Optimisation of extracellular tannase production from <Emphasis Type="Italic">Paecilomyces variotii</Emphasis>

The tannase production by Paecilomyces variotii was confirmed by high performance thin layer chromatography (HPTLC), and substrate specificity of the tannase was determined by zymogram analysis in sodium dodecyl sulphate-polyacrylamide gel electrophoresis (SDS–PAGE). A clear band of activity observed after electrophoresis of culture filtrate in non-denaturing gels indicated the production of extracellular tannase by P. varoitii. HPTLC analysis revealed that gallic acid was the enzymatic degradation product of tannic acid during the fermentation process. The optimum condition for tannase production was at 72 h of incubation in shaking condition and addition of 1.5% tannic acid, 1% glucose and 0.2% sodium nitrate at temperature of 35°C and pH of 5–7. The production of extracellular tannase from Paecilomyces variotii was investigated under optimized conditions in solid-state fermentation (SSF), submerged fermentation (SmF) and liquid surface fermentation (LSF) processes. The maximum extracellular tannase production was obtained within 60 h of incubation under SSF followed by SmF and LSF.     

Fungal cultures of tar bush and creosote bush for production of two phenolic antioxidants (Pyrocatechol and Gallic acid)

‘Tar bush’ and ‘creosote bush’ were substrates of fungal cultivation for tannase production and gallic acid and pyrocatechol accumulation. Aspergillus niger GH1 grew similarly on both plant materials under solid state culture conditions, reaching maximal levels after 4 d. Fungal strain degraded all tannin content of creosote bush after 4 d of fermentation and >75 % of tar bush after 5 d. Higher level of tannase activity was detected in tar bush fermentation. Biotransformation of tannins to gallic acid was high (93 % in creosote bush and 89 % in tar bush). Pyrocatechol was released poorly. Kinetic parameters of tannin conversion were calculated.     

Co-production of tannase and gallic acid by a novel Penicillium rolfsii (CCMB 714)

Abstract

A novel tannase and gallic acid-producing Penicillium rolfsii (CCMB 714) was isolated from cocoa leaves from the South of Bahia. The influence of nutritional sources and the simultaneous effect of parameters involved in the fermentation process were available. Tannase (9.97 U?mL^?1) and gallic acid (9?mg mL^?1) production were obtained in 48?h by submerged fermentation in non-optimized conditions. Among the carbon sources, tested gallic acid and tannic acid showed the highest tannase production (p<.05) when compared with methyl gallate and glucose. After optimization using the temperature and tannic acid concentration as variables with the Central Compound Rotational Design (CCRD), the maximal tannase production (25.6?U mL^?1) was obtained at 29.8?°C and 12.7%, respectively, which represents an increase of 2.56 times in relation to the initial activity. The parameters optimized for the maximum production of gallic acid (21.51?mg mL^?1) were 30?°C and 10% tannic acid. P. rolfsii CCMB 714 is a new strain with a high tannase and gallic acid production and the gallic acid produced is very important, mainly for its applications in the food and pharmaceutical industry.     

Pestalotiopsis mangiferae isolated from cocoa leaves and concomitant tannase and gallic acid production

The enzyme tannase is of great industrial and biotechnological importance for the hydrolysis of vegetable tannins, reducing their undesirable effects and generating products for a wide range of processes. Thus, the search for new microorganisms that permit more stable tannase production is of considerable importance. A strain of P. mangiferae isolated from cocoa leaves was selected and investigated for its capacity to produce tannase enzymes and gallic acid through submerged fermentation. The assessment of the variables affecting tannase production by P. mangiferae showed that tannic acid, ammonium nitrate and temperature were the most significant (8.4 U/mL). The variables were analyzed using Response Surface Methodology - RSM (Box-Behnken design), with the best conditions for tannase production being: 1.9% carbon source, 1% nitrogen source and temperature of 23 °C. Tannase activity doubled (16.9 U/mL) after the optimization process when compared to the initial fermentation. A pH of 7.0 was optimal for the tannase and it presented stability above 80% with pH between 4.0 and 7.0 after 2h of incubation. The optimal temperature was 30 °C and activity remained at above 80% at 40–60 °C after 1 h. Production of gallic acid was achieved with 1% tannic acid (0.9 mg/mL) and P. mangiferae had not used up the gallic acid produced by tannic acid hydrolysis after 144 h of fermentation. A 5% tannic acid concentration was the best for gallic acid production (1.6 mg/mL). These results demonstrate P. mangiferae’s potential for tannase and gallic acid production for biotechnological applications.     

Production of tannase by Aspergillus niger Aa-20 in submerged and solid-state fermentation: influence of glucose and tannic acid

Tannase production by Aspergillus niger Aa-20 was studied in submerged (SmF) and solid-state (SSF) fermentation systems with different tannic acid and glucose concentrations. Tannase activity and productivity were at least 2.5 times higher in SSF than in SmF. Addition of high tannic acid concentrations increased total tannase activity in SSF, while in SmF it was decreased. In SmF, total tannase activity increased from 0.57 to 1.03 IU/mL, when the initial glucose concentration increased from 6.25 to 25 g/L, but a strong catabolite repression of tannase synthesis was observed in SmF when an initial glucose concentration of 50 g/L was used. In SSF, maximal values of total tannase activity decreased from 7.79 to 2.51 IU when the initial glucose concentration was increased from 6.25 to 200 g/L. Kinetic results on tannase production indicate that low tannase activity titers in SmF could be associated to an enzyme degradation process which is not present in SSF. Tannase titers produced by A. niger Aa-20 are fermentation system-dependent, favoring SSF over SmF. Journal of Industrial Microbiology & Biotechnology (2001) 26, 296–302. Received 07 July 2000/ Accepted in revised form 15 February 2001     

Microbial production of gallic acid by modified solid state fermentation

Bioconversion of tannin to gallic acid from powder of teri pod (Caesalpinia digyna) cover was achieved by the locally isolated fungus, Rhizopus oryzae, in a bioreactor with a perforated float for carrying solid substrate and induced inoculum. Modified Czapek-Dox medium, put beneath the perforated float, with 2% tannic acid at pH 4.5, temperature 32°C, 93% relative humidity, incubated for 3 days with 3-day-old inoculum was optimum for the synthesis of tannase vis-à-vis gallic acid production. Conversion of tannin to gallic acid was 90.9%. Diethyl ether was used as the solvent for extraction of gallic acid from the fermented biomass. Received 14 December 1998/ Accepted in revised form 17 June 1999     

Large-scale production of tannase using the yeast <Emphasis Type="Italic">Arxula adeninivorans</Emphasis>

Tannase (tannin acyl hydrolase, EC 3.1.1.20) hydrolyses the ester and depside bonds of gallotannins and gallic acid esters and is an important industrial enzyme. In the present study, transgenic Arxula adeninivorans strains were optimised for tannase production. Various plasmids carrying one or two expression modules for constitutive expression of tannase were constructed. Transformant strains that overexpress the ATAN1 gene from the strong A. adeninivorans TEF1 promoter produce levels of up to 1,642 U L⁻¹ when grown in glucose medium in shake flasks. The effect of fed-batch fermentation on tannase productivity was then investigated in detail. Under these conditions, a transgenic strain containing one ATAN1 expression module produced 51,900 U of tannase activity per litre after 142 h of fermentation at a dry cell weight of 162 g L⁻¹. The highest yield obtained from a transgenic strain with two ATAN1 expression modules was 31,300 U after 232 h at a dry cell weight of 104 g L⁻¹. Interestingly, the maximum achieved yield coefficients [Y(P/X)] for the two strains were essentially identical.     

Statistical optimization for tannase production from <Emphasis Type="Italic">Aspergillus niger</Emphasis> under submerged fermentation

Statistically based experimental design was employed for the optimization of fermentation conditions for maximum production of enzyme tannase from Aspergillus niger. Central composite rotatable design (CCRD) falling under response surface methodology (RSM) was used. Based on the results of ‘one-at-a-time’ approach in submerged fermentation, the most influencing factors for tannase production from A. niger were concentrations of tannic acid and sodium nitrate, agitation rate and incubation period. Hence, to achieve the maximum yield of tannase, interaction of these factors was studied at optimum production pH of 5.0 by RSM. The optimum values of parameters obtained through RSM were 5% tannic acid, 0.8% sodium nitrate, 5.0 pH, 5 × 10⁷ spores/50mL inoculum density, 150 rpm agitation and incubation period of 48 h which resulted in production of 19.7 UmL⁻¹ of the enzyme. This activity was almost double as compared to the amount obtained by ‘one-at-a-time’ approach (9.8 UmL⁻¹).     

Microbial transformation of tannin-rich substrate to gallic acid through co-culture method

Modified solid-state fermentation (MSSF) of tannin-rich substrate yielding tannase and gallic acid was carried out using a co-culture of the filamentous fungi, Rhizopus oryzae (RO IIT RB-13, NRRL 21498) and Aspergillus foetidus (GMRB013 MTCC 3557). Powdered fruits of Terminalia chebula and powdered pod cover of Caesalpinia digyna was used in the process and the different process parameters for maximum production of tannase and gallic acid by co-culture method were optimized through media engineering. MSSF was carried out at the optimum conditions of 30 degrees C and 80% relative humidity. The optimal pH and incubation period was 5.0 and 48 h respectively. Through the co-culture technique the maximum yield of tannase and gallic acid was found to be 41.3 U/ml and 94.8% respectively.     

Effects of temperature, pH and additives on the activity of tannase produced by a co-culture of Rhizopus oryzae and Aspergillus foetidus

Summary Tannase was produced by modified solid-state fermentation (MSSF) of tannin rich substrates by a co-culture of the two filamentous fungi, Rhizopus oryzae and Aspergillus foetidus. The enzyme thus produced was then partially purified by solvent precipitation and DEAE-Sephadex column chromatography. A study on the effects of temperature and pH was made on the activity of tannase so purified. The optimum values of incubation time, reaction temperature and pH for tannase activity were 5 min, 40 °C and 5.0 respectively. The half-life period thermal stability and kinetic constants (K _m 0.21 mM, V _max 4.9×10⁻² M min^-1 at 40 °C) of this tannase were determined and the effects of different metal ions, surfactants, chelators, denaturants and inhibitors on the enzyme activity were also studied.     

青霉单宁酶高活性菌株的诱变选育

利用塔拉单宁诱导丝状真菌产生单宁酶的原理,通过富集培养,从天然源分离得到30株具有较高单宁酶活性的青霉菌;经二级发酵程序,对这30株菌进行了生物转化复筛实验,选择出能水解塔拉单宁,且生物催化活性较高的青霉野生株Penicilliumsp.No.23,对No.23进行经紫外诱变处理,诱变株经筛选,最后得到1株具有稳定遗传性的单宁酶高活性菌株,其单宁酶活性比出发菌株提高了35%。     

Biotransformation of hydrolysable tannin to ellagic acid by tannase from Aspergillus awamori

Madhuca indica, locally known as mahua in India is a multipurpose tree species. Mahua, particularly bark contains a significant amount of hydrolysable tannin (17.31%) which can be utilized for ellagic acid production through biotransformation. In the present study, mahua bark utilized not only as a raw material for tannase production but also for ellagic acid a well-known therapeutic compound. After prior confirmation of hydrolysable tannin content in bark, it has been supplemented, as a substrate for tannase production through solid state fermentation of Aspergillus awamori. Tannase production, as well as biodegradation of the hydrolysable tannin reached a maximum at 72?h of incubation time. The optimum conditions for tannase production are solid to liquid ratio of 1:2, 35?°C, pH 5.5 and 72h incubation time which resulted 0.256?mg/mL of an extract of ellagic acid. Maximum tannase activity of 56.16?IU/gds at 35?°C and 72h of incubation time is recorded. It seems that tannase production and biotransformation of hydrolysable tannins using bark powder of mahua can be considered as an appropriate alternative to the existing procedures of ellagic acid production.     

Production and Partial Purification of Tannase from Aspergillus ficuum Gim 3.6

A novel fungal strain, Aspergillus ficuum Gim 3.6, was evaluated for its tannase-producing capability in a wheat bran-based solid-state fermentation. Thin-layer chromatography (TLC) analysis revealed that the strain was able to degrade tannic acid to gallic acid and pyrogallol during the fermentation process. Quantitation of enzyme activity demonstrated that this strain was capable of producing a relatively high yield of extracellular tannase. Single-factor optimization of process parameters resulted in high yield of tannase after 60 hr of incubation at a pH of 5.0 at 30°C, 1 mL of inoculum size, and 1:1 solid–liquid ratio in the presence of 2.0% (w/v) tannic acid as inducer. The potential of aqueous two-phase extraction (ATPE) for the purification of tannase was investigated. Influence of various parameters such as phase-forming salt, molecular weight of polyethylene glycol (PEG), pH, and stability ratio on tannase partition and purification was studied. In all the systems, the target enzyme was observed to preferentially partition to the PEG-rich top phase, and the best result of purification (2.74-fold) with an enzyme activity recovery of 77.17% was obtained in the system containing 17% (w/w) sodium citrate and 18.18% (w/w) PEG1000, at pH 7.0.     

Solid state fermentation of Bacillus gottheilii M2S2 in laboratory-scale packed bed reactor for tannase production

Abstract

Production of tannase was performed in packed bed reactor filled with an inert support polyurethane foam (PUF) using Bacillus gottheilii M2S2. The influence of process parameters such as fermentation time (24–72?h), tannic acid concentration (0.5–2.5% w/v), inoculum size (7–12% v/v), and aeration rate (0–0.2?L/min) on tannase production with PUF were analyzed using one variable at a time (OVAT) approach. The outcome of OVAT was optimized by central composite design. Based on the statistical investigation, the proposed mathematical model recommends 1% (w/v) of tannic acid, 10% (v/v) of inoculum size and 0.13?L/min of aeration rate for maximum production (76.57?±?1.25?U/L). The crude enzyme was purified using ammonium sulfate salt precipitation method followed by dialysis. The biochemical properties of partially purified tannase were analyzed and found the optimum pH (4.0), temperature (40?°C) for activity, and K_m (1.077?mM) and V_max (1.11?µM/min) with methyl gallate as a substrate. Based on the SDS-PAGE analysis, tannase exhibited two bands with molecular weights of 57.5 and 42.3?kDa. Briefly, the partially purified tannase showed 4.2 fold increase (63?±?1.60?U/L) in comparison to the submerged fermentation and the production of tannase was validated by using NMR spectrometer.     

Tannase production by Aspergillus aculeatus DBF9 through solid-state fermentation

Tannase an industrially important enzyme was produced by Aspergillus aculeatus DBF9 through a solid-state fermentation (SSF). The organism produced good amount of enzyme and gallic acid in wheat bran among the solid substrate used in SSF. Maximum enzyme and gallic acid production occurred in 5% tannic acid after 72 h. Eighty percent initial substrate moisture and 30 degrees C temperature was found suitable for tannase production.     

A new process for simultaneous production of tannase and phytase by <Emphasis Type="Italic">Paecilomyces variotii</Emphasis> in solid-state fermentation of orange pomace

The production of enzymes such as tannases and phytases by solid-state fermentation and their use in animal feed have become a subject of great interest. In the present work, Paecilomyces variotii was used to produce tannase and phytase simultaneously. Solid-state fermentation, a process initially designed for tannase production, was implemented here using orange pomace as substrate. Orange pomace is the waste product of the large orange juice industry in Brazil, and it has also been used as an ingredient in animal feed. In addition to enzymatic production, biotransformation of the phenolic content and antioxidant capacity of the orange pomace were analyzed after fermentation. Fermentation conditions, namely moisture level and tannic acid concentration rate, were studied using CCD methodology. The response surface obtained indicated that the highest tannase activity was 5,000 U/gds after 96 h at 59% (v/w) and 3% (w/w) and that of phytase was 350 U/gds after 72 h at 66% (v/w) and 5.8% (w/w) of moisture level and tannic acid concentration, respectively. The amount of tannase production was similar to the levels achieved in previous studies, but this was accomplished with a 7% (w/w) reduction in the amount of supplemental tannic acid required. These results are the first to show that P. variotii is capable of producing phytase at significant levels. Moreover, the antioxidant capacity of orange pomace when tested against the free radical ABTS was increased by approximately tenfold as a result of the fermentation process.     

Purification and characterization of tannase from Paecilomyces variotii: hydrolysis of tannic acid using immobilized tannase

An extracellular tannase (tannin acyl hydrolase) was isolated from Paecilomyces variotii and purified from cell-free culture filtrate using ammonium sulfate precipitation followed by ion exchange and gel filtration chromatography. Fractional precipitation of the culture filtrate with ammonium sulfate yielded 78.7% with 13.6-folds purification, and diethylaminoethyl–cellulose column chromatography and gel filtration showed 19.4-folds and 30.5-folds purifications, respectively. Molecular mass of tannase was found 149.8 kDa through native polyacrylamide gel electrophoresis (PAGE) analysis. Sodium dodecyl sulphate–PAGE revealed that the purified tannase was a monomeric enzyme with a molecular mass of 45 kDa. Temperature of 30 to 50°C and pH of 5.0 to 7.0 were optimum for tannase activity and stability. Tannase immobilized on alginate beads could hydrolyze tannic acid even after extensive reuse and retained about 85% of the initial activity. Thin layer chromatography, high performance liquid chromatography, and ¹H-nuclear magnetic resonance spectral analysis confirmed that gallic acid was formed as a byproduct during hydrolysis of tannic acid.     

Catechine biotransformation by tannase with sequential addition of substrate

This work studied the effect of a sequential addition of substrate on tannase reaction for the increase of epigallocatechin (EGC) and gallic acid. The addition of 0.5–1% GTE increased the production of gallic acid during 2 h in a single tannase reaction, while the addition of more than 2% in GTE rather showed a decrease in gallic acid level with an increase of EGCG level compared with 1% GTE addition group, suggesting that GTE addition of 2% and over inhibits the reaction of tannase. Examination of sequential addition of 1% GTE on tannase reaction showed that second addition of 1% GTE at 2 h promoted tannase reaction by increasing production of gallic acid, but further addition (2 and 3 h) rather inhibited tannase reaction with lowered gallic acid and enhanced EGCG levels. This result showed that one additional treatment of 1% GTE during tannase reaction is effective in an increase of gallic acid production. Moreover, levels of degallated products including EGC, EC, and GC were increased by 7.3, 4.5, and 3.5-fold, respectively in sequential addition of GTE at 2 h. pH change derived from gallic acid production was not shown to related to tannase activity. Therefore, our study suggests that one sequential addition is a suitable process for desirable production of green tea extracts enriched in active components such as gallic acid and EGC.     

从黑茶中分离和筛选产单宁酶菌株

茶叶中富含单宁化合物。从分离自黑茶的真菌菌株中,筛选高产单宁酶的菌株;进而分离纯化单宁酶,分析单宁酶对茶汤的转溶效果。从不同产地的3个黑茶样品中,共分离获得44个真菌分离物;经初步鉴定,这些真菌分离物以曲霉属（Aspergillus）、青霉属（Penicillium）和散囊菌属（Eurotium）的真菌居多。以单宁酸为底物的鉴别培养基初筛表明,其中26个真菌分离物在鉴别平板上产生透明圈,显示单宁水解酶活性;通过固体发酵复筛,筛选到1株产单宁酶活性较高的菌株,初步鉴定为青霉属（Penicillium）菌株,命名为青霉MP-24菌株。青霉MP-24可以以茶叶、茶梗和麸皮等农副产品作为原料固体发酵产生单宁酶。以麸皮为原料的发酵产物经过硫酸铵分级沉淀、DEAE阴离子交换层析和葡聚糖G-150凝胶层析等分离纯化步骤,得到分子量为70 kDa的单一蛋白质条带,单宁酶活力达到603.68 U/mg。纯化获得的单宁酶对茶汤有良好的转溶效果。研究结果表明,在黑茶相关微生物中含有丰富的产单宁酶菌株,是工业酶制剂的重要资源。     

黑曲霉B0201利用五倍子固体发酵产单宁酶的条件研究

通过比较常规灭菌发酵和生料发酵, 研究黑曲霉B0201利用五倍子固体发酵产单宁酶的条件。结果表明, 在生料发酵过程中, 采用20%五倍子并且以(NH4)2SO4为氮源制备单宁酶的最佳条件为: 液固比=1.6:1、温度30°C、初始pH 6.0。在该条件下通过96 h的培养, 单宁酶的活力可达51.2 U/gds, 是常规灭菌发酵的3.6倍。以上结果显示, 生料发酵生产单宁酶是一种高效可行的方法。