Comprendre comment la biodiversité des prairies répond aux changements d’utilisation des terres constitue un enjeu majeur pour la conservation de la biodiversité et le maintien des services écosystémiques dans les paysages agricoles. Dans ce travail de thèse, nous avons cherché (i) à analyser la réponse simultanée d’un ensemble de taxons appartenant à différents niveaux trophiques (plantes, herbivores, pollinisateurs, prédateurs) aux changements d’utilisation des terres agissant à différentes échelles spatiales et temporelles ; (ii) à approcher les mécanismes impliqués dans cette réponse et notamment le rôle des interactions trophiques. Notre approche est basée sur l’utilisation de multiples traits fonctionnels liés à l’acquisition des ressources, la taille et la mobilité des organismes. Nous avons testé la réponse de ces traits à l’histoire des paysages, leur configuration et leur composition. Nous montrons qu’il existe une réponse générale de la diversité fonctionnelle multitrophique aux changements d’utilisation des terres. Nous mettons en évidence l’importance des effets historiques du changement d’utilisation des terres à l’échelle des paysages agricoles menaçant le maintien de communautés fonctionnellement diversifiées dans ces paysages. En considérant un set de traits multiples, notre travail a permis d’approcher certains mécanismes par lesquels les changements d’utilisation des terres présents et passés impactent différentes facettes de la biodiversité. Enfin, l’utilisation des traits fonctionnels a permis d’appréhender l’importance des interactions trophiques et leur implication dans la structuration des communautés animales dans les milieux agricoles. / Understanding how grassland biodiversity responds to land use intensification is crucial for both biodiversity conservation and the management of key ecosystem services in agricultural landscapes. My PhD aims at (i) identifying and generalising the effects of land use intensification operating at different spatial and temporal scales across multiple taxonomic groups and trophic levels (plants, herbivores, pollinators, predators and top-predators) ; (ii) investigating the underlying mechanisms of biodiversity response, and particularly the role of trophic interactions. We used multiple functional traits related to resource acquisition, the size of the organisms and their mobility. We tested how multitrophic functional trait diversity responded to landscape history, composition and heterogeneity. Considering multiple taxonomic groups simultaneously, our study brings out a clear response of overall biodiversity to land use intensification. We found that legacy effects of land use intensification operating at the landscape scale are major drivers of present-day multitrophic functional trait diversity in agricultural landscapes. By considering a core set of organismal traits reflecting similar functions across trophic levels, our approach reveals multiple dimensions by which land use intensification filters out biodiversity over time and allows us to generalise its effect across multiple trophic levels and trait-spectrum. Finally, trait-based approach allowed us to assess the importance of trophic interactions and their contribution in shaping animal communities in agricultural landscapes.

A non-reactive model system comprising a highly concentrated and unstable oil-in-water emulsion was used to investigate the retention of oil by the membrane in producing biodiesel with a membrane reactor. Critical flux was identified using the relationship between the permeate flux and transmembrane pressure along with the separation efficiency of the membrane. It was shown that separation efficiencies above 99.5% could be obtained at all operating conditions up to the critical flux. It was observed that the concentration of oil in all collected permeate samples using the oil-water system was below 0.2 wt% when operating at a flux below the critical flux. Studies to date have been limited to the characterization of low concentrated emulsions below 15 vol.%. The average oil droplet size in highly concentrated emulsions was measured as 3200 nm employing direct light scattering (DLS) measurement methods. It was observed that the estimated cake layer thickness of 20 to 80 mm was larger than external diameter of the membrane tube i.e. 6 mm based on a large particle size. Settling of the concentrated emulsion permitted the detection of a smaller particle size distribution (30-100 nm) within the larger particles averaging 3200 nm. It was identified that DLS methods could not efficiently give the droplet size distribution of the oil in the emulsion since large particles interfered with the detection of smaller particles. The content of the smaller particles represented 1% of the total weight of oil at 30°C and 5% at 70°C. This was too low to be detected using DLS measurements but was sufficient to affect ultrafiltration. In order to study the critical flux in the presence of transesterification reaction and the effect of cross flow velocity on separation, various oils were transesterified in another membrane reactor providing higher cross flow velocity. higher cross flow velocity provides better separation by reducing materials deposition on the surface of the membrane due to higher shearing. The oils tested were canola, corn, sunflower and unrefined soy oils (Free Fatty Acids (FFA< 1%)), and waste cooking oil (FFA= 9%). The quality of all biodiesel samples was studied in terms of glycerine, mono-glyceride, di-glyceride and tri-glyceride concentrations. The composition of all biodiesel samples were in the range required by ASTM D6751 and EN 14214 standards. A critical flux based on operating pressure in the reactor was reached for waste cooking and pre-treated corn oils. It was identified that the reaction residence time in the reactor was an extremely important design parameter affecting the operating pressure in the reactor. / Natural Sciences and Engineering Research Council of Canada (NSERC)

A non-reactive model system comprising a highly concentrated and unstable oil-in-water emulsion was used to investigate the retention of oil by the membrane in producing biodiesel with a membrane reactor. Critical flux was identified using the relationship between the permeate flux and transmembrane pressure along with the separation efficiency of the membrane. It was shown that separation efficiencies above 99.5% could be obtained at all operating conditions up to the critical flux. It was observed that the concentration of oil in all collected permeate samples using the oil-water system was below 0.2 wt% when operating at a flux below the critical flux. Studies to date have been limited to the characterization of low concentrated emulsions below 15 vol.%. The average oil droplet size in highly concentrated emulsions was measured as 3200 nm employing direct light scattering (DLS) measurement methods. It was observed that the estimated cake layer thickness of 20 to 80 mm was larger than external diameter of the membrane tube i.e. 6 mm based on a large particle size. Settling of the concentrated emulsion permitted the detection of a smaller particle size distribution (30-100 nm) within the larger particles averaging 3200 nm. It was identified that DLS methods could not efficiently give the droplet size distribution of the oil in the emulsion since large particles interfered with the detection of smaller particles. The content of the smaller particles represented 1% of the total weight of oil at 30°C and 5% at 70°C. This was too low to be detected using DLS measurements but was sufficient to affect ultrafiltration. In order to study the critical flux in the presence of transesterification reaction and the effect of cross flow velocity on separation, various oils were transesterified in another membrane reactor providing higher cross flow velocity. higher cross flow velocity provides better separation by reducing materials deposition on the surface of the membrane due to higher shearing. The oils tested were canola, corn, sunflower and unrefined soy oils (Free Fatty Acids (FFA< 1%)), and waste cooking oil (FFA= 9%). The quality of all biodiesel samples was studied in terms of glycerine, mono-glyceride, di-glyceride and tri-glyceride concentrations. The composition of all biodiesel samples were in the range required by ASTM D6751 and EN 14214 standards. A critical flux based on operating pressure in the reactor was reached for waste cooking and pre-treated corn oils. It was identified that the reaction residence time in the reactor was an extremely important design parameter affecting the operating pressure in the reactor. / Natural Sciences and Engineering Research Council of Canada (NSERC)

Die Kulturlandschaft und ihre Bewirtschaftung haben sich seit dem Beginn der großräumigen Intensivierungsprozesse (z.B. Meliorationen, synthetischer Düngung und Herbizidgebrauch) in den 1950/60er Jahren in Mitteleuropa dramatisch geändert. Viele der ehemaligen artenreichen Grünlandflächen wurden in den letzten Jahrzehnten beseitigt (z.B. durch Umbruch zu Acker). Dies führte zu einem allgemeinen Grünlandrückgang in Deutschland. Heute werden die meisten Ackerflächen und die restlichen Grünlandflächen sehr intensiv bewirtschaftet. Die gegenläufige Entwicklung, die Umwandlung von Äckern zu Grünland, ist eher eine regionale Erscheinung, z.B. im Hügeland oder im Zuge von Kompensationsmaßnahmen. Die Artenzusammensetzung dieser Grünländer unterscheidet sich jedoch häufig von solchen mit längerer Habitatkontinuität. Um die Effekte von solch weiträumigen Meliorationsmaßnahmen auf die Phytodiversität, die Landschaftsstruktur und die hiermit einhergehende Grünlandfragmentierung sowie deren Auswirkungen auf die Pflanzenarten des Grünlandes zu erfassen, ist es nötig, historische Daten aus den 1950er Jahren, bevor die gravierenden, ackerbaulichen Intensivierungen begannen, auszuwerten. Feucht- sowie artenreiche Frischgrünländer waren in den 1950/60er Jahren ein typischer und weit verbreiteter Habitattyp, gelten jedoch aktuell als sehr bedroht in Mitteleuropa. Wiederholungsstudien mit mehreren Untersuchungsflächen und einem Untersuchungs-zeitraum von 50-60 Jahren, der vor den weiträumigen Intensivierungen beginnt, fehlen bislang und klar verortete historische Vegetationsdaten sind selten. Obwohl der Graslandanteil in einigen Hügelregionen in Deutschland zugenommen hat ist die ökologische Qualität vieler dieser Flächen gering. Zusätzlich sind artenreiche Kalkmagerrasen als ein Relikt früherer Bewirtschaftsformen und typischer Bestandteil des Hügellandes durch Nutzungsaufgabe (Sukzession) und Nährstoffeintrag gefährdet. Das Ziel dieser Doktorarbeit war es, den Landschaftswandel und die Veränderungen im Grünland in sechs Flussauengebieten (sowie einem durch Naturschutzstatus geschützten Gebiet) und einem typischen Gebiet des Hügellandes in Norddeutschland zu untersuchen. Hierzu wurden sowohl der Grünlandanteil, die Habitatkontinuität, der aktuelle Habitattyp, der Fragmentierungsgrad als auch die Auswirkungen auf die Artenzahlen, Artenzusammensetzung und die funktionelle Diversität untersucht. Die Studien in den Flussauen basieren auf fein aufgelösten historischen Vegetationskarten und dazugehörigen Vegetationsaufnahmen aus demselben Zeitraum. In 2008 wurden diese sechs Gebiete (+1 geschütztes Gebiet) mittels einer Biotoptypenkartierung erneut erfasst. Innerhalb dieser kanpp 2800 ha (2500 + 293 ha) früherer Grünländer wurden randomisierte Punkte gelegt und zusätzlich Vegetationaufnahmen in allen aktuellen Grünländern (inklusive Sukzessionsstadien) angefertigt. Die Fallstudie (2500 ha) aus dem niedersächsischen Hügelland basiert auf aktuellen Vegetationsaufnahmen, die ebenfalls mittels randomisierter Punkte in den bestehenden Grünländern (394 ha) angefertig wurden. Zusatzdaten über z.B. die aktuelle Bewirtschaftung oder die Habitatkontinuität (Auswertung historischer Karten) wurden ebenfalls erfasst. Die erste Studie zeigte, dass die ehemaligen artenreichen Feucht- und Frischgrünländer in den ungeschützten Gebieten drastisch, um über 80% der ursprünglichen Fläche, zurückgegangen sind. Sie wurden größtenteils durch Äcker, Intensivgrünländer aber auch Brachestadien ersetzt. Bedingt durch diesen starken Flächenrückgang hat die Fragmentierung der Restflächen stark zugenommen. Die durch ein Naturschutzgebiet geschützte Untersuchungsfläche an der Havel zeigte im Vergleich relative geringe Veränderungen. Daraus lässt sich deuten, dass lokale Effekte wie Düngung oder Drainage und nicht überregionale Effekte wie Klimaerwärmung oder der Eintrag von Stickstoff durch Luft die Hauptursache für den dokumentierten Wandel sind. Die zweite Studie in den Grünländern der Auen zeigte, dass sich die Artenzusammensetzung in den letzten fünf bis sechs Jahrzehnten in allen Gebieten stark verändert hat, die Artenzahlen der Vegetationsaufnahmen um 30-50% und auch die funktionelle Diversität in ähnlichem Maße zurückgegangen sind. Die Ellenberg-Zeigerwerte (EIV) für Nährstoffverfügbarkeit sind im Vergleich zu den 1950/60er Jahren stark gestiegen und die Unterschiede zwischen den ungeschützen und dem geschützten Gebiet unterstützen ebenfalls die Annahme, dass Veränderungen größtenteils durch lokale Faktoren und nicht durch überregionale Effekte verursacht wurden. Der Trend in den ungeschützten Gebieten geht zu artenamen Grünlandgesellschaften, die von wenigen konkurrenzstarken und mahdtoleranten Arten dominiert werden. Frühblühende und auf Insektenbestäubung angewiesene Pflanzen sind stark zurückgegangen, mit entsprechenden Auswirkungen auf die Tierwelt. Die dritte Studie verknüpft den dramatischen Grünlandrückgang und die zunehmende Fragmentierung mit der Artenverarmung seit den 1950/60er Jahren. Hierfür wurden mittels definierter Kriterien eine Liste von 78 für das Feucht- und Frischgrünland charakteristischen Grünlandarten definiert, die die Grundlage für die weiteren Analysen bildeten. Die Artenzahlen auf Ebene der Vegetationsaufnahmen nahmen um 30-66% ab. Die getesteten Landschaftsstrukturmaße hatten keinen nachweisbaren Einfluss auf die Artenzahlen auf Landschaftsebene. Die Distanz zum nächstgelegenen und geeigneten Habitat für die charakteristischen Arten hatte einen geringen negativen Effekt auf die Artenzahl der Vegetationsaufnahmen. Die Ellenberg-Zeigerwerte (N, F) und die Diversitätsmaßzahlen an charakteristischen Arten weisen ebenfalls auf den Effekt der lokalen Bewirtschaftung und nicht auf Fragmentierung als treibende Kraft beim Rückgang und dem Wandel der Artengarnitur hin. Im Gegensatz zu den Untersuchungsgebieten in den Flussauen hat sich der Grünlandanteil in der Fallstudie im niedersächsischen Hügelland seit den 1950er Jahren verdoppelt. Es wurden sechs verschiedene Grünlandtypen mit einer Spanne von unter 15 bis zu deutlich mehr als 27 Arten pro Aufnahme erfasst. Die besonders artenreichen Bestände sind aber mit ca. 6% der Fläche sehr selten. Die Anzahl an insektenbestäubten Pflanzen als auch die absoluten Artenzahlen gehen mit steigender Nutzungsintensität (indiziert durch die Ellenberg-Zeigerwerte Nährstoffe (N) und Mahdtoleranz (M)) wie in den Untersuchungsgebieten in den Flussauen zurück. Artenreiche Grünländer kommen nur auf mit Schafen beweideten Flächen mit einer Habitatkontinuität von mindestens 100 Jahren vor. Grünländer mit mittleren Artenzahlen sind größtenteils auf früheren Äckern mit einer Habitatkontinuität von weniger als 30 Jahren zu finden. Die dargestellte Untersuchung hat dramatische Verluste in den Grünlandflächen der Flussauen aufgezeigt. Die Restflächen sind fragmentiert und die Artenzahlen sowie die funtionelle Diversität stark zurückgegangen. Die Fallstudie im niedersächsischen Hügelland zeigt, dass selbst in Landschaften mit hohem Grasslandanteil die ökologische Qualität von den meisten Grünländern nur noch gering ist.

A non-reactive model system comprising a highly concentrated and unstable oil-in-water emulsion was used to investigate the retention of oil by the membrane in producing biodiesel with a membrane reactor. Critical flux was identified using the relationship between the permeate flux and transmembrane pressure along with the separation efficiency of the membrane. It was shown that separation efficiencies above 99.5% could be obtained at all operating conditions up to the critical flux. It was observed that the concentration of oil in all collected permeate samples using the oil-water system was below 0.2 wt% when operating at a flux below the critical flux. Studies to date have been limited to the characterization of low concentrated emulsions below 15 vol.%. The average oil droplet size in highly concentrated emulsions was measured as 3200 nm employing direct light scattering (DLS) measurement methods. It was observed that the estimated cake layer thickness of 20 to 80 mm was larger than external diameter of the membrane tube i.e. 6 mm based on a large particle size. Settling of the concentrated emulsion permitted the detection of a smaller particle size distribution (30-100 nm) within the larger particles averaging 3200 nm. It was identified that DLS methods could not efficiently give the droplet size distribution of the oil in the emulsion since large particles interfered with the detection of smaller particles. The content of the smaller particles represented 1% of the total weight of oil at 30°C and 5% at 70°C. This was too low to be detected using DLS measurements but was sufficient to affect ultrafiltration. In order to study the critical flux in the presence of transesterification reaction and the effect of cross flow velocity on separation, various oils were transesterified in another membrane reactor providing higher cross flow velocity. higher cross flow velocity provides better separation by reducing materials deposition on the surface of the membrane due to higher shearing. The oils tested were canola, corn, sunflower and unrefined soy oils (Free Fatty Acids (FFA< 1%)), and waste cooking oil (FFA= 9%). The quality of all biodiesel samples was studied in terms of glycerine, mono-glyceride, di-glyceride and tri-glyceride concentrations. The composition of all biodiesel samples were in the range required by ASTM D6751 and EN 14214 standards. A critical flux based on operating pressure in the reactor was reached for waste cooking and pre-treated corn oils. It was identified that the reaction residence time in the reactor was an extremely important design parameter affecting the operating pressure in the reactor. / Natural Sciences and Engineering Research Council of Canada (NSERC)

A non-reactive model system comprising a highly concentrated and unstable oil-in-water emulsion was used to investigate the retention of oil by the membrane in producing biodiesel with a membrane reactor. Critical flux was identified using the relationship between the permeate flux and transmembrane pressure along with the separation efficiency of the membrane. It was shown that separation efficiencies above 99.5% could be obtained at all operating conditions up to the critical flux. It was observed that the concentration of oil in all collected permeate samples using the oil-water system was below 0.2 wt% when operating at a flux below the critical flux. Studies to date have been limited to the characterization of low concentrated emulsions below 15 vol.%. The average oil droplet size in highly concentrated emulsions was measured as 3200 nm employing direct light scattering (DLS) measurement methods. It was observed that the estimated cake layer thickness of 20 to 80 mm was larger than external diameter of the membrane tube i.e. 6 mm based on a large particle size. Settling of the concentrated emulsion permitted the detection of a smaller particle size distribution (30-100 nm) within the larger particles averaging 3200 nm. It was identified that DLS methods could not efficiently give the droplet size distribution of the oil in the emulsion since large particles interfered with the detection of smaller particles. The content of the smaller particles represented 1% of the total weight of oil at 30°C and 5% at 70°C. This was too low to be detected using DLS measurements but was sufficient to affect ultrafiltration. In order to study the critical flux in the presence of transesterification reaction and the effect of cross flow velocity on separation, various oils were transesterified in another membrane reactor providing higher cross flow velocity. higher cross flow velocity provides better separation by reducing materials deposition on the surface of the membrane due to higher shearing. The oils tested were canola, corn, sunflower and unrefined soy oils (Free Fatty Acids (FFA< 1%)), and waste cooking oil (FFA= 9%). The quality of all biodiesel samples was studied in terms of glycerine, mono-glyceride, di-glyceride and tri-glyceride concentrations. The composition of all biodiesel samples were in the range required by ASTM D6751 and EN 14214 standards. A critical flux based on operating pressure in the reactor was reached for waste cooking and pre-treated corn oils. It was identified that the reaction residence time in the reactor was an extremely important design parameter affecting the operating pressure in the reactor. / Natural Sciences and Engineering Research Council of Canada (NSERC)

<p>  </p> <p>In the pharmaceutical industry, special care must be taken by companies to guarantee high quality medications that are free from byproducts and impurities. The development process involves various considerations including solvent selection, solubility screening, unit operation selection, environmental, and health impact evaluations. Traditionally, pharmaceutical manufacturing consisted of large, centralized facilities to meet pharmaceutical demands; however, there has been a recent shift toward distributed manufacturing. With distributed manufacturing platforms, rapidly changing supply chain needs can be met regionally in addition to supplying small-volume medications and personalized medicines to hospitals and pharmacies. To produce quality pharmaceuticals, distributed manufacturing platforms should integrate digital design, novel unit operations, and process analytical technology (PAT) tools for quality monitoring and control. In this dissertation, a process design and development framework is proposed and implemented for a small-scale pharmaceutical manufacturing platform: MiniPharm.</p> <p>Various approaches to process design are detailed in this dissertation, which include heuristic-based and digital or simulation-based design. For heuristic-based design, the knowledge of the researchers was utilized to provide unit operation evaluation and screening of process alternatives. In cases when unit operations were highly complex, digital or simulation-based design was utilized to conduct sensitivity analyses and simulation-based design of experiments. With the implementation of simulation-based design, material and time needs were reduced while gaining knowledge about the system. The integration of various unit operations comes with increased understanding of start-up dynamics and operational constraints. What was found to be the most successful approach was the combination of heuristics and digital design to combine researcher knowledge and experience with the information gained from process modeling and simulation to create process alternatives that utilized system dynamics to reach desired process outcomes. </p> <p>Additionally, MiniPharm was used for process model development at the small-scale. Various software packages have been made commercially available that focus on production scale; however, models for small-scale operations are not typically implemented in these packages. Models for unit operations were fit with collected experimental data to estimate model parameters for small-scale synthesis, liquid-liquid extraction, and crystallization unit operations. The models were implemented to better capture the heat and mass transfer of the milli-fluidic scale platform, which consist of unit operations housed within microchannels. MATLAB was utilized for estimation of parameters such as kinetic rate constants and overall mass transfer coefficients. These parameters were used for design space determination and process disturbance simulation. The exploration of the impact of various process parameters on quality attributes helps researchers gain a deeper understanding about the manufacturing process and helps to demonstrate how to control the process. </p> <p>An important aspect of MiniPharm is the process development progress that has been demonstrated. With the construction of a modular and reconfigurable platform, various process alternatives can now be experimentally validated. The integration of unit operations operated at a decreased scale makes MiniPharm an example of process intensification. The implementation of integrated unit operations decreases handling time of intermediates and reduces the overall footprint for manufacturing. Designed to allow for increased flexibility of operation, perfluoroalkoxy alkane (PFA) tubing was used for synthesis and purification. With PFA tubing clean in place procedures can be implemented using continuous solvent flow or the low cost, PFA tubing can be replaced. The modular nature of the platform also allows for the investigation of individual unit operations for performance evaluation. </p> <p>Finally, a novel continuous solvent switch distillation unit operation was designed and constructed along with customized reactor and crystallizers for process alternative screening for the synthesis and purification of two compounds: Diphenhydramine hydrochloride and Lomustine. Diphenhydramine hydrochloride is a low-value, high volume allergy medication commonly found in Benadryl and Lomustine is a high-value, low volume cancer medication used to treat glioblastoma and Hodgkin Lymphoma. The production of the compounds demonstrated the flexibility of the manufacturing platform to produce both a generic and a specialty medication. A versatile platform is needed for distributed manufacturing because of quickly changing supply chain needs. Overall, this dissertation successfully demonstrates the process design, development, and simulation for small-scale manufacturing.</p>

‘Net Positive Water’ explores the capability of domestic architecture to combat the developing urban water problem. Urban intensification is contributing to the volatility of urban waters and the breakdown of the urban water cycle. Inhabitant water misuse and overconsumption is overwhelming aging municipal utilities, resulting in the decay of urban water quality. LEEDTM and The Living Building Challenge are recognized Green Building Guidelines prescribing sustainable site and building water standards. Case Studies of domestic Green Building projects will showcase water conservation to enable domestic water renewal. Net Zero Water Guidelines based on the Green Building Guidelines outline Potable and Non-Potable water use to achieve a sustainable volume of water demand at 70 litres per capita per day. Sustainable water practices are encouraged by utilizing domestic building systems to increase water value and water awareness. Time-of-Use and Choice-of-Use exposure for household water related tasks establish water savings through the use of best-performing water fixtures and appliances. Net Positive Water Guidelines will establish On-site and Building standards for sustainable harvesting and storage of water resources. Clean and Dirty water management will prescribe Passive design and Active mechanical processes to maintain best-available water quality in the urban domestic environment. Net Positive Water building typology will integrate urban inhabitation as a functional component of the urban water cycle to use, reuse, and renew water resources. The method will be tested using a Mid-rise Pilot project to deploy the necessary Passive and Active mechanisms to generate Net Positive Water quality through Net Zero Water sustainable water use. The pilot project is situated in Waterfront Toronto - The Lower Don Lands development to harness regional interests for water renewal and environmental revitalization.

‘Net Positive Water’ explores the capability of domestic architecture to combat the developing urban water problem. Urban intensification is contributing to the volatility of urban waters and the breakdown of the urban water cycle. Inhabitant water misuse and overconsumption is overwhelming aging municipal utilities, resulting in the decay of urban water quality. LEEDTM and The Living Building Challenge are recognized Green Building Guidelines prescribing sustainable site and building water standards. Case Studies of domestic Green Building projects will showcase water conservation to enable domestic water renewal. Net Zero Water Guidelines based on the Green Building Guidelines outline Potable and Non-Potable water use to achieve a sustainable volume of water demand at 70 litres per capita per day. Sustainable water practices are encouraged by utilizing domestic building systems to increase water value and water awareness. Time-of-Use and Choice-of-Use exposure for household water related tasks establish water savings through the use of best-performing water fixtures and appliances. Net Positive Water Guidelines will establish On-site and Building standards for sustainable harvesting and storage of water resources. Clean and Dirty water management will prescribe Passive design and Active mechanical processes to maintain best-available water quality in the urban domestic environment. Net Positive Water building typology will integrate urban inhabitation as a functional component of the urban water cycle to use, reuse, and renew water resources. The method will be tested using a Mid-rise Pilot project to deploy the necessary Passive and Active mechanisms to generate Net Positive Water quality through Net Zero Water sustainable water use. The pilot project is situated in Waterfront Toronto - The Lower Don Lands development to harness regional interests for water renewal and environmental revitalization.

<p>The present work is focused on the synthesis of small-scale (modular processes) to produce olefins from light alkane resources in shale gas.</p> <p>Olefins, which are widely used to produce important chemicals and everyday consumer products, can be produced from light alkanes - ethane, propane, butanes etc. Shale gas is comprised of light alkanes in significant proportion; and is available in abundance. Meanwhile, shale gas wells are small sized in nature and are distributed over many different areas or regions. In this regard, using shale gas as raw material for olefin production would require expensive transportation infrastructure to move the gas from the wells or local gas gathering stations to large central processing facilities. This is because existing technologies for natural gas conversions are particularly suited for large-scale processing. One possible way to take advantage of the abundance of shale resource for olefins production is to place small-sized or modular processing plants at the well sites or local gas gathering stations.</p> <p>In this work, new process concepts are synthesized and studied towards developing simple technologies for on-site and modular processing of light alkane resources in shale gas for olefin production. Replacing steam with methane as diluent in conventional thermal cracking processes is proposed to eliminate front-end separation of methane from the shale gas processing scheme. Results from modeling studies showed that this is a promising approach. To eliminate the huge firebox volume associated with thermal cracking furnaces and allow for a compact cracking reactor system, the use of electricity to supply heat to the cracking reactor is considered. Synthesis efforts led to the development of two electrically powered reactor configurations that have improved energy efficiency and reduced carbon footprints over and compare to conventional thermal cracking furnace configurations.</p> <p>The ideas and results in the present work are radical in nature and could lead to a transformation in the utilization of light alkanes, natural gas and shale resources for the commercial production of fuels and chemicals.</p>