Abstract
A three-stage cross-flow Venturi jet reactor was innovatively designed in this study to conduct an experimental study on the physical simulation of the carbonization process of calcified slag. The pH changes during CO2 absorption by NaOH were measured by a pH meter. The influence law of superficial gas velocity, superficial liquid velocity, and inlet pressure on CO2 absorption rate and utilization rate were investigated. The results show that the volumetric mass transfer coefficient with the increase of superficial gas velocity first remains unchanged and then increases, decreases with the increase of superficial liquid velocity, and increases with the increase of inlet pressure, and the latter stage is greater than the previous stage. The CO2 utilization rate does not change with the increase of superficial gas velocity and inlet liquid velocity but increases with the increase of inlet pressure and remains unchanged afterwards. This result provides support for the design and industrial application of carbonization reactors.
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References
Jiang YJ, Wan M (2021) Study on alumina production process. World Nonferrous Metals 17:175–176
Dmitry Z, Liliya P, Mikhail F (2021) Extraction of valuable elements from red mud with a focus on using liquid media—a review. Recycling 6(2):38–38
Pan XL, Lv ZY, Wu HF (2023) Research status and prospects of red mud recycling technology for iron and aluminum resources. Chin J Nonferrous Metals 1–32
Agrawal S, Dhawan N (2021) Evaluation of red mud as a polymetallic source—a review. Miner Eng 171:107084
Steve H (2022) Sustainable bauxite residue management guidance. International Aluminium Institute, London
Zhang TA, Lv GZ, Liu Y (2014) Method for dissolving aluminum oxide from medium and low-grade bauxite based on calcification carbonization transformation. CN102757073B
Lv GZ, Zhang TA, Guo FF (2019) Clean and efficient utilization of low-grade high-iron sedimentary bauxite via calcification-carbonation method. Hydrometallurgy 187
Lv GZ, Zhang TA (2019) Utilization of Bayer red mud by a calcification–carbonation method using calcium aluminate hydrate as a calcium source. Hydrometallurgy 188:248–255
Li RB, Zhang TA, Liu Y (2016) Calcification-carbonation method for red mud processing. J Hazard Mater 316(5):94–101
Zhu XF, Zhang TA, Wang YX (2016) Recovery of alkali and alumina from Bayer red mud by the calcification-carbonation method. Int J Miner Metall Mater 23(3):257–261
Wang Y, Zhang TA (2018) Recovery of alkali and alumina from bauxite residue (red mud) and complete reuse of the treated residue. J Cleaner Prod 188:456–465
Stapurewicz T, Themelis NJ (1987) Mixing and mass transfer phenomena in bottom-injected gas-liquid reactors. Can Metall Q 26(2):123–128
Wang KY, Ma YL, Li C (2022) Gas-liquid mass transfer coefficient of gas-liquid solid micro fluidized beds. J Chem Ind Eng 73(08):3529–354
Wang DX (2017) Simulation study on fluid flow behavior in oxygen bottom blown smelting furnace. Northeastern University
Pucciarelli A, Ambrosini W (2020) A successful general fluid-to-fluid similarity theory for heat transfer at supercritical pressure. Int J Heat Mass Transfer 159:120152
Inada S, Watanabe Z (1976) The effect of gas properties on the rate of CO2 absorption into NaOH aqueous solution. Toki and Ben 62(7):807–816
Liu H, Zeng H, Liu WP (2004) Simulation experimental study on refining aluminum liquid by rotating powder (flux) spraying. Light Alloy Process Technol 32(4):14–15
Acknowledgements
This work was supported by the special support from the China Postdoctoral Science Foundation (in station) (grant number 2023T1600880) and National Natural Science Foundation Youth Science Foundation Project (grant number 52304324).
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Xiang, L. et al. (2024). Design and Research of Three-Stage Reactor of Carbonation Process of Calcified Residue. In: Iloeje, C., et al. Energy Technology 2024. TMS 2024. The Minerals, Metals & Materials Series. Springer, Cham. https://doi.org/10.1007/978-3-031-50244-6_19
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DOI: https://doi.org/10.1007/978-3-031-50244-6_19
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