2644 research outputs found

    High performance polyaniline containing coating system for wet surfaces

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    Application of paint coatings on wet surfaces is rather difficult due to poor adhesion of coatings. For painting of wet surfaces, moisture curable coating systems based on epoxy resin and ketimine are found to be useful. Hence a study has been made on the corrosion protection ability of coating on wet surfaces using epoxy resin, ketimine and polyaniline. Paints with 20–30% PVCwere prepared and applied over the wet steel surface and the corrosion protection performance of the coating was found out by salt spray and electrochemical impedance spectroscopic techniques. Coating with 20% PVC is found to offer very high protection since the impedance values are remained at greater than 109 �cm2 after immersion and salt spray tests

    LiFAP-based PVdF–HFP microporous membranes by phase-inversion technique with Li/LiFePO4 cell

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    Polyvinylidenefluoride–hexafluoropropylene-based (PVdF–HFP-based) gel and composite microporous membranes (GPMs and CPMs) were prepared by phaseinversion technique in the presence 10 wt% of AlO(OH)n nanoparticles. The prepared membranes were gelled with 0.5-M LiPF3(CF2CF3)3 (lithium fluoroalkylphosphate, Li- FAP) in EC:DEC (1 : 1 v/v) and subjected to various characterizations; the AC impedance study shows that CPMs exhibit higher conductivity than GPMs. Mechanical stability measurements on these systems reveal that CPMs exhibit Young’s modulus higher than that of bare and GPMs and addition of nanoparticles drastically improves the elongation break was also noted. Transition of the host from α to β phase after the loading of nanosized filler was confirmed by XRD and Raman studies. Physico-chemical properties, like liquid uptake, porosity, surface area, and activation energy, of the membranes were calculated and results are summarized. Cycling performance of Li/CPM/LiFePO4 coin cell was fabricated and evaluated at C/10 rate and delivered a discharge capacity of 157 and 148 mAhg−1 respectively for first and tenth cycles

    PEFC Electrode with Enhanced Three-Phase Contact and Built-in Supercapacitive Behavior

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    Hydrous ruthenium oxide, which exhibits both protonic and electronic conduction, is incorporated in the cathode electrocatalyst layer of the membrane electrode assembly for polymer electrolyte fuel cells (PEFCs). The supercapacitive behavior of ruthenium oxide helps realize a fuel cell–supercapacitor hybrid. Platinum (Pt)nanoparticles are deposited onto carbon-supported hydrous ruthenium oxide and the resulting electrocatalyst is subjected to both physical and electrochemical characterization. Powder X-ray diffraction and transmission electron microscopy reflect the hydrous ruthenium oxide to be amorphous and well-dispersed onto the catalyst. X-ray photoelectron spectroscopy data confirm that the oxidation state of ruthenium in Pt anchored on carbon-supported hydrous ruthenium oxide is Ru4+. Electrochemical studies, namely cyclic voltammetry, cell polarization, intrinsic proton conductivity, and impedance measurements, suggest that the proton-conducting nature of hydrous ruthenium oxide helps extend the three-phase boundary in the catalyst layer, which facilitates improvement in performance of the PEFC. The aforesaid PEFC operating with hydrogen fuel and oxygen as oxidant shows a higher power density �0.62 W/cm2 @ 0.6 V� in relation to the PEFC comprising carbon-supported Pt electrodes �0.4 W/cm2 @ 0.6 V�. Potential square-wave voltammetry study corroborates that the supercapacitive behavior of hydrous ruthenium oxide helps ameliorate the pulse-power output of the fuel cell

    Corrosion protection of iron by benzoate doped polyaniline containing coatings

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    Polyaniline containing organic coatings based on vinyl and acrylic resins are found to protect iron in acid and neutral media. Since dopants play an important role in forming salts with iron, a study has been made on the effect of benzoate doped polyaniline on the corrosion protection of iron by polyaniline–vinyl coatings in acid and neutral media. EIS studies have been made on the corrosion protection performance of vinyl coating on steel with 1% polyaniline in 0.1N HCl and 3%NaCl up to 100 days of exposure. It has been found that benzoate doped polyaniline containing coating has found to offer more protection in neutral media than that in acidic media due to passivating ability of benzoate ions in neutral solution, along with iron–polyaniline complex

    Studies on a Mg-Al-Zn Alloy as an Anode for the Removal of Fluoride from Drinking Water in an Electrocoagulation Process

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    The present study provides an electrochemical coagulation process for the removal of fluoride from drinking water using a Mg-Al-Zn alloy, magnesium, aluminum and mild steel as anodes and stainless steel as cathode. Various parameters which may affect the removal efficiency of fluoride from water, such as pH, concentration of fluoride, current density, temperature and co-existing ions were studied. Electrochemical coagulation was carried out for 30 min at an initial fluoride concentration of 5.0 mg/ L and this was reduced to 0.2 mg/L. A maximum removal efficiency of 96% was achieved with a magnesium alloy as anode and stainless steel as cathode at a current density of 0.2 A/dm2 and a pH of 7.0

    Electrochemical Degradation of Remazol Black B Dye Effluent

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    This study focused on the electrochemical degradation of hydrolyzed Remazol Black B (CI Reactive Black 5), a common diazo reactive dye, in aqueous solution. In the presence of various auxiliary dye chemicals, a typical Remazol Black simulated exhausted dyebath liquor was treated electrochemically in various basic electrochemical reactor configurations such as batch, batch recirculation and single pass systems. The effect of current density, supporting electrolyte concentration, electrolysis duration, specific electrode surface and fluid flow rate on pollutant removal and energy consumption performance of the systems was critically evaluated. Batch studies show the following operating parameters, current density: 2.5 A/dm2, electrolysis duration: 6 h, and supporting electrolyte concentration: 3 g/L, were optimal for good overall performance of the system. Color removal was complete by 3 h of treatment for all combinations of parameters studied. The pollutant removal performance of the batch recirculation system was found to have improved considerably by increasing the flow rate. Performance of the batch recirculation system was comparatively better than the other rector configurations studied, with respect to capacity utilization and energy consumption

    Tailoring self-assembled monolayers at the electrochemical interface

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    The main focus of this review is to illustrate the amenability of self-assembled monolayers (SAMs) for functionalisation with different receptors, catalytic materials, biomolecules, enzymes, antigen- antibody, etc for various applications. The review discusses initially about the preparation and characterization of SAMs and tailoring of SAMs by incorporation of suitable recognition elements. A description of how the molecular recognition is achieved through forces like electrostatic, covalent and host–guest interactions is included in the review

    Electrochemical degradation of pulp and paper industry waste-water

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    BACKGROUND: Conventional biological waste-water treatment techniques are insufficient to degrade large quantities of dissolved lignin discharged by small-scale paper mills. The current investigation is aimed at comparing the overall performance of basic electrochemical reactor configurations such as batch, batch recirculation, recycle and single pass systems, in removing the organic part of waste-water from a small-scale, agro-based paper industry. The effect of current density, supporting electrolyte concentration, duration of electrolysis, specific electrode surface and fluid flow rate on the removal of pollutants and energy consumption are critically evaluated. The improvement in biodegradability of the effluent during treatment is also noticed. RESULTS: The batch recirculation mode of operation was found to be superior in comparison with a batch system using the same specific electrode surface for both COD removal (73.3 vs. 64%) and capacity utilization (rate constant 1.112 × 10−3 vs. 1.049×10−3 cms−1). Thepollutant removalperformance of thebatch recirculation system improved considerablywith increase in the circulation flow rate. At the best operating point in the recycle system, 59% of COD was removed, corresponding to a current efficiency of 68.9% and specific energy consumption of 18.46 kWh kg−1. The biodegradability index of thewaste-water was improved from 0.18 ± 0.01 to 0.36 ± 0.01. CONCLUSION: A recycle reactor was the best configuration, because of its flexibility of operation. Circulation flow rate and withdrawal flow rate enable the control of transfer coefficients and treatment duration respectively. Electrochemical treatment not only removes the bulk of the organicmatter, but alsomakes the remaining pollutantsmore easily biodegradable

    High performance dye-sensitized solar cells containing 1-methyl-3-propyl imidazolinium iodide-effect of additives and solvents

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    In this work, the influences of redox electrolyte, additives and solvents on the photovoltaic performance of dye-sensitized solar cells (DSSCs) containing 1-methyl-3-propyl-imidazolinium iodide (MPII) as the electrolyte were investigated. An optimum conductivity of 20.31 mS cm1 for 0.6 M MPII in acetonitrile (AN) was found out from the conductivity measurement. Diffusion coefficient of I3 and photocurrent density (JSC) of the DSSC varied with concentration of I2. Among the different inorganic and organic iodides as additives, the DSSC showed high performance with lithium iodide (LiI) and tetrabutylammonium iodide (TBAI), respectively. The performance of the DSSCs with different solvents was studied. From the EIS studies, it was inferred that the poor conversion efficiencies of the DSSCs were associated with high charge transfer resistance, noted along the TiO2/solvent interface. A high conversion efficiency of 6.7% (JSC of 14.8 mA cm�2, VOC of 0.74 V, fill factor (FF) 0.62 under one sun (AM 1.5)) was obtained for the DSSC containing the electrolyte composition of 0.6 M of MPII/0.2 M of LiI/0.06 M of I2/0.5 M of TBP in AN along with the incorporation of light scattering particles (TiO2 of 300 nm)

    Corrosion Protection Mechanism of Polyaniline Blended Organic Coating on Steel

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    Epoxy–coal tar coatings are widely used to protect steel structures exposed to marine atmosphere due to their good barrier property. However, the presence of micropores and microcracks formed during the coating formation leads to failure of the coating due to permeation of corrosive ions. In recent years, it has been established that the coatings containing polyaniline �PANI� is able to protect pinholes and defects due to its passivating ability. Hence, a study has been made on the effect of polyaniline content �1 and 3%� in epoxy–coal tar coating on the corrosion protection of steel in 3% NaCl solution by electrochemical impedance spectroscopy �EIS� studies. Both phosphate- and chloride-doped polyanilines were prepared by a chemical oxidative polymerization method. From EIS studies, it has been found that the resistance value of the coatings containing 1 and 3% phosphate-doped polyaniline and 3% chloride-doped polyaniline pigmented coatings are �109 � cm2 even after 90 days exposure to NaCl solution, which are two orders high in comparison to that of conventional coal tar epoxy coatings. Besides, the conducting state of polyaniline has been found to be decreased after exposure to NaCl solution due to redox property of PANI. X-ray photoelectron spectroscopy studies have shown that polyaniline forms a complex layer with iron beneath the coating along with iron oxide

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