[1]

Dang H, Xu R, Zhang J, Wang M, Zhang J. 2025. Interaction mechanism and kinetic modeling of anthracite and power plant biomass waste during CO2 co-gasification process. Energy 325:136115

doi: 10.1016/j.energy.2025.136115
[2]

Cao X, Bu C, Han Q, Zhao X, Piao G. 2024. Kinetic analysis and model evaluation for steam co-gasification of coal-biomass blended chars using macro-TGA. Fuel Processing Technology 266:108151

doi: 10.1016/j.fuproc.2024.108151
[3]

Ding L, Wang S, Li X, Bai T, Qiu Z, et al. 2024. Experimental and kinetic study of pressurized CO2 gasification of biomass chars. Chemical Engineering Research and Design 212:349−361

doi: 10.1016/j.cherd.2024.11.016
[4]

Wei R, Ren L, Liu L. 2026. Gasification reactivity and kinetic simulation of anthracite/biomass chars and co-pyrolysis chars. Renewable Energy 256:123916

doi: 10.1016/j.renene.2025.123916
[5]

Gupta A, Thengane SK, Mahajani S. 2018. CO2 gasification of char from lignocellulosic garden waste: experimental and kinetic study. Bioresource Technology 263:180−191

doi: 10.1016/j.biortech.2018.04.097
[6]

Iwaszenko S, Howaniec N, Smoliński A. 2019. Determination of random pore model parameters for underground coal gasification simulation. Energy 166:972−978

doi: 10.1016/j.energy.2018.10.156
[7]

Kudva IK, Shinde SG, Pandit K, Fan LS. 2026. Kinetic insights into biomass char gasification for chemical looping reactor design. Chemical Engineering and Processing - Process Intensification 219:110617

doi: 10.1016/j.cep.2025.110617
[8]

Cortazar M, Lopez G, Alvarez J, Arregi A, Amutio M, et al. 2020. Experimental study and modeling of biomass char gasification kinetics in a novel thermogravimetric flow reactor. Chemical Engineering Journal 396:125200

doi: 10.1016/j.cej.2020.125200
[9]

Zhang Y, Ashizawa M, Kajitani S, Miura K. 2008. Proposal of a semi-empirical kinetic model to reconcile with gasification reactivity profiles of biomass chars. Fuel 87:475−481

doi: 10.1016/j.fuel.2007.04.026
[10]

Grasa G, Martínez I, Murillo R. 2024. Gasification kinetics of chars from diverse residues under suitable conditions for the Sorption Enhanced Gasification process. Biomass and Bioenergy 180:107000

doi: 10.1016/j.biombioe.2023.107000
[11]

Felix CB, Chen WH, Ubando AT, Park YK, Lin KYA, et al. 2022. A comprehensive review of thermogravimetric analysis in lignocellulosic and algal biomass gasification. Chemical Engineering Journal 445:136730

doi: 10.1016/j.cej.2022.136730
[12]

Chew JJ, Soh M, Sunarso J, Yong ST, Doshi V, et al. 2020. Isothermal kinetic study of CO2 gasification of torrefied oil palm biomass. Biomass and Bioenergy 134:105487

doi: 10.1016/j.biombioe.2020.105487
[13]

Morin M, Pécate S, Hémati M. 2018. Kinetic study of biomass char combustion in a low temperature fluidized bed reactor. Chemical Engineering Journal 331:265−277

doi: 10.1016/j.cej.2017.08.063
[14]

Betancur M, Arenas CN, Martínez JD, Navarro MV, Murillo R. 2020. CO2 gasification of char derived from waste tire pyrolysis: Kinetic models comparison. Fuel 273:117745

doi: 10.1016/j.fuel.2020.117745
[15]

Parandin MS, Ale Ebrahim H, Norouzi HR. 2024. Towards random pore model for non-catalytic gas-solid reactions. Renewable and Sustainable Energy Reviews 202:114731

doi: 10.1016/j.rser.2024.114731
[16]

González-Vázquez MP, García R, Gil MV, Pevida C, Rubiera F. 2018. Unconventional biomass fuels for steam gasification: kinetic analysis and effect of ash composition on reactivity. Energy 155:426−437

doi: 10.1016/j.energy.2018.04.188
[17]

Gil MV, Fermoso J, Pevida C, Pis JJ, Rubiera F. 2010. Intrinsic char reactivity of plastic waste (PET) during CO2 gasification. Fuel Processing Technology 91:1776−1781

doi: 10.1016/j.fuproc.2010.07.019
[18]

Kramb J, DeMartini N, Perander M, Moilanen A, Konttinen J. 2016. Modeling of the catalytic effects of potassium and calcium on spruce wood gasification in CO2. Fuel Processing Technology 148:50−59

doi: 10.1016/j.fuproc.2016.01.031
[19]

Gomez A, Silbermann R, Mahinpey N. 2014. A comprehensive experimental procedure for CO2 coal gasification: is there really a maximum reaction rate? Applied Energy 124:73−81

doi: 10.1016/j.apenergy.2014.02.077