Jeong F. Kim
Current Organizations / Institutes
The organizations/institutes from the scholar's latest article
Previous Organizations / Institutes
The organizations / institutes from the scholar's other articles in the past ten years
Research Subjects
Jeong F. Kim has a total of 136 co-authors. Here are the top co-authors by number of shared publications:
Seung Hwan Kim
8 shared publicationsBao Tran Duy Nguyen
6 shared publications- Bao Tran Duy Nguyen
Department of Energy and Chemical Engineering, Incheon National University, Incheon 22012, Korea
6 shared publications Jieun Kang
6 shared publications- Young Hoon Cho
Separation and Purification Research Center, Chemical & Process Technology Division, Korea Research Institute of Chemical Technology, 141 Gajeong-ro, Yuseong-gu, Daejeon 34114, Republic of Korea
5 shared publications - Jung-Hyun Lee
Korea University
4 shared publications
Latest Publications
- 27 October 2026
- Published by Elsevier in Journal of Membrane Science
- Vol. 762
Thin-film composite membranes on bioderived and biodegradable Hanji–cellulose supports for organic solvent nanofiltration
- 27 October 2026
- Published by Elsevier in Journal of Membrane Science
- Vol. 762
Thin-film composite membranes on bioderived and biodegradable Hanji–cellulose supports for organic solvent nanofiltration
- 5 January 2026
- Published by Wiley in ChemSusChem
- Vol. 19 (1) , e202502180
Energy‐Efficient Chemical Recycling of Polyethylene Terephthalate via Water‐Free Glycolysis Process Using Membrane Technology
Conventional chemical recycling of polyethylene terephthalate (PET) via glycolysis is hindered by the high energy cost of separating water and ethylene glycol (EG) via distillation. In this work, the energy‐intensive EG‐water separation step was excluded by implementing a water‐free, membrane‐based process for the production and purification of bis(2‐hydroxyethyl) terephthalate (BHET) from PET glycolysis. The proposed approach is built upon three key innovations: (1) a micro‐sized MgO/SiO 2 heterogeneous catalyst that enhances PET depolymerization efficiency, achieving a 95.1% BHET yield, (2) a water‐free glycolysis process that reduces process complexity, and (3) an organic solvent nanofiltration‐based purification and concentration strategy that selectively separates BHET while minimizing energy‐intensive phase‐change operations. A high overall BHET yield of 93.2% was achieved, enabled by a two‐stage cascade concentration with over 99% yield. Compared to conventional distillation, the proposed process reduces energy consumption by 86%. Techno‐economic analysis revealed a return on investment of 2.48 years for a production capacity of 1000 tons of BHET per day, highlighting its economic viability. By minimizing reliance on phase‐change operations, this process presents a scalable and transformative solution for sustainable chemical recycling, serving as an important stepping stone to transform PET glycolysis from a batch to a continuous process.
- 5 January 2026
- Published by Wiley in ChemSusChem
- Vol. 19 (1) , e202502180
Energy‐Efficient Chemical Recycling of Polyethylene Terephthalate via Water‐Free Glycolysis Process Using Membrane Technology
Conventional chemical recycling of polyethylene terephthalate (PET) via glycolysis is hindered by the high energy cost of separating water and ethylene glycol (EG) via distillation. In this work, the energy‐intensive EG‐water separation step was excluded by implementing a water‐free, membrane‐based process for the production and purification of bis(2‐hydroxyethyl) terephthalate (BHET) from PET glycolysis. The proposed approach is built upon three key innovations: (1) a micro‐sized MgO/SiO 2 heterogeneous catalyst that enhances PET depolymerization efficiency, achieving a 95.1% BHET yield, (2) a water‐free glycolysis process that reduces process complexity, and (3) an organic solvent nanofiltration‐based purification and concentration strategy that selectively separates BHET while minimizing energy‐intensive phase‐change operations. A high overall BHET yield of 93.2% was achieved, enabled by a two‐stage cascade concentration with over 99% yield. Compared to conventional distillation, the proposed process reduces energy consumption by 86%. Techno‐economic analysis revealed a return on investment of 2.48 years for a production capacity of 1000 tons of BHET per day, highlighting its economic viability. By minimizing reliance on phase‐change operations, this process presents a scalable and transformative solution for sustainable chemical recycling, serving as an important stepping stone to transform PET glycolysis from a batch to a continuous process.
- 25 October 2025
- Published by Elsevier in Journal of Membrane Science
- Vol. 738
Blood oxygenation artificial lung membranes – three incremental modification strategies to improve hemocompatibility
- 25 October 2025
- Published by Elsevier in Journal of Membrane Science
- Vol. 738
Blood oxygenation artificial lung membranes – three incremental modification strategies to improve hemocompatibility
- 23 June 2025
- Published by Springer Nature in Nature Sustainability
- Vol. 8 (6) , 594-605
Advancing membrane technology in organic liquids towards a sustainable future
- 23 June 2025
- Published by Springer Nature in Nature Sustainability
- Vol. 8 (6) , 594-605
Advancing membrane technology in organic liquids towards a sustainable future
- 1 June 2025
- Published by The Membrane Society of Korea in Membrane Journal
- Vol. 35 (2) , 103-115
Entrainer Assisted Membrane Separation (EMS) Strategy to Overcome the Size Azeotrope
- 1 June 2025
- Published by The Membrane Society of Korea in Membrane Journal
- Vol. 35 (2) , 103-115
Entrainer Assisted Membrane Separation (EMS) Strategy to Overcome the Size Azeotrope
- 21 April 2025
- Published by American Chemical Society (ACS) in ACS Sustainable Chemistry & Engineering
- Vol. 13 (17) , 6044-6050
Entrainer-Assisted Membrane Separation (EMS) Strategy for Circumventing Size-Azeotropes: Li/Na Separation
- 21 April 2025
- Published by American Chemical Society (ACS) in ACS Sustainable Chemistry & Engineering
- Vol. 13 (17) , 6044-6050
Entrainer-Assisted Membrane Separation (EMS) Strategy for Circumventing Size-Azeotropes: Li/Na Separation
- 27 November 2024
- Published by Springer Nature in Cellulose
- Vol. 32 (1) , 467-481
Physicochemical investigation of cellulose microbeads produced through cross-flow membrane emulsification for cosmetic applications
- 27 November 2024
- Published by Springer Nature in Cellulose
- Vol. 32 (1) , 467-481
Physicochemical investigation of cellulose microbeads produced through cross-flow membrane emulsification for cosmetic applications
- 14 November 2024
- Published by American Chemical Society (ACS) in ACS Nano
- Vol. 18 (47) , 32694-32704
Interfacially Assembled Anion Exchange Membranes for Water Electrolysis
High-performance and durable anion exchange membranes (AEMs) are critical for realizing economical green hydrogen production through alkaline water electrolysis (AWE) or AEM water electrosysis (AEMWE). However, existing AEMs require sophisticated fabrication protocols and exhibit unsatisfactory electrochemical performance and long-term durability. Here we report an AEM fabricated via a one-pot, in situ interfacial Menshutkin reaction, which assembles a highly cross-linked polymer containing high-density quaternary ammoniums and nanovoids inside a reinforcing porous support. This structure endows the membrane with high anion-conducting ability, water uptake (but low swelling), and mechanical and thermochemical robustness. Consequently, the assembled membrane achieves excellent AWE (0.97 A cm-2 at 1.8 V) and AEMWE (5.23 A cm-2 at 1.8 V) performance at 5 wt % KOH and 80 °C, significantly exceeding that of commercial and previously developed membranes, and excellent long-term durability. Our approach provides an effective method for fabricating AEMs for various energy and environmental applications.
- 14 November 2024
- Published by American Chemical Society (ACS) in ACS Nano
- Vol. 18 (47) , 32694-32704
Interfacially Assembled Anion Exchange Membranes for Water Electrolysis
High-performance and durable anion exchange membranes (AEMs) are critical for realizing economical green hydrogen production through alkaline water electrolysis (AWE) or AEM water electrosysis (AEMWE). However, existing AEMs require sophisticated fabrication protocols and exhibit unsatisfactory electrochemical performance and long-term durability. Here we report an AEM fabricated via a one-pot, in situ interfacial Menshutkin reaction, which assembles a highly cross-linked polymer containing high-density quaternary ammoniums and nanovoids inside a reinforcing porous support. This structure endows the membrane with high anion-conducting ability, water uptake (but low swelling), and mechanical and thermochemical robustness. Consequently, the assembled membrane achieves excellent AWE (0.97 A cm-2 at 1.8 V) and AEMWE (5.23 A cm-2 at 1.8 V) performance at 5 wt % KOH and 80 °C, significantly exceeding that of commercial and previously developed membranes, and excellent long-term durability. Our approach provides an effective method for fabricating AEMs for various energy and environmental applications.
- 22 October 2024
- Published by Elsevier in Journal of Membrane Science
- Vol. 715
Scalable membrane-assisted ion exchange (MEM-IE) strategy for organic acid purification in biorefinery process
- 22 October 2024
- Published by Elsevier in Journal of Membrane Science
- Vol. 715
Scalable membrane-assisted ion exchange (MEM-IE) strategy for organic acid purification in biorefinery process