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M. Y. Guida
M. Y. Guida
University of Sultan Moulay Slimane, 23000 Béni-Mellal, Morocco
University of Sultan Moulay Slimane, 23000 Béni-Mellal, Morocco
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University of Sultan Moulay Slimane, 23000 Béni-Mellal, Morocco
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A. Hannioui
A. Hannioui
University of Sultan Moulay Slimane, 23000 Béni-Mellal, Morocco
University of Sultan Moulay Slimane, 23000 Béni-Mellal, Morocco
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University of Sultan Moulay Slimane, 23000 Béni-Mellal, Morocco
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In this study, compositional analysis of the products obtained by thermal degradation of sugar cane bagasse at various pyrolysis temperatures (300, 350, 400, 450, 500, 550, 600, 650, 700, 750 and 800 °C) and heating rate (5, 10, 20 and 50 °C/min) was studied. Sugar cane bagasse was pyrolyzed in a stainless steel tubular reactor. The aim of this work was to experimentally investigate how the temperature and heating rate affects liquid and char product yields via pyrolysis and to determine optimal condition to have a better yield of these products. Liquid product (bio-oil) obtained under the most suitable conditions were characterized by elemental analysis, FT-IR, C-NMR and HNMR. In addition, column chromatography was employed to determine the aliphatic fraction (Hexane Eluate); gas chromatography and FT-IR were achieved on aliphatic fractions. For char product (bio-char), the elemental chemical composition and yield of the char were determined. The results of our work showed that the amount of liquid product (bio-oil) from pyrolysis of sugar cane bagasse increases with increasing the final temperature and decreases with increasing the heating rate. The highest yield of liquid product is obtained from the samples at 550 °C and at the heating rate of 5°C/min, the maximal average yield achieved almost 32.80 wt%. The yield of char generally decreases with increasing the temperature, the char yield passes from 39.7 wt% to 21 wt% at the heating rate of 5°C/min and from 32 wt% to 17.2 wt% at the heating rate of 50 °C/min at the same range of temperature (300–800 °C). The analysis of bio-oil showed the presence of an aliphatic character and that it is possible to obtain liquid products similar to petroleum from sugar cane bagasse waste. The solid products (bio-char) obtained in the presence of nitrogen (N2) contain a very important percentage of carbon and high higher heating values (HHV).
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-
[1]
Chen Xu and al. Wyman CE. Biomass ethanol: technical progress, opportunities and commercial challenges. Annu Rev Energy Environ 1999;24:189–226.
-
[2]
Balogh, D.T., Curvelo, A.A.S. and al, 1992. Solvent effect on organosolv lignin from Pinus Caribaea Hondurensis. Holzforschung 46, 343–348.
-
[3]
Carrier, M., Hugo, T. and al, 2011. Comparison of slow and vacuum pyrolysis of sugar cane bagasse. J. Anal. Appl. Pyrol. 90, 18–26.
-
[4]
Devnarain P.B. , 2003. Production of activated carbon from South African sugarcane bagasse. M.Sc. (Eng.) Thesis. University of KwaZulu-Natal.
-
[5]
El Mansouri N.E. , Salvado, J., 2006. Structural characterization of technical lignins for the production of adhesives: application to lignosulfonate, kraft, sodaanthraquinone, organosolv and ethanol process lignins. Ind. Crop. Prod. 24, 8–16.
-
[6]
Jacobsen SE , Wyman CE. Xylose monomer and oligomer yields for uncatalyzed hydrolysis of sugarcane bagasse hemicelluloses at varying solids concentration. Ind Eng Chem Res 2002;41:1454–61.
-
[7]
Ibrahim MH , Agblevor FA and al. Isolation and characterization of cellulose and lignin from steam-exploded lignocellulosic biomass. BioResources 2010;5:397–418.
-
[8]
McLaughlin H and al. All biochars are not created equal, and how to tell them apart. In: North American Biochar Conference, Colorado 2009.
-
[9]
Chan KY and al. Agronomic values of greenwaste biochar as a soil amendment. Soil Res 2007; 45(8): 629–634.
-
[10]
Laird D and al. Biochar impact on nutrient leaching from a Midwestern agricultural soil. Geoderma 2010; 158(3): 436–442.
-
[11]
Baccar R and al. Preparation of activated carbon from Tunisian olive-waste cakes and its application for adsorption of heavy metal ions. J Hazard Mat 2009; 162(2): 1522–1529.
-
[12]
Barbera AC and al. Effects of spreading olive mill wastewater on soil properties and crops, a review. Agric Water Mag 2013; 11 9: 43–53.
-
[13]
Andre RN and al. Fluidised bed co-gasification of coal and olive oil industry wastes. Fuel 2005; 84(12): 1635–1644.
-
[14]
Lafka T-I and al. Phenolic and antioxidant potential of olive oil mill wastes. Food Chem 2011; 125(1): 92–98.
-
[15]
Leon-Camacho M and al. Elimination of polycyclic aromatic hydrocarbons by bleaching of olive pomace oil. Eur J Lipid Sci Technol 2003; 105(1): 9–16.
-
[16]
Miranda T and al. Combustion analysis of different olive residues. Int J Mol Sci 2008; 9(4): 512–525.
-
[17]
Vlyssides AG and al. Integrated strategic approach for reusing olive oil extraction by-products. J Clean Prod 2004; 12(6): 603–611.
-
[18]
Demirbas A. Relationships between lignin contents and heating values of biomass. Energy Convers Mana 2001; 42(2): 183–188.
-
[19]
Goncalves, A.R., Ruzene, D.S., Moriya, R.Y., Oliveria, L.R.M., 2005. Pulping of sugarcane bagasse and straw and biobleaching of the pulps: conditions parameters and recycling of enzymes. In: 59th Appita Conference, Auckland, New Zealand, 16–19 May.
-
[20]
Abu Tayeh H and al. Potential of bioethanol production from olive mill solid wastes. Bioresour. Technol 2014; 15 2: 24–30.
-
[21]
Albalasmeh AA and al. A new method for rapid determination of carbohydrate and total carbon concentrations using UV spectrophotometry. Carbohydr. Polym 2013; 9 7: 253–261.
-
[22]
Banat IM and al. Cost effective technologies and renewable substrates for bio surfactants production. Front. Microbiol 2014; 5: 1–18.
-
[23]
Chang YC and al. Isolation of Bacillus sp. strains capable of decomposing alkali lignin and their application in combination with lactic acid bacteria for enhancing cellulase performance. Biors. Technol; 15 2: 429–436.
-
[24]
Dermeche S and al. Olive mill wastes: biochemical characterizations and valorization strategies. Process Biochem 2013. 48: 1532–1552.
-
[25]
Armesto L and al. Co-combustion of coal and olive industry residues in fluidized bed. Fuel 2003; 8 2: 993–1000.
-
[26]
Arvanitoyiannis, I.S., Kassaveti, A., 2008. Olive oil waste management: treatment methods and potential uses of treated waste. In: Arvanitoyiannis, I.S. (Ed.), Waste Management for the Food Industries. Elsev 208 8: 453–568.
-
[27]
Arvelakis S and al. Agglomeration problems during fluidized bed gasification of olive-oil residue: evaluation of fractionation and leaching as pre-treatments. Fuel 2003; 8 2: 1261–1270.
-
[28]
Ozby N and al. Biocrude from biomass : pyrolysis of cotton seed cake. Renew energy 2001; 2 4: 615–625.
-
[29]
Zabaniotou AA and al. Pyrolysis of forestry biomass by-products in Greece. Eneg sour 1999; 21:395–403.
-
[30]
Christoforou EA and al. Monte Carlo parametric modeling for predicting biomass calorific value. J. Therm. Anal. Calorim 2014; 118 : 1789–1796.
-
[31]
Minkova V and al. Effect of water vapour and biomass nature on the yield and quality of pyrolysis products from biomass, fuel proce tec 2001; 70: 53–61.
-
[32]
Aloma, I. , Martin-Lara, M.A. and al. (2012). Removal of nickel (II) ions from aqueous solutions by biosorption on sugarcane bagasse. Journal of the Taiwan Institute of Chemical Engineers, 43, 275–281.
-
[33]
Putun AE and al. Composition of products obtained via fast pyrolysis of olive-oil residue: effect of pyrolysis temperature, j.anal. appl. Pyrolysis 2007; 79: 147–153.
-
[34]
Minkova V and al. Thermochemical treatment of biomass in a flow of steam or in a mixture of steamand carbon dioxide. Fuel proc tec 2000; 62: 45–52.
-
[35]
Ficher T and al. Pyrolysis behaviour and kinetics of biomass derived materials. J. Anal Appl Pyrol 2002; 62: 331–49.
-
[36]
Aziz, A. , Elandaloussi, E and al. (2009). Efficiency of succinylated-olive stone biosorbent on the removal of cadmium ions from aqueous solutions. Colloids and Surfaces B: Biointerfaces, 73, 192–198.
-
[37]
Sayigh A . Renewable energy-the way forward, appli ener 1999; 64: 15–30.
-
[38]
Rath J and al. Tar cracking from fast pyrolysis of large beech wood particles, journal of analyt & appli pyroly 2002; 62: 83–92.
-
[39]
Lédé J. Cellulose pyrolysis kinetics : an historial review on the existence and role of intermediate active cellulose, Jour of analy and app pyrol 2012; 94: 17–32.
-
[40]
Fatih M. Biowastes-to-biofuels, energy convers and manage 2011; 52: 1815–1828.
-
[41]
Dupont C and al. Biomass experiments in an analytical entrained flow reactor between 1073 K and 1273 K, fuel 2008; 87: 1155–1164.
-
[42]
Doymaz I . Drying characteristics of the solid byproduct of olive oil exctraction, biosyste engineer 2004; 88(2): 213–219.
-
[43]
Erkonak H. Treatment of olive mill wastewater by supercritical water oxidation, j.of supercritical fluids 2008; 46: 142–148.
-
[44]
Reynolds JG and al. Pyrolysis decomposition kinetics of cellulose-based materials by constant heating rate micropyrolysis, energy and fuels 1997; 11: 88–97
Prof. Felföldi, József
Institute: MATE - Hungarian University of Agriculture and Life Sciences, Institute of Food Science and Technology, Department of Measurements and Process Control
Address: 1118 Budapest Somlói út 14-16
E-mail: felfoldi.jozsef@uni-mate.hu
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