This work was supported by the School of Chemical Engineering, Purdue University. Use of the Advanced Photon Source was supported by the U.S. Department of Energy, Office of Basic Energy Sciences, under contract no. DE-AC02-06CH11357. MRCAT operations, beamline 10-BM are supported by the Department of Energy and the MRCAT member institutions. The authors also acknowledge the use of beamline 11-ID-C. We thank Evan Wegener for experimental assistance with the XAS.

1. Synthesis of Supported 2 nm Pt-Cu Bimetallic Nanoparticle Catalysts
<ol>
	<li>Preparation of metal precursor solution
	<ol>
		<li>Dissolve 0.125 g of copper nitrate trihydrate (Cu(NO3)2&#183;3H2O) in 1 mL of water to achieve a sky blue solution. 
		Caution: Use protective gloves when handling chemicals.</li>
		<li>Add ammonia dropwise to the copper nitrate solution, forming dark blue precipitates of copper hydroxide. 
		Caution: Use a fume hood for handling...

<ol>
	<li>Sattler, J. J., Ruiz-Martinez, J., Santillan-Jimenez, E., Weckhuysen, B. M. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Catalytic+dehydrogenation+of+light+alkanes+on+metals+and+metal+oxides.">Catalytic dehydrogenation of light alkanes on metals and metal oxides.</a> Chem. Rev. 114 (20), 10613-10653 (2014).</li><li>Childers, D. J., et al. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Modifying+structure-sensitive+reactions+by+addition+of+Zn+to+Pd.">Modifying structure-sensitive reactions by addition of Zn to Pd.</a> J Catal. 318, 75-84 (2014).</li><li>Gallagher, J. R., et al. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Structural+evolution+of+an+intermetallic+Pd-Zn+catalyst+selective+for+propane+dehydrogenation.">Structural evolution of an intermetallic Pd-Zn catalyst selective for propane dehydrogenation.</a> Phys. Chem. Chem. Phys. 17, 28144-28153 (2015).</li><li>Wu, Z., et al. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Pd-In+intermetallic+alloy+nanoparticles:+highly+selective+ethane+dehydrogenation+catalysts.">Pd-In intermetallic alloy nanoparticles: highly selective ethane dehydrogenation catalysts.</a> Catal Sci Technol. 6 (18), 6965-6976 (2016).</li><li>Siddiqi, G., Sun, P., Galvita, V., Bell, A. T. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Catalyst+performance+of+novel+Pt/Mg+(Ga)(Al)+O+catalysts+for+alkane+dehydrogenation.">Catalyst performance of novel Pt/Mg (Ga)(Al) O catalysts for alkane dehydrogenation.</a> J Catal. 274 (2), 200-206 (2010).</li><li>Passos, F. B., Aranda, D. A., Schmal, M. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Characterization+and+catalytic+activity+of+bimetallic+Pt-In/Al+2+O+3+and+Pt-Sn/Al+2+O+3+catalysts.">Characterization and catalytic activity of bimetallic Pt-In/Al 2 O 3 and Pt-Sn/Al 2 O 3 catalysts.</a> J Catal. 178 (2), 478-488 (1998).</li><li>Virnovskaia, A., Morandi, S., Rytter, E., Ghiotti, G., Olsbye, U. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Characterization+of+Pt,+Sn/Mg+(Al)+O+catalysts+for+light+alkane+dehydrogenation+by+FT-IR+spectroscopy+and+catalytic+measurements.">Characterization of Pt, Sn/Mg (Al) O catalysts for light alkane dehydrogenation by FT-IR spectroscopy and catalytic measurements.</a> J Phys Chem C. 111 (40), 14732-14742 (2007).</li><li>Jablonski, E., Castro, A., Scelza, O., De Miguel, S. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Effect+of+Ga+addition+to+Pt/Al+2+O+3+on+the+activity,+selectivity+and+deactivation+in+the+propane+dehydrogenation.">Effect of Ga addition to Pt/Al 2 O 3 on the activity, selectivity and deactivation in the propane dehydrogenation.</a> Appl Catal A. 183 (1), 189-198 (1999).</li><li>Galvita, V., Siddiqi, G., Sun, P., Bell, A. T. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Ethane+dehydrogenation+on+Pt/Mg+(Al)+O+and+PtSn/Mg+(Al)+O+catalysts.">Ethane dehydrogenation on Pt/Mg (Al) O and PtSn/Mg (Al) O catalysts.</a> J Catal. 271 (2), 209-219 (2010).</li><li>Shen, J., Hill, J. M., Watwe, R. M., Spiewak, B. E., Dumesic, J. A. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Microcalorimetric,+infrared+spectroscopic,+and+DFT+studies+of+ethylene+adsorption+on+Pt/SiO2+and+Pt-Sn/SiO2+catalysts.">Microcalorimetric, infrared spectroscopic, and DFT studies of ethylene adsorption on Pt/SiO2 and Pt-Sn/SiO2 catalysts.</a> J Phys Chem B. 103 (19), 3923-3934 (1999).</li><li>Silvestre-Albero, J., et al. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Microcalorimetric,+reaction+kinetics+and+DFT+studies+of+Pt–Zn/X-zeolite+for+isobutane+dehydrogenation.">Microcalorimetric, reaction kinetics and DFT studies of Pt–Zn/X-zeolite for isobutane dehydrogenation.</a> Catal Lett. 74 (1-2), 17-25 (2001).</li><li>Sun, P., Siddiqi, G., Vining, W. C., Chi, M., Bell, A. T. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Novel+Pt/Mg+(In)(Al)+O+catalysts+for+ethane+and+propane+dehydrogenation.">Novel Pt/Mg (In)(Al) O catalysts for ethane and propane dehydrogenation.</a> J Catal. 282 (1), 165-174 (2011).</li><li>Sun, P., Siddiqi, G., Chi, M., Bell, A. T. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Synthesis+and+characterization+of+a+new+catalyst+Pt/Mg+(Ga)(Al)+O+for+alkane+dehydrogenation.">Synthesis and characterization of a new catalyst Pt/Mg (Ga)(Al) O for alkane dehydrogenation.</a> J Catal. 274 (2), 192-199 (2010).</li><li>Okamoto, H. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=.">.</a> Phase diagrams for binary alloys. Desk handbook. , (2000).</li><li>Hamid, S. B. D. -. A., Lambert, D., Derouane, E. G. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Dehydroisomerisation+of+n-butane+over+(Pt,+Cu)/H-TON+catalysts.">Dehydroisomerisation of n-butane over (Pt, Cu)/H-TON catalysts.</a> Catal Today. 63 (2), 237-247 (2000).</li><li>Veldurthi, S., Shin, C. -. H., Joo, O. -. S., Jung, K. -. D. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Promotional+effects+of+Cu+on+Pt/Al+2+O+3+and+Pd/Al+2+O+3+catalysts+during+n-butane+dehydrogenation.">Promotional effects of Cu on Pt/Al 2 O 3 and Pd/Al 2 O 3 catalysts during n-butane dehydrogenation.</a> Catal Today. 185 (1), 88-93 (2012).</li><li>Han, Z., et al. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Propane+dehydrogenation+over+Pt-Cu+bimetallic+catalysts:+the+nature+of+coke+deposition+and+the+role+of+copper.">Propane dehydrogenation over Pt-Cu bimetallic catalysts: the nature of coke deposition and the role of copper.</a> Nanoscale. 6 (17), 10000-10008 (2014).</li><li>Komatsu, T., Tamura, A. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Pt+3+Co+and+PtCu+intermetallic+compounds:+promising+catalysts+for+preferential+oxidation+of+CO+in+excess+hydrogen.">Pt 3 Co and PtCu intermetallic compounds: promising catalysts for preferential oxidation of CO in excess hydrogen.</a> J Catal. 258 (2), 306-314 (2008).</li><li>Gallagher, J. R., et al. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=In+situ+diffraction+of+highly+dispersed+supported+platinum+nanoparticles.">In situ diffraction of highly dispersed supported platinum nanoparticles.</a> Catal Sci Technol. 4 (9), 3053-3063 (2014).</li><li>Ma, Z., Wu, Z., Miller, J. T. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Effect+of+Cu+content+on+the+bimetallic+Pt-Cu+catalysts+for+propane+dehydrogenation.">Effect of Cu content on the bimetallic Pt-Cu catalysts for propane dehydrogenation.</a> Catal Struct React. 3 (1-2), 43-53 (2017).</li><li>Richards, R. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=.">.</a> Surface and nanomolecular catalysis. , (2006).</li><li>Jiao, L., Regalbuto, J. R. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=The+synthesis+of+highly+dispersed+noble+and+base+metals+on+silica+via+strong+electrostatic+adsorption:+I.+Amorphous+silica.">The synthesis of highly dispersed noble and base metals on silica via strong electrostatic adsorption: I. Amorphous silica.</a> J Catal. 260 (2), 329-341 (2008).</li><li>Miller, J. T., Schreier, M., Kropf, A. J., Regalbuto, J. R. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=A+fundamental+study+of+platinum+tetraammine+impregnation+of+silica:+2.+The+effect+of+method+of+preparation,+loading,+and+calcination+temperature+on+(reduced)+particle+size.">A fundamental study of platinum tetraammine impregnation of silica: 2. The effect of method of preparation, loading, and calcination temperature on (reduced) particle size.</a> J Catal. 225 (1), 203-212 (2004).</li><li>Wei, H., et al. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Selective+hydrogenation+of+acrolein+on+supported+silver+catalysts:+A+kinetics+study+of+particle+size+effects.">Selective hydrogenation of acrolein on supported silver catalysts: A kinetics study of particle size effects.</a> J Catal. 298, 18-26 (2013).</li><li>Ertl, G., Kn&#246;zinger, H., Sch&#252;th, F., Weitkamp, J. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=.">.</a> Handbook of heterogeneous catalysis: 8 volumes. , (2008).</li></ol>

The authors have nothing to disclose.

The Pt-Cu catalysts prepared in this work contain uniform nanoparticles around 2 nm in size, similar to heterogeneous catalysts qualified for industrial application. All the Pt and Cu precursors form bimetallic structures, as opposed to separate monometallic particles. This bimetallic interaction and small particle size are realized by careful control over the synthesis procedures. The impregnation process makes use of the Strong Electrostatic Adsorption (SEA) between metal ions and the surface of certain oxide supports<...

Propane dehydrogenation (PDH) is a key processing step in the production of propylene, taking advantage of shale gas, the fastest growing source of gas in the country1. This reaction breaks two C-H bonds in a propane molecule to form one propylene and molecular hydrogen. Noble metal catalysts, including Pd nanoparticles, exhibit poor selectivity for PDH, breaking the C-C bond to produce methane with a high yield, with the concomitant production of coke, leading to catalyst deactivation. Recent reports showed that selective PDH catalysts could be obtained by the addition of promoters like Zn or In to Pd2,3,4. The promoted catalysts are near 100% selective to PDH, as opposed to less than 50% for monometallic Pd nanoparticles of the same size. The great improvement in selectivity was attributed to the formation of PdZn or PdIn intermetallic compound (IMC) structures on the catalyst surface. The ordered array of two different types of atoms in the IMCs geometrically isolated the Pd active sites with non-catalytic Zn or In atoms, which turned off the side reactions catalyzed by an ensemble (group) of neighboring Pd active sites.
Platinum has the highest intrinsic selectivity among noble metals for propane dehydrogenation, but it is still not satisfactory for commercial use1. Typically, Sn, Zn, In, or Ga is added as promoter for Pt5,6,7,8,9,10,11,12,13. Based on the idea that geometric active site isolation contributes to high selectivity, any non-catalytic element forming an alloy structure with Pt, such as Cu, should also potentially promote catalyst performance14. Several previous studies suggested that the addition of Cu indeed improved the PDH selectivity of Pt catalysts15,16,17,18. Nevertheless, no direct evidence has been reported to determine whether Pt and Cu form bimetallic nanoparticles or ordered structures, which is crucial to understanding the promotional effect of Cu. In the binary phase diagram of Pt-Cu, two different structure types are possible over a wide composition range16,18: intermetallic compound, in which Pt and Cu each occupy specific crystal sites, and solid solution, in which Cu randomly substitutes in the Pt lattice. IMCs form at low temperature and transform into solid solution at around 600 - 800 &#176;C for bulk materials14. This transformation temperature may be lower for nanoparticles, near the reaction temperature of PDH (i.e.&#160;550 &#176;C). Therefore, it is essential to investigate the atomic order of Pt-Cu under reaction conditions. For supported nanoparticles with small particle sizes, it is very challenging to obtain meaningful structural information using laboratory instruments19. The limited repetition of unit cells leads to very broad diffraction peaks with very low intensities. Because of the high fraction of surface atoms in nanoparticles 1 - 3 nm in size, which are oxidized in air, diffraction must be collected in situ using high-flux X-ray, typically available with synchrotron techniques.
The previously reported Pt-Cu PDH catalysts were all larger than 5 nm in size15,16,17,18. However, for noble metal nanoparticle catalysts, there is always a strong desire to maximize catalytic activity per unit cost by synthesizing catalysts with high dispersions (typically around or less than 2 nm in size)19. Though the preparation of bimetallic nanoparticles of this size is possible by standard impregnation methods, rational control over the procedures is necessary. The metal precursors, pH of the impregnating solution, and support type need to be controlled to optimize the anchoring of the metal species onto high-surface area supports. The subsequent calcination and reduction heat treatments should also be carefully controlled to suppress the growth of the metallic nanoparticles.
This article covers the protocol for the synthesis of supported 2 nm Pt-Cu bimetallic nanoparticle catalysts and for the testing of their propane dehydrogenation performance. The structure of the catalysts is investigated by Scanning Transmission Electron Microscopy (STEM), in situ synchrotron X-ray Absorption Spectroscopy (XAS), and in situ synchrotron X-ray diffraction (XRD), which help elucidate the improved catalyst performance upon the introduction of Cu.

<table border="0" cellpadding="0" cellspacing="0" width="988">
	<tbody>
		<tr height="25">
			<td height="25" style="height:25px;width:399px;">1 inch quartz tube reactor&#160;</td>
			<td style="width:195px;">Quartz Scientific</td>
			<td style="width:228px;">Processed by glass blower</td>
			<td style="width:167px;"></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:399px;">drying oven&#160;</td>
			<td style="width:195px;">Fisher Scientific</td>
			<td style="width:228px;"></td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:399px;">calcination Furnace</td>
			<td style="width:195px;">Thermo Sciencfic</td>
			<td style="width:228px;"></td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:399px;">clam-shell temperature programmed furnace&#160;</td>
			<td style="width:195px;">Applied Test System</td>
			<td style="width:228px;">Custom made</td>
			<td></td>
		</tr>
		<tr height="22">
			<td height="22" style="height:22px;width:399px;">propane dehydorgenation performance evaluation system</td>
			<td style="width:195px;"></td>
			<td style="width:228px;">Homemade</td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:399px;">gas chromatography</td>
			<td style="width:195px;">Hewlett-Packard</td>
			<td style="width:228px;">Model 7890</td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:399px;">TEM grid</td>
			<td style="width:195px;">TedPella</td>
			<td style="width:228px;">01824G</td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:399px;">pellet press</td>
			<td style="width:195px;">International Crystal Lab</td>
			<td style="width:228px;">0012-8211</td>
			<td></td>
		</tr>
		<tr height="23">
			<td height="23" style="height:23px;width:399px;">die set</td>
			<td style="width:195px;">International Crystal Lab</td>
			<td style="width:228px;">0012-189</td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:399px;">Linkam Sample Stage</td>
			<td style="width:195px;">Linkam Scientific</td>
			<td style="width:228px;">Model TS1500</td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:399px;">copper nitrate trihydrgate</td>
			<td style="width:195px;">Sigma Aldrich</td>
			<td align="right" style="width:228px;">61197</td>
			<td></td>
		</tr>
		<tr height="22">
			<td height="22" style="height:22px;width:399px;">tetraammineplatinum nitrate&#160;</td>
			<td style="width:195px;">Sigma Aldrich</td>
			<td align="right" style="width:228px;">278726</td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:399px;">ammonia&#160;</td>
			<td style="width:195px;">Sigma Aldrich</td>
			<td align="right" style="width:228px;">294993</td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:399px;">silica</td>
			<td style="width:195px;">Sigma Aldrich</td>
			<td align="right" style="width:228px;">236802</td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:399px;">isopropyl alcohol</td>
			<td style="width:195px;">Sigma Aldrich</td>
			<td style="width:228px;"></td>
			<td></td>
		</tr>
		<tr height="24">
			<td height="24" style="height:24px;width:399px;">balance</td>
			<td style="width:195px;">Denver Instrument Company</td>
			<td style="width:228px;">A-160</td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:399px;">spatulas</td>
			<td style="width:195px;">VWR</td>
			<td style="width:228px;"></td>
			<td></td>
		</tr>
		<tr height="22">
			<td height="22" style="height:22px;width:399px;">ceramic and glass evaporating dishes, beakers</td>
			<td style="width:195px;">VWR</td>
			<td style="width:228px;"></td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;">heating plate</td>
			<td style="width:195px;"></td>
			<td style="width:228px;"></td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:399px;">kimwipe papers</td>
			<td style="width:195px;"></td>
			<td style="width:228px;"></td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:399px;">mortar and pestle</td>
			<td style="width:195px;"></td>
			<td style="width:228px;"></td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:399px;">quartz wool&#160;</td>
			<td style="width:195px;"></td>
			<td style="width:228px;"></td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:399px;">Swagelok tube fittings&#160;</td>
			<td style="width:195px;"></td>
			<td style="width:228px;"></td>
			<td></td>
		</tr>
	</tbody>
</table>

synthesis and testing of supported pt-cu solid solution nanoparticle catalysts for propane dehydrogenation

A convenient method for the synthesis of bimetallic Pt-Cu catalysts and performance tests for propane dehydrogenation and characterization are demonstrated here. The catalyst forms a substitutional solid solution structure, with a small and uniform particle size around 2 nm. This is realized by careful control over the impregnation, calcination, and reduction steps during catalyst preparation and is identified by advanced in situ synchrotron techniques. The catalyst propane dehydrogenation performance continuously improves with increasing Cu:Pt atomic ratio.

The propylene selectivity versus time for Pt and Pt-Cu catalysts measured at an initial propane conversion of about 20% is presented in Figure 1A. Pt catalyst has an initial selectivity of 61%, which increases to about 82% with time on-stream as the catalyst deactivates for 1h. The Pt-0.7Cu catalyst shows a better initial propylene selectivity of 72%. For Pt-2.3Cu and Pt-7.3Cu catalysts, their initial selectivity reach 90% and 96%, respectively, and are maint...

Watch this Scientific Journal Video about Synthesis and Testing of Supported Pt-Cu Solid Solution Nanoparticle Catalysts for Propane Dehydrogenation at JoVE.com

Synthesis and Testing of Supported Pt-Cu Solid Solution Nanoparticle Catalysts for Propane Dehydrogenation

A convenient method for the synthesis of 2 nm supported bimetallic nanoparticle Pt-Cu catalysts for propane dehydrogenation is reported here. In situ synchrotron X-ray techniques allow for the determination of the catalyst structure, which is typically unobtainable using laboratory instruments.

A convenient method for the synthesis of bimetallic Pt-Cu catalysts and performance tests for propane dehydrogenation and characterization are ...

The overall goal of this research is to synthesize new bimetallic catalysts with small uniform particle size and test their performance for alkane dehydrogenation. The goal is to understand the fundamental principles which lead to high olefin selectivity, high rate, long life and thermal stability. This catalyst synthesis method optimizes anchoring of metal species and to support by preparing a solution with a pH that charges the support surface and checks metal ions of opposite charge.Careful control of the calcination and reduction temperatures is needed to achieve small particle size, co-impregnation of the properly chosen metal precursors ensures strong bimetallic interaction which ultimately controls the activity and selectivity. After preparation, we measure the rates, selectivity and stability of the catalysts for alkane dehydrogenation to determine the differences in performance with catalyst composition and correlate these with the structure. First, carefully weight approximately five grams of dry silica on weigh paper and transfer it into a weighing dish.While mixing, add water drop-wise until the silica is completely wet, but with no excess solution. Then, reweigh the wet silica to calculate the amount of water absorbed and to determine the pore volume of the silica support. To prepare the precursor solution, dissolve 0.125 grams of copper nitrate trihydrate in one milliliter of water in a small vile to obtain a sky-blue solution.Add ammonia drop-wise to the copper-nitrate solution forming dark-blue precipitates of copper hydroxide. Continue adding ammonia until the dark-blue precipitates dissolve to form a dark-blue solution and the pH is greater than 10. Next, add 0.198 grams of tetraammineplatinum nitrate to the solution.Then, add water so that the total volume of the solution is 3.5 milliliters which matches the pore volume of five-gram silica support. Heat the solution to 70 degrees Celsius until all the tetraammineplatinum nitrate salts are dissolved. After allowing the dissolved metal precursor solution to cool to room temperature, add a few drops at a time to five grams of silica in a ceramic evaporating dish and stir gently to break up the particles that stick together to achieve a homogeneous distribution of the solution.Dry the impregnated silica-supported catalyst with a copper-to-platinum ratio of 0.7 in an oven at 125 degrees Celsius overnight. On the following day, calcine the cooled catalyst precursor in a furnace at 250 degrees Celsius with a five-degree Celsius permanent ramp rate in air for three hours. Next, transfer the calcined catalyst to a tube furnace for reduction.Place a one-inch layer of quartz wool in the middle of a one-inch quartz tube reactor and load the cooled calcined catalyst into the tube through a plastic funnel. Then, place the tube in a clamshell temperature programmed furnace. After purging the tube with nitrogen for five minutes at room temperature, switch the flow to 5%hydrogen balanced in nitrogen at the same flow rate as nitrogen to reduce the catalyst.Increase the temperature to 150 degrees Celsius with a five-degree Celsius permanent ramp rate and hold for five minutes. Now, start slow-ramping of the temperature at a rate of 2.5 degrees Celsius per minute to 250 degrees Celsius holding the temperature for 15 minutes after every 25-degree-Celsius increase. Ramp to 550 degrees Celsius at 10 degrees Celsius per minute and stay for 30 minutes to complete the reduction.Switch the 5%hydrogen flow back to pure nitrogen to purge the system and cool to room temperature. Then, unload the catalyst and store it in a vial for future use. Place a half-inch layer of quartz wool against the dimple in the middle of a 3/8-inch quartz tube reactor.Next, mix 40 milligrams of silica-supported catalyst precursor with a copper-to-platinum ratio of 0.7 and 960 milligrams of the silica in an empty vial to dilute the catalyst. Using a plastic funnel, load the catalyst mixture into the tube reactor. Wipe the outer wall of both tube ends with lint-free wipes to remove any dirt and to get a good seal with the O-ring.Connect the tube fittings to both ends of the quartz tube reactor and attach them to the reactor system equipped with a clamshell furnace. Following this, turn on the nitrogen flow through the tube reactor. After one minute, close the ball valve on the reactor outlet.After waiting for the system pressure to increase to five pounds per square inch gauge, close the ball valve on the inlet nitrogen line to stop the nitrogen flow and seal the reactor system. After one minute, record the pressure reading from the gauge. Open the ball valve on the reactor outlet to release the pressure before restarting the nitrogen flow by turning on the ball valve on the inlet nitrogen line to purge the system for one minute.Start flowing hydrogen diluted in nitrogen for catalyst reduction before running the reaction and stop the nitrogen flow. Start heating the tube reactor to 550 degrees Celsius with a rate of 10 degrees Celsius. For propane dehydrogenation reaction testing, start the gas chromatograph, or GC, in the reactor system and select the proper method for gas component analysis.Now, switch the reactor gas flow to a bypass line. Flow 100 cubic centimeters per minute of 5%propane and nitrogen diluted in 5%hydrogen diluted in nitrogen. After the propane flow stabilizes, inject the bypass flow into the GC as a reference sample.Next, switch the gas flow back to the reactor tube line to start the reaction and record the time. After the reaction runs for four minutes, inject the reactor outlet gas flow into the GC to get the outlet gas component information. Finally, use the corresponding peak analysis software to analyze each peak.The propylene selectivity versus time for platinum and platinum-copper catalysts is presented here. While the propylene selectivity of the platinum catalysts decreases at higher conversion, the silica-supported catalyst with a copper-to-platinum ratio of 7.3 retains high propylene selectivity at different propane conversions. The catalyst's selectivity increases almost linearly with a copper content in the platinum-copper catalysts.Higher copper content also improves the turnover rates per mole of surface platinum for propane dehydrogenation. There is a close-to-linear relationship between the turnover rate and the catalyst atomic ratio of copper-to-platinum with the carbon balance close to 100%during all reaction tests. The average particle size of the monometallic platinum and platinum-copper catalysts determined by stem imaging are between two and three nanometers.The change of the scattering pattern in the x-ray absorption fine structure spectra of the catalysts with increasing copper-to-platinum ratio suggests the formation of bimetallic nanoparticles with increasing copper content. The XRD pattern of platinum and platinum-copper catalysts showed that their composition differs from the ideal composition of ordered alloys and there is no peak from superlattice diffraction indicating that platinum and copper form a disordered solid solution structure in the catalysts. The diffraction peaks shift to higher angles with increasing copper-to-platinum ratio confirming that the solid solution becomes richer in copper.Once mastered, the impregnation step can be done in about one hour and the consistency like small particles with uniform composition. When preparing metallic alloys by impregnation, it's important to adjust the pH value of the solution and use proper metal complexes according to the type of the support. The solution volume should be equal to the pore volume of the support.After watching this video, you should have a good understanding of how to synthesize supported bimetallic catalysts and test their alkane dehydrogenation performance. This method is broadly applicable and can be used for different catalyst compositions and for many chemical reactions. Don't forget that mixing hydrogen with air in the presence of a metallic catalyst is extremely dangerous and may lead to explosions.You must always purge the reactor with nitrogen before and after hydrogen addition to the catalyst.

synthesis-testing-supported-pt-cu-solid-solution-nanoparticle

Research

JoVE Journal

Chemistry

11.8K 조회수.  Purdue University. The overall goal of this research is to synthesize new bimetallic catalysts with small uniform particle size and test their performance for alkane dehydrogenation. The goal is to understand the fundamental principles which lead to high olefin selectivity, high rate, long life and thermal stability. This catalyst synthesis method optimizes anchoring of metal species and to support by preparing a solution with a pH that charges the support surface and checks metal ions of opposite charge.