2020
DOI: 10.1021/acs.energyfuels.0c00200
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Reactivity of Vacuum Residues by Thermogravimetric Analysis and Nuclear Magnetic Resonance Spectroscopy

Abstract: In this work, the thermal cracking process of seventeen (17) vacuum residues from Colombian crude oils is studied. Cracking tests are carried out in a batch microreactor at 390, 410, 420, and 430 °C, during 60 min of reaction and in an inert atmosphere with nitrogen. The quality of the vacuum residues and its products, obtained under thermal cracking conditions, is determined by thermogravimetric analysis and proton nuclear magnetic resonance (1H NMR) spectroscopy, whereas the yield of liquid products is calcu… Show more

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Cited by 14 publications
(8 citation statements)
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“…This observation confirms that the thermal cracking process is preceded by a vaporization stage, but as the temperature increases more chemical cracking reactions are induced. The thermal reaction stages in the TGA results are represented by the activation energies E a 1 and E a 2 , corresponding to the vaporization and thermal cracking stages, and can be calculated from the slopes − E a / R of the straight lines 27 . The kinetic parameters of the vaporization and thermal cracking sections were obtained by linear regression.…”
Section: Resultsmentioning
confidence: 99%
See 1 more Smart Citation
“…This observation confirms that the thermal cracking process is preceded by a vaporization stage, but as the temperature increases more chemical cracking reactions are induced. The thermal reaction stages in the TGA results are represented by the activation energies E a 1 and E a 2 , corresponding to the vaporization and thermal cracking stages, and can be calculated from the slopes − E a / R of the straight lines 27 . The kinetic parameters of the vaporization and thermal cracking sections were obtained by linear regression.…”
Section: Resultsmentioning
confidence: 99%
“…Further analysis of the thermal stability of the upgraded oil was performed by calculating the activation energy of oil-cracking conversion using the kinetic model discussed in reference [27]. In this model, the oil fraction…”
Section: The Effect Of Temperature and Surfactant On Bitumen's Activa...mentioning
confidence: 99%
“…Then, the reactor is pressurized with nitrogen at room temperature. Figure shows a schematic of the reaction system used for aquathermolysis …”
Section: Methodsmentioning
confidence: 99%
“…Figure 1 shows a schematic of the reaction system used for aquathermolysis. 52 The reactions were carried out at 270 °C, with a pressure of 5.51 MPa. The reaction time was 66 h. The aquathermolysis reactions without catalyst (no catalyst) were carried out under the same temperature, pressure, and reaction time conditions.…”
Section: Catalytic Aquathermolysis Testsmentioning
confidence: 99%
“…Combustibles líquidos (Agudelo et al, 2011;Baldrich & Novoa, 2006;Benjumea et al, 2008;Cacua et al, 2011b;Zuleta et al, 2012) y sólidos(É. Arenas & Chejne, 2004;Blandon et al, 2008;Díez & Pérez, 2017;Jiménez et al, 2012;Orrego et al, 2010;Orrego-Ruiz et al, 2011;Reyes et al, 2003) Fracciones de petróleo (Baldrich Ferrer & Novoa Mantilla, 2007;León et al, 2020;Morantes et al, 2019;Poveda-Jaramillo et al, 2016;Villabona-Estupiñan et al, 2020) Productos de la combustión (Arias et al, 2021;Ávila et al, 2021;Botero et al, 2020Botero et al, , 2021Cadrazco et al, 2019Cadrazco et al, , 2020Johnson-Restrepo et al, 2008;Mendoza et al, 2021;Oliveira et al, 2019;Parga-Lozano et al, 2002;Soriano et al, 2020) Propiedades claves de combustibles como velocidad de llama laminar, las dimensiones y temperatura de la llama, el índice Wobbe, los calores inferiores y superiores de combustión, los límites de inflamabilidad y el punto de rocío (Álvarez et al, 2019;Burbano et al, 2011aBurbano et al, , 2011bCacua et al, 2011b;Y. Cadavid & Amell, 2019;Cala et al, 2013;Cardona Medina et al, 2013;Cardona-Vargas et al, 2020;Cardona Vargas & Amell-Arrieta Andrés Adolfo Arrieta Carlos, 2016;…”
Section: Koreaunclassified