The evaluation of pre-grown mycelial pellets in decolorization of textile dyes during repeated batch process

This study was undertaken for the possibility of application of pre-grown pellets for biotechnological treatment of dyes and textile industry waste waters. Mycelial pellets of five different white rot fungi were tested for their dye decolorization activity. The pellets of Funalia trogii, Phanerochaete chrysosporium and Trametes versicolor were determined as the most effective ones. The decolorization ability of viable pellets was compared with the decolorization (adsorption) ability of dead pellets during repeated batch studies. Astrazon Black dye was decolorized effectively, about 90%, by viable pellets of all fungi during the first use. Viable F. trogii pellets were found as the most effective pellets. Upon pellet treatment not only a high decolorization but also reduced toxicity (antimicrobial activity) of the Astrazon Black dye was recorded. This type of decolorization activity with commercial or crude laccase was partially observed. Growing cells of F. trogii in batch system showed lower efficiency in color removal of mixed dyes compared to the pre-grown pellets in repeated batch system. The results in this study showed that mycelial pellets could effectively be used as an alternative to traditional physicochemical processes.     

Decolourisation of Acid Violet 7 with complex pellets of white rot fungus and activated carbon

Complex mycelium pellets of a white rot fungus, Trametes versicolor, with activated carbon powder were prepared and investigated for decolourisation of an azo dye, Acid Violet 7. The pellets had a black core of activated carbon powder that was surrounded by a layer of white fungal mycelium. Compared to the activated carbon powder, the mycelium pellets (activated carbon free), and the mycelium pellets plus the activated carbon powder that was added into a dye solution, the complex pellets showed the highest and the most stable activity of dye decolourisation in batch cultures. The high decolourisation rate of the complex pellets was attributed not only to dye adsorption by the activated carbon in the complex pellets, but also to adsorption of extracellular enzymes and other reagents involved in dye decolourisation as well as the closeness between the dye molecules and the fungal cells. The complex pellets were further evaluated in a fluidized-bed reactor in two operation modes: a continuous flow feeding and a repeated-batch feeding. The latter gave higher and more stable decolourisation efficiency than the former. Production of laccase in flask culture and the fluidized-bed bioreactor was also compared.     

Isolation and characterization of Bacillus thuringiensis for acid red 119 dye decolourisation

Studies were carried out to isolate Acid red 119 (AR-119) resistant and decolourising bacteria from dye contaminated soil and water samples. Six morphologically distinct bacterial isolates resistant to 100 ppm AR-119 dye were isolated directly from the soil and waste contaminated with azo dyes. The most efficient isolate, which showed decolourisation zone of 44 mm on 100 ppm AR-119 containing plate was identified as Bacillus thuringiensis SRDD. Gradual adaptation increased the efficiency of the isolate and within 7h of incubation it showed decolourisation up to 1000 ppm of AR-119 dye in liquid medium. Addition of 300 ppm of AR-119 in each step in ongoing dye decolourisation flask gave more than 90% decolourisation of 300 ppm AR-119 in time as short as 1.25 h. The developed B. thuringiensis showed 50-60% decolourisation of 5000 ppm AR-119 in 7d of incubation. This organism was also able to remove more than 98%, 92%, 95% and 95% colour of C.I. Acid brown 14, C.I. Acid black 210, C.I. Acid violet 90 and C.I. Acid yellow 42 azo dyes at 100 ppm concentration in 24h, respectively. When the developed isolate was studied for bioremediation of actual azo dye contaminated waste it removed 70% colour from the waste in 24h. The developed B. thuringiensis exhibited excellent resistance and decolourisation ability to AR-119 and other acid azo dyes.     

绒毛栓孔菌菌丝体在无营养条件下对偶氮染料刚果红的脱色作用

【目的】在无营养条件下,利用白腐真菌绒毛栓孔菌(Trametes pubescens)菌丝体对染料进行脱色可减少试验成本,提高染料处理的实用性。【方法】将该菌株液体培养的菌丝体在无营养条件下对染料进行脱色,并对其中脱色效果较好的偶氮染料刚果红的脱色过程进行分析。在此过程中,测定了该菌株分泌的胞外胞内酶活力,优化影响因子如初始pH值、温度、染料浓度和盐度,同时利用气相色谱-质谱联用技术分析无营养条件下偶氮染料刚果红的降解产物。植物毒性试验测定刚果红经绒毛栓孔菌菌丝体脱色前后的毒性变化。【结果】菌丝体对偶氮染料刚果红有较好的脱色效果,在初始pH值为2.0,温度为30°C,染料浓度为80 mg/L,盐度为2.5%(质量体积比)时,150 r/min转速下培养7 d后脱色率可达80.52%。在此过程中,菌丝体可被连续使用2次,且其所分泌的酶系可降解染料。此外,通过气相色谱-质谱联用分析得到刚果红的降解产物为萘胺、联苯胺和叠氮萘。植物毒性试验显示在无营养条件下的绒毛栓孔菌菌丝体对染料有明显的脱毒作用。【结论】研究发现绒毛栓孔菌菌丝体在无营养条件下的偶氮染料废水处理中具有广阔的应用前景。     

Decolorization of reactive dyes by mixed cultures isolated from textile effluent under anaerobic conditions

In the present study mixed cultures that could grew in the molasses media were isolated from textile dye effluent and its decolorization activity was studied in a batch system under anaerobic conditions, in order to determine the optimal conditions required for the highest decolorization activity. The optimum pH value for decolorization was determined as 8 for all the dyes tested. In the experiment with pH 8 dye decolorizations by mixed cultures were investigated at about 96.2–1031.3 mg l⁻¹ initial dye concentrations. The highest dye removal rates of mixed cultures were 94.9% for Reactive Red RB, 91.0% for Reactive Black B and 63.6% for Remazol Blue at 953.2, 864.9 and 1031.3 mg l⁻¹ initial dye concentrations respectively within 24 h incubation period. When the Reactive Red RB was used, approximately 82–98% total color removal was obtained at between 96.2 and 953.2 mg l⁻¹ initial dye concentrations after 12 h of incubation at 35 °C. These results show that our enriched mixed cultures have the potential to serve as an excellent biomass for the use in reactive dye removal from wastewaters under anaerobic conditions.     

Monoazo and diazo dye decolourisation studies in a methanogenic UASB reactor

Mixed anaerobic bacterial consortia have been show to reduce azo dyes and batch decolourisation tests have also demonstrated that predominantly methanogenic cultures also perform azo bond cleavage. The anaerobic treatment of wool dyeing effluents, which contain acetic acid, could thus be improved with a better knowledge of methanogenic dye degradation. Therefore, the decolourisation of two azo textile dyes, a monoazo dye (Acid Orange 7, AO7) and a diazo dye (Direct Red 254, DR254), was investigated in a methanogenic laboratory-scale Upflow Anaerobic Sludge Blanket (UASB), fed with acetate as primary carbon source. As dye concentration was increased a decrease in total COD removal was observed, but the acetate load removal (90%) remained almost constant. A colour removal level higher than 88% was achieved for both dyes at a HRT of 24h. The identification by HPLC analysis of sulfanilic acid, a dye reduction metabolite, in the treated effluent, confirmed that the decolourisation process was due mainly to azo bond reduction. Although, HPLC chromatograms showed that 1-amino-2-naphthol, the other AO7 cleavage metabolite, was removed, aeration batch assays demonstrated that this could be due to auto-oxidation and not biological mineralization. At a HRT of 8h, a more extensive reductive biotransformation was observed for DR254 (82%) than for AO7 (56%). In order to explain this behaviour, the influence of the dye aggregation process and chemical structure of the dye molecules are discussed in the present work.     

Removal of Astrazon Yellow 7GL from aqueous solutions by adsorption onto wheat bran

Adsorption kinetic and equilibrium of a basic dye (Astrazon Yellow 7GL) from aqueous solutions at various initial dye concentration (50-300 mg/l), pH (4-10), adsorbent dosage (2-8 g/l), particle size (354-846 microm) and temperature (30-50 degrees C) on wheat bran were studied in a batch mode operation. The result showed that the amount adsorbed of the dye increased with increasing initial dye concentration and contact time, whereas particle size and pH had no significant affect on the amount of dye adsorbed by the adsorbent. A comparison of kinetic models on the overall adsorption rate showed that dye/adsorbent system was best described by the pseudo second-order rate model. The removal rate was also dependent on both external mass transfer and intra-particle diffusion. The low value of the intraparticle diffusivity, 10(-11) cm2/s, indicated the significant influence of intraparticle diffusion on the kinetic control. The adsorption capacity (Q0) calculated from the Langmuir isotherm was 69.06 mg/g for at pH 5.6, 303 K for the particle size of 354 microm. The experimental data yielded excellent fits with Langmuir and Tempkin isotherm equations. Different thermodynamic parameters showed that the reaction was spontaneous and endothermic in nature.     

Decolourisation of reactive textile dyes Drimarene Blue X3LR and Remazol Brilliant Blue R by <Emphasis Type="Italic">Funalia trogii</Emphasis> ATCC 200800

Decolourisation of reactive dyes Drimarene Blue X3LR and Remazol Brilliant Blue R by white rot fungi Funalia trogii was studied under static conditions. The effect of various conditions such as mycelial age, initial dye and glucose concentrations on decolourisation were also investigated. Decolourisation activity of F. trogii was compared with Phanerochaete chrysosporium known as test microorganism. It was found that 7-day-old cultures were more effective than 5-day-old cultures of F. trogii for decolourisation of these dyes. Decolourisations by F. trogii of both dyes were increased with glucose concentration decreasing. In contrast, decolourisations by P. chrysosporium were decreased. F. trogii decolourised 92–98% of both dyes within 4–10 h. However, P. chrysosporium partially decolourised (11–20%) these dyes during 10days incubation period under the same conditions.     

Improving laccase production by employing different lignocellulosic wastes in submerged cultures of Trametes versicolor

Laccase production by the white-rot fungus Trametes versicolor (CBS100.29) grown in submerged cultures was studied. Addition of different insoluble lignocellulosic materials into the culture medium in order to enhance laccase production was investigated. The lignocellulosic materials were grape seeds, grape stalks and barley bran, selected because of their availability and low cost, since they are agro-industrial wastes abundant in most countries. Barley bran gave the highest activities, a maximum value of 639U/l, which was 10 times the value attained in the cultures without lignocellulosics addition. The decolourisation of a model dye, Phenol Red, by the ligninolytic fluids obtained in the above-mentioned cultures was investigated. Grape stalk and barley bran cultures showed the highest ability to decolourise the dye, attaining a percentage of decolourisation of around 60% in 72 h.     

Biodegradation of Grape Cluster Stems and Ligninolytic Enzyme Production by Phanerochaete chrysosporium during Semi‐Solid‐State Cultivation

The degradation undergone by grape cluster stems (woody component of vine bagasse), an agroindustrial waste, was investigated during the semi‐solid‐state cultivation of Phanerochaete chrysosporium BKM‐F‐1767 (ATCC 24725). For this, the content of lignin, cellulose and hemicellulose in grape cluster stems was determined before and after the enzymatic process. It was found that about 20% of Klason lignin, 48% of hemicellulose and 5% of cellulose were degraded during the process, being the ligninolytic enzymes (manganese‐dependent peroxidase and lignin peroxidase) produced by such cultures responsible for the degradation of grape cluster stems. In parallel, semi‐solid‐state cultures of P. chrysosporium grown on an inert support (cubes of nylon sponge), which is not susceptible to undergoing degradation during the enzymatic process, were used as reference cultures. In addition, the in vivo decolourisation of a model dye, the polymeric dye Poly R‐478, by both grape cluster stem and nylon cultures was studied in order to assess their degradative ability. A percentage of biological decolourisation higher than 90% after four days of dye addition was obtained using nylon sponge cultures, whereas grape cluster stem cultures led to a decolourisation of around 70% after eight days of dye incubation. The lower percentage of dye degradation achieved by the cultures grown on grape cluster stems was due to the enzymes produced, which were not only employed in the decolourisation of the dye but also in the degradation of the support, as indicated by the data mentioned above.     

Biodegradation of different molecular-mass polyphenols derived from olive mill wastewaters by Geotrichum candidum

The decolourisation of fresh and stored olive mill wastewaters (OMW) and the biodegradation of three groups (F1, F2 and F3) of phenolic compounds by Geotrichum candidum were investigated. Separated phenolic compounds derived from natural OMW ultrafiltration using membranes with a cutoff 2and 100 kDa. G. candidum growth on fresh OMW decreased pH and reduced COD and colour of 75% and 65%, respectively. However, on the stored-black OMW a failure of COD and colour removal were observed. G. candidum activity on this later substrate was enhanced by the addition of a carbon source easily metabolised, misleading an improvement of the COD reduction and decolourization that reached 58% and 48%, respectively. Growth of G. candidum in the presence of F2 or F3 polyphenolic fractions induced high decolourisation and depolymerisation of phenolic compounds. Whereas, very week decolourisation and biodegradation were observed with F1 fraction. Moreover, the highest levels of lignin peroxidase (LiP) and manganese peroxidase (MnP) activities were obtained in the presence of F2 fraction. These results showed that increasing of molecular-mass of aromatics led to an increase in levels of depolymerisation, decolourisation and COD removal by G. candidum culture.     

A packed-bed fungal bioreactor for the continuous decolourisation of azo-dyes (Orange II)

The degradation of an azo dye, Orange II, by immobilised Phanerochaete chrysosporium in a continuous packed bed bioreactor for periods longer than 30 days has been carried out. Nearly complete decolourisation (>95%) was achieved when working at a high dye load rate of 0.2 g l⁻¹ d⁻¹, a temperature of 37 °C, a hydraulic retention time (HRT) of 24 h and applying oxygen gas in a pulsed flow. These conditions allowed Manganese peroxidase (MnP) production and the subsequently Orange II decolourisation. A correlation between residual MnP activity in the effluent and decolourisation was established. Apparently, for decolourisation to be effective, a minimum MnP activity was required, no substantial increase in efficiency at MnP activities higher than 10 U 1 ⁻¹ was observed. The treatment caused, the breakdown of the chromophoric group as well as the cleavage of the aromatic ring.     

Effect of redox mediator, AQDS, on the decolourisation of a reactive azo dye containing triazine group in a thermophilic anaerobic EGSB reactor

The feasibility of thermophilic (55 °C) anaerobic treatment applied to colour removal of a triazine contained reactive azo dye was investigated in two 0.53 l expanded granular sludge blanket (EGSB) reactors in parallel at a hydraulic retention time (HRT) of 10 h. Generally, this group of azo dyes shows the lowest decolourisation rates during mesophilic anaerobic treatment. The impact of the redox mediator addition on colour removal rates was also evaluated. Reactive Red 2 (RR2) and anthraquinone-2,6-disulfonate (AQDS) were selected as model compounds for azo dye and redox mediator, respectively. The reactors achieved excellent colour removal efficiencies with a high stability, even when high loading rates of RR2 were applied (2.7 g RR2 l⁻¹ per day). Although AQDS addition at catalytic concentrations improved the decolourisation rates, the impact of AQDS on colour removal was less apparent than expected. Results show that the AQDS-free reactor R2 achieved excellent colour removal rates with efficiencies around 91%, compared with the efficiencies around 95% for the AQDS-supplied reactor R1. Batch experiments confirmed that the decolourisation rates were co-substrate dependent, in which the volatile fatty acids (VFA) mixture was the least efficient co-substrate. The highest decolourisation rate was achieved in the presence of either hydrogen or formate, although the presence of glucose had a significant impact on the colour removal rates.     

Decolourisation and detoxification of synthetic molasses melanoidins by individual and mixed cultures of Bacillus spp

The decolourisation of synthetic melanoidins (i.e., GGA, GAA, SGA, and SAA) by three Bacillus isolates (Bacillus thuringiensis (MTCC 4714), Bacillus brevis (MTCC 4716) and Bacillus sp. (MTCC 6506)) was studied. Significant reduction in the values of physicochemical parameters was noticed alongwith the decolourisation of all four melanoidins (10% v/v). B. thuringiensis (MTCC 4714) caused maximum decolourisation followed by B. brevis (MTCC 4716) and Bacillus sp. (MTCC 6506). A mixed culture comprised of these three strains was capable of decolourising all four melanoidins. The medium that contained glucose as a sole carbon source showed 15% more decolourisation than that containing both carbon and nitrogen sources. Melanoidin SGA was maximally decolourised (50%) while melanoidin GAA was decolourised least ( approximately 06%) in the presence of glucose as a sole energy source. The addition of 1% glucose as a supplementary carbon source was essential for co-metabolism of melanoidin complex. The decolourisation of synthetic melanoidin by three Bacillus spp. significantly reduced the toxicity to the tubificid worm (Tubifex tubifex, Müller).     

Treatment and kinetic modelling of a simulated dye house effluent by enzymatic catalysis

Biocatalytic treatment of a synthetic dye house effluent, simulating a textile wastewater containing various reactive dyestuffs (Reactive Yellow 15, Reactive Red 239 and Reactive Black 5) and auxiliary chemicals, was investigated in a batch reactor using a commercial laccase. A high decolourisation (above 86%) was achieved at the maximum wavelength of Reactive Black 5. The decolourisation at the other dyes wavelengths (above 63% for RY15 and around 41% for RR239) and the total decolourisation based on all the visible spectrum (around 55%) were not so good, being somewhat lower than in the case of a mixture of the dyes (above 89% for RB5, 77% for RY15, 68% for RR239 and above 84% for total decolourisation). Even so, these results suggest the applicability of this method to treat textile dyeing wastewaters. Kinetic models were developed to simulate the synthetic effluent decolourisation by commercial laccase. The kinetic constants of the models were estimated by minimizing the difference between the predicted and the experimental time courses. The close correlation between the experimental data and the simulated values seems to demonstrate that the models are able to describe with remarkable accuracy the simulated effluent degradation. Water quality parameters such as TOC, COD, BOD₅ and toxicity were found to be under the maximum permissible discharge limits for textile industries wastewaters.     

Relationship between pellet formation by Aspergillus oryzae strain KB and the production of β-fructofuranosidase with high transfructosylation activity

Aspergillus oryzae KB produces two β-fructofuranosidases (F1 and F2). F1 has high transfructosylation activity (Ut) to produce fructooligosaccharides. F2 has high hydrolysis activity (Uh), releasing glucose and fructose. It is desirable to selectively produce F1, which can be used for production of fructooligosaccharides. Here, the relationship between filamentous pellet size and selective production of F1 in liquid culture was investigated. Our finding revealed that: (i) The mean particle size of pellets (5.88 ± 1.36 mm) was larger, and the ratio of Ut to Uh was improved (Ut/Uh = 5.0) in 10% sucrose medium compared with 1% sucrose medium (pellet size = 2.60 ± 0.37 mm; Ut/Uh = 0.96). (ii) The final culture pH of the 1% sucrose medium was 8.7; on controlling the pH of 1% sucrose medium at 5.0, increased pellet size (9.69 ± 2.01 mm) and Ut/Uh (7.8) were observed. (iii) When 3% glycerin was used as carbon source, the pellet size decreased to 1.09 ± 0.33 mm and Ut/Uh was 0.57. (iv) In medium containing 1% sucrose, the pellet size was dependent on the number of spores used in the culture inoculum, but, in these experiments, Ut/Uh was almost constant (1.05 ± 0.08). Collectively, the data show that the value of Ut/Uh is proportional to the pellet size when liquid culture of A. oryzae strain KB is performed in some conditions (such as in the presence of high sucrose concentration, low pH, or added Tween surfactant), but in other conditions Ut/Uh is independent of pellet size.     

Relationship between production of 3-indoleacetic acid and peroxidase-laccase activities depending on the culture periods in Funalia trogii (Trametes trogii)

The relationship between production of 3-indoleacetic acid (IAA) and peroxidase and laccase activity was investigated in white-rot fungusFunalia trogii (Trametes trogii). F. trogii produced IAA and peroxidase and laccase as both primary metabolite and secondary metabolite; the levels of IAA may be influenced by peroxidase and laccase. A correlation exists between the levels of IAA and peroxidase-laccase activity.     

Effect of Different Carbon Sources on Decolourisation of an Industrial Textile Dye Under Alkaline–Saline Conditions

White-rot fungal strains of Trametes versicolor and Phanerochaete chrysosporium were selected to study the decolourisation of the textile dye, Reactive Black 5, under alkaline–saline conditions. Free and immobilised T. versicolor cells showed 100 % decolourisation in the growth medium supplemented with 15 g l^?1 NaCl, pH 9.5 at 30 °C in liquid batch culture. Continuous culture experiments were performed in a fixed-bed reactor using free and immobilised T. versicolor cells and allowed 85–100 % dye decolourisation. The immobilisation conditions for the biomass and the additional supply of carbon sources improved the decolourisation performance during a long-term trial of 40 days. Lignin peroxidase, laccase and glyoxal oxidase activities were detected during the experiments. The laccase activity varied depending on carbon source utilized and glycerol-enhanced laccase activity compared to sucrose during extended growth.     

Efficient harvesting of <Emphasis Type="Italic">Synechocystis</Emphasis> sp. PCC 6803 with filamentous fungal pellets

Cyanobacteria play a major role as direct producers of biofuels, such as ethanol and butanol, with the aid of genetic engineering. However, development of a new harvesting-technology is essential to achieve economic viability of biofuel production from cyanobacteria. In this study, we demonstrated the feasibility of harvesting the unicellular cyanobacterium Synechocystis sp. PCC 6803 using pre-made filamentous fungal pellets and investigated key factors affecting efficiency of harvest, including fungal strain, pellet quantity (number of pellets), initial pH, and organic carbon source. Synechocystis sp. PCC 6803 cells attached to Aspergillus oryzae pellets, indicating that this fungal pellet had a desirable harvesting effect, while Rhizopus oryzae pellets had no effect on harvesting. Increasing pellet quantity and adding organic carbon sources, such as glucose and xylose, improved the harvesting efficiency of Aspergillus oryzae pellet; efficiency was not affected by the initial pH.     

一株毛栓菌静置液体发酵产纤维素酶条件研究

考察一株新分离的毛栓菌静置产纤维素酶的条件,通过单因素试验和正交设计试验分别对培养基初始pH、培养基中的碳源、氮源及诱导物进行研究。利用DNS（3,5-二硝基水杨酸）法测定CMC-Na（羧甲基纤维素钠）纤维素酶活。结果表明：该毛栓菌静置发酵产纤维素酶的最适pH为5.0,最适碳源、氮源和诱导物分别是淀粉、酵母粉和干麸皮,且质量浓度分别为淀粉1%、酵母粉0.4%、干麸皮1.5%,在此条件下,进行静置发酵3d,可获得CMC-Na（羧甲基纤维素钠）纤维素酶活力最高为56.62U/mL。此研究开创了纤维素酶生产菌的新发现,与以往所报道的好氧产纤维素酶菌种黑曲霉、木霉等相比,具有发酵时间短、耗能小等优点,具有一定的潜在应用价值。