New approximations of the temperature integral for nonisothermal kinetics

1995 ◽  
Vol 44 (5) ◽  
pp. 1147-1154 ◽  
Author(s):  
R. Quanyin ◽  
Y. Su
Keyword(s):  
Nonisothermal Kinetics ◽  
Temperature Integral

New temperature integral approximation for nonisothermal kinetics

AIChE Journal ◽  
2006 ◽  
Vol 52 (4) ◽  
pp. 1554-1557 ◽  
Author(s):  
Junmeng Cai ◽  
Fusheng Yao ◽  
Weiming Yi ◽  
Fang He
Keyword(s):  
Nonisothermal Kinetics ◽  
Temperature Integral ◽  
Integral Approximation

Nonisothermal Kinetics of the Solid-Solid Phase Transitions in the Perovskite Type Layer Compounds (CnH2n+1NH3)2ZnCl4

2008 ◽  
Vol 26 (1) ◽  
pp. 216-219 ◽  
Author(s):  
Ke-Zhong WU ◽  
Jian-Ling LI ◽  
Jian-Jun ZHANG ◽  
Xiao-Di LIU
Keyword(s):  
Phase Transitions ◽  
Solid Phase ◽  
Nonisothermal Kinetics ◽  
Type Layer ◽  
Kinetics Of ◽  
Perovskite Type

scholarly journals Pyrolysis Kinetic Parameters of Omari Oil Shale Using Thermogravimetric Analysis

Energies ◽  
2020 ◽  
Vol 13 (16) ◽  
pp. 4060
Author(s):  
Ziad Abu El-Rub ◽  
Joanna Kujawa ◽  
Samer Al-Gharabli
Keyword(s):  
Activation Energy ◽  
Thermogravimetric Analysis ◽  
Kinetic Parameters ◽  
Oil Shale ◽  
Arrhenius Plot ◽  
Frequency Factor ◽  
Coefficient Of Determination ◽  
Assay Method ◽  
Temperature Integral ◽  
Integral Approximation

Oil shale is one of the alternative energies and fuel solutions in Jordan because of the scarcity of conventional sources, such as petroleum, coal, and gas. Oil from oil shale reservoirs can be produced commercially by pyrolysis technology. To optimize the process, mechanisms and rates of reactions need to be investigated. Omari oil shale formation in Jordan was selected as a case study, for which no kinetic models are available in the literature. Oil shale was analyzed using the Fischer assay method, proximate analysis (moisture, volatile, and ash), gross calorific value, elemental analysis (CHNS), and X-ray fluorescence (XRF) measurements. Non-isothermal thermogravimetric analysis was applied to study the kinetic parameters (activation energy and frequency factor) at four selected heating rates (5, 10, 15, and 20 °C/min). When oil shale was heated from room temperature to 1100 °C, the weight loss profile exhibited three different zones: drying (devolatilization), pyrolysis, and mineral decomposition. For each zone, the kinetic parameters were calculated using three selected methods: integral, temperature integral approximation, and direct Arrhenius plot. Furthermore, the activation energy in the pyrolysis zone was 112–116 kJ/mol, while the frequency factor was 2.0 × 107 − 1.5 × 109 min−1. Moreover, the heating rate has a directly proportional relationship with the rate constant at each zone. The three different methods gave comparable results for the kinetic parameters with a higher coefficient of determination (R2) for the integral and temperature integral approximation compared with the direct Arrhenius plot. The determined kinetic parameters for Omari formation can be employed in developing pyrolysis reactor models.

Using equations of nonisothermal kinetics for determining the course region of thermal decomposition of copper arsenide

2011 ◽  
Vol 52 (5) ◽  
pp. 406-409
Author(s):  
A. S. Abramov ◽  
V. E. Khrapunov ◽  
A. V. Nitsenko ◽  
R. A. Isakova
Keyword(s):  
Thermal Decomposition ◽  
Nonisothermal Kinetics ◽  
Copper Arsenide
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