<p>Developing efficient propane dehydrogenation (PDH) processes without uses of expensive Pt- and toxic CrO<sub><i>x</i></sub>-based catalysts are of broad interest and great importance. Co-feeding of hydrogen is a widely-adopted strategy to improve catalytic performance of various catalysts in the PDH reaction. Herein, we systematically study the promotion effect of co-fed H<sub>2</sub> on different oxide catalysts in the PDH reaction. It comes mainly from the alleviated poisoning effect on ZnO and additionally from H<sub>2</sub> reduction-enhanced coordination-unsaturated Zr<sup>3+</sup> active sites on ZrO<sub>2</sub>, while mainly from the formation of dynamically-cycles metastable gallium hydride species on Ga<sub>2</sub>O<sub>3</sub> capable of activating the C–H bond activation of propane at significantly reduced barriers <InlineEquation ID="IEq1"> <EquationSource Format="TEX">\(\left( {{{\rm{C}}_{{3}}}{{\rm{H}}_{{8}}} + 2{\rm{Ga(III}}{{\rm{)}}_{{\rm{G}}{{\rm{a}}_{\rm{2}}}{{\rm{O}}_{{3}}}}}{\rm{ - }}{{\rm{H}}^{\rm{*}}} = {{\rm{C}}_{\rm{3}}}{{\rm{H}}_{{6}}} + 2{{\rm{H}}_{{2}}} + 2{\rm{Ga(III}}{{\rm{)}}_{{\rm{G}}{{\rm{a}}_{{2}}}{{\rm{O}}_{{3}}}}}} \right)\)</EquationSource> <EquationSource Format="MATHML"><math display="block"> <mrow> <mo>(</mo> <mrow> <mrow> <msub> <mrow> <mrow> <mi mathvariant="normal">C</mi> </mrow> </mrow> <mrow> <mrow> <mn>3</mn> </mrow> </mrow> </msub> </mrow> <mrow> <msub> <mrow> <mrow> <mi mathvariant="normal">H</mi> </mrow> </mrow> <mrow> <mrow> <mn>8</mn> </mrow> </mrow> </msub> </mrow> <mo>+</mo> <mn>2</mn> <mrow> <mrow> <mi mathvariant="normal">G</mi> <mi mathvariant="normal">a</mi> <mo stretchy="false">(</mo> <mi mathvariant="normal">I</mi> <mi mathvariant="normal">I</mi> <mi mathvariant="normal">I</mi> </mrow> </mrow> <mrow> <msub> <mrow> <mrow> <mo stretchy="false">)</mo> </mrow> </mrow> <mrow> <mrow> <mrow> <mi mathvariant="normal">G</mi> </mrow> </mrow> <mrow> <msub> <mrow> <mrow> <mi mathvariant="normal">a</mi> </mrow> </mrow> <mrow> <mrow> <mn>2</mn> </mrow> </mrow> </msub> </mrow> <mrow> <msub> <mrow> <mrow> <mi mathvariant="normal">O</mi> </mrow> </mrow> <mrow> <mrow> <mn>3</mn> </mrow> </mrow> </msub> </mrow> </mrow> </msub> </mrow> <mrow> <mrow> <mo>−</mo> </mrow> </mrow> <mrow> <msup> <mrow> <mrow> <mi mathvariant="normal">H</mi> </mrow> </mrow> <mrow> <mrow> <mo>∗</mo> </mrow> </mrow> </msup> </mrow> <mo>=</mo> <mrow> <msub> <mrow> <mrow> <mi mathvariant="normal">C</mi> </mrow> </mrow> <mrow> <mrow> <mn>3</mn> </mrow> </mrow> </msub> </mrow> <mrow> <msub> <mrow> <mrow> <mi mathvariant="normal">H</mi> </mrow> </mrow> <mrow> <mrow> <mn>6</mn> </mrow> </mrow> </msub> </mrow> <mo>+</mo> <mn>2</mn> <mrow> <msub> <mrow> <mrow> <mi mathvariant="normal">H</mi> </mrow> </mrow> <mrow> <mrow> <mn>2</mn> </mrow> </mrow> </msub> </mrow> <mo>+</mo> <mn>2</mn> <mrow> <mrow> <mi mathvariant="normal">G</mi> <mi mathvariant="normal">a</mi> <mo stretchy="false">(</mo> <mi mathvariant="normal">I</mi> <mi mathvariant="normal">I</mi> <mi mathvariant="normal">I</mi> </mrow> </mrow> <mrow> <msub> <mrow> <mrow> <mo stretchy="false">)</mo> </mrow> </mrow> <mrow> <mrow> <mrow> <mi mathvariant="normal">G</mi> </mrow> </mrow> <mrow> <msub> <mrow> <mrow> <mi mathvariant="normal">a</mi> </mrow> </mrow> <mrow> <mrow> <mn>2</mn> </mrow> </mrow> </msub> </mrow> <mrow> <msub> <mrow> <mrow> <mi mathvariant="normal">O</mi> </mrow> </mrow> <mrow> <mrow> <mn>3</mn> </mrow> </mrow> </msub> </mrow> </mrow> </msub> </mrow> </mrow> <mo>)</mo> </mrow> </math></EquationSource> </InlineEquation>. During the Ga<sub>2</sub>O<sub>3</sub>-catalyzed PDH reaction with co-fed H<sub>2</sub>, the <InlineEquation ID="IEq2"> <EquationSource Format="TEX">\({\rm{Ga(III}}{{\rm{)}}_{{\rm{G}}{{\rm{a}}_{{2}}}{{\rm{O}}_{{3}}}}}{\rm{ - }}{{\rm{H}}^{\rm{*}}}\)</EquationSource> <EquationSource Format="MATHML"><math display="block"> <mrow> <mrow> <mi mathvariant="normal">G</mi> <mi mathvariant="normal">a</mi> <mo stretchy="false">(</mo> <mi mathvariant="normal">I</mi> <mi mathvariant="normal">I</mi> <mi mathvariant="normal">I</mi> </mrow> </mrow> <mrow> <msub> <mrow> <mrow> <mo stretchy="false">)</mo> </mrow> </mrow> <mrow> <mrow> <mrow> <mi mathvariant="normal">G</mi> </mrow> </mrow> <mrow> <msub> <mrow> <mrow> <mi mathvariant="normal">a</mi> </mrow> </mrow> <mrow> <mrow> <mn>2</mn> </mrow> </mrow> </msub> </mrow> <mrow> <msub> <mrow> <mrow> <mi mathvariant="normal">O</mi> </mrow> </mrow> <mrow> <mrow> <mn>3</mn> </mrow> </mrow> </msub> </mrow> </mrow> </msub> </mrow> <mrow> <mrow> <mo>−</mo> </mrow> </mrow> <mrow> <msup> <mrow> <mrow> <mi mathvariant="normal">H</mi> </mrow> </mrow> <mrow> <mrow> <mo>∗</mo> </mrow> </mrow> </msup> </mrow> </math></EquationSource> </InlineEquation> species initially forms by H<sub>2</sub> dissociation, then reacts with C<sub>3</sub>H<sub>8</sub> to produce C<sub>3</sub>H<sub>6</sub> and H<sub>2</sub>, and finally gets recovered by H<sub>2</sub> dissociation, leading to the dynamically-cycled hydride active site on Ga<sub>2</sub>O<sub>3</sub> with greatly enhanced catalytic performance. Such a hydride catalysis is highly sensitive to the structure of Ga<sub>2</sub>O<sub>3</sub>, being more efficiently on Ga<sub>2</sub>O<sub>3</sub>{111} facets than on Ga<sub>2</sub>O<sub>3</sub>{100} facets. A fine Ga<sub>2</sub>O<sub>3</sub> nanocatalyst with a high ratio of exposed {111} facets and a large specific surface area is fabricated to give a C<sub>3</sub>H<sub>6</sub> space-time yield (STY) as high as <InlineEquation ID="IEq3"> <EquationSource Format="TEX">\({{4}}{{.9}}\,{\rm{k}}{{\rm{g}}_{{{\rm{C}}_3}{{\rm{H}}_6}}}/\left( {{\rm{k}}{{\rm{g}}_{{\rm{catalyst}}}}\,{\rm{h}}} \right)\)</EquationSource> <EquationSource Format="MATHML"><math display="block"> <mrow> <mrow> <mn>4</mn> </mrow> </mrow> <mrow> <mrow> <mn>.9</mn> </mrow> </mrow> <mspace width="thinmathspace" /> <mrow> <mrow> <mi mathvariant="normal">k</mi> </mrow> </mrow> <mrow> <msub> <mrow> <mrow> <mi mathvariant="normal">g</mi> </mrow> </mrow> <mrow> <mrow> <msub> <mrow> <mrow> <mi mathvariant="normal">C</mi> </mrow> </mrow> <mn>3</mn> </msub> </mrow> <mrow> <msub> <mrow> <mrow> <mi mathvariant="normal">H</mi> </mrow> </mrow> <mn>6</mn> </msub> </mrow> </mrow> </msub> </mrow> <mrow> <mo>/</mo> </mrow> <mrow> <mo>(</mo> <mrow> <mrow> <mrow> <mi mathvariant="normal">k</mi> </mrow> </mrow> <mrow> <msub> <mrow> <mrow> <mi mathvariant="normal">g</mi> </mrow> </mrow> <mrow> <mrow> <mrow> <mi mathvariant="normal">c</mi> <mi mathvariant="normal">a</mi> <mi mathvariant="normal">t</mi> <mi mathvariant="normal">a</mi> <mi mathvariant="normal">l</mi> <mi mathvariant="normal">y</mi> <mi mathvariant="normal">s</mi> <mi mathvariant="normal">t</mi> </mrow> </mrow> </mrow> </msub> </mrow> <mspace width="thinmathspace" /> <mrow> <mrow> <mi mathvariant="normal">h</mi> </mrow> </mrow> </mrow> <mo>)</mo> </mrow> </math></EquationSource> </InlineEquation> with a C<sub>3</sub>H<sub>6</sub> selectivity of 96.5% and a good recyclability in the PDH reaction with co-fed H<sub>2</sub> at 550 °C. These results provide an alternative strategy for developing none-Pt- and none-toxic CrO<sub><i>x</i></sub>-based PDH catalysts.</p>

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Structure sensitivity of gallium oxide catalyzed propane dehydrogenation reaction co-fed with hydrogen

  • Hantao Peng,
  • Yi-Chun Chu,
  • Zeyue Wei,
  • Aiping Jia,
  • Yunxing Bai,
  • Zhaorui Li,
  • Xuanyu Zhang,
  • Xin-Ping Wu,
  • Weixin Huang

摘要

Developing efficient propane dehydrogenation (PDH) processes without uses of expensive Pt- and toxic CrOx-based catalysts are of broad interest and great importance. Co-feeding of hydrogen is a widely-adopted strategy to improve catalytic performance of various catalysts in the PDH reaction. Herein, we systematically study the promotion effect of co-fed H2 on different oxide catalysts in the PDH reaction. It comes mainly from the alleviated poisoning effect on ZnO and additionally from H2 reduction-enhanced coordination-unsaturated Zr3+ active sites on ZrO2, while mainly from the formation of dynamically-cycles metastable gallium hydride species on Ga2O3 capable of activating the C–H bond activation of propane at significantly reduced barriers \(\left( {{{\rm{C}}_{{3}}}{{\rm{H}}_{{8}}} + 2{\rm{Ga(III}}{{\rm{)}}_{{\rm{G}}{{\rm{a}}_{\rm{2}}}{{\rm{O}}_{{3}}}}}{\rm{ - }}{{\rm{H}}^{\rm{*}}} = {{\rm{C}}_{\rm{3}}}{{\rm{H}}_{{6}}} + 2{{\rm{H}}_{{2}}} + 2{\rm{Ga(III}}{{\rm{)}}_{{\rm{G}}{{\rm{a}}_{{2}}}{{\rm{O}}_{{3}}}}}} \right)\) ( C 3 H 8 + 2 G a ( I I I ) G a 2 O 3 H = C 3 H 6 + 2 H 2 + 2 G a ( I I I ) G a 2 O 3 ) . During the Ga2O3-catalyzed PDH reaction with co-fed H2, the \({\rm{Ga(III}}{{\rm{)}}_{{\rm{G}}{{\rm{a}}_{{2}}}{{\rm{O}}_{{3}}}}}{\rm{ - }}{{\rm{H}}^{\rm{*}}}\) G a ( I I I ) G a 2 O 3 H species initially forms by H2 dissociation, then reacts with C3H8 to produce C3H6 and H2, and finally gets recovered by H2 dissociation, leading to the dynamically-cycled hydride active site on Ga2O3 with greatly enhanced catalytic performance. Such a hydride catalysis is highly sensitive to the structure of Ga2O3, being more efficiently on Ga2O3{111} facets than on Ga2O3{100} facets. A fine Ga2O3 nanocatalyst with a high ratio of exposed {111} facets and a large specific surface area is fabricated to give a C3H6 space-time yield (STY) as high as \({{4}}{{.9}}\,{\rm{k}}{{\rm{g}}_{{{\rm{C}}_3}{{\rm{H}}_6}}}/\left( {{\rm{k}}{{\rm{g}}_{{\rm{catalyst}}}}\,{\rm{h}}} \right)\) 4 .9 k g C 3 H 6 / ( k g c a t a l y s t h ) with a C3H6 selectivity of 96.5% and a good recyclability in the PDH reaction with co-fed H2 at 550 °C. These results provide an alternative strategy for developing none-Pt- and none-toxic CrOx-based PDH catalysts.