Bioenergy future depends on an increased share of renewable energy, especially in developing countries. Bioconversion of lignocellulosic based biomass to ethanol is significantly hindered by the structural and chemical complexity of biomass, which makes these materials a challenge to be used as feed stocks for cellulosic ethanol production. Bioethanol is one of the most important alternative renewable energy sources that substitute the fossil fuels. Wastepaper has a content of cellulose and hemicelluloses, which make it suitable as fermentation substrate when hydrolyzed. The objective of this work is ethanol production from wastepaper by fermentation process. Eight laboratory experiments were conducted to produce bioethanol from wastepaper. By using Design Expert 7 software, it was formulated the dilute acid hydrolysis step to investigate the effects of hydrolysis parameters on yield of ethanol and optimum condition. All the three hydrolysis parameters were significant variables for the yield of ethanol. The optimum combinations of the three factors chosen for optimum ethanol yield 10.86 ml/50 g sample were 92.59°C hydrolysis temperature, 30 minutes hydrolysis time and 1%v/v acid concentration.
Published in | Science Journal of Energy Engineering (Volume 3, Issue 6) |
DOI | 10.11648/j.sjee.20150306.11 |
Page(s) | 46-53 |
Creative Commons |
This is an Open Access article, distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution and reproduction in any medium or format, provided the original work is properly cited. |
Copyright |
Copyright © The Author(s), 2016. Published by Science Publishing Group |
Bioethanol, Distillation, Fermentation, Hydrolysis, Wastepaper
[1] | Balat H. (2010). Prospects of biofuels for a sustainable energy future: A critical assessment. Energy Educ Sci Technol Part A; 24:85–111 |
[2] | Campbell, C.J., Laherrere, J.H., (1998). The end of cheap oil. Sci. Am. 3, 78–83. |
[3] | Demirbas. (2008). Biofuels sources, biofuel policy, biofuel economy and global biofuel projections Energy Convers Manage, pp. 2106–2116. |
[4] | EIA. International Energy Outlook. (2009). Energy information administration office of integrated analysis and forecasting US Department of Energy. DOE/EIA-0484; |
[5] | Forum for Agricultural Research in Africa (FARA). (2008). Bioenergy value chain research and development Stakes and Opportunities. Burkina Faso, FARA Discussion Paper; April 08. <swww.fara-africa.org/media/.../Bioenergy_Discussion_Paper. [Accessed November 2009]. |
[6] | Galbe, M. and Zacchi, G. (2007). A review of the production of ethanol from softwood. Appl. Biochem. Biotechnol. 59: 618-628. |
[7] | Gaur, K. (2006). Process optimization for the production of ethanol via fermentation. Master thesis, Thapar Institute of Engineering and Technology, Patiala. |
[8] | Hahn-Hagerdal, B., Galbe, M., Gorwa-Grauslund, M., Liden, G. and Zacchi, G. (2006). Bioethanol – the fuel of tomorrow from the residues of today. Tre. Biotechnol. 24: 549-556. |
[9] | Halidini SarakikyaIkeda, Y., Park, E. Y., & Naoyuki, O. (2006). Bioconversion of waste office paper to gluconic acid in a turbine blade reactor by the filamentous fungus Aspergillus niger. Bioresource Technology, 97, 1030–1035.). |
[10] | Ministry of Finance and Economic Development (MoFED). (2010). Ethiopia: Country Report on the Implementation of the Brussels Program of Action (BPOA). Addis Ababa. |
[11] | Prasad S, Singh A, Joshi HC. (2007). Ethanol as an alternative fuel from agricultural, industrial and urban residues. Resour, Conserv Recycl 50:1–39. |
[12] | Stokes H. (2005).Alcohol fuels (ethanol and methanol): safety. In: Presentation at ETHOS conference, Seattle, Washington. |
[13] | Sun, Y. and Cheng, J. (2002). Hydrolysis of lignocellulosic materials for ethanol production: a review. Biores. Technol. 83: 1-11. |
[14] | Taye, A. (2009). Conversion of banana and mango peel to ethanol. Addis Ababa. |
[15] | Veronica Kavila Ngunzi. Analysis of Energy Cost Savings by Substituting Heavy Fuel Oil with Alternative Fuel for a Pozzolana Dryer. Case. |
[16] | Study of Bamburi Cement. American Journal of Energy Engineering. Vol. 3, No. 6, 2015, pp. 93-102. doi: 10.11648/j.ajee.20150306.13. |
APA Style
Solomon Hailu, Solomon Kahsay G. Mariam, Tesfay Berhe. (2016). Optimization and Utilization of Wastepaper for Bio-energy Production. Science Journal of Energy Engineering, 3(6), 46-53. https://doi.org/10.11648/j.sjee.20150306.11
ACS Style
Solomon Hailu; Solomon Kahsay G. Mariam; Tesfay Berhe. Optimization and Utilization of Wastepaper for Bio-energy Production. Sci. J. Energy Eng. 2016, 3(6), 46-53. doi: 10.11648/j.sjee.20150306.11
@article{10.11648/j.sjee.20150306.11, author = {Solomon Hailu and Solomon Kahsay G. Mariam and Tesfay Berhe}, title = {Optimization and Utilization of Wastepaper for Bio-energy Production}, journal = {Science Journal of Energy Engineering}, volume = {3}, number = {6}, pages = {46-53}, doi = {10.11648/j.sjee.20150306.11}, url = {https://doi.org/10.11648/j.sjee.20150306.11}, eprint = {https://article.sciencepublishinggroup.com/pdf/10.11648.j.sjee.20150306.11}, abstract = {Bioenergy future depends on an increased share of renewable energy, especially in developing countries. Bioconversion of lignocellulosic based biomass to ethanol is significantly hindered by the structural and chemical complexity of biomass, which makes these materials a challenge to be used as feed stocks for cellulosic ethanol production. Bioethanol is one of the most important alternative renewable energy sources that substitute the fossil fuels. Wastepaper has a content of cellulose and hemicelluloses, which make it suitable as fermentation substrate when hydrolyzed. The objective of this work is ethanol production from wastepaper by fermentation process. Eight laboratory experiments were conducted to produce bioethanol from wastepaper. By using Design Expert 7 software, it was formulated the dilute acid hydrolysis step to investigate the effects of hydrolysis parameters on yield of ethanol and optimum condition. All the three hydrolysis parameters were significant variables for the yield of ethanol. The optimum combinations of the three factors chosen for optimum ethanol yield 10.86 ml/50 g sample were 92.59°C hydrolysis temperature, 30 minutes hydrolysis time and 1%v/v acid concentration.}, year = {2016} }
TY - JOUR T1 - Optimization and Utilization of Wastepaper for Bio-energy Production AU - Solomon Hailu AU - Solomon Kahsay G. Mariam AU - Tesfay Berhe Y1 - 2016/02/24 PY - 2016 N1 - https://doi.org/10.11648/j.sjee.20150306.11 DO - 10.11648/j.sjee.20150306.11 T2 - Science Journal of Energy Engineering JF - Science Journal of Energy Engineering JO - Science Journal of Energy Engineering SP - 46 EP - 53 PB - Science Publishing Group SN - 2376-8126 UR - https://doi.org/10.11648/j.sjee.20150306.11 AB - Bioenergy future depends on an increased share of renewable energy, especially in developing countries. Bioconversion of lignocellulosic based biomass to ethanol is significantly hindered by the structural and chemical complexity of biomass, which makes these materials a challenge to be used as feed stocks for cellulosic ethanol production. Bioethanol is one of the most important alternative renewable energy sources that substitute the fossil fuels. Wastepaper has a content of cellulose and hemicelluloses, which make it suitable as fermentation substrate when hydrolyzed. The objective of this work is ethanol production from wastepaper by fermentation process. Eight laboratory experiments were conducted to produce bioethanol from wastepaper. By using Design Expert 7 software, it was formulated the dilute acid hydrolysis step to investigate the effects of hydrolysis parameters on yield of ethanol and optimum condition. All the three hydrolysis parameters were significant variables for the yield of ethanol. The optimum combinations of the three factors chosen for optimum ethanol yield 10.86 ml/50 g sample were 92.59°C hydrolysis temperature, 30 minutes hydrolysis time and 1%v/v acid concentration. VL - 3 IS - 6 ER -