A rapid, direct solution-based reduction synthesis method to obtain Au, Pd, and Pt aerogels is presented.
Here, a method to synthesize gold, palladium, and platinum aerogels via a rapid, direct solution-based reduction is presented. The combination of various precursor noble metal ions with reducing agents in a 1:1 (v/v) ratio results in the formation of metal gels within seconds to minutes compared to much longer synthesis times for other techniques such as sol-gel. Conducting the reduction step in a microcentrifuge tube or small volume conical tube facilitates a proposed nucleation, growth, densification, fusion, equilibration model for gel formation, with final gel geometry smaller than the initial reaction volume. This method takes advantage of the vigorous hydrogen gas evolution as a by-product of the reduction step, and as a consequence of reagent concentrations. The solvent accessible specific surface area is determined with both electrochemical impedance spectroscopy and cyclic voltammetry. After rinsing and freeze drying, the resulting aerogel structure is examined with scanning electron microscopy, X-ray diffractometry, and nitrogen gas adsorption. The synthesis method and characterization techniques result in a close correspondence of aerogel ligament sizes. This synthesis method for noble metal aerogels demonstrates that high specific surface area monoliths may be achieved with a rapid and direct reduction approach.
A wide range of energy storage and conversion, catalysis, and sensor applications benefit from three-dimensional metallic nanostructures which provide control over chemical reactivity, and mass transport properties1,2,3,4,5. Such 3-dimensional metallic nanostructures further enhance conductivity, ductility, malleability, and strength8,9. Integration into devices necessitates that materials be free-standing or combined with support materials. Incorporation of nanomaterials onto support structures provides a means of minimizing active material, but may suffer from weak adsorption and eventual agglomeration during device operation10,11.
While there are a variety of synthesis methods to control individual nanoparticle size and shape, few approaches enable control over contiguous 3-dimensional nanomaterials12,13,14. Noble metal 3-dimensional nanostructures have been formed through dithiol linkage of monodisperse nanoparticles, sol-gel formation, nanoparticle coalescence, composite materials, nanosphere chains, and biotemplating15,16,17,18. Many of these approaches require synthesis times on the order of days to weeks to yield desired materials. Noble metal nanofoams synthesized from the direct reduction of precursor salt solutions have been prepared with a faster synthesis timescale and with short-range order of hundreds of micrometers in length, but require mechanical pressing for device integration19,20.
First reported by Kistler, aerogels provide a synthesis route to achieve porous structures with high specific surface areas that are orders of magnitude less dense than their bulk material counterparts21,22,23. Extending 3-dimensional structures to the macroscopic length scale of bulk materials offers an advantage over nanoparticle aggregates or nanofoams that require support materials or mechanical processing. While aerogels provide a synthesis route to control porosity and particle feature size, however, extended synthesis times, and in some cases the use of capping agents or linker molecules, increases overall processing steps and time.
Here a method to synthesize gold, palladium, and platinum aerogels via a rapid, direct solution-based reduction is presented24. Combining various precursor noble metal ions with reducing agents in a 1:1 (v/v) ratio results in the formation of metal gels within seconds to minutes compared to much longer synthesis times for other techniques such as sol-gel. The use of a microcentrifuge tube or small volume conical tube takes advantage of the vigorous hydrogen gas evolution as a by-product of the reduction step facilitating a proposed nucleation, growth, densification, fusion, equilibration model for gel formation. A close correlation in aerogel nanostructure feature sizes is determined with scanning electron microscopy image analysis, X-ray diffractometry, nitrogen gas adsorption, electrochemical impedance spectroscopy, and cyclic voltammetry. The solvent accessible specific surface area is determined with both electrochemical impedance spectroscopy and cyclic voltammetry. This synthesis method for noble metal aerogels demonstrates that high specific surface area monoliths may be achieved with a rapid and direct reduction approach.
CAUTION: Consult all relevant safety data sheets (SDS) before use. Use appropriate safety practices when performing chemical reactions, to include the use of a fume hood and personal protective equipment. Rapid hydrogen gas evolution can cause high pressure in reaction tubes causing caps to pop and solutions to spray out. Ensure that reaction tube caps remain open as specified in the protocol.
1. Metal Gel Preparation
2. Electrochemical Surface Area (ECSA) Characterization of Wet Metal Gels
Note: Electrochemical characterization is performed on wet metal gels prior to conducting freeze drying. The resulting ECSA is then an estimate of the surface of the final aerogel structure. Nitrogen adsorption measurements are used to estimate the surface area of the dried aerogels.
3. Aerogel Preparation and Characterization.
The addition of metal ion and reducing agent solutions together results in solutions immediately turning a dark black color with vigorous gas evolution. Observation of the reaction progress suggests the proposed gel formation mechanism shown in Figure 1. Gel formation proceeds through five steps of 1) nanoparticle nucleation, 2) growth, 3) densification, 4) fusion, and 5) equilibration. The first four steps are observed to occur during the first few minutes of the reaction, with the equilibration fifth step proceeding during the 3-6 h while the gel remains in the reducing agent solution, and continues during the deionized water rinse. Figure 2 shows representative Au, Pd, and Pt aerogels floating on the surface of water indicating a characteristic aerogel hydrophobicity. Pd and Pt gels remained black in color from the initial combination of metal ion and reducing agent solutions, whereas gold gels progressed from black at initial reduction to presenting a red-gold hue during the equilibration phase.
Figure 3 photo images depict wet metal gels after reduction with reducing agent solution replaced with deionized water. A range of metal ion solution concentrations less than the 0.1 M presented in Step 1 of the Protocol section were reduced with the same 0.1 M reducing agent concentrations. For the combinations of HAuCl4•3H2O with DMAB, Na2PdCl4 with NaBH4, and K2PtCl6 (in 50% ethanol) with DMAB, and metal ion concentrations of 5, 10, 25, 50, and 100 mM, gel size was found to decrease with decreasing metal ion concentration. The synthesis method presented here provides the significant advantage of rapid time scales to achieve the aerogel monoliths. However, the final gel size for 0.1 M metal concentrations is seen to be approximately ¼ to ⅓ of the synthesis solution volume. The gel formation mechanism facilitated by rapid hydrogen gas evolution results in fast gel formation, but ultimately results in a lack of shape control for this method.
To test the range of possible gel formation outcomes, various combinations of noble metal ions with three reducing agents were tested using the method presented in Protocol Step 1. The three reducing agents used were DMAB, NaBH4, and sodium hypophosphite (NaH2PO2). All reducing agents were used at 0.1 M concentration. The metal salts used were HAuCl43H2O, Na2PdCl4, Pd(NH3)4Cl2, K2PtCl4, Pt(NH3)4Cl2, and Na2PtCl6. Na2PtCl6 was prepared with deionized water and separately with a 1:1 deionized water to ethanol solvent. Metal ion concentrations were varied across a range of 100, 50, 25, 10, 5, 1, 0.5, and 0.1 mM. Table 1 indicates the minimum metal ion concentration at which gel formation was observed to occur. The metal ions and reducing agent combinations presented in Protocol step 1 resulted in the most reproducible and stable gels. While Au gels formed with the use of NaBH4, gel shapes were more varied and presented a rougher macroscopic surface texture. Pd gels formed with Na2PdCl4 and Pd(NH3)4Cl2 yielded similar results. Stable Pt gels were difficult to achieve using Pt(NH3)4Cl2 and K2PtCl4 likely owing to the thermodynamic stability of the square planar platinum ions. Large gel aggregates formed with Na2PtCl6 prepared in deionized water solvent, whereas the use of Na2PtCl6 prepared in a 1:1 deionized water to ethanol solvent more consistently resulted in monolithic gels. The addition of ethanol as a solvent was based on reports of Pt nanoparticle instability in ethanol to drive particle aggregation and fusion. In general, gel shape became more variable for decreasing precursor salt concentrations for Au, Pd, and Pt.
Scanning electron microscope (SEM) analysis of the gels reveals a hierarchical pore structure for Au, Pd, and Pt aerogels as seen in Figure 4. The range of pore and ligament sizes were determined from SEM image analysis with 200 – 300 measurements for each value. Au aerogels present large macropores with a range of 50 – 600 nm, and smooth ligaments with a diameter range of 18 – 280 nm with an average of 63.7 ± 36.0 nm. Pd and Pt aerogels differ in their structure from Au aerogels, in that they present a "beads-on-a-string" structure with fused nanoparticles. Pd macropores ranged from 50 – 340 nm, with ligament diameters ranging from 12 – 65 nm, with an average of 34.5 ± 9.5 nm. Pt macropores range from 50 – 470 nm, with ligament diameters ranging from 13 – 60 nm, with an average of 29.7 ± 9.0 nm24. The greater range in Pt macropore structure is attributed to Pt nanoparticle stability and the need for ethanol to drive coalescence, and consequent ease of large hydrogen gas bubble evolution during the gel formation process. X-ray diffraction (XRD) spectra from 20 – 70 ° in Figure 5 indicate characteristic peaks for Au, Pd, and Pt aerogels with no detectable oxides.
Nitrogen gas physisorption isotherms are shown for Au, Pd, and Pt aerogels in Figure 6a, 6c, and 6e, and indicate a Type IV isotherm characteristic of mesoporous materials with pores predominantly ranging from 2 – 50 nm28 . The Barrett–Joyner–Halenda (BJH) model for desorption curves was used for Figure 6b, 6d, and 6f to show the cumulative pore volume (cm3/g) and pore size distribution (dV/dd) for Au, Pd, and Pt aerogels with pore sizes in the 2 – 50 nm mesoporous range29 . To determine the aerogel specific surface areas, a multi-point Brunauer-Emmett-Teller (BET) model was used to analyze adsorption isotherms in Figure 6.30 For Au, Pd, and Pt aerogels this resulted in values of 3.06, 15.43, and 20.56 m2/g respectively. Noble metal aerogels synthesized from sol-gels of preformed nanoparticles have achieved similar specific surface areas31. Idealized ligament diameters based on the specific surface areas are 85.4, 33.1, and 13.6 nm for Au, Pd and Pt aerogels and generally correlate to feature sizes determined with SEM image analysis.
Electrochemical impedance spectra for Au, Pd, and Pt gels are shown in Figure 7a. Specific capacitance is plotted as a function of EIS frequency in Figure 7b with estimates of 2.18. 4.13, and 4.20 F/g for Au, Pd, and Pt gels. Based on a nominal 30 µF/cm2 for metal surfaces, Au, Pd, and Pt specific surface areas are 7.27, 13.77, and 14.00 m2/g32. EIS spectra were fit with a transmission line model (TLM) based on a modified Randle's equivalent circuit model shown in Figure 7c. In this model, resistors (R), capacitors (C) or constant phase elements (CPE), and restricted diffusion elements (Zdiff) are connected in parallel and series. Electrolyte resistance and contact resistance with the working electrode at high frequency is represented by R1. Double layer capacitance, charge transfer, material resistance, and restricted ion diffusion through the hierarchically distributed pore network is represented by the parallel arrangement of CPE or C elements with serially connected R and Zdiff33,34. The TLM model effectively modeled EIS spectra for Au, Pd, and Pt gels.
Cyclic voltammetry scans are shown in Figure 8a-8c for Au, Pd, and Pt gels respectively. Using the 1 mV/s CV scan rate, specific capacitances for Au, Pd, and Pt gels were calculated to be 2.67, 7.99, and 5.12 F/g, and using the nominal value of 30 µF/cm2, the same as for EIS capacitances, yields specific surface areas 8.90, 26.63, and 17.07 m2/g.
Reducing Agent | |||
Salt | DMAB | NaBH4 | NaHPO2 |
100 mM | 100 mM | 100 mM | |
[AuCl4]– | 10 mM | 5 mM | No Gel |
[Pd(NH3)4]2+ | 25 mM | 5 mM | No Gel |
[PdCl4]2- | 25 mM | 5 mM | 50 mM |
[Pt(NH3)4]2+ | No Gel | 100 mM | No Gel |
[PtCl4]2- | No Gel | 100 mM | No Gel |
[PtCl6]2- | 25 mM | No Gel | No Gel |
[PtCl6]2- | 10 mM | No Gel | No Gel |
50% EtOH |
Table 1. Concentration thresholds for gel formation for different combinations of salt type and reducing agents. Reproduced from reference 24 with permission.
Figure 1. Proposed mechanism of noble metal gel formation. Synthesis proceeds via (a) initial nucleation of nanoparticles, (b) rapid growth of nanoparticles, (c) densification of nanoparticles due to hydrogen gas evolution, (d) fusion of nanoparticles, and finally (e) surface free energy minimization and equilibration of resulting gel. Reproduced from reference 24 with permission. Please click here to view a larger version of this figure.
Figure 2. (a) Gold, (b) palladium, and (c) platinum aerogels floating on water. Modified from reference 24 with permission. Please click here to view a larger version of this figure.
Figure 3. Noble metal gel synthesis across a range of salt concentrations from right to left of 100, 50, 25, 10, and 5 mM. (a) [AuCl4]– reduced with 100 mM DMAB. (b) [PdCl4]2- reduced with 100 mM NaBH4. (c) [PtCl6]2- prepared in 50% ethanol, reduced with 100 mM DMAB. Modified from reference 24 with permission. Please click here to view a larger version of this figure.
Figure 4. Scanning electron micrographs of (a)-(b) gold, (c)-(d) palladium, and (e)-(f) platinum aerogels. Reproduced from reference 24 with permission. Please click here to view a larger version of this figure.
Figure 5. XRD spectra for platinum (top), palladium (middle), and gold (bottom) aerogels. Modified from reference 24 with permission. Please click here to view a larger version of this figure.
Figure 6. Nitrogen adsorption-desorption isotherms, and pore size distribution with cumulative pore volume for (a)-(b) gold, (c)-(d) palladium, and (e)-(f) platinum aerogels. Reproduced from reference 24 with permission. Please click here to view a larger version of this figure.
Figure 7. (a) Electrochemical impedance spectra for gold, palladium, and platinum gels performed in 0.5 M KCl vs Ag/AgCl reference electrode. (a) (inset) Low frequency EIS spectra from (a). (b) Specific capacitance (Csp) for gels calculated from low frequency EIS spectra in (a). (b) (inset) Low frequency Csp values. (c) RLC fitted transmission line model (TLM) for EIS spectra. Reproduced from reference 24 with permission. Please click here to view a larger version of this figure.
Figure 8. Cyclic voltammetry at scan rates of 50, 25, 10, 5, and 1 mV/s for (a) gold, (b) palladium, and (c) platinum gels. Voltage windows are (a) -0.2 V to 0.2 V, and (b)-(c) 0.1 V to 0.4 V (vs Ag/AgCl). Reproduced from reference 24 with permission. Please click here to view a larger version of this figure.
The noble metal aerogel synthesis method presented here results in the rapid formation of porous, high surface area monoliths that are comparable to slower synthesis techniques. The 1:1 (v/v) metal ion solution to reducing agent solution ratio is critical in facilitating the proposed gel formation model. The rapid hydrogen gas evolution as a by-product of the electrochemical reduction of metal ions serves as a secondary reducing agent and facilitates the densification, and fusion of growing nanoparticles during gel formation. Selection of the optimal combinations of metal ion types and reducing agents is also important given that many synthesis combinations shown in Table 1 do not result in gel formation.
Critical to preserving the gel structure subsequent to chemical reduction is to ensure that gel contact with the solution liquid-air surface is minimized in order to prevent compaction of the gel due to surface tension and capillary forces from water. Extended reduction and rinse times beyond those specified in the protocol may result in further compaction of the metal gels due to continued surface free energy minimization.
The presented synthesis method's primary benefit is the rapid formation of noble metal aerogels with feature sizes commensurate with slower synthesis techniques. The gel feature sizes are achieved without the use of preformed nanoparticles or capping agents during synthesis. Further the experimental correlation of pore and ligament sizes, and surface areas between SEM, XRD, nitrogen gas adsorption, EIS, and CV measurements suggests meaningful and reproducible values.
The protocol may be varied to scale up for the formation of larger aerogels by the use of 15 mL conical tubes with a 3 mL total reaction volume. However, increased reaction volumes are observed to yield increasing variability of final aerogel shape. This increased variability suggests that the aspect ratio of the reaction vessel relative to reaction volume is an important synthesis method consideration. While the primary benefit of the method is rapid gel formation, the lack of shape control reflects the most significant shortcoming for both small and large scale reactions. Future work includes the use of biotemplating and carbon composites as possible approaches to better achieve shape control35,36. As a rationally designed scaffold for metal reduction, biotemplated and composite materials may provide further control over ligament length, diameter, and aerogel shape. The direct and rapid synthesis method presented here offers an advancement in decreasing synthesis steps and times to achieve high specific surface areas, and offers a material approach for energy, catalysis, and sensor applications.
The authors have nothing to disclose.
The authors are grateful to Stephen Steiner at Aerogel Technologies for his inspiration and technical insights, and to Dr. Deryn Chu at the Army Research Laboratory-Sensors and Electron Devices Directorate, Dr. Christopher Haines at the Armament Research, Development and Engineering Center, U.S. Army RDECOM-ARDEC, and Dr. Stephen Bartolucci at the U.S. Army Benet Laboratories for their assistance. This work was supported by a Faculty Development Research Fund grant from the United States Military Academy, West Point.
HAuCl4Ÿ•3H2O | Sigma-Aldrich | 16961-25-4 | |
Na2PdCl4 | Sigma-Aldrich | 13820-40-1 | |
K2PtCl6 | Sigma-Aldrich | 16921-30-5 | |
Pd(NH3)4Cl2 | Sigma-Aldrich | 13933-31-8 | |
K2PtCl4 | Sigma-Aldrich | 10025-99-7 | |
Pt(NH3)4Cl2Ÿ•H2O | Sigma-Aldrich | 13933-31-8 | |
dimethylamine borane (DMAB) | Sigma-Aldrich | 74-94-2 | |
NaBH4 | Sigma-Aldrich | 16940-66-2 | |
NaH2PO2Ÿ•H2O | Sigma-Aldrich | 10039-56-2 | |
Ethanol | Sigma-Aldrich | 792780 | |
Snap Cap Microcentrifuge Tubes, 2.0 mL | Cole Parmer | UX-06333-70 | |
Snap Cap Microcentrifuge Tubes, 1.7 mL | Cole Parmer | UX-06333-60 | |
Conical Centrifuge Tubes 15mL | Stellar Scientific | T15-101 | |
Ag/AgCl Reference Electrode | BASi | MF-2052 | |
Pt wire electrode | BASi | MF-4130 | |
Miccrostop Lacquer | Tober Chemical Division | NA | |
Potentiostat | Biologic-USA | VMP-3 | Electrochemical analysis-EIS, CV |
Freeze Dryer | Labconco | Freezone 2.5 Liter | Aerogel freeze drying |
XRD | PanAlytical | Empyrean | X-ray diffractometry |
Surface and Pore Analyzer | Quantachrome | NOVA 4000e | Nitrogen gas adsorption |
ImageJ, Image analysis software | National Institute of Health | NA | SEM image analysis |