Recyclable Clay-Supported Heteropolyacid Catalysts for Complete Glycolysis and Aminolysis of Post-consumer PET Beverage Bottles

Journal of Polymers and the Environment - In this investigation, the use of phosphotungstic acid (PWA) and phosphomolybdic acid (PMA) as well as Zn2+ containing kaolin and bentonite explored for...     

Preparation of light weight constructional materials from chrome containing buffing dust solid waste generated in leather industry

Journal of Material Cycles and Waste Management - An alternative and environmentally benign method of disposing the buffing dust, generated from leather industry was carried out in the present...     

Immobilized reactor for rapid destruction of recalcitrant organics and inorganics in tannery wastewater

The wastewater discharged from tanneries lack biodegradability due to the presence of recalcitrant compounds at significant concentration. The focal theme of the present investigation was to use chemo-autotrophic activated carbon oxidation(CAACO) reactor, an immobilized cell reactor using chemoautotrophs for the treatment of tannery wastewater. The treatment scheme comprised of anaerobic treatment, sand filtration, and CAACO reactor, which remove COD, BOD, TOC, VFA and sulphides respectively by 86%, 95%, 81%,71% and 100%. Rice bran mesoporous activated carbon prepared indigenously and was used for immobilization of chemoautotrophs. The degradation of xenobiotic compounds by CAACO was confirmed through HPLC and FT-IR techniques.     

Nanoporous activated carbon fluidized bed catalytic oxidations of aqueous o, p and m-cresols: kinetic and thermodynamic studies

Nanoporous activated carbon prepared from rice husk through precarbonisation at 400 °C and phosphoric acid activation at 800 °C was used as fluidized bed in Fenton oxidation of the o, p and m-cresols in aqueous solution. The efficiencies of homogeneous Fenton oxidation, fluidized Fenton oxidation and aerobic biological oxidation systems for the removal of o, p and m-cresols in aqueous solution have been compared. The kinetic constants and the thermodynamic parameters for the homogeneous Fenton, heterogeneous Fenton and aerobic biological oxidations of o, p and m-cresols in synthetic wastewater were determined. The degradation of cresols in synthetic wastewater was confirmed using FT-IR, ¹H-NMR and UV–visible spectroscopy.     

Heterocatalytic Fenton oxidation process for the treatment of tannery effluent: kinetic and thermodynamic studies

Background, aim, scope

Treatment of wastewater has become significant with the declining water resources. The presence of recalcitrant organics is the major issue in meeting the pollution control board norms in India. The theme of the present investigation was on partial or complete removal of pollutants or their transformation into less toxic and more biodegradable products by heterogeneous Fenton oxidation process using mesoporous activated carbon (MAC) as the catalyst.

Materials and methods

Ferrous sulfate (FeSO₄·7H₂O), sulfuric acid (36?N, specific gravity 1.81, 98% purity), hydrogen peroxide (50% v/v) and all other chemicals used in this study were of analytical grade (Merck). Two reactors, each of height 50?cm and diameter 6?cm, were fabricated with PVC while one reactor was packed with MAC of mass 150?g and other without MAC served as control.

Results and discussion

The oxidation process was presented with kinetic and thermodynamic constants for the removal of COD, BOD, and TOC from the wastewater. The activation energy (Ea) for homogeneous and heterogeneous Fenton oxidation processes were 44.79 and 25.89?kJ/mol, respectively. The thermodynamic parameters ??G, ??H, and ??S were calculated for the oxidation processes using Van??t Hoff equation. Furthermore, the degradation of organics was confirmed through FTIR and UV?Cvisible spectroscopy, and cyclic voltammetry.

Conclusions

The heterocatalytic Fenton oxidation process efficiently increased the biodegradability index (BOD/COD) of the tannery effluent. The optimized conditions for the heterocatalytic Fenton oxidation of organics in tannery effluent were pH 3.5, reaction time?C4?h, and H₂O₂/FeSO₄·7H₂O in the molar ratio of 2:1.     

A critical evaluation of combustible/explosible dust testing methods – Part 1

Tests were conducted by the Center for Agricultural Air Quality Engineering and Science (CAAQES) and by Safety Consulting Engineers Inc. (SCE) to determine if dust found in cotton gins (gin dust) would serve as fuel for dust explosions. In other words, is gin dust explosible? The laboratory tests used by CAAQES and SCE are very different. SCE used a totally enclosed 20 liter (L) chamber, flame from a 10,000 J (10 kJ) ignition source, reported that gin dust was a class ‘A’ explosible dust. CAAQES used a 28.3-L (1 ft³) chamber with diaphragm, a stationary coil as the igniter, video and pressure recordings of each test and concluded that gin dust was not explosible. SCE followed the protocols specified by ASTM E1226 and E1515. The only indicator used to determine whether a deflagration occurred during a test was pressure. If the pressure rise exceeded one bar gage (g) in a 20-L chamber test with a flame from a 10 kJ energy source as the igniter, it was assumed that a deflagration occurred in the chamber and the dust was classified as explosible (ASTM E1226-05, 2005). The CAAQES criterion for determining if a dust was explosible consisted of determining the minimum explosive concentration (MEC). If the MEC existed using the CAAQES test system, it was explosible! The criteria used with the CAAQES method for determining the MEC was to test concentrations starting at concentrations above the MEC and lowering the concentrations until at least one of the three tests at that concentration failed to result in a deflagration. The indicators of a deflagration were (1) bursting of a diaphragm, (2) flame front leaving the chamber and (3) characteristic pressure vs. time curve.It was concluded that the ASTM method of using only pressure as the indicator of a deflagration in a totally enclosed chamber would likely result of an “over-driven” test and an incorrect finding that gin dust was explosible. The result of CAAQES testing was that gin dust was not explosible.     

Bacterial composting of animal fleshing generated from tannery industries

Animal fleshing (ANFL) is the major proteinaceous solid waste generated during the manufacture of leather, which requires to be disposed of by environmentally sound manner. This study reports about the treatment of ANFL into an organic compost and its effects on physiological parameters of different crops in a laboratory study. The ANFL was hydrolysed using Selenomonas ruminantium HM000123 and then the hydrolysed ANFL was mixed with cow dung and leaf litter for producing composted organic fertilizer (COF). The COF was characterized for pH, electrical conductivity (EC), total Kjeldhal nitrogen (TKN), and total organic carbon (TOC). The composting resulted in a significant reduction in pH, TOC and C:N ratio and an increase in TKN after 49 days in a compost reactor. Scanning electron microscope and FT-IR were used to analyse the hydrolysis of intra structural ANFL matrix and changes in the functional groups, respectively, in initial and final day COF. Thermogravimetry (TG) analysis was carried out for the raw mixture and COF samples to identify the weight loss under the nitrogen environment. The relative seed germination was found to be 94% in tomato (Lycopersicon esculentum), 92% in green gram (Vigna radiata), 86% in bottle gourd (Lagenaria siceraria (Mol.) Standl.) and 84% in cucumber (Cucumis sativus L.) using the extracts of COF. The results indicate that the combination of both hydrolysis and bacterial composting reduced the overall time required for composting and producing a nutrient-enriched compost product.     

Size-dependent in vitro cytotoxicity assay of gold nanoparticles

Gold nanoparticles (AuNps) may serve as a promising model to address the size-dependent biological response of cell lines. Their size can be controlled with great precision during chemical synthesis. AuNps have potential applications in drug delivery, cancer diagnosis, and therapy, in the food industry, and for environmental remediation. However, some of the recent literature contains conflicting data regarding the cytotoxicity of gold nanoparticles. Against this background, a systematic study of water soluble gold nanoparticles stabilized by citrate ranging in size from 3?nm to 45?nm were synthesized. The cytotoxicity of these particles were tested by employing the (3-[4,5-dimethylthiazol-2-yl]-2,5-diphenyltetrazolium bromide reduction assay), the neutral red cellular uptake assay, and lactate dehydrogenase release assay. Noticeable differences in the cytotoxic effects depending on the assay, and the nanoparticle size have been found. Citrate stabilized gold nanoparticles with sizes of 3?nm, 8?nm, and 30?nm were more sensitive to the cell lines and caused gradual cell death within 24?h at higher concentrations. This results in IC50 values ranging from 57 to 78?μgmL^?1 depending on the particle size, and cell line combinations. In contrast, AuNps with diameters of 5?nm, 6?nm, 10?nm, 17?nm, and 45?nm were nontoxic up to three to four fold higher concentrations, and at long-term exposure.     

Design of Mass Exchange Network and Effluent Distribution System for effective water management

The environmental impact of industrial wastewater and higher cost of fresh water are the serious challenges faced by the process industries. It has led to the development of many new techniques to minimize fresh water consumption. Of the many approaches, which have been developed, the Water Source Diagram (WSD) is a flexible and dynamic alternative for the generation of different scenarios for the management of water networks with reduction in total consumption. In the present study WSD concept was coupled with water mains concept to mains simplify the piping network and reduce the cost. A new procedure was developed for integrating the effluent treatment processes to evolve Effluent Treatment Network. Example from literature having multi contaminants was considered. This simple procedure involving hand calculations will be a useful tool for process engineers to design water and effluent treatment networks. Also the WSD and ETN were combined to form an evolutionary WAMEN (Water Allocation and Mass Exchange Network) and the proposed WAMEN aims for minimum fresh water consumption.