Electrocoagulation Combined with Ultrafiltration Membranes as Pretreatment for RO Desalination of Synthetic Cooling Tower Blowdown Water

  • Kenji Lam
  • , Erika Yamazaki
  • , Rajuan Nelson
  • , Sungsoon Kim
  • , Jane Park
  • , Javier A. Quezada-Renteria
  • , Claire Murphy
  • , Sandip Pal
  • , Lily Lee
  • , Xinyi Wang
  • , Fan Yang
  • , Minhao Xiao
  • , Minju Cha
  • , Costas Tsouris
  • , Marta Hatzell
  • , David Jassby

Research output: Contribution to journalArticlepeer-review

Abstract

Electrocoagulation (EC), an electrochemical water treatment process, is commonly used to remove particulate and colloidal matter from water. Here, we demonstrate that EC, when coupled with membrane filtration, is also capable of removing dissolved species, such as Ca+, Mg2+, and SiOx. The removal of such species is important for downstream membrane-based desalination treatment of the water that can suffer from reduced performance due to membrane scaling. Here, we describe how EC can be combined with a low-pressure membrane (LPM) system to offer efficient (and potentially universal) pretreatment for downstream membrane desalination. Synthetic water, simulating cooling tower blowdown (CTBD) with elevated concentrations of hardness and silicates (Ca: 418 ppm, Mg: 63 ppm, SiO2: 50 ppm) is treated using EC coupled to ultrafiltration (UF) to remove Mg up to 30 ± 1%, Ca up to 29 ± 1%, and silica up to 99 ± 1%. We evaluated the effectiveness of the EC-UF pretreatment system in reducing downstream RO scaling using thermodynamic modeling to predict the saturation index (SI) at the RO membrane/water interface. An SI value below zero (SI < 0) indicates under-saturated conditions (with respect to a particular mineral) where mineral scaling does not take place, which correlates with improved water recovery. Our findings suggest that the EC-UF pretreatment system was able to increase water recovery by up to 30%, compared to 0% recovery without pretreatment, under optimal conditions (feed solution pH of 7 and an EC charge loading of 1800 C/L). Finally, we conducted an economic analysis showing that implementing an EC-UF system for CTBD water could yield a cost benefit of up to $14.13 per m3compared to direct brine disposal.

Original languageEnglish
Pages (from-to)3262-3275
Number of pages14
JournalACS ES and T Engineering
Volume5
Issue number12
DOIs
StatePublished - Dec 12 2025

Funding

Support for this work was provided by the National Alliance for Water Innovation (NAWI), funded through the US Department of Energy (DOE), Office of Energy Efficiency and Renewable Energy (EERE), Advanced Manufacturing Office, under Funding Opportunity Announcement RP20407-003. SEM and EDS data acquisition was performed on the Zeiss Supra 40VP SEM by Judy Su at the Electron Imaging Center for Nanosystems (EICN) at the University of California, Los Angeles’s California for NanoSystems Institute (CNSI), RRID:SCR_022900.

Keywords

  • cooling tower blowdown
  • hardness
  • membrane filtration
  • saturation index
  • silica

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