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ηelectrolyzer E × Q<br />

=<br />

Volt × Current<br />

(2.4)<br />

Where E is the calorific value of <strong>hydrogen</strong> (J/ml) and Q is the <strong>hydrogen</strong> flow rate (ml/s).<br />

The efficiency of an electrolyzer is found to decrease as the current density and<br />

corresponding H2 <strong>production</strong> rate of the cell increases. This means that the required<br />

electrical potential increases as the current density increases. This is due to the<br />

irreversibility occurring in the cell, which can be divided as the activation losses, ohmic<br />

losses, mass transport and concentration losses and increasing crossover of products<br />

through membrane in the high reaction rates and the operating pressures. (Onda et al.<br />

2003).<br />

Typical PEM electrolysis cell voltage is reported to be around 2V and the<br />

commercial electrolyzers have an efficiency ranging <strong>from</strong> 65% to 80% (Barbir 2004).<br />

Although an electrolyzer can be operated at higher efficiencies (up to 95%), this condition<br />

requires a lower cell voltage which also lowers the current passes through the electrolyte<br />

and the <strong>hydrogen</strong> <strong>production</strong> rate (Grigoriev et al. 2006). This dilemma could be overcome<br />

with the utilization of an electrolyzer stack with the high efficiency. Although 70% of the<br />

<strong>hydrogen</strong> <strong>production</strong> cost in PEM electrolyzers is due to the cost of electricity, increasing<br />

the efficiency was reported to compensate the relatively high capital expense of a PEM<br />

electrolyzer (Grigoriev et al. 2006). The analysis reported by Larminie and Dicks 2003<br />

shows that an electrolyzer needed to be optimized by considering the efficiency which in<br />

turn affected the unit <strong>production</strong> cost and also the utilization of electrolyzer which<br />

ultimately affected the initial investment of the device.<br />

Operating temperature of an electrolyzer is another important parameter on the<br />

system design. From electrolysis thermodynamic equations, it is expected that as the<br />

temperature increases the cell voltage should decrease. Yim and coworkers investigated the<br />

temperature effect on PEM electrolyzer with a 4.0 mg/cm 2 Pt loaded electrodes for both<br />

anode and cathode. It was found that voltage decreased <strong>from</strong> 1900mV to 1700mV as the<br />

temperature increased <strong>from</strong> 50 o C to 80 o C at 500mAmp/cm 2 current density (Yim et al.<br />

2004). However, it is known that lifetime of solid polymer electrolytes decreases and<br />

product crossover through membrane increases with the increasing temperature. Thus,<br />

16

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