Articles & Issues
- Language
- English
- Conflict of Interest
- In relation to this article, we declare that there is no conflict of interest.
- Publication history
-
Received October 17, 2019
Accepted December 16, 2019
- This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
Copyright © KIChE. All rights reserved.
All issues
Production of biofuels from pine needle via catalytic fast pyrolysis over HBeta
Young-Min Kim
Hyung Won Lee1
Seong Ho Jang2
Jaehun Jeong1
Sumin Ryu1
Sang-Chul Jung3
Young-Kwon Park1†
Department of Environmental Engineering, Daegu University, Gyeongsan 38453, Korea 1School of Environmental Engineering, University of Seoul, Seoul 02504, Korea 2Department of BioEnvironmental Energy, Pusan National University, Miryang 50463, Korea 3Department of Environmental Engineering, Sunchon National University, Sunchon 57922, Korea
catalica@uos.ac.kr
Korean Journal of Chemical Engineering, March 2020, 37(3), 493-496(4), 10.1007/s11814-019-0467-8
Download PDF
Abstract
The thermal and catalytic pyrolysis of pine needles over HBeta catalysts with different SiO2/Al2O3 ratios (25 and 300) were investigated by thermogravimetric analysis (TGA) and pyrolyzer-gas chromatography/mass spectrometry. TGA showed that the main decomposition of pine needles occurred between 150 and 550 °C. The catalytic DTG curves revealed the same decomposition temperature region as the non-catalytic TG curve of pine needles. Pyrolyzergas chromatography/mass spectrometry suggested that the effective catalytic conversion of pyrolyzate intermediates and other hydrocarbons to aromatic hydrocarbons can be achieved using HBeta catalysts at 600 °C. HBeta(25) produced a larger amount of aromatic hydrocarbons than HBeta(300) because of its higher acid amounts. By increasing the reaction temperature from 500 to 700 °C, the formation of benzene, toluene, ethylbenzene, xylenes (BTEXs) and other polycyclic aromatic hydrocarbons was increased with a concomitant decrease in phenolics and other oxygenates. The formation efficiency of BTEXs was increased further by increasing the catalyst loading.
Keywords
References
Alejandra SB, Daniel LC, Victoria M, Juan JE, Daniel P, Fernando M, Sergi A, Gemma V, Luis FB, Rosalia R, Renew. Energy, 146, 188 (2020)
Sutanto S, Go AW, Chen KH, Nguyen PLT, Ismadji S, Ju YH, Fuel Process. Technol., 167, 281 (2017)
Bourjjat H, Rodat S, Chuayboon S, Abanades S, Energy, 189, 116118 (2019)
McKendry P, Bioresour. Technol., 83(1), 47 (2002)
Dhyani V, Bhaskar T, Renew. Energy, 129, 695 (2018)
Simeoni A, Thomas JC, Bartoli P, Borowieck P, Reszka P, Colella F, Santoni PA, Torero JL, Fire Safety J., 54, 203 (2012)
Varma AK, Mondal P, J. Therm. Anal. Calorim., 131, 2057 (2018)
Varma AK, Mondal P, J. Therm. Anal. Calorim., 124, 487 (2016)
Font R, Conesa JA, Molto J, Munoz M, J. Anal. Appl. Pyrolysis, 85, 276 (2009)
Mandal S, Bhattacharya TK, Verma AK, Haydary J, Chem. Pap., 72, 603 (2018)
Park YK, Jung JS, Jae J, Hong SB, Watanabe A, Kim YM, Chem. Eng. J., 377, 199742 (2019)
Kim YM, Jae J, Kim BS, Hong Y, Jung SC, Park YK, Energy Conv. Manag., 149, 966 (2017)
Park HJ, Heo HS, Jeon JK, Kim J, Ryoo R, Jeong KE, Park YK, Appl. Catal. B: Environ., 95(3-4), 365 (2010)
Kim YM, Lee HW, Lee SH, Kim SS, Park SH, Jeon JK, Kim S, Park YK, Korean J. Chem. Eng., 28(10), 2012 (2011)
Kim BS, Jeong CS, Kim JM, Bin Park S, Park SH, Jeon JK, Jung SC, Kim SC, Park YK, Catal. Today, 265, 184 (2016)
Yang J, Chen H, Zhao W, Zhou J, J. Anal. Appl. Pyrolysis, 117, 296 (2016)
Challinor JM, J. Anal. Appl. Pyrolysis, 25, 349 (1993)
Schultz EL, Mullen CA, Boateng AA, Energy Technol., 5, 196 (2017)
Sutanto S, Go AW, Chen KH, Nguyen PLT, Ismadji S, Ju YH, Fuel Process. Technol., 167, 281 (2017)
Bourjjat H, Rodat S, Chuayboon S, Abanades S, Energy, 189, 116118 (2019)
McKendry P, Bioresour. Technol., 83(1), 47 (2002)
Dhyani V, Bhaskar T, Renew. Energy, 129, 695 (2018)
Simeoni A, Thomas JC, Bartoli P, Borowieck P, Reszka P, Colella F, Santoni PA, Torero JL, Fire Safety J., 54, 203 (2012)
Varma AK, Mondal P, J. Therm. Anal. Calorim., 131, 2057 (2018)
Varma AK, Mondal P, J. Therm. Anal. Calorim., 124, 487 (2016)
Font R, Conesa JA, Molto J, Munoz M, J. Anal. Appl. Pyrolysis, 85, 276 (2009)
Mandal S, Bhattacharya TK, Verma AK, Haydary J, Chem. Pap., 72, 603 (2018)
Park YK, Jung JS, Jae J, Hong SB, Watanabe A, Kim YM, Chem. Eng. J., 377, 199742 (2019)
Kim YM, Jae J, Kim BS, Hong Y, Jung SC, Park YK, Energy Conv. Manag., 149, 966 (2017)
Park HJ, Heo HS, Jeon JK, Kim J, Ryoo R, Jeong KE, Park YK, Appl. Catal. B: Environ., 95(3-4), 365 (2010)
Kim YM, Lee HW, Lee SH, Kim SS, Park SH, Jeon JK, Kim S, Park YK, Korean J. Chem. Eng., 28(10), 2012 (2011)
Kim BS, Jeong CS, Kim JM, Bin Park S, Park SH, Jeon JK, Jung SC, Kim SC, Park YK, Catal. Today, 265, 184 (2016)
Yang J, Chen H, Zhao W, Zhou J, J. Anal. Appl. Pyrolysis, 117, 296 (2016)
Challinor JM, J. Anal. Appl. Pyrolysis, 25, 349 (1993)
Schultz EL, Mullen CA, Boateng AA, Energy Technol., 5, 196 (2017)