Pyrolysis behaviors of waste coconut shell and husk biomasses

Pyrolysis behaviors of waste coconut shell and husk biomasses

Q. WANG J. SARKAR

Graduate School of Science and Engineering Saitama University, Japan

Page: 
34-43
|
DOI: 
https://doi.org/10.2495/EQ-V3-N1-34-43
Received: 
N/A
| |
Accepted: 
N/A
| | Citation

OPEN ACCESS

Abstract: 

Coconut shell and husk are two biomasses wastes abundant in most of the coastal countries. However, despite their enormous potential as energy sources, they are hardly studied and their thermal characteristics are still not well known. In this study, both biomasses are thermally degraded through thermogravimetry (TG-DTA) and their pyrolysis product yield such as char, tar and gases are analyzed. The TG-DTA results show that pyrolysis of biomass consists of three stages. Three stages can be out- lined as: (1) dehydration process for temperatures below 122°C, (2) pyrolytic cracking from 122°C to 400°C, stage consist of two exothermic simultaneous processes where hemicelluloses, cellulose and lignin are decomposed and a high amount of volatile matter formation occurs and (3) the last endother- mic decomposition of the lignin at temperatures above 400°C. From the pyrolytic results, it is showed that the char and gases yields were increased with the decrement tar. The gas-evolving profiles from pyrolyzing the coconut shell and husk components in a packed bed, monitored by a GC-TCD and a GC-FID, showed similar behavior. H2 was released out at a higher temperature (>450°C) and it got the maximum rate at 700°C then it decreased. CO2 was released out at 130°C–750°C and got the maximum releasing value at 300°C–400°C. The released CO showed almost similar pattern with that of CO2. However, the release rate was lower than CO2 and the maximum release rate of CO was found at 300°C –400°C. CH4 was released out at the temperature between 200°C –850°C, and it got the maximum rate at 550°C. The releasing of hydrocarbon was generally very low.

Keywords: 

biomass, fixed bed, pyrolysis, TGA, thermogravimetry

  References

[1] Asadullah, M., Rahman, M.A., Ali, M.M., Rahman, M.S., Motin, M.A., Sultan, M.B. & Alam, M.R., Production of bio-oil from fixed bed pyrolysis of bagasse. Fuel, 86, pp. 2514–2520, 2007.https://doi.org/10.1016/j.fuel.2007.02.007

[2] Appenzeller, T., The end of cheap oil. National Geographic. June 2004.

[3] “China and India: A Rage for Oil”, Business Week, 25 August 2005.

[4] Biomass Energy Center. Available at: http://www.Biomassenergycentre.org.uk

[5] Demirbas, A., Biomass resource facilities and biomass conversion processing for fuels and chemicals. Energy conversion and Management, 42(11), pp. 1357–1378, 2001.https://doi.org/10.1016/s0196-8904(00)00137-0

[6] Chan, E. & Elevitch, C.R., Cocos nucifera (coconut) (version 2.1), 2006.

[7] Shashikumar, S. & Chandrashekar, H.M., An analysis of production and marketing of coconut in Tumkur District, India. International Journal of Current Research and Academic Review, 2(10), pp. 167–175, 2014.

[8] Bangladesh Census of Agriculture, Department of Census and Statistics, 2011.

[9] Reed, A.R. & Williams, P.T., Thermal processing of biomass natural fibre wastes by pyrolysis. International Journal of Energy Research, 28, pp. 131–145, 2004.https://doi.org/10.1002/er.956

[10] White, J.E., Catallo, W.J. & Legendre, B.L., Biomass pyrolysis kinetics: a comparative critical review with relevant agricultural residue case studies. Journal Analytical and Applied Pyrolysis, 91(1), pp. 1–33, 2011.https://doi.org/10.1016/j.jaap.2011.01.004

[11] Bilbao, R., Mastral, J.F., Aldea, M.E. & Ceamanos, J., The influence of the percentage of oxygen in the atmosphere on the thermal decomposition of lignocellulosic materials. Journal Analytical and Applied Pyrolysis, 42, pp. 189–202, 1997.https://doi.org/10.1016/s0165-2370(97)00050-8

[12] Burhenne, L., Messmer, J., Aicher, T. & Laborie, M-P., The effect of the biomass components lignin, cellulose and hemicellulose on TGA and fixed bed pyrolysis. Journal of Analytical and Applied Pyrolysis, 101, pp. 177–184, 2013.https://doi.org/10.1016/j.jaap.2013.01.012

[13] Worasuwannarak, N., Sonobe, T. & Tanthapanichakoon, W., Pyrolysis behaviors of rice straw, rice husk, and corncob by TG-MS technique. Journal Analytical and Applied Pyrolysis, 78, pp. 265–271, 2007.https://doi.org/10.1016/j.jaap.2006.08.002

[14] Wang, Q., Endo, T., Aparu, P. & Kurogawa, H., Study on biomass tar reduction by ash and fluidizing medium in a heterogeneous reaction. International Journal of Sustainable Development and Planning, 9(5), pp. 669–679, 2014.https://doi.org/10.2495/sdp-v9-n5-669-679

[15] Wang, Q., Apaer, P., Kurokawa, H. & Sugiyama, K., Reactivity for pyrolysis and CO2 gasification of alkali metal loaded waste wood char. International Journal of Sustainable Development and Planning, 9(5), pp. 680–691, 2014.https://doi.org/10.2495/sdp-v9-n5-680-691

[16] Wang, Q., Niida, H., Liu, C., Kurokawa, H., Sarkar, A., Sekiguchi, K. & Sugiyama, K., Oil aggregated behavior for coal recovery and combustion characteristics of their aggregates from different grade coals. International Journal of Sustainable Development and Planning, 9(5), pp. 692–704, 2014.https://doi.org/10.2495/sdp-v9-n5-692-704

[17] Wang, W., Aparu, P., Kurogawa, H. & Sugiyama, K., Recovery briquetting technologies of waste biomass and pyrolyzed waste char produced from solid industrial and agricultural organic wastes. International Journal of Sustainable Development and Planning, 9(5), pp. 705–716, 2014. https://doi.org/10.2495/sdp-v9-n5-705-716