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    <title>DSpace Collection:</title>
    <link>https://repositorio.ufu.br/handle/123456789/5468</link>
    <description />
    <pubDate>Fri, 17 Apr 2026 05:46:23 GMT</pubDate>
    <dc:date>2026-04-17T05:46:23Z</dc:date>
    <item>
      <title>Formulação de fluidos de perfuração sintético leves empregando esferas ocas de vidro</title>
      <link>https://repositorio.ufu.br/handle/123456789/48325</link>
      <description>Title: Formulação de fluidos de perfuração sintético leves empregando esferas ocas de vidro
Abstract: Brazil is a leading oil and gas producer in Latin America, with vast reserves and a welldeveloped infrastructure. The advancement of offshore exploration in increasingly deep waters necessitates the development of drilling fluids with enhanced properties. These fluids must be capable of balancing the pressure differential between the hydrostatic column of seawater and the geological formation while minimizing environmental impact. With the gradual depletion of reservoirs at shallow and medium depths, drilling in ultradeep water has become crucial for continued production. However, these operations demand high-performance fluids that can withstand high pressures and temperatures, in addition to complex geological formations. In this context, hollow glass microspheres (HGMs) are being studied as promising additives for drilling fluids, enabling the viability of wells with narrow pressure windows. Due to their incompressibility, these microspheres allow for a reduction in fluid density without compromising their essential rheological properties. In this study, a Central Composite Design (CCD) was conducted to evaluate the influence of key variables—such as HGM concentration, viscosifier concentration, and oil-to-water ratio (%O/W)—on the properties of synthetic drilling fluid. The properties studied included L600, L300, L200, L100, L6, L3, fluid loss, and density. The filtration mechanism of an ultra lightweight, 6.2 ppg, 100% olefinic fluid containing HGMs was also investigated. The results demonstrated the viability of applying HGMs, highlighting their potential for formulating drilling fluids in geologically complex environments.</description>
      <pubDate>Fri, 13 Feb 2026 00:00:00 GMT</pubDate>
      <guid isPermaLink="false">https://repositorio.ufu.br/handle/123456789/48325</guid>
      <dc:date>2026-02-13T00:00:00Z</dc:date>
    </item>
    <item>
      <title>Produção de carbonato de cálcio provenientes de rejeitos de minério de Irecê: estudo experimental</title>
      <link>https://repositorio.ufu.br/handle/123456789/46103</link>
      <description>Title: Produção de carbonato de cálcio provenientes de rejeitos de minério de Irecê: estudo experimental
Abstract: The concern for sustainability and industrial waste management, combined with the environmental, social, and economic demands of the sector, motivated this study on the production of CaCO₃ from fertilizer industry waste. The main objective is to reutilize lime sludge, a waste generated during the phosphate ore concentration process, and carbon dioxide (CO₂), a byproduct of ore calcination, to produce calcium carbonate. The study was conducted through a series of carbonation experiments, investigating the influence of operational variables such as solid content, CO₂ concentration, and mixing speed on reaction time and carbonate mass formation. A central composite design (CCD) was employed to optimize process conditions. The results demonstrated that increasing the CO₂ concentration from 12.5% to 30% and the solid content from 1.0% to 1.8% enhanced reaction efficiency. The optimized conditions for maximizing product yield and minimizing reaction time were a solid content of 1.75%, a mixing speed of 390 rpm, and a CO₂ concentration of 28.5%, achieving a process time of 28 minutes and a CaCO₃ mass of 13.52 g. The study confirms the technical feasibility of reusing waste materials such as lime sludge and CO₂, contributing to the development of sustainable processes aligned with circular economy principles and providing an alternative for the fertilizer industry and related sectors. This work reinforces the potential of sustainable practices in the fertilizer industry, offering an efficient solution for waste management and environmental liability reduction.</description>
      <pubDate>Thu, 27 Feb 2025 00:00:00 GMT</pubDate>
      <guid isPermaLink="false">https://repositorio.ufu.br/handle/123456789/46103</guid>
      <dc:date>2025-02-27T00:00:00Z</dc:date>
    </item>
    <item>
      <title>Avaliação da influência do espectro luminoso na produção de hidrogênio por bactérias fotossintetizantes</title>
      <link>https://repositorio.ufu.br/handle/123456789/45240</link>
      <description>Title: Avaliação da influência do espectro luminoso na produção de hidrogênio por bactérias fotossintetizantes
Abstract: Considering the environmental impacts caused by the combustion of fossil fuels, researchers have been seeking technologies for sustainable energy generation. Hydrogen is seen as a clean and non-polluting alternative, whose production can be carried out biologically through photosynthetic processes, employing photosynthetic bacteria. Some parameters are important to optimize hydrogen synthesis, and evaluating light influence on the photofermentation process is crucial. In this work, the biological production of hydrogen by photofermentation using the purple non-sulfur bacteria Rhodobacter capsulatus and Rhodospirillum rubrum was studied, using lactose from powdered whey permeate at a concentration of 10 g/L as the carbon source. Small-scale assays were conducted with 50 mL reactors, varying light sources, with cold white LEDs, infrared, and spectrum-directed LEDs. It was found that both the visible and infrared ranges produced hydrogen, however, a saturation effect was observed with the combination of the two ranges. The Tukey test was performed to evaluate which light source achieved the best performance, and it was observed that the cold white LED achieved the highest maximum productivity of 8.23 ± 0.10 mmol H2/(L.day). Large-scale assays were also carried out with a 2.1 L plate-type photobioreactor under the same conditions as the small scale, but with the LEDs that achieved the best performance in the small scale. For these assays, the maximum productivity and light conversion efficiency obtained were 10.33 mmol H2/(L.day) and 1.67% for the spectrum-directed LED, and 18.64 mmol H2/(L.day) and 3.26% for the cold white LED, respectively. The condition for large-scale was also evaluated by increasing the light intensity to 5000 lx for the cold white LED and using the revitalization system, achieving a maximum value of 26.93 mmol H2/(L.day) and 4.49% ECL.</description>
      <pubDate>Fri, 26 Jul 2024 00:00:00 GMT</pubDate>
      <guid isPermaLink="false">https://repositorio.ufu.br/handle/123456789/45240</guid>
      <dc:date>2024-07-26T00:00:00Z</dc:date>
    </item>
    <item>
      <title>Dual-function materials for hydrogen production integrated with carbon  dioxide capture and in situ conversion into syngas</title>
      <link>https://repositorio.ufu.br/handle/123456789/45129</link>
      <description>Title: Dual-function materials for hydrogen production integrated with carbon  dioxide capture and in situ conversion into syngas
Abstract: Sorption-enhanced reforming (SER) is a promising technology to produce high-purity H2 and &#xD;
efficient CO2 capture. However, the further application of the captured CO2 is still limited. In &#xD;
this work, we evaluated the sorption-enhanced steam/autothermal reforming (SESR / SEATR) &#xD;
of bioethanol for H2 production and the conversion of the captured CO2 into syngas via reverse &#xD;
water-gas shift reaction (rWGS). The bimetallic NiM/Al-CaO-based catalysts (M = Co or Cu), &#xD;
were synthesized by the sol-gel method and characterized by different techniques. The Ni/Al-&#xD;
CaO  and  NiCo/Al-CaO  catalysts  showed  similar  capture  capacities  after  20 &#xD;
carbonation/regeneration cycles, 0.28 and 0.22 g CO2/g CaO, respectively, while the NiCu/Al-&#xD;
CaO catalyst had the poorest capture capacity, 0.18 g CO2/g CaO. This poorest capture capacity &#xD;
may be related to the formation of the Ca2CuO3 phase, which being a denser phase led to a &#xD;
reduction in the specific surface area of the material and a larger CaO crystallite size, decreasing &#xD;
the adsorption of CO2. These properties also significantly impacted the SESR process, since the &#xD;
NiCu/Al-CaO performed poorly with a H2 mole fraction on a dry and inert-free basis (𝑦̅ 𝐻2) of &#xD;
~ 87%. During SESR, the Ni and NiCo catalysts presented 𝑦̅ 𝐻2 &gt; 93%, and during SEATR &#xD;
𝑦̅ 𝐻2 &gt; 95% with a pre-breakthrough period of 14 min after 10 cycles in both processes. The &#xD;
NiCo/Al-CaO catalyst showed better performance in CO2 conversion and CO selectivity of 87 &#xD;
and 97%, respectively, during rWGS after 10 SEATR cycles. Furthermore, coke deposition in &#xD;
SER was lower when compared  to conventional  processes, and O2  injection during SEATR &#xD;
further contributed to coke reduction.</description>
      <pubDate>Thu, 27 Feb 2025 00:00:00 GMT</pubDate>
      <guid isPermaLink="false">https://repositorio.ufu.br/handle/123456789/45129</guid>
      <dc:date>2025-02-27T00:00:00Z</dc:date>
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