Experimental analysis on calcination and carbonation process in calcium looping for CO2 capture: study case of cement plants in Indonesia

被引:3
|
作者
Febriatna, Triya Setia [1 ]
Darmanto, Prihadi Setyo [2 ]
Juangsa, Firman Bagja [2 ,3 ]
机构
[1] Inst Teknol Bandung, Fac Mech & Aerosp Engn, Master Program Mech Engn, Bandung, Indonesia
[2] Inst Teknol Bandung, Fac Mech & Aerosp Engn, Bandung, Indonesia
[3] Inst Teknol Bandung, Res Ctr New & Renewable Energy, Bandung, Indonesia
来源
CLEAN ENERGY | 2023年 / 7卷 / 02期
关键词
CO2; emissions; cement industry; carbon capture; calcium looping; calcination; carbonation; LIMESTONE CALCINATION; HYDRATION; DECOMPOSITION; REACTIVATION; EMISSIONS; SORBENT; STORAGE; SYSTEM; STEAM;
D O I
10.1093/ce/zkac072
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
This work experimentally investigates calcium looping using limestone obtained directly from several cement factories in Indonesia to observe the carbon-absorption characteristics of limestone from different mining locations. The promising performance of raw limestones allows the possibility of CO2 emission reduction in the sustainable cement-production process. Carbon dioxide (CO2) is the main contributor to greenhouse gases that affect global warming. The industrial sector is the third largest producer of CO2 and the cement industry is one of the industries that consistently produces the most significant CO2 emissions. The cement industry produces 5-8% of global CO2 emissions. Several methods for reducing specific CO2 emissions have been reported in the cement industry, including calcium looping, which uses the reversible reaction between calcination [calcium carbonate (CaCO3) decomposition] and carbonation [CO2 capture by calcium oxide (CaO)]. This work investigates calcium looping employing limestone obtained directly from several cement factories in Indonesia to observe the carbon-absorption characteristics of limestone from different mining locations. The experiment was carried out using a tube furnace equipped with a controlled atmospheric condition that functions as a calciner and a carbonator. X-ray diffraction and scanning electron microscopy with energy-dispersive x-ray spectroscopy characterization were conducted to analyse the changes in the experimental samples. The results demonstrated that the reactor configuration was capable of performing the calcination process, which converted CaCO3 to calcium hydroxide [Ca(OH)(2)], as well as the carbonation process, which captured carbon and converted it back to CaCO3. Parametric analysis was performed on both reactions, including pressure, temperature, duration, particle size and reaction atmosphere. The results show that the limestone obtained from all sites can be used as the sorbents for the calcium-looping process with an average reactivity of 59.01%. Limestone from cement plants in various parts of Indonesia has the potential to be used as carbon sorbents in calcium-looping technology. With a similar CO2 concentration as the flue gas of 16.67%, the experimental results show that Bayah limestone has the maximum reactivity, as shown by the highest carbon-content addition of 12.15 wt% and has the highest CO2-capture capability up to >75% per mole of Ca(OH)(2) as a sorbent. Similar levels of the ability to capture CO2 per mole of Ca(OH)(2) can be found in other limestones, ranging from 14.85% to 34.07%. The results show a promising performance of raw limestones from different mining sites, allowing further study and observation of the possibility of CO2 emission reduction in the sustainable cement-production process.
引用
收藏
页码:313 / 327
页数:15
相关论文
共 50 条
  • [21] Hydrodynamical model and experimental results of a calcium looping cycle for CO2 capture
    Lisbona, Pilar
    Martinez, Ana
    Romeo, Luis M.
    APPLIED ENERGY, 2013, 101 : 317 - 322
  • [22] Investigation of the performance of strontium oxide in carbonation-calcination looping for CO2 capture by the process simulation
    Ani, A. Bakhshi
    Ebrahim, H. Ale
    INTERNATIONAL JOURNAL OF ENVIRONMENTAL SCIENCE AND TECHNOLOGY, 2025, 22 (06) : 4881 - 4890
  • [23] Oxyfuel carbonation/calcination cycle for low Cost CO2 capture in existing power plants
    Romeo, Luis M.
    Abanades, J. Carlos
    Escosa, Jesus M.
    Pano, Jara
    Gimenez, Antonio
    Sanchez-Biezma, Andres
    Ballesteros, Juan C.
    ENERGY CONVERSION AND MANAGEMENT, 2008, 49 (10) : 2809 - 2814
  • [24] Simulation of a calcium looping CO2 capture process for pressurized fluidized bed combustion
    Duhoux, Benoit
    Symonds, Robert T.
    Hughes, Robin
    Mehrani, Poupak
    Anthony, Edward J.
    Macchi, Arturo
    CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 2020, 98 (01) : 75 - 83
  • [25] Calcium looping sorbents for CO2 capture
    Erans, Maria
    Manovic, Vasilije
    Anthony, Edward J.
    APPLIED ENERGY, 2016, 180 : 722 - 742
  • [26] The role of water vapour on CO2 mobility on calcite surface during carbonation process for calcium looping: A DFT study
    Zha, Jianrui
    Yan, Yongliang
    Ma, Peiyong
    Huang, Yaji
    Qi, Fenglei
    Liu, Xiaohao
    Diao, Rui
    Yan, Dongxu
    CARBON CAPTURE SCIENCE & TECHNOLOGY, 2024, 12
  • [27] Progress in reducing calcination reaction temperature of Calcium-Looping CO2 capture technology: A critical review
    Han, Rui
    Wang, Yang
    Xing, Shuang
    Pang, Caihong
    Hao, Yang
    Song, Chunfeng
    Liu, Qingling
    CHEMICAL ENGINEERING JOURNAL, 2022, 450
  • [28] Solar-driven calcium looping system for carbon capture in cement plants: Process modelling and energy analysis
    Ferrario, Daniele
    Stendardo, Stefano
    Verda, Vittorio
    Lanzini, Andrea
    JOURNAL OF CLEANER PRODUCTION, 2023, 394
  • [29] Kinetic Study of Belite Formation in Cement Raw Meals Used in the Calcium Looping CO2 Capture Process
    Alonso, Monica
    Ranuin Fernandez, Jose
    Carlos Abanades, Juan
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2019, 58 (14) : 5445 - 5454
  • [30] Calcium Looping for CO2 Capture at a Constant High Temperature
    Yin, Junjun
    Qin, Changlei
    Feng, Bo
    Ge, Lei
    Luo, Cong
    Liu, Wenqiang
    An, Hui
    ENERGY & FUELS, 2014, 28 (01) : 307 - 318