Hydrogen Production from Methane Cracking in Dielectric Barrier Discharge Catalytic Plasma Reactor Using a Nanocatalyst

被引:22
|
作者
Khoja, Asif Hussain [1 ]
Azad, Abul Kalam [2 ]
Saleem, Faisal [3 ]
Khan, Bilal Alam [4 ]
Naqvi, Salman Raza [5 ]
Mehran, Muhammad Taqi [5 ]
Amin, Nor Aishah Saidina [6 ]
机构
[1] Natl Univ Sci & Technol NUST, US Pakistan Ctr Adv Studies Energy USPCAS E, Dept Thermal Energy Engn, Fossil Fuels Lab, Sect H-12, Islamabad 44000, Pakistan
[2] Cent Queensland Univ, Sch Engn & Technol, 120 Spencer St, Melbourne, Vic 3000, Australia
[3] Univ Engn & Technol, Dept Chem & Polymer Engn, Faisalabad Campus, Lahore 38000, Pakistan
[4] Politecn Torino, Dept Appl Sci & Technol, Corso Duca Abruzzi 24, I-10129 Turin, Italy
[5] Natl Univ Sci & Technol NUST, Sch Chem & Mat Engn, Sect H-12, Islamabad 44000, Pakistan
[6] Univ Technol Malaysia UTM, Chem React Engn Grp, Sch Chem & Energy Engn, Fac Engn, Johor Baharu 81310, Malaysia
关键词
hydrogen production; methane cracking; DBD plasma reactor; MgAl2O4; CNTs; NANOSECOND PULSED PLASMA; COX FREE HYDROGEN; NONTHERMAL PLASMA; CARBON NANOTUBES; MGAL2O4; SPINEL; DRY; DECOMPOSITION; GAS; NI/MGAL2O4; CONVERSION;
D O I
10.3390/en13225921
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
The study experimentally investigated a novel approach for producing hydrogen from methane cracking in dielectric barrier discharge catalytic plasma reactor using a nanocatalyst. Plasma-catalytic methane (CH4) cracking was undertaken in a dielectric barrier discharge (DBD) catalytic plasma reactor using Ni/MgAl2O4. The Ni/MgAl2O4 was synthesised through co-precipitation followed customised hydrothermal method. The physicochemical properties of the catalyst were examined using X-ray diffraction (XRD), scanning electron microscopy-energy dispersive X-ray spectrometry (SEM-EDX) and thermogravimetric analysis (TGA). The Ni/MgAl2O4 shows a porous structure spinel MgAl2O4 and thermal stability. In the catalytic-plasma methane cracking, the Ni/MgAl2O4 shows 80% of the maximum conversion of CH4 with H-2 selectivity 75%. Furthermore, the stability of the catalyst was encouraging 16 h with CH4 conversion above 75%, and the selectivity of H-2 was above 70%. This is attributed to the synergistic effect of the catalyst and plasma. The plasma-catalytic CH4 cracking is a promising technology for the simultaneous H-2 and carbon nanotubes (CNTs) production for energy storage applications.
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页数:15
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