Art à France

Organisation/Company Laboratoire de Génie Chimique Research Field Engineering » Process engineering Researcher Profile Recognised Researcher (R2) Leading Researcher (R4) First Stage Researcher (R1) Established Researcher (R3) Country France Application Deadline 29 Jun 2025 - 22:00 (UTC) Type of Contract Temporary Job Status Full-time Offer Starting Date 1 Oct 2025 Is the job funded through the EU Research Framework Programme? Not funded by a EU programme Is the Job related to staff position within a Research Infrastructure? No

Context and State of the Art

Bipolar Membrane Electrodialysis (BMED) process uses bipolar membranes (BMs) in various types of stacks. These membranes have the capacity, under suitable conditions, to dissociate water into H+ protons and OH- hydroxyls. They therefore allow the pH of solutions to be modified (acidification, alkalization) without the use of chemical inputs (acids or bases). BMED is therefore a particularly advantageous technology in the context of reducing the environmental impact of processes. Implemented in 3-compartment stacks (AEM/BM/CEM), it allows the regeneration of saline solutions into acids and bases. The interest generated by this technology has resulted in 3 review articles published since 2021 (Pârnamâe et al., 2021; Chen et al., 2022; Zhou et al., 2025). They have highlighted the advances, certain limitations, ways for improvement and prospects for the use of BMED. For example, the achievable concentration levels remain limited. “Co-ion leakage” is commonly cited to explain this limitation. This is in reality a co-transfer and not a leak in the strict sense. It results in a deterioration in performance, in terms of yield and quality (purity) of the products obtained. The origin of this phenomenon is still insufficiently identified (migration, diffusion, localization at the level of MEI or MB, etc.), so it remains difficult to limit its impact. Previous work has shown that the water transfer that accompanies the transfer of ions can also limit the achievable concentration level (Bailly et al., 2000; Borges et al., 2008; Han et al., 2015). A recent review (Zhou et al., 2025) further highlights the need to improve knowledge of multi-ionic transfers in the case of the treatment of complex solutions, in order to allow a broader development of the BMED process.

Objectives of the project

The objective of this project is to study the transfer phenomena involved in 3-compartment BMED systems (AEM/BM/CEM), used to produce or regenerate acid and base solutions from complex saline solutions, containing several mineral ions and/or organic impurities. A better understanding of these phenomena will make it possible to identify levers of action (properties of IEM or BM membranes, operating parameters, pretreatment of saline solutions) in order to improve the performance of the process (achievable concentration levels, product purity, etc.). Modelling will also be used based on transfer variables to predict the composition of the processed flows. This work will benefit from the approaches developed in previous studies (Roux de Balmann et al., 2002; Borges et al., 2008; Galier et al., 2013; Han et al., 2017).

Research Methodology

A bibliographic update will be carried out at the start of the project (publications and patents). This will help guide further work on the identified limitations. A report will be written (state of the art, study implementation).

A study will then be conducted at the laboratory scale. Experiments will be conducted with synthetic solutions of different compositions while varying the operating parameters (current density, concentrations, compositions). The transfer quantities will be determined to identify the contribution of the various phenomena involved (ionic transfer and water transfer across the different membranes of the stack, dissociation reaction at the BM level, etc.). Their impact on the performance of the BMED will be characterized (faradic efficiency, product purity). A model will be searched to describe the evolution of BMED performances as a function of the operating parameters. This investigation will be carried out for various stacks, consisting of different IEMs and BMs.

Scaling up will then be addressed through pilot-scale experiments. The transfer quantities will be determined and compared to those previously determined at the laboratory scale. This will highlight the scalable quantities, i.e. independent of the system size, and any performance discrepancies with the laboratory scale. The representativeness of the model developed at the laboratory scale will be assessed. Depending on the observed differences, an adaptation of the model will be considered.

Partners: The Chemical Engineering Laboratory, team led by Professor Sylvain Galier and CNRS Research Director Hélène Roux-de Balmann, specializing in separations using ion exchange membranes. EURODIA: one of the world's leading specialists in electrodialysis, holder of numerous patents, and leader in its application in several industrial fields.

Funding category: Cifre



PHD title: Chemical engineering and environment

PHD Country: France

Master's degree or engineering degree in chemical engineering, process engineering, with research experience. Ability to synthesize, autonomy, rigor, and aptitude for teamwork. Writing skills, fluency in written and oral scientific English