Extraction of Si from Alkaline-Roasted Boron Ore Concentrate

Document Type : Research Article

Authors

1 School of Metallurgy, Northeastern University, Shenyang 110819, P.R. CHINA

2 Liaoning Institute of Science and Technology, Benxi, 117000, P.R. CHINA

3 Department of Materials Science and Engineering, University of Utah, Salt Lake City, UT 84112, USA

4 School of Metallurgy and Environment, Central South University, Changsha 410083, P.R. CHINA

Abstract

The process of alkali roasting boron ore concentrate was proposed for the problems existing in the process of boron ore concentrate smelting. In this research, the influencing factors included the molar ratio of alkali to boron ore concentrate, roasting temperature, and roasting time were investigated. The single experiment and orthogonal experiments show the optimal conditions for roasting under the conditions evaluated including a temperature of 550oC, roasting time of 60 min, and a molar ratio of alkali to ore of 3:1. In the roasting process, the Si extraction correlated with the shrinking core model assuming a solid product layer according to XRD and SEM. Thus, the kinetics is controlled by diffusion through the product layer. The apparent activation energy for Si extraction was 13.47kJ/mol, and the roasting rate can be expressed as:
1-(2/3α)-(1-α)2/3=1.428×10-2exp(-13470/RT)t.

Keywords

Main Subjects


[1] Sun Qing, Zheng Shui-lin, Li Hui, Hou Hui-li. Boron Resource and Prospects of Comprehensive Utilization of Boron Mud as a Resource in China, Earth Science Frontiers, 21(5): 325–330 (2014).
[2] Jiang S.Y., Boron Isotope Geochemistry of Hydrothermal ore Deposits in China: A Preliminary Study, Physics and Chemistry of the Earth Part A Solid, 26: 851–858 (2001).
[3] Yakup Kar, Nejdet Şen, Ayhan Demirbaş. Boron Minerals in Turkey, Their Application Areas and Importance for the Country’s Economy, Minerals and Energy-Raw Materials Report, 20(2): 2–10 (2006).
[4] Tang Yao, Chen Chun-lin, Xiong Xian-xiao, Gao Peng. World Boron Distribution and Current Status of Its Exploitation and Development, Modern Chemical Industry, 33(10): 1−4, 6 (2013). (in Chinese)
[5] Ning Zhi-Qiang, Song Qiu-shi, Zhai Yu-Chun, Xie Hong-Wei, Yu Kai. Desilication Kinetics of Calcined Boron Mud in Molten Sodium Hydroxide Media, Journal of Central South University, 23: 2191−2198 (2016).
[6] Li G., Liang B., Rao M., Zhang Y., Jiang T., An Innovative Process for Extracting Boron and Simultaneous Recovering Metallic Iron from Ludwigite Ore, Miner. Eng., 56: 57–60 (2014).
[7] Qiao X., Li W., Zhang L., White N.C., Zhang F., Yao Z., Chemical and Boron Isotope Compositions of Tourmaline in the Hadamiao Porphyry Gold Deposit, Inner Mongolia, China. Chemical Geology, 519: 39-55 (2019).
[8] Gemici Unsal, Tarcan Gultekin, Helvac Cahit, Somay A. Melis, High Arsenic and Boronconcentrations in Groundwaters Related to Mining Activity in the Bigadic Borate Deposits (Westernturkey), Applied Geochemistry, 23(8): 2402-2407 (2008).
[9] Zhong Hu-Rui, Wen Qi-Hua, Fu Zhou-Mei, Su Wen-Chao, Wu Bi-Xian, Tang Peng-Jian, Zhong Hong. Geological and Geochemical Constraints on the Origin of the Giant Lincang Coal Seamhostedgermanium Deposit, Yunnan, SW China: A Review, Ore Geology Reviews, 36(1-3): 221-234 (2009).
[10] Ning Zhi-Qiang, Zhai Yu-Chun, Zhou Di, Cao Yong-xin, Gu Hui-min. Study of the Technique for the Preparation of Epsosmalt from the Boron Mud, Light Metal, 2007(7): 61−63. [in Chinese]
[11] Lv X., Cui F., Ning Z, Free M.L., Zhai, Yuchun, Mechanism and Kinetics of Ammonium Sulfate Roasting of Boron-Bearing Iron Tailings for Enhanced Metal Extraction, Processes, 7(11): 812 (2019).
[12] Guliyev R., Kuşlu S., Çalban T., Çolak S., Leaching Kinetics of Colemanite in Potassium Hydrogen Sulphate Solutions, Journal of Industrial and Engineering Chemistry, 18(1): 3844 (2012).
[13] DING Y., Wang J., Wang G., MA S., Xue Q., Comprehensive Utilization of Paigeite Ore Using Iron Nugget Making Process, Journal of Iron and Steel Research International, 19(6): 9-13 (2012).
[14] Jie L., Fan Z.G., Liu Y.L., Liu S.L., Jiang T., Xi Z.P., Preparation of Boric Acid from Low-Grade Ascharite and Recovery of Magnesium Sulfate, Tran. Nonferrous Met. Soc. China, 20: 1161–1165 (2010).
[15] Yang T., Dou A., Lei C., Ren J., Liu Z., Ligand Selection for Complex- Leaching Valuable Metals in Hydrometallurgy, Transaction of Nonferrous Metals Society of China, 20(6): 1148-1153 (2010).
[16] Guliyev R., Ku¸slu S., Çalban T., Çolak S., Leaching Kinetics of Colemanite in Potassium Hydrogen Sulphate Solutions, J. Ind. Eng. Chem., 18: 38–44 (2012).
[17] Liang B., Li G., Rao M., Peng Z., Zhang Y., Jiang T., Water Leaching of Boron from Soda-Ash-Activated Ludwigite Ore, Hydrometallurgy, 167: 101–106 (2017).
[18] Erdo ˘Gan Y., Aksu M., Demirba¸s A., Abalı Y., Analyses of Boronic Ores and Sludges and Solubilities of Boron Minerals in CO2-Saturated Water, Resour, Conserve Recycle, 24: 275–283 (1998).
[19] Kavcı E., Calban T., Colak S., Ku¸slu S., Leaching Kinetics of Ulexite in Sodium Hydrogen Sulphate Solutions, J. Ind. Eng. Chem., 20: 2625–2631 (2014).
[20] Qin S., Yin B., Zhang Y., Zhang Y., Leaching Kinetics of Szaibelyite Ore in NaOH Solution, Hydrometallurgy, 157: 333–339 (2015).
[21] Xu Y., Jiang T., Zhou M., Wen J., Chen W., Xue X., Effects of Mechanical Activation on Physicochemical Properties and Alkaline Leaching of Boron Concentrate, Hydrometallurgy, 173: 32–42 (2017).
[22] Xu Y., Jiang T., Wen J., Gao H., Wang J., Xue X., Leaching Kinetics of Mechanically Activated Boron Concentrate in a NaOH Solution, Hydrometallurgy, 179: 60–72 (2018).
[35] Maghsoudi P., Sadeghi S., Xiong Q., Aminossadati S.M., A Multi-Factor Methodology for Evaluation and Optimization of Plate-Fin Recuperators for Micro Gas Turbine Applications Considering Payback Period as Universal Objective Function, International Journal of Numerical Methods for Heat & Fluid Flow, 30(5): 2411-2438 (2019).
 [36] Towler G., Sinnott R., “Chemical Engineering Design: Principles, Practice and Economics of Plant and Process Design”, 2nd ed, Capital Cost Estimating, United Kingdom: Butterworth-Heinemann, (2013).
[37] Chemical Engineering Essential for The CPI Professional, Chemical Engineering Plant Cost Index,
[38] U.S. Energy Information Administration (eia), Electric Power Monthly,
        https://www.eia.gov/electricity/monthly/, December 2018 (Accessed 6 September 2019).
[39] U.S. Energy Information Administration (eia), Price of Liquefied Natural Gas Exports,
        https://www.eia.gov/dnav/ng/hist/n9133us3M.htm, October 2018 (Accessed 6 September 2019).
[41] Hanafizadeh P., Maghsoudi P., Exergy, Economy and Pressure Drop Analyses for Optimal Design of Recuperator Used in Microturbine, Energy Equipment and Systems, 5(2): 95-113 (2017).