Ethanol and acetate synthesis from waste gas using batch culture of Clostridium ljungdahlii

Single inorganic carbon source was used for production of chemicals and fuels via fermentation processes. Clostridium ljungdahlii, a strictly anaerobic autotrophic bacterium, was grown on synthesis gas to produce acetate and ethanol from gaseous substrates. C. ljungdahlii was grown on a various concentrations of carbon monoxide with synthesis gas total pressures of 0.8–1.8 atm with an interval of 0.2 atm. The cell and product yields were 0.015 g cell/g CO and 0.41 g acetate/g CO, respectively. Formation of acetate was steady and the production trend was about the same for all of the gases initial pressure and at constant cell density. The ethanol concentration was enhanced by the initial presence of hydrogen and carbon dioxide in the liquid phase. There was no substrate inhibition while C. ljungdahlii was grown in the batch fermentation, even at high system pressure of 1.6 and 1.8 atm. A desired product molar ratio of ethanol:acetate (5:1) was achieved with total gas pressure of 1.6 and 1.8 atm.     

High-level De novo biosynthesis of arbutin in engineered Escherichia coli

Arbutin is a hydroquinone glucoside compound existing in various plants. It is widely used in pharmaceutical and cosmetic industries owing to its well-known skin-lightening property as well as anti-oxidant, anti-microbial, and anti-inflammatory activities. Currently, arbutin is usually produced by plant extraction or enzymatic processes, which suffer from low product yield and expensive processing cost. In this work, we established an artificial pathway in Escherichia coli for high-level production of arbutin from simple carbon sources. First, a 4-hydroxybenzoate 1-hydroxylase from Candida parapsilosis CBS604 and a glucosyltransferase from Rauvolfia serpentina were characterized by in vitro enzyme assays. Introduction of these two genes into E. coli led to the production of 54.71 mg/L of arbutin from glucose. Further redirection of carbon flux into arbutin biosynthesis pathway by enhancing shikimate pathway genes enabled production of 3.29 g/L arbutin, which is a 60-fold increase compared with the initial strain. Final optimization of glucose concentration added in the culture medium was able to further improve the titer of arbutin to 4.19 g/L in shake flasks experiments, which is around 77-fold higher than that of initial strain. This work established de novo biosynthesis of arbutin from simple carbon sources and provided a generalizable strategy for the biosynthesis of shikimate pathway derived chemicals. The high titer achieved in our engineered strain also indicates the potential for industrial scale bio-manufacturing of arbutin.     

Novel minor lipase from Rhizopus chinensis during solid-state fermentation: Biochemical characterization and its esterification potential for ester synthesis

Rhizopus chinensis produces two lipases that catalyze ester synthesis when cultured under solid-state fermentation. The Lip2 was purified to homogeneity by ammonium sulphate precipitation, hydrophobic interaction chromatography and gel filtration chromatography. It has an apparent molecular weight of 33 kDa estimated from SDS–PAGE and 32 kDa calculated from analytical gel permeation, with synthetic activity and purification fold of 96.8 U/mg and 138.3, respectively. Maximum hydrolytic activity was obtained at pH 8.0–8.5 and 40 °C using pNPP as substrate. Slight activation of the enzyme was observed when Mn²⁺ is present. The enzyme was most active on p-nitrophenyl laurate (C12). The purified lipase exhibited maximum synthetic activity at pH memory of 6.0 and 30 ^oC. Most of ethyl esters synthesized by lyophilized enzyme achieved good yields (>90%), and caprylic acid served as the best acyl donor. The enzyme presented a particular affinity for ethanol, n-propanol and n-hexanol, with conversion of 92%, 93% and 92%, respectively, after 20 h incubation.     

Medium optimization for the high yield production of single (+)-terrein by Aspergillus terreus strain PF26 derived from marine sponge Phakellia fusca

Terrein has potential application in the fields of medicine, cosmetology and agriculture, however, the chemical synthesis of terrein with single configuration is a difficult task, and the biosynthesis of terrein always results in low production (ca. 0.33–400 mg/L). In this study, we reported an Aspergillus terreus strain PF26 which could produce (+)-terrein on a high level. After the selection of a suitable basic medium, the component concentrations were optimized using Plackett–Burman design and response surface methodology. Consequently, an optimal medium containing 28.41 g glucose, 23.18 g maltose, 20.00 g mannitol, 8.52 g malt extract, 10.00 g monosodium glutamate 10.00 g NH₄Cl in 1 L ASW was obtained, and a high (+)-terrein production of 3.71 g/L fermentation broth was achieved, which represents the highest fermentation production of (+)-terrein to date. The result highlighted the industry's potential of A. terreus strain PF26 in the production of bioactive (+)-terrein on a large-scale.     

The stability and thermodynamic parameters of a very thermostable and calcium-independent α-amylase from a newly isolated bacterium,Anoxybacillus beppuensis TSSC-1

Anoxybacillus beppuensis TSSC-1 (GenBank Number, EU710556), a thermophilic bacterium isolated from a hot spring reservoir, was found to optimally secrete a monomeric α-amylase at 55 °C and pH 7. The enzyme was purified to homogeneity by a single-step purification on phenyl sepharose 6FF, achieving a 58% yield, 10,000 U/mg specific activity and 19.5 fold purification. The molecular weight, K_m and V_max were 43 kD, 0.5 mg ml^?1 and 3571.42 μmol ml^?1 m^?1, respectively. The enzymatic catalysis of soluble starch was optimum at 80 °C and pH 7. The thermodynamic parameters, K_d, t_1/2, ΔH*, ΔS*, E and ΔG*, were consistent. The very compact structure of the enzyme and the transitional enzyme–substrate complex resisted denaturation at extreme temperatures and alkaline pH. The K_d and t_1/2 measurements were consistent with the high thermostability and pH tolerance observed. The structural stability of the enzyme was also reflected by the values of ΔH*, ΔS*, E and ΔG*. While the enzyme did not exhibit metal ion dependency, it was resistant to chemical denaturation. The broad thermo- and pH-tolerance of this enzyme suggests potential commercial opportunities.     

Improvement of succinate production by overexpression of a cyanobacterial carbonic anhydrase in Escherichia coli

Succinate fermentation was investigated in Escherichia coli strains overexpressing cyanobacterium Anabaena sp. 7120 ecaA gene encoding carbonic anhydrase (CA). In strain BL21 (DE3) bearing ecaA, the activity of CA was 21.8 U mg⁻¹ protein, whereas non-detectable CA activity was observed in the control strain. Meanwhile, the activity of phosphoenolpyruvate carboxylase (PEPC) increased from 0.2 U mg⁻¹ protein to 1.13 U mg⁻¹ protein. The recombinant bearing ecaA reached a succinate yield of 0.39 mol mol⁻¹ glucose at the end of the fermentation. It was 2.1-fold higher than that of control strain which was just 0.19 mol mol⁻¹ glucose. EcaA gene was also introduced into E. coli DC1515, which was deficient in glucose phosphotransferase, lactate dehydrogenase and pyruvate:formate lyase. Succinate yield can be further increased to 1.26 mol mol⁻¹ glucose. It could be concluded that the enhancement of the supply of HCO₃⁻ in vivo by ecaA overexpression is an effective strategy for the improvement of succinate production in E. coli.     

Structural characterization of thermostable,solvent tolerant,cytosafe tannase from Bacillus subtilis PAB2

Tannase production by Bacillus subtilis PAB2, was investigated under solid state fermentation using tamarind seed as sole carbon source and it was found as the highest titer (73.44 U/gds). The enzyme was purified to homogeneity, which showed the molecular mass around 52 kDa (K_m = 0.445 mM, V_max = 125.8 mM/mg/min and K_cat = 2.88 min^–1). The enzyme was found stable in a range of pH (3.0–8.0) and temperature (30–70 °C) with an optimal activity at pH 5.0, pI of 4.4 and at 40 °C temperature. It exhibited half-life (t_1/2) of 4.5 h at 60 °C. The enzyme comprised a typical secondary structure containing α-helix (9.3%), β-pleated sheet (33.6%) and β-turn (17.2%). The native conformation of the enzyme was alike a 44 nm spherical nanoparticle upon aggregation. Thermodynamic parameters of tannase revealed that it was stable at 40 °C and showed Q₁₀, ΔG_d and ΔS_d values of 2.08, 99.37 KJ/mol and 252.38 J mol⁻¹ K⁻¹, respectively. Organic solvents were stimulatory with regard to enzyme activity. Moreover, the altered enzyme activity was determined to be correlated with the changes in structural conformation in presence of inducer and inhibitor. Tannase was explored to have no cytotoxicity on Vero cell line as well as rat model study.     

Enhanced production of (+)-terrein by Aspergillus terreus strain PF26 with epigenetic modifier suberoylanilide hydroxamic acid

New strategies for improving the fermentation yield of (+)-terrein which is a fungal metabolite with multiple bioactivities are very urgent. In this study, the effect of suberoylanilide hydroxamic acid, one kind of epigenetic modifier, on the biosynthesis of (+)-terrein by Aspergillus terreus strain PF26 isolated from the marine sponge Phakellia fusca was investigated. It was found that suberoylanilide hydroxamic acid exhibited a positive impact on (+)-terrein production, resulting from promoting the biosynthesis of 6-hydroxymellein, the precursor of (+)-terrein. Through optimization of feeding concentration and time of suberoylanilide hydroxamic acid, 5.58 g/L (+)-terrein could be obtained in shake flask cultivation, 29.5% higher than the control. Correspondingly, the fermentation of A. terreus strain PF26 in 7.5-L stirred bioreactor with feeding suberoylanilide hydroxamic acid (900 μM, day 4) yielded 9.07 g/L (+)-terrein, 77.1% higher than the control. These results showed that the epigenetic modifier-suberoylanilide hydroxamic acid could be utilized to enhance the production of (+)-terrein, which laid the foundation of massive production of (+)-terrein by fermentation.     

Correlation of pigment production with mycelium morphology in extractive fermentation of Monascus anka GIM 3.592

Extractive fermentation with nonionic surfactants is a potential method for producing Monascus pigments. In this study, the correlation between mycelium morphology and pigment production was investigated in extractive fermentation of Monascus anka GIM 3.592. The results demonstrated that pigment biosynthesis was associated with mycelial morphology and the accumulation of granular inclusions in cells. The physiological status in terms of hyphal and pellet diameters exhibited an excellent correlation with pigment accumulation, especially the yield of extracellular pigment in extractive fermentation (r > 0.85, p < 0.05). Nonionic surfactants could reduce pigment yield by influencing the morphology of hyphae and mycelium pellets. High yields of both intracellular and extracellular pigments could be achieved by controlling variations in hyphal diameters in two-stage extractive fermentation. Moreover, continuous extractive fermentation led to stable pigment production, with a relatively high productivity of total pigments reaching 72.3 AU/day. This study proposed a simple method for monitoring pigment biosynthesis in extractive fermentation using mycelium morphology as an indicating factor.     

Dihydroxyacetone production in an engineered Escherichia coli through expression of Corynebacterium glutamicum dihydroxyacetone phosphate dephosphorylase

Dihydroxyacetone (DHA) has several industrial applications such as a tanning agent in tanning lotions in the cosmetic industry; its production via microbial fermentation would present a more sustainable option for the future. Here we genetically engineered Escherichia coli (E. coli) for DHA production from glucose. Deletion of E. coli triose phosphate isomerase (tpiA) gene was carried out to accumulate dihydroxyacetone phosphate (DHAP), for use as the main intermediate or precursor for DHA production. The accumulated DHAP was then converted to DHA through the heterologous expression of Corynebacterium glutamicum DHAP dephosphorylase (cghdpA) gene. To conserve DHAP exclusively for DHA production we removed methylglyoxal synthase (mgsA) gene in the ΔtpiA strain. This drastically improved DHA production from 0.83 g/l (0.06 g DHA/g glucose) in the ΔtpiA strain bearing cghdpA to 5.84 g/l (0.41 g DHA/g glucose) in the ΔtpiAΔmgsA double mutant containing the same gene. To limit the conversion of intracellular DHA to glycerol, glycerol dehydrogenase (gldA) gene was further knocked out resulting in a ΔtpiAΔmgsAΔgldA triple mutant. This triple mutant expressing the cghdpA gene produced 6.60 g/l of DHA at 87% of the maximum theoretical yield. In summary, we demonstrated an efficient system for DHA production in genetically engineered E. coli strain.     

Over expression of GroESL in Cupriavidus necator for heterotrophic and autotrophic isopropanol production

We previously reported a metabolic engineering strategy to develop an isopropanol producing strain of Cupriavidus necator leading to production of 3.4 g L⁻¹ isopropanol. In order to reach higher titers, isopropanol toxicity to the cells has to be considered. A toxic effect of isopropanol on the growth of C. necator has been indeed observed above a critical value of 15 g L⁻¹. GroESL chaperones were first searched and identified in the genome of C. necator. Native groEL and groES genes from C. necator were over-expressed in a strain deleted for PHA synthesis. We demonstrated that over-expressing groESL genes led to a better tolerance of the strain towards exogenous isopropanol. GroESL genes were then over-expressed within the best engineered isopropanol producing strain. A final isopropanol concentration of 9.8 g L⁻¹ was achieved in fed-batch culture on fructose as the sole carbon source (equivalent to 16 g L⁻¹ after taking into account evaporation). Cell viability was slightly improved by the chaperone over-expression, particularly at the end of the fermentation when the isopropanol concentration was the highest. Moreover, the strain over-expressing the chaperones showed higher enzyme activity levels of the 2 heterologous enzymes (acetoacetate carboxylase and alcohol dehydrogenase) of the isopropanol synthetic operon, translating to a higher specific production rate of isopropanol at the expense of the specific production rate of acetone. Over-expressing the native chaperones led to a 9–18% increase in the isopropanol yield on fructose.     

Selection of an endogenous 2,3-butanediol pathway in Escherichia coli by fermentative redox balance

Fermentative redox balance has long been utilized as a metabolic evolution platform to improve efficiency of NADH-dependent pathways. However, such system relies on the complete recycling of NADH and may become limited when the target pathway results in excess NADH stoichiometrically. In this study, endogenous capability of Escherichia coli for 2,3-butanediol (2,3-BD) synthesis was explored using the anaerobic selection platform based on redox balance. To address the issue of NADH excess associated with the 2,3-BD pathway, we devised a substrate-decoupled system where a pathway intermediate is externally supplied in addition to the carbon source to decouple NADH recycling ratio from the intrinsic pathway stoichiometry. In this case, feeding of the 2,3-BD precursor acetoin effectively restored anaerobic growth of the mixed-acid fermentation mutant that remained otherwise inhibited even in the presence of a functional 2,3-BD pathway. Using established 2,3-BD dehydrogenases as model enzyme, we verified that the redox-based selection system is responsive to NADPH-dependent reactions but with lower sensitivity. Based on this substrate-decoupled selection scheme, we successfully identified the glycerol/1,2-propanediol dehydrogenase (Ec-GldA) as the major enzyme responsible for the acetoin reducing activity (k_cat/K_m≈0.4 mM⁻¹ s⁻¹) observed in E. coli. Significant shift of 2,3-BD configuration upon withdrawal of the heterologous acetolactate decarboxylase revealed that the endogenous synthesis of acetoin occurs via diacetyl. Among the predicted diacetyl reductase in E. coli, Ec-UcpA displayed the most significant activity towards diacetyl reduction into acetoin (V_max≈6 U/mg). The final strain demonstrated a meso-2,3-BD production titer of 3 g/L without introduction of foreign genes. The substrate-decoupled selection system allows redox balance regardless of the pathway stoichiometry thus enables segmented optimization of different reductive pathways through enzyme bioprospecting and metabolic evolution.     

Metabolic engineering of Clostridium tyrobutyricum for enhanced butyric acid production from glucose and xylose

Clostridium tyrobutyricum is a promising microorganism for butyric acid production. However, its ability to utilize xylose, the second most abundant sugar found in lignocellulosic biomass, is severely impaired by glucose-mediated carbon catabolite repression (CCR). In this study, CCR in C. tyrobutyricum was eliminated by overexpressing three heterologous xylose catabolism genes (xylT, xylA and xlyB) cloned from C. acetobutylicum. Compared to the parental strain, the engineered strain Ct-pTBA produced more butyric acid (37.8 g/L vs. 19.4 g/L) from glucose and xylose simultaneously, at a higher xylose utilization rate (1.28 g/L·h vs. 0.16 g/L·h) and efficiency (94.3% vs. 13.8%), resulting in a higher butyrate productivity (0.53 g/L·h vs. 0.26 g/L·h) and yield (0.32 g/g vs. 0.28 g/g). When the initial total sugar concentration was ~120 g/L, both glucose and xylose utilization rates increased with increasing their respective concentration or ratio in the co-substrates but the total sugar utilization rate remained almost unchanged in the fermentation at pH 6.0. Decreasing the pH to 5.0 significantly decreased sugar utilization rates and butyrate productivity, but the effect was more pronounced for xylose than glucose. The addition of benzyl viologen (BV) as an artificial electron carrier facilitated the re-assimilation of acetate and increased butyrate production to a final titer of 46.4 g/L, yield of 0.43 g/g sugar consumed, productivity of 0.87 g/L·h, and acid purity of 98.3% in free-cell batch fermentation, which were the highest ever reported for butyric acid fermentation. The engineered strain with BV addition thus can provide an economical process for butyric acid production from lignocellulosic biomass.     

Heterologous expression of codon optimized Trichoderma reesei Cel6A in Pichia pastoris

The Cel6A deficiency has become one of the limiting factors for cellulose saccharification in biochemical conversion of cellulosic biomass to fuels and chemicals. The work attempted to use codon optimization to enhance Trichoderma reesei Cel6A expression in Pichia pastoris. Two recombinants P. pastoris GS115 containing AOX1 and GAP promotors were successfully constructed, respectively. The optimal temperatures and pHs of the expressed Cel6A from two recombinants were consistent with each other, were also in the extremely similar range to that reported on the native Cel6A from T. reesei. Based on the shake flask fermentation, AOX1 promotor enabled the recombinant to produce 265 U/L and 300 mg/L of the Cel6A enzyme, and the GAP promotor resulted in 145 U/L and 200 mg/L. High cell density fed batch (HCDFB) fermentation significantly improved the enzyme titer (1100 U/L) and protein yield (2.0 g/L) for the recombinant with AOX1 promotor. Results have showed that the AOX1 promotor is more suitable than the GAP for the Cel6A expression in P. pastoris. And the HCDFB cultivation is a favorable way to express the Cel6A highly in the methanol inducible yeast.     

Enhancing GDP-fucose production in recombinant Escherichia coli by metabolic pathway engineering

Guanosine 5′-diphosphate (GDP)-fucose is the indispensible donor substrate for fucosyltransferase-catalyzed synthesis of fucose-containing biomolecules, which have been found involving in various biological functions. In this work, the salvage pathway for GDP-fucose biosynthesis from Bacterioides fragilis was introduced into Escherichia coli. Besides, the biosynthesis of guanosine 5′-triphosphate (GTP), an essential substrate for GDP-fucose biosynthesis, was enhanced via overexpression of enzymes involved in the salvage pathway of GTP biosynthesis. The production capacities of metabolically engineered strains bearing different combinations of recombinant enzymes were compared. The shake flask fermentation of the strain expressing Fkp, Gpt, Gmk and Ndk obtained the maximum GDP-fucose content of 4.6 ± 0.22 μmol/g (dry cell mass), which is 4.2 fold that of the strain only expressing Fkp. Through fed-batch fermentation, the GDP-fucose content further rose to 6.6 ± 0.14 μmol/g (dry cell mass). In addition to a better productivity than previous fermentation processes based on the de novo pathway for GDP-fucose biosynthesis, the established schemes in this work also have the advantage to be a potential avenue to GDP-fucose analogs encompassing chemical modification on the fucose residue.     

Coordination of metabolic pathways: Enhanced carbon conservation in 1,3-propanediol production by coupling with optically pure lactate biosynthesis

Metabolic engineering has emerged as a powerful tool for bioproduction of both fine and bulk chemicals. The natural coordination among different metabolic pathways contributes to the complexity of metabolic modification, which hampers the development of biorefineries. Herein, the coordination between the oxidative and reductive branches of glycerol metabolism was rearranged in Klebsiella oxytoca to improve the 1,3-propanediol production. After deliberating on the product value, carbon conservation, redox balance, biological compatibility and downstream processing, the lactate-producing pathway was chosen for coupling with the 1,3-propanediol-producing pathway. Then, the other pathways of 2,3-butanediol, ethanol, acetate, and succinate were blocked in sequence, leading to improved d-lactate biosynthesis, which as return drove the 1,3-propanediol production. Meanwhile, efficient co-production of 1,3-propanediol and l-lactate was also achieved by replacing ldhD with ldhL from Bacillus coagulans. The engineered strains PDL-5 and PLL co-produced over 70 g/L 1,3-propanediol and over 100 g/L optically pure d-lactate and l-lactate, respectively, with high conversion yields of over 0.95 mol/mol from glycerol.     

Enhanced production of periplasmic interferon alpha-2b by Escherichia coli using ion-exchange resin for in situ removal of acetate in the culture

The possibility of using in situ addition of anion-exchange resin for the removal of acetate in the culture aimed at improving growth of E. coli and expression of periplasmic human interferon-α2b (PrIFN-α2b) was studied in shake flask culture and stirred tank bioreactor. Different types of anion-exchange resin were evaluated and the concentration of anion-exchange resin was optimized using response surface methodology. The addition of anion-exchange resins reduced acetate accumulation in the culture, which in turn, improved growth of E. coli and enhanced PrIFN-α2b expression. The presence of anion-exchange resins did not influence the physiology of the cells. The weak base anion-exchange resins, which have higher affinity towards acetate, yielded higher PrIFN-α2b expression as compared to strong anion-exchange resins. High concentrations of anion-exchange resin showed inhibitory effect towards growth of E. coli as well as the expression of PrIFN-α2b. The maximum yield of PrIFN-α2b in shake flask culture (501.8 μg/L) and stirred tank bioreactor (578.8 μg/L) was obtained at ion exchange resin (WA 30) concentration of 12.2 g/L. The production of PrIFN-α2b in stirred tank bioreactor with the addition of ion exchange resin was about 1.8-fold higher than that obtained in fermentation without ion exchange resin (318.4 μg/L).     

Dynamic control of the mevalonate pathway expression for improved zeaxanthin production in Escherichia coli and comparative proteome analysis

Engineered heterologous multi-gene metabolic pathways often suffer from flux imbalance and toxic metabolites, as the production host typically lacks the regulatory mechanisms for the heterologous pathway. Here, we first coordinated the expression of all genes of the mevalonate (MEV) pathway from Saccharomyces cerevisiae using the tunable intergenic regions (TIGRs), and then dynamically regulated the TIGR-mediated MEV pathway to prevent the accumulation of toxic metabolites by using IPP/FPP-responsive promoter. After introduction of the dynamically controlled TIGR-mediated MEV pathway into Escherichia coli, the content and concentration of zeaxanthin in shaker flask cultures were 2.0- and 2.1-fold higher, respectively, than those of the strain harboring the statically controlled non-TIGR-mediated MEV pathway. The content and concentration of zeaxanthin in E. coli ZEAX (pZSP_gadE-MevT_TIGR-MevB_TIGRIS-2) reached 722.46 mg/L and 23.16 mg/g dry cell weight (DCW), respectively, in 5.0 L fed-batch fermentation. We also comparatively analyzed the proteomes between E. coli ZEAX and E. coli ZEAX (pZSP_gadE-MevT_TIGR-MevB_TIGRIS-2) to understand the mechanism of zeaxanthin biosynthesis. The results of the comparative proteomes demonstrate that zeaxanthin overproduction may be associated with increased precursor availability, increased NADPH availability, increased ATP availability, oxidative stress response, and increased membrane storage capacity for zeaxanthin due to changes in both cellular shape and membrane composition.     

Characterization of an extracellular thermophilic alkaline esterase produced by Bacillus subtilis DR8806

This work is a report of the characterization of an alkaline lipolytic enzyme isolated from Bacillus subtilis DR8806. The extracellular extract was concentrated using ammonium sulfate, and ultrafiltration. The active enzyme was purified by Q-sepharose ion exchange chromatography. The molecular mass of the enzyme was estimated to be 60.25 kDa based on SDS-PAGE (sodium dodecyl sulfate polyacrylamide gel electrophoresis). The optimum pH and temperature of this enzyme were observed to be 8.0 and 50 °C, respectively. The enzyme exhibited a half-life of 72 min at its optimum temperature. It was stable in the presence of metal ions (10 mM) such as Ca²⁺, K⁺ and Na⁺, whereas Cu²⁺, Fe²⁺, Zn²⁺, Mn²⁺, Co²⁺, Mg²⁺ and Hg²⁺ were found to have inhibitory effects. However, the enzyme activity was not affected significantly by 1% Triton X-100. The study of substrate specificity showed that the purified enzyme has a preferential specificity for small ester of p-nitrophenyl acetate (C₂), and it was the most efficiently hydrolyzed substrate as compared to the other esters. The kinetic parameters showed that the enzyme has K_m of 4.2 mM and V_max of 151 μmol min⁻¹ mg⁻¹ for p-nitrophenyl acetate. The hydrolysis rates of the fluorescence substrates were increased in the presence of the purified enzyme. Regarding the features of the enzyme, it may be utilized as a novel candidate for industrial applications.