Dissertations / Theses on the topic 'Biocrust'
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BLANCO, SACRISTAN JAVIER. "Investigation of terrain control on dryland functioning and composition using multiple remote sensing sensors and platforms." Doctoral thesis, Università degli Studi di Milano-Bicocca, 2020. http://hdl.handle.net/10281/294894.
Full textDrylands are among the most sensitive areas to actual global change and their cover will increase in the next decades. Terrain has a key role in the distribution of water and nutrients in drylands and shaping their composition. These environments are composed by vegetation and bare soil, many times colonized by biocrusts, which are expected to suffer compositional changes. Remote sensing has been highlighted as an important tool for dryland monitoring. It is a very cost-effective approach to identify biodiversity hotspots, predict changes in their composition, and to evaluate the relationships these changes have with the terrain. Using the proper image analysis according to the study case, remote sensing has proved to be useful for monitoring well differentiated drylands, but not when dryland components are mixed. Thus, the main aim of this dissertation was to study how heterogeneous dryland composition and functioning is affected by the terrain using different multiple remote sensing sensors and platforms. Data from very high spatial resolution RGB, thermal infrared, multi- and hyperspectral imagery, retrieved in the laboratory and in the field using airborne, UAV and stationary platforms were used. The next specific objectives were set: - Evaluating whether SfM techniques can be used in drylands with complex surfaces to derive their terrain from UAV imagery; - Developing a reproducible technique to relate human actions to changes in the health of dryland scarce vegetation communities by using object-based image analysis; - Testing whether the spectral heterogeneity of lichens can be used to estimate their α-diversity using hyperspectral imagery; - Developing a methodology to evaluate the control that terrain has on dryland biocrusts’ distribution using information solely retrieved from UAV; - Testing if TIR imagery can estimate soil moisture in heterogeneous drylands. This PhD thesis comprises an evaluation of SfM techniques at different scales and their applicability at different levels. It also comprises a novel methodology to monitor vegetation in a ground-water dependent ecosystem, where their health is key for the ecosystem’s functioning. Moreover, the application of close-range hyperspectral imagery allowed to estimate the α-diversity of biocrust-forming lichens using their spectral diversity. This led to a better understanding of the spectral behaviour of biocrusts depending on their composition and allowed to develop a methodology to produce accurate maps of land cover in a dryland ecosystem of heterogeneous composition and to relate the effect of terrain atrributes on dryland composition.
Bahr, Jason R. "Exploring Post-Fire Recovery of Biocrusts and Desert Ecosystem Services." BYU ScholarsArchive, 2013. https://scholarsarchive.byu.edu/etd/4285.
Full textGuo, Meina. "Aggregation and biological processes in ion-adsorption rare earth mine tailings under natural restoration and reclamation approaches." Electronic Thesis or Diss., Université de Lorraine, 2022. http://www.theses.fr/2022LORR0301.
Full textIon-adsorption REE deposits are one of the main reservoirs of REEs worldwide, mainly distributing in southern China. In the past decades, the production of REEs has caused serious environmental damage and left over a large area of tailings which continuously threaten the surrounding environment. The main obstacles for ecological restoration of such tailings are poor physical structure, low nutrients, high pollution of REEs and Al. These unfavourable factors hinder the colonization of organisms and the restoration of ecosystem services. Therefore, how to restore the structure and function of soil and ecosystem has become a major issue. Natural succession and phytoremediation provide an option for restoration of mine tailings. However, so far less is understood in terms of the mechanisms of soil formation and ecological succession of REE tailings under different strategies. Therefore, the objectives of this thesis are to: 1) study the evolution mechanism of structure and function of tailing soils and ecosystem in natural succession; 2) study the restoration effects of various phytoremediation strategies; and 3) assess the soil and ecological environment quality under natural succession and phytoremediation. The main findings are as follows. (1) In natural succession of a 15-year chronosequence, soil and ecological functions are significantly increasing over time. There are three completely different evolution patterns (i.e. visual bare, biocrust and vascular vegetation) in the early stage of succession. The evolution between biocrusts and vascular plants occurs from the initial mutual promotion to the later competition. The formation of large aggregates (> 0.25 mm) is mainly controlled by the electrostatic interaction of minerals and biological activities, which improves the diversity of microorganisms and accumulation of nutrients, and controls the migration of REEs. (2) The macroaggregates associated with biocrusts (BC) and with vascular plant root soils (RS) show different morphologies, that is, longitudinal stratification of biocrust and interlacement within the rhizosphere. Both BC and RS are significantly enriched in nutrients. The highest REE concentration is observed in BC while the lowest is found in RS, suggesting that REEs could be redistributed among different horizons by biotic processes. Interestingly, autotrophic microorganisms are more concentrated in the BC, while heterotrophic rhizosphere growth-promoting bacteria are preferentially distributed in the RS. These results show that, although in the same site, the mechanism of soil formation and recovery of soil function under different evolution patterns are quite different. (3) In consideration of time and efficiency, different phytoremediation strategies (i.e. amendment and plantation of pioneer plant Miscantus sinensis and commercial grasses) were conducted by a plot experiment. Compared with bare tailings, the addition of amendment induces a significant increase in nutrients, promotes the formation of macroaggregates, and reduces the availability of REEs. In addition, phytoremediation introduces nitrogen fixing bacteria (e.g. Burkholderia), which change the biological characteristics of tailings and promote nutrient cycling. Our results have proved the effectiveness and sustainability of the amendment input. Nevertheless, the plant effect is not significantly visible within only a 16 month-experiment in this study. In conclusion, this research shows that nature, as an “engineer”, is uninterruptedly improving the soil and ecological environment quality, while phytoremediation efforts can significantly enhance the soil and ecological environment function but the effect weakens with time, which requires longer-term observation
Taghipour, Alireza. "Fractional distillation of hydrothermal liquefaction Biocrude." Thesis, Queensland University of Technology, 2021. https://eprints.qut.edu.au/213838/1/Alireza_Taghipour_Thesis.pdf.
Full textRutherford, William A., Thomas H. Painter, Scott Ferrenberg, Jayne Belnap, Gregory S. Okin, Cody Flagg, and Sasha C. Reed. "Albedo feedbacks to future climate via climate change impacts on dryland biocrusts." NATURE PUBLISHING GROUP, 2017. http://hdl.handle.net/10150/623195.
Full textKristianto, Ivan. "Nitrogen Analysis of Biocrude Oil Derived From Carbohydrates and Proteins." Thesis, The University of Sydney, 2021. https://hdl.handle.net/2123/27211.
Full textObeid, Farah. "Nitrogen in HTL microalgae biocrude: Production, engine performance and emissions." Thesis, Queensland University of Technology, 2019. https://eprints.qut.edu.au/135304/1/Farah_Obeid_Thesis.pdf.
Full textGuzman, Jonathan. "Process Design and Technical feasibility analysis of Catalytic fas tpyrolysis for biocrude production." Thesis, KTH, Materialvetenskap, 2018. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-224532.
Full textEfterfrågan om förnyelsebara bränslen ökar. Catalytic Fast Pyrolysis är en växande teknologisom skulle kunna förse med bio-crude av hög kvalité för att användas med dagensinfrastruktur. Den process som valdes för att implementera denna teknologi är in-situcirculating fluidized bed med sågspån som inmatning. Två fall blev utformade och sedanmodellerade i ASPEN Plus. Det första fallet använder sig av ånga som flödare och andrafallet använder sig av återvunnen pyrolysgas. Båda fallen var självförsörjande med endastbiomassa som energikälla. Enligt parameterstudien stämmer detta endast för biomassa medmindre än 40% fuktinnehåll.
Longhin, Francesco. "Electrocatalytic hydrogenation of biocrude from hydrothermal liquefaction: focus on palmitic acid as model compound." Master's thesis, Alma Mater Studiorum - Università di Bologna, 2021. http://amslaurea.unibo.it/24416/.
Full textPeterson, Benjamin L. "Development and Optimization of a Produced Water, Biofilm Based Microalgae Cultivation System for Biocrude Conversion with Hydrothermal Liquefaction." DigitalCommons@USU, 2018. https://digitalcommons.usu.edu/etd/7237.
Full textRamos, Tercero Elia Armandina. "LARGE SCALE PRODUCTION OF BIOCRUDE FROM MICROALGAE: EXPERIMENTAL MEASUREMENTS AND PROCESS SIMULATIONS TO ASSESS ITS ECONOMIC VIABILITY." Doctoral thesis, Università degli studi di Padova, 2015. http://hdl.handle.net/11577/3424656.
Full textI biocarburanti provenienti da biomassa microalgale sono considerati come una delle alternative migliori e più a breve termine per produrre energia pulita. Le microalghe sono microorganismi capaci di convertire l’energia solare in energia chimica che può essere sfruttata come combustibili di diverse tipologie sia liquida sia gassosa. L’obiettivo della ricerca presentata in questa Tesi é di valutare il potenziale della tecnologia per la produzione di olio da microalghe, analizzando diverse alternative e concetti sia in modo sperimentale che tramite simulazioni del processo. Il Capitolo 1 é una discussione introduttiva sulla situazione mondiale delle microalghe, recenti studi e gli ultimi risultati riportati su questa tecnologia. Dal punto di vista sperimentali, nei Capitoli 2 e 3 di questa tesi si sono approfonditi, la coltivazione di microalghe in acque reflue e la capacità che presentano alcune specie di microalghe di crescere in acque reflue non trattate, verificata con la microalga Chlorella protothecoides. La crescita é stata valutata in acque provenienti da diversi step del di trattamento delle acque, per selezionare la stream ottimale per la crescita delle microalghe. Inoltre, é stata testata la efficienza nella rimozione di nutrienti e i tassi di rimozione in acque reflue reali. Nel Capitolo 2 si riportano anche la produzione di biomassa in stato stazionario con alimentazione continua del effluente. Nel Capitolo 3 sono stati studiati gli effetti della temperatura, l’irradiazione in ciclo giorno/notte e la competizione batterica sulla crescita di C. protothecoides, e la rimozione dei nutrienti con l’obiettivo d’integrare entrambe tecnologie in un approccio realistico. É stato infine proposto uno schema modificato dell’impianto di depurazione. Il Capitolo 4 presenta il lavoro sperimentale per la valutazione della capacità di produzione di biogas da microalghe e le loro velocità di degradazione nel processo di digestione anaerobica: sono state testate diverse condizioni come la tipologia del’inoculo batterico e la concentrazione della biomassa algale all’inizio delle prove. Inoltre, questo capitolo riporta anche la ricerca nel recupero del contenuto energetico dalla biomassa residua dopo l’estrazione di olio, dimostrando che il metodo di estrazione dell’olio é un fattore importante. La produzione di biogas e sua corrispondente frazione di metano sono stati testati considerando l’effetto della miscela di solvente usato nella estrazione, e i risultati sono stati confrontati con quelli della biomassa microalgale prima della estrazione. Il Capitolo 5 é focalizzato sulla conversione di biomassa mediante il processo di liquefazione idrotermica (HTL) che viene svolto a temperature tra 200 C e 375 C (la pressione é quella necessaria per mantenere l’acqua in stato liquido), ed é caratterizzato da alte rese. Tuttavia, uno dei sottoprodotti é una fase acquosa con alto contenuto di componenti organici che deve essere trattata adeguatamente per evitare ulteriori costi. In questo capitolo si riporta il lavoro sperimentale svolto con l’obiettivo di recuperare e riutilizzare l’acqua di processo mediante un riciclo nel sistema stesso. Inoltre si é misurato l’effetto della temperatura e del numero di ricicli nelle rese di produzione di olio, gas, residuo solido e la fase acquosa e la composizione dei prodotti. Nel Capitolo 6 si riporta l’analisi energetica del processo per la produzione di biocrudo: lo studio é stato svolto considerando diverse tipologie e condizioni di processo, i quali sono stati modellati e simulati dal simulatore di processo Aspen PlusTM, col fine di verificare e ottimizzare i profitti energetici rispetto all’analisi del EROEI, e di proporre un processo energeticamente autosufficiente. Dei diversi processi studiati per ottenere energia della biomassa quello che utilizza la combustione di biomassa dopo estrazione dell’olio é risultato il più favorevole in termini energetici. In particolare, due casi di questo processo sono stati confrontati con un caso base, variando la provenienza dei requisiti energetici (calore ed elettricità), fornendoli sia da fonti esterne che dal processo steso. In ultimo, nel Capitolo 7 si riporta una valutazione tecnica di un impianto per la produzione di biodiesel da microalghe in cui si propone una nuova configurazione della sezione di crescita, un fotobioreattore ibrido, il Closed Pond Reactor (CPR). L’intero processo é stato simulato Aspen PlusTM e ottimizzato per ottenere i migliori benefici in termini energetici. La progettazione e il dimensionamento delle attrezzature tecnologiche sono stati effettuati per ottenere una stima realistica dei costi, considerando sia CAPEX (costi di capitale) e OPEX (costi operativi). Nell’analisi economica si é valutata, la redditività del processo su scala industriale e sono stati calcolati i prezzi di vendita corrispondenti dell’olio e del biodiesel necessario per rendere la produzione economicamente sostenibile.
Ramirez, Jerome Luigi A. "Modelling a commercial-scale bagasse liquefaction plant using ASPEN Plus." Thesis, Queensland University of Technology, 2018. https://eprints.qut.edu.au/120019/1/Jerome_Ramirez_Thesis.pdf.
Full textHossain, Md Farhad. "Experimental investigation of thermochemically-derived fuels in a diesel engine." Thesis, Queensland University of Technology, 2018. https://eprints.qut.edu.au/115545/1/Md.%20Farhad_Hossain_Thesis.pdf.
Full text"Biocrust Responses to Altered Precipitation Regimes." Doctoral diss., 2020. http://hdl.handle.net/2286/R.I.62843.
Full textDissertation/Thesis
Doctoral Dissertation Microbiology 2020
"Microbial Restoration Ecology of Biological Soil Crusts." Doctoral diss., 2019. http://hdl.handle.net/2286/R.I.53653.
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Doctoral Dissertation Liberal Studies 2019
"Rates of Lateral Expansion of Biological Soil Crusts." Master's thesis, 2017. http://hdl.handle.net/2286/R.I.44262.
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Masters Thesis Biology 2017
Olarra, Jennifer A. "Biological soil crusts in forested ecosystems of southern Oregon : presence, abundance and distribution across climate gradients." Thesis, 2012. http://hdl.handle.net/1957/36077.
Full textGraduation date: 2013
Yan, Penghui. "Hydrodeoxygenation of biocrude oil to value-added products." Thesis, 2020. http://hdl.handle.net/1959.13/1411892.
Full textThe utilisation of biomass has drawn widespread attention due to the fast depletion of fossil energy resources and environmental challenges. Biocrude oil, derived from pyrolysis or liquefaction of lignocellulosic biomass, contains a high level of oxygen leading to some detrimental properties (high viscosity, high corrosivity, low heating value and low thermal stability). Therefore, hydrodeoxygenation of the biocrude is necessary to remove the oxygen atoms and produce value-added fuels and chemicals. Hydrodeoxygenation (HDO) is a two-step process which involves the hydrogenation and deoxygenation. The hydrogenation commonly occurs in the presence of metal sites, and the acid sites play a crucial role in the deoxygenation. Therefore, the HDO catalysts are routinely composed of metals (such as Pt, Pd, Ru, and Ni) and supports (ZrO₂, Al₂O₃ and zeolites). Due to the complexity of biocrude oil, a model compound (guaiacol), which possesses two different oxygen-containing groups, was employed in this study. In the first step, the Ru/BEA and Ru/ZSM-5 with varied Si/Al ratios were studied to examine the influence of supports with varying acidity and pore size on HDO of biocrude oil and guaiacol in a batch-type reactor operated at 4.0 MPa hydrogen. It was observed that a decrease in the Si/Al ratio of the support generated an increase in the yield of cyclohexane and a decrease in the yield of 2-methoxycyclohexanol in HDO of guaiacol. Both Ru/BEA and Ru/ZSM-5, possessing low Si/Al ratios, displayed a high activity for HDO for guaiacol while only Ru/BEA catalyst exhibits a high activity for HDO of biocrude oil. Catalyst characterisation shows that the Ru/BEA catalyst, with a low Si/Al ratio, not only possesses strong B acid sites but also contains extensive mesoporosity. Notably, these mesopores appear to facilitate the hydrogenation, deoxygenation, and ring-opening of large oxygenated and condensed-ring hydrocarbons in biocrude oil which then leads to a high yield of cycloalkanes. As expected, the Ru/Al₂O₃ and Ru/SiO₂ catalysts exhibit a high hydrogenation activity but a low deoxygenation activity in the HDO of guaiacol and biocrude oil due to the absence of B acid sites. These results suggest that the larger pore support, with strong B acid sites, engendered the observed HDO activity. The reaction pathway for the main components of biocrude oil was proposed based on the observed reaction product distribution. Although Ru-based catalysts display a high HDO activity, the high cost could hinder their wide application in industry. Therefore, metallic Ni, which is low cost, non-sulfided, and has the advantage of high hydrogenation activity was employed as the main metal phase in this project. The influence of catalyst pore size and shape selectivity on the catalytic hydrodeoxygenation (HDO) of biocrude oil has been investigated by comparing the activity of nickel catalysts on the supports of different pore sizes towards model compounds of increasing dimension. Five model compounds (guaiacol, anisole, phenanthrene, pyrene, and 1,3,5-trimethoxybenzene), and five zeolite supports (small-pore ZSM-5, medium-pore MOR, large-pore Beta and Y, and mesoporous Al-MCM-41) have been investigated. Hydrodeoxygenation and hydrogenation activities were determined on the basis of the yield of the associated cycloalkanes. All catalysts show a high HDO activity for small molecules (anisole and guaiacol) while the catalysts with medium and large pore supports display high HDO activity for 1,3,5-trimethoxybenzene. Furthermore, the large pore catalysts (Ni/Y and Ni/Beta) exhibit high hydrogenation activity for phenanthrene, while only the extra-large pore size catalyst (Ni/Y) presents good hydrogenation and HDO activities for all model compounds. The mesoporous Ni/Al-MCM-41 catalyst shows low HDO and hydrogenation activities for large model compounds, which can be ascribed to its low metal dispersion and low concentration of acid sites. In addition, the Ni/Beta and Ni/ZSM-5 were also tested in HDO of biocrude oil. Ni/Beta catalyst displays a higher yield of cycloalkanes than that of Ni/ZSM-5, which confirms that the selection of catalyst support can have impact on the product distribution in HDO of biocrude. The BEA supported Ni catalyst, which possesses high concentration of acid sites and mesopores, displays a high HDO activity for guaiacol and biocrude oil, however, results from batch reactor cannot provide the information about turnover frequency of active sites. Therefore BEA zeolite, with different Si/Al ratios (12.5, 25, 175) and varying metal loadings (2.3 ~23.4 wt%), was studied in a flow reactor to examine the influence of catalyst acidity and the structure of Ni on the performance, with particular emphasis on the change in product selectivity. The ratio of cyclohexane formation rate to the concentration of acid sites in reduced catalysts was found to be roughly constant when HDO of guaiacol in a flow reactor over 15.7 wt% Ni/BEA catalysts with different acid site concentrations, demonstrating the deoxygenation activity increases with increasing number of acid sites. On the other hand, the materials with the majority of isolated Ni sites (prepared by ion exchange) showed no cyclohexane yield at 230 degree. However, at higher temperatures, the formation of cyclohexane was observed, as a result of a consecutive reaction where catechol was generated by acid sites and subsequently reduced to cyclohexane on isolated Ni sites. With respect to catalysts with higher Ni-loading, the selectivity towards cyclohexane increases with an increased Ni loading up to 15.7 wt%. This is attributed to the formation of larger Ni nanoparticles upon H₂ reduction. A higher concentration of nickel hydrides compared to isolated Ni sites was observed by H₂-TPD and H₂-FTIR. The nickel hydrides are believed to be crucial intermediates in the hydrogenation reaction. Based on the product distribution over catalysts containing mainly isolated Ni sites and the Ni nanoparticles, two different reaction pathways were proposed. Traditionally, catalysts with high metal loadings are indispensable for improved catalytic performance. Supported metal catalysts are typically prepared by incipient wetness impregnation, which inevitably gives rise to inhomogeneous metal distribution and leads to large metal particles formed via agglomeration. Therefore, highly dispersed Ni/BEA catalysts prepared via ion-exchange-deposition-precipitation (IDP) utilising careful pH control were conducted. In comparison, catalysts prepared by incipient wetness impregnation (IWI) and deposition-precipitation (DP) methods were also investigated and IDP catalysts were shown to have higher dispersion. A significantly increased selectivity toward hydrocarbons was observed over these carefully prepared catalysts. The presence of nickel hydrides was confirmed by H₂-TPD and H₂-FTIR. IDP catalyst exhibits a higher metal dispersion and higher concentration of nickel hydrides than impregnated and DP catalysts, while larger Ni nanoparticles formed in impregnated catalysts show a higher concentration of nickel hydrides per surface Ni. The guaiacol conversion was not significantly affected by the catalyst preparation method, while the product selectivity was altered. Higher cyclohexane formation rate was detected over IDP catalysts compared to DP and impregnated catalysts. Besides, cyclohexane formation rate presents a positive linear correlation with the concentration of nickel hydrides, suggesting nickel hydrides play a crucial role in the hydrodeoxygenation reaction. The factors affecting catalyst deactivation during HDO in a continuous-flow reactor were investigated in order to gain insight into the deactivation mechanism of BEA-supported Ni catalyst. Phenolic-OH group moieties accelerate catalyst deactivation through the production of condensed-ring compounds, which then leads to the blockage of pores. In contrast, the yield of cycloalkane did not change with time-on-stream when using toluene, cyclohexanol and anisole as feeds, suggesting aromatic-ring, alkyl-OH and aromatic-OCH₃ have negligible effect on catalyst deactivation. Operation at low weight hour space velocity (WHSV) values increase the yield of cycloalkane and reduce the rate of catalyst deactivation. High metal loadings can increase selectivity to cyclohexane, however, the production of condensed-ring products is also enhanced, which is likely to be the result of an increased concentration of surface cyclohexane carbocations. Furthermore, high metal loadings play a limited role in preventing the catalyst from deactivation. In addition, the activity and stability of catalysts were positively affected by an increase in reaction temperature (up to 230°C). Based on the product distribution observed, a coupling reaction pathway (leading to the formation of condensed-ring products and cycloalkanes) is proposed.
Roque, Jessica Pina. "Characterization of cyanobacterial strains isolated from Portuguese soil/soil biocrusts and a first insight into this community." Master's thesis, 2021. https://hdl.handle.net/10216/139400.
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