Made available in DSpace on 2017-07-24T19:37:52Z (GMT). No. of bitstreams: 1 Ariana Rodrigues.pdf: 4102019 bytes, checksum: 823cb458ebe2eea53b3ba0d11aed9880 (MD5) Previous issue date: 2012-03-06 / Fundação Araucária de Apoio ao Desenvolvimento Científico e Tecnológico do Paraná / The increasing pathogenic bacteria resistance to antibiotics has led to the development of new alternatives to replace them. The Photodynamic Antimicrobial Chemotherapy (PACT) is one of the alternatives recently researched. Several associations between photosensitizer (PS) and light sources are used to inactivate different micro-organisms. The porphyrin derivatives have interesting features and are amongst the most investigated compounds in PACT, showing promising results. The light-emitting diode (LED) source presents advantages, since this device has been shown efficient against bacteria and is economically feasible. The present study investigated the photodynamic activity of different porphyrin derivatives/LED systems for application in PACT. The following porphyrin derivatives were used: 5,10,15,20-tetrakis(2,6-difluor-5-sulfonatophenyl) sodium porphyrinate, Na4[H2(TDFSPP)], 5,10,15,20-tetrakis(2,6-difluor-5-sulfonatophenyl) zinc (II) sodium porphyrinate, Na4[Zn(TDFSPP)]) and 5,10,15,20-tetrakis(4-sulfonatophenyl) manganese (III) sodium porphyrinate, Na4[Mn(TSPP)]. LED systems were used in different emission bands: orange, red, green and blue. The photodynamic activity of PS/LED systems were analyzed through the photobleaching test, photoxidation of bovine serum albumin (BSA) protein, uric acid and microbiological assay with ATCC and hospital Staphylococcus aureus strains. The results showed no significant photobleaching of porphyrin derivatives using LED as a light source. The PS/LED systems led to oxidation of the BSA protein and uric acid, except for the derivative Na4[Mn(TSPP)]. The photoxidation constant rate for Na4[H2(TDFSPP)]/green and blue LED, Na4[Zn(TDFSPP)]/green and blue LED systems, were close to the constant rate for drugs with application in photodynamic therapy (PDT). The uric acid test result indicated that compounds are capable of generating singlet oxygen. The Na4[H2(TDFSPP)]/blue LED system had a higher photodynamic activity against ATCC and hospital S. aureus strains. The results demonstrated that the systems under study present potential to be used in PDT and PACT. / A crescente resistência de bactérias patogênicas a antibióticos levou ao desenvolvimento de novas alternativas que possam substituí-los. Uma das alternativas investigadas atualmente é a quimioterapia fotodinâmica antimicrobiana (PACT). Várias associações entre fotossensibilizadores (FS) e fontes de luz são utilizadas para inativar diferentes micro-organismos, comprovando a eficiência dessa terapia. Os derivados porfirínicos apresentam características interessantes para aplicação em PACT e estão entre os compostos mais investigados, apresentando resultados promissores. O uso de LED como fonte de luz apresenta vantagens, uma vez que esse dispositivo tem mostrado bons resultados na eliminação de bactérias e é economicamente mais viável. Assim, no presente estudo, investigou-se a atividade fotodinâmica de diferentes sistemas derivados porfirínicos/LEDs para possível aplicação em PACT. Para isso, utilizou-se os seguintes derivados porfirínicos: 5,10,15,20-tetrakis (2,6-difluoro-5-sulfonatofenil) porfirinato de sódio, Na4[H2(TDFSPP)], 5,10,15,20-tetrakis (2,6-difluoro-5-sulfonatofenil) zinco (II) porfirinato de sódio, Na4[Zn(TDFSPP)], e 5,10,15,20-tetrakis (4-sulfonatofenil) manganês (III) porfirinato de sódio, Na4[Mn(TSPP)]. A irradiação dos compostos foi feita utilizando-se sistemas de LED com diferentes faixas de emissão: alaranjado, vermelho, verde e azul. A atividade fotodinâmica dos sistemas FS/LED foi avaliada por meio dos testes de fotobranqueamento, foto-oxidação da proteína BSA, ácido úrico e de ensaio microbiológico, utilizando-se a bactéria Staphylococcus aureus de origem ATCC e hospitalar. Os resultados mostraram que os derivados porfirínicos não sofreram fotobranqueamento quando associados aos diferentes LEDs. Os sistemas FS/LED levaram à oxidação da proteína BSA e à degradação da molécula de ácido úrico, exceto para o derivado Na4[Mn(TSPP)]. As constantes de foto-oxidação obtidas para os sistemas Na4[H2(TDFSPP)]/LED verde e azul; Na4[Zn(TDFSPP)]/LED verde e azul, ficaram próximas aos valores obtidos para fármacos com aplicação em Terapia Fotodinâmica (TFD). Os resultados do teste do ácido úrico para esses mesmos sistemas indicaram que eles são capazes de gerar oxigênio singlete. O sistema Na4[H2(TDFSPP)]/LED azul apresentou maior atividade fotodinâmica sobre as cepas de S. aureus ATCC e hospitalar. Assim, os resultados demonstram que os sistemas investigados apresentam potencial para aplicação em TFD e PACT.

Passiflora alata Curtis e P. nitida Kunth, espécies brasileiras, foram submetidas ao estudo farmacognóstico comparativo. P. alata tem sido utilizada há tempos na medicina tradicional e em preparações farmacêuticas. No estudo farmacobotânico, as folhas das duas espécies apresentaram semelhança na forma, no tamanho e na ausência de indumento. Diferem quanto ao número de glândulas peciolares. P. alata apresenta geralmente dois pares de glândulas e P. nitida, um par. Anatomicamente, as duas espécies mostraram características comuns ao gênero Passiflora: mesofilo dorsiventral; drusas no mesofilo, na nervura mediana, na região cortical, medular e floemática do caule; feixes vasculares colaterais. Embora as duas espécies apresentem nervura mediana biconvexa, a de P. alata evidencia as carenas pronunciadamente salientes, principalmente na face abaxial. Outro aspecto diferencial observa-se na forma do caule: em P. alata é quadrangular e, em P. nitida, arredondada. A seqüência de tecidos assemelha-se, com exceção do maior desenvolvimento de colênquima nas arestas de P. alata. A triagem fitoquímica evidenciou a presença de flavonóides nas duas espécies e a ausência de alcalóides em ambas, tanto na droga vegetal quanto nos extratos. Formação de espuma persistente foi observada com a droga vegetal preparada com P. alata. A hemólise foi observada com a droga e o extrato desta espécie. Os flavonóides foram quantificados como 0,42% ± 0,01 em P. alata e 0,10% ± 0,01 em P. nitida. No ensaio da atividade antioxidante, a EC50 de P. alata foi de 1061,2 ± 8,5 µg/mL e a de nitida 128,0 ± 0,9 µg/mL, no ensaio do DPPH, e de 1076 ± 85 µµmol de Trolox/g de extrato e de 1985 ± 104 µmol de Trolox/g de extrato no ensaio de ORAC, respectivamente. No ensaio de atividade antiúlcera aguda P. alata exibiu, na área total de lesão (ATL), proteção contra as lesões gástricas de 100%, P. nitida de 84% e lansoprazol, o controle positivo, de 76%. Quanto à área relativa de lesão (ARL), alata exibiu proteção contra as lesões de 99,45%; P. nitida, de 82,27% lansoprazol, de 81,44%, no ensaio de lesão gástrica induzida por etanol/HCI com 300 mmol/L de HCI e extratos na dose de 400 mg/kg. As doses de 100,200 e 400 mg/kg dos extratos foram testadas nas mesmas condições com 150 mmol/L de HCI. P. alata apresentou, na ATL, 100% de proteção contra as lesões gástricas nas três concentrações e lansoprazol, de 75%. Na ARL, P. alata exibiu 100% de proteção lansoprazol, de 76,92%. P. nitida apresentou, na ATL, proteção contra as lesões gástricas de 25%, 74% e 94% nas três concentrações, respectivamente e, lansoprazol, de 80%. Na ARL, P. nitida exibiu 27,40%, 74,00% e 91,78% de proteção, respectivamente e lansoprazol, de 78,08%. Baseando-se neste estudo possível distinguir as duas espécies através de características morfoanatômicas das folhas e dos caules e, através do perfil cromatográfico. Ambas as espécies apresentaram atividade antiúlcera promissora. / Passiflora alata Curtis and P. nitida Kunth, Brazilian species, were selected for the comparative pharmacognostic study. P. alata has been used for a long time folk medicine and pharmaceutical preparations. In the pharmacobotanic study, leaves from both species showed similarities in shape, size and in the absence indumenta. They differ by the number of petiolar glands. P. alata presents generally two pairs of glands and P. nitida, one pair. Anatomically, both species showed common characteristics to the Passiflora genera: dorsiventral mesophyll; druses the mesophyll, midrib, cortex, medulla and phloem; collateral vascular bundles. Both species\' midrib presented a biconvex shape, but P. alata\'s was prominently shaped, notably in the abaxial surface. Another differential aspect was observed the stem shape: P. alata was quadrangular and P. nitida was rounded. The tissues sequence presented similarity, with exception to larger collenchyma development in P. alata\'s edges. The phytochemical screening showed presence of flavonoids and absence of alkaloids in both species, in the crude drug and extracts. Formation persistent foam was observed with the crude drug of P. alata. Hemolisis was observed with the crude drug and extract of this species. Flavonoids were quantified as 0.42% ± 0.01 in P. alata and 0.10% ± 0.01 in P. nitida. In the antioxidant activity assay, the EC50 of P. alata was 1061.2 ± 8.5 µg/mL and of P. nitida , 128.0 ± 0.9 µg/mL, in the DPPH assay, and 1076 ± 85 µmol Trolox/g extract and 1985 ± 104 µmol Trolox/g extract in the ORAC assay, respectively. In the antiulcer activity assay P. alata showed, in total lesion area (TLA), protection against gastric lesions 100%, P. nitida 84% and lansoprazole, the positive control, 76%. In relative lesion area (RLA), P. alata showed protection against lesions of 99.45%, P. nitida82.27% and lansoprazole 81.44%, in the HCl/ethanol-induced gastric lesion assay, with HCI 300 mmol/L and extracts at doses of 400 mg/kg. Doses of 100, 200 e 400 mg/kg extracts were tested in the same conditions with HCl 150 mmol/L. P. alata showed, TLA, protection against gastric lesions of 100% in the three concentrations and lansoprazole 75%. In RLA, P. alata showed 100% of protection and lansoprazole 76.92%. P. nitida showed, in TLA, protection against gastric lesions of 25%,74% and 94% in the three concentrations, respectively and lansoprazole 80%. In RLA, nitida showed 27.40%, 74.00% and 91.78% of protection, respectively and lansoprazole 78.08%. Based upon this study it is possible to distinguish both species by leaf and stem morphoanatomic characters and by chromatographic profile. Both species presented promising antiulcer activity.

Τα τελευταία χρόνια διεξάγεται µια έντονη ερευνητική προσπάθεια µε στόχο την ανά- πτυξη αποτελεσµατικών καταλυτών για την εκλεκτική οξείδωση του CO παρουσία περίσσειας H2. Το ενδιαφέρον για αυτήν την διεργασία εντοπίζεται στην εφαρµογή της για τον καθαρισµό από το περιεχόµενο CO, πλούσιων σε Η2 αέριων µιγµάτων τα οποία χρησιµοποιούνται ως καύσιµο σε κυψελίδες καυσίµου τύπου PEM. Στην παρούσα διδακτορική διατριβή εξετάστηκαν οι καταλυτικές ιδιότητες τριών συ- στηµάτων: Au/α-Fe2O3, Pt/γ-Al2O3 και CuO-CeO2, για την εν λόγω διεργασία. Η µελέτη εντοπί- στηκε, κατά κύριο λόγο, στους καταλύτες CuO-CeO2, οι οποίοι δε περιέχουν πολύτιµο µέταλλο. Στους εν λόγω καταλύτες, παράµετροι της µελέτης ήταν η µέθοδος παρασκευής, η φόρτιση των καταλυτών σε ενεργό φάση και η θερµοκρασία ενεργοποίησής τους. Σε κάθε περίπτωση εξετά- στηκε η ενεργότητα, εκλεκτικότητα και σταθερότητα των καταλυτών, καθώς και η ανθεκτικότητά τους στην παρουσία CO2 και Η2Ο στην τροφοδοσία. Για το χαρακτηρισµό των καταλυτών χρησι- µοποιήθηκαν: α) φασµατοσκοπία ατοµικής απορρόφησης, β) ρόφηση Ν2, γ) περίθλαση ακτίνων Χ, δ) ηλεκτρονική µικροσκοπία, ε) θερµοσταθµική ανάλυση, στ) φασµατοσκοπία φωτοηλεκτρο- νίων ακτίνων Χ και ζ) δυναµικά πειράµατα µε προγραµµατισµό θερµοκρασίας. Επιπλέον, κινητι- κές µελέτες πραγµατοποιήθηκαν σε επιλεγµένα δείγµατα CuO-CeO2. Οι καταλύτες CuO-CeO2 βρέθηκαν να έχουν σχεδόν ιδανική εκλεκτικότητα σε θερµο- κρασίες µικρότερες από 130οC. Ενεργοί και εξαιρετικά εκλεκτικοί καταλύτες CuO-CeO2 παρα- σκευάστηκαν µε διαφορετικές τεχνικές, και εµφάνισαν µεγάλη σταθερότητα µε το χρόνο αντί- δρασης και ικανοποιητική ανθεκτικότητα στην παρουσία Η2Ο και CO2. H σειρά ενεργότητας των καταλυτών, µε βάση τη µέθοδο παρασκευής τους, ήταν: (sol-gel) > (καύση) > (κιτρικά-υδρο- θερµική) > (συγκαταβύθιση) > (εµποτισµός). Ο βέλτιστος καταλύτης CuO-CeO2, ο οποίος παρα- σκευάστηκε µε τεχνική sol-gel, έδωσε ~99% µετατροπή του CO, µε ~87% εκλεκτικότητα, στους 175οC, σε συνθήκες εκλεκτικής οξείδωσης του CO (παρουσία CO2 και Η2Ο). Γενικά, η ένταση της αλληλεπίδρασης CuO-CeO2 βρέθηκε να εξαρτάται από τη θερµοκρασία ενεργοποίησης των καταλυτών. Σε χαµηλές θερµοκρασίες ενεργοποίησης η προω- θητική δράση της δηµήτριας εντοπίζεται στην αύξηση της ειδικής επιφάνειας των καταλυτών και στη δηµιουργία νέων ενεργών κέντρων, πιθανά στη διεπιφάνεια των δύο φάσεων. Απ’ την άλλη πλευρά, η ένταση της αλληλεπίδρασης ενισχύεται σε υψηλές θερµοκρασίες ενεργοποίησης, µε συνέπεια την αύξηση της εγγενούς ενεργότητας των ενεργών κέντρων. Στα περισσότερα καταλυ- τικά δείγµατα το οξείδιο του χαλκού βρισκόταν πολύ καλά διασπαρµένο στην επιφάνεια της δηµήτριας. Επιπλέον, η παρουσία και σταθεροποίηση ιόντων Cu1+ στους καταλύτες που παρα- σκευάστηκαν µε καύση, συγκαταβύθιση και sol-gel, και ενεργοποιήθηκαν σε υψηλές θερµοκρασίες, αποτελεί ένδειξη ισχυρής αλληλεπίδρασης ανάµεσα στο οξείδιο του χαλκού και στη δηµήτρια, µε αποτέλεσµα την εισχώρηση ιόντων Cu1+ στα πρώτα επιφανειακά στρώµατα της δηµήτριας. Κινητικά µοντέλα βασιζόµενα σε έναν οξειδοαναγωγικό µηχανισµό, µπορούν να περι- γράψουν τις αντιδράσεις οξείδωσης του CO και του Η2, τόσο στο καθαρό CuO, όσο και στους κα- ταλύτες CuO-CeO2. H αλληλεπίδραση ανάµεσα στο CuO και τη δηµήτρια έχει ως αποτέλεσµα την ευκολότερη αναγωγή των οξειδωµένων ενεργών κέντρων, σε σχέση µε το καθαρό CuO. Η ευχερέστερη αναγωγή αυτών των κέντρων από το CO, σε σχέση µε το Η2, είναι η αιτία της υψη- λής εκλεκτικότητας των καταλυτών CuO-CeO2. Η ενεργότητα των καταλυτών Au βρέθηκε να εξαρτάται από την επιφανειακή συγκέ- ντρωση του Au, γεγονός που καταδεικνύει τη σηµασία ύπαρξης καλώς διασπαρµένων νανοσωµα- τιδίων Au (µεγέθους ~3 nm), για την επίτευξη υψηλής καταλυτικής ενεργότητας. Την καλύτερη συµπεριφορά παρουσίασε το δείγµα µε 2.94 wt% Au, για το οποίο προσδιορίστηκε η µεγαλύτερη τιµή επιφανειακής συγκέντρωσης Au. Με αυτό το δείγµα επιτεύχθηκε µετατροπή του CO µεγαλύτερη από 99% (µε 52% εκλεκτικότητα), στους 100οC, σε ρεαλιστικές συνθήκες εκλεκτικής oξείδωσης του CO (παρουσία CO2 και Η2Ο). Η σύγκριση της καταλυτικής συµπεριφοράς καταλυτών Au/α-Fe2O3, Pt/γ-Al2O3 και CuOCeO2 έδειξε ότι σε σχετικά χαµηλές θερµοκρασίες λειτουργίας (<80oC) ο καταλύτης Au/α-Fe2O3 εµφανίζει τη βέλτιστη συµπεριφορά για την εκλεκτική οξείδωση του CO. Σε υψηλότερες θερµοκρασίες, καλύτερα αποτελέσµατα έδωσαν οι καταλύτες CuO-CeO2, ο οποίοι ήταν αντί- στοιχα ενεργοί, και σε κάθε περίπτωση πιο εκλεκτικοί από τον καταλύτη Pt/γ-Al2O3. Η παρουσία H2O και CO2 στο αντιδρόν µίγµα προκάλεσε σηµαντική µείωση στην ενεργότητα των καταλυτών Au/α-Fe2O3 και CuO-CeO2, αλλά δεν επηρέασε, τουλάχιστον αρνητικά, την ενεργότητα του Pt/γ- Al2O3. Οι καταλύτες CuO-CeO2 και Pt/γ-Al2O3 παρουσίασαν σταθερή καταλυτική συµπεριφορά για το χρονικό διάστηµα που εξετάστηκαν σε ρεαλιστικές συνθήκες αντίδρασης (7-8 ηµέρες), σε αντίθεση µε τον καταλύτη Au/α-Fe2O3. / The development of efficient catalysts for the selective oxidation of CO in the presence of excess H2 is the goal of intense research effort during the last years, due to the application of this process in removal of CO from H2-rich gas mixtures, which are used as fuel in PEM fuel cells. The catalytic properties of three systems: Au/α-Fe2O3, Pt/γ-Al2O3 και CuO-CeO2, were investigated for the title process of the present thesis. The study was focused mainly on the CuOCeO2 catalysts, which do not contain a noble metal. Parameters of the study were: the preparation method, the metal loading and the activation temperature. The activity, selectivity and stability of catalysts, and also their tolerance in the presence of CO2 and Η2Ο in the feed, were examined. The catalysts were characterized by: a) atomic adsorption spectroscopy, b) N2 adsorption, c) X-ray diffraction, d) electron microscopy, e) thermogravimetry, f) X-ray photoelectron spectroscopy and g) temperature-programmed dynamic tests. Additionally, kinetic studies were performed with selected CuO-CeO2 samples. CuO-CeO2 catalysts were found to be almost ideally selective in temperatures lower than 130οC. Active and selective CuO-CeO2 catalysts were prepared with various techniques, and showed high stability with time on stream and good resistance towards Η2Ο and CO2. Based on the preparation method, the activity ranking of the catalysts was: (sol-gel) > (combustion) > (citrate- hydrothermal) > (coprecipitation) > (impregnation). The best CuO-CeO2 catalyst, prepared with a sol-gel technique, showed ~99% CO conversion, with ~87% selctivity, at 175οC (in the presence of CO2 and Η2Ο). The interaction intensity between copper oxide and ceria was generally found to depend on the activation temperature of the catalysts. At low activation temperatures, the promoting effect of ceria causes enhancement of surface area and creation of additional active sites, probably at the interface of the two phases. On the other hand, the interaction is enhanced at high activation temperatures, resulting in increase of intrinsic activity of active sites. In most of the catalytic samples, copper oxide was well dispersed on the ceria surface. In addition, the presence and stabilization of Cu1+ ions in the catalysts that were prepared with combustion, coprecipitation and sol-gel, and were activated at high temperatures, indicates the presence of strong interaction between copper v oxide and ceria, resulting to the penetration of Cu1+ ions into the first surface layers of ceria. Kinetic models, based on the redox mechanism, can describe the oxidation reactions of CO and Η2, for both pure CuO and CuO-CeO2 catalysts. The interaction between CuO and ceria results in easier reduction of oxidized active sites, compared to pure CuO. The easier reduction of these sites from CO, compared to Η2, is the cause of high selectivity of CuO-CeO2 catalysts. The activity of gold catalysts was found to depend on the surface concentration of Au, implying that well-dipersed gold nanoparticles (size of ~3 nm) are essential for the achievement of high catalytic activity. The best performance was found for the sample with 2.94 wt% Au, which had the highest value of surface concentration of gold. In this case, CO conversion higher than 99% (with 52% selectivity) was obtained at 100οC, under realistic conditions of selective CO oxidation (in the presence of CO2 and Η2Ο). Comparison of the catalytic performance of Au/α-Fe2O3, Pt/γ-Al2O3 and CuO-CeO2 catalysts, showed that the Au/α-Fe2O3 catalyst is superior for the selective oxidation of CO at relatively low operation temperatures (<80oC). At higher temperatures, best results were obtained with the CuO-CeO2 catalysts, which proved to be comparably active, and in any case more selective than the Pt/γ-Al2O3 catalyst. The presence of H2O and CO2 in the reactant mixture caused a significant decrease in the catalytic activity of Au/α-Fe2O3 and CuO-CeO2 catalysts, but didn’t affect, at least negatively, the activity of Pt/γ-Al2O3. With the exception of Au/α-Fe2O3, the CuO-CeO2 and Pt/γ-Al2O3 catalysts exhibited a stable catalytic performance for at least 7-8 days under realistic reaction conditions.

?rea de concentra??o: Produtos e coprodutos. / Submitted by Jos? Henrique Henrique (jose.neves@ufvjm.edu.br) on 2017-10-03T14:42:21Z No. of bitstreams: 2 license_rdf: 0 bytes, checksum: d41d8cd98f00b204e9800998ecf8427e (MD5) wayler_silva_santos.pdf: 9149649 bytes, checksum: 7d300a18f29fb2d1bfa9a3ab5c806ad3 (MD5) / Approved for entry into archive by Rodrigo Martins Cruz (rodrigo.cruz@ufvjm.edu.br) on 2017-10-09T14:02:32Z (GMT) No. of bitstreams: 2 license_rdf: 0 bytes, checksum: d41d8cd98f00b204e9800998ecf8427e (MD5) wayler_silva_santos.pdf: 9149649 bytes, checksum: 7d300a18f29fb2d1bfa9a3ab5c806ad3 (MD5) / Made available in DSpace on 2017-10-09T14:02:32Z (GMT). No. of bitstreams: 2 license_rdf: 0 bytes, checksum: d41d8cd98f00b204e9800998ecf8427e (MD5) wayler_silva_santos.pdf: 9149649 bytes, checksum: 7d300a18f29fb2d1bfa9a3ab5c806ad3 (MD5) Previous issue date: 2017 / Universidade Federal dos Vales do Jequitinhonha e Mucuri (UFVJM) / Funda??o de Amparo ? Pesquisa do Estado de Minas Gerais (FAPEMIG) / A convers?o da energia da radia??o solar em H2(g), combust?vel verde, usando-se c?lulas fotoeletroqu?micas (PEC) ? uma estrat?gia atraente para armazenar energia e minimizar o uso extensivo de combust?veis f?sseis. Neste trabalho, foram fabricados fotoeletrodos por deposi??o spray pyrolysis de um comp?sito de BiVO4/Bi4V2O11 puro ou dopado com W, depositado diretamente sobre um substrato condutor FTO (sigla para fluorine-doped tin oxide) ou sobre uma camada de SnO2 previamente depositada sobre o substrato FTO. Inicialmente, os materiais foram testados na clivagem molecular da ?gua. Verificou?se a forma??o de uma camada de invers?o de buracos induzida pela perovskita ferroel?trica Bi4V2O11 na interface com BiVO4 de tipo?n criando uma jun??o p?n virtual. A fotovoltagem de sa?da elevada da jun??o, em rela??o a uma heterojun??o p?n convencional, que pode ser ainda aumentada alterando-se a polariza??o e dopando-se o material ferroel?trico com tungst?nio, acarreta diminui??o da recombina??o dos pares el?tron?buracos fotogerados na superf?cie e aumenta a fotocorrente em at? 180%. O comportamento de semicondutores de tipo?p e n quando iluminados sugere o uso potencial da heterojun??o como fotoanodo e fotocatodo em uma c?lula PEC (ou photoelectrochemical cell) com dois fotoeletrodos. Este conceito foi comprovado pela conex?o do fotoanodo BiVO4/Bi4V2O11 dopado com 1% em massa de tungst?nio com o fotocatodo BiVO4/Bi4V2O11 n?o dopado. O sistema formado pelo acoplamento fotoanodo-fotocatodo produziu uma fotovoltagem de 1,54 V, e 0,36% de efici?ncia STH (solar-to-hydrogen efficiency). Um fotoeletrodo BiVO4/Bi4V2O11 dopado com 2% em massa de W foi otimizado. Evidenciou-se a forma??o da camada de invers?o de buracos na interface semicondutora no filme mais denso. Este ?ltimo foi testado em diferentes solu??es, obtendo-se elevadas densidades de corrente em NaAc 0,5 mol L-1, ? medida que se adicionou glicerina e vinha?a. Obteve?se a menor resist?ncia na transfer?ncia de cargas na interface eletrodo/eletr?lito 1,16 k? sob ilumina??o, utilizando a solu??o NaAc 0,5 mol L-1 contendo 20 %v/v de vinha?a. Nessas condi??es, a efici?ncia da convers?o de energia foi aumentada em aproximadamente 100%, e dependendo do potencial aplicado a efici?ncia aumentou cerca de 30% em solu??o contendo 10 %v/v de glicerina, com rela??o ? solu??o NaAc 0,5 mol L-1 pura, demonstrando que glicerina e vinha?a atuam como agentes de sacrif?cio eficazes no sequestro de buracos eletr?nicos, para evitar a recombina??o dos pares de el?tron?buraco, no processo de foto?oxida??o acionado por buracos. / Tese (Doutorado) ? Programa de P?s-gradua??o em Biocombust?veis, Universidade Federal dos Vales do Jequitinhonha e Mucuri, 2017. / The conversion of solar energy into green fuel H2(g) using photoelectrochemical cells (PEC) is an attractive strategy for storing energy and minimizing the extensive use of fossil fuels. In this work, photoelectrodes were prepared by pyrolysis spray deposition from a pure or W?doped BiVO4/Bi4V2O11 composite deposited directly onto an FTO (fluorine-doped tin oxide) electron-conductive substrate or onto a SnO2 layer previously deposited on an FTO substrate. Initially, these materials were tested for molecular water cleavage. It was observed a hole inversion layer induced by the ferroelectric perovskite Bi4V2O11 at the interface of the n?type BiVO4; a virtual p?n junction with high output photovoltage in relation to a conventional p?n heterojunction was also created. Altering the polarization and doping the ferroelectric material with tungsten may increase the p-n heterojunction. This polarization also reduces the recombination of the photogenerated electron?hole pairs on the surface, to increase the photocurrent to as much as 180%. This characteristic behavior of the p?type and n?type semiconductors when illuminated suggests the use of such a heterojunction as photoanode and photocatode in a PEC cell with two coupled photoelectrodes. This concept was proved to effectively work, by connecting the photovoltaic BiVO4/Bi4V2O11 doped with 1 mass% of W to the non?doped BiVO4/Bi4V2O11 photocathode, which produced a high photovoltage of 1.54 V, and 0.36% STH (solar-to-hydrogen) efficiency. A BiVO4/Bi4V2O11 photoelectrode doped with 2 mass% tungsten was optimized, evidencing the inversion of the hole layer at the semiconductor interface in the resulting denser film. This film tested in different liquid solutions revealed to produce high current densities in 0.5 mol L-1 sodium acetate (NaAc), if glycerol and vinasse were added. The electric resistance in the charge transfer at the electrode/electrolyte interface was relatively low, or 1.16 k? under illumination using 0.5 mol L-1 NaAc solution containing 20 %v/v vinasse. Adding vinasse meant an increase of the energy conversion efficiency corresponding to approximately 100%, and depending on the applied potential efficiency increased by about 30% in solution containing 10% v/v glycerin, relatively to the pure 0.5 mol L-1 NaAc solution. These results evidence that glycerin and vinasse act as effective sacrificing agents, to sequester holes and avoid the recombination of electron?hole pairs in the photo?oxidation driven by holes.

Les travaux développés dans cette thèse traitent de la thématique du vieillissement des Piles à Combustible (PàC) à Membranes Echangeuses de Protons Basse Température (PEM BT). L’utilisation d’une PàC dans un contexte stationnaire à l’intérieur d’une batterie H2 (tandem PàC/Electrolyseur avec un étage de stockage H2 voire O2) est envisagée dans le cadre du déploiement d’un micro-réseau insulaire basé sur des sources d’énergie renouvelables (éolien et photovoltaïque). Deux aspects connexes associés à l’utilisation de la PàC et à son vieillissement dans cet environnement sont investigués dans ce travail de thèse : d’une part la manière dont les performances de la PàC et son rendement vont se dégrader au cours du temps et d’autre part les méthodes et outils qui vont être utilisés pour évaluer son état de santé durant sa période d’activité. La première de ces deux thématiques est abordée via l’étude d’une base de données d’essais en endurance à courant constant effectués sur des prototypes de stack PEM BT fonctionnant en H2/O2. L’hétérogénéité du vieillissement pour les différents stacks testés est mise en avant, de même que le découplage entre les pertes d’étanchéité interne et les dégradations des performances en tension au courant nominal durant les différentes campagnes. Une méthodologie proposant une dissociation des dynamiques réversibles et irréversibles de décroissance de la tension de la PàC au cours du temps est ensuite exposée et sert de base à la construction d’un modèle de dégradation de la tension sur un fonctionnement à courant fixe. Le modèle montre des résultats encourageants et une perspective liée à son utilisation dans le cadre du pronostic est suggérée. La question de la sensibilité du vieillissement aux variations dynamiques de la charge est ensuite abordée de manière complémentaire à ces essais d’endurance (effectués à charge constante) via une campagne de vieillissement effectuée sur des monocellules hybridées ou non directement par des supercondensateurs et cyclant sur un profil de courant dynamique. Une comparaison des évolutions des performances des monocellules au cours du temps dans les deux cas (hybridé et non-hybridé) est effectuée et met en avant l’effet du cyclage dynamique sur la dégradation des performances des PàC. La deuxième thématique touchant les méthodes et outils dédiés à l’évaluation de l’état de santé de la PàC durant son fonctionnement est introduite dans la suite de ces travaux en se penchant notamment sur une des causes majeures de la fin de vie des PàC : l’accroissement du crossover d’H2 vers l’O2 lié à la perte d’étanchéité interne de la membrane. Des mesures de tension à vide (OCV) effectuées lors de phases d’arrêt/démarrage sont scrutées a posteriori pour une des campagnes de la base de données d’essais en endurance. L’objectif est de rechercher des éventuelles corrélations entre l’accroissement des fuites internes et l’évolution de ces mesures au cours du temps afin de développer des potentiels indicateurs des fuites internes. Une séquence opératoire de mise en gaz mettant en avant un lien entre le niveau de crossover d’H2 et la vitesse d’effondrement de l’OCV pour certaines cellules du stack est identifiée et reproduite à l’occasion d’une campagne complémentaire d’essais. Une dernière partie du manuscrit est finalement consacrée à une approche théorique prospective dédiée à l’intégration d’un phénomène parasite, l’oxydation du Pt, dans la modélisation des performances statiques et dynamiques d’une PàC. Les retombées attendues portent sur l’amélioration de l’interprétation des caractérisations menées régulièrement (EIS, OCV, balayages sinus de forte amplitude aux très basses fréquences…), permettant le suivi du vieillissement. / This thesis work deals with the thematic of the Low Temperature Proton Exchange Membrane (PEM LT) Fuel Cell (FC) aging. The use of a FC inside a H2 battery (association of a FC, an electrolyzer and H2 / O2 tanks) in a stationary context is considered in an island micro-grid based on renewable energies (wind and solar power). Two axes linked with the FC use and aging in this context are investigated in this work: one of the axes is centered in the study of the FC performance decrease dynamics over time and the other on the development of methods and tools dedicated to the state of health monitoring during the FC operation. The first thematic is introduced through the exploitation of several aging campaigns performed on PEM FC stack prototypes under constant current solicitations. The stacks considered are fed with pure O2 on the cathode side. A focus is made on the aging heterogeneity inside the stacks and a decoupling between the nominal voltage degradation dynamics and the development of the H2 internal leak with time is highlighted for the different stacks and campaigns. A generic methodology dissociating the reversible and the irreversible voltage losses dynamics is proposed and is further used as a basis to model the nominal voltage degradation with time. The model built in this way is showing encouraging results and its potential use for prognostic purpose is suggested. Whereas these investigations focus on the FC performance degradations under constant current solicitation, the impact of load current dynamic variations on the FC aging is also treated with an experimental study performed on single cells. An ageing campaign under a dynamic load profile is performed on several single cells directly hybridized or not by supercapacitors. The hybridized cells are cycling on an almost-constant current profile whereas the non-hybridized cells are cycling on a dynamic one. A comparison of the performances evolution with time in both cases (hybridized and nothybridized) is done and highlights the effect of the dynamic cycling on the FC performance degradation. The second thematic dealing with the FC state of health evaluation is introduced with one of the main causes of the FC end-of-life: the development of the H2 internal leak between the anode and cathode compartments. Open Circuit Voltage (OCV) measurements performed during start-up and shut-down routines phases are scanned a posteriori in one of the aging campaign of the database. The objective is to seek some potential correlations between those OCV measurements and the H2 internal leak increase over time in order to develop internal leak indicators. A gases introduction operating sequence highlighting a link between the internal leak level and the OCV drift for some stack’s cells is identified during some start-up phases and reproduced during a complementary campaign. A last part of the manuscript is finally dedicated to the integration of a parasitic mechanism (the Pt oxidation) into the FC theoretical quasi-static and dynamic performance modeling. The model integrating this phenomenon is showing some abilities to explain and analyze several experimental features observed on classical performance characterization measurements (EIS, OCV measurements, large amplitude sinus sweep at very low frequency…), opening some perspectives for the FC state of health monitoring.

La liqueur noire, sous-produit de l’industrie papetière, est convertie par un processus hydrothermal. Elle a été choisie pour son contenu élevé en eau (80 wt%), matière organique (14 wt%) et minéraux (6 wt%) qui font d'elle une biomasse à haute valeur ajoutée bien qu'encore peu exploitée. L'étude en batch, balayant une large gamme de température (350°C-600°C), permet d'identifier deux flux sortant : une proportion d'hydrogène élevée dans la phase gazeuse (600°C), ainsi qu'une phase solide, appelée coke, générée quelques soient les conditions opératoires utilisées. La génération de solide modifie la composition du milieu réactionnel en procédé batch et peut poser problème en cas de transposition en réacteur continu. Il est donc important de comprendre sa formation pour pallier ces verrous. L'analyse du résidu montre qu'à 350°C, pour des temps de réaction courts (<2h), de microparticules carbonées se forment. Leur taille est influencée par les vitesses de montée et descente en température. Pour des températures plus hautes, le solide ne présente pas d'intérêt morphologique et sa proportion massique augmente avec la température. Ainsi, une production d'hydrogène significative s'accompagnera d'un dépôt solide dans le réacteur. Une étude catalytique a donc été menée en vue d'augmenter la quantité d'hydrogène et de diminuer la formation de coke tout en travaillant à plus basse température. Cette étude, menée à 350°C et 450°C, montre que les réactions d'hydrogénation et d'oxydation mises en jeu par le catalyseur conduisent aux résultats escomptés. La conversion de molécules modèles de la liqueur noire, menée dans les mêmes conditions d'expériences, a permis d'appréhender les mécanismes majeurs mises en jeu lors de la conversion hydrothermale. Les microparticules à 350°C peuvent être valorisées. Cependant, le changement de taille et de morphologie au cours du temps interroge sur la possibilité de passer en réacteur continu. La formation de solide peut être évitée à partir de 450°C en présence de catalyseur, favorisant en parallèle la production d'hydrogène. De ce fait, ce travail de thèse aborde les verrous scientifiques, techniques et technologiques liés à la conversion hydrothermale de la liqueur noire et notamment de la formation du solide, en présence ou non de catalyseur. / Black liquor, a by-product of paper industry, is converted by hydrothermal process. It was chosen for its high water content (80 wt%), organic material (14 wt%) and minerals (6 wt%) that make it a high-value biomass while still untapped. The study in batch, screening a wide temperature range (350°C-600°C), used to identify two outgoing flows: a high proportion of hydrogen in the gas phase (600°C) and a solid phase, called coke, generated regardless the operating conditions used. The generation of solid changes the composition of the reaction medium in batch process and can be problematic in case of transposition in continuous reactor. Thus it is important to understand its formation to overcome these obstacles. Analysis of the residue shows that at 350°C, for short reaction times (< 2h), carbonaceous micro-particles are formed. Their size is influenced by the temperature rates of rise and fall. For higher temperatures, the solid is of no morphological interest and its weight proportion increased with temperature. Thus, a significant production of hydrogen will be associated with a solid deposit in the reactor. A catalytic study was conducted to increase the amount of hydrogen and reduce the formation of coke while working at lower temperature. This study, conducted at 350°C and 450°C, shows that hydrogenation and oxidation reactions involved with the catalyst, lead to the expected results. Converting models molecules of black liquor, conducted with the same experimental conditions, helped to understand the major mechanisms involved during the hydrothermal conversion. The micro-particles at 350°C can be valorized. However, the change in size and morphology over time wondered about the possibility of implement in continuous reactor. The solid formation can be prevented from 450°C in the presence of catalyst, favoring in parallel hydrogen production. Therefore, this thesis deals with scientific, technical and technological locks related to hydrothermal conversion of black liquor and especially the solid formation, with or without catalyst.

Satellite communication is a widely known method for communicating with remote or disaster-strickenplaces. Sometimes, thecommunication can be a matter of life and death,and it is thus vital that it works well. For two-way communication (such as internet) it is necessary for the antenna on Earth to point towards the satellite with a pointing error not larger than a few tenths of a degree. For example, regulations decided by the authorities in the U.S. forbid pointing errors larger than 0.5°. In some cases the antenna on Earth has to be moving while satellite communication is maintained. Such cases can be when the antenna is mounted to a vehicle, and the antenna thus has to compensate for the vehicle’s movement in order to point at the satellite. This application of satellite communication is called Satcom on the Move (SOTM). By constructing a Simulink model of an entire SOTM-system, including vehicle dynamics, satellite position, signal behavior, sensors, and actuators, different control strategies can be compared. This thesis compares the performance of an H2- and an LQG-controller for a static initial acquisition case, and a dynamic inertial stabilization case. The static initial acquisition case is performed with a search algorithm (SpiralSearch) aiming to find the satellite signalin the shortest possible time for a given initial pointing error. The dynamic inertial stabilization case is performed by allowing the simulated vehicle to drive in a slalom pattern and over uneven grounds. The controllers are designed based on modern control theory.The conclusion of this thesis is that the H2-controller performs slightly better in the static testcase,whereastheLQG-controller performs slightly better in the dynamic test cases. However, the results are greatly influenced by the tuning of the controllers, meaning that the comparison is not necessarily true for the controllers rather than the tuning parameters. / Satellitkommunikation är en allmänt känd metod för att kommunicera med avlägsna eller katastrofdrabbade platser. Ibland kan kommunikationen vara en fråga om liv och död, och det är därför viktigt att den fungerar bra. För tvåvägskommunikation (som internet) är det nödvändigt att antennen på jorden pekar mot satelliten med ett pekfel som inte är större än några tiondels grader. Exempelvis finns det lagar i USA som förbjuder pekfel större än 0,5°. I vissa fall måste antennen på jorden röra sig medan satellitkommunikation upprätthålls. Sådana fall kan vara när antennen är monterad på ett fordon och antennen således måste kompensera för fordonets rörelse för att peka mot satelliten. Denna applikation av satellitkommunikation kallas Satcom on the Move(SOTM). Genom att konstruera en simulinkmodell av ett fullständigt SOTM-system, inklusive fordonsdynamik, satellitposition, signalbeteende, sensorer och ställdon, kan olika reglerstrategier jämföras. Denna avhandling jämför en H2 - och en LQG-regulator för ett statiskt fall, samt ett dynamiskt fall. Det statiska fallet utförs med en sökalgoritm (spiralsökning) som syftar till att hitta en specifik satellitsignal på kortast möjliga tid för ett givet initialt pekfel. Det dynamiska fallet utförs genom att låta det simulerade fordonet köra i slalommönster och på ojämnt underlag. Regulatorerna är designade baserade på modern kontrollteori.  Slutsatsen av denna avhandling är att H2-regulatorn presterar något bättre i det statiska testfallet, medan LQG-regulatorn presterar något bättre i de dynamiska testfallen. Resultaten påverkas emellertid kraftigt av de designade reglerparametrarna, vilket innebär att jämförelsen inte nödvändigtvis är sann för kontrollerna, utan snarare förde specifika reglerparametrarna.

Control and monitoring networks often operate on AC/DC power systems. DC batteries and chargers are commonly used on industrial plants as auxiliary DC power systems for these control and monitoring networks. The energy demand and load profiles for these control networks differ from application to application. Proper design, sizing, and maintenance of the components that forms part of the DC control power system are therefore required. Throughout the load profile of a control and monitoring system there are various peak currents. The peak currents are classified as inrush and momentary loads. These inrush and momentary loads play a large role when calculating the required battery size for an application. This study investigates the feasibility of using supercapacitors in conjunction with batteries, in order to reduce the size of the required battery capacity. A reduction in the size of the required battery capacity not only influences the cost of the battery itself, but also influences the hydrogen emissions, the physical space requirements, and the required rectifiers and chargers. When calculating the required size batteries for an auxiliary power system, a defined load profile is required. Control and monitoring systems are used to control dynamic processes, which entails a continuous starting and stopping of equipment as the process demands. This starting and stopping of devices will cause fluctuations in the load profile. Ideally, data should be obtained from a live plant for the purpose of defining load profiles. Unfortunately, due to the economic risks involved, installing data logging equipment on a live industrial plant for the purpose of research, is not allowed. There are also no historical data available from which load profiles could be generated. In order to evaluate the influence of supercapacitors, complex load profiles are required. In this study, an alternative method of defining the load profile for a dynamic process is investigated. Load profiles for various applications are approximated using a probabilistic approach. The approximation methodology make use of plant operating philosophies as input to the Markov Chain Monte Carlo simulation theory. The required battery sizes for the approximated profiles are calculated using the IEEE recommended practice for sizing batteries. The approximated load profile, as well the calculated battery size are used for simulating the auxiliary power system. A supercapacitor is introduced into the circuit and the simulations are repeated. The introduction of the supercapacitor relieves the battery of the inrush and momentary loads of the load profile. The battery sizing calculations are repeated so as to test the influence of the supercapacitor on the required battery capacity. In order to investigate the full influence of adding a supercapacitor to the design, the impact on various factors are considered. In this study, these factors include the battery size, charger size, H2 extraction system, as well as maintenance requirements and the life of the battery. No major cost savings where evident from the results obtained. Primary reasons for this low cost saving are the fixed ranges in which battery sizes are available, as well as conservative battery data obtained from battery suppliers. It is believed that applications other than control and monitoring systems will show larger savings. / MIng (Computer and Electronic Engineering), North-West University, Potchefstroom Campus, 2015

Control and monitoring networks often operate on AC/DC power systems. DC batteries and chargers are commonly used on industrial plants as auxiliary DC power systems for these control and monitoring networks. The energy demand and load profiles for these control networks differ from application to application. Proper design, sizing, and maintenance of the components that forms part of the DC control power system are therefore required. Throughout the load profile of a control and monitoring system there are various peak currents. The peak currents are classified as inrush and momentary loads. These inrush and momentary loads play a large role when calculating the required battery size for an application. This study investigates the feasibility of using supercapacitors in conjunction with batteries, in order to reduce the size of the required battery capacity. A reduction in the size of the required battery capacity not only influences the cost of the battery itself, but also influences the hydrogen emissions, the physical space requirements, and the required rectifiers and chargers. When calculating the required size batteries for an auxiliary power system, a defined load profile is required. Control and monitoring systems are used to control dynamic processes, which entails a continuous starting and stopping of equipment as the process demands. This starting and stopping of devices will cause fluctuations in the load profile. Ideally, data should be obtained from a live plant for the purpose of defining load profiles. Unfortunately, due to the economic risks involved, installing data logging equipment on a live industrial plant for the purpose of research, is not allowed. There are also no historical data available from which load profiles could be generated. In order to evaluate the influence of supercapacitors, complex load profiles are required. In this study, an alternative method of defining the load profile for a dynamic process is investigated. Load profiles for various applications are approximated using a probabilistic approach. The approximation methodology make use of plant operating philosophies as input to the Markov Chain Monte Carlo simulation theory. The required battery sizes for the approximated profiles are calculated using the IEEE recommended practice for sizing batteries. The approximated load profile, as well the calculated battery size are used for simulating the auxiliary power system. A supercapacitor is introduced into the circuit and the simulations are repeated. The introduction of the supercapacitor relieves the battery of the inrush and momentary loads of the load profile. The battery sizing calculations are repeated so as to test the influence of the supercapacitor on the required battery capacity. In order to investigate the full influence of adding a supercapacitor to the design, the impact on various factors are considered. In this study, these factors include the battery size, charger size, H2 extraction system, as well as maintenance requirements and the life of the battery. No major cost savings where evident from the results obtained. Primary reasons for this low cost saving are the fixed ranges in which battery sizes are available, as well as conservative battery data obtained from battery suppliers. It is believed that applications other than control and monitoring systems will show larger savings. / MIng (Computer and Electronic Engineering), North-West University, Potchefstroom Campus, 2015

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