Academic literature on the topic 'Biomasse granulari'
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Journal articles on the topic "Biomasse granulari"
Lima, Jéssyca De Freitas, Elivânia Vasconcelos Moraes dos Santos, Heraldo Antunes Silva Filho, José Tavares de Sousa, and Adrianus Cornelius Van Haandel. "AVALIAÇÃO DA SEDIMENTABILIDADE DE BIOMASSA GRANULAR E FLOCULENTA EM SISTEMAS DE LODO ATIVADO." HOLOS 3 (July 3, 2014): 319. http://dx.doi.org/10.15628/holos.2014.1916.
Full textHernández, A. E., L. C. Belalcazar, M. S. Rodríguez, and E. Giraldo. "Retention of granular sludge at high hydraulic loading rates in an anaerobic membrane bioreactor with immersed filtration." Water Science and Technology 45, no. 10 (May 1, 2002): 169–74. http://dx.doi.org/10.2166/wst.2002.0321.
Full textPires, Danilo Prado, Julio César Benatti, and Edson Aparecido Abdul Nour. "Desenvolvimento de lodo granular aeróbio em reatores em batelada sequencial com baixa velocidade de sedimentação." Engenharia Sanitaria e Ambiental 26, no. 6 (December 2021): 1015–24. http://dx.doi.org/10.1590/s1413-415220200180.
Full textBeltrame Benatti, Julio César, Pedro Menuzzo de Almeida Prado, and Edson Aparecido Abdul Nour. "Desenvolvimento de lodo granular aeróbio em reatores em batelada sequencial utilizando esgoto sanitário e baixas taxas de aeração." Revista DAE 68, no. 227 (October 21, 2020): 6–19. http://dx.doi.org/10.36659/dae.2020.078.
Full textGrgas, Dijana, Tibela Landeka Dragičević, Anita Štrkalj, Andrijana Brozinčević, Adelina Ladavac, Tea Štefanac, and Mirjana Galant. "Aerobni granulirani mulj u obradi otpadnih voda." Hrvatski časopis za prehrambenu tehnologiju, biotehnologiju i nutricionizam 16, no. 1-2 (June 1, 2021): 20–27. http://dx.doi.org/10.31895/hcptbn.16.1-2.3.
Full textPronk, Mario, Andreas Giesen, Andrew Thompson, Struan Robertson, and Mark van Loosdrecht. "Aerobic granular biomass technology: advancements in design, applications and further developments." Water Practice and Technology 12, no. 4 (December 1, 2017): 987–96. http://dx.doi.org/10.2166/wpt.2017.101.
Full textZitomer, Daniel H., Metin Duran, Richard Albert, and Engin Guven. "Thermophilic aerobic granular biomass for enhanced settleability." Water Research 41, no. 4 (February 2007): 819–25. http://dx.doi.org/10.1016/j.watres.2006.11.037.
Full textCarrera, P., A. Mosquera-Corral, R. Méndez, J. L. Campos, and A. Val del Rio. "Pulsed aeration enhances aerobic granular biomass properties." Biochemical Engineering Journal 149 (September 2019): 107244. http://dx.doi.org/10.1016/j.bej.2019.107244.
Full textSaha, Shaswati, Jo De Vrieze, Rima Biswas, and Tapas Nandy. "In situammonia removal by methanogenic granular biomass." Environmental Science: Water Research & Technology 4, no. 4 (2018): 559–68. http://dx.doi.org/10.1039/c7ew00444c.
Full textDai, Jianjun, and John R. Grace. "Biomass granular screw feeding: An experimental investigation." Biomass and Bioenergy 35, no. 2 (February 2011): 942–55. http://dx.doi.org/10.1016/j.biombioe.2010.11.026.
Full textDissertations / Theses on the topic "Biomasse granulari"
Dai, Jianjun. "Biomass granular feeding for gasification and combustion." Thesis, University of British Columbia, 2007. http://hdl.handle.net/2429/31282.
Full textApplied Science, Faculty of
Chemical and Biological Engineering, Department of
Graduate
Isanta, Monclús Eduardo. "Towards granular biomass implementation for urban wastewater treatment." Doctoral thesis, Universitat Autònoma de Barcelona, 2014. http://hdl.handle.net/10803/284924.
Full textGranular biomass has been proposed as an alternative to activated sludge for the sewage treatment. The morphological characteristics of granular biomass, provides granules two main advantages over flocular biomass: (i) the ability of settling faster, and (ii) the possibility of performing aerobic, anoxic and anaerobic processes simultaneously. Two different granular systems have a demonstrated potential for the treatment of urban wastewater. First, aerobic granular sequencing batch reactors (GSBR), which perform the same nutrient removal process occurring in activated sludge systems, but taking advantage of the abovementioned granular sludge properties. Second, an anammox-based sewage treatment, which could allow obtaining a more sustainable (energy-neutral or even energy-positive) wastewater treatment. This thesis is focused in improving the knowledge of these granular biomass systems towards confirming granular biomass as a real alternative to urban wastewater treatment with activated sludge. For urban wastewater treatment with GSBRs, two different studies were done. First, the stability of granules and their performance at pilot scale were first studied in a 100 L GSBR treating low-strength wastewater for simultaneous carbon, nitrogen and phosphorus removal was operated for eleven months. Mature granules prevailed in the GSBR during a period of five months. The biological nitrogen removal with mature granules was mainly performed via nitrite. Nitrification efficiency was higher than 75% and occurred simultaneously with denitrification during the aerobic phase of the GSBR. A progressive accumulation of P-salts (probably apatite), was found from days 150 to 300, which could enhance the destabilization of granules at the end of the experimental period. Second, a model-based study was carried out to determine the guidelines to design an automatic control strategy with the final aim of enhancing biological N-removal in a GSBR. Specific simulations were designed to elucidate the effect of DO concentration, granule size, influent C/N ratio and NLR on the nitrification-denitrification efficiency. Simulation results showed that, in general, high N-removal efficiencies (from 70 to 85 %) could be obtained only setting the appropriate DO concentration. That appropriate DO concentration could be easily found based on effluent ammonium concentration. Those results were used to propose a control strategy to enhance N-removal efficiencies. Regarding the anammox-based sewage treatment in a two-step system, two additional studies were carried out. For the partial nitritation step, a bench-scale granular sludge bioreactor was operated in continuous mode with a low nitrogen concentration wastewater at low temperatures. An effluent suitable to feed a subsequent anammox reactor was maintained stable during more than 450 days, including more than 365 days at temperatures equal or lower than 15ºC. A previously existing mathematical model was used to determine why partial nitritation was feasible. Simulations showed that NOB was only effectively repressed when their oxygen half-saturation coefficient was higher than that of AOB. Simulations also indicated that a lower specific growth rate of NOB was maintained at any point in the biofilm due to the bulk ammonium concentration imposed through the control strategy. Finally, pyrosequencing technique was used to explore the microbial community structure changes during the recovery process of an anammox granular reactor after a temperature shock. The temperatures shock reduced the nitrogen removal rate up to 92% compared to that just before the temperature shock, and it took 70 days to recover a similar nitrogen removal rate to that before the temperature shock. Pyrosequencing results indicated that microbial diversity in the reactor decreased as the reactor progressively recovered from the temperature shock. In general, pyrosequencing results were in agreement with N-removal performance results and SAA measured in the reactor during the recovery process. An anammox specific primer was used to precisely determine the anammox species in the biomass samples.
Woolley, Sylvia. "Aerobic granular biomass using municipal primary effluent : a comparative monitoring study." Thesis, University of British Columbia, 2017. http://hdl.handle.net/2429/63114.
Full textApplied Science, Faculty of
Civil Engineering, Department of
Graduate
Salmistraro, Marco. "Mainstream deammonification reac-tor at low DO values and employing granular biomass." Thesis, KTH, Mark- och vattenteknik, 2015. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-180284.
Full textManas, Llamas Angela. "Immobilisation du phosphore par précipitation induite dans un procédé aérobie à biomasse granulaire." Thesis, Toulouse, INPT, 2011. http://www.theses.fr/2011INPT0122/document.
Full textOver the last decade, aerobic granulation processes have araised as a promising technology for treating wastewater effluents containing high nitrogen, phosphorus and carbon concentrations. The microbial complexity of granules and the mechanisms by which they acquire excellent settleability properties, still constitute important research goals to investigate. This thesis is focused on a mechanism that has been little addressed in literature, that is, phosphate precipitation in the core of aerobic granules. Different analytical techniques, sometimes adapted for the first time to this type of systems, like Raman spectroscopy, have let an exhaustive characterization of biominerals in the core of granules. Analyses performed on aerobic granules grown with synthetic fed in a lab-scale SBR (Sequential Batch Reactor), revealed a calcium phosphate core made of hydroxyapatite [Ca5(PO4)3(OH)]. This precipitation phenomenon is induced by local pH and supersaturation gradients issued of biological reactions inside granules. The study of the biomineralization phenomenon has been extended into anaerobic granules coming from UASB reactors at different cheese wastewater treatment plants. A physico-chemical model has been described in a form of matrix with AQUASIM® software, and coupled with a thermodynamic database (PHREEQC®), in an attempt to hypothesize the mechanisms that influence the biomineralization phenomena. It has been proposed the formation of an amorphous precursor (ACP) prior hydroxyapatite precipitation in the core of granules, suggesting the thermodynamic constant (pKsp|20ºC=28.07±0.58) and kinetic constants at different operating conditions. It has been also estimated the contribution of the biomineralization to the overall phosphorus removal process (up to 46% at the operating conditions tested), thanks to the development and study of a GSBR (Granular Sludge Batch Reactor) in labscale, for more than 900 days. The fate of the biomineralization process in granules, regarding the contribution to their stabilization and physical properties, has been also dealt in this thesis. The reactor stability and performances have been assessed by alternating anoxic/aerobic and anaerobic/aerobic cycles, in sights of a future industrial application. The induction of precipitation by local variation of pH and supersaturation issued of biological reactions has been here introduced, although it will need further investigation
Zimmer, Thiago Ruiz. "Influência da carga orgânica e do tempo de enchimento sobre o desempenho do reator anaeróbio em batelada seqüencial com biomassa granulada tratando soro de queijo." Universidade de São Paulo, 2006. http://www.teses.usp.br/teses/disponiveis/18/18138/tde-14092006-222626/.
Full textThe effect of volumetric organic load (VOL) and fill time on the stability and efficiency of an ASBR was assessed. The ASBR containing granular biomass was operated in batch and fed-batch mode and treated diluted cheese whey. Assays were performed at 30 'degrees' C with total medium volume of 5.0 liters and 8-h cycle lengths. In a first stage the reactor was operated batch-wise with fill time ('T IND.feed') of 10 min and agitation frequency of 150 rpm. At each cycle 2.0 liters of medium were fed at influent concentration ('C IND.infl') of 1000, 2000, 4000 and 6000 mg/L, in terms of COD. Alkalinity supplementation was gradually optimized from 100% to 25% of 'NA'H'CO IND.3'/COD ratio. At these conditions the reactor attained stability at applied VOL of 4.8 g/L.d, alkalinity supplementation of 25% and organic matter removal efficiency of 96.0% and 98.4% in terms of soluble and total COD, respectively. In a second stage due to operational problems devices were developed to assure biomass retention and hence make fed-batch operation feasible. The tested devices included hybrid ASBR, agitation system with two impellers: helix and inclined blade impeller (a) and helix and inclined turbine impeller (b). The system chosen was the helix and inclined turbine. With this configuration agitation frequency and biomass volume were reduced to 75 rpm and 1.0 L, respectively. This way, it was possible to assess feed strategies ('T IND.feed') of 360, 180 and 10 minutes at constant applied VOL of 2.4 g/L.d, for 'C IND.infl' of 4000 mg/L at 'V IND.feed' of 1.0 L and for 'C IND.infl' of 8000 mg/L at 'V IND.feed' of 0.5 L. At 'C IND.infl' of 4000 mg/L increase in 'T IND.feed' resulted in decrease in efficiency in terms of soluble COD, which amounted to 97.8, 96.7 and 94.5% for 'T IND.feed' of 10, 180 and 360 minutes, respectively. At 'C IND.infl' of 8000 mg/L the increase in 'T IND.feed' resulted in lower values for COD effluent
Michelan, Rogério. "Influência do tipo de impelidor sobre o desempenho do reator anaeróbio em batelada seqüencial com biomassa granulada tratando esgoto sintético." Universidade de São Paulo, 2006. http://www.teses.usp.br/teses/disponiveis/18/18138/tde-13092006-092030/.
Full textThe effect of flow type and rotor speed were investigated in a round-bottom reactor with 5 L useful volume containing granular biomass and treating synthetic wastewater with organic load of 800 mgCOD.'L POT.-1'. Five impellers have been used to this end, namely: turbine and paddle with six-vertical-flat blade, turbine and paddle with six-45 degrees-inclined-flat-blade and helix, commonly used in biological processes. Utilization of a draft tube together with the helix and six-alternately-inclined-flat-blade impellers was also assessed as a means to improve mixing and consequently mass transfer in the reaction medium. Results showed that altering impeller type and variation in rotor speed did not exert significant effect on the stability and performance of the investigated systems. However, analysis of the first order kinetic model constants showed that alteration in rotor speed resulted in increase in the values of the constants, demonstrating that increase in rotor speed improves solid-liquid mass transfer in the reaction medium. Analysis of the kinetic constants also showed that axial flow in mechanically stirred reactors is preferable over radial flow when the vertical flat blade impeller is compared to the inclined flat blade impeller. The presence of the draft tube showed significant improvement in mass transfer, which could be seen by the increase in the values of the constants used in the fit of the first order kinetic model to the experimental values. The power consumed was less than 1.6.'10 POT.-3' HP/'M POT.3' at rotor frequency below 200 rpm and the axial impellers consumed 75% less power than the radial ones
Matos, Talita de Santana. "Avalia??o da efici?ncia agron?mica de novos fertilizantes nitrogenados granulados baseados no uso da ureia." Universidade Federal Rural do Rio de Janeiro, 2011. https://tede.ufrrj.br/jspui/handle/jspui/1272.
Full textMade available in DSpace on 2016-10-10T17:18:18Z (GMT). No. of bitstreams: 1 2011 - Talita de Santana Matos.pdf: 652723 bytes, checksum: 16c30eb83b6db70231ab44534e188e6c (MD5) Previous issue date: 2011-10-31
Coordena??o de Aperfei?oamento de Pessoal de N?vel Superior - CAPES
A study was conducted to evaluate the agronomic efficiency of nitrogen fertilizer with slow-release urea, measuring their losses by volatilization of NH3-N, N2O emission and recovery of fertilizer nitrogen applied as top dressing compared with commercioal urea to corn crop. All experiments were conducted at Embrapa Agrobiology. Firstly, the experiments were performed under controlled conditions in a greenhouse using soil layer of 0-10 cm of a haplic planosol. In the first experiment, the plastic trays were used as experimental units for evaluation of losses due to volatilization chambers with the aid of semi-open static free (SALE). Commercial urea was applied (UC), urea + KCl (UK), humic acid + urea (UH), urea + zeolitic sandstone (UZ) and urea + gypsum (UG) in two conditions of pH (5.4 and 6,5). Secondly, the other experiment was conducted using plastic pots containing the same soil samples as experimental units where they were planted three plants of Brachiaria decumbens. In this case, fertilizers were enriched with 15N, in two pH conditions too (pH 5,4 and 6,5). Treatments UZ and UK were more efficient in retaining N in the soil than the UC, with smaller losses through volatilization of NH3-N, and 20,2 and 15,8% on condition of lime and 22 and 17,2% when Liming did not occur, respectively. The UK fertilizer and UG showed overall increase of about 149 and 146% on dry biomass production at the end of the cycle on condition of pH 5,4. At pH 6,5 UG fertilizer showed yield increases of 149,3%. The accumulation of N in the plant and was 279,2 and 270,3 mg N.vaso-1 when no lime was applied to the UK and UG treatments, respectively, and the limed, 207.4 and 200,6 mg N. vaso-1 for the treatments UG and UH, respectively. Treatments UZ and UK had the highest recovery of applied N by plants, with values of 65,5 and 61,9% without lime, 60,2 and 45,7% with lime, respectively. Thirdly, other experiment was conducted at the experimental field at Embrapa Agrobiology in order to quantify the PNV, N2O emissions and efficiency of nitrogen fertilizer use (NFUE) slow-release by a corn crop on N balance Treatments consisted of field application of nitrogen fertilizers in coverage along the rows and a control treatment. Emissions of N2O were evaluated using static chambers closed. Was used fertilizers enriched with 15N in little plots for the assessment of NFUE. The treatments UZ and UK reduced the losses of N-NH3 by volatilization in approximately 18 and 14%, respectively. These losses corresponded to 32,3 and 35,7% of total N applied to soil. For N2O emissions the UK treatment showed the largest emission of N2O losses reaching values of 2.02 kgN.ha-1. The highest yield of grain were obtained by treatments that UG and UZ had a better response of grain production reaching values of 9666 and 9940 kg ha-1 respectively. To NFUE treatment UZ showed the highest values of N recovered reaching 67% of the total N applied system soil plant.
O trabalho objetivou avaliar a efici?ncia agron?mica de fertilizantes nitrogenados de libera??o lenta baseados no uso da ureia, quantificando suas perdas por volatiliza??o de NNH3 (PNV), emiss?o de N2O e a recupera??o do N-fertilizante aplicado em cobertura em compara??o com a ureia comercial na cultura de milho. Todos os esperimentos foram conduzidos na Embrapa Agrobiologia. Os primeiros experimentos foram realizados em condi??es controladas em casa de vegeta??o, utilizando solo da camada de 0-10 cm de um Planossolo H?plico. No primeiro experimento foram usadas bandejas pl?sticas como unidades experimentais para avalia??o das perdas por volatiliza??o com aux?lio de c?maras semi-aberta livre est?tica (SALE). Aplicou-se ureia comercial (UC), ureia + KCl (UK), ureia + ?cido h?mico (UH), ureia +arenito zeol?tico (UZ) e ureia +gesso agr?cola (UG) em duas condi??es de pH (5,4 e 6,5). O outro experimento utilizou vasos pl?sticos contendo amostras do mesmo solo como unidades experimentais onde foram plantados 3 plantas de Brachiaria decumbens. Neste caso os fertilizantes foram enriquecidos com 15N, tamb?m em duas condi??es de pH (pH 5,4 e 6,5). Os tratamentos UZ e UK foram mais eficientes na reten??o do N no solo do que a UC, apresentando menores perdas por volatiliza??o de N-NH3 de 20,2 e 15,8% sob condi??o de calagem e 22 e 17,2% quando sem calagem, respectivamente. Os fertilizantes UK e UG apresentaram aumento total de aproximadamente 149 e 146% na produ??o de biomassa seca ao final do ciclo da cultura em condi??o de pH 5,4. Em pH 6,5 o fertilizante UG apresentou aumento de rendimento de 149,3%. O ac?mulo de N na planta foi de 279,2 e 270,3 mg N.vaso-1 quando n?o foi aplicado calagem para os tratamentos UK e UG, respectivamente e quando com calagem, 207,4 e 200,6 mg N.vaso-1 para os tratamentos UG e UH, respectivamente. Os tratamentos UZ e UK apresentaram maior recupera??o pelas plantas do N aplicado, com valores de 65,5 e 61,9% sem calagem e 60,2 e 45,7% com calagem, respectivamente. O outro experimento foi realizado no campo na ?rea experimental da Embrapa Agrobiologia com objetivo de quantificar as perdas por volatilza??o de am?nio, as emiss?es de N2O e a efici?ncia do uso de fertilizantes nitrogenados (EUFN) de libera??o lenta pela cultura de milho, no balan?o de N. Os tratamentos consistiram da aplica??o no campo em cobertura dos fertilizantes nitrogenados ao lado da linha de plantio e um tratamento controle. As emiss?es de N2O foram avaliadas utilizando-se c?maras est?ticas fechadas. Foi utilizado fertilizantes enriquecidos com 15N em microparcelas para a avalia??o da EUFN. Os tratamentos UZ e UK reduziram as perdas de N-NH3 por volatiliza??o em aproximadamente 18 e 14%, respectivamente. Estas perdas corresponderam a 32,3 e 35,7% do total de N aplicado no solo. Para as emiss?es de N2O o tratamento UK foi o que apresentou maiores perdas por emiss?o de N2O atingindo valores de 2,02 kg N.ha-1. As maiores produtividades de gr?o foram obtidas pelos tratamentos UG e UZ que apresentaram melhor resposta de produ??o de gr?os atingindo valores de 9.666 e 9.940 kg.ha-1, respectivamente. Para EUFN o tratamento UZ apresentou o maior valor de N recuperado chegando a 67% do total do N aplicado no sistema solo-planta.
Sguanci, Sara [Verfasser], and Dr Ing Dockhorn Thomas [Akademischer Betreuer] Prof. "Granular biomasses for biological treatment of breeding wastewater / Sara Sguanci ; Betreuer: Thomas Prof. Dr.-Ing. Dockhorn." Braunschweig : Technische Universität Braunschweig, 2015. http://d-nb.info/1175818178/34.
Full textMockaitis, Gustavo. "Redução de sulfato em biorreator operado em batelada e batelada alimentada seqüenciais contendo biomassa granulada com agitação mecânica e Draft-Tube." Universidade de São Paulo, 2008. http://www.teses.usp.br/teses/disponiveis/18/18138/tde-03122008-141204/.
Full textThis present work evaluate an anaerobic sequencing batch reactor (ASBR), fed in batch and fed-batch, and cycles of 8 hours, using granulated biomass and mechanical stirring in a draft-tube, fed with synthetic wastewater (500 mgCOD/L), enriched with sulfate in some COD/[\'SO IND.4\'POT.2-\'] relations. In all operations the reactor showed a stable operation, producing alkalinity and maintaining the volatile acids in adequate levels. Considering the fed periods of 10 min, 3 h and 6 h, respectively, the removal efficiencies of the sulfate was 30, 72 e 72%, in the operations when the reactor was fed with a COD/[\'SO IND.4\'POT.2-\'] relation of 1,34. In the essays when the reactor was fed in COD/[\'SO IND.4\'POT.2-\'] relation of 0,67, the efficiencies of the sulfate reduction was 25, 58 e 55%, respectively. When the reactor was operated with COD/[\'SO IND.4\'POT.2-\'] relation of 0,34, the efficiencies of sulfate reduction 23, 37 e 27%, respectively. Thus, is possible to conclude that the operations in fed-batch increased the efficiency of sulfate removal, at what time was observed that in batch operations the organic matter removal attained improved efficiencies.
Book chapters on the topic "Biomasse granulari"
Dulekgurgen, Ebru, Nazik Artan, and Derin Orhon. "Morphological and Physiological Features of an Aerobic Granular EBPR Biomass Fed with Propionate." In Survival and Sustainability, 1327–41. Berlin, Heidelberg: Springer Berlin Heidelberg, 2010. http://dx.doi.org/10.1007/978-3-540-95991-5_125.
Full textCorsino, S. F., M. Capodici, M. Torregrossa, and G. Viviani. "Biokinetic Behaviour of Autochthonous Halophilic Biomass at Different Salinity: Comparison Between Activated Sludge and Granular Sludge Systems." In Lecture Notes in Civil Engineering, 73–78. Cham: Springer International Publishing, 2017. http://dx.doi.org/10.1007/978-3-319-58421-8_12.
Full textMuda, Khalida, Azmi Aris, Mohd Razman, and Zaharah Ibrahim. "Sequential Anaerobic-Aerobic Phase Strategy Using Microbial Granular Sludge for Textile Wastewater Treatment." In Biomass Now - Sustainable Growth and Use. InTech, 2013. http://dx.doi.org/10.5772/54458.
Full textVal del Río, Ángeles, Alba Pedrouso Fuentes, Elisa Amanda Giustinianovich, José Luis Campos Gomez, and Anuska Mosquera-Corral. "Anammox Process." In Technologies for the Treatment and Recovery of Nutrients from Industrial Wastewater, 264–89. IGI Global, 2017. http://dx.doi.org/10.4018/978-1-5225-1037-6.ch010.
Full textShikuku, Victor Odhiambo, George Oindo Achieng', and Chrispin O. Kowenje. "Removal of Dyes From Wastewater by Adsorption Onto Low-Cost Adsorbents." In Impact of Textile Dyes on Public Health and the Environment, 239–57. IGI Global, 2020. http://dx.doi.org/10.4018/978-1-7998-0311-9.ch011.
Full textConference papers on the topic "Biomasse granulari"
Kruggel-Emden, Harald, Siegmar Wirtz, Erdem Simsek, and Viktor Scherer. "Discrete Element Simulation (DEM) for Coupled Description of Material and Energy Flow Within Moving Granular Media." In ASME 2005 Pressure Vessels and Piping Conference. ASMEDC, 2005. http://dx.doi.org/10.1115/pvp2005-71360.
Full textYulianto, Andik, Prayatni Soewondo, Marissa Handajani, and Herto Dwi Ariesyady. "Preliminary study on aerobic granular biomass formation with aerobic continuous flow reactor." In PROCEEDINGS FROM THE 14TH INTERNATIONAL SYMPOSIUM ON THERAPEUTIC ULTRASOUND. Author(s), 2017. http://dx.doi.org/10.1063/1.4978186.
Full textAli Uzair, Muhammad, Francesco Fornarelli, Sergio Mario Camporeale, and Marco Torresi. "Detailed Description of the Fluidized Bed Mixing and Heat Transfer by Means of Eulerian Multi-Fluid Numerical Simulations." In ASME Turbo Expo 2020: Turbomachinery Technical Conference and Exposition. American Society of Mechanical Engineers, 2020. http://dx.doi.org/10.1115/gt2020-14993.
Full textPEKARSKAS, Juozas, Algirdas GAVENAUSKAS, Anželika DAUTARTĖ, and Aida STIKLIENĖ. "RECYCLING OF MINERAL SERPENTINITE WASTE FROM MINING INDUSTRY AND ITS USE IN AGRICULTURE TO IMPROVE SOIL AGROCHEMICAL PROPERTIES." In RURAL DEVELOPMENT. Aleksandras Stulginskis University, 2018. http://dx.doi.org/10.15544/rd.2017.102.
Full textDimter, Sanja, Martina Zagvozda, Branimir Milovanović, and Miroslav Šimun. "Usage of wood ash in stabilization of unbound pavement layers." In 6th International Conference on Road and Rail Infrastructure. University of Zagreb Faculty of Civil Engineering, 2021. http://dx.doi.org/10.5592/co/cetra.2020.1016.
Full textRodrigues Ramos, Lucas, and Edson Luiz Silva. "EFEITO DO TEMPO DE DETENÇÃO HIDRÁULICA NA PRODUÇÃO DE HIDROGÊNIO ATRAVÉS DE FERMENTAÇÃO ACIDOGÊNICA DE SORO DE LEITE EM REATOR ANERÓBIO DE LEITO GRANULAR EXPANDIDO." In Simpósio Nacional de Bioprocessos e Simpósio de Hidrólise Enzimática de Biomassa. Campinas - SP, Brazil: Galoá, 2015. http://dx.doi.org/10.17648/sinaferm-2015-33331.
Full textGhosh, Sayanti, and Saswati Chakraborty. "Bioremediation of hydrocarbon-rich wastewater by aerobic granules of oil degrading bacterial strains in salinity influence." In International Web Conference in Civil Engineering for a Sustainable Planet. AIJR Publisher, 2021. http://dx.doi.org/10.21467/proceedings.112.23.
Full textSafitri, Anissa Sukma, and Roald Kommedal. "Effect of temperatures on anaerobic granulated biofilm modelling." In 63rd International Conference of Scandinavian Simulation Society, SIMS 2022, Trondheim, Norway, September 20-21, 2022. Linköping University Electronic Press, 2022. http://dx.doi.org/10.3384/ecp192030.
Full textHenrique Alves da Silva, Cassio, Danilo Prado Pires, and EDSON APARECIDO ABDUL NOUR. "Desempenho de Reator Aeróbio de Mistura Completa com Biomassa Granular: Avaliação da Eficiência de Remoção de Compostos de Nitrogênio." In XXV Congresso de Iniciação Cientifica da Unicamp. Campinas - SP, Brazil: Galoa, 2017. http://dx.doi.org/10.19146/pibic-2017-78971.
Full textVanessa Andriguetto, Kellin, Breno Magno Silva dos Santos, TAUÃ OSAIDA DA SILVA, JANAINE GIOMBELLI JACHI, ADRIANA MARIA GRIEBELER, Liandra da Silva Denardi, FELIPE TURCHETTO, and Gabriel Coelho Waimer. "EFEITO DO USO DE FERTILIZANTE GRANULADO A BASE DE DEJETO SUÍNO NA BIOMASSA E ÍNDICE DE CLOROFILA EM PLANTAS DE Cordia americana." In 9° Congresso Florestal Brasileiro. Rio Grande do Sul: Softaliza Tecnologias LTDA, 2022. http://dx.doi.org/10.55592/cfb.2022.7159402.
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