Sviluppo di un metodo elettrochimico per la determinazione della capacità antiossidante

The aim of the present thesis, carried out at the Analytical Group of the Faculty of Industrial Chemistry in Bologna, is to develop a new electrochemical method for the determination of the Antioxidant Capacity (AOC). The approach is based on the deposition of a non-conducting polymeric film on the working electrode surface and the following exposition to the radicals OH· produced by H2O2 photolysis. The strongly oxidant action of hydroxyl radicals degrades, causing an increase of the Faradic current, relevant to the redox couple [Ru(NH3)6]2+/3+ monitored by cyclic voltammetry(CV); the presence of an antioxidant compound in solution slows down the radical action, thus protecting the polymeric film and blocking the charge transfer. The parameter adopted for the quantification of the AOC, was the induction time, called also lag phase, which is the time when the degradation of the film starts. Five pure compounds, among most commonly antioxidant, were investigated : Trolox®(an analogue water-soluble of vitamin E), (L)-ascorbic acid, gallic acid, pyrogallol and (-)- epicatechin. The AOC of each antioxidant was expressed by TEAC index (Trolox® Equivalent Antioxidant Capacity), calculated from the ratio between the slope of the calibration curve of the target compound and the slope of the calibration curve of Trolox®. The results from the electrochemical method, have been compared with those obtained from some other standardized methods, widely employed. The assays used for the comparison, have been: ORAC, a spectrofluorimetric method based on the decrease of fluorescein emission after the attack of alkylperoxide radicals, ABTS and DPPH that exploit the decoloration of stable nitrogen radicals when they are reduced in presence of an antioxidant compound and, finally, a potentiometric method based on the response of the redox couple [Fe(CN)6]3-/ [Fe(CN)6]4-. From the results obtained from pure compounds, it has been found that ORAC is the methodology showing the best correlation with the developed electrochemical method, maybe since similar radical species are involved. The comparison between the considered assays, was also extended to the analysis of a real sample of fruit juice. In such a case the TEAC value resulting from the electrochemical method is higher than those from standardized assays.

Catalizzatori per la reazione di Water Gas Shift a media ed alta temperatura

L’H2 è un vettore energetico di elevato interesse, utilizzato nell’industria chimica per la produzione di NH3 e CH3OH, oltre che per le reazioni di idrogenazione ed HDS. Un importante processo nella produzione di H2 è la reazione di Water Gas Shift (WGS), usata nel trattamento delle correnti uscenti dal reattore di Steam Reforming (SR) del metano: CO + H2O  CO2 + H2 ∆H0298K = -41,2 KJ/mol. Sulla base di precedenti lavori, sono stati sviluppati nuovi catalizzatori per la reazione WGS ad alta temperatura (HTS), alternativi ai tradizionali sistemi a base di Fe/Cr, in considerazione dei vincoli economici (elevati valori del rapporto vapore/gas secco o S/DG) ed ambientali (formazione di CrVI) di questi sistemi. Partendo da sistemi Cu/Zn/Al con un basso contenuto di rame, ottenuti da precursori tipo idrotalcite (HT), stato studiato l’effetto dell’aggiunta di piccole quantità di alcuni promotori sull’attività e stabilità dei catalizzatori ottenuti, osservando un effetto positivo sulle caratteristiche fisiche, come l’aumento dell’area superficiale e della dispersione della fase attiva. I campioni contenenti i promotori erano inoltre caratterizzati da una maggiore stabilità termica e, in alcuni casi, da un’attività catalitica superiore a quella del catalizzatore di riferimento privo di promotori. L’aggiunta di piccole quantità di alcali alla formulazione con la migliore attività portava ad un ulteriore aumento di attività e di stabilità, attribuibile ad una minore formazione di coke sulla superficie. I sistemi più interessanti potevano operare anche a bassi valori del rapporto S/DG, interessanti dal punto di vista industriale. Lo studio dell’adsorbimento di CO mediante FT-IR ha permesso di ipotizzare la possibile natura della fase attiva nei sistemi. Infine, lo studio è stato esteso a sistemi per la reazione di WGS a media temperatura (MTS), osservando anche in questo caso un positivo effetto legato all’aggiunta di promotori, con un aumento dell’attività catalitica e della stabilità con il tempo di reazione.

Catalizzatori polifunzionali per la sintesi di Metil Isobutil Chetone

In this work, we have examined the activity and selectivity of new catalysts for the single-stage production of methyl isobutyl ketone (MIBK, 4- methyl-2-pentanone) from acetone (both in liquid and gas phase), using a fixed bed reactor operated in the temperature range between 373 and 473 K. The main reaction pathways for the synthesis of MIBK from acetone are given in Fig.1. The first step is the self condensation of acetone to diacetone alcohol (DAA, 4-hydroxy-4-methyl-2-pentanone); the second step is the dehydration of DAA to mesityl oxide (MO, 4-methyl-3-penten-2-one); the final step is the selective hydrogenation of the carbon–carbon double bond of MO to form MIBK. The most commonly observed side reactions are over-condensations and unselective hydrogenations (also shown in Fig.1). Two types of catalysts were studied: i)Pd supported on MgO-SiO2 mixed oxides with ratio of Mg to Si, synthetized using Ohnishi’s method and ii)Pd supported on alumina doped with 5% or 10% of MgO. The different Mg-Si and Mg-Al catalysts were characterized by different techniques (XRD, BET, SEM, NH3-TPD and CO2-TPD) and tested under different conditions in the condensation of acetone to diacetone alcohol and its dehydration to mesityl oxide to enhance the activity. Palladium was chosen as metal component, and its hydrogenation activity was studied. A low hydrogenation activity negatively affects the acetone conversion and promotes the production of mesityl oxide. Hydrogenation conditions being too severe may favor the unwanted hydrogenation of acetone to 2-propanol and of MIBK to methyl isobutyl carbinol (MIBC, 4-methyl-2-pentanol) but this effect is less detrimental to the MIBK selectivity than an unsufficient hydrogenation activity.