<p>  </p> <p>Protecting crops from disease requires continuous research because plant pathogen incidence, geographical range, and pathogenicity, are constantly shifting variables as agronomic practices and climate continue to evolve. The objectives of this research are to i.) evaluate field-scale fungicide timing programs for corn (<em>Zea mays L.</em>) diseases at multiple locations in Indiana; ii.) evaluate field-scale fungicide timing programs for soybean (<em>Glycine Max</em> (L.) Merr.) diseases at multiple locations in Indiana; iii.) continue to identify, document, and confirm the distribution of populations of the soybean frogeye leaf spot pathogen (<em>Cercospora sojina)</em> that contain the G143A mutation conferring resistance to quinone outside inhibitor (QoI) fungicides in Indiana; and iv.) assess the incidence, severity, and prevalence of tar spot (<em>Phyllachora maydis</em>) in Indiana. For the first and second objectives, field scale trials were established at three locations in Indiana from 2019 to 2022. No application timings at any location provided significant yield protection for corn or soybeans. To achieve the third objective, 165 isolates of <em>C. Sojina </em>were tested. In total, 24 out of the 32 counties sampled in 2021 and 2022 were documented with QoI-resistance. The fourth objective was accomplished by surveying Indiana counties for incidence and severity of tar spot. As of 2022, 86 out of 92 Indiana counties have been confirmed for the presence of tar spot.</p>

No description available.

Under våren 2021 upptäcktes förhöjda halter av polyaromatiska kolväten (PAH) i Björklinges dricksvattennät. Då ett vattenprov taget hos användare påvisade halter som låg över Livsmedelsverkets gränsvärden och källan till föroreningen inte identifierats, rekommenderades hushållen i Björklinge att inte använda kranvattnet till mat och dryck under en period. Efter sektionering av nätet och provtagning identifierades en äldre, nyligen reparerad, ledningssträcka av gjutjärn som trolig föroreningskälla. Denna typ av ledning är relativt vanligt förekommande i delar av Uppsala Vattens nät. Syftet med denna studie var att få en djupare förståelse för orsakerna till PAH-föroreningen i Björklinge och bedöma risken för att liknande föroreningar ska hända igen, samt att tillhandahålla ett beslutsunderlag för Uppsala Vattens hantering av äldre gjutjärnsledningar.En litteraturstudie genomfördes och data från Björklinge analyserades. Resultaten av litteraturstudien visade att frisättning av PAH från äldre gjutjärnsrör med korrosionsskydd innehållande stenkolstjära eller bitumen är ett välkänt fenomen. Biofilmen har en skyddande effekt och graden av frisättning kan därför påverkas av faktorer som klorering eller syrehalt i vattnet. Även mekaniskt slitage i form av reparationsarbete och tryckvågor kan leda till förhöjda nivåer av PAH. Korrosion av ledningarna är troligen också en viktig faktor.Utifrån litteraturstudien och resultaten från användarprover tagna i Björklinge respektive Skuttunge kunde det konstateras att problemen i Björklinge hade ett samband med frisättning av PAH från gjutjärnsrör. Vid tidpunkten för studien kunde ökande PAH-halter observeras på vissa platser i ledningsnätet även efter ledningsbytet i Björklinge våren 2021, vilket tydde på fortsatt kontaminering. Inga uppmätta halter i användarprover låg dock över något av Livsmedelsverkets gränsvärden och PAH i dricksvattnet anses inte vara ett stort hälsomässigt problem i dagsläget. Det är däremot viktigt att fortsätta monitorera halterna av PAH i Uppsala Vattens nät då denna typ av problem kan uppstå igen. Man bör också vara försiktig med åtgärder som kan påverka biofilmen samt vara återhållsam med spoling av denna typ av ledningar. De ledningar som identifierats som föroreningskällor bör åtgärdas. Med tanke på ledningarnas stigande ålder, begränsad kunskap om PAH och dess hälsoeffekter, samt WHOs rekommendationer bör man dock initiera ett långsiktigt arbete med att byta ut eller renovera denna typ av ledningar i Uppsala Vattens nät. / During the spring of 2021 elevated levels of polyaromatic hydrocarbons (PAH) were discovered in the drinking water supply network of Björklinge. Levels above the limit set by the Swedish Food Agency were observed in one user sample, which led to the inhabitants of Björklinge being recommended not to use the tap water for drinking or cooking while the source of the contamination was being identified. After sectioning and sampling the network, an older, recently repaired cast iron pipe was identified as the probable source of the contamination. This type of pipe is not uncommon in the drinking water network of Uppsala Vatten. The purpose of this study was to gain a deeper understanding of the causes of the PAH contamination in Björklinge and to determine the risk of similar contaminations happening again. Further, it aimed to provide a basis for future decisions regarding the handling of older cast iron pipes in the drinking water network of Uppsala Vatten.A literature study was done and data from Björklinge was analysed. The results of the literature study showed that the release of PAH from older cast iron pipes with coal tar or bitumen coating is a well-known phenomenon. The biofilm has protective properties, and the degree of PAH release can hence be affected by factors such as chlorination or oxygen concentration of the water. Mechanical wear in the form of repair work or pressure waves can also cause increased levels of PAH in the water.Based on the literature study as well as the results from the user samples of Björklinge and Skuttunge, it could be determined that the PAH contamination in Björklinge was related to the release of PAH from old cast iron pipes. At the time of this study, increasing levels of PAH could be observed in some parts of the drinking water network even after the suspected pipes had been replaced during the spring of 2021. This might indicate that the contamination was still ongoing. However, no samples were above the limits set by the Swedish Food Agency and PAH is currently not considered a major health problem. Despite this, it is important to keep monitoring the levels of PAH in the drinking water since the PAH levels might increase again. It is also important to be careful with measures that might affect the biofilm and when flushing cast iron pipes. The pipes that have already been identified as sources of contamination should be replaced. Given the increasing age of the cast iron pipes, the limited knowledge of PAH and its health effects, as well as the recommendations from the WHO, a long-term plan for how to remove or renovate this type of pipes from the drinking water network of Uppsala Vatten should be initiated.

Canada has the second largest proven oil reserves next to Saudi Arabia which is mostly located in Alberta and Saskatchewan but is unconventional heavy oil and bitumen. The tar sands are found at the surface and are mined, yet 80% of the 173 billion barrels of heavy oil and bitumen exist in-situ according to the Canadian Association of Petroleum Producers (CAPP). Two factors inhibit the economic extraction and processing of Canadian heavy oil; its enormous viscosity ranging from 1000 to over 1 million mPa.s and the asphaltene content (high molecular weight molecules containing heavy metals and sulphur). Heavy oil and bitumen were only included in the reserves estimates through the efforts of Canadian enhanced oil recovery (EOR) research. Viscosity reduction is the one common element of in-situ methods of heavy oil recovery with the exception of cold production. Currently, steam assisted gravity drainage (SAGD) and cyclic steam stimulation (CSS) are being used commercially in the field where the oil’s viscosity is reduced by injecting steam. Thermal methods are energy intensive requiring vast volumes of water such that any improvement would be beneficial. Solvent extraction is one alternative requiring no water, the solvent is recoverable and reusable, and depending on the mode of operation the heavy oil is upgraded in-situ. Vapour Extraction (VAPEX) and enhanced solvent extraction (N-SolvTM) are two such methods. VAPEX and N-Solv reduce the bitumen’s viscosity via mass transfer and a combination of mass and heat transfer, respectively. A light hydrocarbon solvent (instead of steam) is injected into an upper horizontal well where the solvent mixes with the heavy oil, reduces its viscosity and allows the oil to drain under gravity to a bottom production well. The idea of using solvents for heavy oil extraction has been around since the 1970s and both VAPEX and N-Solv are patented processes. However, there is still much to be learned about how these processes physically work. Research to date has focused on varying system parameters (including model dimensions, permeability, heavy oil viscosity, solvent type and injection rate, etc.) to observe the effect on oil production from laboratory scale models. Based on an early mass balance model by Butler and Mokrys (1989) and an improvement by Das (1995), molecular diffusion alone cannot account for the produced oil rates observed from laboratory models. Until recently, very little progress had been made towards qualifying and quantifying the mass transfer mechanisms with the exception of the diffusivity of light hydrocarbons in heavy oil. Mass transfer can only be by diffusion and convection. Differentiating and quantifying the contribution of each is complex due to the nature and viscosity of the oil. The goal of this thesis is to investigate the mass transfer mechanisms during the solvent recovery of heavy oil. Quantifying the diffusion of light hydrocarbon solvents has been an active topic of research with limited success since the mid 1990’s. The experimental approach presented here focused on capturing the rate of solvent mass transfer into the bitumen by measuring the bitumen swelling and the butane uptake independently. Unlike early pressure decay methods, the pressure is held constant to not violate the assumed equilibrium solvent concentration at the interfacial boundary condition. The high solubility of solvent in heavy oil complicates the physical modeling because simplifying assumptions of a constant diffusion coefficient, constant density and a quiescent liquid should not be used. The model was developed from first principles to predict the bitumen swelling. The form of the concentration dependent diffusivity was assumed and the diffusivity coefficients initially guessed. The swelling (moving boundary) was fixed by defining a new dimensionless space coordinate and the set of partial differential equations solved using the method of lines. Using the non-linear regression (lsqnonlin) function in MATLAB®, optimising for the difference in predicted and experimentally found bitumen heights and independently validating the result using the solvent uptake, the diffusivity of butane in heavy oil (at 25oC) was found to be Dsb = 4.78 x 10-6ωs + 4.91 x 10-6 cm2/s where ωs is the solvent mass fraction. Diffusion alone has proven inadequate in predicting oil recovery rates from laboratory scale models. It is logical to assume that convective mass transfer plays a role at mixing the solvent and bitumen while draining via gravity through the reservoir porous matrix. Solvent extraction experiments were conducted in etched glass micromodels to observe the pore scale phenomena. The pore scale mechanisms were found to differ depending on how the solvent extraction was operated, with non-condensing (VAPEX) or condensing (N-SolvTM) solvent. Observations show increased convective mixing and an increased rate of interface advancement when the solvent condenses on the bitumen surface. Evidence of trapped butane vapour being mobilised with the draining live oil and a technique of observing solvent extraction using UV light confirm that the draining live oil is on average one pore deep. While the interface appears from a distance to be uniform, at the pore scale it is not. Live oil can drain from one to two pores via capillary displacement mechanisms in one section of the interface and via film flow only in another area (James and Chatzis 2004; James et al. 2008). This work also shows the detrimental impact of having a non-condensable gas present during solvent extraction (James and Chatzis 2008). In summary, this work emphasises the mass transfer and drainage displacement mechanisms of non-condensing (VAPEX) and condensing (N-Solv) solvent extraction methods of heavy oil recovery.

Canada has the second largest proven oil reserves next to Saudi Arabia which is mostly located in Alberta and Saskatchewan but is unconventional heavy oil and bitumen. The tar sands are found at the surface and are mined, yet 80% of the 173 billion barrels of heavy oil and bitumen exist in-situ according to the Canadian Association of Petroleum Producers (CAPP). Two factors inhibit the economic extraction and processing of Canadian heavy oil; its enormous viscosity ranging from 1000 to over 1 million mPa.s and the asphaltene content (high molecular weight molecules containing heavy metals and sulphur). Heavy oil and bitumen were only included in the reserves estimates through the efforts of Canadian enhanced oil recovery (EOR) research. Viscosity reduction is the one common element of in-situ methods of heavy oil recovery with the exception of cold production. Currently, steam assisted gravity drainage (SAGD) and cyclic steam stimulation (CSS) are being used commercially in the field where the oil’s viscosity is reduced by injecting steam. Thermal methods are energy intensive requiring vast volumes of water such that any improvement would be beneficial. Solvent extraction is one alternative requiring no water, the solvent is recoverable and reusable, and depending on the mode of operation the heavy oil is upgraded in-situ. Vapour Extraction (VAPEX) and enhanced solvent extraction (N-SolvTM) are two such methods. VAPEX and N-Solv reduce the bitumen’s viscosity via mass transfer and a combination of mass and heat transfer, respectively. A light hydrocarbon solvent (instead of steam) is injected into an upper horizontal well where the solvent mixes with the heavy oil, reduces its viscosity and allows the oil to drain under gravity to a bottom production well. The idea of using solvents for heavy oil extraction has been around since the 1970s and both VAPEX and N-Solv are patented processes. However, there is still much to be learned about how these processes physically work. Research to date has focused on varying system parameters (including model dimensions, permeability, heavy oil viscosity, solvent type and injection rate, etc.) to observe the effect on oil production from laboratory scale models. Based on an early mass balance model by Butler and Mokrys (1989) and an improvement by Das (1995), molecular diffusion alone cannot account for the produced oil rates observed from laboratory models. Until recently, very little progress had been made towards qualifying and quantifying the mass transfer mechanisms with the exception of the diffusivity of light hydrocarbons in heavy oil. Mass transfer can only be by diffusion and convection. Differentiating and quantifying the contribution of each is complex due to the nature and viscosity of the oil. The goal of this thesis is to investigate the mass transfer mechanisms during the solvent recovery of heavy oil. Quantifying the diffusion of light hydrocarbon solvents has been an active topic of research with limited success since the mid 1990’s. The experimental approach presented here focused on capturing the rate of solvent mass transfer into the bitumen by measuring the bitumen swelling and the butane uptake independently. Unlike early pressure decay methods, the pressure is held constant to not violate the assumed equilibrium solvent concentration at the interfacial boundary condition. The high solubility of solvent in heavy oil complicates the physical modeling because simplifying assumptions of a constant diffusion coefficient, constant density and a quiescent liquid should not be used. The model was developed from first principles to predict the bitumen swelling. The form of the concentration dependent diffusivity was assumed and the diffusivity coefficients initially guessed. The swelling (moving boundary) was fixed by defining a new dimensionless space coordinate and the set of partial differential equations solved using the method of lines. Using the non-linear regression (lsqnonlin) function in MATLAB®, optimising for the difference in predicted and experimentally found bitumen heights and independently validating the result using the solvent uptake, the diffusivity of butane in heavy oil (at 25oC) was found to be Dsb = 4.78 x 10-6ωs + 4.91 x 10-6 cm2/s where ωs is the solvent mass fraction. Diffusion alone has proven inadequate in predicting oil recovery rates from laboratory scale models. It is logical to assume that convective mass transfer plays a role at mixing the solvent and bitumen while draining via gravity through the reservoir porous matrix. Solvent extraction experiments were conducted in etched glass micromodels to observe the pore scale phenomena. The pore scale mechanisms were found to differ depending on how the solvent extraction was operated, with non-condensing (VAPEX) or condensing (N-SolvTM) solvent. Observations show increased convective mixing and an increased rate of interface advancement when the solvent condenses on the bitumen surface. Evidence of trapped butane vapour being mobilised with the draining live oil and a technique of observing solvent extraction using UV light confirm that the draining live oil is on average one pore deep. While the interface appears from a distance to be uniform, at the pore scale it is not. Live oil can drain from one to two pores via capillary displacement mechanisms in one section of the interface and via film flow only in another area (James and Chatzis 2004; James et al. 2008). This work also shows the detrimental impact of having a non-condensable gas present during solvent extraction (James and Chatzis 2008). In summary, this work emphasises the mass transfer and drainage displacement mechanisms of non-condensing (VAPEX) and condensing (N-Solv) solvent extraction methods of heavy oil recovery.

Der Einfluss des Biofilms, der Inkrustation, der Fließgeschwindigkeit und der Wasserqualität auf die Freisetzung von PAK wurde in Batch-, Drehkolbenreaktorversuchen und an einem Rohrleitungssystem untersucht. Chlorung von tauchgeteerten Edelstahlcoupons mit Biofilm führten zu einer fast vollständigen Ablösung des Biofilms und einer Zunahme der Freisetzung von Fluoren, Phenanthren und Fluoranthen. Die PAK-Freisetzung von tauchgeteerten Edelstahlcou-pons in einer Lösung von Trinkwasser mit 0,1% Natriumazid als Hemmstoff der Atmungskette, der den Biofilm nicht ablöst, führten zu einer Zunahme aller untersuchten PAK in der gleichen Größenordnung wie ohne Bio-film. In chloriertem Teerleachat wurden unter der teilweisen Anwendung einer einfachen Methode der kontinu-ierlichen Extraktion folgende PAK-Derivate analysiert: Chloracenaphthen, 1-Chlorpyren, 9-Fluorenon, Anthron. Da Reaktionsprodukte von Phenanthren und Fluoranthen nicht gefunden werden konnten, wird eine Weiterreaktion zu 9-Fluorenon vorgeschlagen, die durch die Pechoberfläche katalysiert wird. Instationäre Korrosion und nicht vorhandener aerober Abbau sind die Gründe für eine PAK-Zunahme während Stagnationphasen. / The influence of biofilm, encrustation, flow velocity and water quality on the release of PAHs was investigated in batch, continuously flown reactor experiments and in a pipe rig system. Chlorination of coal-tar coated stainless steel slides with biofilm resulted in an almost complete removal of the biofilm and an increase of the release of fluorene, phenanthrene and fluoranthene. PAH release of coal-tar coated stainless steel slides exposed to a solution of drinking water with 0,1% sodium azide as an inhibitor of the respiratory chain which did not remove the biofilm led to an increase of all observed PAHs up to the same magnitude as without biofilm. In chlorinated coal-tar leachate the following derivatives were detected while partly utilizing an easy method for a continuously extrac-tion: chloroacenaphthene, 1-chloropyrene, 9-fluorenone, anthrone. While reaction products of phenanthrene and fluoranthene could not be found a further reaction to 9-fluorenone catalysed by the coal-tar surface is proposed. Instationary corrosion and no aerobic degradation are the reasons for PAH increase during stagnation periods.

Reliable energy supply is a major concern and crucial for development of the global society. To address the dependency on fossil fuel and the negative effects of this reliance on climate, there is a need for a transition to cleaner sources. An attractive solution for replacing fossil-based products is renewable substitutes produced from biomass. Gasification and pyrolysis are two promising thermochemical conversion technologies, facing challenges before large-scale commercialization becomes viable. In case of biomass gasification, tar is often and undesired by-product. An attractive option to convert tar into syngas is nickel-based catalytic steam reforming (SR). For biomass pyrolysis, catalytic SR is in early stages of investigation as a feasible option for bio-crude conversion to syngas. The focus of the thesis is partly dedicated to describe research aimed at increasing the knowledge around tar reforming mechanisms and effect of biomass-derived impurities on Ni-based tar reforming catalyst downstream of gasifiers. The work focuses on better understanding of gas-phase alkali interaction with Ni-based catalyst surface under realistic conditions. A methodology was successfully developed to enable controlled investigation of the combined sulfur (S) and potassium (K) interaction with the catalyst. The most striking result was that K appears to lower the sulfur coverage and increases methane and tar reforming activity. Additionally, the results obtained in the atomistic investigations are discussed in terms of naphthalene adsorption, dehydrogenation and carbon passivation of nickel. Furthermore, the thesis describes research performed on pyrolysis gas pre-conditioning at a small-industrial scale, using an iron-based catalyst. Findings showed that Fe-based materials are potential candidates for application in a pyrolysis gas pre-conditioning step before further treatment or use, and a way for generating a hydrogen-enriched gas without the need for bio-crude condensation. / Tillförlitlig energiförsörjning är en stor utmaning och avgörande för utvecklingen av det globala samhället. För att ta möta beroendet av fossil råvara och de negativa effekter som detta beroende medför för klimatet finns ett stort behov av en övergång till renare energiråvaror. En attraktiv lösning är att ersätta nuvarande fossil råvara med produkter från biomassa. Förgasning och pyrolys är två lovande teknologier för termokemisk omvandling av biomassa. Kommersialisering av dessa teknologier är inte helt problemfritt. I fallet förgasning så behöver, bl.a. oönskade tyngre kolväten (tjära) hanteras innan den producerade orenade produktgasen kan användas i syntesgastillämpningar. Ett effektivt alternativ för detta är gaskonditionering vid höga temperaturer, baserade på katalytisk ångreformering med en nickelkatalysator. Katalytisk ångreformering är en möjlig teknik för omvandling av bioråvara, producerad från pyrolys av biomassa, till syntesgas. Avhandlingen fokuserar delvis på att beskriva den forskning som utförts för att öka kunskapen kring mekanismer för tjärreformering och effekterna av föroreningar från biomassan på en nickelkatalysator nedströms förgasare. Arbetet bidrar till en bättre förståelse av hur alkali i form av kalium (K) i gasfasen upptas, jämviktas och växelverkar med ytan hos nickelkatalysatorn under fullt realistiska förhållanden. Inledningsvis utvecklades en metod för att möjliggöra kontrollerade studier av den kombinerade effekten av S och K, vilken inkluderar exakt dosering av alkali till en produktgas, eliminering av transienter i katalysatoraktiviteten samt katalysatorkarakterisering. Det mest lovande resultatet är att K både sänker ytans svavelinnehåll och ökar aktiviteten för omvandlingen av metan och tjära. För att ytterligare fördjupa kunskaperna i mekanismerna för tjärnedbrytning utfördes experimentella och teoretiska ytstudier på en enkristallnickelyta med naftalen som modellförening. Resultat avseende naftalenadsorption, dehydrogenering av naftalen och kolpassivering av nickelytan diskuteras. Därutöver så beskriver avhandlingen den forskning som utförts inom förkonditionering av pyrolysgas med en järnkatalysator för varsam deoxygenering av biooljan och vätgasproduktion. Detta utfördes vid en småskalig industriell anläggning. De experimentella studierna visar att den undersökta järnkatalysatorn resulterar i en vätgasberikad gas och att den är en potentiell kandidat för tillämpning i ett förkonditioneringssteg. / <p>QC 20170830</p>

Der Einfluss des Biofilms, der Inkrustation, der Fließgeschwindigkeit und der Wasserqualität auf die Freisetzung von PAK wurde in Batch-, Drehkolbenreaktorversuchen und an einem Rohrleitungssystem untersucht. Chlorung von tauchgeteerten Edelstahlcoupons mit Biofilm führten zu einer fast vollständigen Ablösung des Biofilms und einer Zunahme der Freisetzung von Fluoren, Phenanthren und Fluoranthen. Die PAK-Freisetzung von tauchgeteerten Edelstahlcou-pons in einer Lösung von Trinkwasser mit 0,1% Natriumazid als Hemmstoff der Atmungskette, der den Biofilm nicht ablöst, führten zu einer Zunahme aller untersuchten PAK in der gleichen Größenordnung wie ohne Bio-film. In chloriertem Teerleachat wurden unter der teilweisen Anwendung einer einfachen Methode der kontinu-ierlichen Extraktion folgende PAK-Derivate analysiert: Chloracenaphthen, 1-Chlorpyren, 9-Fluorenon, Anthron. Da Reaktionsprodukte von Phenanthren und Fluoranthen nicht gefunden werden konnten, wird eine Weiterreaktion zu 9-Fluorenon vorgeschlagen, die durch die Pechoberfläche katalysiert wird. Instationäre Korrosion und nicht vorhandener aerober Abbau sind die Gründe für eine PAK-Zunahme während Stagnationphasen. / The influence of biofilm, encrustation, flow velocity and water quality on the release of PAHs was investigated in batch, continuously flown reactor experiments and in a pipe rig system. Chlorination of coal-tar coated stainless steel slides with biofilm resulted in an almost complete removal of the biofilm and an increase of the release of fluorene, phenanthrene and fluoranthene. PAH release of coal-tar coated stainless steel slides exposed to a solution of drinking water with 0,1% sodium azide as an inhibitor of the respiratory chain which did not remove the biofilm led to an increase of all observed PAHs up to the same magnitude as without biofilm. In chlorinated coal-tar leachate the following derivatives were detected while partly utilizing an easy method for a continuously extrac-tion: chloroacenaphthene, 1-chloropyrene, 9-fluorenone, anthrone. While reaction products of phenanthrene and fluoranthene could not be found a further reaction to 9-fluorenone catalysed by the coal-tar surface is proposed. Instationary corrosion and no aerobic degradation are the reasons for PAH increase during stagnation periods.

Introduction: Les personnes vivant avec le VIH (PVVIH) présentent des risques accrus d’ostéoporose et de lipodystrophie. Peu d’études se sont penchées sur l’association entre les déterminants du style de vie, le risque d’ostéoporose et le risque de lipodystrophie chez les PVVIH. Objectifs: L’objectif primaire était d’évaluer l’association entre l’ostéoporose, la lipodystrophie ainsi que différents déterminants du style de vie chez les PVVIH. Méthodologie: Tous les participants de la Cohorte canadienne VIH et vieillissement (CCVV) avec des données sur la densité minérale osseuse (DMO), mesurée par absortiométrie biphotonique à rayons X (DXA), ont été inclus dans cette étude transversale. Les déterminants du style de vie d’intérêt étaient : le revenu annuel, le niveau d’éducation, l’exercice physique ainsi que les consommations d’alcool, de tabac et de drogues illicites. Les covariables mesurées incluaient l’historique complet de la médication antirétrovirale, les comorbidités, les co-infections, la charge virale, le compte de CD4+ au recrutement et le compte de CD4+ nadir. L’ostéoporose a été définie par un score T de -2.5 ou moins. La lipodystrophie, évaluée par la composition corporelle via DXA, a été définie par un fat mass ratio (rapport des pourcentages de gras entre le tronc et les membres inférieurs) supérieur à 1.33 pour les femmes et 1.96 pour les hommes. Les rapports des cotes et les intervalles de confiance à 95% (IC95%) au recrutement ont été estimés en utilisant des régressions logistiques multivariées. Résultats: Nous avons inclus 547 PVVIH (âge médian 55 ans, 88% d’hommes) et 97 contrôles séronégatifs au VIH (âge médian 54 ans, 54% d’hommes). L’ostéoporose était présente chez 13% des PVVIH et 6% des contrôles (OR 2.21, IC 95% [0.96 – 6.06]). La lipodystrophie était présente chez 138 (28.3%, IC 95% 24.3 – 32.3%) des 487 PVVIH avec des données sur la disposition du gras corporel. Aucun des déterminants du style de vie était associé à l’ostéoporose ou à la lipodystrophie. Par contre, les covariables associées à un risque accru d’ostéoporose étaient l’âge avancé, un indice de masse corporelle (IMC) réduit et la co-infection à l’hépatite C. Les covariables associées au risque accru de lipodystrophie étaient l’âge avancé, l’hypertension, l’exposition prolongée aux antirétroviraux, ainsi que les expositions prolongées aux inhibiteurs nucléosidiques de la transcriptase inverse (INTI) et aux inhibiteurs de l’intégrase (INI). Conclusion: Aucune association n’a été décelée entre les déterminants du style de vie étudiés et l’ostéoporose ou la lipodystrophie. / Background: As a consequence of ART, people living with HIV (PLWH) are at higher risk for osteoporosis and lipodystrophy. However, the risk may also be influenced by lifestyle factors, but few studies have explored the association between modifiable lifestyle factors and the risk of osteoporosis or lipodystrophy in the PLWH population. Objectives: Our primary objective was to evaluate the lifestyle factors in relation to the risks of osteoporosis and lipodystrophy in a PLWH-based cohort. Methods: We conducted a cross-sectional analysis of data from the Canadian HIV and Aging Cohort Study (CHACS). We included all participants with available bone mineral density T-scores, which were measured by dual-energy X-ray absorptiometry (DXA) scans. Lifestyle risk factors of interest included annual income, education level, alcohol intake, tobacco use, illicit drug use and physical exercise. Other covariates considered were full antiretroviral medication history, medical comorbidities, coinfections, viral load, nadir CD4+ and current CD4+ count. Osteoporosis was defined by a T-score of -2.5 or lower at any of the measured sites. Lipodystrophy was assessed on whole body DXA and defined as a fat mass ratio (the ratio between trunk and lower limbs fat mass) greater than 1.33 for women and 1.96 for men. Baseline prevalence odds ratios (ORs) and 95% confidence intervals (95% CIs) were estimated by multivariate logistic regressions. Results: We included 547 PLWH (median age 55 years, 88% males) and 97 HIV-uninfected controls (median age 57 years, 64% males). Osteoporosis was present in 13.0% of PLWH (95% CI 10.2 – 15.8%) and 6% of controls (95% CI 1.4 – 11.0%); the OR of osteoporosis for HIV seropositivity was 2.21 (95% CI [0.96 – 6.06]). Lipodystrophy was found in 138 (28.3%, 95% CI 24.3 – 32.3%) of the 487 PLWH for which a fat mass ratio (FMR) was available. None of the lifestyle factors of interest were associated with osteoporosis or lipodystrophy. However, covariates associated with an increased risk of osteoporosis were increasing age, lower body mass index (BMI) and hepatitis C coinfection. Covariates associated with an increased risk of lipodystrophy were older age, hypertension, longer antiretroviral duration, and longer exposure to nucleoside reverse transcriptase inhibitors (NRTIs) and integrase strand inhibitors (INSTIs). Conclusion: No association was found between any of the lifestyle factors of interest and osteoporosis or lipodystrophy.

No description available.