Cholinium carboxylate ionic liquids for pretreatment of lignocellulosic materials to enhance subsequent enzymatic saccharification

The present study is the first report demonstrating that ionic liquids consisting of cholinium cations and linear carboxylate anions ([Ch][CA] ILs) can be used for pretreatment of lignocellulosic materials to enhance subsequent enzymatic saccharification. Six variants of [Ch][CA] ILs were systematically prepared by combining cholinium cations with linear monocarboxylate anions ([C_nH_2n+1–COO]⁻, n = 0–2) or dicarboxylate anions ([HOOC–C_nH_2n+1–COO]⁻, n = 0–2). These [Ch][CA] ILs were analyzed for their toxicity to yeast cell growth and their ability to pretreat kenaf powder for subsequent enzymatic saccharification. When assayed against yeast growth, the EC₅₀ for choline acetate ([Ch][OAc]) was 510 mM, almost one order of magnitude higher than that for 1-ethyl-3-methylimidazolium acetate ([Emim][OAc]). The cellulose saccharification ratio after pretreatment at 110 °C for 16 h with [Ch][OAc] (100.6%) was almost comparable with that after pretreatment with [Emim][OAc]. Therefore, [Ch][OAc] is a biocompatible alternative to [Emim][OAc] for lignocellulosic material pretreatment.     

Application of liquid chromatography-tandem mass spectrometry (LC–MS/MS) for the analysis of stable isotope enrichments of phenylalanine and tyrosine

Whole-body protein synthesis and breakdown are measured by a combined tracer infusion protocol with the stable isotope amino acids l-[ring-²H₅]-phenylalanine, l-[ring-²H₂]-tyrosine and l-[ring-²H₄]-tyrosine that enable the measurement of the phenylalanine to tyrosine conversion rate. We describe a liquid chromatography–tandem mass spectrometry (LC–MS/MS) method for the measurement of very low tracer–tracee ratios (TTR) of the amino acids l-phenylalanine and l-tyrosine in human plasma. TTR calibration curves of the tracers l-[ring-²H₅]-phenylalanine, l-[ring-²H₂]-tyrosine and l-[ring-²H₄]-tyrosine were linear (r² > 0.99) in the range between 0.01% and 5.0% TTR and lowest measurable TTR for the tracers was 0.01% at a physiological concentration of 60 μM. The method was applied successfully to plasma samples from a clinical study reaching a steady state enrichment plateau (mean ± SD) of 3.33 ± 0.19% for l-[ring-²H₅]-phenylalanine, 2.40 ± 0.43% for l-[ring-²H₂]-tyrosine and 0.29 ± 0.07% for l-[ring-²H₄]-tyrosine, respectively. The LC–MS/MS method can be applied for measurement of very low plasma enrichments of phenylalanine and tyrosine for the determination of whole-body protein synthesis and breakdown rates in humans.     

Electro-Fenton,hydrogenotrophic and Fe2+ ions mediated TOC and nitrate removal from aquaculture system: Different experimental strategies

A number of methods for denitrification were studied including Electro-Fenton method, hydrogenotrophic as well as innovative Fe²⁺ mediated denitrification and their technical feasibility in terms of changes in TOC and nitrate concentrations, effect of different Fenton’s reagent dosage, current and the effect of the pH was investigated. This study was carried out using tailor made electrodialytic reactor. It was found that the highest TOC removal was achieved at pH 2.2 and 2.4 (77.1% and 97.8%, respectively) at the anode and the lowest accumulation of 33% at pH of 6.2 at the cathode. The highest TOC removal in terms of using different H₂O₂ concentrations was achieved at 40 mM reaching as high as 97.3%. Regardless experimental strategy, initially nitrates migrated towards the cathode due to the strong hydraulic gradient under the applied electric current. During the course of experiments, nitrates were transported towards the anode where their concentration decreased. The highest nitrate removal was achieved at 0.12 mA cm^?2 electric current density (94.8%) at the anode and a complete removal at the cathode. Hydrogenotrophic denitrification was the highest reaching 92.5%, however, when Fe²⁺ ions as electron donor was used for the destruction of nitrates, only 66.6% removal was achieved. Denitrification using only Fe²⁺ ions was a factor 1.4 less than using electrically generated hydrogen or a Fenton’s reagent.     

Low pH (6, 5 and 4) sulfate reduction during the acidification of sucrose under thermophilic (55 °C) conditions

The effect of a low pH (6, 5 and 4) and different COD/SO₄²⁻ ratios (9 and 3.5) on thermophilic (55 °C) sulfate reduction and acidification of sucrose was investigated using three upflow anaerobic sludge bed reactors fed with sucrose at an organic loading rate of 3.5 gCOD (l_reactor d)⁻¹. The three reactors showed nearly 100% acidification of sucrose for all pH values and COD/SO₄²⁻ ratios investigated. Sulfate reduction was complete at pH 6 and a COD/SO₄²⁻ ratio of 9. At pH 5, sulfate reduction efficiencies were 80–95% for both COD/SO₄²⁻ ratios (9 and 3.5). At pH 4, sulfate reduction efficiencies further dropped to 55–65% at a COD/SO₄²⁻ ratio of 9 and 30–40% at a COD/SO₄²⁻ ratio of 3.5. The pH decrease from 6 to 5 or 4 caused a shift in the acidification products from mainly acetate to butyrate, as well as a higher production of ethanol, especially at pH 4. At pH 4, propionate and methane were not formed and hydrogen concentrations in the biogas reached 50%, equivalent to a hydrogen yield of 1.3 mol H₂ (mol glucose)⁻¹. This study shows that sulfate reduction is possible in the acidification phase of anaerobic wastewater treatment at pH values as low as 6 till 4 and that the pH strongly affects both the acidification pathways and the sulfate reduction efficiencies.     

Magnetic nanocomposite of anti-human IgG/COOH-multiwalled carbon nanotubes/Fe₃O₄ as a platform for electrochemical immunoassay

An electrochemical immunosensing method was developed based on a magnetic nanocomposite. The multiwalled carbon nanotubes (MWCNTs) were treated with nitric acid to produce carboxyl groups at the open ends. Then, Fe₃O₄ nanoparticles were deposited on COOH–MWCNTs by chemical coprecipitation of Fe²⁺ and Fe³⁺ salts in an alkaline solution. Goat anti-human IgG (anti-hIgG) was covalently attached to magnetic nanocomposite through amide bond formation between the carboxylic groups of MWCNTs and the amine groups of anti-hIgG. The prepared bio-nanocomposite was used for electrochemical sensing of human tetanus IgG (hIgG) as a model antigen. The anti-hIgG magnetic nanocomposite was fixed on the surface of a gold plate electrode using a permanent magnet. The hIgG was detected using horseradish peroxidase (HRP)-conjugated anti-hIgG in a sandwich model. Electrochemical detection of hIgG was carried out in the presence of H₂O₂ and KI as substrates of HRP. Using this method, hIgG was detected in a concentration range from 30 to 1000 ng ml^?1 with a correlation coefficient of 0.998 and a detection limit of 25 ng ml^?1 (signal/noise = 3). The designed immunosensor was stable for 1 month.     

Sensitization of H2O2-induced TRPM2 activation and subsequent interleukin-8 (CXCL8) production by intracellular Fe2+ in human monocytic U937 cells

Transient receptor potential melastatin 2 (TRPM2) is an oxidative stress-sensitive Ca²⁺-permeable channel. In monocytes/macrophages, H₂O₂-induced TRPM2 activation causes cell death and/or production of chemokines that aggravate inflammatory diseases. However, relatively high concentrations of H₂O₂ are required for activation of TRPM2 channels in vitro. Thus, in the present study, factors that sensitize TRPM2 channels to H₂O₂ were identified and subsequent physiological responses were examined in U937 human monocytes. Temperature increase from 30 °C to 37 °C enhanced H₂O₂-induced TRPM2-mediated increase in intracellular free Ca²⁺ ([Ca²⁺]_i) in TRPM2-expressing HEK 293 cells (TRPM2/HEK cells). The H₂O₂-induced TRPM2 activation enhanced by the higher temperature was dramatically sensitized by intracellular Fe²⁺-accumulation following pretreatment with FeSO₄. Thus intracellular Fe²⁺-accumulation sensitizes H₂O₂-induced TRPM2 activation at around body temperature. Moreover, intracellular Fe²⁺-accumulation increased poly(ADP-ribose) levels in nuclei by H₂O₂ treatment, and the sensitization of H₂O₂-induced TRPM2 activation were almost completely blocked by poly(ADP-ribose) polymerase inhibitors, suggesting that intracellular Fe²⁺-accumulation enhances H₂O₂-induced TRPM2 activation by increase of ADP-ribose production through poly(ADP-ribose) polymerase pathway. Similarly, pretreatment with FeSO₄ stimulated H₂O₂-induced TRPM2 activation at 37 °C in U937 cells and enhanced H₂O₂-induced ERK phosphorylation and interleukin-8 (CXCL8) production. Although the addition of H₂O₂ to cells under conditions of intracellular Fe²⁺-accumulation caused cell death, concentration of H₂O₂ required for CXCL8 production was lower than that resulting in cell death. These results indicate that intracellular Fe²⁺-accumulation sensitizes TRPM2 channels to H₂O₂ and subsequently produces CXCL8 at around body temperature. It is possible that sensitization of H₂O₂-induced TRPM2 channels by Fe²⁺ may implicated in hemorrhagic brain injury via aggravation of inflammation, since Fe²⁺ is released by heme degradation under intracerebral hemorrhage.     

Phenol and sulfide oxidation in a denitrifying biofilm reactor and its microbial community analysis

A microbial consortium attached onto a polyethylene support was used to evaluate the simultaneous oxidation of sulfide and phenol by denitrification. The phenol, sulfide and nitrate loading rates applied to an inverse fluidized bed reactor were up to 168 mg phenol–C/(l d), 37 mg S^2?/(l d) and 168 mg NO₃^?–N/(l d), respectively. Under steady state operation the consumption efficiencies of phenol, sulfide and nitrate were 100%. The N₂ yield (g N₂/g NO₃^?–N) was 0.89. The phenol was mineralized resulting in a yield of 0.82 g bicarbonate–C/g phenol–C and sulfide was completely oxidized to sulfate with a yield of 0.99 g SO₄^2?–S/g S^2?. 16S rRNA gene-based microbial community analysis of the denitrifying biofilm showed the presence of Thauera aromatica, Thiobacillus denitrificans, Thiobacillus sajanensis and Thiobacillus sp. This is the first work reporting the simultaneous oxidation of sulfide and phenol in a denitrifying biofilm reactor.     

Microbial processes and bacterial populations associated to anaerobic treatment of sulfate-rich wastewater

A pilot-scale (1.2 m³) anaerobic sequencing batch biofilm reactor (ASBBR) containing mineral coal for biomass attachment was fed with sulfate-rich wastewater at increasing sulfate concentrations. Ethanol was used as the main organic source. Tested COD/sulfate ratios were of 1.8 and 1.5 for sulfate loading rates of 0.65–1.90 kgSO₄²⁻/cycle (48 h-cycle) or of 1.0 in the trial with 3.0 gSO₄²⁻ l⁻¹. Sulfate removal efficiencies observed in all trials were as high as 99%. Molecular inventories indicated a shift on the microbial composition and a decrease on species diversity with the increase of sulfate concentration. Beta-proteobacteria species affiliated with Aminomonas spp. and Thermanaerovibrio spp. predominated at 1.0 gSO₄²⁻ l⁻¹. At higher sulfate concentrations the predominant bacterial group was Delta-proteobacteria mainly Desulfovibrio spp. and Desulfomicrobium spp. at 2.0 gSO₄²⁻ l⁻¹, whereas Desulfurella spp. and Coprothermobacter spp. predominated at 3.0 gSO₄²⁻ l⁻¹. These organisms have been commonly associated with sulfate reduction producing acetate, sulfide and sulfur. Methanogenic archaea (Methanosaeta spp.) was found at 1.0 and 2.0 gSO₄²⁻ l⁻¹. Additionally, a simplified mathematical model was used to infer on metabolic pathways of the biomass involved in sulfate reduction.     

Application of experimental designs to optimize medium composition for production of thermostable lipase/esterase by Geobacillus thermodenitrificans AZ1

Thirty two morphologically different bacterial were isolated from different soil samples and screened for their ability to produce lipolytic enzymes. Among all isolates, the isolate coded AZ1 was selected due to its high potency to produce lipase at elevated temperature up to 65 °C. Phylogenetic analysis based on 16SrDNA sequence revealed its close relationship to Geobacillus thermodenitrificans. The effect of ten culture variable on lipase production was evaluated by implementing Plackett–Burman statistical design. d-sucrose, peptone and soy bean flour were the most significant variables affecting lipase production. A pre-optimized medium based on this experiment yielded an enzyme activity of 260 U min^?1 ml^?1. For further optimization, a fourteen trials’ multi-factorial Box–Behnken experimental design was applied to find out the optimum level of each of the significant variables. The tested variables, namely: d-sucrose (X₁); peptone (X₂) and soy bean flour (X₃) were examined, each at three different levels coded ?1, 0, +1. The optimal levels of the three components were founded to be (g/L): d-sucrose, 6.56; peptone, 6.35; and soy bean flour, 6.92, with a predicted activity of approximately 610 U min^?1 ml^?1. According to the results of the Plackett–Burman and Box–Behnken designs the following medium composition is expected to be optimum (g/L): d-sucrose 6.56, peptone 6.35, soy bean flour 6.92, CaCl₂ 0.02, Y.E. 2.5, K₂HPO₄ 1.0, MgSO₄.7H₂O 0.2 and Fe₂ (SO₄)₃ 0.02; pH, 8; cultivation temperature 55 °C and incubation time 24 h, the enzyme activity measured in the medium was approximately 593 U min^?1 ml^?1.     

Isoorientin-6″-O-glucoside,a water-soluble antioxidant isolated from Gentiana arisanensis

The antioxidant activities of isoorientin-6″-O-glucoside were studied using various models. Isoorientin-6″-O-glucoside was more potent than Trolox, probucol and butylated hydroxytoluene (BHT) in reducing the stable free radical 1,1-diphenyl-2-picrylhydrazyl (DPPH). It also scavenged superoxide anion, peroxyl and hydroxyl radicals that were generated by xanthine/xanthine oxidase, 2,2′-azobis(2-amidinopropane) dihydrochloride (AAPH) and Fe³⁺–ascorbate–EDTA–H₂O₂ system, respectively. The IC₅₀ value, stoichiometry factor and second-order rate constant were 9.0 ± 0.8 μM, 1.8 ± 0.1 and 2.6 × 10¹⁰ M⁻¹ s⁻¹ for superoxide generation, peroxyl and hydroxyl radicals. However, isoorientin-6″-O-glucoside did not inhibit xanthine oxidase activity or scavenge hydrogen peroxide (H₂O₂), carbon radical or 2,2′-azobis(2,4-dimethylvaleronitrile) (AMVN)-derived peroxyl radical in hexane. Isoorientin-6″-O-glucoside inhibited Cu²⁺-induced oxidation of human low-density lipoprotein (LDL) as measured by fluorescence intensity, thiobarbituric acid-reactive substance formation and electrophoretic mobility. Since isoorientin-6″-O-glucoside did not possess pro-oxidant activity, it may be an effective water-soluble antioxidant that can prevent LDL against oxidation.     

High-rate denitrifying sulfide removal process in expanded granular sludge bed reactor

An expanded granular sludge bed (EGSB) reactor was adopted to incubate bio-granules that could simultaneously convert 4.8 kg-S m^?3 d^?1 of sulfide in 97% efficiency; 2.6 kg-N m^?3 d^?1 of nitrate in 92% efficiency; and 2.7 kg-C m^?3 d^?1 acetate in 95% efficiency. Mass balance calculation of sulfur, nitrogen, and carbon over the EGSB reactor confirmed the performance results. This noted reactor performance is much higher than those reported in literature. Stoichiometric relation suggests that the nitrate was reduced to nitrite via autotrophic denitrification pathway, then the formed nitrite was converted via heterotrophic denitrification pathway to N₂.     

Pharmacokinetic and tissue distribution study of [14C]fluasterone in male Beagle dogs following intravenous,oral and subcutaneous dosing routes

The purpose of this work was to compare the pharmacokinetics (PK) and tissue distribution of [¹⁴C]fluasterone following intravenous (iv), subcutaneous (sc) and oral (po) administration in male Beagle dogs. The main goal of the investigation was to discover if non-oral routes would alter parameters observed in this study following the administration of [¹⁴C]fluasterone. The oral formulation had a lower bioavailability (47%) compared to the sc formulation (84%). Po and sc administration resulted in a similar t_max; however, the observed C_max following sc dosing was less than half of that after oral dosing. The sc route had the greatest overall exposure (AUC_0–∞). Tissue distribution analysis 2 h post-intravenous dosing showed that connective tissue (adipose and bone), liver, and skeletal muscle accumulated relatively high levels of fluasterone. The majority of the dose was retained during the first 24 h. Elimination of [¹⁴C]fluasterone-derived radioactivity following intravenous dosing resulted in urine and feces containing 7.6% and 28%, respectively, of the total dose over the first 24 h. Elimination of [¹⁴C]fluasterone-derived radioactivity following subcutaneous dosing resulted in 4.6% in urine and 7.8% in feces of the total dose over the first 24 h. Following oral dosing, elimination resulted in 3.8% in urine and 36% in feces over the first 24 h. In conclusion, the sc route of administration offers some advantages to po and iv due to the prolonged release and increased retention through 24 h.     

Hydrogen and oxygen trapping at the H-cluster of [FeFe]-hydrogenase revealed by site-selective spectroscopy and QM/MM calculations

[FeFe]-hydrogenases are superior hydrogen conversion catalysts. They bind a cofactor (H-cluster) comprising a four-iron and a diiron unit with three carbon monoxide (CO) and two cyanide (CN^?) ligands. Hydrogen (H₂) and oxygen (O₂) binding at the H-cluster was studied in the C169A variant of [FeFe]-hydrogenase HYDA1, in comparison to the active oxidized (Hox) and CO-inhibited (Hox-CO) species in wildtype enzyme. ⁵⁷Fe labeling of the diiron site was achieved by in vitro maturation with a synthetic cofactor analogue. Site-selective X-ray absorption, emission, and nuclear inelastic/forward scattering methods and infrared spectroscopy were combined with quantum chemical calculations to determine the molecular and electronic structure and vibrational dynamics of detected cofactor species. Hox reveals an apical vacancy at Fe_d in a [4Fe4S-2Fe]^3 ? complex with the net spin on Fe_d whereas Hox-CO shows an apical CN^? at Fe_d in a [4Fe4S-2Fe(CO)]^3 ? complex with net spin sharing among Fe_p and Fe_d (proximal or distal iron ions in [2Fe]). At ambient O₂ pressure, a novel H-cluster species (Hox-O₂) accumulated in C169A, assigned to a [4Fe4S-2Fe(O₂)]^3 ? complex with an apical superoxide (O₂^?) carrying the net spin bound at Fe_d. H₂ exposure populated the two-electron reduced Hhyd species in C169A, assigned as a [(H)4Fe4S-2Fe(H)]^3 ? complex with the net spin on the reduced cubane, an apical hydride at Fe_d, and a proton at a cysteine ligand. Hox-O₂ and Hhyd are stabilized by impaired O₂^– protonation or proton release after H₂ cleavage due to interruption of the proton path towards and out of the active site.     

Hydrogen sulphide removal from air by biotrickling filter using open-pore polyurethane foam as a carrier

A study was conducted on H₂S removal in a biotrickling filter packed with open-pore polyurethane foam. Thiobacillus denitrificans was used as inoculum and a mixed culture population was developed during the process. The inhibitory effect of sulphate concentration (1.8–16.8 g L⁻¹), pH (6.9–8.6), trickling liquid velocity (TLV, 9.1–22.8 m h⁻¹), H₂S inlet concentration (20–157 ppmv) and the empty bed residence time (EBRT, 9–57 s) on the H₂S removal efficiency (RE) were thoroughly investigated. An increase in pH from 6.9 to 8.5 led to a corresponding increase in H₂S removal. In addition, an inhibitory effect of sulphate concentration was observed from 16.8 g L⁻¹ and the maximum elimination capacity was found to be 22 gS m⁻³ h⁻¹ (RE 98%). The RE was constant (98.8 ± 0.30%) for EBRT ≥ 16 s, but a decrease in the EBRT from 16 to 9 s led to a corresponding decrease in RE from 98.2 to 89.6% for a TLV of 9.1 m h⁻¹ and from 97.9 to 94.9% for a TLV of 22.8 m h⁻¹ (inlet load of 11.0 ± 0.2 gS m⁻³ h⁻¹). The sulphur oxidation capacity in the biotrickling filter was not diminished by the presence of other bacteria.     

Profiling oestrogens and testosterone in human urine by stable isotope dilution/benchtop gas chromatography–mass spectrometry

Oestrogens, such as oestrone (E₁), 17β-oestradiol (E₂), oestriol (E₃) and their biologically active metabolites 2-methoxyoestrone (2-MeOE₁), 2-hydroxyoestradiol (2-OHE₂) 16-ketooestradiol (16-OE₂), 16-epioestriol (16-epiE₃), as well as testosterone (T) play an important role in physiological and pathological developmental processes during human development. We therefore aimed at developing an isotope dilution/bench top gas chromatography–mass spectrometry (ID/GC–MS) method, based on benchtop GC–MS, for the simultaneous determination (‘profiling’) of the above analytes in children. The method consisted of equilibration of urine (5 ml) with a cocktail containing stable isotope-labelled analogues of the analytes as internal standards ([2,4-²H₂]E₁, [2,4,16,16-²H₄]E₂, [2,4,17-²H₃]E₃, [16,16,17-²H₃]T, [1,4,16,16-²H₄]2-MeOE₁, [1,4,16,16,17-²H₅]2-OHE₂, [2,4,15,15,17-²H₅]16-OE₂ and [2,4-²H₂]16-epiE₃). Then, solid-phase extraction (C₁₈ cartridges), enzymatic hydrolysis (sulphatase from Helix pomatia (type H-1)), re-extraction, purification by anion exchange chromatography and derivatisation to trimethylsilyl ethers followed. The samples were analysed by GC–MS (Agilent GC 6890N/5975MSD; fused silica capillary column 25 m × 0.2 mm i.d., film 0.10 μm). Calibration plots were linear and showed excellent reproducibility with coefficients of determination (r²) between 0.999 and 1.000. Intra- and inter-assay coefficients of variation (CV) were <2.21% for all quantified metabolites. Sensitivity was highest for 2-OHE₂ (0.25 pg per absolute injection: signal-to-noise ratio (S/N) = 3) and lowest for 16-epiE₃ (2 pg per absolute injection: S/N = 2.6), translating into corresponding urine sample analyte concentrations of 0.025 ng ml^?1 and 0.2 ng ml^?1, respectively. Accuracy – determined in a two-level spike experiment – showed relative errors ranging between 0.15% for 16-OE₂ and 11.63% for 2-OHE₂. Chromatography showed clear peak shapes for the components analysed. In summary, we describe a practical, sensitive and specific ID/GC–MS assay capable of profiling the above-mentioned steroids in human urine from childhood onwards.     

Batch and continuous fermentative production of hydrogen with anaerobic sludge entrapped in a composite polymeric matrix

Cell immobilization techniques were adopted to biohydrogen production using immobilized anaerobic sludge as the seed culture. Sucrose-based synthetic wastewater was converted to H₂ using batch and continuous cultures. A novel composite polymeric material comprising polymethyl methacrylate (PMMA), collagen, and activated carbon was used to entrap biomass for H₂ production. Using the PMMA immobilized cells, the favorable conditions for batch H₂ fermentation were 35 °C, pH 6.0, and an 20 g COD l⁻¹ of sucrose, giving a H₂ production rate of 238 ml h⁻¹ l⁻¹ and a H₂ yield of 2.25 mol H₂ mol sucrose⁻¹. Under these optimal conditions, continuous H₂ fermentation was conducted at a hydraulic retention time (HRT) of 4–8 h, giving the best H₂-producing rate of 1.8 l h⁻¹ l⁻¹ (over seven-fold of the best batch result) at a HRT of 6 h and a H₂ yield of 2.0 mol H₂ mol sucrose⁻¹. The sucrose conversion was essentially over 90% in all runs. The biogas consisted of only H₂ and CO₂. The major soluble metabolites were butyric acid, acetic acid, and 2,3-butandiol, while a small amount of ethanol also detected. The PMMA-immobilized-cell system developed in this work seems to be a promising H₂-producing process due to the high stability in continuous operations and the capability of achieving a competitively high H₂ production rate under a relatively low organic loading rate.     

Operation of an aerobic granular pilot scale SBR plant to treat swine slurry

A pilot-scale Sequencing Batch Reactor was operated during 307 days in order to treat swine slurry characterized by its high variable composition: organic and nitrogen applied loading rates and C/N ratio were 1.4–6.3 kg COD_s/(m³ d), 0.5–2.5 kg N/(m³ d) and 1.9–9.4 g COD_s/(g N), respectively. Aerobic granules successfully developed in the reactor and their physical properties remained rather stable despite the feeding composition variability. Organic and ammonia removal efficiency reached 61–73% and 56–77%, respectively, however ammonia was mainly oxidized to nitrite. The reactor had a good biomass retention capacity to select for granular biomass. However, its efficiency to retain the solids present in the feeding was low. Aerobic granulation in SBR systems appears as an interesting alternative to treat slurry in small livestock facilities where the implementation of anaerobic digestion systems is not a feasible option or the removal of nitrogenous compounds is required.     

Thermophilic treatment of bulk drug pharmaceutical industrial wastewaters by using hybrid up flow anaerobic sludge blanket reactor

The hybrid up flow anaerobic sludge blanket reactor was evaluated for efficacy in reduction of chemical oxygen demand (COD) and biochemical oxygen demand (BOD) of bulk drug pharmaceutical wastewater under different operational conditions. The start-up of the reactor feed came entirely with glucose, applied at an organic loading rate (OLR) 1 kg COD/m³ d. Then the reactor was studied at different OLRs ranging from 2 to 11 kg COD/m³ d with pharmaceutical wastewater. The optimum OLR was found to be 9 kg COD/m³ d, where we found 65–75% COD and 80–94% of BOD reduction with biogas production containing 60–70% of methane and specific methanogenic activity was 320 ml CH₄/g-VSS d. By the characterization studies of effluent using GC–MS, the hazardous compounds like phenol, l,2-methoxy phenol, 2,4,6-trichloro phenol, dibutyl phthalate, 1-bromo naphthalene, carbamazepine and antipyrine were present. After the treatment, these compounds degraded almost completely except carbamazepine. Thermophilic methanothrix and methanosaetae like bacteria are present in the granular sludge.     

Two ways to achieve an anammox influent from real reject water treatment at lab-scale: Partial SBR nitrification and SHARON process

A comparative study to produce the correct influent for Anammox process from anaerobic sludge reject water (700–800 mg NH₄⁺-N L⁻¹) was considered here. The influent for the Anammox process must be composed of NH₄⁺-N and NO₂⁻-N in a ratio 1:1 and therefore only a partial nitrification of ammonium to nitrite is required. The modifications of parameters (temperature, ammonium concentration, pH and solid retention time) allows to achieve this partial nitrification with a final effluent only composed by NH₄⁺-N and NO₂⁻-N at the right stoichiometric ratio. The equal ratio of HCO₃⁻/NH₄⁺ in reject water results in a natural pH decrease when approximately 50% of NH₄⁺ is oxidised. A Sequencing batch reactor (SBR) and a chemostat type of reactor (single-reactor high activity ammonia removal over nitrite (SHARON) process) were studied to obtain the required Anammox influent. At steady state conditions, both systems had a specific conversion rate around 40 mg NH₄⁺-N g⁻¹ volatile suspended solids (VSS) h⁻¹, but in terms of absolute nitrogen removal the SBR conversion was 1.1 kg N day⁻¹ m⁻³, whereas in the SHARON chemostat was 0.35 kg N day⁻¹ m⁻³ due to the different hydraulic retention time (HRT) used. Both systems are compared from operational (including starvation experiments) and kinetic point of view and their advantages/disadvantages are discussed.     

An amperometric H2O2 biosensor based on cytochrome c immobilized onto nickel oxide nanoparticles/carboxylated multiwalled carbon nanotubes/polyaniline modified gold electrode

Cytochrome c was immobilized covalently onto nickel oxide nanoparticles/carboxylated multiwalled carbon nanotubes/polyaniline composite (NiO-NPs/cMWCNT/PANI) electrodeposited on gold (Au) electrode. An amperometric H₂O₂ biosensor was constructed by connecting this modified Au electrode along Ag/AgCl as reference and Pt wire as counter electrode to the galvanostat. The modified Au electrode was characterized by cyclic voltammetry (CV), electrochemical impedance spectroscopy (EIS), scanning electron microscopy (SEM) and Fourier transform infra-red spectroscopy (FTIR). Cyclic voltammetric (CV) studies of the electrode at different stages demonstrated that the modified Au electrode had enhanced electrochemical oxidation of H₂O₂, which offered a number of attractive features to develop an amperometric biosensor based on split of H₂O₂. There was a good linear relationship between the current (mA) and H₂O₂ concentration in the range 3–700 μM. The sensor had a detection limit of 0.2 μM (S/N = 3) with a high sensitivity of 3.3 mA μM^?1 cm^?2. The sensor gave accurate and satisfactory results, when employed for determination of H₂O₂ in different fruit juices.