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

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5. Place the cathode side GDL into the cathode graphite layer.<br />

6. Cover the cathode GDL with 1mm thick silicon gasket.<br />

7. Submerge the MEA into <strong>water</strong> and wait until the expansion of membrane stops<br />

8. Insert the wet MEA on cathode GDL.<br />

9. Place the anode side GDL on the anode side of the bipolar plate.<br />

10. Cover the anode GDL with 1mm thick silicon gasket.<br />

11. Place the bipolar plate with its mounted components on MEA.<br />

12. Place the cathode GDL into the cathode side of the bipolar plate.<br />

13. Go to step 6 (repeat this step equal to the “number of <strong>cells</strong> -1” in the stack)<br />

14. Place the <strong>water</strong> inlet, <strong>hydrogen</strong> and oxygen outlet graphite plate.<br />

15. Place the copper plate on anode graphite.<br />

16. Place a silicon layer on copper plate.<br />

17. Fixate the anode side end plate.<br />

18. Insert the cap screws to the bolts and tighten them diagonally.<br />

19. Stick the thermocouple probe on to graphite.<br />

Multiple cell electrolyzers have smaller heat transfer area per active electrolysis<br />

area with respect to single cell ones. Thus, the stack electrolyzers tend to get hotter than<br />

single cell ones; especially at a low <strong>water</strong> flow and a high current density. Hot electrolysis<br />

surfaces usually damage the membrane thus it should be avoided. To control the <strong>water</strong> inlet<br />

temperature, <strong>water</strong> reservoir was placed in a constant temperature <strong>water</strong> bath.<br />

Non-uniform <strong>water</strong> distribution, contact pressure differences between <strong>cells</strong>, clogged<br />

passage ways may cause voltage and temperature gradient between <strong>cells</strong> or even the<br />

melting of the membrane. So, the aim was to operate all the <strong>cells</strong> of the stack at the same<br />

current, voltage and temperature. This requires proper <strong>water</strong> distribution and gas collecting<br />

through all the <strong>cells</strong> of the stack. Applied current and <strong>water</strong> feed were kept the same as the<br />

previous experimental sets but the occurred electrical potential or temperature of the <strong>cells</strong><br />

due to less heat transfer area were different. Deionized <strong>water</strong> was fed to the <strong>water</strong> inlet via<br />

peristaltic pump until the <strong>water</strong> flooded <strong>from</strong> the oxygen output. The oxygen output was<br />

connected to the inlet <strong>water</strong> reservoir to return the unreacted <strong>water</strong>. Hydrogen output line<br />

39

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