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different drawbacks such as difficulty in separation of the catalysts from the product stream, requirement of large amount of catalyst, and disposal of the solid waste formed during the reaction. Furthermore, the cost of process installation and maintenance

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(“special purity” grade) from an aqueous solution followed by thorough washing by distilled water. The sample weight was 5.0 g. The grain size of the metal ranged between 0.5 and 1.0 mm. After placing the sample into the vacuum installation, it was subjected

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. Di Giovacchino , B. Bianchi , P. Catalano . Evolution technologique des installations d’extraction de l’huile d’olives . Olivae 48 ( 1993 ) 43 – 53 . [23] S. H

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instead of hydrogarnet. It can be formed in the CaO–Al 2 O 3 –CaSO 4 –H 2 O system for example in the case when fly ash and calcium sulphate were added to CAC [ 17 ]. Spent catalyst from the fluidized catalytic cracking installation (named here as

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Acta Microbiologica et Immunologica Hungarica
Authors: Szabolcs Vigvári, Áron Vincze, Jenő Solt, Dávid Sipos, Zsófia Feiszt, Beáta Kovács, Ágnes Kappéter and Zoltán Péterfi

. : Results of fecal donor installation therapy for recurrent Clostridium difficile associated diarrhea . Scan J Infect Dis 42 , 857 – 861 ( 2010 ). 10.3109/00365548.2010.499541 17

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Journal of Thermal Analysis and Calorimetry
Authors: J. J. H. Lancastre, F. M. A. Margaça, L. M. Ferreira, A. N. Falcão, I. M. Miranda Salvado, M. S. M. S. Nabiça, M. H. V. Fernandes and L. Almásy

SANS-II at SINQ installation of the former Ris⊘-SANS facility . Physica B Condens Matter 350 (1–3) Suppl 1 E783 – E786 10.1016/j.physb.2004.03.204 . 13. Portela Marques , MM , Miranda

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obtained nanocomposites was performed with an installation equipped with a data acquisition system. Results and discussion Former studies on the redox reaction between metallic nitrates and diols (EG, 1,2 PG, 1,3 PG) [ 9 , 21

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Journal of Thermal Analysis and Calorimetry
Authors: María Villanueva, Jorge Proupín, José A. Rodríguez-Añón, L. Fraga-Grueiro, Josefa Salgado and Nieves Barros

of moisture in Paulownia, installations dedicated to the use of biomass for the elaboration of solid fuels must be near the production zone (less than 15 km) and they must have natural drying places to avoid excessive cost in the transportation and

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, copper acetate monohydrate) or solvents were of p.a. purity and were also used as such. Water was deionized by a Millipore installation. Support functionalization The functionalization of the supports concerns the

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Reaction Kinetics, Mechanisms and Catalysis
Authors: Viorel Chihaia, Karl Sohlberg, B. Grzybowska-Świerkosz, M. Ruszel, R. Grabowski, L. Kępiński, M. A. Małecka and J. Sobczak

and H 2 O, occurring on supported metal catalysts (Pt and its alloys, Pd), is widely used for the removal of toxic impurities in the exhaust gases of numerous installations, in particular in transport vehicles [ 14 ]. In several scientific papers, Au

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