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Shi D, Liu T. Versatile Gas-Transfer Membrane in Water and Wastewater Treatment: Principles, Opportunities, and Challenges. ACS ENVIRONMENTAL AU 2025; 5:152-164. [PMID: 40125285 PMCID: PMC11926753 DOI: 10.1021/acsenvironau.4c00134] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Key Words] [Grants] [Track Full Text] [Download PDF] [Figures] [Subscribe] [Scholar Register] [Received: 11/28/2024] [Revised: 01/15/2025] [Accepted: 01/15/2025] [Indexed: 03/25/2025]
Abstract
Technologies using liquid-transfer membranes, such as microfiltration, ultrafiltration, and reverse osmosis, have been widely applied in water and wastewater treatment. In the last few decades, gas-transfer membranes have been introduced in various fields to facilitate mass transfer, in which gaseous compounds permeate through membrane pores driven by gradients in chemical concentration or potential. A notable knowledge gap exists among researchers working on these emerging gas-transfer membranes as they approach this subject from different angles and areas of expertise (e.g., material science versus microbiology). This review explores the versatile applications of gas-transfer membranes in water and wastewater treatment, categorizing them into three primary types according to the function of membranes: water vapor transferring, gaseous reactant supplying, and gaseous compound extraction. For each type, the principles, evolution, and potential for further development were elaborated. Moreover, this review highlights the potential knowledge transfer between different fields, as insights from one type of gas-transfer membrane could potentially benefit another. Despite their technical innovations, these processes still face challenges in practical operation, such as membrane fouling and wetting. We advocate for research focusing on more practical and sustainable membranes and careful consideration of these emerging membrane technologies in specific scenarios. The current practicality and maturity of these emerging processes in water and wastewater treatment are described by the Technology Readiness Level (TRL) framework. Particularly, ongoing fundamental progress in membranes and engineering is expected to continue fueling the future development of these technologies.
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Affiliation(s)
- Danting Shi
- Department of Civil and Environmental
Engineering, The Hong Kong Polytechnic University, Hong Kong 999077, PR China
| | - Tao Liu
- Department of Civil and Environmental
Engineering, The Hong Kong Polytechnic University, Hong Kong 999077, PR China
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Liu Y, Xiao M, Huang X, Park J, Hoffman ME, Feng Y, An AK, Li Q, Hoek EMV, Jassby D. Mitigating CaCO 3 crystal nucleation and growth through continuous ion displacement via alternating electric fields. Nat Commun 2025; 16:35. [PMID: 39746967 PMCID: PMC11697440 DOI: 10.1038/s41467-024-55176-z] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Key Words] [Grants] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 06/13/2024] [Accepted: 12/04/2024] [Indexed: 01/04/2025] Open
Abstract
Mineral crystal formation poses a challenge on surfaces (e.g., heat exchangers, pipes, membranes, etc.) in contact with super-saturated fluids. Applying alternating currents (AC) to such surfaces can prevent surface crystallization under certain conditions. Here, we demonstrate that ion displacement induced by periodic charging and discharging of the electrical double layer (EDL) inhibits both heterogeneous and homogeneous nucleation (and crystal growth) of CaCO3. Titanium sheets (meant to simulate metallic heat exchanger surfaces) are immersed in super-saturated CaCO3 solutions with a saturation index >11. We show that at relatively high AC frequencies, incomplete EDL formation leads to an alternating electric field that propagates far into the bulk solution, inducing rapid ion migration that overwhelms the Brownian motion of ions. Electrochemical characterization reveals EDL charging/discharging under AC conditions that greatly inhibits precipitation. Operating at 4 Vpp, 0.1-10 Hz reduces turbidity by over 96% and reduces CaCO3 coverage on the metal plates by over 92%. Based on electrokinetic and crystallization models, the ion displacement velocity (exceeding the mean Brownian velocity) and displacement length disrupts ion collision and crystal nucleation. Overall, the technique has potential for preventing mineral crystal formation in heat exchangers and many other industrially relevant systems.
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Affiliation(s)
- Yiming Liu
- Department of Civil & Environmental Engineering, University of California Los Angeles (UCLA), Los Angeles, CA, USA
- National Science Foundation (NSF) Nanosystems Engineering Research Center for Nanotechnology-Enabled Water Treatment, Rice University, Houston, TX, USA
- Department of Civil & Environmental Engineering, Rice University, Houston, TX, USA
| | - Minhao Xiao
- Department of Civil & Environmental Engineering, University of California Los Angeles (UCLA), Los Angeles, CA, USA
| | - Xiaochuan Huang
- National Science Foundation (NSF) Nanosystems Engineering Research Center for Nanotechnology-Enabled Water Treatment, Rice University, Houston, TX, USA
- Department of Civil & Environmental Engineering, Rice University, Houston, TX, USA
| | - Jane Park
- Department of Chemical & Biomolecular Engineering, UCLA, Los Angeles, CA, USA
| | - Matthew E Hoffman
- Department of Civil & Environmental Engineering, University of California Los Angeles (UCLA), Los Angeles, CA, USA
| | - Yuren Feng
- National Science Foundation (NSF) Nanosystems Engineering Research Center for Nanotechnology-Enabled Water Treatment, Rice University, Houston, TX, USA
- Department of Civil & Environmental Engineering, Rice University, Houston, TX, USA
| | - Alicia Kyoungjin An
- Department of Chemical & Biological Engineering, The Hong Kong University of Science and Technology, Hong Kong SAR, China
| | - Qilin Li
- National Science Foundation (NSF) Nanosystems Engineering Research Center for Nanotechnology-Enabled Water Treatment, Rice University, Houston, TX, USA
- Department of Civil & Environmental Engineering, Rice University, Houston, TX, USA
- Department of Chemical & Biomolecular Engineering, Rice University, Houston, TX, USA
- Department of Materials Science & NanoEngineering, Rice University, Houston, TX, USA
| | - Eric M V Hoek
- Department of Civil & Environmental Engineering, University of California Los Angeles (UCLA), Los Angeles, CA, USA.
- California NanoSystems Institute, UCLA, Los Angeles, CA, USA.
- Institute of the Environment & Sustainability, UCLA, Los Angeles, CA, USA.
- Energy Storage & Distributed Resources Division, Lawrence Berkeley National Laboratory, Berkeley, CA, USA.
| | - David Jassby
- Department of Civil & Environmental Engineering, University of California Los Angeles (UCLA), Los Angeles, CA, USA.
- California NanoSystems Institute, UCLA, Los Angeles, CA, USA.
- Institute of the Environment & Sustainability, UCLA, Los Angeles, CA, USA.
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Lu S, McGaughey A, Im S, Liu Y, Wang X, Leininger A, Jassby D, Hoek E, Ren ZJ. Membrane electrolysis distillation for volatile fatty acids extraction from pH-neutral fermented wastewater. WATER RESEARCH 2024; 265:122306. [PMID: 39182349 DOI: 10.1016/j.watres.2024.122306] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 06/09/2024] [Revised: 08/14/2024] [Accepted: 08/19/2024] [Indexed: 08/27/2024]
Abstract
Volatile fatty acids (VFAs) serve as building blocks for a wide range of chemicals, but it is difficult to extract VFAs from pH-neutral wastewater using evaporation methods because of the ionized form. This study presents a new membrane electrolysis distillation (MED) process that extracts VFAs from such fermentation solutions. MED uniquely integrates pH regulation and joule heating to facilitate the efficient evaporation of VFAs. This integration occurs alongside a hydrophobic membrane that ensures effective gas-liquid phase separation. Operating solely on electricity, MED achieved an acid flux rate of 12.03 g/m2/h at 6V. In contrast, the control results without the joule heating or pH swing only obtained a 0.23 g/m2/h and 0.32 g/m2/h flux, respectively. In addition, a physicochemical model was developed to assess the impacts of temperature on membrane surface pH. This system enhances resource recovery from waste streams and helps achieve a circular carbon economy.
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Affiliation(s)
- Sidan Lu
- Department of Civil and Environmental Engineering and Andlinger Center for Energy and the Environment, Princeton University, Princeton, NJ 08544, United States
| | - Allyson McGaughey
- Department of Civil and Environmental Engineering and Andlinger Center for Energy and the Environment, Princeton University, Princeton, NJ 08544, United States
| | - Sungju Im
- Department of Civil and Environmental Engineering, University of California, Los Angeles, CA 90095, United States
| | - Yiming Liu
- Department of Civil and Environmental Engineering, University of California, Los Angeles, CA 90095, United States
| | - Xinyi Wang
- Department of Civil and Environmental Engineering, University of California, Los Angeles, CA 90095, United States
| | - Aaron Leininger
- Department of Civil and Environmental Engineering and Andlinger Center for Energy and the Environment, Princeton University, Princeton, NJ 08544, United States
| | - David Jassby
- Department of Civil and Environmental Engineering, University of California, Los Angeles, CA 90095, United States
| | - Eric Hoek
- Department of Civil and Environmental Engineering, University of California, Los Angeles, CA 90095, United States
| | - Zhiyong Jason Ren
- Department of Civil and Environmental Engineering and Andlinger Center for Energy and the Environment, Princeton University, Princeton, NJ 08544, United States.
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Liu Z, Lu X, Wu C, Gu J, Wu Q. Exploiting the potential of a novel "in-situ latent heat recovery" in hollow-fiber vacuum membrane distillation process for simultaneously improved water production and energy efficiency. WATER RESEARCH 2024; 256:121586. [PMID: 38631240 DOI: 10.1016/j.watres.2024.121586] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 12/12/2023] [Revised: 03/26/2024] [Accepted: 04/07/2024] [Indexed: 04/19/2024]
Abstract
Thermal driven membrane distillation (MD) technology is a promising method for purifying & recovering various salty (especially high salty) or contaminated wastewaters with low-grade heat sources. However, the drawbacks of "high energy consumption" and "high cooling water consumption" pose special challenges for the future development of this technology. In this article, we report an innovative strategy called "in-situ heat transfer", which is based on the jacketed structure composed of hollow fiber membranes and capillary heat exchange tubes, to simplify the migration steps of condensation latent heat in MD heat recovery process. The results indicate that the novel heat recovery strategy exhibits higher growth rates both in the flux and gained output ratio (47.4 % and 173.1 %, respectively), and further reduces the system's dependence on cooling water. In sum, under the control of the "in-situ heat transfer" mechanism, the functional coupling of "vapor condensation (exothermic)" and "feed evaporation (endothermic)" in limited-domain space is an attractive alternative solution, because it eliminates the disadvantages of the imbalance between heat supply and demand in traditional heat recovery methods. Our research may facilitate the development of MD heat recovery modules for industrial applications, which will help to further achieve the goal of energy saving and emission reduction.
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Affiliation(s)
- Ziqiang Liu
- State Key Laboratory of Separation Membranes and Membrane Processes, School of Material Science and Engineering, Tiangong University, Tianjin 300387, PR China
| | - Xiaolong Lu
- State Key Laboratory of Separation Membranes and Membrane Processes, School of Material Science and Engineering, Tiangong University, Tianjin 300387, PR China; State Key Laboratory of Membrane Materials and Membrane Applications, Tianjin Motimo Membrane Technology Co., Ltd., Tianjin 300457, PR China.
| | - Chunrui Wu
- State Key Laboratory of Separation Membranes and Membrane Processes, School of Material Science and Engineering, Tiangong University, Tianjin 300387, PR China
| | - Jie Gu
- State Key Laboratory of Separation Membranes and Membrane Processes, School of Material Science and Engineering, Tiangong University, Tianjin 300387, PR China
| | - Qiang Wu
- State Key Laboratory of Separation Membranes and Membrane Processes, School of Material Science and Engineering, Tiangong University, Tianjin 300387, PR China
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