Global Waste Management Symposium 2014 Information
Transcrição
Global Waste Management Symposium 2014 Information
Global Waste Management Symposium 2014 Information on Authors Name of Presenting/Corresponding Author: Sellin, Noeli Masters in Process Engineering, University of Joinville Region, Brazil Professor [email protected] +55 47 3461 9209 Names of Other Authors: Krohl, Ricardo, Diego Masters in Process Engineering, University of Joinville Region, Brazil Msc. Student [email protected] +55 47 3461 9209 Marangoni, Cintia Masters in Process Engineering, University of Joinville Region, Brazil Professor [email protected] +55 47 3461 9180 Maia, Bianca, G. de Oliveira Department of Mechanical Engineering - EMC, Federal University of Santa Catarina, Brazil PhD Student [email protected] +55 47 9651 3006 Souza, Ozair Masters in Process Engineering, University of Joinville Region, Brazil Professor [email protected] +55 47 3461 9180 Abstract Title: Fast pyrolysis of semi-dried banana leaves Abstract Topic: Waste minimization, reuse, recycling and management policy, regulation, economics, and planning Facility operation and design Organics diversion and management Anaerobic Digestion/Fermentation of Solid Waste Global climate change Chemical and biological treatment and processes Life cycle analysis/Sustainability Conversion technologies and diversion strategies Waste containment and geosynthetics Leachate treatment and management Bioreactors Air/gas emission quality, collection, control, utilization, and destruction X Waste-based energy Waste collection, transport, equipment and safety Environmental characterization of waste Management and re-use of industrial, oil/gas, coal ash, waste materials Other __________________________________________________________________________________ Preference for Poster or Oral Presentation: Poster Fast pyrolysis of semi-dried banana leaves Introduction Brazil is the fourth-largest producer of bananas in the world, after India, the Philippines and China. In the 2012/2013 harvest, the state of Santa Catarina, located in the southern region of Brazil, produced approximately 683,592 tons of bananas (CEPA, 2014). For every ton of bananas harvested, approximately four tons of lignocellulosic waste are generated (three tons of pseudostem, 160 kg of stems, 480 kg of leaves and 440 kg of banana peels), and approximately 100 kg of fruit are rejected. After the harvest, banana peels are used as feed for pigs and small amount of the leaves are used for packaging foods or for cooking (packing foods that are baked in the oven), but this is done in a rudimentary way (homemade) (Tock et al, 2010). The rest remains in the area of cultivation to its spontaneous decomposition. However, the accumulation of material disposed produces methane gas and carbon dioxide by the action of specific bacteria during the biodegradation. These gases and other harmful actions are directly linked to global warming and the depletion of the ozone layer in the atmosphere. Research in the bioenergy field has become increasingly relevant to Brazil because it is estimated that approximately 440 million tons of agro-industrial, agricultural and livestock waste and byproducts are produced annually. However, only a small fraction of this biomass, approximately 5-8%, is used in Brazil, whereas the use of such waste in other countries can reach up to 36% (Oliveira, 2014). There is little information in literature about the use of banana culture waste as biomass for energy generation. Some researchers have demonstrated the potential of banana waste based on the production of biogas through digestion process (Souza et al, 2010; Tock et al, 2010), briquettes and bioethanol (Souza et al, 2012; Oberoi et al, 2011) production from banana peels and rejected banana fruit. The use of these wastes in the production of inputs or their transformation into true commodity, besides allowing the reduction of environmental pollution, would add value to the banana crop, which in recent years has faced great challenges generated by the oscillation of the product in the domestic market. Among the possibilities of recovery these waste is to be used as biomass to generate renewable energy. Agricultural and agro-industrial wastes are increasingly being used as biomass to generate energy and raw materials via thermochemical conversion. Biomass sources such as sugar cane straw and bagasse, wood briquettes, eucalyptus sawdust, elephant grass, rice husks or corn straw and cobs are been subjected to thermochemical conversion by liquefaction, gasification, pyrolysis and combustion (Zhang and Xu, 2010). Among these processes, pyrolysis has been highlighted as one of the most promising methods due to its great flexibility, as it can be controlled to obtain specific products. During pyrolysis, a solid residue rich in carbon (vegetable coal) and a volatile fraction consisting of non-condensable gases and condensable organic vapors (bio-oil and the pyroligneous acid) are formed. The products obtained from the pyrolysis of biomass have a number of applications, especially in the generation of energy and the production of chemicals (Bridgwater and Peacocke, 2000; Bridgwater, 2012). The characteristics and properties of these products depend on the parameters that characterize the slow, fast or flash pyrolysis process; they also depend on the proportions of the components that constitute the biomass. Fast pyrolysis is presented as a process of increasing study in which the biomass is heated to 450-500 °C in oxygen-free or low oxygen atmosphere and low residence time (on the order of seconds), forming products such as coal and a fraction composed of volatile gases and condensable organic vapors (bio-oil), but with higher yield for bio-oil (Choi et al, 2012). Experimental Banana semi-dried leaves samples were obtained directly from banana trees and only the leaves that were already dried were collected. The samples were ground in a mill to produce the particles with less than 1 mm of average size and later 12 kg/h of the samples were submitted to rapid pyrolysis in a fluidized bed reactor (PPR-10 pilot plant, Bioware Co., Figure 1), at temperature of 500 °C. The flow of air fed to the pyrolysis reactor was approximately 0.6 kg of air per kg biomass, i.e. 10% over stoichiometric. The bed particle was sand (with silica and quartz). The pyrolysis tests were performed in triplicate. Figure 1. Pyrolysis plant (BIOWARE Co.). The pyrolysis products were gas, liquid (bio-oil) and vegetal coal. The non-condensable gas fraction obtained was burned in a combustor and the energy released was used to heat the air to fluidize the bed in the reactor during the pyrolysis process. The bio oil showed two fractions, heavy phase and light phase (pyroligneous acid). The recovery system of bio-oil and acid extract combines indirect cooling with water and centrifugal separation. The vegetal coal was separated in the process by cyclones. The bio-oil, heavy and light phase, and vegetal coal were characterized through elemental chemical analysis (carbon, hydrogen and nitrogen content) using a Perkin-Elmer CHN 2400 elemental analyzer and the sulfur content was determined with a Spectro Ciros inductively coupled plasma atomic emission spectrometer equipped with a charge-coupled device (CCD); and high heating value (HHV) in a bomb calorimeter, Parr model 1241. The compounds of bio-oil light phase were characterized by gas chromatography coupled to mass spectrometry (GC-MS). The sample was injected directly into the Agilent 7890A gas chromatograph with an HP-5 column. The identification of compounds was performed by comparing the mass spectra obtained with the NIST 05 Mass Spectral Library. The bio-oil heavy phase was characterized by Infrared Fourier Transform Spectroscopy (FTIR) in a spectrophotometer of Perkin Helmer One B, with twelve scans, with a resolution of 4 cm -1 and using accessory (zinc selenide crystal) for attenuated total reflectance (ATR), in order to identify the chemical compounds present. Results and Discussion Table 1 shows the mass yield of pyrolysis products and the Table 2 the elemental chemical composition (CHNS) and high heating value (HHV) of bio-oil phases and vegetal coal. The gas and bio-oil had major yield than vegetal coal, characteristic of fast pyrolysis. The bio-oil heavy phase showed HHV of 25 MJ/kg and high carbon of 55.9 %. The HHV of vegetal coal was 18.2 MJ/kg and the carbon content was high, of 48.1 %. The high carbon content of the vegetal coal indicates the presence of an organic load and a susceptibility to be used as a combustible. Low contents of sulfur and nitrogen are observed in coal. These results are satisfactory because the quantities of sulfur oxides, nitrogen oxides and the toxic and corrosives gases generated during combustion process were low. Table 1. Mass yield of fast pyrolysis products. Products Bio-oil heavy phase Bio-oil light phase Vegetal coal Gás Mass yield (%) 10.7 1.2 16.5 1.4 23.3 2.9 49.7 5.3 Table 2. CHNS elemental composition and high heating value (HHV) of bio-oil phases and coal. Sample Bio-oil heavy phase Bio-oil light phase Vegetal coal Carbon (%) 55.9 Hydrogen (%) 7.8 Nitrogen (%) 0.87 Sulfur (%) 0.08 HHV (MJ/kg) 25 16.9 8.8 - 0.01 1.2 48.1 3.3 1.2 0.33 18.2 Table 3 lists some compounds identified by GC-MS in the bio-oil light phase (pyroligneous acid) produced by the pyrolysis of the banana leaves. The pyroligneous acid contained large amounts of complex chemical compounds with various chemical functional groups, e.g., alcohols, phenols, ketones. Phenolic compounds were also formed, for example, dimethoxyphenol, which has commercial value and is a major component of creosote, which is used as a wood preservative (Uzun et al, 2007). Table 3. Chemical compounds identified by GC-MS present in the bio-oil light phase from the pyrolysis of banana leaves. Bio-oil light phase (Pyroligneous Acid) Molecular * Compound Name tR (min) Formula 1-hydroxybutanone C4H8O2 2.839 Cyclopentanone C5H8O 2.983 2-methylpyridine C7H8N 3.387 2-cyclopenten-1-one C5H6O 3.498 Furanmethanol C5H6O 3.749 Acetylfuran C6H6O 4.403 Butyrolactone C4H6O2 4.463 Phenol C6H6O 5.124 2-hydroxy-3-methyl-2C6H8O2 5.606 cyclopenten-1-one 2-methylphenol C7H8O 5.835 2-methoxyphenol C7H8O2 6.188 Hydroquinone C6H6O2 7.604 2,6-dimetoxyphenol C8H10O3 8.232 * Retention time on the column (minutes). The pyroligneous acid contained large amounts of complex chemical compounds with various chemical functional groups, e.g., alcohols, phenols, ketones. Phenolic compounds were also formed, for example, dimethoxyphenol, which has commercial value and is a major component of creosote, which is used as a wood preservative (Uzun et al, 2007). The FTIR/ATR spectrum of heavy phase bio-oil (Figure 2) reveals a significant presence of oxygen compounds like aldehydes, ketones, esters and aromáticos, in the region 1500-1700 cm-1, and alcohols, phenols and ether, in the region 1100-1300 cm-1. Figure 2. FTIR/ATR spectrum of bio-oil heavy phase from the pyrolysis of banana leaves. Conclusion The products obtained from fast pyrolysis of banana semi-dried leaves had characteristics and properties similar to other biomass like agro industrial waste already studied, demonstrating potential to produce energy, fuel, materials and chemicals through pyrolysis. Furthermore, these thermochemical conversion processes reduce the waste volume significantly and contribute to reducing the environmental impact generally caused by the disposal of such waste. References Bridgwater A. V. Review of fast pyrolysis of biomass and product upgrading. Biomass and Bioenergy, v. 38, p. 68-94, 2012. Bridgwater A. V., Peacocke G. V. C. Fast pyrolysis processes for biomass. Renewable and Sustainable Energy Review, v. 4, p. 1-23, 2000. CEPA - Center of Socioeconomic and Agricultural Planning, EPAGRI - SC. Production Tables Comparison of crops. Available in: www.cepa.epagri.sc.gov.br. Accessed in december 2013 (in Portuguese). Choi H. S., Choi Y. S., Park H. C. Fast pyrolysis characteristics of lignocellulosic biomass with varying reaction conditions. Renewable Energy, v. 42, p. 131-135, 2012. Oberoi, H. S.; Vadlani, P. V.; Saida, L.; Bansal, S.; Hughes, J. D. Ethanol production from banana peels using statistically optimized simultaneous saccharification and fermentation process. Waste Management, v. 31, n. 7, p. 1576-1584, 2011. Oliveira C. M. Renewable Energy. 1st. Edition. Available in: http://pt.calameo.com/read/00020096870b93510ec6c. Accessed in February 2014 (in Portuguese). Souza O., Federizzi M., Coelho B., Wagner T. M., Wisbeck E. Biodegradation of lignocellulosic waste generated in the banana plantations and their appreciation for the production of biogas. Brazilian Journal of Agricultural and Environmental Engineering, v.14, n.14, p. 438-443, 2010 (in Portuguese). Souza O.,Schulz M. A., Fischer G. A. A., Wagner T. M., Sellin, N. Alternative energy biomass: Bioethanol from the skin and pulp of banana. Brazilian Journal of Agricultural and Environmental Engineering, v. 16, p. 1-7, 2012 (in Portuguese). Tock J. Y., Lai C. L., Lee K. T., Tan K. T, Bhatia S. Banana biomass to renewable energy resource potential: The Malaysian case study. Renewable and Sustainable Energy Review, v. 14, p. 798-805, 2010. Uzun B. B., Pütün A. E., Pütün E. Composition of products obtained via fast pyrolysis of oliveoil residue: Effect of pyrolysis temperature. Journal of Analytical Applied Pyrolysis, v. 79, p. 147-153, 2007. Zhang L., Xu C., Champagne P. Overview of recent advances in thermo-chemical conversion of biomass. Energy Conversion and Management, v. 51, n. 5, p. 969-982, 2010.
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