Second generation biofuels production from waste cooking oil via pyrolysis process

被引:0
作者
Ben Hassen Trabelsi A. [1 ]
Zaafouri K. [2 ]
Baghdadi W. [1 ]
Naoui S. [1 ]
Ouerghi A. [1 ,2 ]
机构
[1] Laboratory of Wind Energy Control and Waste Energy Recovery, LMEEVED, Research and Technology Centre of Energy, CRTEn, Borj-CedriaTechnopark, B.P No. 95, 2050, Hammam Lif
[2] Laboratory of Microbial Ecology and Technology, LETMi-INSAT, The National Institute of Applied Sciences and Technology INSAT, Carthage University, 2 Boulevard de la Terre, BP 676, Tunis
关键词
Bio-oil; Biochar; Pyrolysis; Stochiometric model; Syngas; Waste cooking oil;
D O I
10.1016/j.renene.2018.04.002
中图分类号
学科分类号
摘要
The thermal cracking of waste cooking oil (WCO) via pyrolysis was performed using a laboratory scale fixed-bed reactor. The effects of the final pyrolysis temperature (from 550 °C to 800 °C) and the heating rate (5 °C/min, 15 °C/min, 20 °C/min, 25 °C/min) on pyrolysis products distribution has been investigated and a maximum bio-oil yield of 80 wt% has been obtained at 800 °C and 15 °C/min. The bio-oil fuel properties shows that this pyrolytic oil has high caloric value (HHV around 8843 kg/Kcal) promoting its use as a liquid fuel but some other properties (high acidity index around 126.8 mg KOH/g sample and high viscosity about 8.95 cSt) need to be upgraded. The GC/MS characterization of the bio-oil highlights its high molecular complexity allowing it to be used as source of chemical products and of active molecules. The syngas heating value (reaching 8 MJ/kg) is suitable for its application as source of energy for the pyrolysis reactor. The remaining biochar is suitable for application as fertilizer since it is rich of iron and organic carbon. The stochiometric model of WCO pyrolysis has been established basing on the pyrolysis products yields, the CHNS-O composition of raw material and remaining biochar, and the syngas chemical composition. © 2018 Elsevier Ltd
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页码:888 / 896
页数:8
相关论文
共 31 条
[11]  
Gornay J., Transformation par voie thermique de triglycerides et d'acides gras. Application a la valorisation chimique des dechets lipidiques, (2006)
[12]  
Wiggers V.R., Meier H.F., Wisniewski A., ChivangaBarros A.A., WolfMaciel M.R., Biofuels from continuous fast pyrolysis of soybean oil: a pilotplant study, Bioresour. Technol, 100, Issue 24, pp. 6570-6577, (2009)
[13]  
Wisniewski J.A., Wiggers V.R., Simionatto E.L., Meier H.F., Barros A.A.C., Madureira L.A.S., Fuel, 89, pp. 563-568, (2010)
[14]  
Kraiem T., Ben Hassen-Trabelsi A., Naoui S., Belayouni H., Jeguirim M., Characterization of the liquid products obtained fromTunisianwaste fish fats using the pyrolysis process, Fuel Processing Technology, 138, pp. 404-412, (2015)
[15]  
Kitamura K., Studies of pyrolysis of triglycerides, Bull. Chem. Soc. Jpn, 44, pp. 1606-1609, (1971)
[16]  
Higman E.B., Schmeltz I., Higman H.C., Chortyk O.T., Studies on thermal degradation of naturally occurring materials. 2. Products from pyrolysis of triglycerides at 400 degrees, J. Agric. Food Chem., 21, pp. 202-204, (1973)
[17]  
Chang C.C., Wan S.W., Chinas motor fuels from tung oil, Ind. Eng. Chem., 39, pp. 1543-1548, (1947)
[18]  
Schwab A.W., Dykstra G.J., Selke E., Sorenson S.C., Pryde E.H., Diesel fuel from thermal-decomposition of soybean oil, JAOCS, 65, pp. 1781-1786, (1988)
[19]  
Idem R.O., Katikaneni S.P.R., Bakhshi N.N., Thermal cracking of canola oil: reaction products in the presence and absence of steam, Energy Fuels, 10, pp. 1150-1162, (1996)
[20]  
Lima S.D.G., Soares V.C.D., Ribeiro E.B., Carvalho D.A., Cardoso E.C.V., Rassi F.C., Diesel-like fuel obtained by pyrolysis of vegetable oils, J. Anal. Appl. Pyrolysis, 71, pp. 987-996, (2004)