Bioconversion of farnesol and 1,4-dihydroxy-2-naphthoate to menaquinone by an immobilized whole-cell biocatalyst using engineered <Emphasis Type="Italic">Elizabethkingia meningoseptica</Emphasis>

Menaquinone (MK) has important applications in the pharmaceutical and food industries. To increase the production rate (Q_P) of MK-4, we developed a straightforward biotransformation method for MK-4 synthesis directly from its precursors 1,4-dihydroxy-2-naphthoate (DHNA) and farnesol using whole cells of genetically engineered Elizabethkingia meningoseptica. Results showed that MK-4 can be produced directly from farnesol and DHNA using both free and immobilized FM-D198 cells. MK-4 yield peaked at 29.85?±?0.36 mg/L in the organic phase and 24.08?±?0.33 mg/g DCW after 12 h of bioconversion using free cells in a two-phase conversion system. MK-4 yield reached 26.34?±?1.35 mg/L and 17.44?±?1.05 mg/g DCW after 8 h using immobilized cells. Although this yield was lower than that using free cells, immobilized cells can be re-used for MK-4 production via repeated-batch culture. After ten batch cultures, efficient MK-4 production was maintained at a yield of more than 20 mg/L. After optimizing the catalysis system, the MK-4 yield reached 26.91?±?1.27 mg/L using the immobilized cells and had molar conversion rates of 58.56 and 76.90% for DHNA and farnesol, respectively.     

Influence of SiO<Subscript>2</Subscript> Spacer Layer Thickness on Performance of Plasmonic Textured Silicon Solar Cell

We investigated the effect of SiO₂ spacer layer thickness between the textured silicon surface and silver nanoparticles (Ag NPs) on solar cell performance using quantum efficiency analysis. Separation of Ag NPs from high index silicon with SiO₂ layer led to modified absorption and scattering cross-sections due to graded refractive index medium. The forward scattering from Ag NPs is very sensitive to SiO₂ layer thickness in plasmonic silicon cell performance due to the evanescent character of generated near-fields around the NPs. With the optimized ～30–40 nm SiO₂ spacer layer, we observed an enhancement of solar cell efficiency from ～8.7 to ～10 %, which is due to the photocurrent enhancement in the off-resonance surface plasmon region. We also estimated minority carrier diffusion lengths (L _eff) from internal quantum efficiency data, which are also sensitive to SiO₂ spacer layer thickness. We observed that the L _eff values are enhanced from ～356 to ～420 μm after placing Ag NPs on ～40 nm spacer layer due to improved forward (angular) scattering of light from the Ag NPs into silicon.     

Difference analysis of the enzymatic hydrolysis performance of acid-catalyzed steam-exploded corn stover before and after washing with water

The difference in the enzymatic hydrolysis yield of acid-catalyzed steam-exploded corn stover (ASC) before and after washing with water reached approximately 15 % under the same conditions. The reasons for the difference in the yield between ASC and washed ASC (wASC) were determined through the analysis of the composition of ASC prehydrolyzate and sugar concentration of enzymatic hydrolyzate. Salts produced by neutralization (CaSO₄, Na₂SO₄, K₂SO₄, and (NH₄)₂SO₄), sugars (polysaccharides, oligosaccharides, and monosaccharides), sugar-degradation products (weak acids and furans), and lignin-degradation products (ethyl acetate extracts and nine main lignin-degradation products) were back-added to wASC. Results showed that these products, except furans, exerted negative effect on enzymatic hydrolysis. According to the characteristics of acid-catalyzed steam explosion pretreatment, the five sugar-degradation products’ mixture and salts [Na₂SO₄, (NH₄)₂SO₄] showed minimal negative inhibition effect on enzymatic hydrolysis. By contrast, furans demonstrated a promotion effect. Moreover, soluble sugars, such as 13 g/L xylose (decreased by 6.38 %), 5 g/L cellobiose (5.36 %), 10 g/L glucose (3.67 %), as well as lignin-degradation products, and ethyl acetate extracts (4.87 %), exhibited evident inhibition effect on enzymatic hydrolysis. Therefore, removal of soluble sugars and lignin-degradation products could effectively promote the enzymatic hydrolysis performance.     

Molecular cloning and characterization of a GH11 endoxylanase from Chaetomium globosum, and its use in enzymatic pretreatment of biomass

An endo-1,4-β-xylanase gene, xylcg, was cloned from Chaetomium globosum and successfully expressed in Escherichia coli. The complete gene of 675 bp was amplified, cloned into the pET 28(a) vector, and expressed. The optimal conditions for the highest activity of the purified recombinant XylCg were observed at a temperature of 40 °C and pH of 5.5. Using oat-spelt xylan, the determined K _m, V _max, and k _cat/K _m values were 0.243 mg?ml^?1, 4,530 U?mg^?1 protein, and 7,640 ml?s^?1?mg^?1, respectively. A homology model and sequence analysis of XylCg, along with the biochemical properties, confirmed that XylCg belongs to the GH11 family. Rice straw pretreated with XylCg showed 30 % higher conversion yield than the rice straw pretreated with a commercial xylanase. Although xylanases have been characterized from fungal and bacterial sources, C. globosum XylCg is distinguished from other xylanases by its high catalytic efficiency and its effectiveness in the pretreatment of lignocellulosic biomass.     

Esterification of Levulinic Acid Using ZrO<Subscript>2</Subscript>-Supported Phosphotungstic Acid Catalyst for Ethyl Levulinate Production

Ethyl levulinate (EL) is a versatile bio-based chemical with various applications such as fragrance and flavoring agents and also fuel blending component. EL can be produced through catalytic esterification of levulinic acid (LA) with ethanol. Herein, a series of zirconia (ZrO₂)-supported phosphotungstic acid (HPW) (HPW/Zr) catalyst, 15-HPW/Zr, 20-HPW/Zr, and 25-HPW/Zr, were prepared, characterized, and tested for EL production. The physicochemical properties of catalysts were characterized using Fourier-transformed infrared (FTIR) spectroscopy, x-ray diffraction (XRD), field emission scanning electron microscope (FESEM), N₂ physisorption, and ammonia temperature-programmed desorption (NH₃-TPD). The effect of reaction parameters: reaction time, temperature, catalyst loading, and molar ratio of LA to ethanol was inspected on LA conversion and EL yield. The catalyst with high surface area and high acidity seemed suitable for EL production. Among the catalysts tested, 20-HPW/Zr exhibited the highest EL yield of 97.3% at the following conditions: 150 °C, 3 h, 1.0 g of 20-HPW/Zr and 1:17 M ratio of LA to ethanol. The 20-HPW/Zr could be reused for at least four times with insignificant decrease in the EL yield. This study demonstrates the potential of ZrO₂-supported HPW for bio-based alkyl levulinate production at mild process conditions.     

Production,purification, characterization and usage of a detergent additive of endoglucanase from isolated halotolerant Amycolatopsis cihanbeyliensis mutated strain Mut43

The Amycolatopsis cihanbeyliensis Mut43, which is obtained by UV radiation, exhibited endoglucanase activity of 5.21?U/mL, which was ～2.3-fold higher than that of the wild strain (2.04?U/mL). The highest enzyme activity was obtained after 3 days of incubation at 32?°C, pH 7.0, 150?rpm, and 6% NaCl in a liquid medium containing 1.5% (w/v) wheat straw (0.25?mm of particle size) and 0.6% (w/v) yeast extract. Enzyme activity was eluted as a single peak (gel filtration chromatography), and Sodium dodecyl sulfate–polyacrylamide gel electrophoresis (SDS–PAGE) analysis of the corresponding peak revealed a molar mass of 30?kDa. Zymogram analysis confirmed the presence of a single active endoglucanase component. The enzyme was purified to ～21-fold, and the mean overall yield was ～6%. The purified endoglucanase was active up to 80?°C and showed a half-life of 214?min at 60?°C in the absence of substrate at pH 8.0. The apparent K_m value for the purified endoglucanase was 0.70?mg/mL, while the V_max value was 6.20 Units/μg. Endoglucanase activity was reduced (25%) by treatment with 30?U of proteinase K/mg. The addition of Mg⁺² and Ca⁺² (5?mM) enhanced endoglucanase activity. Additionally, endoglucanase activity in the presence of 5?mM SDS or organic solvents was 75 and 50% of maximum activity, respectively. The high levels of enzyme production from A. cihanbeyliensis Mut43 achieved under batch conditions, coupled with the temperature stability, activity over a broad pH range, relatively high stability (70–80%) in the presence of industrial laundry detergents and storage half-lives of 45 days at +4?°C and 75 days at ?20?°C signify the suitability of this enzyme for industrial applications as detergent additive.     

Nutrient Flows and Quality of Bio-crude Oil Produced via Catalytic Hydrothermal Liquefaction of Low-Lipid Microalgae

Five heterogeneous and two alkaline catalysts were applied into the hydrothermal liquefaction (HTL) of Chlorella pyrenoidosa, a low-lipid microalgal species. The effects of catalysts on the bio-crude oil yield were more substantial at 280?ºC (bio-crude oil yield was increased by 10 %) than at 240?ºC although bio-crude oil formation had already occurred at the low temperature. At 240?ºC, additions of catalyst could improve the boiling point distribution of bio-crude oil. At 280?ºC, addition of alkaline catalysts increased the fractions of compounds with high boiling points due to the formation of nitrogen and oxygen heterocyclic compounds. The majority of nitrogen (59～68 %) and phosphorus (52～86 %) content in the feedstock remained in the aqueous phase after the HTL process, implying the possible feasibility to reuse the nutrients in the post-HTL water. Carbon deposition and mineral mixing were found on the surface of metal catalysts after HTL.     

Alkaline-sulfite pretreatment and use of surfactants during enzymatic hydrolysis to enhance ethanol production from sugarcane bagasse

Sugarcane bagasse is a by-product from the sugar and ethanol industry which contains approximately 70 % of its dry mass composed by polysaccharides. To convert these polysaccharides into fuel ethanol it is necessary a pretreatment step to increase the enzymatic digestibility of the recalcitrant raw material. In this work, sugarcane bagasse was pretreated by an alkaline-sulfite chemithermomechanical process for increasing its enzymatic digestibility. Na₂SO₃ and NaOH ratios were fixed at 2:1, and three increasing chemical loads, varying from 4 to 8 % m/m Na₂SO₃, were used to prepare the pretreated materials. The increase in the alkaline-sulfite load decreased the lignin content in the pretreated material up to 35.5 % at the highest chemical load. The pretreated samples presented enhanced glucose yields during enzymatic hydrolysis as a function of the pretreatment severity. The maximum glucose yield (64 %) was observed for the samples pretreated with the highest chemical load. The use of 2.5 g l^?1 Tween 20 in the hydrolysis step further increased the glucose yield to 75 %. Semi-simultaneous hydrolysis and fermentation of the pretreated materials indicated that the ethanol yield was also enhanced as a function of the pretreatment severity. The maximum ethanol yield was 56 ± 2 % for the sample pretreated with the highest chemical load. For the sample pretreated with the lowest chemical load (2 % m/m NaOH and 4 % m/m Na₂SO₃), adding Tween 20 during the hydrolysis process increased the ethanol yield from 25 ± 3 to 39.5 ± 1 %.     

Sequential Thermochemical Hydrolysis of Corncobs and Enzymatic Saccharification of the Whole Slurry Followed by Fermentation of Solubilized Sugars to Ethanol with the Ethanologenic Strain <Emphasis Type="Italic">Escherichia coli</Emphasis> MS04

Interest in the use of corncobs as feedstock for bioethanol production is growing. This study assesses the feasibility of sequential thermochemical diluted sulfuric acid pretreatment of corncobs at moderate temperature to hydrolyze the hemicellulosic fraction, followed by enzymatic hydrolysis of the whole slurry, and fermentation of the obtained syrup. The total sugar concentration after enzymatic hydrolysis was 85.21 g/l, i.e., 86 % of the sugars were liberated from the polymeric fractions, together with a low amount of furfural (0.26 g/l) and 4.01 g/l of acetic acid. The syrups, which contained 36.3, 40.9, 4.47, and 1.84 g/l of xylose, glucose, arabinose, and mannose, respectively, were fermented (pH 7, 37 °C, 150 rpm) to ethanol with the metabolically engineered acetate-tolerant Escherichia coli strain MS04 under non-aerated conditions, producing 35 g/l of ethanol in 18 h (1.94 g_EtOH/l/h), i.e., a conversion yield greater than 80 % of the theoretical value based on total sugars was obtained. Hence, using the procedures developed in this study, 288 l of ethanol can be produced per metric ton of dry corncobs. Strain MS04 can ferment sugars in the presence of acetate, and the amount of furans generated during the sequential thermochemical and enzymatic hydrolysis was low; hence, the detoxification step was avoided. The residual salts, acetic acid, and solubilized lignin present in the syrup did not interfere with the production of ethanol by E. coli MS04 and the results show that this strain can metabolize mixtures of glucose and xylose simultaneously.     

DFT study of conductive properties of three polymers formed by bicyclic furans

Density functional theory methods were employed to study the electronic, structural and conductive properties of classical bicyclic furans. In this paper, studies of monomers, oligomers and polymers of furo[3,4-b]furan, furo[2,3-b]furan and furo[3,2-b]furan are presented. To gain detailed information on conjugational degree, we selected the nucleus-independent chemical shift as a method for examining the changes in conjugational degree. Furthermore, three parameters of density of state, effective mass (m*) and kinetic model of mobility (μ) were also investigated. The variable trends of all parameters from monomers to tetramers indicate that poly(4,4′-bifuro[3,4-b]furan), poly(trans-2,2′-bifuro[3,2-b]furan) and poly(cis-2,2′-bifuro[3,2-b]furan) are good candidates for conductive materials, which are consistent with band structure analyses showing that the three polymers had narrower band gaps (1.21, 1.93 and 1.89 eV, respectively) than other polymers.     

Effect of static magnetic field on electricity production and wastewater treatment in microbial fuel cells

The effect of a magnetic field (MF) on electricity production and wastewater treatment in two-chamber microbial fuel cells (MFCs) has been investigated. Electricity production capacity could be improved by the application of a low-intensity static MF. When a MF of 50 mT was applied to MFCs, the maximum voltage, total phosphorus (TP) removal efficiency, and chemical oxygen demand (COD) removal efficiency increased from 523?±?2 to 553?±?2 mV, ～93 to ～96 %, and ～80 to >90 %, respectively, while the start-up time and coulombic efficiency decreased from 16 to 10 days and ～50 to ～43 %, respectively. The MF effects were immediate, reversible, and not long lasting, and negative effects on electricity generation and COD removal seemed to occur after the MF was removed. The start-up and voltage output were less affected by the MF direction. Nitrogen compounds in magnetic MFCs were nitrified more thoroughly; furthermore, a higher proportion of electrochemically inactive microorganisms were found in magnetic systems. TP was effectively removed by the co-effects of microbe absorption and chemical precipitation. Chemical precipitates were analyzed by a scanning electron microscope capable of energy-dispersive spectroscopy (SEM-EDS) to be a mixture of phosphate, carbonate, and hydroxyl compounds.     

Free fatty acid production in Escherichia coli under phosphate-limited conditions

Microbially synthesized fatty acids are an attractive platform for producing renewable alternatives to petrochemically derived transportation fuels and oleochemicals. Free fatty acids (FFA) are a direct precursor to many high-value compounds that can be made via biochemical and ex vivo catalytic pathways. To be competitive with current petrochemicals, flux through these pathways must be optimized to approach theoretical yields. Using a plasmid-free, FFA-producing strain of Escherichia coli, a set of chemostat experiments were conducted to gather data for FFA production under phosphate limitation. A prior study focused on carbon-limited conditions strongly implicated non-carbon limitations as a preferred media formulation for maximizing FFA yield. Here, additional data were collected to expand an established kinetic model of FFA production and identify targets for further metabolic engineering. The updated model was able to successfully predict the strain’s behavior and FFA production in a batch culture. The highest yield observed under phosphate-limiting conditions (0.1 g FFA/g glucose) was obtained at a dilution rate of 0.1 h^?1, and the highest biomass-specific productivity (0.068 g FFA/gDCW/h) was observed at a dilution rate of 0.25 h^?1. Phosphate limitation increased yield (～45 %) and biomass-specific productivity (～300 %) relative to carbon-limited cultivations using the same strain. FFA production under phosphate limitation also led to a cellular maintenance energy ～400 % higher (0.28 g/gDCW/h) than that seen under carbon limitation.     

Bioconversion of p-coumaric acid to p-hydroxystyrene using phenolic acid decarboxylase from B. amyloliquefaciens in biphasic reaction system

Phenolic acid decarboxylase (PAD) catalyzes the non-oxidative decarboxylation of p-coumaric acid (pCA) to p-hydroxystyrene (pHS). PAD from Bacillus amyloliquefaciens (BAPAD), which showed k _cat/K _m value for pCA (9.3?×?10³?mM^?1?s^?1), was found as the most active one using the “Subgrouping Automata” program and by comparing enzyme activity. However, the production of pHS of recombinant Escherichia coli harboring BAPAD showed only a 22.7 % conversion yield due to product inhibition. Based on the partition coefficient of pHS and biocompatibility of the cell, 1-octanol was selected for the biphasic reaction. The conversion yield increased up to 98.0 % and 0.83 g/h/g DCW productivity was achieved at 100 mM pCA using equal volume of 1-octanol as an organic solvent. In the optimized biphasic reactor, using a three volume ratio of 1-octanol to phosphate buffer phase (50 mM, pH 7.0), the recombinant E. coli produced pHS with a 88.7 % conversion yield and 1.34 g/h/g DCW productivity at 300 mM pCA.     

Acidic resin-catalysed conversion of fructose into furan derivatives in low boiling point solvents

Conversion of fructose into furan derivatives 5-hydroxymethylfurfural (HMF) and 5-methoxymethylfurfural (MMF) is performed in tetrahydrofuran (THF) and methanol–organic solvent systems, catalysed by an acidic resin Amberlyst-15. The melted fructose can be converted into HMF on the surface of the solid resin catalyst in the presence of THF as an extracting phase, which is a good solvent for HMF and other by-products. The solid resin catalyst can be reused eleven times without losing its catalytic ability, with an average HMF yield of approximately 50%. Upon the addition of methanol, the generated HMF can further react with methanol to form MMF, and the total yield of HMF and MMF could be promoted to 65%. GC–MS analysis confirms the formation of a small amount of methyl levulinate in methanolorganic solvent system.     

Biomass production potential of grasslands in the oak savanna region of Minnesota, USA

Biomass harvested from grasslands formerly used for forage production or set aside for conservation has been identified as a potential source of bioenergy feedstocks. Our objective was to characterize yield and chemical composition of biomass harvested from existing grasslands in the oak savanna region of Minnesota and to determine whether aggregated soil properties and grassland type influence biomass yield and feedstock properties. The influence of soil type and dominant functional plant groups on biomass yield, theoretical ethanol yield, and mineral, ash, and lignocellulosic concentration was measured on biomass harvested from 32 grassland sites. Soils with high productivity ratings, as measured by the Minnesota Crop Productivity Index, produced 36 % more biomass than lower quality soils. Grasslands dominated by warm-season species produced 18 % more biomass than those dominated by cool-season species, when measured after senescence during the late-fall harvest time. Biomass harvested from sites dominated by cool-season grasses had higher N, Mg and Cl concentrations than those dominated by warm-season grasses, suggesting that such grasslands could have lower efficiency in thermochemical conversion processes and that repeated harvesting from such grasslands could remove nutrients from the systems. In addition, glucose and xylose concentrations were slightly higher in biomass from sites dominated by warm-season grasses, which resulted in an estimated additional 12 L?Mg^?1 of ethanol over those dominated by cool-season grasses. Combined with the greater yields, warm-season grasslands could produce an additional 376 L?ha^?1 year^?1.     

Potentiation of cystic fibrosis transmembrane conductance regulator (CFTR) Cl− currents by the chemical solvent tetrahydrofuran

The chemical solvent tetrahydrofuran (THF) increases short-circuit current (I_sc) in renal epithelia endogenously expressing the cystic fibrosis transmembrane conductance regulator (CFTR). To understand how THF increases I_sc, we employed the Ussing chamber and patch-clamp techniques to study cells expressing recombinant human CFTR. THF increased I_sc in Fischer rat thyroid (FRT) epithelia expressing wild-type CFTR with half-maximal effective concentration (K_D) of 134?mM. This THF-induced increase in I_sc was enhanced by forskolin (10 µM), inhibited by the PKA inhibitor H-89 (10 µM) and the thiazolidinone CFTR_inh-172 (10 µM) and attenuated greatly in FRT epithelia expressing the cystic fibrosis mutants F508del- and G551D-CFTR. By contrast, THF (100?mM) was without effect on untransfected FRT epithelia, while other solvents failed to increase I_sc in FRT epithelia expressing wild-type CFTR. In excised inside-out membrane patches, THF (100?mM) potentiated CFTR Cl^? channels open in the presence of ATP (1?mM) alone by increasing the frequency of channel openings without altering their duration. However, following the phosphorylation of CFTR by PKA (75?nM), THF (100?mM) did not potentiate channel activity. Similar results were obtained with the ?R-S660A-CFTR Cl^? channel that is not regulated by PKA-dependent phosphorylation and using 2′deoxy-ATP, which gates wild-type CFTR more effectively than ATP. Our data suggest that THF acts directly on CFTR to potentiate channel gating, but that its efficacy is weak and dependent on the phosphorylation status of CFTR.     

Conversion of acid hydrolysate of oil palm empty fruit bunch to L-lactic acid by newly isolated Bacillus coagulans JI12

Cost-effective conversion of lignocellulose hydrolysate to optically pure lactic acid is commercially attractive but very challenging. Bacillus coagulans JI12 was isolated from natural environment and used to produce L-lactic acid (optical purity?>?99.5 %) from lignocellulose sugars and acid hydrolysate of oil palm empty fruit bunch (EFB) at 50 °C and pH 6.0 without sterilization of the medium. In fed-batch fermentation with 85 g/L initial xylose and 55 g/L xylose added after 7.5 h, 137.5 g/L lactic acid was produced with a yield of 98 % and a productivity of 4.4 g/L?h. In batch fermentation of a sugar mixture containing 8.5 % xylose, 1 % glucose, and 1 % L-arabinose, the lactic acid yield and productivity reached 98 % and 4.8 g/L?h, respectively. When EFB hydrolysate was used, 59.2 g/L of lactic acid was produced within 9.5 h at a yield of 97 % and a productivity of 6.2 g/L?h, which are the highest among those ever reported from lignocellulose hydrolysates. These results indicate that B. coagulans JI12 is a promising strain for industrial production of L-lactic acid from lignocellulose hydrolysate.     

Characterization of a novel endo-β-1,4-glucanase from Armillaria gemina and its application in biomass hydrolysis

A novel endo-β-1,4-glucanase (EG)-producing strain was isolated and identified as Armillaria gemina KJS114 based on its morphology and internal transcribed spacer rDNA gene sequence. A. gemina EG (AgEG) was purified using a single-step purification by gel filtration. The relative molecular mass of AgEG by sodium dodecyl sulfate polyacrylamide gel electrophoresis was 65 kDa and by size exclusion chromatography was 66 kDa, indicating that the enzyme is a monomer in solution. The pH and temperature optima for hydrolysis were 5.0 and 60 °C, respectively. Purified AgEG had the highest catalytic efficiency with carboxymethylcellulose (k _cat/K _m?=?3,590 mg mL^?1 s^?1) unlike that reported for any fungal EG, highlighting the significance of the current study. The amino acid sequence of AgEG showed homology with hydrolases from the glycoside hydrolase family 61. The addition of AgEG to a Populus nigra hydrolysate reaction containing a commercial cellulase mixture (Celluclast 1.5L and Novozyme 188) showed a stimulatory effect on reducing sugar production. AgEG is a good candidate for applications that convert lignocellulosic biomass to biofuels and chemicals.     

Conversion of levulinic acid to 2-butanone by acetoacetate decarboxylase from Clostridium acetobutylicum

In this study, a novel system for synthesis of 2-butanone from levulinic acid (γ-keto-acid) via an enzymatic reaction was developed. Acetoacetate decarboxylase (AADC; E.C. 4.1.1.4) from Clostridium acetobutylicum was selected as a biocatalyst for decarboxylation of levulinic acid. The purified recombinant AADC from Escherichia coli successfully converted levulinic acid to 2-butanone with a conversion yield of 8.4–90.3 % depending on the amount of AADC under optimum conditions (30 °C and pH 5.0) despite that acetoacetate, a β-keto-acid, is a natural substrate of AADC. In order to improve the catalytic efficiency, an AADC-mediator system was tested using methyl viologen, methylene blue, azure B, zinc ion, and 2,2-azino-bis(3-ethylbenzothiazoline-6-sulfonic acid) as mediators. Among them, methyl viologen showed the best performance, increasing the conversion yield up to 6.7-fold in comparison to that without methyl viologen. The results in this study are significant in the development of a renewable method for the synthesis of 2-butanone from biomass-derived chemical, levulinic acid, through enzymatic decarboxylation.