Feasibility assessment of small-scale methanol production via power-to-X

被引:16
作者
Moioli, Emanuele [1 ]
Wotzel, Anne
Schildhauer, Tilman [1 ]
机构
[1] Paul Scherrer Inst, Energy & Environm Div, Forschungstr 111, Villigen, Switzerland
关键词
Power-to-methanol; Methanol synthesis; Techno-economic analysis; Renewable energy; Small-scale energy storage; DIRECT CATALYTIC METHANATION; CARBON-DIOXIDE; CO2; BIOGAS; GASIFICATION; OPTIMIZATION; PERSPECTIVES; CONVERSION; HYDROGEN; STORAGE;
D O I
10.1016/j.jclepro.2022.132071
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Decentralized methanol production in the context of energy storage (also called power-to-methanol or PtMeOH) requires the development of new process configurations. This is due to the need to avoid energy-intensive compression stages and to adapt to intermittent H2 availability. This study aimed at the determination of the techno-economic feasibility of new small-scale PtMeOH process configurations. It was proposed that, in small scale, the pressure should be limited to 30 bar, the standard H2 delivery pressure of an electrolyzer. This is due to the cost and complexity of a H2 compressor, unsuitable for small-scale systems. As CO2 conversion is limited under these conditions, several configurations differing in the valorization strategy of the unreacted stream were assessed. Additionally, the possible coupling with other processes (e.g., biogas upgrading) was considered. It was found that it was not possible to obtain a profit in the production of methanol from renewable H2 in any configuration at high electricity prices due to the important impact of H2 cost. The highest electricity price allowing profitable operation was 0.07 USD/kWh for the recycling process. If PtMeOH is coupled with biogas upgrading, the process can also be operated in the cascade configuration with a similar economic performance. Hence, the small-scale PtMeOH process is feasible only under very specific conditions: constant low electricity price or coupled with waste-handling facilities. This study determined the set of parameters with which the PtMeOH process can be economically profitable, highlighting under which conditions cleaner methanol production can be envisaged in the near future.
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页数:17
相关论文
共 36 条
  • [21] Analysis of CO2 utilization for methanol synthesis integrated with enhanced gas recovery
    Minh Tri Luu
    Milani, Dia
    Abbas, Ali
    [J]. JOURNAL OF CLEANER PRODUCTION, 2016, 112 : 3540 - 3554
  • [22] Synthesis of grid compliant substitute natural gas from a representative biogas mixture in a hybrid Ni/Ru catalysed reactor
    Moioli E.
    Mutschler R.
    Borsay A.
    Calizzi M.
    Züttel A.
    [J]. Chemical Engineering Science: X, 2020, 8
  • [23] Renewable energy storage via CO2 and H2 conversion to methane and methanol: Assessment for small scale applications
    Moioli, Emanuele
    Mutschler, Robin
    Zuettel, Andreas
    [J]. RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2019, 107 : 497 - 506
  • [24] Methanol synthesis using captured CO2 as raw material: Techno-economic and environmental assessment
    Perez-Fortes, Mar
    Schoeneberger, Jan C.
    Boulamanti, Aikaterini
    Tzimas, Evangelos
    [J]. APPLIED ENERGY, 2016, 161 : 718 - 732
  • [25] Assessment of Methanol Synthesis Utilizing Exhaust CO2 for Chemical Storage of Electrical Energy
    Rihko-Struckmann, Liisa K.
    Peschel, Andreas
    Hanke-Rauschenbach, Richard
    Sundmacher, Kai
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2010, 49 (21) : 11073 - 11078
  • [26] Feasibility study of methanol production from different renewable sources and thermo-economic analysis
    Rivarolo, M.
    Bellotti, D.
    Magistri, L.
    Massardo, A. F.
    [J]. INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2016, 41 (04) : 2105 - 2116
  • [27] Investigation of power-to-methanol processes coupling electrolytic hydrogen production and catalytic CO2 reduction
    Rivera-Tinoco, R.
    Farran, M.
    Bouallou, C.
    Aupretre, F.
    Valentin, S.
    Millet, P.
    Ngameni, J. R.
    [J]. INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2016, 41 (08) : 4546 - 4559
  • [28] Critical assessment of steady-state kinetic models for the synthesis of methanol over an industrial Cu/ZnO/Al2O3 catalyst
    Slotboom, Y.
    Bos, M. J.
    Pieper, J.
    Vrieswijk, V.
    Likozar, B.
    Kersten, S. R. A.
    Brilman, D. W. F.
    [J]. CHEMICAL ENGINEERING JOURNAL, 2020, 389 (389)
  • [29] Tsotsas E., 2018, WARMELEITUNG DISPERS, P1, DOI [10.1007/978-3-662-52991-1_102-1, DOI 10.1007/978-3-662-52991-1_102-1]
  • [30] ULRICH G.D., 2004, CHEM ENG PROCESS DES