Catalytic dehydration of glycerol to acrolein: catalysts and processes

The valorization of glycerol has been widely studied notably due to the oversupply of the latter from biodiesel production. Among the different upgrading reactions, dehydration to acrolein is of high interest due to the importance of acrolein as an intermediate for polymer industry (via acrylic acid) and for feed additive (synthon for DL-methionine). It is known that acrolein can be obtained by glycerol catalytic dehydration over acid catalysts. Zeolites and heteropolyacid catalysts are initially highly active, but deactivate rapidly with time on stream by coking, whilst mixed metal oxides are more stable catalytic systems but less selective and in addition they require an activation period. In this talk, the strategy we followed is described. It consisted in a parallel approach in which we developed supported heteropolyacid-based catalysts with increased stability and acrolein selectivity by using a ZrO2-grafted SBA-15 playing the role of the support for silico-tungstic acid active phase, as well as a new concept based on a two zones fluidized bed reactor (TZFBR) to tackle the unavoidable deactivation issue of the HPA catalysts. This type of reactor comprises – in one single capacity – reaction and regeneration zones. In the second part of the lecture the REALCAT platform was introduced. REALCAT (French acronym standing for ‘Advanced High-Throughput Technologies Platform for Biorefineries Catalysts Design’) is an highly integrated platform devoted to the acceleration of innovation in all the fields of industrial catalysis with an emphasis on emergent biorefinery catalytic processes. In this extremely competitive field, REALCAT consists in a versatile High-Throughput Technologies (HTT) platform devoted to innovation in heterogeneous, homogeneous or biocatalysts AND their combinations under the ultra-efficient very novel concept of hybrid catalysis.

Celdas de pilas de oxidó solido, avance en el procesado de materiales

Póster presentado en el XIV Congreso Nacional de Materiales (CNMAT) en Gijón (España), del 8 al 10 de Junio de 2016

Scalable synthetic method for IT-SOFCs compounds

Póster presentado en: 12th EUROPEAN SOFC & SOE FORUM 2016. 5–8 July 2016, KKL Lucerne/Switzerland

Estudo de sistemas vítreos para infiltração em alumina

The system in-Ceram Alumina, produced by VITA, consists in a technique of prepare of a substructure of ceramics to dental crowns. First burning is made in the alumina decanted by slip casting process under a stone die that reproduces the tooth prepared to receive a crown. In a second burning, alumina is infiltrated by vitreous system, giving to this set a high mechanic resistance. In this work, it s made a study of the composition of a new infiltrating material more used nowadays, giving to alumina desirable mechanics proprieties to its using like substructure of support to ceramic s crown used in the market today. The addition of Lanthanum oxide (frit A) and calcium oxide (frit B) was made in attempt to increase the viscosity of LZSA and to reduce fusion temperature. The frits were put over samples of alumina and took to the tubular oven to 1400ºC under vacuum for two groups (groups 1 and 2). For another two groups (groups 3 and 4) it was made a second infiltration, following the same parameters of the first. A fifth group was utilized like group of control where the samples of pure alumina were not submitted to any infiltrating process. Glasses manifested efficient both in quality and results of analysis of mechanic resistance, being perfectly compatible with oral environment in this technical requisite. The groups that made a second infiltration had he best results of fracture toughness, qualify the use in the oral cavity in this technical question. The average of results achieved for mechanic resistance to groups 1, 2, 3, 4 and 5 were respectively 98 MPa, 90 MPa, 144 MPa, 236 MPa and 23 MPa

Estudo da viabilidade do sistema LZAS para uso como selante de PaCOS

Cells the solid oxide fuel are systems capable to directly convert energy of a chemical reaction into electric energy in clean, quiet way and if its components in the solid state differentiate of excessively the techniques for having all. Its more common geometric configurations are: the tubular one and to glide. Geometry to glide beyond the usual components (anode, cathode and electrolyte) needs interconnect and sealant. E the search for materials adjusted for these components is currently the biggest challenge found for the production of the cells. The sealants need to present chemical stability in high temperatures, to provoke electric isolation, to have coefficient of compatible thermal expansion with the excessively component ones. For presenting these characteristics the glass-ceramics materials are recommended for the application. In this work the study of the partial substitution of the ZrO2 for the Al2O3 in system LZS became it aiming at the formation of system LZAS, this with the addition of natural spodumene with 10, 20 and 30% in mass. The compositions had been casting to a temperature of 1500°C and later quickly cooled with the objective to continue amorphous. Each composition was worn out for attainment of a dust with average diameter of approximately 3μm and characterized by the techniques of DRX, FRX, MEV, dilatometric analysis and particle size analysis. Later the samples had been conformed and treated thermally with temperatures in the interval between 700-1000 °C, with platform of 10 minutes and 1 hour. The analyses for the treated samples had been: dilatometric analysis, DRX, FRX, electrical conductivity and tack. The results point with respect to the viability of the use of system LZAS for use as sealant a time that had presented good results as isolating electric, they had adhered to a material with similar α of the components of a SOFC and had presented steady crystalline phases

Formulación optimizada del refractario AZS/43-20-37

Los refractarios electro-fundidos con 32-35%, en peso de ZrO2 son utilizados en hornos para fundir vidrio.

Influencia de la inserción de nano-óxidos cerámicos sobre la microestructura y propiedades de una porcelana triaxial.

La nanociencia y nanotecnología han revolucionado las investigaciones en ciencia de los materiales, permitiendo el desarrollo de nuevos productos con desempeño superior a los convencionales. Conceptos nanotecnológicos como la adición de partículas en tamaños nanométricos para incrementar las propiedades finales han sido demostrados en cerámicos, sin embargo esta alternativa prácticamente no ha sido investigada en sistemas porcelánicos, específicamente en porcelanas triaxiales con aplicaciones eléctricas. Este trabajo de investigación presenta el desarrollo de una formulación de porcelana triaxial silicosa, de grado eléctrico, con características mecánicas y dieléctricas mejoradas mediante la incorporación de nanopartículas cerámicas. Se estudió la influencia de la adición de dos tipos de óxidos cerámicos en tamaño nanométrico, α- alúmina (α-Al2O3) y circonia (ZrO2), en las propiedades y microestructura de la porcelana triaxial, al variar la concentración de las nanopartículas en la composición inicial. En la primera parte de la experimentación, se elaboraron probetas experimentales siguiendo un proceso a nivel laboratorio haciendo uso de un conformado por presión uniaxial. Posteriormente, se elaboraron pastas porcelánicas a nivel planta-prototipo mediante un proceso de conformado por extrusión plástica. Las probetas sinterizadas fueron caracterizadas mediante evaluaciones físicas tales como densidad, porosidad, absorción de humedad y contracción lineal; así mismo se llevaron a cabo análisis microestructurales y de fases a través de las técnicas de DR-X, MEB y DSC-TGA. Por último, se realizaron evaluaciones mecánicas por medio de ensayos de resistencia a la compresión y módulo de ruptura (por tres puntos), así como la evaluación de la capacidad aislante con pruebas de resistencia dieléctrica. Los resultados obtenidos demuestran que la inserción de nanopartículas de alúmina y circonia, ayudan en el reforzamiento mecánico del sistema porcelánico triaxial estudiado, además de mejorar sus características dieléctricas, lo que representa una alternativa tecnológicamente factible para mejorar el desempeño de productos de porcelana, como es el caso de aisladores eléctricos

Estudo da influência da temperatura de brasagem nas uniões zircônia/aço inox 304 utilizando metalização mecânica

Metal-Ceramic (M/C) Zirconia-stainless steel interfaces have been processed through brazing techniques due to the excellent combination of properties such as high temperature stability, high corrosion resistance and good mechanical properties. However, some M/C interfaces show some defects, like porosity and cracks results in the degradation of the interfaces, leading even to its total rupture. Most of time, those defects are associated with an improper brazing parameters selection to the M/C system. In this work, ZrO2 Y-TZP and ZrO2 Mg - PSZ were joint with the stainless steel grade 304 by brazing using a eutectic silver-copper (Ag28Cu) interlayer alloy with different thermal cycles. Ceramic surfaces were previous mechanically metallized with titanium to improve adhesion of the system. The effect of temperature on the M/C interface was studied. SEM-EDS and 3 point flexural bend test were performed to evaluate morphology, chemical composition and mechanical resistance of the M/C interfaces. Lower thermal cycle temperatures produced better results of mechanical resistance, and more regular/ homogeneous reaction layers between braze alloy and metal-ceramic surfaces. Also was proved the AgCu braze alloy activation in situ by titanium

Catalytic upgrading of carboxylic acids and esters to bio fuels and bio chemicals

The research activity was focused on the transformation of methyl propionate (MP) into methyl methacrylate (MMA), avoiding the use of formaldehyde (FAL) thanks to a one-pot strategy involving in situ methanol (MeOH) dehydrogenation over the same catalytic bed were the hydroxy-methylation/dehydration of MP with FAL occurs. The relevance of such research line is related to the availability of cheap renewable bio-glycerol from biodiesel production, from which MP can be obtained via a series of simple catalytic reactions. Moreover, the conventional MMA synthesis (Lucite process) suffers from safety issues related to the direct use of carcinogenic FAL and depends on non-renewable MP. During preliminary studies, ketonization of carboxylic acids and esters has been recognized as a detrimental reaction which hinders the selective synthesis of MMA at low temperature, together with H-transfer hydrogenation with FAL or MeOH as the H-donor at higher temperatures. Therefore, ketonization of propionic acid (PA) and MP was investigated over several catalysts (metal oxides and metal phosphates), to obtain a better understanding of the structure-activity relationship governing the reaction and to design a catalyst for MMA synthesis capable to promote the desired reaction while minimizing ketonization and H-transfer. However, ketonization possesses scientific and industrial value itself and represents a strategy for the upgrade of bio oils from fast pyrolysis of lignocellulosic materials, a robust and versatile technology capable to transform the most abundant biomass into liquid biofuels. The catalysts screening showed that ZrO2 and La2O3 are the best catalysts, while MgO possesses low ketonization activity, but still, H-transfer parasitic hydrogenation of MMA reduces its yield over all catalysts. Such study resulted in the design of Mg/Ga mixed oxides that showed enhanced dehydrogenating activity towards MeOH at low temperatures. It was found that the introduction of Ga not only minimize ketonization, but also modulates catalyst basicity reducing H-transfer hydrogenations.

Upgrading Bio-Platform Molecules in the Gas-Phase: From Levulinic Acid to Bio-Chemicals

Levulinic acid (LA) is a polyfunctional molecule obtained from biomass. Because of its structure, the United States Department of energy classified LA as one of the top 12 building block chemicals. Typically, it is valorized through chemical reduction to γ-valerolactone (GVL). It is usually done with H2 in batch systems with high H2 pressures and noble metal catalysts, making it expensive and less applicable. Therefore, alternative approaches such as catalytic transfer hydrogenation (CTH) through the Meerwein–Ponndorf–Verley (MPV) reaction over heterogeneous catalysts have been studied. This uses organic molecules (alcohols) which act as a hydride transfer agent (H-donor), to reduce molecules containing carbonyl groups. Given the stability of the intermediate, reports have shown the batch liquid-phase CTH of levulinate esters with secondary alcohols, and remarkable results (GVL yield) have been obtained over ZrO2, given the need of a Lewis acid (LASites) and base pair for CTH. However, there were no reports of the continuous gas-phase CTH of levulinate esters. Therefore, high surface area ZrO2 was tested for gas-phase CTH of methyl levulinate (ML) using ethanol, methanol and isopropanol as H-donors. Under optimized conditions with ethanol (250 ℃), the reaction is selective towards GVL (yield 70%). However, heavy carbonaceous materials over the catalyst surface progressively blocked LASites changing the chemoselectivity. The in situ regeneration of the catalyst permitted a partial recovery of the LASites and an almost total recovery of the initial catalytic behavior, proving the deactivation reversible. Tests with methanol were not promising (ML conversion 35%, GVL yield 4%). As expected, using isopropanol provided complete conversion and a GVL yield of 80%. The reaction was also tested using bioethanol derived from agricultural waste. In addition, a preliminary study was performed for the hydrogenolysis of polyols to produce bioethanol, were Pd-Fe catalyst promoted the ethanol selective (37%) hydrogenolysis of glycerol.

Investigation of gold-based catalysts for liquid phase oxidation of glucose to glucaric acid

Glucaric acid (GA) is one of the building block chemicals derived from sugar biomass with higher added value. Nowadays, GA is produced by oxidation of glucose (Glu) with either stoichiometric oxidants (HNO3), or by means of electrochemical or biochemical synthesis. However, these processes show drawbacks from either the environmental or economic viewpoint. For this reason, gold nanoparticles (Au NPs) supported on activated carbon (AC) have been studied as catalysts for the oxidation of Glu, using O2 as oxidant in the presence of a base. Using sol immobilization technique, Au NPs have been supported on AC following different experimental procedures. UV-Vis spectroscopy, XRD, TEM and TG analysis were utilized in the characterization of the catalysts. The operational conditions were optimized obtaining 24% of yield of GA, 37% to GO and 27% to byproducts in 1 h, 1000 rpm, 10 bar of O2 and Glu:Au:NaOH molar ratio of 1000:1:3000. Under such conditions, catalysts show relatively high Glu conversion (≥82%) with different GA yields. GO+GA yield is around 58-61%. Therefore, the oxidation reaction was performed at 15 min where Au/AC PVA0 reached the highest yield of GA (16%) and Au/AC PVA2.4 gave the lowest (8%). It is evident that the presence of PVA influences to a higher degree the reaction rate than the Au NPs size. Hence, the effect of different heat treatments where applied for the removal of PVA: washing with water at 60℃ or heat treatment (120-250℃) with Air/H2. Washing treatment and heat treatment at 120℃ with Air/H2 may have resulted in the mildest treatments for the removal of PVA. Finally, two different supports have been used in order to study the effect of metal-support interaction in the immobilization of Au NPs: ZrO2 and AC. Au/AC catalyst demonstrated a higher conversion of GO to GA at short reaction times (15.1% yield GA) compared to Au/ZrO2 (2.4% yield GA).

Dimetiladipato: una via di sintesi alternativa da chetoni e carbonati organici

In questo progetto è stata studiata la reazione tra dimetil carbonato e ciclopentanone come possibile alternativa sostenibile per la produzione di dimetiladipato, composto di notevole interesse industriale. Lo studio si è basato su reazioni in fase liquida con catalizzatori eterogenei (commerciali e di sintesi), sia in condizioni batch che soprattutto continue, mai riportate in letteratura, per le quali un apposito reattore a letto fisso è stato progettato e messo a punto. I parametri indagati sono il tempo di contatto, il rapporto di alimentazione dei due reagenti ed il catalizzatore utilizzato, osservando anche l’andamento di grandezze quali rese e conversioni nel tempo. Sono stati inoltre effettuate delle prove per approfondire il meccanismo e lo schema di reazione. Per il processo continuo è risultato come un maggior tempo di contatto porti a maggiori conversioni e rese, mentre per quanto riguarda il rapporto molare di alimentazione, il rapporto ottimale tra dimetilcarbonato e ciclopentanone sembra essere 15:1, sia come resa di dimetil adipato che come compromesso tra reazioni parassite dovute all’eccesso di dimetil carbonato e reazioni di autocondensazione del ciclopentanone. Tra i catalizzatori testati, i più efficienti nella conversione dei reagenti e nella formazione del prodotto sono risultati essere quelli con caratteristiche basiche come MgO e CeO2, rispetto ad un catalizzatore meno basico come ZrO2.

Studio della reazione di hydrogen-transfer di metil levulinato con etanolo in fase vapore: effetto del palladio supportato su catalizzatori contenenti zirconio

La valorizzazione di biomasse lignocellulosiche rappresenta la strada che la chimica può percorrere per svincolarsi dalle fonti fossili e virare verso un futuro incentrato sulla sostenibilità ambientale. In quest’ottica, l’acido levulinico (AL) e i suoi esteri, detti alchil levulinati, ottenibili dalla valorizzazione di biomasse di scarto, rappresentano una classe di composti di grande interesse industriale. Infatti, dalla loro riduzione è possibile ottenere g-valerolattone (GVL), un’importante molecola piattaforma per l’industria chimica, o alchil valerati, composti interessanti per diverse branche dell’industria chimica e per la formulazione di bio-carburanti. Già da tempo è nota la possibilità di effettuare la riduzione di AL in fase liquida in presenza di alcoli come H-Donor secondo un meccanismo detto Catalytic Transfer Hydrogenation che può essere promosso da ossido di zirconio (ZrO2). Recentemente, è stato ottimizzato un processo che impiega i reagenti appena citati in un reattore continuo operante in fase gassosa con ZrO2 come catalizzatore. In questo lavoro, si è dopato tale sistema catalitico con palladio, al fine di promuovere le reazioni di riduzione consecutiva al GVL e si sono ottimizzati i parametri operativi come tempo di contatto, temperatura e rapporto tra substrato e H-Donor.

Studio di ossidi misti Ti/Zr/O per la valorizzazione catalitica di furfurale a GVL in un reattore continuo in fase liquida

Il cambiamento climatico è una delle sfide più ardue che il nostro pianeta abbia mai dovuto affrontare. Negli ultimi anni si sta rendendo sempre più evidente la necessità di un profondo cambiamento ideologico e sociale in ogni campo. La Green Chemistry mira a capeggiare questo cambiamento proponendo dei principi guida in modo da indirizzare la chimica verso tale traguardo. Possibili strumenti attuativi di questa visione sono senza alcun dubbio le bioraffinerie. Raffinerie appunto, nate però per processare materie prime provenienti da fonti rinnovabili, le biomasse. Esistono diversi tipi di biomasse, dalle quali possono essere ricavate differenti molecole piattaforma. La biomassa lignocellulosica, per esempio, viene sfruttata per ottenere perlopiù composti furanici. Tra questi di particolare interesse è la furfurale(FUR), un’aldeide particolarmente reattiva dalla quale possono essere ottenute numerose sostanze chimiche ad alto valore aggiunto. Tra queste si trova il γ-valerolattone(GVL), estere ciclico a cinque atomi di carbonio, promettente prodotto preliminare nella sintesi di combustibili a base biologica e prodotti chimici di base. Il processo che porta dalla FUR al GVL comprende diversi step di reazione, alcuni catalizzati da acidità di Lewis, altri da acidità di Brønsted. Gli step di riduzione possono essere eseguiti mediante una reazione di Catalytic Transfer Hydrogenation (CTH) utilizzando isopropanolo piuttosto che H2 gassoso. La scelta del solvente/riducente assieme all’utilizzo di un sistema catalitico eterogeneo permettono la realizzazione della reazione con un basso impatto ambientale. Per quanto riguarda la scelta del sistema catalitico, particolarmente interessante è la combinazione TiO2-ZrO2. Lo scopo di questa tesi è stato quello di sintetizzare e valutare le performance di sistemi catalitici a base di ossidi misti Ti/Zr/O con diverse composizioni nella conversione della FUR a GVL in un reattore in fase liquida.

Studio della sintesi del 2-acetil furano mediante chetonizzazione in fase vapore

La reazione tra due acidi carbossilici o esteri a dare un chetone, H2O e CO2 (chetonizzazione) è molto studiata per l’upgrading del bio-olio grezzo, perché permette di ridurne l’acidità ed il tenore di ossigeno aumentandone il potere calorifico. Tuttavia, con opportuni accorgimenti questa reazione potrebbe essere impiegata anche per la sintesi selettiva di chetoni asimmetrici ad alto valore aggiunto; un esempio è l’acetil-furano (AF), che trova applicazione come aroma nell’industria alimentare e come intermedio per la sintesi dell’antibiotico Cefuroxima. In questo lavoro di tesi la sintesi di AF mediante la chetonizzazione incrociata tra 2-metil furoato (MF) ed etil acetato (EA) oppure acido acetico (AA), è stata investigata in fase gassosa con catalizzatori eterogenei (ZrO2, CeO2 e un ossido misto Ce/Zr/O), come alternativa più sostenibile al processo di sintesi industriale di AF basato sull’acilazione di Friedel-Crafts del furano con anidride acetica in fase liquida in reattori batch. Uno screening iniziale dei tre catalizzatori (350 °C, τ = 1 s, stechiometrica MF/AA = 1 in alimentazione) ha dimostrato che ZrO2 è di gran lunga più attivo e selettivo degli altri materiali, e che la chetonizzazione incrociata tra MF e AA è di gran lunga più selettiva di quella tra MF ed EA. Tuttavia, in queste condizioni la omochetonizzazione di AA (reagente limitante) compete con la chetonizzazione incrociata riducendo la massima conversione di MF ottenibile; pertanto, il rapporto AA/MF è stato aumentato fino a 4 ed in queste condizioni è stato possibile ottenere una conversione di MF quantitativa e una resa in AF pari al 70 %. Infine, la versatilità di questa via sintetica è stata ampliata sintetizzando chetoni furanici con catene alifatiche più lunghe propanoil furano (PF, resa = 82 %) e butanoil furano (BF, resa = 69 %) mediante la chetonizzazione incrociata di MF con acido propionico (AP) ed acido butirrico (AB).