Low Cost Bipolar Plates for Large Scale PEM Electrolyzers
Authors: Gago Aldo Saul , Ansar Asif Syed , Gazdzicki Pawel , Wagner Norbert , Arnold Johannes , Friedrich Kaspar Andreas 
Published: February 2020

Hydrogen can be used as an energy carrier when produced from renewable energies such as solar or wind by using proton exchange membrane water electrolysis (PEMWE) systems. Key components of PEMWE that determine largely the stack cost are the bipolar plates (BPP) [1, 2]. The high cost of the BBPs is due to the following:

The use of titanium as base material.

Machining process of flow fields on titanium which is complicated and costly [3].

The need of coatings on titanium for reducing anodization [4, 5]. The oxide layer that is formed on the surface of the metal under high potentials in acid medium increases the ohmic resistance, limiting the durability of the stack.

A more suitable material for bipolar plates would be stainless steel, which is cheaper and easier to machine than titanium. However, it corrodes dramatically when used in PEMWE. Moreover, the ions released from the corrosion process poison the catalysts coated membrane (CCM) of the electrolyzer. Consequently, stainless steel has to be protected with a coating that is corrosion resistant in acid environment and conductive at the same time.

In this sense, a titanium coating for stainless steel BPP of PEMWE has been developed by vacuum plasma spraying (VPS) [6]. Subsequently, the coating was physically and electrochemically characterized. The minimum thickness achieved was 13.5 µm. After surface modification the coating has an interfacial contact resistance (ICR) of less than 10 mΩ cm2 at 140 N cm-2, see Figure 1a, which meets the DOE 2015 target for BPP of PEM fuel cells. Corrosion measurements were performed in simulated environment of PEMWE. Figure 1b presents the potentiodynamic polarization curves of the uncoated and coated stainless steel substrate (ss) with titanium (Ti/ss). The electrochemical characteristic of Ti/ss was measured after a constant polarisation at 2 V vs. RHE for 24 h. Neither corrosion of the ss substrate, nor oxygen evolution on the sample was observed. Furthermore, the current transients were highly dependent on the surface finishing of the coating, although the protection offered to the substrate remained. XPS measurements showed that the oxidation of the coating occurs as a result of the anodization process in acid medium and not during thermal spray deposition. Given the superior characteristics of the coating, it might have a large impact on the cost of PEMWE systems for large scale electricity storage from renewables.

References

[1] Emile Tabu Ojong, Eric Mayousse, Tom Smolinka, Nicolas Guillet. Fraunhofer ISE. TECHNOPORT RERC 2012 Trondheim, April 16 - 18, 2012.

[2] K.E. Ayers, E.B. Anderson, C. Capuano, B. Carter, L. Dalton, G. Hanlon, J. Manco, M. Niedzwiecki, ECS Trans. 33 (2010) 3.

[3] H.G. Kim, L.K. Kwa, W. Han, in:, Int. Conf. Power Energy Syst. Lect. Notes Inf. Technol. Vol.13, 2012, pp. 373–379.

[4] J.-T. Wang, W.-W. Wang, C. Wang, Z.-Q. Mao, Int. J. Hydrogen Energy 37 (2012) 12069.

[5] H.-Y. Jung, S.-Y. Huang, B.N. Popov, J. Power Sources 195 (2010) 1950.

[6] A. S. Gago, S. A. Ansar, N. Wagner, J. Arnold, K.A. Friedrich, in:, 4th Eur. PEFC H2 Forum 2 - 5 July 2013, Lucerne Switz., 2013, pp. Chapter 06 – Session A07, 11–18.