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Journal articles on the topic 'Carbonation and Calcination'

Author: Grafiati

Published: 4 June 2021

Last updated: 11 February 2022

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1

Chou, Yiang-Chen, Jui-Yen Cheng, Wan-Hsia Liu, and Heng-Wen Hsu. "Effects of Steam Addition during Calcination on Carbonation Behavior in a Calcination/Carbonation Loop." Chemical Engineering & Technology 41, no. 10 (2018): 1921–27. http://dx.doi.org/10.1002/ceat.201800133.

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2

Li, Ying Jie, Xin Xie, Chang Tian Liu, and Sheng Li Niu. "Cyclic Carbonation Properties of CMA as CO₂ Sorbent at High Temperatures." Advanced Materials Research 518-523 (May 2012): 655–58. http://dx.doi.org/10.4028/www.scientific.net/amr.518-523.655.

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Calcium-based minerals cyclic calcination/carbonation reaction is an effective approach to CO2 capture for coal-fired power plants. It was proposed that dolomite modified with acetic acid solution, i.e. calcium magnesium acetate (CMA), acted as a new CO2 sorbent for calcination/carbonation cycles. The carbonation conversions for CMA and dolomite with the number of cycles were experimentally investigated. The cyclic conversion for CMA is much greater than that for dolomite for the carbonation at 650-700 °C. The carbonation conversion for CMA achieves as high as 0.6 after 20 cycles. CMA maintain

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3

Tomaszewicz, Grzegorz, Michalina Kotyczka-Morańska, and Agnieszka Plis. "Studies on the carbonation of Czatkowice limestone in Calcium Looping process." Polish Journal of Chemical Technology 18, no. 2 (2016): 53–58. http://dx.doi.org/10.1515/pjct-2016-0029.

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Abstract The growing demand for the reduction of anthropogenic CO2 emissions has stimulated the development of CO2 capture methods. One of the best capture methods comprises the calcium looping process, which incorporates calcium-based sorbents during the calcination and carbonation cycles. Czatkowice limestone may be considered to be a prospective chemical sorbent for the calcium looping process because of its formation characteristics. This paper addresses the thermogravimetric studies conducted under varying conditions of temperature and various concentrations of CO2 during the carbonation

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4

Wei, Ri Guang, Jian Mei, Jian Qiang Gao, Hong Wei Chen, and Chun Bo Wang. "The Study on the Effect of Water Vapor for the Decarbonization Capacity of CaO." Advanced Materials Research 610-613 (December 2012): 2149–52. http://dx.doi.org/10.4028/www.scientific.net/amr.610-613.2149.

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In order to find the trends of carbonation conversion rate X when the carbonated atmosphere contains water vapor, experiments were carried out by the homemade calcination/carbonation fixed-bed reactor, in which water vapor could be added in the reaction atmosphere. By experiments in different conditions, the results have showed that: with the increase of the water vapor content X was improved significantly, and the exaltation was also reflected in the cycles; when the carbonation temperature was low water vapor on the absorbent performance will show a greater improvement; calcination temperatu

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5

Chen, Hong Wei, Ri Guang Wei, Jian Mei, Jian Qiang Gao, and Chun Bo Wang. "Experimental Study on Factors for the Capability of Ca-Based Absorbent for CO₂-Capture." Advanced Materials Research 356-360 (October 2011): 1546–50. http://dx.doi.org/10.4028/www.scientific.net/amr.356-360.1546.

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In order to find the factors and their effects for the Ca-based absorbent for CO2-capture, the experimental method was used to research the limestone in the calcination/carbonation fixed bed process. Then measured the specific surface and specific pore volume respectively by the method of COULTER_SA_3100 nitrogen absorption specific surface and the method of BET and BJH through pore size analyzer. The result has showed that the microstructure of absorber and conversion ratio of carbonation X was affected by the operating parameters including calcination temperature (Tcal), CO2 concentration in

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6

Wang, Chunbo, Xing Zhou, Lufei Jia, and Yewen Tan. "Sintering of Limestone in Calcination/Carbonation Cycles." Industrial & Engineering Chemistry Research 53, no. 42 (2014): 16235–44. http://dx.doi.org/10.1021/ie502069d.

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7

Daud, Farah Diana Mohd, Kumaravel Vignesh, Srimala Sreekantan, and Abdul Rahman Mohamed. "Improved CO2 adsorption capacity and cyclic stability of CaO sorbents incorporated with MgO." New Journal of Chemistry 40, no. 1 (2016): 231–37. http://dx.doi.org/10.1039/c5nj02081f.

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The CO<sub>2</sub> adsorption capacity of CaO sorbents with different MgO wt% (calcination temperature 800 °C, carbonation at 650 °C with 100% CO<sub>2</sub>, and de-carbonation at 800 °C in 100% N<sub>2</sub>).

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8

Li, Y. J., C. S. Zhao, H. C. Chen, L. B. Duan, and X. P. Chen. "CO2Capture Behavior of Shell during Calcination/Carbonation Cycles." Chemical Engineering & Technology 32, no. 8 (2009): 1176–82. http://dx.doi.org/10.1002/ceat.200900008.

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9

Tian, Si-cong, Jian-guo Jiang, Kai-min Li, Feng Yan, and Xue-jing Chen. "Performance of steel slag in carbonation–calcination looping for CO2capture from industrial flue gas." RSC Adv. 4, no. 14 (2014): 6858–62. http://dx.doi.org/10.1039/c3ra47426g.

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The carbonation–calcination looping route of steel slag can significantly improve its CO<sub>2</sub>capture capacity compared to the conventional route of direct carbonation sequestration, thus providing an alternative and more feasible option for the use of alkaline industrial wastes to capture CO<sub>2</sub>from industrial flue gases.

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10

Mora Mendoza, Eduin Yesid, Armando Sarmiento Santos, Enrique Vera López, et al. "Siderite Formation by Mechanochemical and High Pressure–High Temperature Processes for CO2 Capture Using Iron Ore as the Initial Sorbent." Processes 7, no. 10 (2019): 735. http://dx.doi.org/10.3390/pr7100735.

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Iron ore was studied as a CO2 absorbent. Carbonation was carried out by mechanochemical and high temperature–high pressure (HTHP) reactions. Kinetics of the carbonation reactions was studied for the two methods. In the mechanochemical process, it was analyzed as a function of the CO2 pressure and the rotation speed of the planetary ball mill, while in the HTHP process, the kinetics was studied as a function of pressure and temperature. The highest CO2 capture capacities achieved were 3.7341 mmol of CO2/g of sorbent in ball milling (30 bar of CO2 pressure, 400 rpm, 20 h) and 5.4392 mmol of CO2/

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11

Bouquet, Eric, Gontrand Leyssens, Cornelius Schönnenbeck, and Patrick Gilot. "The decrease of carbonation efficiency of CaO along calcination–carbonation cycles: Experiments and modelling." Chemical Engineering Science 64, no. 9 (2009): 2136–46. http://dx.doi.org/10.1016/j.ces.2009.01.045.

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12

Liu, Xiaotong, Xiaoxun Ma, Liu He, and Shisen Xu. "Effect of pre-calcination for modified CaO-based sorbents on multiple carbonation/calcination cycles." Chinese Journal of Chemical Engineering 25, no. 10 (2017): 1412–21. http://dx.doi.org/10.1016/j.cjche.2017.05.016.

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13

Lu, Shangqing, and Sufang Wu. "Calcination–carbonation durability of nano CaCO3 doped with Li2SO4." Chemical Engineering Journal 294 (June 2016): 22–29. http://dx.doi.org/10.1016/j.cej.2016.02.100.

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14

Cai, Jianjun, Shuzhong Wang, and Cao Kuang. "Modeling of carbonation reaction for CaO-based limestone with CO2 in multitudinous calcination-carbonation cycles." International Journal of Hydrogen Energy 42, no. 31 (2017): 19744–54. http://dx.doi.org/10.1016/j.ijhydene.2017.06.173.

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15

Wu, Szu-Chen, Po-Hsueh Chang, Chieh-Yen Lin, and Cheng-Hsiung Peng. "Multi-Metals CaMgAl Metal-Organic Framework as CaO-based Sorbent to Achieve Highly CO2 Capture Capacity and Cyclic Performance." Materials 13, no. 10 (2020): 2220. http://dx.doi.org/10.3390/ma13102220.

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In this study, Ca-based multi-metals metal-organic framework (CaMgAl-MOF) has been designed as precursor material for carbon dioxide (CO2) capture to enhance the CO2 capture capacity and stability during multiple carbonation-calcination cycles. The CaMgAl-MOFs were constructed from self-assembly of metal ions and organic ligands through hydrothermal process to make metal ions uniformly distributed through the whole structure. Upon heat treatment at 600 °C, the Ca-based multi-metals CaMgAl-MOF would gradually transform to CaO and MgO nanoparticles along with the amorphous aluminum oxide distrib

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16

Ahn, Ji Whan, Jung Ah Kim, Kwang Suk You, Hwan Kim, Hee Chan Cho, and Im Chan Lee. "The Effect of Initial Hydration Temperature on the Characteristics of Calcium Hydroxide and Aragonite Precipitated Calcium Carbonate." Solid State Phenomena 124-126 (June 2007): 815–18. http://dx.doi.org/10.4028/www.scientific.net/ssp.124-126.815.

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Precipitated Calcium Carbonate (PCC) is obtained through three processes; that of calcination, hydration, and carbonation. Thus, changes in each process condition determine the particle size or morphology of the mediums (calcium oxide and calcium hydroxide) as well as the product (PCC). To date, studies concerning precipitated calcium carbonate have mainly focused on the carbonation process, aimed at the manufacturing of PCC. Thus far, few studies on calcination or hydration have been conducted. Calcium hydroxide is regarded as the most important factor during the carbonation process. It is ob

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17

Fedunik-Hofman, Larissa, Alicia Bayon, and Scott W. Donne. "Kinetics of Solid-Gas Reactions and Their Application to Carbonate Looping Systems." Energies 12, no. 15 (2019): 2981. http://dx.doi.org/10.3390/en12152981.

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Reaction kinetics is an important field of study in chemical engineering to translate laboratory-scale studies to large-scale reactor conditions. The procedures used to determine kinetic parameters (activation energy, pre-exponential factor and the reaction model) include model-fitting, model-free and generalized methods, which have been extensively used in published literature to model solid-gas reactions. A comprehensive review of kinetic analysis methods will be presented using the example of carbonate looping, an important process applied to thermochemical energy storage and carbon capture

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18

Qiu, Yu Chong, Ke Hui Qiu, Jun Han Li, and Pei Cong Zhang. "Preparation of Al₂O₃ from the Nepheline Ore of Nanjiang County, Sichuan Province of China." Materials Science Forum 814 (March 2015): 230–34. http://dx.doi.org/10.4028/www.scientific.net/msf.814.230.

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Crystalline alumina samples with Al2O3 content of 95.23 wt.% were prepared directly from the nepheline ore in Nanjiang county, Sichuan province of China. Four steps were involved in the experiment of alumina preparation, including calcination, dissolution, carbonation and re-calcination. Lime was used in the calcination process with the nepheline concentrates powders to generate soluble aluminates and insoluble silicates. NaOH solution was used as the mother solution in the dissolution process. CO2 was introduced into the solution to precipitate the Al (OH)3 precursor, which was then fired to

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19

Li, Yan, Steve Buchi, John R. Grace, and C. Jim Lim. "SO2Removal and CO2Capture by Limestone Resulting from Calcination/Sulfation/Carbonation Cycles." Energy & Fuels 19, no. 5 (2005): 1927–34. http://dx.doi.org/10.1021/ef058003q.

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20

Grasa, Gemma S., and J. Carlos Abanades. "CO2Capture Capacity of CaO in Long Series of Carbonation/Calcination Cycles." Industrial & Engineering Chemistry Research 45, no. 26 (2006): 8846–51. http://dx.doi.org/10.1021/ie0606946.

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21

Yue, Lindsey, and Wojciech Lipiński. "Thermal transport model of a sorbent particle undergoing calcination-carbonation cycling." AIChE Journal 61, no. 8 (2015): 2647–56. http://dx.doi.org/10.1002/aic.14840.

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22

Krishnan, S. V., and Stratis V. Sotirchos. "Effective diffusivity changes during calcination, carbonation, recalcination, and sulfation of limestones." Chemical Engineering Science 49, no. 8 (1994): 1195–208. http://dx.doi.org/10.1016/0009-2509(94)85090-9.

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23

Fan, Hui-ming, Gao-peng Zhu, Ya-nan Qi, and Jian-an Liu. "Calcination-carbonization two-step process to improve the brightness of fly ash and its application in paper filling." Nordic Pulp & Paper Research Journal 34, no. 1 (2019): 59–66. http://dx.doi.org/10.1515/npprj-2018-0004.

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Abstract Chromogenic sources such as carbon particles and magnetic particles are the key factors restricting the brightness of fly ash. This study explored the feasibility of calcination-carbonation two-step method to improve the brightness of fly ash and apply it to paper filling. The results show that Under the condition of high temperature, the unburned carbon particles in fly ash are removed, and the brightness of fly ash is increased from 30 %ISO to 49 %ISO with the increase of burning loss. The dense calcium carbonate coating can be formed on the surface of fly ash particles modified by

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24

Zhao, Yu Qing, Chun Zhen Qiao, and Wei Jiao Chen. "Activation of Ca-Based CO₂ Sorbent by Hydration in Repetitive Calcination-Carbonation Reactions." Applied Mechanics and Materials 587-589 (July 2014): 755–60. http://dx.doi.org/10.4028/www.scientific.net/amm.587-589.755.

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The carbonation characteristics of Ca-based CO2 absorbent hydrated by water were investigated as part of a multi-cycle performance study, and the change of the microstructure, pore radius and specific surface area of the absorbent with the number of cycles was researched. The results show that, conversion of sorbent hydrated by water is enhanced to 85% after 10 cycle, significantly higher than the 20% achieved by dry limestone cycle. Because the specific surface area is greatly enhanced, as well as the distributions of pore radius is improved in the hydration process, which develop an effectiv

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25

Andrade, Carmen, and Miguel Sanjuán. "Updating Carbon Storage Capacity of Spanish Cements." Sustainability 10, no. 12 (2018): 4806. http://dx.doi.org/10.3390/su10124806.

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The fabrication of cement clinker releases CO2 due to the calcination of the limestone used as raw material, which contributes to the greenhouse effect. The industry is involved in a process of reducing this amount liberated to the atmosphere by mainly lowering the amount of clinker in the cements. The cement-based materials, such as concrete and mortars, combine part of this CO2 by a process called “carbonation”. Carbonation has been studied lately mainly due to the fact that it induces the corrosion of steel reinforcement when bringing the CO2 front to the surface of the reinforcing bars. Th

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26

Zhou, Wei, Peng Zhu, Wenjun Qu, Wu Yao, and Shengji Wu. "Study on the Influence of Calcined Underground Ant Nest Powder on the Durability of Concrete." Materials 13, no. 9 (2020): 2119. http://dx.doi.org/10.3390/ma13092119.

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Ants have strict requirements on the building materials of the nest, such as the size, weight, luster and color of soil particles. The soil of underground ant nests is composed of clay particles cemented together to form a hard brick-like material. The ant nest powder shows pozzolanic activity after calcination, which can meet the requirements for active admixture of concrete. Under the standard curing condition, the influence of calcined ant nest clay powder (CANCP) on the durability of concrete is evaluated by chloride penetration resistance, carbonization resistance and freeze–thaw resistan

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27

Rodaev, Vyacheslav V., and Svetlana S. Razlivalova. "The Zr-Doped CaO CO2 Sorbent Fabricated by Wet High-Energy Milling." Energies 13, no. 16 (2020): 4110. http://dx.doi.org/10.3390/en13164110.

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We fabricated the Zr-doped CaO sorbent for high-temperature CO2 capture by the wet high-energy co-milling of calcium carbonate and natural zirconium dioxide (baddeleyite) for the first time. The morphology of the material was examined by scanning electron microscopy, energy-dispersive X-ray analysis and X-ray diffraction. Its CO2 uptake capacity was determined using thermogravimetric analysis. After 50 carbonation–calcination cycles, the Zr-doped CaO sorbent characterized by a high enough CO2 uptake capacity of 8.6 mmol/g and unchanged microstructure due to CaZrO3 nanoparticles uniformly distr

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28

José, Nobre, Hawreen Ahmed, Bravo Miguel, Evangelista Luís, and de Jorge. "Magnesia (MgO) Production and Characterization, and Its Influence on the Performance of Cementitious Materials: A Review." Materials 13, no. 21 (2020): 4752. http://dx.doi.org/10.3390/ma13214752.

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This paper presents a literature review concerning the characteristics of MgO (magnesium oxide or magnesia) and its application in cementitious materials. It starts with the characterization of MgO in terms of production processes, calcination temperatures, reactivity, and physical properties. Relationships between different MgO characteristics are established. Then, the influence of MgO incorporation on the properties of cementitious materials is investigated. The mechanical strength and durability behaviour of cement pastes, mortars and concrete mixes made with MgO are discussed. The studied

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29

Ávila, I., A. Mortari, A. M. Santos, and P. M. Crnkovic. "THE CALCIUM LOOPING CYCLE STUDY FOR CAPTURING CARBON DIOXIDE APPLIED TO THE ENERGY GENERATION." Revista de Engenharia Térmica 12, no. 2 (2013): 28. http://dx.doi.org/10.5380/reterm.v12i2.62041.

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The calcium looping process (Ca-L) is a promising technology to reduce of the carbon dioxide (CO2) emissions when applied in energy generation systems. Ca-based materials (usually limestone) are used in this process as CO2 sorbents. Thus, the CO2 capture occurs by the reversible reaction between calcium oxide (CaO) and CO2, resulting in the calcium carbonate form (CaCO3). Compared to other technologies applied to carbon sequestration process, the Ca-L offers additional advantages such: the use of fluidized bed technology that is already well established; this process occurs at high temperature

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30

Stanmore, B. R., and P. Gilot. "Review—calcination and carbonation of limestone during thermal cycling for CO2 sequestration." Fuel Processing Technology 86, no. 16 (2005): 1707–43. http://dx.doi.org/10.1016/j.fuproc.2005.01.023.

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31

GRASA, G., J. ABANADES, M. ALONSO, and B. GONZALEZ. "Reactivity of highly cycled particles of CaO in a carbonation/calcination loop." Chemical Engineering Journal 137, no. 3 (2008): 561–67. http://dx.doi.org/10.1016/j.cej.2007.05.017.

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32

Chen, Huichao, Changsui Zhao, Yingjie Li, and Xiaoping Chen. "CO2Capture Performance of Calcium-Based Sorbents in a Pressurized Carbonation/Calcination Loop." Energy & Fuels 24, no. 10 (2010): 5751–56. http://dx.doi.org/10.1021/ef100565d.

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33

Grasa, Gemma S., Mónica Alonso, and J. Carlos Abanades. "Sulfation of CaO Particles in a Carbonation/Calcination Loop to Capture CO2." Industrial & Engineering Chemistry Research 47, no. 5 (2008): 1630–35. http://dx.doi.org/10.1021/ie070937+.

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34

Zhen-shan, Li, Cai Ning-sheng, and Eric Croiset. "Process analysis of CO2 capture from flue gas using carbonation/calcination cycles." AIChE Journal 54, no. 7 (2008): 1912–25. http://dx.doi.org/10.1002/aic.11486.

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35

Sun, Ping, C. Jim Lim, and John R. Grace. "Cyclic CO2 capture by limestone-derived sorbent during prolonged calcination/carbonation cycling." AIChE Journal 54, no. 6 (2008): 1668–77. http://dx.doi.org/10.1002/aic.11491.

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36

Wardhani, Sri, Fanny Prasetia, Mohammad Misbah Khunur, Danar Purwonugroho, and Yuniar Ponco Prananto. "Effect of CO₂ Flow Rate and Carbonation Temperature in the Synthesis of Crystalline Precipitated Calcium Carbonate (PCC) from Limestone." Indonesian Journal of Chemistry 18, no. 4 (2018): 573. http://dx.doi.org/10.22146/ijc.26608.

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The effect of CO2 flow rate and carbonation temperature were studied in the synthesis of PCC from limestone using carbonation method. The synthesis was started by dissolving CaO that was obtained from calcination of limestone into HNO3 6M. The solution was then added with ammonia solution and then streamed with CO2 until pH 8 with flow rates of 0.5; 1.0; 1.5; and 2.0 L/min. The optimum flow rate obtained from this stage was then applied in the carbonation process with temperatures of 50, 80, 100, 150, 200, and 250 °C. The results showed that low flow rate give reasonably high yield but the yie

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37

Cai, Jianjun, Shuzhong Wang, and Cao Kuang. "A Modified Random Pore Model for Carbonation Reaction of CaO-based Limestone with CO 2 in Different Calcination-carbonation Cycles." Energy Procedia 105 (May 2017): 1924–31. http://dx.doi.org/10.1016/j.egypro.2017.03.561.

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38

Wang, Rong-Chi, and Wang-Chi Chuang. "Experimental studies of modified limestone for CO2 capture in multiple carbonation/calcination cycles." Journal of the Taiwan Institute of Chemical Engineers 44, no. 6 (2013): 1067–74. http://dx.doi.org/10.1016/j.jtice.2013.06.029.

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39

Li, Ying-jie, Chang-sui Zhao, Lun-bo Duan, et al. "Cyclic calcination/carbonation looping of dolomite modified with acetic acid for CO2 capture." Fuel Processing Technology 89, no. 12 (2008): 1461–69. http://dx.doi.org/10.1016/j.fuproc.2008.07.008.

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40

Chen, Huichao, Changsui Zhao, Minliang Chen, Yingjie Li, and Xiaoping Chen. "CO2 uptake of modified calcium-based sorbents in a pressurized carbonation–calcination looping." Fuel Processing Technology 92, no. 5 (2011): 1144–51. http://dx.doi.org/10.1016/j.fuproc.2011.01.011.

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41

Alvarez, Diego, Miguel Peña, and Angeles G. Borrego. "Behavior of Different Calcium-Based Sorbents in a Calcination/Carbonation Cycle for CO2Capture." Energy & Fuels 21, no. 3 (2007): 1534–42. http://dx.doi.org/10.1021/ef060573i.

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42

Salaudeen, Shakirudeen A., S. M. Al-Salem, Mohammad Heidari, Bishnu Acharya, and Animesh Dutta. "Eggshell as a Carbon Dioxide Sorbent: Kinetics of the Calcination and Carbonation Reactions." Energy & Fuels 33, no. 5 (2019): 4474–86. http://dx.doi.org/10.1021/acs.energyfuels.9b00072.

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43

Li, Y. J., C. S. Zhao, C. R. Qu, L. B. Duan, Q. Z. Li, and C. Liang. "CO2 Capture Using CaO Modified with Ethanol/Water Solution during Cyclic Calcination/Carbonation." Chemical Engineering & Technology 31, no. 2 (2008): 237–44. http://dx.doi.org/10.1002/ceat.200700371.

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44

Romeo, Luis M., J. Carlos Abanades, Jesús M. Escosa, et al. "Oxyfuel carbonation/calcination cycle for low cost CO2 capture in existing power plants." Energy Conversion and Management 49, no. 10 (2008): 2809–14. http://dx.doi.org/10.1016/j.enconman.2008.03.022.

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45

Wang, William, Shwetha Ramkumar, Danny Wong, and Liang-Shih Fan. "Simulations and process analysis of the carbonation–calcination reaction process with intermediate hydration." Fuel 92, no. 1 (2012): 94–106. http://dx.doi.org/10.1016/j.fuel.2011.06.059.

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46

BARELLI, L., G. BIDINI, A. CORRADETTI, and U. DESIDERI. "Study of the carbonation–calcination reaction applied to the hydrogen production from syngas." Energy 32, no. 5 (2007): 697–710. http://dx.doi.org/10.1016/j.energy.2006.04.016.

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47

BARELLI, L., G. BIDINI, A. CORRADETTI, and U. DESIDERI. "Production of hydrogen through the carbonation–calcination reaction applied to CH4/CO2 mixtures." Energy 32, no. 5 (2007): 834–43. http://dx.doi.org/10.1016/j.energy.2006.06.008.

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48

Kavosh, Masoud, Kumar Patchigolla, John E. Oakey, Edward J. Anthony, Scott Champagne, and Robin Hughes. "Pressurised calcination–atmospheric carbonation of limestone for cyclic CO2 capture from flue gases." Chemical Engineering Research and Design 102 (October 2015): 116–23. http://dx.doi.org/10.1016/j.cherd.2015.06.024.

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49

Li, Yingjie, Rongyue Sun, Changtian Liu, Hongling Liu, and Chunmei Lu. "CO2 capture by carbide slag from chlor-alkali plant in calcination/carbonation cycles." International Journal of Greenhouse Gas Control 9 (July 2012): 117–23. http://dx.doi.org/10.1016/j.ijggc.2012.03.012.

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50

Wang, Ming Wei, Jing Yang, Hong Wen Ma, Jie Shen, Jin Hong Li, and Feng Guo. "Extraction of Aluminum Hydroxide from Coal Fly Ash by Pre-Desilication and Calcination Methods." Advanced Materials Research 396-398 (November 2011): 706–10. http://dx.doi.org/10.4028/www.scientific.net/amr.396-398.706.

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Using coal fly ash from one thermal power plant in Ningxia, China as the raw material, aluminum hydroxide powder was successfully extracted by pre-desilication , calcination, dissolution and carbonation precipitation processes. The research results indicated that the mullite, Quartz and glass phase in the coal fly ash could be changed into NaSiO3, NaAlO2 and Na2CaSiO4 after the coal fly ash was treated by desilication and calcination. The SiO2and Al2O3 components in the coal fly ash were mainly separated by dissolving the calcined sample using water. The dissolution rate of Al2O3 from the calc

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