Hydrogen from catalytic non-thermal plasma-assisted steam methane reforming reaction

被引:4
|
作者
Bajpai, Abhinav [1 ]
Mehta, Shweta [2 ,3 ]
Joshi, Kavita [2 ,3 ]
Kumar, Sushant [1 ]
机构
[1] Indian Inst Technol Patna, Dept Chem & Biochem Engn, Gas Solid Interact Lab, Patna 801106, Bihar, India
[2] CSIR Natl Chem Lab, Phys & Mat Chem Div, Dr Homi Bhabha Rd, Pune 411008, India
[3] Acad Sci & Innovat Res AcSIR, Sect 19, Ghaziabad 201002, India
关键词
Steam methane reforming; Dielectric barrier discharge; Selectivity; Specific energy input; DFT; Non-thermal plasma; TOTAL-ENERGY CALCULATIONS; CARBON-DIOXIDE; ZNO NANOSTRUCTURES; OXIDATION; CO2; CONVERSION; CU; DISSOCIATION; ACTIVATION; SUPPORT;
D O I
10.1016/j.ijhydene.2023.03.281
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Steam methane reforming reaction was carried out in a dielectric barrier plasma reactor. A systematic study is conducted to understand the influence of input power, flow rate, and water for the conversion, yield, and selectivity of the reaction over strategically designed catalysts. In particular, the production rate and selectivity of the products (H2, CO and C2 hydrocarbons) are monitored. CeO2 was used as packing material, mixed with oxides of manganese or copper and their combination. The optimum Cu/CeO2 catalyst illustrated the production rate of 248.7 mmolg-1h-1 and 11.25 mmolg-1h-1 for H2, and CO, respectively at specific energy input of 19.8 JL-1. DFT calculations exhibit apparent change in electronic structure of the CeO2 after inclusion of oxides of manganese and copper that enhance interaction with methane. Based on these findings, a plausible mechanism is elucidatedSteam methane reforming reaction was carried out in a dielectric barrier plasma reactor. A systematic study is conducted to understand the influence of input power, flow rate, and water for the conversion, yield, and selectivity of the reaction over strategically designed catalysts. In particular, the production rate and selectivity of the products (H2, CO and C2 hydrocarbons) are monitored. CeO2 was used as packing material, mixed with oxides of manganese or copper and their combination. The optimum Cu/CeO2 catalyst illustrated the production rate of 248.7 mmolg-1h-1 and 11.25 mmolg-1h-1 for H2, and CO, respectively at specific energy input of 19.8 JL-1. DFT calculations exhibit apparent change in electronic structure of the CeO2 after inclusion of oxides of manganese and copper that enhance interaction with methane. Based on these findings, a plausible mechanism is elucidated which can help to design catalyst for other applications in non-thermal plasma atmosphere. & COPY; 2023 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:24328 / 24341
页数:14
相关论文
共 50 条
  • [31] Non-thermal plasma-assisted hydrogenolysis of polyethylene to light hydrocarbons
    Yao, Libo
    King, Jaelynne
    Wu, Dezhen
    Chuang, Steven S. C.
    Peng, Zhenmeng
    [J]. CATALYSIS COMMUNICATIONS, 2021, 150
  • [32] Structured Catalysts for Non-Thermal Plasma-Assisted Ammonia Synthesis
    Meloni, Eugenio
    Cafiero, Liberato
    Martino, Marco
    Palma, Vincenzo
    [J]. ENERGIES, 2023, 16 (07)
  • [33] A comparative study of non-thermal plasma assisted reforming technologies
    Petitpas, G.
    Rollier, J.-D.
    Darmon, A.
    Gonzalez-Aguilar, J.
    Metkemeijer, R.
    Fulcheri, L.
    [J]. INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2007, 32 (14) : 2848 - 2867
  • [34] Investigating the Plasma-Assisted and Thermal Catalytic Dry Methane Reforming for Syngas Production: Process Design, Simulation and Evaluation
    Delikonstantis, Evangelos
    Scapinello, Marco
    Stefanidis, Georgios D.
    [J]. ENERGIES, 2017, 10 (09):
  • [35] Non-Thermal Plasma for Process and Energy Intensification in Dry Reforming of Methane
    Abiev, Rufat Sh
    Sladkovskiy, Dmitry A.
    Semikin, Kirin, V
    Murzin, Dmitry Yu
    Rebrov, Evgeny, V
    [J]. CATALYSTS, 2020, 10 (11) : 1 - 41
  • [36] Steam Plasma Methane Reforming for Hydrogen Production
    Hrabovsky, M.
    Hlina, M.
    Kopecky, V.
    Maslani, A.
    Krenek, P.
    Serov, A.
    Hurba, O.
    [J]. PLASMA CHEMISTRY AND PLASMA PROCESSING, 2018, 38 (04) : 743 - 758
  • [37] Steam Plasma Methane Reforming for Hydrogen Production
    M. Hrabovsky
    M. Hlina
    V. Kopecky
    A. Maslani
    P. Krenek
    A. Serov
    O. Hurba
    [J]. Plasma Chemistry and Plasma Processing, 2018, 38 : 743 - 758
  • [38] Reforming of methane into Syngas in a plasma-assisted reactor.
    Czernichowski, A
    Czernichowski, M
    Czernichowski, P
    Cooley, TE
    [J]. ABSTRACTS OF PAPERS OF THE AMERICAN CHEMICAL SOCIETY, 2002, 223 : U580 - U580
  • [39] Evaluation of Non-thermal Plasma-assisted Combustion Temperature by Spectroscopic Measurement
    Tanaka, Ryo
    Imazato, Ryosuke
    Yamamoto, Tsuyoshi
    Itaya, Yoshinori
    [J]. KAGAKU KOGAKU RONBUNSHU, 2013, 39 (04) : 331 - 336
  • [40] Non-thermal plasma-assisted capture and conversion of CO2
    Li, Sirui
    Ongis, Michele
    Manzolini, Giampaolo
    Gallucci, Fausto
    [J]. Chemical Engineering Journal, 2021, 410