputs by optimization of influential anodic operational parameters.

Results

A maximum power density of 1.4 W/m³ was obtained by an enriched mixed electrogenic consortium in microbial fuel cells using acetate as substrate. This was further increased to 5.43 W/m³ by optimization of influential anodic parameters. By utilizing dark fermentative effluents as substrates, the maximum power densities ranged from 5.2 to 6.2 W/m³ with an average COD removal efficiency of 75% and a columbic efficiency of 10.6%.

Conclusion

A simple strategy is provided for selective enrichment of electrogenic bacteria that can be used in microbial fuel cells for generating power from various dark fermentative effluents.

     

Improved production of carotenoid-free welan gum in a genetic-engineered <Emphasis Type="Italic">Alcaligenes</Emphasis> sp. ATCC31555

Objective

To improve the production of welan gum and obtain a carotenoid-free strain while reducing the fermentation and post-treatment costs.

Results

The vitreoscilla globin (vgb) gene combined with the β-galactosidase (lacZ) promoter was inserted into the phytoene synthase (crtB) gene region of the chromosome in Alcaligenes sp. ATCC31555. When the recombinant strain was grown in a 5 l fermentor, welan gum was produced at 24 ± 0.4 g l^?1 compared to 21 g ± 0.4 g l^?1 in the wild type. Furthermore, the carotenoid-free welan gum produced using Alcaligenes sp. ATCC31555 VHb strain was less expensive with improved properties.

Conclusions

Alcaligenes sp. ATCC31555 VHb strain was a better neutral welan-producing strain with a higher production than the wild-type strain.

     

Characterization of a novel asparaginase from soil metagenomic libraries generated from forest soil

Objectives

To screen soil metagenomic libraries for novel enzymes with enhanced activities.

Results

To screen soil metagenomic libraries for novel enzymes with enhanced activities. A novel l-asparaginase was identified from forest soil metagenome and its characteristics were studied. The purified protein had a specific activity of 696 IU mg^?1 and optimum activity at pH 7 and 35 °C. Enhanced enzyme activities were observed in the presence of Mg²⁺, Ca²⁺ and K⁺. The K_m value, 2 mM, and enzyme specificity constant 7.7 mM^?1s^?1 indicated that the recombinant enzyme has good substrate affinity to l-asparagine compared with commercially-available Escherichia coli asparaginase. The IC₅₀ value of 0.78 µg ml^?1 (0.47 IU ml^?1) was observed with HL60 cell line and 0.39 µg ml^?1(0.23 IU ml^?1) with MOLT-3 and MOLT-4 cell lines, which is better than that of commercially-available drugs.

Conclusion

The soil metagenome derived l-asparaginase with enhanced activities could be a potential candidate to develop as a drug in Acute Lymphoblastic Leukemia (ALL) therapy.

     

Production of <Emphasis Type="Italic">trans</Emphasis>-10,<Emphasis Type="Italic">cis</Emphasis>-12-conjugated linoleic acid using permeabilized whole-cell biocatalyst of <Emphasis Type="Italic">Yarrowia lipolytica</Emphasis>

Objective

To improve the production of trans-10,cis-12-conjugated linoleic acid (t10,c12-CLA) from linoleic acid in recombinant Yarrowia lipolytica.

Results

Cells of the yeast were permeabilized by freeze/thawing. The optimal conditions for t10,c12-CLA production by the permeabilized cells were at 28 °C, pH 7, 200 rpm with 1.5 g sodium acetate l^?1, 100 g wet cells l^?1, and 25 g LA l^?1. Under these conditions, the permeabilized cells produced 15.6 g t10,c12-CLA l^?1 after 40 h, with a conversion yield of 62 %. The permeabilized cells could be used repeatedly for three cycles, with the t10,c12-CLA extracellular production remaining above 10 g l^?1.

Conclusion

Synthesis of t10,c12-CLA was achieved using a novel method, and the production reported in this work is the highest value reported to date.

     

Effects of light intensity and quality on phycobiliprotein accumulation in the cyanobacterium <Emphasis Type="Italic">Nostoc sphaeroides</Emphasis> Kützing

Objectives

To assess the effects of light intensity and quality on the growth and phycobiliproteins (PBP) accumulation in Nostoc sphaeroides Kützing (N. sphaeroides).

Results

Dry weights, dry matter, protein, chlorophyll and PBP contents were higher under 90 μmol m^?2 s^?1 than under other intensities (both higher and lower). Phycocyanin and allophycocyanin increased with light intensity while phycoerythrin decreased. Fresh weights, protein and PBP contents increased at the highest rates under blue light. Red light resulted in higher values of dry matter, phycocyanin and chlorophyll a.

Conclusion

White light at 90 μmol m^?2 s^?1 or blue light 30 μmol m^?2 s^?1 were optimal for the growth and phycobiliprotein accumulation in N. sphaeroides.

     

Co-expression of <Emphasis Type="SmallCaps">l</Emphasis>-glutamate oxidase and catalase in <Emphasis Type="Italic">Escherichia coli</Emphasis> to produce α-ketoglutaric acid by whole-cell biocatalyst

Objectives

To improve the production of α-ketoglutaric acid (α-KG) from l-glutamate by whole-cell biocatalysis.

Results

A novel and highly active l-glutamate oxidase, SmlGOX, from Streptomyces mobaraensis was overexpressed and purified. The recombinant SmlGOX was approx. 64 kDa by SDS-PAGE. SmlGOX had a maximal activity of 125 ± 2.7 U mg^?1 at pH 6.0, 35 ^oC. The apparent K_m and V_max values of SmlGOX were 9.3 ± 0.5 mM and 159 ± 3 U mg^?1, respectively. Subsequently, a co-expression plasmid containing the SmlGOX and KatE genes was constructed to remove H₂O₂, and the protein levels of SmlGOX were improved by codon optimization. Finally, by optimizing the whole-cell transformation conditions, the production of α-KG reached 77.4 g l^?1 with a conversion rate from l-glutamate of 98.5% after 12 h.

Conclusions

An efficient method for the production of α-KG was established in the recombinant Escherichia coli, and it has a potential prospect in industrial application.

     

Increased production of plumbagin in <Emphasis Type="Italic">Plumbago indica</Emphasis> root cultures by biotic and abiotic elicitors

Objectives

To evaluate the effects of 12 biotic and abiotic elicitors for increasing the production of plumbagin in Plumbago indica root cultures.

Results

Most elicitors showed minimal effects on the root dry weight, except for 250 mg chitosan l^?1 and 10 mM l-alanine that markedly decreased root biomass by about 40 % compared to the untreated root cultures (5 g l^?1). Treatments with 100 µM AgNO₃ significantly increased intracellular plumbagin production by up to 7.6 mg g^?1 DW that was 4-fold more than the untreated root cultures (1.9 mg g^?1 DW). In contrast, treatments with 150 mg chitosan l^?1, 5 mM l-alanine, and 50 µM 1-naphthol significantly enhanced the extracellular secretion of plumbagin by up to 10.6, 6.9, and 5.7 mg g^?1 DW, respectively, and increased the overall production of plumbagin by up to 12.5, 12.5, and 9.4 mg g^?1 DW, respectively.

Conclusions

Chitosan (150 mg l^?1), l-alanine (5 mM), and 1-naphthol (50 µM) were the best elicitors to enhance plumbagin production in P. indica root cultures.

     

Isolation and characterization of a novel <Emphasis Type="SmallCaps">l</Emphasis>-glutamate oxidase with strict substrate specificity from <Emphasis Type="Italic">Streptomyces diastatochromogenes</Emphasis>

Objectives

To find an l-glutamate oxidase (LGox), to be used for the quantitative analysis of l-glutamic acid, an lgox gene encoding LGox from Streptomyces diastatochromogenes was isolated, cloned and characterized.

Results

The gene had an ORF of 1974 bp encoding a protein of 657 amino acid residues. In comparison to the LGox precursor, the proteinase K-treated enzyme exhibited improved affinity to substrate and with a K _m of 0.15 mM and V _max of 62 μmol min^?1 mg^?1. The 50% thermal inactivation temperature of the proteinase K treated enzyme was increased from 50 to 70 °C. The enzyme exhibited strict specificity for l-glutamate.

Conclusions

LGox treated by proteinase K exhibited strict specificity for l-glutamate, good thermostability and high substrate affinity.

     

Rapid and efficient degradation of bisphenol A by chloroperoxidase from <Emphasis Type="Italic">Caldariomyces fumago</Emphasis>: product analysis and ecotoxicity evaluation of the degraded solution

Objectives

To degrade enzymatically bisphenol A (BPA) that causes serious environmental concerns and is difficult to be degraded by chemical or physical methods.

Results

BPA (150 mg l^?1) was completely degraded by chloroperoxidase (CPO)/H₂O₂ within 7 min at room temperature, atmospheric pressure with the enzyme at 6 μg CPO ml^?1. The degradation products were identified by HPLC–MS, which suggested involvement of multiple steps. Enzymatic treatment followed by existing bioremediation technologies (activated sludge) enhanced removal of COD from 9 to 54 %. Using an ecotoxicity evaluation with Chlorella pyrenoidosa, the degradation products had a lower toxicity than BPA.

Conclusion

BPA can be degraded rapidly and efficiently under mild conditions with chloroperoxidase at 6 μg ml^?1. The degradation products had a lower toxicity than BPA.