Issue 4, 2014

Material requirements for membrane separators in a water-splitting photoelectrochemical cell

Abstract

A fully integrated model of a photoelectrochemical cell for water electrolysis is applied to the case of light-absorbing particles embedded in a membrane separator. Composition of the product gases is shown to be one critical measure of device performance. Not only must the composition be kept outside the explosive window for mixtures of H2 and O2, but also product purity is a concern. For the absorber-in-membrane geometry and the model assumptions used here, results show purely water-saturated H2 on the cathode side and water-saturated O2 on the anode side. Since it is possible to design devices that violate these assumptions, it should not be assumed that a polymer separator or an absorber-in-membrane geometry will be effective in preventing explosive mixtures in all cases. Net H2 collected, iH2,net, is the second essential performance metric, and it is shown to differ significantly from the more commonly reported total H2 produced and operating current density. Schemes which co-evolve H2 and O2 violate the first metric and do not provide the second. A composite of triple-junction silicon absorbers in a Nafion membrane is shown to have an optimum thickness of 30 μm, dependent on the properties of the light absorber. Varying membrane properties reveals a tradeoff between conductivity, κm, and gas permeabilities, ψH2 and ψO2, that can potentially be exploited differently than in a fuel cell. Modulating the relative humidity (RH) is insufficient. The maximum iH2,net is calculated to be 6.97 mA cm−2 at RH = 30% relative to a value of 6.92 mA cm−2 at RH = 100%. The model identifies target material properties for new polymers. If ψ is dropped one order of magnitude below that of Nafion (ψ/ψNafion = 0.1), the optimum value for iH2,net increases by 63.5%. For ψ/ψNafion = 0.01, the optimum iH2,net increases by 73.5%, which compares favorably to the 74.5% improvement that would result if Nafion were made impermeable (ψ/ψNafion = 0). Meanwhile, κm can drop to a value of 1.2 × 10−3 S cm−1 (two orders of magnitude below liquid-equilibrated Nafion) with less than a 5% decline in iH2,net.

Graphical abstract: Material requirements for membrane separators in a water-splitting photoelectrochemical cell

Article information

Article type
Paper
Submitted
21 Nov 2013
Accepted
11 Feb 2014
First published
11 Feb 2014

Energy Environ. Sci., 2014,7, 1468-1476

Material requirements for membrane separators in a water-splitting photoelectrochemical cell

A. Berger, R. A. Segalman and J. Newman, Energy Environ. Sci., 2014, 7, 1468 DOI: 10.1039/C3EE43807D

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