The impregnation of mesoporous carbon cloth with alumina has been studied. The most successful method of impregnation resulted from preparation of the alumina phase by a sol/gel route. This method involves a boehmite intermediate, and the heating environment for the thermal transition of boehmite to the final alumina was investigated. Heat treatment of the boehmite intermediate under flowing N2, flowing air and vacuum was found to give a different pore size distribution for the final alumina than did still air heat treatment. For the former environments the transition from boehmite to alumina was not accompanied by the usual increase in pore size. Alumina/carbon composites were made by dipping pieces of mesoporous carbon cloth in a boehmite sol. The distribution of boehmite about the carbon cloth was found to be improved by pre-wetting the carbon cloth and by the use of ultrasonic dispersion during boehmite impregnation. Dried boehmite/carbon composites, with loading levels of up to 180wt.%, were heated under vacuum to 5000 C. In this manner alumina/carbon composites of up to 60wt.% alumina were fabricated. The distribution of the alumina phase about the carbon cloth was investigated by electron microscopy and by gas adsorption techniques. Nitrogen isotherm data indicated that the mesopores of the carbon cloth were not blocked by the deposited alumina, rather the pore volume of the carbon cloth was increased by the clustering of porous alumina about the pore entrances of the carbon cloth. Water isotherms were determined for the composite materials. The water activity of the composite, particularly at low relative pressures, was found to be significantly greater than that of the carbon cloth as a result of the presence of alumina. CO2 activity of the composites was investigated by a gas chromatographic technique. The CO2 activity of the composite material was found to be up to 500 times greater than that of virgin carbon cloth.

The modification of anode materials is important to enhance the power generation of MFCs (microbial fuel cells). A novel and cost-effective modified anode that is fabricated by dispersing manganese dioxide (MnO2) and HNTs (Halloysite nanotubes) on carbon cloth to improve the MFCs' power production was reported. The results show that the MnO2/HNT anodes acquire more bacteria and provide greater kinetic activity and power density compared to the unmodified anode. Among all modified anodes, 75 wt% MnO2/HNT exhibits the highest electrochemical performance. The maximum power density is 767.3 mWm(-2), which 21.6 higher than the unmodified anode (631 mW/m(2)). Besides, CE (Coulombic efficiency) was improved 20.7, indicating that more chemical energy transformed to electricity. XRD (X-Ray powder diffraction) and FTIR (Fourier transform infrared spectroscopy) are used to characterize the structure and functional groups of the anode. CV (cyclic voltammetry) scans and SEM (scanning electron microscope) images demonstrate that the measured power density is associated with the attachment of bacteria, the microorganism morphology differed between the modified and the original anode. These findings demonstrate that MnO2/FINT nanocomposites can alter the characteristics of carbon cloth anodes to effectively modify the anode for practical MFC applications. (C) 2016 Elsevier Ltd. All rights reserved.

Les carbones activés, de par leur nanotexture développée, sont performants pour l’élimination de micropolluants organiques à l’état de traces. Ils trouvent une place prépondérante au sein des usines de traitement pour la dépollution de l’eau. Néanmoins, l’adsorption de ces composés, conduit à la saturation du matériau selon un processus d’adsorption irréversible. Un procédé électrochimique capable d’opérer à la régénération in situ des adsorbants carbonés chargés en polluants est proposé. L’applicabilité du procédé a été évaluée sur une grande diversité de micropolluants rencontrés dans les effluents traités. Ces molécules s’adsorbent préférentiellement au niveau des ultramicropores via des interactions dispersives de type π-π. La régénération électrochimique de l’adsorbant s’effectue grâce à l’application d’une polarisation, qui génère une interface chargée et induit un champ électrostatique entre les deux électrodes. La décomposition de l’électrolyte, confiné dans les pores, engendre des effets de pH localisés, responsables de la dissociation de la molécule adsorbée. La désorption sous polarisation fait intervenir des répulsions électrostatiques entre la surface chargée du matériau carboné et le polluant dissocié. Ce procédé de régénération, applicable à de nombreux micropolluants, montre des efficacités différentes selon de la nature du polluant adsorbé. La désorption est favorisée pour des polluants de petite taille, facilement ionisables et solubles ; des efficacités de régénération élevées (jusqu’à 80 %) à partir du quatrième cycle sont reportées. Une partie des polluants est piégée irréversiblement soit parce qu’ils sont bloqués dans les ultramicropores, soit parce qu’ils s’adsorbent au niveau de sites énergétiques ou via des interactions plus spécifiques. L’obstruction cumulative de la porosité par un adsorbat volumineux par exemple, engendre une diminution des efficacités de régénération avec la répétition des cycles. / Due to their developed porosity, the activated carbons are efficient for the removal of organic micropollutants at trace concentration. They find an important place in wastewater treatment for water decontamination. Nevertheless, the adsorption of these compounds leads to the adsorbent saturation and therefore makes the process irreversible. We have developed an electrochemical process which is able to operate to the in situ adsorbent regeneration. The process applicability was assessed on a wide range of micropollutants, found in the treated effluents. These molecules are adsorbed in the ultramicropores through π-π interactions. The electrochemical regeneration of the loaded adsorbent is performed by applying a polarization, which generates an electrically charged carbon surface and induced an electrostatic field between the two electrodes. The electrochemical decomposition of the electrolyte inside the porosity, leads to local pH effects which are responsible of the dissociation of the adsorbed molecule. The desorption under polarization implies electrostatic repulsions between the polarized carbon surface and the dissociated pollutant. This regeneration process can be broadened to numerous micropollutants and shows an efficiency which depends on the adsorbat nature. We have shown that the desorption of small pollutants which are easily ionisable and soluble is promoted. High desorption levels until 80 % after four desorption cycle are indeed reported. A part of the adsorbed molecules is trapped irreversibly either because they are blocked in the ultramicropores or due to the micropollutant adsorption at high energy sites and/or through specific strong interactions. For example, the porosity obstruction caused by a voluminous molecule leads to the decrease of the regeneration efficiency along the cycles repetition.

The Polymer Electrolyte Membrane (PEM) fuel cell has a great potential in leading the future energy generation due to its advantages of zero emissions, higher power density and efficiency. For a PEM fuel cell, the Membrane-Electrode Assembly (MEA) is the key component which consists of a membrane, two catalyst layers and two gas diffusion layers (GDL). The success of optimum PEM fuel cell power output relies on the mass transport to the electrode especially on the cathode side. The carbon based GDL is one of the most important components in the fuel cell since it has one of the basic roles of providing path ways for reactant gases transport to the catalyst layer as well as excess water removal. A detailed understanding and visualization of the GDL from micro-scale level is limited by traditional numerical tool such as CFD and experimental methods due to the complex geometry of the porous GDL structural. In order to take the actual geometry information of the porous GDL into consideration, the x-ray tomography technique is employed which is able to reconstructed the actual structure of the carbon paper or carbon cloth GDLs to three-dimensional digital binary image which can be read directly by the LB model to carry out the simulation. This research work contributes to develop the combined methodology of x-ray tomography based the three-dimensional single phase Lattice Boltzmann (LB) simulation. This newly developed methodology demonstrates its capacity of simulating the flow characteristics and transport phenomena in the porous media by dealing with collision of the particles at pore-scale. The results reveal the heterogeneous nature of the GDL structures which influence the transportation of the reactants in terms of physical parameters of the GDLs such as porosity, permeability and tortuosity. The compression effects on the carbon cloth GDLs have been investigated. The results show that the c applied compression pressure on the GDLs will have negative effects on average pore size, porosity as well as through-plane permeability. A compression pressure range is suggested by the results which gives optimum in-plane permeability to through-plane permeability. The compression effects on one-dimensional water and oxygen partial pressures in the main flow direction have been studied at low, medium and high current densities. It s been observed that the water and oxygen pressure drop across the GDL increase with increasing the compression pressure. Key Words: PEM fuel cell, GDL, LB simulation, SPSC, SPMC, x-ray tomography, carbon paper, carbon cloth, porosity, permeability, degree of anisotropy, tortuosity, flow transport.

This thesis examines the use of electrochemically treated viscose rayon based activated carbon cloth (ACC) for the removal of metal ions from aqueous effluent streams. Two types of treatment were performed: (i) electrochemical oxidation and (ii) electrochemical reduction to enhance cation and anion sorption capacities of the ACC, respectively. Electrochemical oxidation resulted in a loss of 61% BET surface area due to blockage of pores through formation of carboxylic acidic groups but its cation exchange capacity and oxygen content increased by 365% and 121%, respectively. The optimum constant current at which a combination of applied current and oxidation time at any extent of oxidation to produce ACC of maximum cation exchange capacity was found to be 1.1 A, with voltage of 4.2 V and current density of 0.8 mA/m2. Batch sorption experiments showed that the maximum copper and lead sorption capacities for electrochemically oxidised ACC increased 17 and 4 times, respectively, for noncompetitive sorption and 8.8 and 8.6 times, respectively for competitive sorption. Therefore, electrochemically oxidised ACC is an effective adsorbent for treating aqueous solution contaminated with copper/lead in both single component and multi-component systems. Industrial wastewaters are multicomponent systems, therefore, electrochemical oxidation of ACC is an efficient way of enhancing lead and copper ions sorptive capacity for industrial wastewater treatment. Electrochemical reduction resulted in a loss of 28% BET surface area due to formation of ether groups but its anion exchange capacity increased by 292%. The optimum constant current at which a combination of applied current and reduction time at any extent of reduction to produce ACC of maximum anion exchange capacity was found to be 5.5 A, with voltage of 9.8 V and current density of 6.4 mA/m2. Batch sorption experiments showed that the maximum chromium(VI) sorption capacity for electrochemically reduced ACC increased 2.12 times, with highest maximum chromium(VI) sorption capacity of 3.8 mmol/g at solution pH 4. Most industrial wastewaters contaminated with chromium(VI) are highly acidic, therefore, electrochemical reduction of ACC is an efficient way of enhancing chromium(VI) sorptive capacity for industrial wastewater treatment.

No / Here we report a hierarchical composite structure composed of few-layers molybdenum disulfide nanosheets supported by vertical graphene on conductive carbon cloth (MDNS/VG/CC) for high-performance electrochemical hydrogen evolution reaction (HER). In the fabrication, 3D vertical graphene is first prepared on carbon cloth by a micro-wave plasma enhanced chemical vapor deposition (MPCVD) and then few-layers MoS2 nanosheets are in-situ synthesized on the surface of the vertical graphene through a simple hydrothermal reaction. This integrated catalyst exhibits an excellent HER electrocatalytic activity including an onset potential of 50 mV, an overpotential at 10 mA cm(-2) (eta(10)) of 78 mV, a Tafel slop of 53 mV dec(-1), and an excellent cycling stability in acid solution. The excellent catalytic performance can be ascribed to the abundant active edges provided by the vertical MoS2 nanosheets, as well as the effective electron transport route provided by the graphene arrays on the conductive substrate. Moreover, the vertical graphene offers robust anchor sites for MoS2 nanosheets and appropriate intervals for electrolyte infiltration. This not only benefits hydrogen convection and release but also avoids the damaging or restacking of catalyst in electrochemical processes. / This work was financially supported by the National Natural Science Foundation of China (Grant nos. 61176007, 51372213, and 51402343).

Capacitive deionization is a promising technology for purification and desalination of brackish water with great advantages over current technologies due to its low operating cost and high-water recovery ratio. Most of the system studied relies on the adsorption/desorption capacity of activated carbon electrodes due to its high surface area. However, its specific adsorption capacity is limited since the adsorption is predominantly on the surface of the electrodes. In this thesis we propose the use of polyaniline as a chloride-ion adsorption material. Polyaniline is a redox polymer able to accommodate anions in several of its three states when subjected to an external voltage. To this end, we synthesized polyaniline by electrodeposition technique and its electrochemical behavior was studied. A hybrid CDI system was assembled, using PANI as anode material and activated carbon cloth as cathode, showing outstanding adsorption of 37.26 mg/g Cl at current densities of 250 A/g. The energy consumption of this system was of 0.4979 kWh/m3. Its stability was evaluated over 50 cycles with negligible capacity loss. Along with its use in a CDI system, the aim of this thesis was to understand the mechanisms of operation of this material, by means of its physical and electrochemical characterization, as well as its efficiency and stability through the use of this material in capacitive deionization cells. / Kapacitiv avjonisering är en lovande teknik för rening och avsaltning av bräckt vatten med stora fördelar jämfört med nuvarande teknik på grund av dess låga driftskostnader och höga vattenåtervinningsgrad. De flesta av de studerade systemen bygger på adsorptions/desorptionskapaciteten hos elektroder av aktivt kol på grund av dess stora yta. Dess specifika adsorptionskapacitet är dock begränsad eftersom adsorptionen huvudsakligen sker på elektrodernas yta. I den här avhandlingen föreslår vi att polyanilin används som adsorptionsmaterial för kloridjoner. Polyanilin är en redoxpolymer som kan ta emot anjoner i flera av sina tre tillstånd när den utsätts för en extern spänning. För detta ändamål syntetiserade vi polyanilin genom elektrodepositionsteknik och dess elektrokemiska beteende studerades. Ett hybrid CDI-system monterades med PANI som anodmaterial och aktiverad kolduk som katod, vilket visade en enastående adsorption av 37,26 mg/g Cl vid en strömtäthet på 250 A/g. Energiförbrukningen för detta system var 0,4979 kWh/m3. Systemets stabilitet utvärderades över 50 cykler med försumbar kapacitetsförlust. Förutom användningen i ett CDI-system var syftet med denna avhandling att förstå detta materials funktionsmekanismer genom fysisk och elektrokemisk karakterisering samt dess effektivitet och stabilitet genom användning av detta material i kapacitiva avjoniseringsceller.