Batch tests for assessing decolourisation of azo dyes by methanogenic and mixed cultures

Most of the published studies on azo dye colour removal involve anaerobic mixed cultures and there is some interest in the knowledge of how dye reduction occurs, if by facultative, strictly anaerobic or both bacterial trophic groups present in classic anaerobic digestors. This paper describes the behaviour of methanogenic and mixed bacteria cultures on the colour removal in batch systems, of a commercial azo dye, C.I. Acid Orange 7, used in paper and textile industries. The aim of this study is to demonstrate, by analysing dye decolourisation, that it occurs with mixed cultures as well as with strictly anaerobic (methanogenic) cultures. Tests were performed with a range of dye concentrations between 60 and 300 mg l⁻¹. The influence of dye concentration on the carbon source removal and decolourisation processes was studied. The effect of carbon source concentration on colour removal was also analysed for both cultures. The degradation rates in mixed and methanogenic cultures were compared. The consumption of carbon source was monitored by COD analysis and dye degradation by ultraviolet-visible spectrophotometry and thin layer chromatography.     

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.     

Dye decolorization by manganese peroxidase in an enzymatic membrane bioreactor

In the present work an enzymatic membrane reactor (EMR) for the oxidation of azo dyes by manganese peroxidase (MnP) has been developed. The configuration consisted of a stirred tank reactor coupled with an ultrafiltration membrane. The membrane allowed for most of the enzymatic activity to be recovered while both the parent dye and the degradation products could pass through. Different operational strategies (batch, fed-batch, and continuous) and parameters such as enzyme activity, H(2)O(2) feeding rate, hydraulic retention time (in continuous operation), and dye loading rate were studied. At best conditions, a continuous operation with a dye decolorization higher than 85% and minimal enzymatic deactivation was feasible for 18 days, attaining an efficiency of 42.5 mg Orange II oxidized/MnP unit consumed.     

Decolorization of textile dyes by whole cultures of Ischnoderma resinosum and by purified laccase and Mn-peroxidase

Ischnoderma resinosum produced extracellular ligninolytic enzymes laccase and MnP. The activity of laccase achieved the maximum on day 10 (29.4 U L⁻¹), the MnP on day 14 (34.5 U L⁻¹). Laccase and Mn-peroxidase were purified from the culture liquid using gel permeation and ion-exchange chromatographies. Purified Mn-peroxidase performed decolorization of all textile dyes tested (Reactive Black 5, Reactive Blue 19, Reactive Red 22 and Reactive Yellow 15). Laccase was inactive with Reactive Black 5 and Reactive Red 22, while all dyes were decolorized after addition of the redox mediators violuric acid (VA) and hydroxybenzotriazole (HBT). The culture liquid from I. resinosum cultures was also able to decolorize all dyes as well as the synthetic dyebaths in the presence of VA and HBT. The highest decolorization rates were detected in acidic pH (3–4).     

Angiotensin II and angiotensin-(1-7) inhibit the inner cortex Na+ -ATPase activity through AT2 receptor

In the present paper, the modulation of the basolateral membrane (BLM) Na⁺-ATPase activity of inner cortex from pig kidney by angiotensin II (Ang II) and angiotensin-(1–7) (Ang-(1–7)) was evaluated. Ang II and Ang-(1–7) inhibit the Na⁺-ATPase activity in a dose-dependent manner (from 10⁻¹¹ to 10⁻⁵ M), with maximal effect obtained at 10⁻⁷ M for both peptides. Pharmacological evidences demonstrate that the inhibitory effects of Ang II and Ang-(1–7) are mediated by AT₂ receptor: The effect of both polypeptides is completely reversed by 10⁻⁸ M PD 123319, a selective AT₂ receptor antagonist, but is not affected by either (10⁻¹²–10⁻⁵ M) losartan or (10⁻¹⁰–10⁻⁷ M) A779, selective antagonists for AT₁ and AT_(1–7) receptors, respectively. The following results suggest that a PTX-insensitive, cholera toxin (CTX)-sensitive G protein/adenosine 3′,5′-cyclic monophosphate (cAMP)/PKA pathway is involved in this process: (1) the inhibitory effect of both peptides is completely reversed by 10⁻⁹ M guanosine 5′-O-(2-thiodiphosphate) (GDPβS; an inhibitor of the G protein activity), and mimicked by 10⁻¹⁰ M guanosine 5′-O-(3-thiotriphosphate) (GTPγS; an activator of the G protein activity); (2) the effects of both peptides are mimicked by CTX but are not affected by PTX; (3) Western blot analysis reveals the presence of the G_s protein in the isolated basolateral membrane fraction; (4) (10⁻¹⁰–10⁻⁶ M) cAMP has a similar and non-additive effect to Ang II and Ang-(1–7); (5) PKA inhibitory peptide abolishes the effects of Ang II and Ang-(1–7); and (6) both angiotensins stimulate PKA activity.     

Effect of various synthetic dyes on the production of manganese-dependent peroxidase isoenzymes by immobilized <Emphasis Type="Italic">Irpex lacteus</Emphasis>

The effect of manganese and selected synthetic dyes on the production of manganese-dependent peroxidase (MnP) by Irpex lacteus immobilized on polyurethane foam was studied. In the cultures grown in a medium containing 65 μM Mn (II), up to three various isoenzymes of MnP were resolved by isolectrofocusing, with pI values within the range of 3.50–6.04. In the cultures grown in a medium containing 2.9 mM Mn (II), two new MnP isoforms (pI 3.28, 3.75) were produced. The addition of structurally different synthetic dyes, an azo dye Reactive Orange 16 (RO16), an anthraquinonic dye Remazol Brilliant Blue R (RBBR), and a triphenylmethane dye Bromophenol Blue (BPB), to the fungal cultures grown in the presence of high manganese inhibited the production of low pI MnP isoforms. However, in the presence of BPB a new MnP isoform with pI 5.67 was detected. BPB was found to induce MnP isoforms which are more effective in RBBR decolorization in vitro than the low pI isoforms present in the control cultures.     

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.     

Kinetic studies on 1:1 electron transfer reactions involving blue copper proteins : 8. Reactions of plastocyanin and azurin with cytochrome c and high potential iron-sulfur protein

Rate constants determined by the stopped-flow method for four protein-protein reactions at 25°C, pH's in the range 5.8–7.5. I = 0.10 M (NaCI), are as follows: cytochrome c(II) with plastocyanin, PCu(II). 1.5 × 10⁶ M⁻¹ sec⁻¹, pH 7.6; high-potential iron-sulfur protein (Hipip) with PCu(II), 3.7 × 10⁵ M⁻¹sec⁻¹. pH 5.8; cytochrome c(II) with azurin, ACu(ll). 6.4 × 10³ M⁻¹sec⁻¹, pH 6.1; Hipip with ACu(II), 2.2 × 10⁵ M⁻¹sec⁻¹, pH 5.8. Activation parameters have been determined for all four reactions; they indicate higher enthalpy requirements and less negative entropy requirements for the PCu(II) as opposed to ACu(II) reactions. Equilibrium constants K for association prior to electron transfer are < 150 M⁻¹ for the cytochrome c(II) reduction of PCu(II) (estimated charges 8 + and 9-,respectively), and < 300 M⁻¹ for the other reactions, indicating no favorable interactions. Rate constants have been analyzed in terms of the simple Marcus theory, which has previously given an excellent fit to thirteen protein-protein reactions considered by Wherland and Pecht. No similar correlation exists in the present studies, and calculated rate constants differ by orders of magnitude from experimentally determined values.     

Assessment of the biodegradability of a monosulfonated azo dye and aromatic amines

Biodecolourisation of an azo dye by anaerobic cultures using a liposomal textile levelling agent as primary substrate was assessed. Liposomes seem to facilitate the uptake of the dye (Acid Orange 7) by anaerobic biomass, leading to a fast decolourisation (colour removal of 96% was achieved in the first sample port of the reactor profiles). On the other hand, the presence of dye (60–300 mg l⁻¹) caused a decrease in the chemical oxygen demand (COD) degradation rate (4.1–2.5 g COD removed l⁻¹ d⁻¹ for 60 and 300 mg l⁻¹ of dye, respectively), suggesting inhibitory effects.Aerobic degradation of aromatic amines was investigated in aerobic respirometric assays with different types of inocula. Sulfanilic acid and aniline were mineralised by inocula with a significant microbiological diversity, even with domestic effluent. These results were confirmed by a significant reduction of COD, total organic carbon (TOC) and a high oxygen consumption (biochemical oxygen demand/theoretical oxygen demand), 92±4%. Kinetic analysis showed that a sigmoid function describes quite well the experimental data, even better than the exponential model. Orthanilic and metanilic acids and 1-amino-2-naphtol were persistent under the tested conditions.     

Effect of oxygen transfer rate on levels of key enzymes of xylose metabolism in Debaryomyces hansenii

The titers of key enzymes of xylose metabolism were measured and correlated with the kinetics of xylitol production by Debaryomyces hansenii under different oxygen transfer rates (OTR) in a batch reactor. An OTR change from 2.72 to 4.22 mmol O₂ l⁻¹ min⁻¹ resulted in a decrease in NADPH-dependent xylose reductase (XR) and NAD ± -dependent xylitol dehydrogenase (XDH) activities. For higher values of OTR (12.93 mmol O₂ l⁻¹ min⁻¹, the XDH titer increased twofold whereas the XR titer did not show a significant change. At the lowest OTR (2.72 mmol O₂ l⁻¹ min⁻¹), xylitol (and ethanol) production rates showed the highest values. However, xylitol specific productivity was twice as high as ethanol specific productivity. The titer of the NADPH-forming enzyme, glucose-6-phosphate dehydrogenase (GPDH), increased from 333 to 412 mU mg⁻¹ when the OTR was increased. However, 6-phosphogluconate dehydrogenase (PGDH) activity remained unchanged and at a lower level, which indicates that this enzyme is responsible for the carbon flux control of the oxidative branch of the pentose phosphate pathway. The activity of the alcohol-forming enzyme was repressed at the higher amount of oxygen, decreasing its activity more than 50%. The changes in ADH suggested that two different metabolic regions under oxygen-limited conditions can be hypothesized for xylose metabolism by D. hansenii. For low OTR values (up to 4.22 mmol O₂ l⁻¹ min⁻¹), a fermentative-type activity is displayed. At higher OTR values (above 4.22 mmol O₂ l⁻¹ min⁻¹), no significant fermentative activity is reported.     

Perchlorate and nitrate reductase activity in the perchlorate-respiring bacterium perclace

The perchlorate (ClO₄⁻)-respiring organism, strain perc1ace, can grow using nitrate (NO₃⁻) as a terminal electron acceptor. In resting cell suspensions, NO₃⁻ grown cells reduced ClO₄⁻, and ClO₄⁻ grown cells reduced NO₃⁻. Activity assays showed that nitrate reductase (NR) activity was 1.31 μmol min⁻¹ (mg protein)⁻¹ in ClO₄⁻ grown cells, and perchlorate reductase (PR) activity was 4.24 μmol min⁻¹ (mg protein)⁻¹ in NO₃⁻ grown cells. PR activity was detected within the periplasmic space, with activities as high as 14 μmol min⁻¹ (mg protein)⁻¹. The NR had a pH optimum of 9.0 while the PR had an optimum of 8.0. This study suggests that separate terminal reductases are present in strain perclace to reduce NO₃⁻ and ClO₄⁻.     

Rapid decolorization of azo dyes by crude manganese peroxidase from Schizophyllum sp. F17 in solid-state fermentation

The production of ligninolytic enzymes by the fungus Schizophyllum sp. F17 using a cost-effective medium comprised of agro-industrial residues in solid-state fermentation (SSF) was optimized. The maximum activities of the enzymes manganese peroxidase (MnP), laccase (Lac), and lignin peroxidases (LiP) were 1,200, 586, and 109 U/L, respectively, on day 5 of SSF. In vitro decolorization of three structurally different azo dyes by the extracellular enzymes was monitored to determine its decolorization capability. The results indicated that crude MnP, but not LiP and Lac, played a crucial role in the decolorization of azo dyes. After optimization of the dye decolorization system with crude MnP, the decolorization rates of Orange IV and Orange G, at an initial dye concentration of 50 mg/L, were enhanced to 76 and 57%, respectively, after 20 min of reaction at pH 4 and 35°C. However, only 8% decolorization of Congo red was observed. This enzymatic reaction system revealed a rapid decolorization of azo dyes with a low MnP activity of 24 U/L. Thus, this study could be the basis for the production and application of MnP on a larger scale using a low-cost substrate.     

CI-NMR measurement of chloride binding to the oxygen-evolving complex of spinach Photosystem II

The mechanism by which Cl⁻ activates the oxygen-evolving complex (OEC) of Photosystem II (PS II) in spinach was studied by ³⁵Cl-NMR spectroscopy and steady-state measurements of oxygen evolution. Measurements of the excess ³⁵Cl-NMR linewidth in dark-adapted, Cl⁻-depleted thylakoid and Photosystem II membranes show an overall hyperbolic decrease which is interrupted by sharp increases in linewidth (linewidth maxima) at approx. 0.3 mM, 0.75 mM, 3.25 mM (2.0 mM in PS II membranes), and 7.0 mM Cl⁻. The rate of the Hill reaction (H₂O → 2,6-dichlorophenolindophenol) at low light intensities (5% of saturation) as a function of [Cl⁻] in thylakoids shows three intermediary plateaus in the concentration range between 0.1 and 10 mM Cl⁻ indicating kinetic cooperativity with respect to Cl⁻. The presence of linewidth maxima in the ³⁵Cl-NMR binding curve indicates that Cl⁻ addition exposes four types of Cl⁻ binding site that were previously inaccessible to exchange with Cl⁻ in the bulk solution. These results are best explained by proposing that Cl⁻ binds to four sequestered (salt-bridged) domains within the oxygen-evolving complex. Binding of Cl⁻ is facilitated by the presence of H⁺ and vice versa. The pH dependence of the excess ³⁵Cl-NMR linewidth at 0.75 mM Cl⁻ shows that Cl⁻ binding has a maximum at pH 6.0 and two smaller maxima at pH 5.4 and 6.5 which may suggest that as many as three groups (perhaps histidine) with pK_a values in the region may control the binding.     

Degradation of ferrous(II) cyanide complex ions by Pseudomonas fluorescens

Degradation of ferrous(II) cyanide complex (ferrocyanide) ions by free cells of P. fluorescens in the presence of glucose and dissolved oxygen was investigated as a function of initial pH, initial ferrocyanide and glucose concentrations and aeration rate in a batch fermenter. The microorganism used the ferrocyanide ions as the sole source of nitrogen. The ferrocyanide biodegradation rate was 30.7 mg g⁻¹ h⁻¹ under the conditions of initial pH: 5, stirring rate: 150 rpm, aeration rate: 0.15 vvm, initial ferrous(II) cyanide complex ion and glucose concentrations: 100 mg l⁻¹ and 0.465 g l⁻¹, respectively. The culture utilized glucose as the main substrate following the non-competitive toxic component inhibition model in the presence of 100 mg l⁻¹ initial ferrous(II) cyanide complex ion concentration. The inhibition of ferrous(II) cyanide complex ions as a secondary substrate began at very low concentrations. A mathematical model, based on non-competitive substrate inhibition was used to describe the inhibitory effect of ferrous(II) cyanide complex ions on the growth of microorganism and the best fitted model parameters were determined by non-linear regression techniques.     

Cadmium biosorption on Spirulina platensis biomass

Dry biomass of Spirulina platensis re-hydrated for 48 h was employed as a biosorbent in tests of cadmium(II) removal from water. Various concentrations of biomass (from 1 to 4 g l⁻¹) and metal (from 100 to 800 mg l⁻¹) were tested. Low biomass levels (X_o  2 g l⁻¹) ensured metal removal up to 98% only at Cd₀= 100 and 200 mg l⁻¹, while X_o  2.0 g l⁻¹ were needed at Cd₀ = 400 mg l⁻¹ to achieve satisfactory results. Whereas X_o = 4.0 g l⁻¹ was effective to remove up to Cd₀ = 500 mg l⁻¹, a further increase in metal concentration (Cd₀ = 600 and 800 mg l⁻¹) led to progressive worsening of the system performance. At a given biomass levels, the kinetics of the process was better at low Cd²⁺ concentrations, while, raising the adsorbent level from 1.0 to 2.0 g l⁻¹ and then to 4.0 g l⁻¹, the rate constant of biosorption increased by about one order of magnitude in both cases and the adsorption capacity of the system progressively decreased from 357 to 149 mg g⁻¹.     

Studies on the ferrochelatase activity of isolated rat liver mitochondria with special reference to the effect of oxidizable substrates and oxygen concentration

The mitochondrial ferrochelatase activity has been studied in coupled rat liver mitochondria using deuteroporphyrin IX (incorporated into liposomes of lecithin) and Fe(III) or Co(II) as the substrates.

1. 1. It was found that respiring mitochondria catalyze the insertion of Fe(II) and Co(II) into deuteroporphyrin. When Fe(III) was used as the metal donor, the reaction revealed an absolute requirement for a supply of reducing equivalents supported by the respiratory chain.

2. 2. A close correlation was found between the disappearance of porphyrin and the formation of heme which allows an accurate estimate of the extinction coefficient for the porphyrin to heme conversion. The value Δ (mM⁻¹ · cm⁻¹) = 3.5 for the wavelength pair 498 509 nm, is considerably lower than previously reported.

3. 3. The maximal rate of deuteroheme synthesis was found to be approx. 1 nM · min⁻¹ · mg⁻¹ of protein at 37 °C, pH 7.4 and optimal substrate concentrations, i.e. 75 μM Fe(III) and 50 μM deuteroporphyrin.

4. 4. Provided the mitochondria are supplemented with an oxidizable substrate, the presence of oxygen has no effect on the rate of deuteroheme synthesis.

白囊耙齿菌产锰过氧化物酶条件优化及其对染料的脱色

锰过氧化物酶（manganese peroxidase,MnP）是白腐真菌降解多种异生物质的主要降解酶之一。本研究对白囊耙齿菌Irpex lacteus产MnP的酶活曲线进行监测,利用单因素和正交试验对I. lacteus产MnP的发酵条件进行优化,同时检测了I. lacteus的MnP粗酶液对5种染料的脱色效果。结果显示,I. lacteus在培养5d时MnP活性较大;I. lacteus产MnP较优的条件为：可溶性淀粉20g/L、尿素1g/L、pH 6.3、CaCl₂ 1mmol/L、FeCl₃ 1mmol/L,该条件下MnP活性达29.24U/L,与优化前MnP活性相比提高了1.25倍;I. lacteus的MnP粗酶液对5种染料均可脱色,其中对直接大红和活性红的脱色效果更为明显,脱色5d后的脱色率分别达到82%和81%。     

Rapid production of thermostable cellulase-free xylanase by a strain of Bacillus subtilis and its properties

A Bacillus subtilis strain isolated from a hot-spring was shown to produce xylanolytic enzymes. Their associative/synergistic effect was studied using a culture medium with oat spelts xylan as xylanase inducer. Optimal xylanase production of about 12 U ml⁻¹ was achieved at pH 6.0 and 50°C, within 18 h fermentation. At 50°C, xylanase productivity obtained after 11 h in shake-flasks, 96,000 U l⁻¹ h⁻¹, and in reactor, 104,000 U l⁻¹ h⁻¹ was similar. Increasing temperature to 55°C a higher productivity was obtained in the batch reactor 45,000 U l⁻¹ h⁻¹, compared to shake-flask fermentations, 12,000 U l⁻¹ h⁻¹. Optimal xylanolytic activity was reached at 60°C on phosphate buffer, at pH 6.0. The xylanase is thermostable, presenting full stability at 60°C during 3 h. Further increase in the temperature caused a correspondent decrease in the residual activity. At 90°C, 20% relative activity remains after 14 min. Under optimised fermentation conditions, no cellulolytic activity was detected on the extract. Protein disulphide reducing agents, such as DTT, enhanced xylanolytic activity about 2.5-fold. When is used xylan as substrate, xylanase production decreased as function of time in contrast, with trehalose as carbon source, xylanase production in maintained constant for at least 80 h fermentation.     

The versatile coordination chemistry of tricyanoethenolate, [(NC)2C=C(CN)O]

The reaction of meso-tetrakis (4-dimethoxyphenyl) porphinatomanganese(II), MnTP_OMeP, with TCNE (TCNE = tetracyanoethylene) leads to the formation of [MnTP_OMeP]⁺ [TCNE]⁻ and [MnTP_OMeP]⁺[OC(CN)C(CN)₂]⁻. The single-crystal X-ray structures of the latter as well as [Cu(bipy)₂Cl]⁺ [OC(CN)C(CN)₂]⁻ were determined. The former has a disordered [OC(CN)C(CN)₂]⁻ bridging via C and O between a pair of Mn^III sites, whereas the latter has an isolated [OC(CN)C(CN)₂]⁻ unbound to Cu^II. The IR characterization for μ₂-C,O bound [OC(CN)C(CN)₂]⁻ is at 2219m and 2196s (νCN) cm⁻¹ and at 1558s (νCO) cm⁻¹ while for unbound [OC(CN)C(CN)₂]⁻ it is at 2210m, 2203m, 2181m (νCN) cm⁻¹ and at 1583s (νCO) cm⁻¹.     

Electron exchange reaction of bis(terpyridine)cobalt re-examined by NMR

The rate of the electron transfer self-exchange reaction between bis(terpyridine) cobalt(III) and bis(terpyridine)cobalt(II) has been reexamined by proton NMR. The rate constant of 4×10² M⁻¹ s⁻¹ at 50 °C is dependent on the identity of the anion. Average activation parameters of 32 kJ mol⁻¹ and −96 J K⁻¹ mol⁻¹ are in agreement with previous measurements by other techniques. There is no evidence for either spin restrictions or non-adiabtaticity in this and related cobalt(III)/(II) electron exchange reactions. An alternative explanation is offered for the anomalously negative volumes of activation reported elsewhere.