Kinetics of Solid-Gas Reactions and Their Application to Carbonate Looping Systems

被引:95
作者
Fedunik-Hofman, Larissa [1 ,2 ]
Bayon, Alicia [2 ]
Donne, Scott W. [1 ]
机构
[1] Univ Newcastle, Discipline Chem, Callaghan, NSW 2308, Australia
[2] CSIRO Energy, POB 330, Newcastle, NSW 2300, Australia
关键词
kinetics; solid-gas reactions; carbonate looping; calcium looping; thermochemical energy storage; carbon capture and storage; THERMOCHEMICAL ENERGY-STORAGE; THERMAL-DECOMPOSITION KINETICS; CALCIUM-OXIDE CARBONATION; CO2; CAPTURE; SIZE-DISTRIBUTION; CAO-CARBONATION; PRODUCT LAYER; PARTICLE-SIZE; GRAIN-SIZE; MODEL;
D O I
10.3390/en12152981
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
Reaction kinetics is an important field of study in chemical engineering to translate laboratory-scale studies to large-scale reactor conditions. The procedures used to determine kinetic parameters (activation energy, pre-exponential factor and the reaction model) include model-fitting, model-free and generalized methods, which have been extensively used in published literature to model solid-gas reactions. A comprehensive review of kinetic analysis methods will be presented using the example of carbonate looping, an important process applied to thermochemical energy storage and carbon capture technologies. The kinetic parameters obtained by different methods for both the calcination and carbonation reactions are compared. The experimental conditions, material properties and the kinetic method are found to strongly influence the kinetic parameters and recommendations are provided for the analysis of both reactions. Of the methods, isoconversional techniques are encouraged to arrive at non-mechanistic parameters for calcination, while for carbonation, material characterization is recommended before choosing a specific kinetic analysis method.
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页数:35
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