Catalytically Active Aerogel Material for Automotive ... · is relatively easy to incorporate a...

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/ muse.union.edu/aerogels Catalytically Active Aerogel Material for Automotive Exhaust Mitigation Applications Bradford A. Bruno 1 , Ann M. Anderson 1 , and Mary K. Carroll 2 Department of Mechanical Engineering 1 & Department of Chemistry 2 Union College, Schenectady NY Abstract Potential Aerogel Advantages Results and Discussion Background Future Work Aerogels are high surface area, low density, low thermal mass, nanoporous materials that are stable at high temperatures. Due to this unique combination of properties, aerogels have potential applications in a range of areas including sensing, insulation, comet dust collection, and catalysis. We have developed a series of catalytically active aerogels which show activity as three-way catalysts. These materials are fabricated using a rapid supercritical extraction method [1]. It is relatively easy to incorporate a variety of metals, including non-PGM metals such as nickel [2], copper [3] and cerium [4] into a silica- or alumina-based backbone. Through use of the Union Catalytic Aerogel Testbed, UCAT, an in- house designed catalytic test system [5], we have demonstrated that these materials have three-way catalytic ability. UCAT tests catalytic material performance for conversion of NO, UHCs and CO over a range of temperatures from 200-700 C using customizable simulated exhaust gas mixtures. Aerogels can be readily tailored for catalytic activity by combining a catalytically active metal species with an aerogel support matrix. The aerogel structure consists of nanoscale-sized spherical clusters linked together in chains, ultimately forming an amorphous spatial grid with air-filled pores on the order of tens of nanometers. This nanostructure can be tailored to fit a specific activity through control of synthesis and processing conditions. We have developed methods for making a variety of catalytic aerogels (see Figs 1-3) using the patented Union College rapid supercritical extraction (RSCE) method. To date several candidate catalytic aerogels have undergone performance screening tests in UCAT. These include: cobalt-alumina aerogels (Figure 5), nickel-alumina aerogels [2], several types of coper- silica and copper-alumina aerogels [3] (e.g. Figure 6), ceria-alumina and ceria-silica aerogels [4] as well as “neat” alumina and silica aerogels (which are largely inert). Figure 5: Cobalt-alumina aerogel (~3 mol%) steady-state UHC, NO, and CO conversion versus temperature when exposed to: a) BAR 97 exhaust blend without oxygen, b) BAR 97 exhaust blend with oxygen. Data points represent the average of three runs with error bars representing ±1 standard deviation. (reprinted from SAE 2016-01 0920) Figure 6 illustrates that higher copper loading in copper-alumina (Cu-Al) aerogels decreases the light-off temperature. The 8g, 4g, and 2g samples were manufactured via a copper impregnation method [3] where 8g, 4g and 2g refer to the amount of copper salt used in the first solvent exchange which affects how much copper is impregnated into the aerogel, but the response is not linear. Analysis determined that actual Cu concentrations in the 4g and 8g aerogels are similar, but higher than the 2g aerogels. This explains why the 4g and 8g Cu-Al aerogels have comparable performance and both are more efficient than the 2g Cu-Al aerogel. As expected, all the Cu-Al aerogels perform betters than an inert silica aerogel. Figure 6: Average percent conversion for copper-alumina aerogels, with varying amounts of copper impregnated in the aerogel. The mass refers to the amount of copper salt in the first solvent exchange. Inert refers to a silica aerogel that has no copper in it. The graphs illustrate that aerogels with higher copper levels are better three-way catalysts. All tests conducted with BAR 97 based exhaust blends. References and Acknowledgements 1. Gauthier, B. M., Bakrania, S. D., Anderson, A. M., & Carroll, M. K. (2004). A fast supercritical extraction technique for aerogel fabrication. Journal of Non- Crystalline Solids, 350, 238-243. 2. Juhl, S. J., Dunn, N. J., Carroll, M. K., Anderson, A. M., Bruno, B. A., Madero, J. E., & Bono Jr, M. S. (2015). Epoxide-assisted alumina aerogels by rapid supercritical extraction. Journal of Non-Crystalline Solids, 426, 141-149. 3. Tobin, Z. M., Posada, L. F., Bechu, A. M., Carroll, M. K., Bouck, R. M., Anderson, A. M., & Bruno, B. A. (2017). Preparation and characterization of copper- containing alumina and silica aerogels for catalytic applications. Journal of Sol-Gel Science and Technology, 84(3), 432-445. 4. Posada, L. F., Carroll, M. K., Anderson, A. M., & Bruno, B. A. (2019). Inclusion of Ceria in Alumina-and Silica-Based Aerogels for Catalytic Applications. The Journal of Supercritical Fluids. in Press, https://doi.org/10.1016/j.supflu.2019.05.004 . 5. Bruno, B. A., Anderson, A. M., Carroll, M., Swanton, T., Brockmann, P., Palace, T., & Ramphal, I. A. (2016). Benchtop scale testing of aerogel catalysts: preliminary results (No. 2016-01-0920). SAE Technical Paper. 6. The Advanced Combustion and Emission Control (ACEC) Technical Team, “Aftertreatment Protocols for Catalyst Characterization and Performance Evaluation: Low-Temperature Three-Way Catalyst Test Protocol”, Crosscut Lean Exhaust Emissions Reduction Simulations We acknowledge support from the National Science Foundation (NSF) through NSF 1823899 I-Corps grant and NSF CBET 1228851 MRI grant for funding development of UCAT. We also thank Matthew LaRosa, Chris O’Brien and Ryan Puglisi for assistance with running UCAT tests, and Thomas Andre and Xiao Peng Li for synthesizing the catalytic aerogel samples for testing. Future studies will focus on development and testing of higher performance catalytic aerogels with the goal of replacing traditional TWC catalysts. Candidate aerogels will be fabricated containing different catalyst species, using nanoparticle metal species, and with combinations of several metal species. Additionally, an improved exhaust blend based on US Drive recommendations [6] will be utilized in future tests. Bottled Simulated Exhaust Mix Gas Control System Exhaust Sample line to Five Gas Analyzer (one per test cell) Test Cell Bypass Lines Test Sections Oven 0 10 20 30 40 50 60 70 80 90 100 150 250 350 450 550 650 HC % Conversion (with air) Temperature (°C ) 8g 4g 2g Inert -20 -10 0 10 20 30 40 50 60 70 80 90 100 150 250 350 450 550 650 NO % Conversion (no air) Temperature (°C ) 8g 4g 2g Inert 0 10 20 30 40 50 60 70 80 90 100 150 250 350 450 550 650 CO % Conversion (with air) Temperature (°C ) 8g 4g 2g Inert Cu-Al Cu-Si Cu-Si (NP) Ce-Cu-Al Ce-Al Figure 1. Catalytic aerogel synthesis method. Chemical processing (left) and RSCE (right). Figure 2. Images of various catalytic aerogels fabricated through RSCE. Figure 3. SEM (left) and EDX (right) micrographs of Cu-Al aerogels show evidence of formation of copper-containing nanoparticles. Figure 4: Flow chart depicting the relations between the numerous subsystems that comprise the UCAT. The Union Catalytic Aerogel Testbed (UCAT, shown in in Figure 4) is designed to test the potential of catalytic aerogels to act as three-way catalysts [5]. UCAT is designed to work with small (15 - 25 mL), easily manufactured quantities of candidate aerogels. Aerogel catalyst performance (i.e. pollutant conversion efficiency) can be measured over a range of temperatures (150°C - 800°C), bulk space velocities (15 - 35 1/s) and exhaust chemistries (i.e. rich / lean, dry / humidified, various initial concentrations of NO, CO, CO 2, H 2 ,O 2 , and UHC simulant (e.g. propane, propene, etc.). The primary analytical capability of the UCAT is provided by conventional five-gas analyzers (one per test cell, Infrared Industries FGA-4000XDS). It has two test cells to increase experimental throughput. Typical UCAT testing protocol: A measured volume and mass of aerogel catalyst is placed into a UCAT test cell, typically as a packed bed of aerogel monolith “chunks” (see Figure 2). The oven is set to a desired test temperature and a flow rate is selected to provide the desired bulk space velocity through the sample. Shop air is passed over the sample until steady state temperature conditions are reached, at which point the warm up air is stopped and the selected simulated emissions mix flow is started. Recipes for these blends are provided in Table 1. Pollutant concentrations are measured with the five-gas analyzer, first with the emission blend bypassing the sample, next with the emissions blend flowing through the sample, and then again with the blend bypassing the sample. In all cases care is taken to ensure that sufficient time is provided for the five-gas analyzer readings to reach steady state. Exhaust Legacy California BAR 97 Low Based Mixes New US Drive Based Mixes Component BAR 97L BAR 97L + O 2 US Drive Recommended [6] US Drive HC Modified NO (ppm) 300 295 1000 1000 UHC (ppm) Propane, 200 Propane, 197 Ethene, 525 Propene, 500 Propane, 150 Propene, 1000 CO (%) 0.5 0.49 0.5 0.5 H 2 (%) 0 0 0.17 0.17 CO 2 (%) 6% 5.9% 13 13 H 2 O (%) 0 0 13 13 O 2 (%) 0 3.6% 0.12-1.15 0.12-1.15 Table 1. Simulated emissions blend used in UCAT Testing. a b Union Catalytic Aerogel Testbed High Surface Area: More active sites Improved gas/solid interaction High Thermal Stability: Close coupling Reduced active site diffusion/sintering Chemically Tailorable: PGM reduction or elimination Low Thermal Inertia: Reduced time to light-off temperature

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/muse.union.edu/aerogels

Catalytically Active Aerogel Material for Automotive Exhaust Mitigation Applications

Bradford A. Bruno1, Ann M. Anderson1, and Mary K. Carroll2Department of Mechanical Engineering1 & Department of Chemistry2

Union College, Schenectady NY

Abstract Potential Aerogel Advantages Results and Discussion

Background

Future Work

Aerogels are high surface area, low density, low thermal mass, nanoporousmaterials that are stable at high temperatures. Due to this unique combination ofproperties, aerogels have potential applications in a range of areas includingsensing, insulation, comet dust collection, and catalysis. We have developed aseries of catalytically active aerogels which show activity as three-way catalysts.These materials are fabricated using a rapid supercritical extraction method [1]. Itis relatively easy to incorporate a variety of metals, including non-PGM metalssuch as nickel [2], copper [3] and cerium [4] into a silica- or alumina-basedbackbone. Through use of the Union Catalytic Aerogel Testbed, UCAT, an in-house designed catalytic test system [5], we have demonstrated that thesematerials have three-way catalytic ability. UCAT tests catalytic materialperformance for conversion of NO, UHCs and CO over a range of temperaturesfrom 200-700 C using customizable simulated exhaust gas mixtures.

Aerogels can be readily tailored for catalytic activity by combining a catalyticallyactive metal species with an aerogel support matrix. The aerogel structure consists of nanoscale-sized spherical clusters linked

together in chains, ultimately forming an amorphous spatial grid with air-filledpores on the order of tens of nanometers.

This nanostructure can be tailored to fit a specific activity through control ofsynthesis and processing conditions.

We have developed methods for making a variety of catalytic aerogels (seeFigs 1-3) using the patented Union College rapid supercritical extraction(RSCE) method.

To date several candidate catalytic aerogels have undergone performance screeningtests in UCAT. These include: cobalt-alumina aerogels (Figure 5), nickel-aluminaaerogels [2], several types of coper- silica and copper-alumina aerogels [3] (e.g.Figure 6), ceria-alumina and ceria-silica aerogels [4] as well as “neat” alumina andsilica aerogels (which are largely inert).

Figure 5: Cobalt-alumina aerogel (~3 mol%) steady-state UHC, NO, and CO conversion versus temperaturewhen exposed to: a) BAR 97 exhaust blend without oxygen, b) BAR 97 exhaust blend with oxygen. Data pointsrepresent the average of three runs with error bars representing ±1 standard deviation. (reprinted from SAE2016-01 0920)

Figure 6 illustrates that higher copper loading in copper-alumina (Cu-Al) aerogelsdecreases the light-off temperature. The 8g, 4g, and 2g samples were manufacturedvia a copper impregnation method [3] where 8g, 4g and 2g refer to the amount ofcopper salt used in the first solvent exchange which affects how much copper isimpregnated into the aerogel, but the response is not linear. Analysis determined thatactual Cu concentrations in the 4g and 8g aerogels are similar, but higher than the 2gaerogels. This explains why the 4g and 8g Cu-Al aerogels have comparableperformance and both are more efficient than the 2g Cu-Al aerogel. As expected, allthe Cu-Al aerogels perform betters than an inert silica aerogel.

Figure 6: Average percent conversion for copper-alumina aerogels, with varying amounts of copperimpregnated in the aerogel. The mass refers to the amount of copper salt in the first solvent exchange. Inertrefers to a silica aerogel that has no copper in it. The graphs illustrate that aerogels with higher copper levelsare better three-way catalysts. All tests conducted with BAR 97 based exhaust blends.

References and Acknowledgements 1. Gauthier, B. M., Bakrania, S. D., Anderson, A. M., & Carroll, M. K. (2004). A fast supercritical extraction technique for aerogel fabrication. Journal of Non-

Crystalline Solids, 350, 238-243.2. Juhl, S. J., Dunn, N. J., Carroll, M. K., Anderson, A. M., Bruno, B. A., Madero, J. E., & Bono Jr, M. S. (2015). Epoxide-assisted alumina aerogels by rapid

supercritical extraction. Journal of Non-Crystalline Solids, 426, 141-149.3. Tobin, Z. M., Posada, L. F., Bechu, A. M., Carroll, M. K., Bouck, R. M., Anderson, A. M., & Bruno, B. A. (2017). Preparation and characterization of copper-

containing alumina and silica aerogels for catalytic applications. Journal of Sol-Gel Science and Technology, 84(3), 432-445.4. Posada, L. F., Carroll, M. K., Anderson, A. M., & Bruno, B. A. (2019). Inclusion of Ceria in Alumina-and Silica-Based Aerogels for Catalytic Applications. The

Journal of Supercritical Fluids. in Press, https://doi.org/10.1016/j.supflu.2019.05.004.5. Bruno, B. A., Anderson, A. M., Carroll, M., Swanton, T., Brockmann, P., Palace, T., & Ramphal, I. A. (2016). Benchtop scale testing of aerogel catalysts:

preliminary results (No. 2016-01-0920). SAE Technical Paper.6. The Advanced Combustion and Emission Control (ACEC) Technical Team, “Aftertreatment Protocols for Catalyst Characterization and Performance Evaluation:

Low-Temperature Three-Way Catalyst Test Protocol”, Crosscut Lean Exhaust Emissions Reduction Simulations

We acknowledge support from the National Science Foundation (NSF) through NSF 1823899 I-Corps grant and NSF CBET 1228851 MRI grant for funding development of UCAT. We also thank Matthew LaRosa, Chris O’Brien and Ryan Puglisi for assistance with running UCAT tests, and Thomas Andre and Xiao Peng Li for synthesizing the catalytic aerogel samples for testing.

Future studies will focus on development and testing of higher performancecatalytic aerogels with the goal of replacing traditional TWC catalysts. Candidateaerogels will be fabricated containing different catalyst species, using nanoparticlemetal species, and with combinations of several metal species. Additionally, animproved exhaust blend based on US Drive recommendations [6] will be utilized infuture tests.

Bottled Simulated Exhaust Mix

Gas Control System

Exhaust

Sample line toFive Gas Analyzer(one per test cell)

Test Cell Bypass Lines

Test Sections

Oven

0

10

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HC

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onve

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n (w

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ir)

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8g

4g

2g

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-20-10

0102030405060708090

100

150 250 350 450 550 650

NO

% C

onve

rsio

n (n

o ai

r)

Temperature (°C )

8g

4g

2g

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% C

onve

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n (w

ith a

ir)

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8g4g2gInert

Cu-Al Cu-Si Cu-Si (NP) Ce-Cu-Al Ce-Al

Figure 1. Catalytic aerogel synthesis method. Chemical processing (left) and RSCE (right).

Figure 2. Images of various catalytic aerogels fabricated through RSCE.

Figure 3. SEM (left) and EDX (right) micrographs of Cu-Al aerogels show evidence of formation of copper-containing nanoparticles.

Figure 4: Flow chart depicting the relations between the numerous subsystems that comprise the UCAT.

The Union Catalytic Aerogel Testbed (UCAT, shown in in Figure 4) is designed to test thepotential of catalytic aerogels to act as three-way catalysts [5]. UCAT is designed to work withsmall (15 - 25 mL), easily manufactured quantities of candidate aerogels. Aerogel catalystperformance (i.e. pollutant conversion efficiency) can be measured over a range of temperatures(150°C - 800°C), bulk space velocities (15 - 35 1/s) and exhaust chemistries (i.e. rich / lean, dry /humidified, various initial concentrations of NO, CO, CO2, H2, O2, and UHC simulant (e.g.propane, propene, etc.). The primary analytical capability of the UCAT is provided by conventionalfive-gas analyzers (one per test cell, Infrared Industries FGA-4000XDS). It has two test cells toincrease experimental throughput.

Typical UCAT testing protocol: A measured volume and mass of aerogel catalyst is placedinto a UCAT test cell, typically as a packed bed of aerogel monolith “chunks” (see Figure 2). Theoven is set to a desired test temperature and a flow rate is selected to provide the desired bulkspace velocity through the sample. Shop air is passed over the sample until steady statetemperature conditions are reached, at which point the warm up air is stopped and the selectedsimulated emissions mix flow is started. Recipes for these blends are provided in Table 1.Pollutant concentrations are measured with the five-gas analyzer, first with the emission blendbypassing the sample, next with the emissions blend flowing through the sample, and then againwith the blend bypassing the sample. In all cases care is taken to ensure that sufficient time isprovided for the five-gas analyzer readings to reach steady state.

Exhaust

Legacy California BAR 97 Low Based Mixes New US Drive Based MixesComponent BAR 97L BAR 97L + O2 US Drive

Recommended [6]US Drive

HC ModifiedNO (ppm) 300 295 1000 1000

UHC (ppm) Propane, 200 Propane, 197Ethene, 525

Propene, 500Propane, 150

Propene, 1000

CO (%) 0.5 0.49 0.5 0.5H2 (%) 0 0 0.17 0.17CO2 (%) 6% 5.9% 13 13H2O (%) 0 0 13 13O2 (%) 0 3.6% 0.12-1.15 0.12-1.15

Table 1. Simulated emissions blend used in UCAT Testing.

a b

Union Catalytic Aerogel Testbed

High Surface Area:• More active sites• Improved gas/solid interaction

High Thermal Stability:• Close coupling• Reduced active site diffusion/sintering

Chemically Tailorable:• PGM reduction or elimination

Low Thermal Inertia:• Reduced time to light-off temperature