Solar-Aided Calcination of Limestone: First Modeling of the SOLCEMENT Process

被引:2
作者
Nikolakopoulos, Athanassios [1 ,2 ]
Steriotis, Theodore [1 ]
Charalambopoulou, Georgia [1 ]
Karagiannakis, George [3 ]
Dimitrakis, Dimitrios [3 ]
Konstandopoulos, Athanasios G. [3 ,4 ]
Michalis, Vasileios [5 ]
Katsiotis, Marios [5 ]
机构
[1] Natl Ctr Sci Res Demokritos, Athens 15341, Greece
[2] Natl Tech Univ Athens, Athens 15780, Greece
[3] Ctr Res Technol Hellas, Chem Proc Energy Resources, Thessaloniki 57001, Greece
[4] Aristotle Univ Thessaloniki, Univ Campus, Thessaloniki 54124, Greece
[5] TITAN Cement Grp, Kamari Plant, Elefsina 19200, Greece
来源
SOLARPACES 2020 - 26TH INTERNATIONAL CONFERENCE ON CONCENTRATING SOLAR POWER AND CHEMICAL ENERGY SYSTEMS | 2022年 / 2445卷
关键词
ENERGY; DESIGN;
D O I
10.1063/5.0085791
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
Cement production is one of the most energy intensive industrial processes, accounting for approximately 5% of the total CO2 emissions worldwide; about 2/3 of such emissions are due to limestone calcination. The SOLCEMENT process pertains to the use of concentrated solar radiation for limestone calcination in cement plants. The process employs also a thennochemical storage reactor (TSR) integrated into the conventional solids preheating system, to partially compensate for the intermittent nature of sunlight, by enabling the transfer of stored solar energy to night operation thereby reducing the use of fossil fuels. In addition to fossil fuels replacement during daytime, the partial solarization of limestone calcination has the potential of CO2 recovery produced by the chemical reaction in pure form. A first detailed Ilowsheet of the integrated process is presented and reveals the possibility to transfer daily 28-52 MWh of solar energy between day and night operations for a 2.4 kt/day limestone calcination capacity cement plant. The study adopts a Process Systems Engineering approach which involves process modeling and optimization of design and operating parameters, towards maximization of solids' temperature (up to 850 degrees C) after preheating, as well as optimal loading and use of the TSR (up to 6 MW). Four operating scenarios were considered, and show that the process perfonnance scales with the temperature of the calciner flue gases, saving 52 IVIA,Vh for 1000 degrees C, which accounts for 6% of the total required energy during non-solar operation (-856 MWh).
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页数:8
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