Here we present protocols for preparing and testing catalytic aerogels by incorporating metal species into silica and alumina aerogel platforms. Methods for preparing materials using copper salts and copper-containing nanoparticles are featured. Catalytic testing protocols demonstrate the effectiveness of these aerogels for three-way catalysis applications.
Protocols for preparing and testing catalytic aerogels by incorporating metal species into silica and alumina aerogel platforms are presented. Three preparation methods are described: (a) the incorporation of metal salts into silica or alumina wet gels using an impregnation method; (b) the incorporation of metal salts into alumina wet gels using a co-precursor method; and (c) the addition of metal nanoparticles directly into a silica aerogel precursor mixture. The methods utilize a hydraulic hot press, which allows for rapid (<6 h) supercritical extraction and results in aerogels of low density (0.10 g/mL) and high surface area (200-800 m2/g). While the work presented here focuses on the use of copper salts and copper nanoparticles, the approach can be implemented using other metal salts and nanoparticles. A protocol for testing the three-way catalytic ability of these aerogels for automotive pollution mitigation is also presented. This technique uses custom-built equipment, the Union Catalytic Testbed (UCAT), in which a simulated exhaust mixture is passed over an aerogel sample at a controlled temperature and flow rate. The system is capable of measuring the ability of the catalytic aerogels, under both oxidizing and reducing conditions, to convert CO, NO and unburned hydrocarbons (HCs) to less harmful species (CO2, H2O and N2). Example catalytic results are presented for the aerogels described.
Silica- and alumina-based aerogels have remarkable properties, including low density, high porosity, high surface area, good thermal stability and low thermal conductivity1. These properties render the aerogel materials attractive for a variety of applications1,2. One application that exploits the thermal stability and high surface area of aerogels is heterogeneous catalysis; several articles review the literature in this area2,3,4,5. There are many approaches to the fabrication of aerogel-based catalysts, including incorporation or entrapment of catalytic species within the framework of a silica or alumina aerogel5,6,7,8,9,10,11. The present work focuses on protocols for preparation via rapid supercritical extraction (RSCE) and catalytic testing of aerogel materials for automotive pollution mitigation, and uses copper-containing aerogels as examples.
Three-way catalysts (TWCs) are commonly employed in pollution mitigation equipment for gasoline engines12. Modern TWCs contain platinum, palladium and/or rhodium, platinum-group metals (PGMs) that are rare and, therefore, expensive and environmentally costly to obtain. Catalyst materials based on more readily available metals would have significant economic and environmental advantages.
Aerogels can be prepared from wet gels using a variety of methods1. The goal is to avoid pore collapse as solvent is removed from the gel. The process employed in this protocol is a rapid supercritical extraction (RSCE) method in which the extraction occurs from a gel confined within a metal mold in a programmable hydraulic hot press13,14,15,16. The use of this RSCE process for the fabrication of silica aerogel monoliths has been previously demonstrated in a protocol17, in which the relatively short preparation time associated with this approach was emphasized. Supercritical CO2 extraction is a more common approach, but takes more time and requires greater use of solvents (including CO2) than RSCE. Other groups have recently published protocols for preparation of a variety of types of aerogels utilizing supercritical CO2 extraction18,19,20.
Here, protocols for fabricating and catalytically testing a variety of types of copper-containing catalytic aerogels are presented. Based on the NO reduction and CO oxidation activity ranking of carbon-supported base metal catalysts under conditions of interest to automotive pollution mitigation provided by Kapteijn et al.21, copper was selected as the catalytic metal for this work. Fabrication approaches include (a) impregnation (IMP) of copper salts into alumina or silica wet gels11, (b) using copper(II) and aluminum salts as co-precursors (Co-P) when fabricating copper-alumina aerogels6,22, and (c) entrapping copper-containing nanoparticles into a silica aerogel matrix during fabrication10. In each case, an RSCE method is used for removal of solvent from the pores of the wet gel matrix13,14,15.
A protocol for assessment of the suitability of these materials as TWCs for automotive pollution mitigation, using the Union Catalytic Testbed (UCAT)23, is also presented. The purpose of the UCAT system, key portions of which are shown schematically in Figure 1, is to simulate the chemical, thermal, and flow conditions experienced in a typical gasoline engine catalytic converter. UCAT functions by passing a simulated exhaust mixture over an aerogel sample at a controlled temperature and flow rate. The aerogel sample is loaded into a 2.25-cm-diameter tubular packed bed flow cell ("test section"), which contains the sample between two screens. The loaded flow cell is placed into an oven to control the exhaust gas and catalyst temperature, and samples of treated exhaust (i.e. exhaust flowed through the packed bed) and untreated gas (i.e. bypassing the packed bed) are examined at a range of temperatures up to 700 ˚C. The concentrations of the three key pollutants — CO, NO, and unburned hydrocarbons (HCs) — are measured using a five-gas analyzer after being treated by the aerogel catalyst and, separately, in an untreated ("bypass") flow; from these data the "percent conversion" for each pollutant is calculated. For the testing described herein, a commercially available exhaust blend, California Bureau of Automotive Repair (BAR) 97 LOW emissions blend was employed. Full details of the UCAT's design and functioning are presented in Bruno et al.23
Figure 1. UCAT Test Section and Sampling Systems. Reprinted with permission from 2016-01-0920 (Bruno et al.23), Copyright 2016 SAE International. Further distribution of this material is not permitted without prior permission from SAE. Please click here to view a larger version of this figure.
Safety Considerations: Wear safety glasses or goggles and laboratory gloves at all times when performing preparatory work with chemical solutions and when handling wet gels or catalytic aerogel materials. Handle propylene oxide, tetramethyl orthosilicate (TMOS), ethanol, methanol, ammonia, nanoparticles and solutions containing any of these within a fume hood. Read Safety Data Sheets (SDS) for all chemicals, including nanoparticles, prior to working with them. Wear a particulate mask when crushing aerogel samples and during loading and unloading of the test cell. Wear safety glasses or goggles when operating the hydraulic hot press or catalytic test bed. Tie back long hair and do not wear loose clothing (scarves, for example) when working with the hot press. As noted in our previous protocol17, employ a safety shield around the hot press, properly vent the hot press and make certain that there are no ignition sources nearby. Provide correct ventilation of the test bed and all gas exhausts and. Install NO and CO gas monitors in the operator space associated with the catalytic test bed. Wear oven gloves when removing or replacing a hot test cell.
1. Fabrication of Alumina-Copper Sol Gels using Copper Salts
Note: Recipes for alumina-copper (Al-Cu) sol gels are shown in Table 1. All solution preparations are performed within a fume hood.
2. Fabrication of Silica-Copper Sol Gels using Copper Salts
Note: The recipe for silica-copper (Si-Cu) sol gels is shown in Table 2. All solution preparations are performed within a fume hood.
3. Processing Alumina-Copper and Silica-Copper Sol Gels made using Copper Salts into Aerogels via Rapid Supercritical Extraction
4. Fabrication of Copper-Nanoparticle-Doped Silica Aerogel Monoliths (Si-Cu NP)
5. Operating the Union Catalytic Test Bed
Chemical | Amount (Impregnation Method) | Amount (Co-Precursor Method) |
AlCl3•7H2O | 5.92 g | 4.52 g |
Cu(NO3)2•3H2O | 1.4 g | 1.4 g |
Propylene oxide | 8 mL | 9.5 mL |
Reagent-grade ethanol | 40 mL | 40 mL |
Absolute ethanol | 120 mL | 120 mL |
Table 1. Recipe for Preparation of Alumina-Copper Sol Gels.
Chemical | Amount (Impregnation Method) |
TMOS | 8.5 mL |
MeOH | 27.5 mL |
H2O | 3.6 mL |
1.5-M NH3 | 1.35 mL |
Absolute Ethanol | 60 mL |
Cu(NO3)2•3H2O | 0.55 g |
Table 2. Recipe for Preparation of Silica-Copper Sol Gels.
Step # | Temperature (°C) | Temp Rate (°C/min) | Force (kN) | Force Rate (kN/min) | Dwell Time (min) |
1 | 30 | 300 | 200 | 3000 | 0.25 |
2 | 250 | 2.2 | 200 | — | 30 |
3 | 250 | — | 4.5 | 4.5 | 15 |
4 | 30 | 2.2 | 4.5 | — | 1 |
5 | END |
Table 3. Hot-Press Extraction Program Parameters for Alumina-Copper and Silica-Copper Sol Gels.
Step # | Temperature (°C) | Temp Rate (°C/min) | Force (kN) | Force Rate (kN/min) | Dwell Time (min) |
1 | OFF | — | 90 | 3000 | 10 |
2 | END |
Table 4. Hot-Press Sealing Program Parameters.
Step # | Temperature (°C) | Temp Rate (°C/min) | Force (kN) | Force Rate (kN/min) | Dwell Time (min) |
1 | 30 | 300 | 180 | 3000 | 0.25 |
2 | 290 | 1.6 | 180 | — | 30 |
3 | 290 | — | 4.5 | 4.5 | 15 |
4 | 40 | 1.6 | 4.5 | — | 1 |
5 | END |
Table 5. Hot-Press Extraction Program Parameters for Copper-nanoparticle-doped Silica aerogels.
Chemical | Amount (mL) | Amount (g) |
TMOS | 12.75 | 13.04 |
Methanol | 41.25 | 32.63 |
Water | 3.9 | 3.9 |
Nanodispersion | 1.5 | 1.5 |
Ammonia | 0.2 | 0.15 |
Table 6. Recipe for Fabrication of 5 wt% Copper-nanoparticle-doped Silica Aerogels.
Photographic images of the resulting aerogels are presented in Figure 2. Because the wet gels were broken into pieces prior to solvent exchange, the Al-Cu IMP and Si-Cu IMP aerogels are in small, irregularly shaped monolithic pieces. It is clear from the coloration of these samples that the aerogels contain copper species and that variations in copper speciation and/or ligand structure occur within the materials. Al-Cu IMP aerogels (Figure 2a) appear red to green-gray in color11. Al-Cu CoP aerogels (not shown) are green to green-gray in color. Si-Cu IMP aerogels have a mottled appearance, with red, yellow and green colors observed (Figure 2b). Si-Cu NP aerogels are monolithic with colors that vary with weight percent of nanoparticle and also vary from well to well in the mold, indicating some variation in processing conditions experienced at different locations in the mold.10 For example, Si-Cu NP aerogel monoliths prepared from the Cu+2 dispersion at 3 wt%, and processed in the same batch, are yellow, purple, pink (Figure 2c) and green (not shown).
Table 7 lists representative physical characteristics of the as-prepared copper-containing aerogels. For the Si-Cu NP aerogels the surface area decreases as the weight percent of nanoparticles increases, as described in Anderson et al.10
Evidence of entrapment of copper in the aerogels is shown in the SEM/EDX images of Figure 3 and the XRD patterns of Figure 4. Figures 3a and 3b show SEM/EDX images of the Si-Cu NP aerogel prepared using the Cu+2 nanodispersion. A ca. 400-nm-diameter nanoparticle containing copper is shown, indicating that some agglomeration of the 25- to 55-nm nanoparticles in the original nanodispersion has occurred. Figure 3c shows smaller (ca. 50 nm) nanoparticles dispersed in the Al-Cu IMP aerogel.
The XRD patterns of the as-prepared Si-Cu IMP and Si-Cu NP aerogels (Figure 4, lower traces) contain peaks corresponding to metallic copper at 2θ = 43, 50 and 74°, indicating that alcohothermal reduction of the copper species occurred during RSCE processing of the gels10,11. The as-prepared Al-Cu IMP aerogel pattern (Figure 4, top trace) shows XRD peaks consistent with the pseudoboehmite form of alumina and a copper(II)-containing species11. After heat treatment above 700 °C, all of these copper-containing aerogels have XRD peaks (not shown) indicative of copper(II) oxide10,11.
The data in Figure 5 show that the copper-containing alumina aerogels are capable of catalyzing reactions that can eliminate each of the three major pollutants of concern in gasoline engine exhaust (CO, NO, and HCs) under the conditions tested11. Figure 6 demonstrates the catalytic ability in copper-containing silica aerogels10,11 and thereby provides evidence that the catalytic capabilities of metal-doped aerogels are robust (i.e. activity is demonstrated with the active copper species included in more than one aerogel matrix) and tailorable. The catalytic activity appears to depend on the details of the copper (speciation, particle size, loading level, etc.), how copper is introduced to the aerogel (impregnation, co-precursor, doping with copper nanoparticles) and the underlying aerogel itself (i.e. silica vs. alumina). The details of how these parameters and interactions affect catalytic performance are not yet well understood, but they do indicate that there is a significant "design space" for tailoring aerogel catalysts to specific functions, and that this is a rich area for future work. Further discussion of these results can be found in previously published work10,11,23.
Aerogel | Density (g/mL) | Surface Area (m2/g) |
Cu-Si Imp | 0.11 | 780 ± 50 |
Cu-Al Imp | 0.09 – 0.11 | 390 – 430 |
Si-Cu NP | 0.08 – 0.10 | 200 – 500 |
Table 7. Representative Physical Characterization Data for the As-prepared Aerogels.
Figure 2. Photographic images of copper-containing aerogels. (a) Al-Cu IMP; (b) Si-Cu IMP; (c) Si-Cu NP (made from 3 wt% Cu+2). Note that variations in color occur within aerogels fabricated in the same batch. Please click here to view a larger version of this figure.
Figure 3. SEM micrographs of as-prepared aerogels. (a) EDX backscattering image of 3 Si-Cu NP (made from 3 wt% Cu+2) (scale bar in bottom right corner: 800 nm); (b) EDX image of Cu signal for sample as in (a) (scale bar in bottom right corner: 800 nm); (c) SEM image of Al-Cu IMP aerogel (scale bar in bottom left corner: 200 nm). All images taken at 50kX magnification. Figures 3a and 3b have been reprinted from Anderson et al.10 Figure 3c has been reprinted from Tobin et al.11 Please click here to view a larger version of this figure.
Figure 4. XRD patterns of as-prepared aerogels. The Al-Cu IMP aerogel shows evidence of pseudoboehmite (B) and crystals of a copper(II) salt (X). Both types of Si-Cu aerogels (IMP and NP) show evidence of metallic copper (Cu). Note the x-axis scale represents reflected beam for data collected using a copper X-ray source tube; y-axis scale not indicated because patterns are offset for clarity. This figure has been modified from Anderson et al.10 and Tobin et al.11 Please click here to view a larger version of this figure.
Figure 5. Conversion of HCs, NO and CO for a copper-containing alumina aerogel prepared via the impregnation method. (a) In the absence of oxygen (300 ppm NO, 0.5% CO, 6.0% CO2 200 ppm propane for HC) and (b) in the presence of oxygen (0.36% O2, 295 ppm NO, 0.49% CO, 5.9% CO2 197 ppm propane for HC). Tests were performed using a space velocity of 20 s-1. Error bars represent the standard deviation in five runs. Lines are included as an aid to the eye. Shaded regions (pink for NO, green-brown for CO on left; blue for HC and green-gray for CO on right) indicate the conversion activity measured for an inert (silica) aerogel. This figure is reprinted from Tobin et al.11 Please click here to view a larger version of this figure.
Figure 6. Conversion of NO and CO for copper-nanoparticle-doped silica aerogels. (a) In the absence of oxygen (300 ppm NO, 0.5% CO, 6.0% CO2 200 ppm propane for HC) and (b) in the presence of oxygen (0.36% O2, 295 ppm NO, 0.49% CO, 5.9% CO2 197 ppm propane for HC). Tests were performed using a space velocity of 20 s-1.Three different types of nanoparticles were employed (Cu0, Cu+1, Cu+2) with weight percent as noted in legend. Data for unmodified silica aerogel and Si-Cu IMP aerogels are also included from Tobin et al.11 for comparison. Error bars represent the standard deviation of 2 or 3 runs. Lines are included as an aid to the eye. This figure is reprinted from Anderson et al.10
The utility of the RSCE method for fabrication of catalytic aerogels and the UCAT system for demonstrating catalytic ability has been demonstrated herein. Major advantages of these protocols over other methods are the speed of RSCE aerogel fabrication and the relatively inexpensive approach to catalytic testing by UCAT.
Gels to be extracted can be prepared via a variety of methods, including impregnation of metal salts into an alumina or silica wet gel matrix, inclusion of metal salts as co-precursors with aluminum salts, and incorporation of metal-containing nanoparticles into silica aerogels. When the wet gel pores contain only alcohol and water (i.e. silica protocols), solvent exchange is not required. In that case, the liquid precursor mixture can be poured directly into the metal mold, with gelation and extraction both occurring during the hot-press process, as demonstrated previously in Carroll et al.17 and in this protocol for Si-Cu NP aerogels. We use a somewhat longer hot press process to ensure gelation occurs in the mold prior to extraction. In this approach, a recipe that would gel under ambient conditions in <4 h is desirable. Alternately, the RSCE method can be used to extract solvent from pre-gelled monolithic samples6,11 or smaller pieces of gel, as in the Si-Cu IMP, Al-Cu IMP and Al-Cu CoP sol gels in this protocol.
As noted in previous publications16,17, appropriately setting the restraining force supplied to the metal mold is very important to successful RSCE; this force must be adjusted depending on the mold size and shape. Each hot press has a maximum restraining force, which will limit the achievable volume of aerogel per extraction. Gels and solvents suitable for the RSCE process are limited to those that can withstand the temperature and pressure (T/P) conditions employed and do not react with either the metal mold or gasket materials. In addition, the T/P conditions must bring the solvent(s) in the gel above the critical point, or collapsed gels will be formed rather than aerogels. Because of the lack of shrinkage in the RSCE process, open-bottom molds are used to fabricate monoliths. Sealing an open-bottom mold is required to prevent leakage of precursor mixture onto the hot press platens. A closed-bottom mold is recommended for ease of use if intact monoliths are not needed for the end application.
Approaches in which nanoparticles are included in the precursor mixture for a base-catalyzed reaction of silica alkoxide precursors yield monolithic aerogels in a process that requires only 8 h from mixing the chemicals to removal of the aerogels from the mold10,17. This is considerably shorter than the total time of preparation of aerogels by supercritical CO2 extraction (including gel formation, solvent exchanges over a multiple-day period, processing). The processing time can be shortened to as little as 3 h by increasing the heating and cooling rates employed in the hot press program24. Use of an impregnation approach, as in the Al-Cu IMP gels demonstrated in this protocol, requires at least one solvent exchange, and thereby lengthens the overall time needed for aerogel fabrication. The epoxide-assisted method for preparing gels from salts22 requires multiple solvent exchanges prior to processing, in order to remove excess epoxide and byproducts of the reaction6. Consequently, although the time needed for mixing and gelation is short (< 1 h) and RSCE can be accomplished in 5 h, the overall time for making the alumina-based aerogels described in this protocol is extended over several days.
Although this protocol has focused on the preparation of copper-containing aerogels, these methods can be used to incorporate a wide variety of metal-containing species, including nanoparticles, into alumina- or silica-based aerogels7,8,9. When employing suspensions of nanoparticles, settling of the nanoparticles within the precursor mixture may result in non-uniform distribution in the resulting aerogel material. Moreover, variations in colors of materials obtained in a single batch of aerogel indicate that subtle changes in conditions are sometimes experienced by a gel during processing, for example, in different positions within the metal mold. In the case of copper-containing species, significant changes in copper oxidation state and ligand structure occur during processing10,11, which merits further study.
The UCAT system23 allows for testing of catalytic aerogels under conditions that approximate those encountered in an automotive catalytic converter without requiring laboratory use of an automobile and sophisticated, expensive commercial test equipment. The cost of construction of UCAT was approximately $75k. Detection is limited to those gases detectable by the five-gas analyzer (CO, CO2, NO, O2, HCs), which does not provide a complete assessment of reaction products. When operated under the conditions demonstrated in this protocol, catalyst performance under reducing and oxidizing conditions can be assessed. Ongoing work focuses on adding capabilities to UCAT to permit testing under more varied conditions, including humidification and transient exhaust mixtures.
The authors have nothing to disclose.
Development of the synthesis methods for catalytic aerogels was funded through National Science Foundation (NSF) grant No. DMR-1206631. The design and construction of UCAT was funded through NSF grant No. CBET-1228851. Additional funding was provided by the Union College Faculty Research fund. The authors would also like to acknowledge the contributions of Zachary Tobin, Aude Bechu, Ryan Bouck, Adam Forti, and Vinicius Silva.
Variable micropipettor, 100-1000 µL | Manufactured by Eppendorf, purchased from Fisher Scientific www.fishersci.com | S304665 | Any 100-1000 µL pipettor is suitable. |
Variable Pipettor, 2.5-10 mL | Manufactured by Eppendorf, purchased from Fisher Scientific www.fishersci.com | 21-379-25 | Any variable pipettor is suitable. |
Pasteur pipettes | FisherScientific | 13-678-6A | |
Syringe | Purchased from Fisher Scientific | Z181390 syringe with Z261297 needle | |
Digital balance | OHaus Explorer Pro | Any digital balance is suitable. | |
Beakers | Purchased from Fisher Scientific | Any glass beaker is suitable. | |
Graduated Cylinder | Purchased from Fisher Scientific | Any glass graduated cylinder is suitable. | |
Magnetic Plate/Stirrer | FisherScientific Isotemp | SP88854200P | Any magnetic plate/stirrer is suitable. |
Ultrasonic Cleaner | FisherScientific FS6 | 153356 | Any sonicator is suitable. |
Mold | Fabricated in House | Fabricate from cold-rolled steel or stainless steel. | |
Hydraulic Hot Press | Tetrahedron www.tetrahedronassociates.com | MTP-14 | Any hot press with temperature and force control will work. Needs maximum temperature of ~550 F and maximum force of 24 tons. |
UCAT (Union Catalytic Testbed) | Fabricated in House | Described in detail in reference #21: Bruno, B.A., Anderson, A.M., Carroll, M.K., Brockmann, P., Swanton, T., Ramphal, I.A., Palace, T. Benchtop Scale Testing of Aerogel Catalysts. SAE Technical Paper 2016-01-920 (2016). | |
Bar 97 Gas | Praxair | MS_BAR97ZA-D7 |