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hydrogen production from water using solar cells powered nafion ...

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In fact, it was observed on the disassembled cell that there was not any hole or a<br />

tear occurred on the membrane, though the gas collection parts located at the top of the<br />

graphite was too big and the soft silicon sheet on the top of this part generated an<br />

imbalanced pressure on membrane that caused the membrane to stretch <strong>from</strong> anode to<br />

cathode which allowed the gas mixing.<br />

It was decided to remove the gas/liquid exit openings beside the empty field to<br />

support the gasket all along the surrounding line of the active electrolysis area. To do that,<br />

gas removal and <strong>water</strong> feed line passages were drilled crosswise <strong>from</strong> behind the GDL. The<br />

graphite plate shown in Figure 4.4 was used in the seventh design.<br />

Figure 4.4. Empty Flow field with crosswise ducts<br />

Silicon gaskets were used again while the compression of the cell was provided by<br />

plastic covered metal bolts with compression plates as used in the sixth design. In the first<br />

step, the cell was tested up to 250mAmp/cm 2 . The potential difference was found to be<br />

1.80V at 200mAmp/cm 2 and also mass balance made on the cell was closed within 3%<br />

error. The heat dissipation was very low due to low electrolysis overvoltage. Then, based<br />

on the encouraging results, the cell was tested with current densities up to 500mAmp/cm 2 .<br />

The voltage-current characteristic was almost a linear line and the voltage of the cell was<br />

measured as 2.20V at 500mAmp/cm 2 .<br />

47

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