An investigation into the effects of homopteran honeydew sugars versus floral nectar sugars on black fly longevity, flight performance and digestion /

Floral nectar is thought to be the primary carbohydrate source for most dipteran species. However, it has been shown that black flies (Burgin & Hunter 1997 a,b,c), mosquitoes (Foster 1995; Burkett et al. 1999; Russell & Hunter 2002), deer flies (Magnarelli & Burger 1984; Janzen & Hunter 1998; Ossowski & Hunter 2000), horse flies (Schutz & Gaugler 1989; Hunter & Ossowski 1999) and sand flies (MacVicker et al. 1990; Wallbanks et al. 1990; Cameron et al. 1992, 1995; Schlein & Jacobson 1994, 1999; Hamilton & EI Naiem 2000) feed on homopteran honeydew as well as floral nectar. Prior to 1997 floral nectar was thought to be the main source of carbohydrates for black flies. However, Burgin & Hunter (1 997a) demonstrated that up to 35% of black flies had recently consumed meals of homo pte ran honeydew. This information has necessitated a re-assessment of many life history aspects of black flies. Attempts are being made to examine the effects of nectar versus honeydew on black fly fecundity and parasite transmission (Hazzard 2003). Recently, Stanfield and Hunter (unpublished data) have shown that in female black flies, honeydew sugars produce flights of longer distance and duration than do nectar sugars. This thesis examines two aspects of black fly biology as it relates to sugar meal consumption. First, the effects of honeydew and nectar on black fly longevity are examined. Second, the proximate causation behind longer flight performances in honeydew-fed flies will be examined. The comparison between these two sources is important because nectar is composed of mainly simple sugars (monosaccharides and disaccharides) whereas honeydew is composed of both simple and complex sugars (including trisaccharides and tetrasaccharides ).

Indenture for Partition Wall between William Woodruff and John Plimpton

Indenture regarding an agreement for a partition wall between William Woodruff and John Plimpton, June 24, 1829.

Développement de méthodes analytiques de séparation des produits de digestion enzymatique des dérivés de cellulose

La cellulose et ses dérivés sont utilisés dans un vaste nombre d’applications incluant le domaine pharmaceutique pour la fabrication de médicaments en tant qu’excipient. Différents dérivés cellulosiques tels que le carboxyméthylcellulose (CMC) et l’hydroxyéthylcellulose (HEC) sont disponibles sur le commerce. Le degré de polymérisation et de modification diffèrent énormément d’un fournisseur à l’autre tout dépendamment de l’origine de la cellulose et de leur procédé de dérivation, leur conférant ainsi différentes propriétés physico-chimiques qui leurs sont propres, telles que la viscosité et la solubilité. Notre intérêt est de développer une méthode analytique permettant de distinguer la différence entre deux sources d’un produit CMC ou HEC. L’objectif spécifique de cette étude de maitrise était l’obtention d’un profil cartographique de ces biopolymères complexes et ce, par le développement d’une méthode de digestion enzymatique donnant les oligosaccharides de plus petites tailles et par la séparation de ces oligosaccharides par les méthodes chromatographiques simples. La digestion fut étudiée avec différents paramètres, tel que le milieu de l’hydrolyse, le pH, la température, le temps de digestion et le ratio substrat/enzyme. Une cellulase de Trichoderma reesei ATCC 26921 fut utilisée pour la digestion partielle de nos échantillons de cellulose. Les oligosaccharides ne possédant pas de groupements chromophores ou fluorophores, ils ne peuvent donc être détectés ni par absorbance UV-Vis, ni par fluorescence. Il a donc été question d’élaborer une méthode de marquage des oligosaccharides avec différents agents, tels que l’acide 8-aminopyrène-1,3,6-trisulfonique (APTS), le 3-acétylamino-6-aminoacridine (AA-Ac) et la phénylhydrazine (PHN). Enfin, l’utilisation de l’électrophorèse capillaire et la chromatographie liquide à haute performance a permis la séparation des produits de digestion enzymatique des dérivés de cellulose. Pour chacune de ces méthodes analytiques, plusieurs paramètres de séparation ont été étudiés.

Factorisation de la fonction de partition du modèle d'Ising en deux dimensions défini sur deux régions contiguës

Mémoire numérisé par la Division de la gestion de documents et des archives de l'Université de Montréal

Un calcul algébrique détaillé de la fonction de partition du modèle d'Ising bidimensionnel

Mémoire numérisé par la Division de la gestion de documents et des archives de l'Université de Montréal

A Study of Single Stage Semi‐Dry Anaerobic Digestion of Organic Fraction of Municipal Solid Waste

Solid waste generation is a natural consequence of human activity and is increasing along with population growth, urbanization and industrialization. Improper disposal of the huge amount of solid waste seriously affects the environment and contributes to climate change by the release of greenhouse gases. Practicing anaerobic digestion (AD) for the organic fraction of municipal solid waste (OFMSW) can reduce emissions to environment and thereby alleviate the environmental problems together with production of biogas, an energy source, and digestate, a soil amendment. The amenability of substrate for biogasification varies from substrate to substrate and different environmental and operating conditions such as pH, temperature, type and quality of substrate, mixing, retention time etc. Therefore, the purpose of this research work is to develop feasible semi-dry anaerobic digestion process for the treatment of OFMSW from Kerala, India for potential energy recovery and sustainable waste management. This study was carried out in three phases in order to reach the research purpose. In the first phase, batch study of anaerobic digestion of OFMSW was carried out for 100 days at 32°C (mesophilic digestion) for varying substrate concentrations. The aim of this study was to obtain the optimal conditions for biogas production using response surface methodology (RSM). The parameters studied were initial pH, substrate concentration and total organic carbon (TOC). The experimental results showed that the linear model terms of initial pH and substrate concentration and the quadratic model terms of the substrate concentration and TOC had significant individual effect (p < 0.05) on biogas yield. However, there was no interactive effect between these variables (p > 0.05). The optimum conditions for maximizing the biogas yield were a substrate concentration of 99 g/l, an initial pH of 6.5 and TOC of 20.32 g/l. AD of OFMSW with optimized substrate concentration of 99 g/l [Total Solid (TS)-10.5%] is a semi-dry digestion system .Under the optimized condition, the maximum biogas yield was 53.4 L/kg VS (volatile solid).. In the second phase, semi-dry anaerobic digestion of organic solid wastes was conducted for 45 days in a lab-scale batch experiment for substrate concentration of 100 g/l (TS-11.2%) for investigating the start-up performances under thermophilic condition (50°C). The performance of the reactor was evaluated by measuring the daily biogas production and calculating the degradation of total solids and the total volatile solids. The biogas yield at the end of the digestion was 52.9 L/kg VS for the substrate concentration of 100 g/l. About 66.7% of volatile solid degradation was obtained during the digestion. A first order model based on the availability of substrate as the limiting factor was used to perform the kinetic studies of batch anaerobic digestion system. The value of reaction rate constant, k, obtained was 0.0249 day-1. A laboratory bench scale reactor with a capacity of 36.8 litres was designed and fabricated to carry out the continuous anaerobic digestion of OFMSW in the third phase. The purpose of this study was to evaluate the performance of the digester at total solid concentration of 12% (semi-dry) under mesophlic condition (32°C). The digester was operated with different organic loading rates (OLRs) and constant retention time. The performance of the reactor was evaluated using parameters such as pH, volatile fatty acid (VFA), alkalinity, chemical oxygen demand (COD), TOC and ammonia-N as well as biogas yield. During the reactor’s start-up period, the process is stable and there is no inhibition occurred and the average biogas production was 14.7 L/day. The reactor was fed in continuous mode with different OLRs (3.1,4.2 and 5.65 kg VS/m3/d) at constant retention time of 30 days. The highest volatile solid degradation of 65.9%, with specific biogas production of 368 L/kg VS fed was achieved with OLR of 3.1 kg VS/m3/d. Modelling and simulation of anaerobic digestion of OFMSW in continuous operation is done using adapted Anaerobic Digestion Model No 1 (ADM1).The proposed model, which has 34 dynamic state variables, considers both biochemical and physicochemical processes and contains several inhibition factors including three gas components. The number of processes considered is 28. The model is implemented in Matlab® version 7.11.0.584(R2010b). The model based on adapted ADM1 was tested to simulate the behaviour of a bioreactor for the mesophilic anaerobic digestion of OFMSW at OLR of 3.1 kg VS/m3/d. ADM1 showed acceptable simulating results.