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8Amp, respectively. The calculated and measured results are given in Figure 4.11(a) for<br />

oxygen flow and Figure 4.11(b) for <strong>hydrogen</strong> flow.<br />

Oxygen Production (ml/min)<br />

35<br />

30<br />

25<br />

20<br />

15<br />

10<br />

5<br />

0<br />

a b<br />

Figure 4.11. Calculated and Measured Oxygen and Hydrogen Flows<br />

Averages of the measured gas output were within 1% range of the calculated values<br />

although oxygen output readings fluctuated within 10% range of flow. This might be due to<br />

that the excess <strong>water</strong> and oxygen competed each other to escape <strong>from</strong> the cell and also<br />

oxygen gas bubbled through the upper part of the <strong>water</strong> reservoir was coming out; resulting<br />

in difficulties in flow measurements with the soap flow meter.<br />

The single cell operated at 500mAmp/cm 2 shows that the cell can generate<br />

<strong>hydrogen</strong> at 67.9% to 75.2% efficiency. The reason of the change in the efficiency is due to<br />

the temperature and non-optimized design of the current cell, though the results seem to be<br />

promising as compared to previously constructed alkaline electrolyzer which operated in<br />

previous studies at about 3.5V per cell in our institute (Atagündüz, 1993). However, the<br />

major drawback of the current design proposed in this thesis is the operating temperature<br />

limitation of the materials used to assemble the cell, such as melting of gasket. This<br />

problem prevented the cell <strong>from</strong> being used at high efficiency levels; i.e. at high<br />

temperatures.<br />

2 4 6 8 10 12<br />

Experiment Number<br />

Calculated O 2 at 2Amp<br />

Measured O 2 at 2Amp<br />

Calculated O 2 at 8Amp<br />

Measured O 2 at 8Amp<br />

Moreover, to increase the cell efficiency, thinner proton exchange membranes can<br />

be used instead of <strong>using</strong> N-117 which is 150µm in thickness because voltage drop on<br />

membrane was proportional with its thickness. Though thinner membranes such as N-112<br />

(50µm) have higher <strong>hydrogen</strong> back diffusion rates. Especially at low current densities,<br />

Hydrogen Production (ml/min)<br />

70<br />

60<br />

50<br />

40<br />

30<br />

20<br />

10<br />

0<br />

2 4 6 8 10 12<br />

Experiment Number<br />

Calculated H 2 at 2Amp<br />

Measured H 2 at 2Amp<br />

Calculated H 2 at 8Amp<br />

Measured H 2 at 8Amp<br />

55

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