Investigation of carbon dioxide photoreduction process in a laboratory-scale photoreactor by computational fluid dynamic and reaction kinetic modeling

被引:7
|
作者
Lu, Xuesong [1 ]
Luo, Xiaojiao [1 ]
Thompson, Warren A. [1 ]
Tan, Jeannie Z. Y. [1 ]
Maroto-Valer, M. Mercedes [1 ]
机构
[1] Heriot Watt Univ, Sch Engn & Phys Sci, Res Ctr Carbon Solut, Edinburgh EH14 4AS, Midlothian, Scotland
基金
英国工程与自然科学研究理事会;
关键词
carbon dioxide photoreduction; computational fluid dynamic simulation; kinetic model; Langmuir adsorption; PHOTOCATALYTIC CO2 REDUCTION; TIO2; NANOPARTICLES; CH4; ADSORPTION; HYDROGEN; H2O; TRANSITION; CONVERSION; TITANIA; OXYGEN;
D O I
10.1007/s11705-021-2096-0
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The production of solar fuels via the photoreduction of carbon dioxide to methane by titanium oxide is a promising process to control greenhouse gas emissions and provide alternative renewable fuels. Although several reaction mechanisms have been proposed, the detailed steps are still ambiguous, and the limiting factors are not well defined. To improve our understanding of the mechanisms of carbon dioxide photoreduction, a multi-physics model was developed using COMSOL. The novelty of this work is the computational fluid dynamic model combined with the novel carbon dioxide photoreduction intrinsic reaction kinetic model, which was built based on three-steps, namely gas adsorption, surface reactions and desorption, while the ultraviolet light intensity distribution was simulated by the Gaussian distribution model and Beer-Lambert model. The carbon dioxide photoreduction process conducted in a laboratory-scale reactor under different carbon dioxide and water moisture partial pressures was then modeled based on the intrinsic kinetic model. It was found that the simulation results for methane, carbon monoxide and hydrogen yield match the experiments in the concentration range of 10(-4) mol.m(-3) at the low carbon dioxide and water moisture partial pressure. Finally, the factors of adsorption site concentration, adsorption equilibrium constant, ultraviolet light intensity and temperature were evaluated.
引用
收藏
页码:1149 / 1163
页数:15
相关论文
共 14 条
  • [11] Computational fluid dynamic modeling and simulation of biomass pyrolysis vapor-phase upgrading process at reactor scale
    Gao, Xi
    Li, Tingwen
    Rogers, William
    Panday, Rupen
    Li, Cheng
    Ashfaq, Huda
    Hughes, Bryan
    ABSTRACTS OF PAPERS OF THE AMERICAN CHEMICAL SOCIETY, 2019, 258
  • [12] Computational fluid-dynamic investigation of a centrifugal compressor with inlet guide vanes for supercritical carbon dioxide power systems
    Romei, Alessandro
    Gaetani, Paolo
    Persico, Giacomo
    ENERGY, 2022, 255
  • [13] Using The Computational Fluid Dynamic Software To Mixing Process Modeling In The Industrial Scale Vessel With Side-Mounted Agitator
    Havryliv, Roman
    Kostiv, Iryna
    Maystruk, Volodymyr
    2020 10TH INTERNATIONAL CONFERENCE ON ADVANCED COMPUTER INFORMATION TECHNOLOGIES (ACIT), 2020, : 192 - 195
  • [14] Investigation of Variable Impurity Profile from a Mitsunobu Reaction Using Insights from Kinetic Modeling, Multi-Phase Interactions, and Computational Fluid Dynamics
    Mukherjee, Samrat
    Bordawekar, Shailendra
    Nere, Nandkishor
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2016, 55 (17) : 4867 - 4877