The size, shape, and dispersion of active sites on AC-supported copper nanocatalysts with polyol process: The effect of precursors

This study mainly focuses on the preparation of copper catalysts by the polyol process using different precursors (acetate, nitrate, and sulfate). The shapes and sizes of the particles of the catalysts formed with various precursors are not similar in the polyol process. The particle of Cu-A/AC cont...

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Veröffentlicht in:Applied catalysis. A, General General, 2008-07, Vol.344 (1), p.36-44
Hauptverfasser: Lu, Chi-Yuan, Wey, Ming-Yen, Fu, Ying-Hui
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description This study mainly focuses on the preparation of copper catalysts by the polyol process using different precursors (acetate, nitrate, and sulfate). The shapes and sizes of the particles of the catalysts formed with various precursors are not similar in the polyol process. The particle of Cu-A/AC contains two types of active phases: one is spherical (50–70 nm) and the other is cubic (>1 μm). ▪ The polyol process is simple to conduct and can enhance the diffusion of active sites and control the shape of the active phase during catalyst preparation. Activated carbon (AC) was chosen as the support, and copper nitrate, copper acetate, and copper sulfate were used as precursors to prepare the AC-supported copper catalysts. Toluene was chosen as the pollutant for the activity test. The experimental results showed that the copper particles were nanosized and were highly dispersed on the AC; such dispersion improved the thermal stabilization of the AC-supported catalyst. The copper content observed in an inductively coupled plasma-mass spectrometer was the same even for increased amounts of copper sulfate; however, for the other two precursors, the copper content increased with the amount of precursor. Different precursors gave rise to different types of active phases. For example, when copper acetate was used as the precursor, the catalyst had pellet (50–70 nm)- and cubic (>1 μm)-shaped active phases. The activities of the copper catalysts were in the order copper nitrate > copper acetate > copper sulfate. Among the catalysts tested, Cu-N/Al 2O 3 with 5 wt.% Cu loading exhibited the highest activity at 158,720 h −1. For Al 2O 3-supported catalysts prepared by the polyol process, the Cu-A/Al 2O 3 catalyst exhibited the highest activity. Thus, the polyol process has the potential to be used in catalyst preparation along with various different precursors to control gaseous pollutants.
doi_str_mv 10.1016/j.apcata.2008.03.036
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The shapes and sizes of the particles of the catalysts formed with various precursors are not similar in the polyol process. The particle of Cu-A/AC contains two types of active phases: one is spherical (50–70 nm) and the other is cubic (&gt;1 μm). ▪ The polyol process is simple to conduct and can enhance the diffusion of active sites and control the shape of the active phase during catalyst preparation. Activated carbon (AC) was chosen as the support, and copper nitrate, copper acetate, and copper sulfate were used as precursors to prepare the AC-supported copper catalysts. Toluene was chosen as the pollutant for the activity test. The experimental results showed that the copper particles were nanosized and were highly dispersed on the AC; such dispersion improved the thermal stabilization of the AC-supported catalyst. The copper content observed in an inductively coupled plasma-mass spectrometer was the same even for increased amounts of copper sulfate; however, for the other two precursors, the copper content increased with the amount of precursor. Different precursors gave rise to different types of active phases. For example, when copper acetate was used as the precursor, the catalyst had pellet (50–70 nm)- and cubic (&gt;1 μm)-shaped active phases. The activities of the copper catalysts were in the order copper nitrate &gt; copper acetate &gt; copper sulfate. Among the catalysts tested, Cu-N/Al 2O 3 with 5 wt.% Cu loading exhibited the highest activity at 158,720 h −1. For Al 2O 3-supported catalysts prepared by the polyol process, the Cu-A/Al 2O 3 catalyst exhibited the highest activity. Thus, the polyol process has the potential to be used in catalyst preparation along with various different precursors to control gaseous pollutants.</description><identifier>ISSN: 0926-860X</identifier><identifier>EISSN: 1873-3875</identifier><identifier>DOI: 10.1016/j.apcata.2008.03.036</identifier><language>eng</language><publisher>Amsterdam: Elsevier B.V</publisher><subject>Catalysis ; Chemical synthesis ; Chemistry ; Diffusion ; Electron microscopy ; Exact sciences and technology ; General and physical chemistry ; Oxidation ; Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry</subject><ispartof>Applied catalysis. 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A, General</title><description>This study mainly focuses on the preparation of copper catalysts by the polyol process using different precursors (acetate, nitrate, and sulfate). The shapes and sizes of the particles of the catalysts formed with various precursors are not similar in the polyol process. The particle of Cu-A/AC contains two types of active phases: one is spherical (50–70 nm) and the other is cubic (&gt;1 μm). ▪ The polyol process is simple to conduct and can enhance the diffusion of active sites and control the shape of the active phase during catalyst preparation. Activated carbon (AC) was chosen as the support, and copper nitrate, copper acetate, and copper sulfate were used as precursors to prepare the AC-supported copper catalysts. Toluene was chosen as the pollutant for the activity test. The experimental results showed that the copper particles were nanosized and were highly dispersed on the AC; such dispersion improved the thermal stabilization of the AC-supported catalyst. The copper content observed in an inductively coupled plasma-mass spectrometer was the same even for increased amounts of copper sulfate; however, for the other two precursors, the copper content increased with the amount of precursor. Different precursors gave rise to different types of active phases. For example, when copper acetate was used as the precursor, the catalyst had pellet (50–70 nm)- and cubic (&gt;1 μm)-shaped active phases. The activities of the copper catalysts were in the order copper nitrate &gt; copper acetate &gt; copper sulfate. Among the catalysts tested, Cu-N/Al 2O 3 with 5 wt.% Cu loading exhibited the highest activity at 158,720 h −1. For Al 2O 3-supported catalysts prepared by the polyol process, the Cu-A/Al 2O 3 catalyst exhibited the highest activity. Thus, the polyol process has the potential to be used in catalyst preparation along with various different precursors to control gaseous pollutants.</description><subject>Catalysis</subject><subject>Chemical synthesis</subject><subject>Chemistry</subject><subject>Diffusion</subject><subject>Electron microscopy</subject><subject>Exact sciences and technology</subject><subject>General and physical chemistry</subject><subject>Oxidation</subject><subject>Theory of reactions, general kinetics. Catalysis. 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The particle of Cu-A/AC contains two types of active phases: one is spherical (50–70 nm) and the other is cubic (&gt;1 μm). ▪ The polyol process is simple to conduct and can enhance the diffusion of active sites and control the shape of the active phase during catalyst preparation. Activated carbon (AC) was chosen as the support, and copper nitrate, copper acetate, and copper sulfate were used as precursors to prepare the AC-supported copper catalysts. Toluene was chosen as the pollutant for the activity test. The experimental results showed that the copper particles were nanosized and were highly dispersed on the AC; such dispersion improved the thermal stabilization of the AC-supported catalyst. The copper content observed in an inductively coupled plasma-mass spectrometer was the same even for increased amounts of copper sulfate; however, for the other two precursors, the copper content increased with the amount of precursor. Different precursors gave rise to different types of active phases. For example, when copper acetate was used as the precursor, the catalyst had pellet (50–70 nm)- and cubic (&gt;1 μm)-shaped active phases. The activities of the copper catalysts were in the order copper nitrate &gt; copper acetate &gt; copper sulfate. Among the catalysts tested, Cu-N/Al 2O 3 with 5 wt.% Cu loading exhibited the highest activity at 158,720 h −1. For Al 2O 3-supported catalysts prepared by the polyol process, the Cu-A/Al 2O 3 catalyst exhibited the highest activity. Thus, the polyol process has the potential to be used in catalyst preparation along with various different precursors to control gaseous pollutants.</abstract><cop>Amsterdam</cop><pub>Elsevier B.V</pub><doi>10.1016/j.apcata.2008.03.036</doi><tpages>9</tpages></addata></record>
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subjects Catalysis
Chemical synthesis
Chemistry
Diffusion
Electron microscopy
Exact sciences and technology
General and physical chemistry
Oxidation
Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry
title The size, shape, and dispersion of active sites on AC-supported copper nanocatalysts with polyol process: The effect of precursors
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