Biomass power plant integrated with a thermochemical heat storage system using a fluidized bed reactor worked by variable renewable energy: Dynamic simulation, energetic and economic analyses

被引:11
作者
Uchino, Takayuki [1 ]
Yasui, Takahito [1 ]
Fushimi, Chihiro [1 ]
机构
[1] Tokyo Univ Agr & Technol, Dept Chem Engn, 2-24-16 Naka Cho, Koganei, Tokyo 1848588, Japan
关键词
Biomass power plant; Carnot battery; Thermochemical heat storage; Fluidized bed; Process evaluation; Dynamic simulation; DEHYDRATION PROCESS; CALCIUM HYDROXIDE; LAB SCALE; CAO/CA(OH)(2); GENERATION; CA(OH)(2); ENHANCEMENT; REHYDRATION; PERFORMANCE; PRESSURES;
D O I
10.1016/j.est.2023.106720
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
This study focused on a biomass power plant (Organic Rankine Cycle: ORC, 1 MWe) integrated with a ther-mochemical heat storage (TCS) system as a Carnot battery. In the TCS, a fluidized bed reactor using CaO/Ca (OH)2/alumina particles was used, and steam was used as a fluidizing and reacting gas. The surplus electricity from variable renewable energy (VRE) is converted to heat and stored during daytime, and the stored energy is utilized to generate power in the evening. In this study, there were three objectives. First, process performances were compared when R245fa or R1233zd was used as a working fluid of ORC, and influences of ORC parameters such as the turbine inlet temperature, superheat temperature, and the scale of the power generation, were evaluated. In addition, effects of the fluidized bed volume and the reduction of biomass fuel combustion were also investigated. Second, a potential of the proposed process that can absorb the VRE fluctuation was evaluated by the dynamic calculation. Third, the economics of the TCS system was evaluated. Results show that the round-trip efficiency of the process using R1233zd was 8.77 %, which was slightly lower than that of the process using R245fa (8.84 %). The increases of a turbine inlet temperature led to the increase of heat recovery from the outlet steam of the TCS reactor, meanwhile, the round-trip efficiency decreased. The efficiencies of the cases changing the superheat temperature (5 -> 15 degrees C) were slightly changed (<0.5 %). To achieve high energy efficiencies, a large-scale biomass power plant and a small-fluidized bed volume was effective. It was found that the VRE fluctuation was mostly absorbed by the TCS with a fluidized bed and ORC process. In the economic evaluations, the levelized cost of storage regarding only the TCS system was 0.92-2.37 USD/kWhe when the charging elec-tricity cost is 0.05 USD/kWhe. LCOS also decreases to 0.50-1.14 USD/kWhe if the electricity cost is free during daytime in the future and power output is two times in a day.
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页数:14
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共 61 条
  • [1] Final conversion and reaction rate of CaO hydration in different experimental systems
    Abliz, S
    Ogura, H
    Kage, H
    [J]. KAGAKU KOGAKU RONBUNSHU, 2005, 31 (04) : 253 - 258
  • [2] Kinetic study of CaO/Ca(OH)2 reversible chemical reaction in vacuumed forced convection for thermal energy storage
    Abliz, S
    Ogura, H
    Kage, H
    Matsuno, Y
    [J]. KAGAKU KOGAKU RONBUNSHU, 2002, 28 (03) : 345 - 349
  • [3] Semipermeable encapsulation of calcium hydroxide for thermochemical heat storage solutions
    Afflerbach, S.
    Kappes, M.
    Gipperich, A.
    Trettin, R.
    Krumm, W.
    [J]. SOLAR ENERGY, 2017, 148 : 1 - 11
  • [4] Design of a MW-scale thermo-chemical energy storage reactor
    Angerer, Michael
    Becker, Moritz
    Haerzschel, Stefan
    Kroeper, Konstantin
    Gleis, Stephan
    Vandersickel, Annelies
    Spliethoff, Hartmut
    [J]. ENERGY REPORTS, 2018, 4 : 507 - 519
  • [5] [Anonymous], 2021, BP STASTICAL REV WOR
  • [6] Techno-economic assessment of solid-gas thermochemical energy storage systems for solar thermal power applications
    Bayon, Alicia
    Bader, Roman
    Jafarian, Mehdi
    Fedunik-Hofman, Larissa
    Sun, Yanping
    Hinkley, Jim
    Miller, Sarah
    Lipinski, Wojciech
    [J]. ENERGY, 2018, 149 : 473 - 484
  • [7] Carnot batteries, EN CONS EN STOR
  • [8] Cost Indices, TOW SKI
  • [9] Experimental investigation and model validation of a CaO/Ca(OH)2 fluidized bed reactor for thermochemical energy storage applications
    Criado, Yolanda A.
    Huille, Arthur
    Rouge, Sylvie
    Carlos Abanades, J.
    [J]. CHEMICAL ENGINEERING JOURNAL, 2017, 313 : 1194 - 1205
  • [10] Enhancement of a CaO/Ca(OH)2 based material for thermochemical energy storage
    Criado, Yolanda A.
    Alonso, Monica
    Carlos Abanades, J.
    [J]. SOLAR ENERGY, 2016, 135 : 800 - 809