An alkaline direct borohydride fuel cell with hydrogen peroxide as oxidant

https://doi.org/10.1016/j.jpowsour.2004.08.059Get rights and content

Abstract

A novel alkaline direct borohydride fuel cell (ADBFC) using varying concentrations of hydrogen peroxide as oxidant and sodium borohydride with sodium hydroxide, each of differing concentration, as fuel is reported. A peak power density of ca. 150 mW cm−2 at a cell voltage of 540 mV can be achieved from the optimized ADBFC operating at 70 °C.

Introduction

Proton exchange membrane fuel cells (PEFCs) are subject to problems of carbon monoxide poisoning of anode [1], [2], [3] when using a reformer, and hydrogen storage when using a direct fuel. Therefore, alternative hydrogen-carrying liquid fuels, such as methanol, have attracted attention for fuelling PEFCs directly with methanol [4], [5], [6]. Such cells are referred to as direct methanol fuel cells (DMFCs). This use of methanol highly simplifies the engineering problems at the front end of the fuel cell and hence reduces system complexity and lowers cost [7]. Nevertheless, DMFCs have limitations of low open-circuit potential, low electrochemical activity, and methanol cross-over [8].

Attempts are being made to overcome the above limitations by using other hydrogen-carrying liquid fuels such as borohydrides [9], [10], [11], [12], [13], [14], [15], [16], e.g., sodium borohydride it at has a capacity of 5.67 Ah g−1 and a hydrogen content of about 11 wt.%. Amendola et al. [12], [13] were the first to report an OH-ion conducting anion exchange membrane-based borohydride–air fuel cell, which had a power density close to 60 mW cm−2 at 70 °C. It was found that the cell suffered from borohydride cross-over as BH4-ions could pass through the anion-exchange membrane. In additions, it is mandatory to scrub carbon dioxide from the air inlet of such a fuel cell to avoid carbonate fouling. In order to mitigate borohydride cross-over, Suda [15] and Li et al. [16], [17] adopted a fuel-cell structure with a Nafion membrane as the electrolyte in order to separate the fuel from the cathode. But even in the borohydride-air cell reported by Suda [15], it would be compulsory to scrub carbon dioxide, not only to avoid carbonate fouling but also to prevent accumulation of alkali in the cathode pores so as to facilitate oxidant flux [15].

This communication describes an alkaline direct borohydride fuel cell (ADBFC) that uses hydrogen peroxide as oxidant to prevent carbonate fouling of the cathode. The use of hydrogen peroxide as oxidant in fuel cells also extends their operation to locations with limited air convection, e.g., underwater applications.

Section snippets

Preparation of AB5 and AB2 alloys

Various AB5 and AB2 alloys were prepared by arc-melting stoichiometric amounts of the constituent metals in a water-cooled copper crucible under argon atmosphere [18], [19], [20], [21], [22], [23]. The alloy ingots were mechanically pulverized to fine powders. The various AB5 alloys employed in this study were MmNi4.5Al0.5, MmNi3.2Al0.2Mn0.6Co1.0, MmNi3.55Al0.3Mn0.4Co0.75, and MmNi3.2Al0.2Mn0.6B0.03Co1.0, where Mm (Misch metal) comprises La-30 wt.%, Ce-50 wt.%, Nd-15 wt.%, Pr-5 wt.%. The AB2 alloy

Results and discussion

Powder X-ray diffraction patterns of various AB5 and AB2-group alloys employed in this study are shown in Fig. 2(a)–(e) [19], [20], [21], [22], [23]. The XRD patterns for AB5-group alloys (Fig. 2(a)–(d)) were indexed in a hexagonal space group: P6/mmm. The structural details and lattice parameters for these alloys are given in Table 1. The powder XRD pattern (Fig. 2(e)) for the AB2-group alloy of composition Zr0.9Ti0.1V0.2Mn0.6Cr0.05Co0.05Ni1.2 suggests that it crystallizes in C-15 cubic Laves

Conclusions

The study demonstrates that it is possible to assemble and operate an alkaline direct borohydride fuel cell with hydrogen peroxide as oxidant with a maximum power density of about 150 mW cm−2 while operating at 70 °C. The cell performance depends highly on the concentration of hydrogen peroxide since the power density may change by as high a value as 25 mW cm−2 with peroxide concentration. It is found that 4.45 M H2O2 is optimum for the ADBFCs reported here.

Acknowledgments

Financial assistance from the Council of Scientific and Industrial Research, New Delhi is gratefully acknowledged. We thank Dr. R.A. Mashelkar, FRS for his keen interest and encouragement.

References (31)

  • R.A. Lemons

    J. Power Sources

    (1990)
  • H. Igarashi et al.

    J. Electroanal. Chem.

    (1995)
  • J. Han et al.

    J. Power Sources

    (2002)
  • A.K. Shukla et al.

    Electrochim. Acta

    (2002)
  • A.K. Shukla et al.

    J. Electroanal. Chem.

    (2004)
  • S.C. Amendola et al.

    J. Power Sources

    (1999)
  • Z.P. Li et al.

    J. Power Sources

    (2004)
  • V.G. Kumar et al.

    J. Power Sources

    (1996)
  • S. Hikita et al.

    JSAE Rev.

    (2001)
  • S. Gottesfeld et al.

    J. Electrochem. Soc.

    (1988)
  • A.S. Aricò et al.

    Fuel Cells

    (2001)
  • A.K. Shukla et al.

    Bull. Mater. Sci.

    (2003)
  • M.E. Indig et al.

    J. Electrochem. Soc.

    (1962)
  • M. Jung, H.H. Kroeger, US Patent 3,511,710...
  • J.-Y. Lee, US Patent 5,599,640...
  • Cited by (0)

    View full text