Resumo Carbetos de metais de transição vêm sendo aplicados com sucesso em substituição aos catalisadores convencionais principalmente devido às suas propriedades físico-químicas. A estrutura da superfície, composição química, interação metal-suporte e condições de processamento são essenciais na aplicação dos carbetos para esse fim. O presente estudo teve como objetivo sintetizar, em leito fixo, a partir de reação gás-sólido, carbeto de molibdênio puro, bimetálico (Mo-Ni) e suportado em carvão ativado obtido através da pirólise do lodo de esgoto, e compará-los visando aplicação em reações catalíticas. O carvão foi submetido a um processo de ativação química utilizando KOH e tratamento térmico. Os materiais foram caracterizados através das análises de TG, DRX, FRX, MEV, área superficial e volume de poros através do método BET e análise granulométrica. As isotermas de adsorção e dessorção foram também obtidas para os diferentes materiais. Os resultados mostraram que a metodologia utilizada para síntese dos materiais foi satisfatória, principalmente tendo em vista o aumento significativo da área superficial dos materiais, de 13 para 141 m2/g, quando o carvão foi tratado com KOH bem como quando o mesmo foi adicionado ao carbeto (de 45 para 73 m2/g), o qual pode justificar uma aplicação catalítica.

Abstract Transition metal carbides have been successfully used as substitute materials for conventional noble metal catalyst in several important industrial reactions due to their interesting physicochemical properties. Surface structure, chemical composition and metal-support interactions, as well as processing conditions, are of utmost importance in the use of such materials in catalysis. The present study aimed to synthesize and evaluate pure molybdenum carbide with and without support, and bimetallic Mo-Ni carbide over a carbon active support derived from sewage sludge pyrolysis. The support was chemically (KOH) and physically (thermal treatment) activated before use. TG/DTG, XRD, XRF, SEM, BET and particle size evaluation were performed, together with adsorption/desorption isotherms. Results indicated that the applied synthesis method was adequate for the obtainment of pure materials. The increase in surface area of the support was significant, from 13 to 141 m².g-1 after the thermal and chemical treatment; also, supporting Mo2C over carbon provided an increase from 45 to 73 m².g-1 in surface area, which indicated its potential as a catalytic material as well as the effectiveness of the applied methodology.

In the present work, a synthetic effluent of phenol was treated by means of a total oxidation process-Catalyzed Wet Oxidation (CWO). A mixed oxide of Mn-Ce (7:3), the catalyst, was synthesized by co-precipitation from an aqueous solution of MnCl2 and CeCl3 in a basic medium. The mixed oxide, MnO2/CeO2, was characterized and used in the oxidation of phenol in a slurry reactor in the temperature range of 80-130ºC and pressure of 2.04-4.76 MPa. A phenol solution containing 2.4-dichlorophenol and 2.4-dichlorophenoxyacetic acid was also degraded with good results. A lumped kinetic model, with two parallel reaction steps, fits precisely with the integrated equation and the experimental data. The kinetic parameters obtained are in agreement with the Arrhenius equation. The activation energies were determined to be 38.4 for the total oxidation and 53.4 kJ/mol for the organic acids formed.

A rotating cylinder reactor was designed for the synthesis of niobium carbide powders at 1173 K. Niobium carbide, NbC, was prepared by carbothermal reduction starting from commercial niobium pentoxide powders. The reactor was heated using a custom-made, two-part, hinged, electric furnace with programmable temperature control. The design and operational details of the reactor are presented. The longitudinal temperature gradient inside the reactor was determined. Total reaction time was monitored by a gas chromatograph equipped with an FID detector for determination of methane concentrations. The results show that time of reaction depended on rotation speed. NbC was also prepared in a static-bed alumina reactor using the same conditions as in the previous case. The niobium carbide powders were characterized by X-ray diffraction and compared with commercially available products. Morphological, particle size distribution and surface area analyses were obtained using SEM, LDPS and BET, respectively. Therefore, the present study offers a significant technological contribution to the synthesis of NbC powders in a rotating cylinder reactor.