Thermochemical transformation of CO2 for CH4 production using metal hydride and carbonates as portable sources

被引:2
作者
Grasso, Maria Laura [1 ]
Azcona, Sara Rozas [2 ,3 ]
Larochette, Pierre Arneodo [1 ,4 ]
Aparicio, Santiago [2 ,3 ]
Gennari, Fabiana [1 ,4 ,5 ]
机构
[1] Consejo Nacl Invest Cient & Tecn CONICET, Ctr Atom Bariloche CNEA, Ave Bustillo 9500,R8402AGP, San Carlos De Bariloche, Rio Negro, Argentina
[2] Univ Burgos, Dept Chem, Burgos 09001, Spain
[3] Univ Burgos, Int Res Ctr Crit Raw Mat Adv Ind Technol ICCRAM, Burgos 09001, Spain
[4] Univ Nacl Cuyo, Inst Balseiro, Ctr Atom Bariloche CNEA, Ave Bustillo 9500,R8402AGP, San Carlos De Bariloche, Rio Negro, Argentina
[5] Ave Bustillo 9500,R8402AGP, San Carlos De Bariloche, Rio Negro, Argentina
关键词
Hydrides; Carbonates; Methane; CCU; CO2; conversion; HYDROGEN-PRODUCTION; ADSORPTION; DIOXIDE; POWER; NI; SORPTION; METHANE; SYSTEMS; OXIDE; IR;
D O I
10.1016/j.ijhydene.2023.03.032
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
The thermochemical reaction between MgH2 and Li2CO3 is investigated for the first time for the CO2 transformation into fuels with and without nickel as a catalyst. Successful production of CH4 with high yields is reached depending on different reaction conditions such as microstructural refining, MgH2:Li2CO3 molar ratio, temperature and time. In absence of a catalyst, a methane yield of 68.2% was achieved by heating the milled MgH2:Li2CO3 mixture at 450 & DEG;C for 5 h. The global mechanism involves the reduction of CO2 from Li2CO3 by MgH2/ Mg, producing CH4 and Li2O/MgO. For the Ni-catalyzed system, the highest methane yield of >90% was reached at 400 & DEG;C after 5 h of thermal treatment. The global process responds to a Sabatier reaction, with a contribution of a direct reduction of CO2 depending on the starting mol ratio. The results demonstrate that thermochemical activation of the Nicatalyzed MgH2:Li2CO3 mixture is a powerful process for the generation of CH4 and CO2 utilization.& COPY; 2023 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:21835 / 21849
页数:15
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