2019
DOI: 10.1016/j.fuel.2018.10.093
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Assessment of combustion rates of coal chars for oxy-combustion applications

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Cited by 30 publications
(22 citation statements)
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“…Insights about the kinetics of n -C 7 asphaltene catalytic oxidation were realized on the basis of fitting a n -order kinetic model. , The instantaneous reactivity r of the fraction is described by eqs and where P O 2 n (bar) represents the partial pressure of the reactant gas (O 2 ), k is the velocity constant, θ is associated with the conversion of asphaltene at any time t , n is the order of reaction, R (J mol –1 K –1 ) is the universal gas constant, E a (kJ mol –1 ) is the effective activation energy, k o (s –1 bar – n ) is the pre-exponential factor, and f (θ) considers the asphaltene conversion degree during the test. Variable separation and integration was performed to eq , obtaining eq . , Considering the activation energy values constant and applying natural logarithm in both sides, eq is obtained where t a, i is the time for the reaction to reach a defined conversion degree (θ) at a given temperature ( i ). Considering the volumetric model for the radial consumption of the particle, eq is written as follows: Finally, the effective activation energy and pre-exponential factor are obtained from the slope and intercept through the plot ln­( t a, i ) against 1/ T i when 100% n -C 7 asphaltene consumption is reached.…”
Section: Methodsmentioning
confidence: 99%
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“…Insights about the kinetics of n -C 7 asphaltene catalytic oxidation were realized on the basis of fitting a n -order kinetic model. , The instantaneous reactivity r of the fraction is described by eqs and where P O 2 n (bar) represents the partial pressure of the reactant gas (O 2 ), k is the velocity constant, θ is associated with the conversion of asphaltene at any time t , n is the order of reaction, R (J mol –1 K –1 ) is the universal gas constant, E a (kJ mol –1 ) is the effective activation energy, k o (s –1 bar – n ) is the pre-exponential factor, and f (θ) considers the asphaltene conversion degree during the test. Variable separation and integration was performed to eq , obtaining eq . , Considering the activation energy values constant and applying natural logarithm in both sides, eq is obtained where t a, i is the time for the reaction to reach a defined conversion degree (θ) at a given temperature ( i ). Considering the volumetric model for the radial consumption of the particle, eq is written as follows: Finally, the effective activation energy and pre-exponential factor are obtained from the slope and intercept through the plot ln­( t a, i ) against 1/ T i when 100% n -C 7 asphaltene consumption is reached.…”
Section: Methodsmentioning
confidence: 99%
“…Insights about the kinetics of n-C 7 asphaltene catalytic oxidation were realized on the basis of fitting a n-order kinetic model. 48,49 The instantaneous reactivity r of the fraction is described by eqs 2 and 3 50…”
Section: Methodsmentioning
confidence: 99%
“…Since thermal decomposition of asphaltenes is a complex process that entails consecutive and parallel reactions, the kinetic variables allow a representation of the consecutive reaction history. 42,43 The instantaneous reactivity r of a fraction is described by the following expression (eq 1), for an n-order kinetic equation, 44 which can be rewritten as eq 2.…”
Section: Kinetic Analysis Of Asphaltene Thermo-oxidative Decompositionmentioning
confidence: 99%
“…Thermal behavior analysis is performed to obtain information about the kinetic parameters of asphaltene cracking under high-pressure conditions in different temperature regions. Since thermal decomposition of asphaltenes is a complex process that entails consecutive and parallel reactions, the kinetic variables allow a representation of the consecutive reaction history. , The instantaneous reactivity r of a fraction is described by the following expression (eq ), for an n -order kinetic equation, which can be rewritten as eq . where P O 2 n (bar) represents the pressure of the reactant gas (O 2 ), k is the velocity constant, θ is associated with the conversion of asphaltene at any time t , n is the order of reaction, R (kJ·mol –1 ·K –1 ) is the universal gas constant, E a (kJ·mol –1 ) is the effective activation energy, k o (s –1 ·bar – n ) is the pre-exponential factor, and F (θ) takes into account the asphaltene conversion degree during the test. Making a substitution for the heating rate, according to the expression β = d T /d t , employing the volumetric model for a radial consumption of the n -C 7 asphaltenes f (θ) = (1 – θ) and applying the Ozawa–Wall–Flynn approximation to resolve the integral of conversion, eq is obtained where F (θ) = ∫dθ/ f (θ).…”
Section: Kinetic Analysis Of Asphaltene Thermo-oxidative Decompositionmentioning
confidence: 99%
“…The n-C 7 asphaltene oxidation with and without nanocatalysts is described through a model based on the experimental results according to a single power-law expression, considering the instantaneous reactivity (r) of the adsorbate over wide pressure and temperatures ranges. 64,65 n-C 7 asphaltene conversion is herein defined as in eq 5 m m m m t 0 ()…”
Section: Modelingmentioning
confidence: 99%