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        <identifier>oai:figshare.com:article/32630073</identifier>
        <datestamp>2026-10-01T17:28:33Z</datestamp>
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          <dc:title>Super-ambient temperature gas phase photocatalysis</dc:title>
          <dc:creator>Michael Bingham (8957498)</dc:creator>
          <dc:subject>PUREID: 220698967</dc:subject>
          <dc:description>&lt;p&gt;This thesis is concerned with the use of a continuous flow
gas phase photocatalytic system to produce hydrogen as a cleaner fuel source.
M/TiO2 photocatalysts (where M is Pt, Pd, Au and Ag) was used in a continuous
flow gas phase photocatalytic system. Two main reactions were examined in
detail, the reaction of water and methanol to form carbon dioxide and hydrogen,
and the water gas shift reaction, i.e. the reaction of water and carbon
monoxide to form carbon dioxide and hydrogen. The catalysts were made via a wet
impregnation method, typically between 0.01 to 10 wt.%. &lt;/p&gt;

&lt;p&gt; &lt;/p&gt;

&lt;p&gt;It was observed for both these reactions that as the metal
loading increased so did the rate of reaction for hydrogen production. This
usually occurred until the metal loading reached a loading of around 0.2-0.5
wt.%, where after this loading, say &gt; 0.5 wt.% until around 1 or even 10
wt.%, the rate of reaction greatly plummets, until very little or no rate of
hydrogen production is observed. A theoretical rationale was applied and the
metal support interface (MSI) model was replaced with a new expanding
photocatalytic area overlap model (EPAO). This model gives a good fit to the
data reported in this thesis but also to the data reported in the literature. A
visual representation of this model is also provided and explored as a function
of metal and particle or ‘dot’ size. &lt;/p&gt;

&lt;p&gt; &lt;/p&gt;

&lt;p&gt;Further to this, selectivity in the methanol steam reforming
reaction was explored for various M/TiO2 photocatalysts showing differing
selectivity, either towards methanol oxidation to CO2 or methanol degradation
to CO. The water gas reaction was probed further as a function of temperature,
where Arrhenius kinetics are applied, and as a function of reactant
concentration, where Langmuir-Hinshelwood kinetics are observed.&lt;/p&gt;</dc:description>
          <dc:date>2026-10-01T17:28:33Z</dc:date>
          <dc:type>Text</dc:type>
          <dc:type>Thesis</dc:type>
          <dc:identifier>10.17034/32630073.v1</dc:identifier>
          <dc:relation>https://figshare.com/articles/thesis/Super-ambient_temperature_gas_phase_photocatalysis/32630073</dc:relation>
          <dc:rights>All Rights Reserved</dc:rights>
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