Made available in DSpace on 2014-12-17T14:08:46Z (GMT). No. of bitstreams: 1 AnelieseLF_DISSERT.pdf: 3198107 bytes, checksum: 808e93eb6952cb8e374d91afa53cabe1 (MD5) Previous issue date: 2011-07-01 / Coordena??o de Aperfei?oamento de Pessoal de N?vel Superior / This master thesis aims at developing a new methodology for thermochemical degradation of dry coconut fiber (dp = 0.25mm) using laboratory rotating cylinder reactor with the goal of producing bio-oil. The biomass was characterized by infrared spectroscopy with Fourier transform FTIR, thermogravimetric analysis TG, with evaluation of activation energy the in non-isothermal regime with heating rates of 5 and 10 ?C/min, differential themogravimetric analysis DTG, sweeping electron microscopy SEM, higher heating value - HHV, immediate analysis such as evaluated all the amounts of its main constituents, i.e., lignin, cellulose and hemicelluloses. In the process, it was evaluated: reaction temperature (450, 500 and 550oC), carrier gas flow rate (50 and 100 cm?/min) and spin speed (20 and 25 Hz) to condensate the bio-oil. The feed rate of biomass (540 g/h), the rotation of the rotating cylinder (33.7 rpm) and reaction time (30 33 min) were constant. The phases obtained from the process of pyrolysis of dry coconut fiber were bio-oil, char and the gas phase non-condensed. A macroscopic mass balance was applied based on the weight of each phase to evaluate their yield. The highest yield of 20% was obtained from the following conditions: temperature of 500oC, inert gas flow of 100 cm?/min and spin speed of 20 Hz. In that condition, the yield in char was 24.3%, non-condensable gas phase was 37.6% and losses of approximately 22.6%. The following physicochemical properties: density, viscosity, pH, higher heating value, char content, FTIR and CHN analysis were evaluated. The sample obtained in the best operational condition was subjected to a qualitative chromatographic analysis aiming to know the constituents of the produced bio-oil, which were: phenol followed by sirigol, acetovanilona and vinyl guaiacol. The solid phase (char) was characterized through an immediate analysis (evaluation of moisture, volatiles, ashes and fixed carbon), higher heating value and FTIR. The non-condensing gas phase presented as main constituents CO2, CO and H2. The results were compared to the ones mentioned by the literature. / O presente trabalho tem como objetivo o desenvolvimento de uma metodologia de degrada??o termoqu?mica da fibra do coco seco (dp = 0,25 mm) utilizando reator de cilindro rotativo em escala de laborat?rio, visando a produ??o de bio-?leo. A biomassa foi caracterizada por an?lise elementar (C, H, N), espectroscopia no infravermelho com transformada de Fourier - IVTF, an?lise termogravim?trica ATG, com avalia??o da energia de ativa??o no regime n?o isot?rmico com taxas de aquecimento de 5 e 10 oC/min, an?lise diferencial termogravim?trica - DTG, microscopia eletr?nica de varredura - MEV, poder calor?fico superior - PCS, an?lise imediata (avalia??o da umidade, materiais vol?teis, cinzas e carbono fixo) bem como avalia??o dos teores dos principais constituintes, ou seja, lignina, celulose e hemicelulose. No processo de pir?lise os seguintes par?metros foram estudados: temperatura da rea??o (450, 500 e 550 ?C), vaz?o do g?s de arraste (50 e 100 cm?/min) e velocidade de centrifuga??o para condensa??o do bio-?leo (20 e 25 Hz). O fluxo de alimenta??o da biomassa (540 g/h), a rota??o do cilindro rotativo (33,7 rpm) e o tempo de rea??o (30 33 min) foram mantidos constantes. Os produtos obtidos no processo da pir?lise da fibra do coco seco foram o bio-?leo, os finos de carv?o e a fase gasosa n?o condensada. Um balan?o de massa macrosc?pico aplicado tendo como base o peso de cada produto permitiu obter o rendimento dessas fases. O melhor rendimento de 18,1 % em bio-?leo foi obtido nas seguintes condi??es: temperatura de 500 ?C, vaz?o de g?s inerte 100 cm?/min e velocidade de centrifuga??o de 20 Hz. Nessas condi??es, o rendimento em finos de carv?o foi de 21,7 %, fase gasosa n?o condens?vel 37,6 % e perdas da ordem de 22,6 %. Algumas propriedades f?sicas do bio-?leo foram avaliadas, a saber, a densidade, viscosidade, pH, poder calor?fico superior, teor de finos de carv?o, an?lise por IVTF e CHN. A an?lise cromatogr?fica do bio-?leo mostrou que os principais constituintes de sua composi??o foram o fenol seguido do sirigol, aceto vanilona e vinil guaiacol. A fase s?lida (finos de carv?o) obtida foi caracterizada por an?lise imediata, poder calor?fico superior e IVTF. A fase gasosa n?o condensada apresentou como principais constituintes o CO2, CO e H2. Os resultados foram comparados com dados da literatura.

Made available in DSpace on 2014-12-17T15:01:32Z (GMT). No. of bitstreams: 1 KarenPBA_DISSERT.pdf: 3887883 bytes, checksum: 3ebc4a634530a0a4a6493a962284d14f (MD5) Previous issue date: 2013-10-18 / Coordena??o de Aperfei?oamento de Pessoal de N?vel Superior / The bio-oil obtained from the pyrolysis of biomass has appeared as inter-esting alternative to replace fossil fuels. The aim of this work is to evaluate the influence of temperature on the yield of products originating from the pyrolysis process of the powder obtained from the dried twigs of avel?s (Euphorbia tirucalli), using a rotating cylinder reactor in laboratory scale. The biomass was treated and characterized by: CHNS, moisture, volatiles, fixed carbon and ashes, as well as evaluation of lignin, cellulose and hemicellulose, besides other instrumental techniques such as: FTIR, TG/DTG, DRX, FRX and MEV. The activation energy was evaluated in non-isothemichal mode with heating rates of 5 and 10 oC/min. The obtained results showed biomass as feedstock with potential for biofuel production, because presents a high organic matter content (78,3%) and fixed-carbon (7,11%). The activation energy required for the degradation of biomass ranged between 232,92 392,84 kJ/mol, in the temperature range studied and heating rate of 5 and 10?C/min. In the pyrolysis process, the influence of the reaction temperature was studied (350-520 ? C), keeping constant the other variables, such as, the flow rate of carrier gas, the centrifugal speed for the bio-oil condensationa, the biomass flow and the rotation of the reactor. The maximum yield of bio-oil was obtained in the temperature of 450?C. In this temperature, the results achieved where: content of bio-oil 8,12%; char 32,7%; non-condensed gas 35,4%; losts 23,8%; gross calorific value 3,43MJ/kg; pH 4,93 and viscosity 1,5cP. The chromatographic analysis of the bio-oil produced under these conditions shows mainly the presence of phenol (17,71%), methylciclopentenone (10,56%) and dimethylciclopentenone (7,76%) / O bio-?leo obtido da pir?lise da biomassa tem aparecido como alternativa interessante para substitui??o dos combust?veis f?sseis. O objetivo deste trabalho ? avaliar a influ?ncia da temperatura no rendimento dos produtos originados do processo de pir?lise do p? obtido dos galhos secos do avel?s (Euphorbia tirucalli), utilizando um reator de cilindro rotativo em escala de laborat?rio. A biomassa foi tratada e caracterizada por: CHNS, umidade, materiais vol?teis, cinzas e carbono fixo, bem como, avalia??o dos teores de lignina, celulose e hemicelulose, al?m de outras t?cnicas instrumentais, tais como: FTIR, TG/DTG, DRX, FRX e MEV. A energia de ativa??o foi avaliada no regime n?o isot?rmico com taxas de aquecimento de 5 e 10 oC/min. Os resultados obtidos mostraram a biomassa como mat?ria prima com potencial para produ??o de biocombust?veis, pois apresenta alto teor de mat?ria org?nica (78,3%) e carbono fixo (7,11%). A energia de ativa??o exigida para degrada??o da biomassa variou entre 232,92 392,84 kJ/mol, no intervalo de temperatura da rea??o estudado e taxa de aquecimento de 5 e 10oC/min. No processo de pir?lise, estudou-se a influ?ncia da temperatura da rea??o (350-520 ?C), mantendo-se constantes as demais vari?veis, ou seja, a vaz?o do g?s de arraste , a velocidade de centrifuga??o para condensa??o do bio-?leo, a vaz?o de biomassa e a rota??o do reator. O rendimento m?ximo em bio-?leo foi obtido na temperatura de 450?C. Nessa temperatura, os resultados alcan?ados foram: teor de bio?leo de 8,12%; carv?o 32,7%; fase gasosa n?o condensada 35,4%; perdas 23,8%; poder calor?fico superior 3,43MJ/kg; pH 4,93; viscosidade 1,5cP. A an?lise cromatogr?fica do bio-?leo produzido nessas condi??es mostra a presen?a, principalmente, de fenol (17,71%), metilciclopentenona (10,56%) e dimetilciclopentenona (7,76%)

Made available in DSpace on 2014-12-17T15:01:35Z (GMT). No. of bitstreams: 1 KarenPBA_DISSERT.pdf: 3887883 bytes, checksum: 3ebc4a634530a0a4a6493a962284d14f (MD5) Previous issue date: 2013-10-18 / Coordena??o de Aperfei?oamento de Pessoal de N?vel Superior / The bio-oil obtained from the pyrolysis of biomass has appeared as inter-esting alternative to replace fossil fuels. The aim of this work is to evaluate the influence of temperature on the yield of products originating from the pyrolysis process of the powder obtained from the dried twigs of avel?s (Euphorbia tirucalli), using a rotating cylinder reactor in laboratory scale. The biomass was treated and characterized by: CHNS, moisture, volatiles, fixed carbon and ashes, as well as evaluation of lignin, cellulose and hemicellulose, besides other instrumental techniques such as: FTIR, TG/DTG, DRX, FRX and MEV. The activation energy was evaluated in non-isothemichal mode with heating rates of 5 and 10 oC/min. The obtained results showed biomass as feedstock with potential for biofuel production, because presents a high organic matter content (78,3%) and fixed-carbon (7,11%). The activation energy required for the degradation of biomass ranged between 232,92 392,84 kJ/mol, in the temperature range studied and heating rate of 5 and 10?C/min. In the pyrolysis process, the influence of the reaction temperature was studied (350-520 ? C), keeping constant the other variables, such as, the flow rate of carrier gas, the centrifugal speed for the bio-oil condensationa, the biomass flow and the rotation of the reactor. The maximum yield of bio-oil was obtained in the temperature of 450?C. In this temperature, the results achieved where: content of bio-oil 8,12%; char 32,7%; non-condensed gas 35,4%; losts 23,8%; gross calorific value 3,43MJ/kg; pH 4,93 and viscosity 1,5cP. The chromatographic analysis of the bio-oil produced under these conditions shows mainly the presence of phenol (17,71%), methylciclopentenone (10,56%) and dimethylciclopentenone (7,76%) / O bio-?leo obtido da pir?lise da biomassa tem aparecido como alternativa interessante para substitui??o dos combust?veis f?sseis. O objetivo deste trabalho ? avaliar a influ?ncia da temperatura no rendimento dos produtos originados do processo de pir?lise do p? obtido dos galhos secos do avel?s (Euphorbia tirucalli), utilizando um reator de cilindro rotativo em escala de laborat?rio. A biomassa foi tratada e caracterizada por: CHNS, umidade, materiais vol?teis, cinzas e carbono fixo, bem como, avalia??o dos teores de lignina, celulose e hemicelulose, al?m de outras t?cnicas instrumentais, tais como: FTIR, TG/DTG, DRX, FRX e MEV. A energia de ativa??o foi avaliada no regime n?o isot?rmico com taxas de aquecimento de 5 e 10 oC/min. Os resultados obtidos mostraram a biomassa como mat?ria prima com potencial para produ??o de biocombust?veis, pois apresenta alto teor de mat?ria org?nica (78,3%) e carbono fixo (7,11%). A energia de ativa??o exigida para degrada??o da biomassa variou entre 232,92 392,84 kJ/mol, no intervalo de temperatura da rea??o estudado e taxa de aquecimento de 5 e 10oC/min. No processo de pir?lise, estudou-se a influ?ncia da temperatura da rea??o (350-520 ?C), mantendo-se constantes as demais vari?veis, ou seja, a vaz?o do g?s de arraste , a velocidade de centrifuga??o para condensa??o do bio-?leo, a vaz?o de biomassa e a rota??o do reator. O rendimento m?ximo em bio-?leo foi obtido na temperatura de 450?C. Nessa temperatura, os resultados alcan?ados foram: teor de bio?leo de 8,12%; carv?o 32,7%; fase gasosa n?o condensada 35,4%; perdas 23,8%; poder calor?fico superior 3,43MJ/kg; pH 4,93; viscosidade 1,5cP. A an?lise cromatogr?fica do bio-?leo produzido nessas condi??es mostra a presen?a, principalmente, de fenol (17,71%), metilciclopentenona (10,56%) e dimetilciclopentenona (7,76%)