How to make sustainable CO2 conversion to Methanol: Thermocatalytic versus electrocatalytic technology

被引:67
作者
Guzman, Hilmar [1 ,2 ]
Salomone, Fabio [1 ]
Batuecas, Esperanza [3 ]
Tommasi, Tonia [1 ]
Russo, Nunzio [1 ]
Bensaid, Samir [1 ]
Hernandez, Simelys [1 ,2 ]
机构
[1] Politecn Torino, CREST Grp, Dept Appl Sci & Technol DISAT, Cso Duca Abruzzi 24, I-10129 Turin, Italy
[2] IIT Ist Italian Tecnol, Via Livorno 60, I-10144 Turin, Italy
[3] Carlos III Univ Madrid, Thermal & Fluid Engn Dept, Av Univ 30, Madrid 28911, Spain
关键词
Life Cycle Assessment (LCA); CO2; hydrogenation; Electroreduction; Methanol; Ternary oxides; Synthetic fuels; Power-to-Fuels; LIFE-CYCLE ASSESSMENT; HIGH-TEMPERATURE ELECTROLYSIS; CUMULATIVE ENERGY DEMAND; SYNTHETIC NATURAL-GAS; CARBON-DIOXIDE; ELECTROCHEMICAL REDUCTION; WATER ELECTROLYSIS; CEMENT PLANT; CAPTURED CO2; CATALYST;
D O I
10.1016/j.cej.2020.127973
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Electrocatalytic (EC) and thermocatalytic (TC) conversion of CO2 to methanol are promising carbon capture and utilization technologies. Herein, these CO2-to-methanol conversion processes are analysed in terms of technical, environmental and economic feasibility. To this purpose, the catalytic performance of the same catalyst (CuO/ZnO/Al2O3) was evaluated in both EC and TC processes. Here is showed for the first time that this catalyst is (apart from TC route) also able to generate methanol through CO2 EC reduction. This work presents lab scale tests, scaled-up simulations and evaluates the environmental and economic performance of these processes. The carbon footprint of the TC and EC processes, scaled-up to the same productivity of similar to 3 kg/h methanol, scored similar to 8 kg(CO2) eq/kg(CH3OH). Strategies to reduce this impact are presented, such as improving the current density of the EC cell (i.e. 200 mA/cm(2) results in a reduction of 68% to 2.72 kg(CO2) eq/kg(CH3OH)) and the availability of 100% renewable electricity (saving up to 62% carbon footprint of both processes). Considering an effective allocation of the methanol productivity on a real market scenario, both the TC and EC processes would start to be economically competitive at methanol productivities > 19.1 kg/h and 3.3 kg/h, respectively. Moreover, if O-2 valorisation, a low price of the renewable electricity and a carbon tax are considered, the economic profitability will rise; e.g. the minimum levelised cost of product (LCOP of 1.45 (sic)/kg and 1.67 (sic)/kg, respectively) could be reduced by 53%. Finally, our results pointed out that the CO2 electroreduction process must be optimized (e.g. improving catalysts performance and EC cell design reducing mass transfer limitations) to achieve industrially relevant rates and the maturity of the thermocatalytic technology.
引用
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页数:15
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