ISSN: 0256-1115 (print version) ISSN: 1975-7220 (electronic version)
Copyright © 2024 KICHE. All rights reserved

Articles & Issues

Language
English
Conflict of Interest
In relation to this article, we declare that there is no conflict of interest.
Publication history
Received March 5, 2021
Accepted May 11, 2021
articles 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

Effect of temperature and feed rate on pyrolysis oil produced via helical screw fluidized bed reactor

1Department of Chemical Engineering, Faculty of Engineering, University of Malaya, Kuala Lumpur, Malaysia 2School of Energy and Chemical Engineering, Xiamen University Malaysia, Jalan Sunsuria, Bandar Sunsuria, 43900 Sepang, Selangor Darul Ehsan, Malaysia 3College of Chemistry and Chemical Engineering, Xiamen University, Xiamen, 361005, Fujian, China 4Department of Chemical and Materials Engineering, Faculty of Engineering, King Abdulaziz University, Rabigh, 21911, Saudi Arabia
Korean Journal of Chemical Engineering, September 2021, 38(9), 1797-1809(13), 10.1007/s11814-021-0842-0
downloadDownload PDF

Abstract

A series of experiments was conducted to study the effect of temperature and feed rate on physicochemical properties and yield of bio-oil. The experiments were performed in a helical screw fluidized bed reactor and about 150-gram palm shell (PS) was pyrolyzed in each run at 275 °C/min heating rate. The first set of experiments was conducted at temperature ranging from 400 to 650 °C without using any inert gas for fluidization. While the second set of experiments were performed at feed rates ranging from 3 to 25 g/min in order to investigate the effects of feed rate on pyrolytic products. Results showed that the bio-oil yield was increased with the increase in temperature and feed rate due to the enhanced biomass volatilization. In a similar vein to this, a greater extent in oxygenates cracking was also noted in the bio-oil. A maximum liquid yield of about 72.84 wt% was obtained at 500°C, while 72.92 wt% liquid yield was obtained with 25 g/min feed rate. The HHV of bio-oil was also increased from 38.52 to 43.13 MJ/kg when pyrolysis temperature was increased from 400 to 650 °C.

References

Ayala-Cortes A, Lobato-Peralta DR, Arreola-Ramos CE, et al., J. Anal. Appl. Pyrolysis, 140, 290 (2019)
Miranda T, Montero I, Sepulveda FJ, Arranz JI, Rojas CV, Nogales S, Mater., 8, 1413 (2015)
Abnisa F, Arami-Niya A, Daud WMAW, Sahu JN, Noor IM, Energy Conv. Manag., 76, 1073 (2013)
Qureshi KM, Abnisa F, Wan Daud WMA, J. Anal. Appl. Pyrolysis, 142, 104605 (2019)
Akhtar J, Amin NS, Renew. Sust. Energ. Rev., 16, 5101 (2016)
Qureshi KM, Kay Lup AN, Khan S, Abnisa F, Daud WMAW, J. Anal. Appl. Pyrolysis, 131, 52 (2018)
Xiong Z, Syed-Hassan SSA, Hu X, Guo JH, Chen YJ, Liu Q, Wang Y, Su S, Hu S, Xiang J, Fuel, 233, 461 (2018)
Uddin MN, Techato K, Taweekun J, Rahman MM, Rasul MG, Mahlia TMI, Ashrafur SA, Energies, 11, 3115 (2018)
Jahirul MI, Rasul MG, Chowdhury AA, Ashwath N, Energies, 5, 4952 (2012)
Qureshi KM, Kay Lup AN, Khan S, Abnisa F, Wan Daud WMA, Cleaner Eng. Technol., 4, 100174 (2021)
Montoya JI, Chejne-Janna F, Garcia-Perez M, DYNA, 82, 239 (2015)
Quan C, Gao N, BioMed Res. Int., 2016, 619786 (2016)
Wang Y, Qiu L, Zhu M, Sun G, Zhang T, Kang K, Sci. Rep., 9, 5535 (2019)
Zaman CZ, et al., Pyrolysis, (2017).
Bridgwater AV, Biomass Bioenerg., 38, 68 (2012)
Kan T, Strezov V, Evans TJ, Renew. Sust. Energ. Rev., 57, 1126 (2016)
Bhattacharjee N, Biswas AB, J. Energy Inst., 91, 605 (2018)
Mutsengerere S, Chihobo CH, Musademba D, Nhapi I, Renew. Sust. Energ. Rev., 104, 328 (2019)
Heidari A, Stahl R, Younesi H, Rashidi A, Troeger N, Ghoreyshi AA, J. Ind. Eng. Chem., 20(4), 2594 (2014)
Zhou R, Lei H, Julson JL, Int. J. Agric. Biol. Eng., 6, 53 (2013)
Guedes RE, Luna AS, Torres AR, J. Anal. Appl. Pyrolysis, 129, 134 (2018)
Xiong QG, Aramideh S, Kong SC, Energy Fuels, 27(10), 5948 (2013)
Qureshi KM, Abnisa F, Wan Daud WMA, J. Anal. Appl. Pyrolysis, 142, 104605 (2019)
Abnisa F, Daud WMAW, Husin WNW, Sahu JN, Biomass Bioenerg., 35(5), 1863 (2011)
Moraes MSA, et al., Frontiers in bioenergy and biofuels (2017).
Lu Y, Li GS, Lu YC, Fan X, Wei XY, Int. J. Anal. Chem.,., 2017, 929852 (2017)
Montoya JI, Chejne-Janna F, Garcia-Perez M, DYNA, 82, 239 (2015)
Ranzi E, Cuoci A, Faravelli T, Frassoldati A, Migliavacca G, Pierucci S, Sommariva S, Energy Fuels, 22(6), 4292 (2008)
Branca C, Di Blasi C, Ind. Eng. Chem. Res., 45(17), 5891 (2006)
Bridgwater AV, Biomass Bioenerg., 38, 68 (2012)
Powar RV, Gangil S, Int. J. Renew. Energy Res., 3, 519 (2013)
Kim SW, Koo BS, Ryu JW, Lee JS, Kim CJ, Lee DH, Kim GR, Choi S, Fuel Process. Technol., 108, 118 (2013)
Williams PT, Williams EA, J. Anal. Appl. Pyrolysis, 51, 107 (1999)
Zhou S, Garcia-Perez M, Pecha B, McDonald AG, Kersten SRA, Westerhof RJM, Energy Fuels, 27, 1428 (2013)
Jalalifar S, Abbassi R, Garaniya V, Hawboldt K, Ghiji M, Fuel, 234, 616 (2018)
Treedet W, Suntivarakorn R, Fuel Process. Technol., 179, 17 (2018)
Bardalai M, Mahanta DK, Int. J. Renew. Energy Res., 5, 277 (2015)
Tanvidkar PS, Catalytic up-gradation of bio-oil by pyrolysis of biomass (2015).
Bertero M, Gorostegui HA, Orrabalis CJ, Guzman CA, Calandri EL, Sedran U, Fuel, 116, 409 (2014)
Lu Q, Li WZ, Zhu XF, Energy Conv. Manag., 50(5), 1376 (2009)
Ringer M, Putsche V, Scahill J, Large-scale pyrolysis oil production: A technology assessment and economic analysis (2006).
Yiin CL, Yusup S, Udomsap P, Yoosuk B, Sukkasi S, Computer Aided Chem. Eng., 33, 223 (2014)
Kundu K, et al., Prospects of alternative transportation fuels (2018).
Hossain FM, Kosinkova J, Brown RJ, Ristovski Z, Hankamer B, Stephens E, Rainey TJ, Energies, 10, 467 (2017)
Kay Lup AN, Abnisa F, Daud WMAW, Aroua MK, Asia-Pacific J. Chem. Eng., 14, e2293 (2019)
Khan S, Kay Lup AN, Qureshi KM, Abnisa F, Wan Daud WMA, Patah MFA, J. Anal. Appl. Pyrolysis, 140, 1 (2019)
Lup ANK, Abnisa F, Daud WMAW, Aroua MK, J. Ind. Eng. Chem., 56, 1 (2017)
Lup ANK, Abnisa F, Daud WMAW, Aroua MK, Appl. Catal. A: Gen., 541, 87 (2017)
Lyu G, Wu S, Zhang H, Front. Energy Res., 3, 28 (2015)
Fu P, Hu S, Xiang J, Li P, Huang D, Jiang L, Zhang A, Zhang J, J. Anal. Appl. Pyrolysis, 88, 117 (2010)
Hu CS, Zhang HY, Xiao R, Energy Conv. Manag., 177, 765 (2018)
Chang SH, Biomass Bioenerg., 119, 263 (2018)
Ogunkanmi JO, Kulla DM, Omisanya NO, Sumaila M, Obada DO, Dodoo-Arhin D, Case Studies Therm. Eng., 12, 711 (2018)
Kay Lup AN, et al., Acidity, oxophilicity and hydrogen sticking probability of supported metal catalysts for hydrodeoxygenation process (2018).
Lup ANK, Abnisa F, Daud WMAW, Aroua MK, Chin. J. Chem. Eng., 27(2), 349 (2019)
Fan LL, Zhang YN, Liu SY, Zhou N, Chen P, Cheng YL, Addy M, Lu Q, Omar MM, Liu YH, Wang YP, Dai LL, Anderson E, Peng P, Lei HW, Ruan R, Bioresour. Technol., 241, 1118 (2017)
Miranda T, Montero I, Sepulveda FJ, Arranz JI, Rojas CV, Nogales S, Materials, 8, 1413 (2015)
Rafiq MK, Bachmann RT, Rafiq MT, Shang Z, Joseph S, Long R, PloS One, 11, e01568 (2016)
Hamza UD, Nasri NS, Amin NS, Mohammed J, Zain HM, Desalin. Water Treat., 57, 7999 (2016)
Yang HP, Yan R, Chen HP, Lee DH, Zheng CG, Fuel, 86(12-13), 1781 (2007)
Lu Y, Lu YC, Hu HQ, Xie FJ, Wei XY, Fan X, J. Spectroscopy, 2017, 1 (2017)
Kim SJ, Jung SH, Kim JS, Bioresour. Technol., 101(23), 9294 (2010)

The Korean Institute of Chemical Engineers. F5, 119, Anam-ro, Seongbuk-gu, 233 Spring Street Seoul 02856, South Korea.
Phone No. +82-2-458-3078FAX No. +82-507-804-0669E-mail : kiche@kiche.or.kr

Copyright (C) KICHE.all rights reserved.

- Korean Journal of Chemical Engineering 상단으로