Comparative techno-economic and life-cycle assessment of power-to-methanol synthesis pathways

被引:132
作者
Adnan, Muflih A. [1 ,2 ]
Kibria, Md Golam [1 ]
机构
[1] Univ Calgary, Dept Chem & Petr Engn, 2500 Univ Dr NW, Calgary, AB T2N 1N4, Canada
[2] Islamic Univ Indonesia, Dept Chem Engn, Sleman 55584, Daerah Istimewa, Indonesia
关键词
MeOH production; Economic analysis; CO2; reduction; Greenhouse emission; Electrochemical reaction; WATER-GAS SHIFT; HYDROGEN-PRODUCTION; CAPTURED CO2; ELECTROLYSIS; STORAGE; ENERGY; FUELS; LIMITATIONS; DESIGN; SYSTEM;
D O I
10.1016/j.apenergy.2020.115614
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 deployment of "Power-to-Methanol" technologies by exploiting electrochemical reactions with CO2 as feedstock has received traction lately; primarily due to the continuous drop in renewable electricity price. Here, we compare techno-economic and climate benefits of three emerging "Power-to-Methanol" routes, including one-step CO2-to-methanol electrolysis; two-step synthesis, involving H2O electrolysis; and three-step synthesis, involving H2O electrolysis, and CO2-to-CO electrolysis. This study identifies key economic drivers and sets the technological goals for "Power-to-Methanol" routes to be competitive. We report that under current techno-economic conditions, none of these three emerging routes are compelling with levelized cost $860-$1585/ton methanol, which is similar to 2-4 times higher than the current market price ($300/ton-$500/ton). However, under future conditions (notably electricity price <3 cents/kWh), all three electrochemical routes become compelling with the levelized cost between $430-$435/ton methanol. Cradle-to-gate life-cycle-analysis reveals that electricity emission factor below <130 g CO2/kWh is required for "Power-to-Methanol" pathways to provide climate benefits over conventional route. When electricity is sourced fully from wind and nuclear power, all three routes would provide net negative emission potential of 170-195 thousand ton CO2/year. While economically all three routes seem to be equally competitive under optimistic scenario, at present only two-step synthesis is technically feasible at scale. Consequently, we establish performance targets for CO2 electrolysis under future conditions (electricity price of 3 cents/ kWh), including a current density (>130 mA/cm(2) (CO2-to-CH3OH), >360 mA/cm(2) (CO2-to-CO)), and energy efficiency >40%, which would make one- and three-step "Power-to-Methanol" routes economically and environmentally competitive over fossil-based process in future.
引用
收藏
页数:23
相关论文
共 85 条
  • [1] Agency IE, 2009, IEA CCS ROADMAP CONT
  • [2] Towards the electrochemical conversion of carbon dioxide into methanol
    Albo, J.
    Alvarez-Guerra, M.
    Castano, P.
    Irabien, A.
    [J]. GREEN CHEMISTRY, 2015, 17 (04) : 2304 - 2324
  • [3] Modeling a novel combined solid oxide electrolysis cell (SOEC) - Biomass gasification renewable methanol production system
    Ali, Shahid
    Sorensen, Kim
    Nielsen, Mads P.
    [J]. RENEWABLE ENERGY, 2020, 154 (154) : 1025 - 1034
  • [4] [Anonymous], 2017, METH PRIC SKYR 180 L
  • [5] [Anonymous], 2017, RENEWABLE POWER GENE
  • [6] [Anonymous], 2011, AM CLIMATE CHOICES
  • [7] [Anonymous], 2020, ANN EN OUTL 2020 PRO
  • [8] [Anonymous], 2019, NEW METH PLANTS EXP
  • [9] [Anonymous], 2020, METH POSTS REG CONTR
  • [10] [Anonymous], 2016, CARB DIOX EM COEFF