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1<br />

285,830J/mol + H 2O(l)<br />

→ H 2(g)<br />

+ O2(g)<br />

2<br />

(2.1)<br />

However by applying the electricity <strong>water</strong> can be split into <strong>hydrogen</strong> and oxygen ions at<br />

lower temperatures, the dissociation of <strong>water</strong> requires the amount of electrical energy<br />

corresponding to ∆G of the <strong>water</strong> splitting reaction. The electrical potential proportional to<br />

reaction Gibbs free energy is required between the electrodes to initiate <strong>water</strong><br />

decomposition. This voltage is found <strong>from</strong> the definition of Gibbs free energy. In fact,<br />

theoretically it is the minimum electrolysis voltage (i.e. the ideal fuel cell voltage). The<br />

summation of the required electrical potential to compensate the Gibbs free energy and<br />

entropy at a temperature is called the thermoneutral (VTN) voltage at the standard<br />

temperature and pressure, it equals to;<br />

V<br />

t, p<br />

− ∆G<br />

=<br />

nF<br />

t, p<br />

T∆∆ − ∆H<br />

+ =<br />

nF nF<br />

t, p<br />

−(<br />

−285830<br />

)<br />

= = 1,481V<br />

2×<br />

96485<br />

(2.2)<br />

VTN is the voltage at which a perfectly insulated electrolyzer would operate. Thus, VTN is<br />

equal to the sum of higher heating value voltage corresponding to the energy required for<br />

the saturation of <strong>hydrogen</strong> and oxygen with <strong>water</strong> vapor (Oi and Sakaki 2004). The cell<br />

efficiency is found through <strong>using</strong> the thermoneutral voltage. In this case, VTN is divided by<br />

the actual voltage applied to the cell to obtain the efficiency of an electrolyzer (Oi and<br />

Sakaki 2004).<br />

η=<br />

V<br />

V<br />

TN<br />

ACT<br />

1.481<br />

=<br />

V<br />

ACT<br />

(2.3)<br />

Another way to find the efficiency of an electrolyzer is that the energy equivalent of<br />

<strong>hydrogen</strong> output is divided by the given energy as shown in the equation 2.4 below (Ahmad<br />

et al. 2006).<br />

15

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