Plasma-Catalytic Dry Reforming of CH4 over Calcium Oxide: Catalyst Structural and Textural Modifications

被引:20
作者
Bouchoul, Nassim [1 ]
Fourre, Elodie [1 ]
Tatibouet, Jean-Michel [1 ]
Batiot-Dupeyrat, Catherine [1 ]
机构
[1] Univ Poitiers, UMR CNRS 7285, ENSIP, IC2MP, 1 Rue Marcel Dore,TSA 41105, F-86073 Poitiers 9, France
关键词
Nonthermal plasma; Methane; Carbon dioxide; Calcium oxide; DIELECTRIC-BARRIER DISCHARGE; CARBON-DIOXIDE; SYNTHESIS GAS; NONTHERMAL PLASMA; METHANE; CONVERSION; CO2; SYNGAS; ACTIVATION; REACTOR;
D O I
10.1007/s11090-019-09966-9
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The coupling of catalyst and nonthermal plasma for the dry reforming of methane was investigated with a special attention to the textural and structural catalyst modifications under plasma discharge. The reaction was performed using calcium oxide as material located into the DBD plasma reactor, while the deposited power was fixed at 8W and the total gas flow at 40mL/min (75% helium as diluent). The results obtained showed that CaO grain size affects the reactant transformation in the range: 250-1000 mu m. CH4 and CO2 conversion increases from 18.1 to 21.1% and 8.7 to 11.2% respectively from the biggest to the smallest catalyst grain. Ethane formation is favored when the biggest particles are used, corresponding to the largest gas space between grains, suggesting the preferential recombination of CH3 radicals to form C2H6 in gaseous phase and not at the surface of the solid. The reaction was performed from room temperature to 300 degrees C, little effect were observed for methane conversion while high CO2 conversion was observed during the 20min at 300 degrees C. The characterization of the catalyst after reaction under plasma shows structural catalyst modification and the carbonation of CaO at the highest temperatures. The amount of carbonate species was quantified and the results show that 59 monolayers of CaCO3 are obtained after 1h of plasma at P=8W using a mixture with a CH4/CO2 ratio of 2.
引用
收藏
页码:713 / 727
页数:15
相关论文
共 39 条
[1]   Conversion limits in the reaction of CO2 with lime [J].
Abanades, JC ;
Alvarez, D .
ENERGY & FUELS, 2003, 17 (02) :308-315
[2]  
Brook SL, 1998, J CATAL, V180, P225
[3]   Review of packed-bed plasma reactor for ozone generation and air pollution control [J].
Chen, Hsin Liang ;
Lee, How Ming ;
Chen, Shiaw Huei ;
Chang, Moo Been .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2008, 47 (07) :2122-2130
[4]   Dry Reforming of Methane with Dielectric Barrier Discharge and Ferroelectric Packed-Bed Reactors [J].
Chung, Wei-Chieh ;
Pan, Kuan-Lun ;
Lee, How-Ming ;
Chang, Moo-Been .
ENERGY & FUELS, 2014, 28 (12) :7621-7631
[5]   The Dominant Pathways for the Conversion of Methane into Oxygenates and Syngas in an Atmospheric Pressure Dielectric Barrier Discharge [J].
De Bie, Christophe ;
van Dijk, Jan ;
Bogaerts, Annemie .
JOURNAL OF PHYSICAL CHEMISTRY C, 2015, 119 (39) :22331-22350
[6]   MODELING OF DIELECTRIC BARRIER DISCHARGE CHEMISTRY [J].
ELIASSON, B ;
EGLI, W ;
KOGELSCHATZ, U .
PURE AND APPLIED CHEMISTRY, 1994, 66 (06) :1279-1286
[7]   Methane adsorption and plasma-assisted catalytic conversion on the surface of γ-alumina [J].
Gadzhieva, NN .
HIGH ENERGY CHEMISTRY, 2003, 37 (01) :38-43
[8]   Influence of the Plasma Power Supply Nature on the Plasma-Catalyst Synergism for the Carbon Dioxide Reforming of Methane [J].
Goujard, Valentin ;
Tatibouet, Jean-Michel ;
Batiot-Dupeyrat, Catherine .
IEEE TRANSACTIONS ON PLASMA SCIENCE, 2009, 37 (12) :2342-2346
[9]   Use of a non-thermal plasma for the production of synthesis gas from biogas [J].
Goujard, Valentin ;
Tatibouet, Jean-Michel ;
Batiot-Dupeyrat, Catherine .
APPLIED CATALYSIS A-GENERAL, 2009, 353 (02) :228-235
[10]   Combination of non-thermal plasma and heterogeneous catalysis for oxidation of volatile organic compounds Part 1. Accessibility of the intra-particle volume [J].
Holzer, F ;
Roland, U ;
Kopinke, FD .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2002, 38 (03) :163-181