MRS Meetings and Events

 

EN01.02.02 2022 MRS Fall Meeting

Quantifying Chlorine Gas Evolution from Mixed-Acid Vanadium Redox Flow Batteries

When and Where

Nov 29, 2022
9:00am - 9:15am

Hynes, Level 3, Room 301

Presenter

Co-Author(s)

Reed Wittman1,Cassandria Poirier1,Harry Pratt1,Travis Anderson1,Yuliya Preger1

Sandia National Laboratories1

Abstract

Reed Wittman1,Cassandria Poirier1,Harry Pratt1,Travis Anderson1,Yuliya Preger1

Sandia National Laboratories1
Mixed-Acid (MA) Vanadium Redox Flow Batteries (VRFB) improve on standard VRFBs’ energy density via the addition of hydrochloric acid (HCl) to the standard sulfuric acid (H<sub>2</sub>SO<sub>4</sub>) electrolyte. This improves the stability of the vanadium (V) in the solution, which allows for electrolytes with higher concentrations of V ions and increased operating temperatures. However, the addition of HCl to the system introduces a new safety risk, the evolution of chlorine gas (Cl<sub>2</sub>) from the catholyte.<br/> In this study, we cycled an MA VRFB under a range of conditions to understand the fundamental causes of gas evolution. We constructed a single cell MA VRFB using a standard electrolyte composition of 2M H<sub>2</sub>SO<sub>4</sub>, 5M HCl and 2M V, with a gas analyzer sampling the head space of the catholyte chamber. Cl<sub>2</sub> gas quantity was measured under systematically varied cycling rates and potential holds. The mechanism of gas evolution was determined to be an electrochemical side reaction that occurs when charging the cell beyond 1.5 volts. Depending on the duration the cell was held at high voltage and the maximum voltage, headspace Cl<sub>2</sub> concentrations between 1 and 4.2% were observed. Overcharging the cell beyond 1.7 volts (the standard VRFB upper limit) generated gas concentrations near 10%. These concentrations represent a significant safety risk that may occur during system operation and need to be mitigated.<br/> Previously it was assumed that the 360 millivolts potential difference between the V<sup>4+</sup>/V<sup>5+</sup> (1.00 volts vs SHE) charging reaction in the posolyte and the 2Cl<sup>-</sup>/Cl<sub>2</sub> (1.36 volts vs SHE) gas evolution reaction would prevent Cl<sub>2</sub> gas evolution through electrochemical means. We will discuss how solution chemistry and cell inefficiencies make Cl<sub>2</sub> generation a viable side reaction when charging a cell above 1.5 volts. This new understanding of gas evolution will aid development of safer MA VRFB systems that mitigate Cl<sub>2</sub> formation during operation.<br/> <br/> <br/>Sandia National Laboratories is a multi-mission laboratory managed and operated by National Technology & Engineering Solutions of Sandia, LLC, a wholly owned subsidiary of Honeywell International Inc., for the U.S. Department of Energy’s National Nuclear Security Administration under contract DE-NA0003525.

Symposium Organizers

James McKone, University of Pittsburgh
Qing Chen, Hong Kong University of Science and Technology
Yi-Chun Lu, Chinese University of Hong Kong
Wei Wang, Pacific Northwest National Laboratory

Symposium Support

Bronze
Gamry Instruments
Journal of Materials Chemistry A
Neware Technology LLC
Pacific Northwest National Laboratory

Publishing Alliance

MRS publishes with Springer Nature