Evaluation of hydrodynamic efficiency of a vertical spiral scrubber: analysis of channel geometry influence on secondary flows and pressure drop
DOI:
https://doi.org/10.14311/AP.2026.66.0433Keywords:
spiral scrubber, wet gas cleaning, secondary flows, pressure drop, centrifugal intensification, liquid-to-gas ratio ( L/G), hollow-cone nozzles, geometric optimisation, energy efficiency, flue gas desulfurisationAbstract
This paper addresses the critical engineering challenge of optimising the hydraulic efficiency and energy consumption of wet gas cleaning systems in thermal power plants. While Venturi scrubbers and packed columns provide high removal efficiency, they often suffer from excessive hydraulic resistance or fouling issues. This study focuses on determining the optimal geometric parameters of a vertically oriented spiral scrubber to ensure an energy-efficient operating mode for a medium-capacity industrial flow of 25 000 m3 h−1. Using a theoretical calculation model integrated with 3D-modeling (SolidWorks) and engineering verification (AutoCAD), we analysed the influence of the spiral channel geometry (helix inclination angle α, number of turns, and radius of curvature) on the generation of secondary flows and pressure drop (ΔP).The results indicate that the optimal configuration is achieved at α = 7°, ensuring a stable film regime and an active contact path of 36 meters. We proposed an optimised irrigation system configuration utilising 24–28 hollow-cone nozzles arranged across three vertical manifolds, achieving an ultra-low liquid-to-gas ratio ( L/G) of 0.55–0.70 kgm−3 while maintaining a stable phase contact through a high-gravity centrifugal field (10–15 g). A comparative analysis showed that this configuration ensures a total pressure drop of 397.4Pa at an inlet gas velocity of 7.7 ms−1, which is significantly lower than that of traditional Venturi apparatuses. The obtained dependencies provide a basis for the rational design of large-scale gas-liquid contactors with a reduced carbon footprint and lower operational energy penalties.
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[1] World Health Organization. WHO global air quality guidelines: Particulate matter (PM2.5 and PM10), ozone, nitrogen dioxide, sulfur dioxide and carbon monoxide, 2021. [2026-04-13]. https://apps.who.int/iris/handle/10665/345329
[2] P. Sicard, E. Agathokleous, A. De Marco, et al. Urban population exposure to air pollution in Europe over the last decades. Environmental Sciences Europe 33(1):28, 2021. https://doi.org/10.1186/s12302-020-00450-2
[3] I. Manisalidis, E. Stavropoulou, A. Stavropoulos, E. Bezirtzoglou. Environmental and health impacts of air pollution: A review. Frontiers in Public Health 8:14, 2020. https://doi.org/10.3389/fpubh.2020.00014
[4] M. Zhao, P. Xue, J. Liu, et al. A review of removing SO2 and NOx by wet scrubbing. Sustainable Energy Technologies and Assessments 47:101451, 2021. https://doi.org/10.1016/j.seta.2021.101451
[5] S. Wang, S. Xu, S. Gao, et al. Simultaneous removal of SO2 and NOx from flue gas by low-temperature adsorption over activated carbon. Scientific Reports 11(1):11003, 2021. https://doi.org/10.1038/s41598-021-90532-9
[6] S. Hu, Y. Gao, G. Feng, et al. Experimental study of the dust-removal performance of a wet scrubber. International Journal of Coal Science & Technology 8(2):228–239, 2021. https://doi.org/10.1007/s40789-021-00410-y
[7] T. Mkilima, S. Manyele. Assessment of a multi-stage wet scrubber performance based on characteristics of scrubbing solution. Tanzania Journal of Engineering and Technology 42(2):206–223, 2023. https://doi.org/10.52339/tjet.v42i2.836
[8] D. Mchabe, R. C. Everson, P. A. Ramachandran, et al. Development of an integrated model for absorption of sulphur dioxide in limestone slurry. Chemical Engineering Science 229:116050, 2021. https://doi.org/10.1016/j.ces.2020.116050
[9] B. A. Patel, C. S. Pereira. Process intensification at scale: An industrial perspective. Chemical Engineering and Processing – Process Intensification 181:109098, 2022. https://doi.org/10.1016/j.cep.2022.109098
[10] Z. Zhu, B. Xu. Purification technologies for NOx removal from flue gas: A review. Separations 9(10):307, 2022. https://doi.org/10.3390/separations9100307
[11] S. Guo, Y. Liu, C. Zhang, et al. Computational fluid dynamics analysis of wet dust removal in high-gravity countercurrent rotating packed bed. Atmosphere 15(2):157, 2024. https://doi.org/10.3390/atmos15020157
[12] L. D. G. Sigalotti, C. E. Alvarado-Rodríguez, O. Rendón. Fluid flow in helically coiled pipes. Fluids 8(12):308, 2023. https://doi.org/10.3390/fluids8120308
[13] L. Qin, Z. Jiang, D. Zhou, et al. Numerical investigation of vortex-induced enhancement in the mixing characteristics of double-spiral and serpentine microchannels. Micromachines 16(9):1016, 2025. https://doi.org/10.3390/mi16091016
[14] A. Y. Gelfgat, A. L. Yarin, P. Z. Bar-Yoseph. Dean vortices-induced enhancement of mass transfer through an interface separating two immiscible liquids. Physics of Fluids 15(2):330–347, 2003. https://doi.org/10.1063/1.1532732
[15] H. Guo, S. Zhou, M. Shreka, Y. Feng. A numerical investigation on the optimization of uneven flow in a marine De-SOx scrubber. Processes 8(7):862, 2020. https://doi.org/10.3390/pr8070862
[16] I. E. Idelchik. Handbook of hydraulic resistance. Begell House, New York, 4th edn., 2008. https://doi.org/10.1615/978-1-56700-251-5.0
[17] R. K. Srivastava, W. Jozewicz. Flue gas desulfurization: The state of the art. Journal of the Air & Waste Management Association 51(12):1676–1688, 2001. https://doi.org/10.1080/10473289.2001.10464387
[18] J. Zhu, Q. Xu, L. P. Zhang. Experimental study on internal flow field of wet desulphurization tower. Advanced Materials Research 354–355:137–144, 2011. https://doi.org/10.4028/www.scientific.net/AMR. 354-355.137
[19] A. K. Sleiti, E. J. Naimaster. Heat transfer and pressure drop through rectangular helical ducts. In Proceedings of the ASME 2009 International Mechanical Engineering Congress and Exposition, vol. 9, p. 133–139. ASME, 2009. https://doi.org/10.1115/IMECE2009-12316
[20] T. Anil Kumar, G. M. J. Raju, G. V. S. Sarma, K. V. Ramesh. Mass transfer at the confining wall of helically coiled circular tubes with gas-liquid flow and fluidized beds. Chemical Engineering Journal 153(1–3):114–119, 2009. https://doi.org/10.1016/j.cej.2009.02.039
[21] H. Ito. Friction factors for turbulent flow in curved pipes. Journal of Basic Engineering 81(2):123–132, 1959. https://doi.org/10.1115/1.4008390
[22] D.-E. Jugănaru, M. Panaitescu, L.-C. Stan. Comparative CFD based parametric analysis of gas flow in two conter-flow wet scrubber systems. Journal of Marine Technology and Environment 1:28–32, 2021. https://doi.org/10.53464/JMTE.01.2021.04
[23] J. A. S. Gonçalves, D. F. Alonso, M. A. M. Costa, et al. Evaluation of the models available for the prediction of pressure drop in Venturi scrubbers. Journal of Hazardous Materials 81(1–2):123–140, 2001. https://doi.org/10.1016/S0304-3894(00)00336-8
[24] H. T. Kim, C. H. Jung, S. N. Oh, K. W. Lee. Particle removal efficiency of gravitational wet scrubber considering diffusion, interception, and impaction. Environmental Engineering Science 18(2):125–136, 2001. https://doi.org/10.1089/10928750151132357
[25] C. J. Geankoplis. Transport Processes and Separation Process Principles. Pearson, 4th edn., 2003.
[26] N. Qamaruz-Zaman, Y. Kun, M. S. Hossain. Recent advances in hybrid wet scrubbing techniques for NOx and SO2 removal: State of the art and future research. Chemosphere 273:129695, 2021. https://doi.org/10.1016/j.chemosphere.2021.129695442
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