11920 J. Phys. Chem. B, Vol. 105, No. 47, 2001
Barton et al.
at a linear velocity of 10 cm/s, the 0.24 cm cell would produce
3
1
.2 mW. It would generate in one week the amount of energy
stored in the highest energy density lithium battery of equal
volume. A cathode operating in a major blood vessel of an
animal would require a wired laccase electrode that would not
loose its activity when the pH is raised from 5 to 7 and when
-
Cl is present at its physiological concentration. A recent study
suggests that the activity of laccase from Pleurotus ostreatus
declines only moderately upon increasing the pH from 5 to 7.17
The observed optimal enzyme mass fraction was ∼40% for
both the carbon cloth and the vitreous carbon electrodes (Figure
5
). The constancy of the ratio suggests that the thicknesses of
the electroactive zones were similar for both structures, and that
the increased current density with the cloth derives solely from
an increase in active surface area when enzyme kinetics and
Figure 6. Dependence of the current density of the noncomposite
polished and catalyst coated) vitreous carbon electrodes on pH and
1
8
(
electron transport are not re-balanced.
on the chloride ion concentration. 0.62 V (NHE), 900 rpm. Conditions
as in Figure 3b.
The wired laccase cathode was reasonably stable even when
the electrode was continuously stressed by shearing at 0.1 N/m2
through rotation at 1000 rpm (Figure 7a). The major cause of
loss was the stripping of the electrocatalytic film, suggested by
the fact that not only the current density but also the voltam-
metric peaks declined (Figure 7b). If enzyme deactivation were
the dominant cause of loss, only the O2 electroreduction current,
2
+/3+
not the voltammetric peaks of Os
electrooxidation/reduc-
tion, would have declined. After 4.7 days of continuous oper-
ation, 66% of the O2 electroreduction current and 42% of the
2
+/3+
electroactive Os
centers were lost. This suggests that en-
dz ya ym s e. degradation caused only ∼24% of the current loss in 5
Conclusions
O2 was electroreduced to water at pH 5 on a rotating (1000
rpm) carbon-cloth composite “wired” laccase (45 wt % laccase,
2
4
9 wt % redox polymer) cathode at 5 mA/cm current density
at 0.62 V in O2-saturated pH 5 citrate buffer at 37 °C. In
stagnant, air-saturated, citrate buffer the current density was
2
∼
100 µA/cm . The half-life of the cathode was ∼3 days when
it was sheared at a stress comparable to that of fast-flowing
blood in a major blood vessel. The next necessary step toward
a fuel cell implanted in a major blood would be the extension
of the cathode’s operating pH from pH 5 to the physiological
pH 7.2-7.4 range and its operation in the presence of chloride
at its physiological concentration.
Figure 7. Operational stability of the “wired” laccase electrode. (a.)
Time-dependence of the current density of carbon-cloth composite and
of the vitreous carbon noncomposite electrodes poised at 0.62 V (NHE).
Acknowledgment. DARPA/ONR and The Welch Founda-
tion supported this work. The authors thank Jason Cole and
Keith A. Friedman for their advice and assistance.
(b.) The change in the cyclic voltammograms of the carbon cloth
composite electrode after 4.6 days of operation. Scan rate 50 mV/s.
The composition, loading and conditions were as in Figure 3b.
References and Notes
composite “wired” laccase cathode. At 0.8 V, a potential just
(1) Tarasevich, M. R.; Yaropolov, A. I.; Bogdanovskaya, V. A.;
Varfolomeev, S. D. Bioelectrochem. Bioenerg. 1979, 6, 393-403.
0.15 V below the standard pH 5 potential for the four-electron
(
2) Tarasevich, M. R.; Bogdanovskaya, V. A.; Gavrilova, E. F.; Orlov,
S. B. J. Electroanal. Chem. Interfacial Electrochem. 1986, 206, 217-227.
3) Yaropolov, A. I.; Kharybin, A. N.; Emneus, J.; MarkoVarga, G.;
Gorton, L. Bioelectrochem. Bioenerg. 1996, 40, 49-57.
4) Santucci, R.; Ferri, T.; Morpurgo, L.; Savini, I.; Avigliano, L.
reduction of O2 to water, the current density exceeds 1 mA/
2
2
cm (Figure 4). Higher current densities (of 1 A/cm ) have
previously been reached below 100 °C only at pH 0, and only
in cathodes based on platinum-group alloy catalysts. To illustrate
the power density that might be reached in a future biofuel cell
made with the cathode and with a glucose electrooxidizing anode
(
(
Biochem. J. 1998, 332, 611-615.
(5) Trudeau, F.; Daigle, F.; Leech, D. Anal. Chem. 1997, 69, 882-
886.
2
operating at > 2 mA/cm poised at 0.2 V, we consider a cell
(
6) Lee, C. W.; Gray, H. B.; Anson, F. C.; Malmstroem, B. G. J.
Electroanal. Chem. Interfacial Electrochem. 1984, 172, 289-300.
7) Palmore, G. T. R.; Kim, H.-H. J. Electroanal. Chem. 1999, 464,
10-117.
8) Thuesen, M. H.; Farver, O.; Reinhammar, B.; Ulstrup, J. Acta Chem.
Scand. 1998, 52, 555-562.
consisting of a 1 cm long, 0.4 cm diameter hollow tubular anode
and a similar cathode. If operation of the cathode would be
extended to pH 7, with no inhibition by chloride anions and
other blood constituents, then with arterial blood (8 mM
hemoglobin-bound O2, 5 mM glucose) flowing through the cell
(
1
(