Evaluation of CO2 sources for Power-to-Liquid plants producing Fischer-Tropsch products

被引:15
作者
Pratschner, Simon [1 ]
Hammerschmid, Martin [1 ]
Mueller, Stefan [1 ]
Winter, Franz [1 ]
机构
[1] Tech Univ Wien, Inst Chem Environm & Biosci Engn, Fac Tech Chem, Getreidemarkt 9-166, A-1060 Vienna, Austria
关键词
Power-to-Liquid; Carbon capture and utilization; Solid-oxide electrolysis; Fischer-Tropsch synthesis; Process simulation; CO2; sources; SOLID OXIDE ELECTROLYZER; WASTE HEAT-RECOVERY; CEMENT INDUSTRY; CAPTURE; TECHNOLOGIES; PERFORMANCE; NI/YSZ; WATER; MODEL; GAS;
D O I
10.1016/j.jcou.2023.102508
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
In addition to the climate crisis's looming dangers, Europe was recently affected by profoundly volatile energy markets, entailing soaring inflation and political uncertainty. Power-to-Liquid processes have the potential to curb global warming by valorizing CO2 to produce synthetic fuels and platform chemicals while simultaneously substituting fossil energy imports. The impact of the CO2 source, i.e., cement production, biogas upgrading and solid biomass combustion, on Power-to-Liquid plants was evaluated by implementing the designed configuration, including CO2 capture, solid-oxide electrolyzer, Fischer-Tropsch synthesis and steam reforming, in IPSEpro, a stationary equation-based process simulation tool. Maximum Power-to-Liquid efficiency of 63.8% and maximum carbon efficiency of 88.6% were obtained by exploiting CO2 emitted by a biogas upgrading unit. Solid-oxide electrolyzers ranging from 23 MWel. (biogas) to 504 MWel. (cement) are required to process CO2 streams from 4.5 to 100 t/h. In addition, the mass and energy balances of the three considered configurations were determined and embedded in a process flow diagram. The presented study aims to facilitate future decisions concerning carbon capture and utilization policy by assessing the CO2 source's influence on Power-to-Liquid plants' key performance indicators. Furthermore, the underlying work supports a sustainable realization of Power-to-Liquid plants by offering a framework for exploiting CO2 sources.
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页数:14
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共 77 条
  • [1] Chemical equilibrium analysis of hydrogen production from shale gas using sorption enhanced chemical looping steam reforming
    Adiya, Zainab Ibrahim S. G.
    Dupont, Valerie
    Mahmud, Tariq
    [J]. FUEL PROCESSING TECHNOLOGY, 2017, 159 : 128 - 144
  • [2] 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
  • [3] [Anonymous], 2022, Trends in Atmospheric Carbon Dioxide
  • [4] [Anonymous], 2022, Cement
  • [5] [Anonymous], 2018, Handelsblatt
  • [6] Production of Fischer-Tropsch liquid fuels from high temperature solid oxide co-electrolysis units
    Becker, W. L.
    Braun, R. J.
    Penev, M.
    Melaina, M.
    [J]. ENERGY, 2012, 47 (01) : 99 - 115
  • [7] Estimating the waste heat recovery in the European Union Industry
    Bianchi, Giuseppe
    Panayiotou, Gregoris P.
    Aresti, Lazaros
    Kalogirou, Soteris A.
    Florides, Georgios A.
    Tsamos, Kostantinos
    Tassou, Savvas A.
    Christodoulides, Paul
    [J]. ENERGY ECOLOGY AND ENVIRONMENT, 2019, 4 (05) : 211 - 221
  • [8] CO2 Capture in the Cement Industry, Norcem CO2 Capture Project (Norway)
    Bjerge, Liv-Margrethe
    Brevik, Per
    [J]. 12TH INTERNATIONAL CONFERENCE ON GREENHOUSE GAS CONTROL TECHNOLOGIES, GHGT-12, 2014, 63 : 6455 - 6463
  • [9] CO2 Capture Technologies for Cement Industry
    Bosoaga, Adina
    Masek, Ondrej
    Oakey, John E.
    [J]. GREENHOUSE GAS CONTROL TECHNOLOGIES 9, 2009, 1 (01): : 133 - 140
  • [10] Brevik C.C.S, 2022, BREVIK CCS WORLDS 1