Development of a Membrane Desalination and Coprecipitation System for Enhanced Reclamation of Cooling Tower Water: Mechanism Evaluation and Pilot-Scale Study

The raw water in southern Taiwan has high hardness and high silica (SiO2) characteristics. If the high SiO2-content water is used as a makeup water source for cooling towers (CT), the SiO2 concentration in the tower blowdown (BD) would exceed the saturation level (120 mg/L) within a short operational period. The objective of this study was to develop a combined coprecipitation (first stage) and membrane desalination [ultrafiltration (UF)/reverse osmosis (RO) (second stage)] system to enhance the water reclamation efficiency of cooling tower (CT) in the petrochemical industry. Flue gas desulfurization (FGD) wastewater containing magnesium ions (Mg2+) and cooling tower blowdown (CTBD) were mixed, and Mg2+ and silica (SiO2) were removed through the coprecipitation process (core mechanism). The supernatant was directed to the UF/RO for reclamation. Results show that alkaline environments promoted the creation of Mg2+─SiO2 coprecipitates [Mg3Si2O5(OH)4, Mg2SiO4 and MgSiO3], which allowed for the effective removal of SiO2. Under alkaline conditions, when the molar ratio of Mg2+/calcium ions (Ca2+)∶SiO2 was 1∶1, Mg2+ exhibited more pronounced advantages for SiO2 removal. The maximum SiO2 removal rate reached 99% in the Mg2+∶SiO2 group, compared to 75% in the Ca2+∶SiO2 group. Mg2+ showed a stronger correlation (R2=0.95) with SiO2 removal than Ca2+ (R2=0.61355). Following the coprecipitation process, the supernatant was transferred to the UF/RO for desalination. The pilot-scale study results indicate that up to 92% of SiO2 in CTBD could be removed. When the volume ratio of FGD wastewater to CTBD was 1∶5 (pH=10.5), the SiO2 concentration was reduced to below 25 mg/L. The UF/RO treatment results show that the conductivity, alkalinity, and Mg2+ concentrations were reduced to 179 μS/cm, 15 mg as CaCO3/L, and not detectable, respectively. The regenerated water is suitable for reuse as makeup water for CT.

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Journal
Journal of Environmental Engineering
Published
2025-04-09
DOI
https://doi.org/10.1061/joeedu.eeeng-8006
Primary Topic
Solar-Powered Water Purification Methods
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article
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article

Development of a Membrane Desalination and Coprecipitation System for Enhanced Reclamation of Cooling Tower Water: Mechanism Evaluation and Pilot-Scale Study

Chih‐Ming Kao, Tian C. Zhang, Jinmin Li, Boming Yang et al.
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Journal of Environmental Engineering
Solar-Powered Water Purification Methods
article

Development of a Membrane Desalination and Coprecipitation System for Enhanced Reclamation of Cooling Tower Water: Mechanism Evaluation and Pilot-Scale Study

Chih‐Ming Kao, Tian C. Zhang, Jinmin Li, Boming Yang, Chathura Dhanasinghe
article en

Abstract

The raw water in southern Taiwan has high hardness and high silica (SiO2) characteristics. If the high SiO2-content water is used as a makeup water source for cooling towers (CT), the SiO2 concentration in the tower blowdown (BD) would exceed the saturation level (120 mg/L) within a short operational period. The objective of this study was to develop a combined coprecipitation (first stage) and membrane desalination [ultrafiltration (UF)/reverse osmosis (RO) (second stage)] system to enhance the water reclamation efficiency of cooling tower (CT) in the petrochemical industry. Flue gas desulfurization (FGD) wastewater containing magnesium ions (Mg2+) and cooling tower blowdown (CTBD) were mixed, and Mg2+ and silica (SiO2) were removed through the coprecipitation process (core mechanism). The supernatant was directed to the UF/RO for reclamation. Results show that alkaline environments promoted the creation of Mg2+─SiO2 coprecipitates [Mg3Si2O5(OH)4, Mg2SiO4 and MgSiO3], which allowed for the effective removal of SiO2. Under alkaline conditions, when the molar ratio of Mg2+/calcium ions (Ca2+)∶SiO2 was 1∶1, Mg2+ exhibited more pronounced advantages for SiO2 removal. The maximum SiO2 removal rate reached 99% in the Mg2+∶SiO2 group, compared to 75% in the Ca2+∶SiO2 group. Mg2+ showed a stronger correlation (R2=0.95) with SiO2 removal than Ca2+ (R2=0.61355). Following the coprecipitation process, the supernatant was transferred to the UF/RO for desalination. The pilot-scale study results indicate that up to 92% of SiO2 in CTBD could be removed. When the volume ratio of FGD wastewater to CTBD was 1∶5 (pH=10.5), the SiO2 concentration was reduced to below 25 mg/L. The UF/RO treatment results show that the conductivity, alkalinity, and Mg2+ concentrations were reduced to 179 μS/cm, 15 mg as CaCO3/L, and not detectable, respectively. The regenerated water is suitable for reuse as makeup water for CT.

Journal of Environmental EngineeringVol. 151(6)
University of Nebraska–Lincoln (US), National Sun Yat-sen University (TW), Formosa Plastics (Taiwan) (TW)
Clean water and sanitation
Openalex Percentile: Top 96%
Solar-Powered Water Purification Methods
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