The purpose of this study was to examine VT and LT in boys and men. Eight boys (10-11 years) and nine men (18-30 years) completed a graded exercise test on a cycle ergometer. A two-way (group x threshold) ANOVA compared physiological responses (V02 1/min and ml/kg/min, percentage of V02max, and HR) at VT and LT. Statistical significance was set at P < 0.05. No significant interaction was observed. Significant main effects for group included a higher V02 (1/min) in the men, and a higher percentage of VO2max in the boys. Significant main effects for threshold showed all variables were greater at VT than LT. Within each group, all variables were significantly higher at VT than LT. For the boys and all subjects together, significant correlations between thresholds were observed for V02 (1/min and ml/kg/min) and HR, but not percentage of VO2max. For the men alone, no significant correlations were found. Together, these results suggest that physiological changes associated with LT may contribute to the onset of VT, and the occurrence of the thresholds (expressed as a percentage of VO2max) declines with maturation. / School of Physical Education

L(+)-Lactic acid is a commonly occurring organic acid, which is valuable due to its wide use in food and food-related industries, and its potential for the production of biodegradable and biocompatible polylactate polymers. The aim of this study was to optimize and scale-up a biotechnological process of L(+)-lactic acid production by suspended cells of R. arrhizus DAR 36017 with waste potato starch as the substrate. Commonly used inorganic and organic nitrogen sources, including ammonium sulphate, ammonium nitrate, urea, yeast extract and peptone, were assessed in conjunction with various ratios of carbon to nitrogen (C:N). Fermentation media with a low C:N ratio enhanced the production of lactic acid, biomass and ethanol, while a high C:N ratio led to production of more fumaric acid as a by-product. The use of organic nitrogen sources (yeast extract, peptone and urea) resulted in a significant reduction of lactic acid yields by 15% - 34% with a decrease of C:N from 168 to 28. The use of inorganic nitrogen sources (ammonium nitrate and ammonium sulphate) led to a high lactic acid yield of 84% - 91% at a C:N below 168. Therefore, ammonium nitrate and ammonium sulphate were considered to be better nitrogen sources for lactic acid production. Small pellets are the favoured morphological form for many fermentation processes by filamentous fungi. However, to control filamentous Rhizopus sp in the pellet form in a submerged fermentation system is difficult due to its filamentous characteristics. An acidadapted preculture technique was developed to induce the formation of the pellet form in bioreactors. Using the acid-adapted precultures, the fungal biomass can be controlled in small dispersed pellets as a dominant morphological form. With these small pellets, a lactic acid yield of 86-89%, corresponding to a concentration of 86-89g/L, was obtained in a laboratory scale process using a stirred tank reactor (STR) and a bubble column reactor (BCR). A batch bioprocess for lactic acid production was successfully scaled-up from shake flasks to laboratory scale bioreactors. Results from a simulated scale-up process revealed that the concentration and productivity of lactic acid decreased with the increase of the scale-up steps because of increased pellet size. This suggested that a one-step scale-up process using the acid-adapted preculture may be feasible in an industrial-scale bioreactor system. A comprehensive investigation of the impact of cultivation parameters on the morphology of R. arrhizus and lactic acid production was carried out in the BCR. The results showed that the fungal morphology was significantly influenced by carbon sources, pH, starch concentrations, sparger designs and aeration rates. The favoured morphology for lactic acid production was freely dispersed small pellets, which could be retained as a dominant morphology under operation conditions at pH 5.0 – 6.0, starch concentrations of 60 – 120 g/L and aeration rates of 0.2 – 0.8 vvm, using a sintered stainless steel disc sparger. The optimal cultivation conditions at pH 6.0 and aeration rate of 0.4 vvm resulted in the formation of the freely dispersed small pellets and production of 103.8 g/L lactic acid, with a yield of 87%, from 120 g/L liquefied potato starch in 48 h. This study shows a technically feasible and economically promising process for the production of lactic acid from waste potato starch. The use of waste potato starch instead of pure glucose or starch as substrate can significantly reduce the production cost, making this technology environmentally and economically attractive. / http://proxy.library.adelaide.edu.au/login?url= http://library.adelaide.edu.au/cgi-bin/Pwebrecon.cgi?BBID=1339122 / Thesis (Ph.D.) -- University of Adelaide, School of Chemical Engineering, 2008

Diss. (sammanfattning) Uppsala : Sveriges lantbruksuniv. / Härtill 4 uppsatser.

Diss. (sammanfattning) Uppsala : Sveriges lantbruksuniversitet, 2005. / Härtill 5 uppsatser.

Thesis (Ph.D.)--Mississippi State University. Department of Food Science, Nutrition and Health Promotion. / Title from title screen. Includes bibliographical references.

Thesis (MSc Food Sc)--Stellenbosch University, 2013. / ENGLISH ABSTRACT: A wide variety of traditionally and commercially fermented milks are commonly consumed in various countries of Sub-Saharan Africa. Commercially fermented milk is produced on an industrial scale according to well-managed, standardised production processes and starters are used to initiate fermentation. Traditionally fermented milk is prepared domestically and fermentation occurs spontaneously at ambient temperatures. Lactic acid bacteria (LAB) are responsible for milk fermentation during which they convert the milk carbohydrates to lactic acid, carbon dioxide, alcohol and other organic metabolites. Acetic acid bacteria (AAB), yeasts and mycelial fungi have also been isolated from fermented milks. In this study the microbial consortium present in three traditionally fermented milks, namely omashikwa from Namibia, masse from Mozambique and chekapmkaika from Uganda and two commercially fermented milks, namely chambiko from Malawi and omaere from Namibia, were isolated and enumerated on six different selective media that included MSR + C (specific for lactobacilli), KCA + TTC (specific for lactococci), KCA + V (specific for leuconostocs), MRS + E (specific for AAB), MEA (specific for mycelial fungi) and YPD (specific for yeasts). No significant differences were found between the enumeration values obtained for the three chambiko samples, as well as for enumeration values obtained for the two omaere samples on each of the selective media, indicating low sample variance. Significant differences between enumeration values obtained for the three omashikwa samples were found on all six selective media. Significant differences between enumeration values of the three masse samples and both the chekapmkaika samples were also observed on the selective media. In addition to this, significant differences were observed between average enumeration values obtained for each media between the masse and chekapmkaika, the chambiko and omaere, as well as when the traditional and commercial milks were compared. According to the average enumeration values obtained on each media selective for LAB, the highest bacterial counts were detected on KCA + TTC medium for omaere (2.3 x 106 cfu.ml-1), KCA + V for chambiko (1.8 x 105 cfu.ml-1), KCA + TTC for omashikwa and MRS + C for masse and chekapmkaika (6.2 x 106 and 2.0 x 103 cfu.ml-1, respectively). After isolation and enumeration of the microbes present in each milk, bacterial isolates on the media selective for LAB and AAB were obtained according to the Harrison Disk method. These isolates were identified by amplifying a 1.5 kilobase (kb) part of the 16S ribosomal RNA (rRNA) gene using the polymerase chain reaction (PCR), followed by DNA sequencing. The isolates were identified by comparing the sequences obtained to sequences listed in the NCBI database using the BLAST algorithm and searching for the closest relative. The main LAB group present in the omaere was lactococci (94%), in chambiko and chekapmkaika it was lactobacilli (30% and 45%, respectively), in omashikwa it was enterococci (43%) and in masse it was leuconostocs (68%). The same microbial species were present on a number of the selective media used in this study. Lactococcus spp., Enterococcus spp. and Lactobacillus spp. were isolated from MRS + C, KCA + TTC, KCA + V and MRS + E and Leuconostoc spp. were isolated from MRS + C, MRS + E and KCA + V. Hygienic standards during traditional milk fermentation is often poor and, therefore, microbial contaminants were isolated from the traditional milk and these included Acinetobacter johnsonii and Klebsiella pneumoniae from KCA + V, Mesorhizobium loti, Acinetobacter radioresistens, Escherichia coli, Staphylococcus spp., Kluyvera georgiana, Enterobacter spp. and Klebsiella oxytoca from KCA + TTC, Staphylococcus spp. from MRS + C and Bacillus spp. from MRS + E. Since the media used for the isolation of the LAB and AAB in this study were not selective further identification of the enumerated microbes is of importance for the identification of the microbial groups present in each fermented milk. The data obtained in this study clearly shows that fermented milks from Sub-Saharan Africa vary significantly from each other in terms of microbial numbers, microbial diversity and the dominant microbial groups present. The microbial diversity of the traditionally fermented milks was more diverse than the microbial diversity of the commercially fermented milks. LAB strains isolated from these traditionally fermented milks can be used to develop novel starters and as a result new commercially fermented dairy products with unique aromas, tastes and characteristics can be produced. / AFRIKAANSE OPSOMMING: 'n Wye verskeidenheid tradisioneel en kommersieel gefermenteerde melk produkte word algeneem verbruik in verskeie lande van Sub-Sahara Afrika. Kommersieel gefermenteerde melk word geproduseer op groot skaal, deur deeglik bestuurde gestandardiseerde produksieprosesse en 'n beginkultuur word gebruik om fermentasie te inisieer. Tradisioneel gefermenteerde melk word tuis gemaak en fermentasie gebeur spontaan by kamertemperatuur. Melksuurbakterieë (MSB) is verantwoordelik vir melkfermentasie waartydens die bakterieë koolhidrate omskakel na melksuur, koolstofdioksied, alkohol en ander organiese sure. Asetaatsuurbakterieë (ASB), giste en miseliale fungi is ook al van gefermenteerde melk geïsoleer. In hierdie studie is die mikrobiese konsortium teenwoordig in drie soorte tradisioneel gefermenteerde melk, naamlik omashikwa van Namibië, masse van Mosambiek en chekapmkaika van Uganda en twee soorte kommersieel gefermenteerde melk, naamlik chambiko van Malawi en omaere van Namibië, geïsoleer en getel op ses verskillende selektiewe groeimedia insluitend MRS + C (spesifiek vir lactobacilli), KCA + TTC (spesifiek vir lactococci), KCA + V (spesifiek vir leuconostocs), MRS + E (spesifiek vir ASB), MEA (spesifiek vir miseliale fungi) en YPD (spesifiek vir giste). Geen betekenisvolle verskille is gevind tussen die mikrobiese tellings verkry vir die drie chambiko monsters nie, sowel as tussen die mikrobiese tellings verkry vir die twee omaere monsters, op elk van die selektiewe groeimedia, wat dui op lae monster variansie. Betekenisvolle verskille is gevind tussen die mikrobiese tellings verkry vir die drie omashikwa monsters op al ses selektiewe groeimedia. Betekenisvolle verskille is ook waargeneem tussen die mikrobiese tellings van die drie masse monsters en beide die chekapmkaika monsters op die selektiewe groeimedia. Daarbenewens is betekenisvolle verskille waargeneem tussen gemiddelde mikrobiese tellings verkry vir elke groeimedium tussen die masse en chekapmkaika, die chambiko en omaere asook toe die tradisionele en kommersiële melk produkte met mekaar vergelyk is. Volgens die gemiddelde mikrobiese tellings verkry op elk van die groeimedia selektief vir MSB, is die hoogste mikrobiese telling waargeneem op KCA + TTC medium vir omaere (2.3 x 106 kve.ml-1), KCA + V vir chambiko (1.8 x 105 kve.ml-1), KCA + TTC vir omashikwa en MRS + C vir masse en chekapmkaika (6.2 x 106 en 2.0 x 103 kve.ml-1, respektiewelik). Na die isolasie en tel van die mikrobes teenwoordig in elke melk is bakteriese isolate op die media selektief vir MSB en ASB verkry volgends die Harrison Disk metode. Hierdie isolate is geïdentifiseer deur amplifikasie van „n 1.5 kilobasis (kb) gedeelte van die 16S ribosomale RNS (rRNS) geen deur gebruik te maak van die polimerase kettingreaksie gevolg deur DNS klonering. Die isolate is geïdentifiseer deur die gekloneerde insetsels se volgordes te vergelyk met volgordes beskikbaar op die NCBI webwerf deur van die BLAST algoritme gebruik te maak en die naas verwante insetsel op te spoor. Die hoof MSB groep teenwoordig in die omaere was lactococci (94%), in chambiko en chekapmkaika was dit lactobacilli (30% en 45%, respektiewelik), in die omashikwa was dit enterococci (43%) en in die masse was dit leuconostocs (68%). Dieselfde mikrobiese spesies was teenwoordig op verskeie van die selektiewe groeimedia gebruik in hierdie studie. Lactococcus spp., Enterococcus spp. en Lactobacillus spp. is geïsoleer van MRS + C, KCA + TTC, KCA + V en MRS + E en Leuconostoc spp. is geïsoleer van MRS + C, MRS + E en KCA + V. Higiëniese standaarde tydens tradisionele melkfermentasie is dikwels swak en dus is mikrobiese kontaminante geïsoleer van die tradisionele melk produkte insluitend Acinetobacter johnsonii en Klebsiella pneumoniae van KCA + V, Mesorhizobium loti, Acinetobacter radioresistens, Escherichia coli, Staphylococcus spp., Kluyvera georgiana, Enterobacter spp. en Klebsiella oxytoca van KCA + TTC, Staphylococcus spp. van MRS + C en Bacillus spp. van MRS + E. Aangesien die media wat gebruik is vir die isolasie van die MSB en ASB in hierdie studie nie selektief was nie, is verdere identifikasie van die getelde mikrobes belangrik vir die identifikasie van die mikrobiese groepe teenwoordig in elke melk. Die data verkry in hierdie studie dui aan dat gefermenteerde melk produkte van Sub-Sahara Afrika betekenisvol van mekaar verskil in terme van mikrobiese getalle, mikrobiese diversiteit en die dominante mikrobiese groepe teenwoordig. Die mikrobiese diversiteit van die tradisioneel gefermenteerde melk produkte was meer divers as die mikrobiese diversiteit van die kommersieel gefermenteerde melk produkte. MSB spesies geïsoleer van hierdie tradisioneel gefermenteerde melk produkte kan gebruik word om nuwe beginkulture te ontwikkel en gevolglik kan nuwe kommersieel gefermenteerde suiwelprodukte met unieke aromas, smake en eienskappe geproduseer word.

Made available in DSpace on 2014-06-11T19:32:55Z (GMT). No. of bitstreams: 0 Previous issue date: 2011-02-11Bitstream added on 2014-06-13T19:03:40Z : No. of bitstreams: 1 coelho_lf_dr_rcla.pdf: 3999428 bytes, checksum: b2a1c737e7c2bb5f6e89843add264993 (MD5) / Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP) / O objetivo deste trabalho foi isolar micro-organismos produtores de D-(-) e L-(+) ácido lático, os quais são utilizados na síntese de polímeros empregados na produção de diversos materiais resistentes e biodegradáveis, além de otimizar a produção de ácido lático, a partir da utilização de diversos resíduos agro-industriais. Os micro-organismos mais promissores para produção de L-(+) ácido lático foram os isolados de Keffir (Ke6, Ke11, Ke8 e Ke24) e o Lactobacillus rhamnosus B103, já para a produção de D-(-) ácido lático, os mais promissores foram os isolados de iogurte (Y15C e Y15A) e o Leuconostoc mesenteroides B512. Pode-se afirmar que os micro-organismos selecionados apresentaram grande potencial para utilização na indústria de biopolímeros e indústria de alimentos. O soro de queijo e a manipueira foram os melhores resíduos para produção de L-(+) ácido lático por Lactobacillus rhamnosus B103. Quando se utilizou 160 g/L de lactose de soro de queijo, 60 mL/L de água de maceração de milho (AMM), 2 mL/L de Tween 80 e 0,10 g/L de MnSO4, observou-se alta produção de L- (+) ácido lático (142 g/L) e baixo residual de lactose (3,2 g/L). Para a otimização com manipueira, foi obtido 41,58 g/L de L-(+) ácido lático, a partir de 50 g/L de açúcar redutor total (ART), 65,40 mL/L de AMM e 1,27 mL/L de Tween 80. Nas otimizações com Leuconostoc mesenteroides B512 foi observado produção de 60,20 g/L de D-(-) ácido lático, utilizando 116,90 g/L de ART de caldo de cana e 44,25 g/L de autolisado de levedura. Nas otimizações com L. plantarum Lmism6 observou-se uma produção de 63,40 g/L de ácido lático, 0,40 g/L de ART residual e alta conversão de substrato (99,40%), quando se utilizou 70 g/L de ART de melaço, 30,00 mL/L de AMM, 2 g/L de K2HPO4 e 1 mL/L de Tween 80 / The aim of this study was to isolate D-(-) and L-(+) lactic acid producers micro-organisms, which are used in the synthesis of polymers used in the production of many resistant and biodegradable materials and optimize the lactic acid production, from agro-industrial residues. The most promising micro-organisms for L-(+) lactic acid production were Lactobacillus rhamnosus B103, as well as, the isolated from Keffir (Ke6, Ke11, Ke8 Ke24) and the most promising D-(-) lactic acid producers were strains of yogurt (Y15C and Y15A) and Leuconostoc mesenteroides B512. Cheese whey and cassava wastewater (CW) were the best residues for L-(+) lactic acid production by Lactobacillus rhamnosus B103. Using 160 g/L of lactose from whey, 60 mL/L of CSL, 2 mL/L of Tween 80 and 0.10 g/L of MnSO4, there was higher production of L-(+) lactic acid (142 g/L) and low lactose residual (3.20 g/L). For optimizations with CW, it was obtained 41.58 g/L of L-(+) lactic acid from 50 g/L of reducing sugar, 65.40 mL/L and 1.27 mL of corn steep liquor (CSL) and Tween 80 respectively. Leuconostoc mesenteroides B512 produced 60.20 g/L of D-(-) lactic acid, using 116.90 g/L of sugarcane juice and 44.25 g/L of yeast autolysate. L. plantarum Lmism6 produced 63.40 g/L of lactic acid, with less residual reducing sugar (0.41 g/L) and higher substrate conversion (99.41%), by using 70 g/L of sugar reducing from molasses, 30 mL/L of CSL, 2 g/L of K2HPO4, and 1 mL/L of Tween 80

Made available in DSpace on 2014-12-17T14:07:18Z (GMT). No. of bitstreams: 1 BeatrizSSNM_DISSERT.pdf: 3822050 bytes, checksum: cb23d4096043d3edf7fed1c6cb6c7f6a (MD5) Previous issue date: 2013-11-01 / Conselho Nacional de Desenvolvimento Cient?fico e Tecnol?gico / The environmental impact caused by the disposal of non-biodegradable polymer packaging on the environment, as well as the high price and scarcity of oil, caused increase of searches in the area of biodegradable polymers from renewable resources were developed. The poly (lactic acid) (PLA) is a promising polymer in the market, with a large availability of raw material for the production of its monomer, as well as good processability. The aimed of this study was synthesis PLA by direct polycondesation of lactic acid, using the tool of experimental design (DOE) (central composite rotatable design (CCRD)) to optimize the conditions of synthesis. The polymer obtained was characterized by scanning electron microscopy (SEM), Fourier transform infrared spectroscopy (FTIR), viscosimetric analysis, differential scanning calorimeter (DSC) and size exclusion chromatography (SEC). The results confirmed the formation of a poly (lactic acid) semicrystalline in the syntheses performed. Through the central composite rotatable design was possible to optimize the crystallization temperature (Tc) and crystallinity degree (Xc). The crystallization temperature maximum was found for percentage of catalyst around the central point (0,3 (%W)) and values of time ranging from the central point (6h) to the upper level (+1) (8h). The crystallization temperature maximum was found for the total synthesis time of 4h (-1) and percentage of catalyst 0,1(W%) (-1). The results of size exclusion chromatography (SEC) showed higher molecular weights to 0,3 (W%) percent of catalyst and total time synthesis of 3,2h / Os impactos ambientais causados pelo descarte de embalagens polim?ricas n?o biodegrad?veis no meio ambiente, assim como o alto pre?o e escassez do petr?leo, fizeram com que pesquisas crescentes na ?rea de pol?meros biodegrad?veis provenientes de fontes renov?veis fossem desenvolvidas. O poli (?cido l?ctico) (PLA) ? um pol?mero promissor nesse mercado, com uma grande disponibilidade de mat?ria-prima para produ??o do seu mon?mero, assim como tamb?m boa processabilidade. Dessa forma, este trabalho teve como objetivo a s?ntese por policondensa??o direta do poli (?cido L?ctico) a partir do ?cido-L-l?ctico utilizando a ferramenta de planejamento fatorial, por meio de um delineamento composto central rotacional (DCCR), visando otimizar as condi??es de s?ntese. O pol?mero obtido foi caracterizado por microscopia eletr?nica de varredura (MEV), espectroscopia na regi?o do infravermelho (FTIR), an?lise viscosim?trica, calorimetria explorat?ria diferencial (DSC) e cromatografia por exclus?o de tamanho (SEC). Os resultados obtidos confirmaram a forma??o do poli (?cido l?ctico) semicristalino em todas as s?nteses realizadas. Atrav?s do delineamento composto central rotacional foi poss?vel a otimiza??o da temperatura de cristaliza??o (Tc) e do grau cristalinidade (Xc). A temperatura de cristaliza??o m?xima foi obtida para percentuais de catalisador em torno do ponto central (0,3(W%)) e valores de tempo variando do ponto central (6h) ao n?vel superior (+1) (8h). O grau de cristalinidade (Xc) m?ximo foi obtido para o tempo total de s?ntese de 4h (-1) e percentual de catalisador de 0,1 (W%) (-1). A an?lise de cromatografia por exclus?o de tamanho (SEC) forneceu resultados de maiores massas molares dentre todos os pol?meros sintetizados, para o percentual de catalisador (octoato de estanho) de 0,3(W%) e tempo total de s?ntese de 3,2h

Le phosphore est un élément crucial pour la vie sur Terre, de par son implication dans les processus bioénergétiques, le stockage et le traitement de l'information génétique. C'est également l'un des nutriments limitants en agriculture, aux côtés de l'azote et du potassium. Depuis la révolution verte au milieu du 20ième siècle, le monde agricole est dépendant des engrais phosphorés à bas coûts, fabriqués à partir d'une ressource fossile et nécessaires à l'amélioration des rendements des cultures à même de répondre aux besoins en nourriture d'une population en forte croissance. Cependant cette ressource, la roche phosphatée, s'épuise progressivement. De plus, son utilisation est très peu efficiente : moins de 20% du phosphore extrait se retrouve effectivement dans la nourriture consommée. L'une des raisons de cette faible efficience est la spécialisation de régions entières dans des productions agricoles spécifiques. Ainsi, les régions spécialisées dans les cultures à hauts rendements ont besoin de grandes quantités d'engrais minéraux alors que les régions d'élevage intensif ont des excédents de lisier sans terres agricoles suffisamment grandes et proches pour servir de zones d'épandage. L'épandage excessif de lisier en Bretagne est la cause première d'eutrophisation des cours d'eau. Le phosphore contenu dans le lisier porcin pourrait être recyclé sous forme de struvite (MgNH4PO4,6H2O), un engrais phosphaté à dissolution lente, très concentré et facilement transportable vers les régions de cultures végétales nécessitant une fertilisation phosphatée importante. Le phosphore du lisier porcin étant initialement présent sous une forme minérale solide, il est nécessaire de le dissoudre avant de le précipiter en struvite. Parce-que la dissolution par acidification chimique est trop chère et implique un mauvais bilan environnemental, le procédé développé lors de cette thèse utilise l'acidogénèse, un procédé biologique au cours duquel la matière organique est convertie en acides organiques en absence d'oxygène, acidifiant naturellement le lisier porcin. Différents déchets organiques ont été testés en tant que co-substrats dans du lisier porcin brut ou digéré, provoquant une fermentation de type lactique lorsque le co-substrat possédait une forte teneur en glucides facilement biodégradables, et une fermentation avec de nombreux acides organiques produits lorsque la teneur en glucides facilement biodégradables était faible. Il a pu être démontré que la fermentation lactique était le fait de bactéries appartenant au genre Lactobacillus, alors que divers Clostridiales dominaient lors des autres fermentations avec la production d'acétate, propionate, butyrate et valérate. Un réacteur en semi continu alimenté d'un mélange de lisier brut de petit pois et de carottes a permis la dissolution de 50% du phosphore total soit 750 mg-P/L. Après centrifugation, 3.4 g d'hydroxyde de magnésium par litre de surnageant a été ajouté afin d'élever le pH à 8 et ainsi précipiter la struvite. 99% du phosphore dissous a alors été abattu. Le solide obtenu contenait 70% de struvite, un léger excès de phosphore et de magnésium, ainsi que de la matière organique. L'acidogénèse permet l'hydrolyse de la matière organique complexe et la formation d'acides organiques. De ce fait, ce procédé de recyclage du phosphore contenu dans le lisier porcin pourrait être implémenté dans les nombreuses unités de méthanisation présentes en Bretagne et qui traitent des effluents animaux ainsi que des déchets organiques d'origine agricole, industrielle et municipale. La struvite obtenue pourrait être vendue dans les régions ayant besoin de fertilisation phosphatée alors que la matière organique du digestat pourrait être maintenue en Bretagne. Un tel procédé réduirait significativement l'eutrophisation due à l'épandage excessif du lisier tout en diminuant les besoins en fertilisants minéraux fossiles grâce à une source alternative aux performances fertilisantes équivalentes. / Phosphorus is a crucial nutrient for life, implicated in cellular bioenergetics as well as storage and processing of genetic information. It is also one of the limiting nutrients in agriculture with nitrogen and potassium. Since the green revolution in the middle of the 20th century, agriculture has relied on increasing amounts of cheap mineral P-fertilizers produced from a fossil resource to improve crop yields and sustain population growth. However, the resource is depleting and its use efficiency is poor: less than 20% of extracted P is actually consumed in food. One of the reasons for this is the specialization of entire regions into on type of agricultural production or another. Thus, regions focusing on high yield crops require large applications of fossil mineral fertilizers while intensive livestock breeding areas cannot find an output for their P-rich manure due to the distance with crop fields in need of P fertilization. Over application of animal manure in Brittany is the main cause of eutrophication in the region. Phosphorus could be recovered from pig manure as struvite, a concentrated, slow-release mineral fertilizer easily transported to crop-oriented regions in need of P fertilization. P in pig slurry is mostly under a solid inorganic form, requiring dissolution prior to precipitation as struvite. Because chemical acidification is too expensive and harmful to the environment, the process developed in this PhD relied on acidogenesis, a biological process in which organic matter is converted to organic acids under anaerobic conditions, thus naturally acidifying the swine slurry. Various organic wastes were tested as organic co-substrates on raw and digested pig slurry, leading to lactic acid fermentation when the co-substrate had a high content in easily biodegradable carbohydrates and a fermentation with diverse organic acids produced at low content in easily biodegradable carbohydrates. Lactobacillus was the genus responsible for lactic acid fermentation and various Clostridiales dominated otherwise, producing acetate, propionate, butyrate and valerate. A reactor was operated with semi-continuous feeding of raw swine slurry and carrot/pea, leading to the dissolution of 50% total-phosphorus or 750 mg-P/L. After centrifugation, struvite was precipitated in the supernatant by adding magnesium hydroxide to increase the pH to 8. 99% of dissolved P precipitated. The solid recovered contained 70% of struvite, a slight excess of P and Mg as well as organic matter. Because hydrolysis of organic matter and production of organic acids occurs during acidogenesis, the process could be implemented in the many anaerobic digestion units installed in Brittany treating animal manure and agricultural, industrial and municipal organic waste. The struvite recovered could be sold to regions in need while the digestate impoverished in P and rich in organic matter could be kept locally. Such process would reduce eutrophication due to over application of pig manure and also reduce the reliance on fossil P fertilizer by offering an alternative source with equivalent fertilizing performances.

Submitted by Weslei Diego Pavini null (wesleydiego@gmail.com) on 2017-05-23T14:13:00Z No. of bitstreams: 1 Dissertação mestrado - Weslei D. Pavini.pdf: 7330663 bytes, checksum: a86ba8ec10a0627ea18d3883c094b461 (MD5) / Approved for entry into archive by Luiz Galeffi (luizgaleffi@gmail.com) on 2017-05-23T18:18:34Z (GMT) No. of bitstreams: 1 pavini_wd_me_araiq_par.pdf: 737035 bytes, checksum: 22742b425e546a6ef2e994294d7d9349 (MD5) / Made available in DSpace on 2017-05-23T18:18:34Z (GMT). No. of bitstreams: 1 pavini_wd_me_araiq_par.pdf: 737035 bytes, checksum: 22742b425e546a6ef2e994294d7d9349 (MD5) Previous issue date: 2017-05-02 / Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES) / Biorreatores têm sido estudados para obtenção de H2, um produto de alto valor agregado usado na indústria química e afim e na produção de energia. Neste trabalho foi desenvolvido um método para análise de compostos orgânicos voláteis (VOCs) produzidos em biorreatores para auxiliar na pesquisa e no controle operacional da produção de H2. Com base nos compostos de interesse foi otimizado um procedimento de microextração líquido-líquido (LLME) para recuperação destes do meio aquoso. Para isto foi usado 400 µL de 1-octanol, um solvente lipofílico e biodegradável, sulfato de sódio e 1,2 mL de amostra. Em seguida foi desenvolvido um método de separação e detecção por cromatografia em fase gasosa acoplada a um detector de ionização em chama (GC-FID). A separação foi feita usando coluna de polietilenoglicol de 30 m de comprimento e hélio como gás de arraste. O tempo de análise total foi de 16 min. Através deste método foi possível extrair, separar e quantificar 12 compostos: acetona, metanol, etanol, 1-propanol, 1-butanol, ácido acético, ácido propiônico, ácido butírico, ácido isovalérico, ácido valérico, ácido capróico e ácido láctico. Todas as curvas analíticas foram validadas usando a análise de variância (ANOVA). Além disso, foram calculadas algumas figuras de mérito, como o limite de detecção, o intervalo de quantificação, a exatidão e a precisão. Foram realizados testes de efeito matriz e estabilidade da amostra. Algumas amostras provenientes dos biorreatores de produção de H2 foram analisadas através do método proposto. O método desenvolvido mostrou-se preciso, exato e tem vasta gama de aplicação. / Bioreactors have been studied to obtain H2, a high value-added product used in the chemical and allied industry and in energy production. In this work a method was developed for the analysis of volatile organic compounds (VOCs) produced in bioreactors to assist in the research and operational control of H2 production. Based on the compounds of interest, a liquid-liquid micro extraction procedure (LLME) was optimized for recovery of these from the aqueous medium. 400 μl of 1-octanol, a lipophilic and biodegradable solvent, sodium sulfate and 1.2 mL of sample were used for this. Next, a separation and detection method was developed by gas chromatography coupled to a flame ionization detector (GC-FID). The separation was done using 30 m polyethylene glycol column and helium as carrier gas. The total analysis time was 16 min. This method was used to extract, separate and quantify 12 compounds: acetone, methanol, ethanol, 1-propanol, 1-butanol, acetic acid, propionic acid, butyric acid, isovaleric acid, valeric acid, caproic acid and lactic acid. All analytical curves were validated using analysis of variance (ANOVA). In addition, some figures of merit were calculated, such as limit of detection, interval of quantification, accuracy and precision. The matrix effect and stability of the samples were also performed. Some samples from the H2 production bioreactors were analyzed using the proposed method. The method developed proved accurate, precise and has a wide range of application.