Thermogravimetric assessment of the thermal degradation during combustion of crude and pure glycerol

被引:17
作者
Almazrouei, Manar [1 ]
Adeyemi, Idowu [2 ,3 ]
Janajreh, Isam [2 ,3 ]
机构
[1] United Arab Emirates Univ, Dept Mech Engn, Al Ain 15551, U Arab Emirates
[2] Khalifa Univ, Dept Mech Engn, Abu Dhabi 127788, U Arab Emirates
[3] Khalifa Univ, Ctr Membrane & Adv Water Technol, Abu Dhabi 127788, U Arab Emirates
关键词
Pure/crude glycerol; Thermogravimetric analysis; Kinetics parameters; Thermodynamic properties; THERMODYNAMIC PARAMETERS; BIODIESEL PRODUCTION; KINETIC-ANALYSIS; PYROLYSIS; BIOMASS; COAL; TRANSESTERIFICATION; TEMPERATURES; IGNITION; OIL;
D O I
10.1007/s13399-022-02526-w
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
According to the United States Energy Information Administration (US EIA), the annual pure biodiesel production in the USA was 6.88 million cubic meters in 2020. Similarly, significant biodiesel production was reported across the world with countries like Brazil, Germany, and Indonesia estimated to have produced 5.9, 3.2, and 6.2 million cubic meters in 2019. This enormous biodiesel production, which is widespread globally, has led to huge amount of waste in the form of glycerol as a product of transesterification. It was estimated that crude glycerol production was 189.27 million cubic meters in 2021. Thermochemical conversion processes, such as combustion, gasification, and pyrolysis, are viable ways to utilize the waste glycerol. In this study, the thermogravimetric analyzer was used to investigate and compare the characteristics of crude and pure glycerol combustion. In particular, the kinetic and thermodynamic parameters as well as the ignition and burnout temperatures were evaluated for the two fuels. The glycerol samples were subjected to a temperature range of 50-700 degrees C under dissimilar heating rates, i.e., 5, 10, 15, and 20 degrees C/min. Results of the thermal decomposition process indicate that while there is a single stage in pure glycerol, the crude glycerol is characterized with three decomposition stages. In addition, the experimental results showed that the main combustion process in both samples occurred at about 150-(325 +/- 25) degrees C. The effect of heating rate on TG and DTG curves showed that at higher heating rates, the degradation curves shifts to higher temperature values. The crude glycerol ignition temperature is in the range of 195-218 degrees C compared to 180-212 degrees C for pure glycerol, and their burnout temperatures were 463-508 degrees C and 238-276 degrees C, respectively. The activation energies were evaluated with Kissinger method and found to be 75 kJ/mol for the devolatilization event in the crude glycerol and 79.6 kJ/mol for the pure glycerol.
引用
收藏
页码:4403 / 4417
页数:15
相关论文
共 44 条
[1]   The effect of wood biomass blending with pulverized coal on combustion characteristics under oxy-fuel condition [J].
Ahn, Seongyool ;
Choi, Gyungmin ;
Kim, Duckjool .
BIOMASS & BIOENERGY, 2014, 71 :144-154
[2]   Model-fitting approach to kinetic analysis of non-isothermal pyrolysis of pure and crude glycerol [J].
Almazrouei, Manar ;
Janajreh, Isam .
RENEWABLE ENERGY, 2020, 145 :1693-1708
[3]   Thermogravimetric study of the combustion characteristics of biodiesel and petroleum diesel [J].
Almazrouei, Manar ;
Janajreh, Isam .
JOURNAL OF THERMAL ANALYSIS AND CALORIMETRY, 2019, 136 (02) :925-935
[4]   Glycerol Production and Transformation: A Critical Review with Particular Emphasis on Glycerol Reforming Reaction for Producing Hydrogen in Conventional and Membrane Reactors [J].
Bagnato, Giuseppe ;
Iulianelli, Adolfo ;
Sanna, Aimaro ;
Basile, Angelo .
MEMBRANES, 2017, 7 (02)
[5]   Pyrolysis of pellets made with biomass and glycerol: Kinetic analysis and evolved gas analysis [J].
Bartocci, P. ;
Anca-Couce, A. ;
Slopiecka, K. ;
Nefkens, S. ;
Evic, N. ;
Retschitzegger, S. ;
Barbanera, M. ;
Buratti, C. ;
Cotana, F. ;
Bidini, G. ;
Fantozzi, F. .
BIOMASS & BIOENERGY, 2017, 97 :11-19
[6]   Homer Kissinger and the Kissinger equation [J].
Blaine, Roger L. ;
Kissinger, Homer E. .
THERMOCHIMICA ACTA, 2012, 540 :1-6
[7]   Glycerol combustion and emissions [J].
Bohon, Myles D. ;
Metzger, Brian A. ;
Linak, William P. ;
King, Charly J. ;
Roberts, William L. .
PROCEEDINGS OF THE COMBUSTION INSTITUTE, 2011, 33 :2717-2724
[8]   Kinetic study of thermal processing of glycerol by thermogravimetry [J].
Castello, Margarida L. ;
Dweck, Jo ;
Aranda, Donato A. G. .
JOURNAL OF THERMAL ANALYSIS AND CALORIMETRY, 2011, 105 (03) :737-746
[9]   Glycerol waste to value added products and its potential applications [J].
Chilakamarry, Chaitanya Reddy ;
Sakinah, A. M. Mimi ;
Zularisam, A. W. ;
Pandey, Ashok .
SYSTEMS MICROBIOLOGY AND BIOMANUFACTURING, 2021, 1 (04) :378-396
[10]   Continuous esterification for biodiesel production from palm fatty acid distillate using economical process [J].
Chongkhong, S. ;
Tongurai, C. ;
Chetpattananondh, R. .
RENEWABLE ENERGY, 2009, 34 (04) :1059-1063