Nicholas C. Nelson’s research while affiliated with Pacific Northwest National Laboratory and other places

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Publications (5)


rWGS reaction rate as a function of time. Conditions: T=400 °C; CO2:4 H2:5 He; flow rate=10 mL min⁻¹.
a) CO probe molecule IR spectroscopy with λmax and fwhm values corresponding to the primary peak. Additional IR spectra can be found in Figure S4. b–d) Pd cross‐sections for Pd/TiO2‐0.01 (b), Pd/TiO2‐0.1 (c), and precatalyst (d). STEM images can be found in Figure S5.
a) rWGS reaction rate as a function of time. Conditions: T=400 °C; CO2:4 H2:5 He; flow rate=10 mL min⁻¹. b) CO probe molecule IR spectroscopy of Pd/TiO2‐0.01 after 92 h TOS.
Pd K‐edge XAS of the precatalyst, Pd/TiO2‐0.1, Pd/TiO2‐0.01, and reference materials. a) Fourier transform magnitudes of k²‐weighted EXAFS in R‐space (non‐phase corrected) with first‐shell fittings (solid line). Fitting parameters are reported in Table S1. b) XANES region after normalization.
a) IR spectrum of Pd/TiO2‐0.01 recorded at 300 °C under steady‐state rWGS conditions. The prominent band in each spectrum is gas‐phase CO2. b) Mass spectrum of ¹²CO and ¹³CO recorded during isotopic switching (¹²CO2/H2/He/Ar to ¹³CO2/H2/He) at 300 °C.
In Situ Dispersion of Palladium on TiO2 During Reverse Water–Gas Shift Reaction: Formation of Atomically Dispersed Palladium
  • Article
  • Publisher preview available

August 2020

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39 Reads

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87 Citations

Nicholas C. Nelson

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Linxiao Chen

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Debora Meira

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The application of single‐atom catalysts (SACs) to high‐temperature hydrogenation requires materials that thermodynamically favor metal atom isolation over cluster formation. We demonstrate that Pd can be predominantly dispersed as isolated atoms onto TiO2 during the reverse water–gas shift (rWGS) reaction at 400 °C. Achieving atomic dispersion requires an artificial increase of the absolute TiO2 surface area by an order of magnitude and can be accomplished by physically mixing a precatalyst (Pd/TiO2) with neat TiO2 prior to the rWGS reaction. The in situ dispersion of Pd was reflected through a continuous increase of rWGS activity over 92 h and supported by kinetic analysis, infrared and X‐ray absorption spectroscopies and scanning transmission electron microscopy. The thermodynamic stability of Pd under high‐temperature rWGS conditions is associated with Pd‐Ti coordination, which manifests upon O‐vacancy formation, and the artificial increase in TiO2 surface area.

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In Situ Dispersion of Pd on TiO2 During Reverse Water‐Gas Shift Reaction: Formation of Atomically Dispersed Pd

June 2020

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27 Reads

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27 Citations

Angewandte Chemie

Dilution of Pd/TiO2 with neat TiO2 results in the formation of atomically dispersed Pd under reverse water–gas shift (rWGS) reaction conditions at 400 °C and a several‐fold increase in activity. Abstract The application of single‐atom catalysts (SACs) to high‐temperature hydrogenation requires materials that thermodynamically favor metal atom isolation over cluster formation. We demonstrate that Pd can be predominantly dispersed as isolated atoms onto TiO2 during the reverse water–gas shift (rWGS) reaction at 400 °C. Achieving atomic dispersion requires an artificial increase of the absolute TiO2 surface area by an order of magnitude and can be accomplished by physically mixing a precatalyst (Pd/TiO2) with neat TiO2 prior to the rWGS reaction. The in situ dispersion of Pd was reflected through a continuous increase of rWGS activity over 92 h and supported by kinetic analysis, infrared and X‐ray absorption spectroscopies and scanning transmission electron microscopy. The thermodynamic stability of Pd under high‐temperature rWGS conditions is associated with Pd‐Ti coordination, which manifests upon O‐vacancy formation, and the artificial increase in TiO2 surface area.


Heterolytic Hydrogen Activation: Understanding Support Effects in Water–Gas Shift, Hydrodeoxygenation, and CO Oxidation Catalysis

April 2020

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22 Reads

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37 Citations

ACS Catalysis

Identifying the role of oxide supports in transition metal catalysis is critical toward our understanding of heterogeneous catalysis. The water-gas shift (WGS) reaction is a prototypical example where oxide support dictates catalytic activity, yet the cause for this remains uncertain. Herein, we show that a single descriptor—the equilibrium constant for hydroxyl formation—relates the WGS turnover frequency across disparate oxide supports. The dissimilar equilibrium constant, or oxophilicity, between early and late transition metals exemplify the utility of metal-support interfacial sites to circumvent adsorption-energy scaling restrictions, thereby providing bifunctional gains for the WGS reaction class. In relation, the equilibrium constant for hydroxyl formation is equivalent to the equilibrium constant for the formal heterolytic dissociation of hydrogen, and therefore, reflects the ability of the metal-support interface to participate in hydrogen heterolysis. The ubiquitous coexistence, yet divergent chemical behavior of homo- and heterolytically activated hydrogen renders oxide support identity central toward our understanding of hydrogenation catalysis.


Heterolytic Hydrogen Activation: Understanding Support Effects in Water-Gas Shift, Hydrodeoxygenation, and CO Oxidation Catalysis

October 2019

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21 Reads

Identifying the role of oxide supports in transition metal catalysis is critical toward our understanding of heterogeneous catalysis. The water-gas shift (WGS) reaction is a prototypical example where oxide support dictates catalytic activity, yet the cause for this remains uncertain. Herein, we show that a single descriptor—the equilibrium constant for hydroxyl formation—relates the WGS turnover frequency across disparate oxide supports. The dissimilar equilibrium constant, or oxophilicity, between early and late transition metals exemplify the utility of metal-support interfacial sites to circumvent adsorption-energy scaling restrictions, thereby providing bifunctional gains for the WGS reaction class. In relation, the equilibrium constant for hydroxyl formation is equivalent to the equilibrium constant for the formal heterolytic dissociation of hydrogen, and therefore, reflects the ability of the metal-support interface to participate in hydrogen heterolysis. The ubiquitous coexistence, yet divergent chemical behavior of homo- and heterolytically activated hydrogen renders oxide support identity central toward our understanding of hydrogenation catalysis.


Carboxyl intermediate formation via an in situ-generated metastable active site during water-gas shift catalysis

October 2019

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245 Reads

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108 Citations

Definitive experimental proof for catalytic pathways and active sites during the low-temperature water-gas shift reaction remains elusive. Herein, we combine spectroscopic, kinetic and computational analyses to address the decades-long mechanistic controversy by studying the reverse water-gas shift over Pd/Al2O3. Isotopic transient kinetic analysis established the minor role of the formate intermediate, whereas hydrogen titration experiments confirmed the intermediacy of carboxyl. The ability to decouple the parallel formate and carboxyl pathways led to the identification of a distinct active site that exhibits regio- and chemoselective hydrogen addition to CO2 to yield the carboxyl intermediate. The metastable active site is formed in situ, resulting in hydroxylation of the metal–support interface and electronic restructuring. Atomistic simulations of the active site electronic structure and mechanistic landscape provided a framework that is consistent with experimental observations. Our study highlights the dynamic creation of a coordinatively unsaturated metal site caused by substrate adsorption on an adjacent support site. Due to its importance, the water-gas shift reaction has been the subject of numerous studies; however, a unifying mechanistic picture has not yet emerged. Now, a combination of spectroscopic, kinetic and computational methods reveal the crucial role of carboxyl intermediate for this centuries-old process.

Citations (4)


... Furthermore, the RWGS reaction directly influences the synthesis of synthesis gas (syngas), a fundamental precursor in a plethora of industrial processes. Syngas serves as a versatile feedstock in producing fuels, chemicals, and materials, rendering the RWGS reaction indispensable in sectors ranging from petrochemicals to ammonia production and synthetic fuel manufacturing [4,16,23]. The efficient operation of the RWGS reaction hinges significantly on the judicious selection of catalysts, control of reaction conditions, and the optimization of process parameters. ...

Reference:

High-performance single-atom M/TiO2 catalysts in the reverse water-gas shift reaction: A comprehensive experimental and theoretical investigation
In Situ Dispersion of Palladium on TiO2 During Reverse Water–Gas Shift Reaction: Formation of Atomically Dispersed Palladium

... To address this challenge, in addition to increasing the ambient sunlight-driven temperature, the key is to decrease the reaction temperature of RWGS. This has led scientists to develop catalysts based on platinum-group metals that are highly active for RWGS at low temperatures (21)(22)(23)(24). For instance, a Pt-MoO x /Mo 2 N catalyst achieves an RWGS CO generation rate of 619.2 mmol g −1 hour −1 at 300°C (25). ...

In Situ Dispersion of Pd on TiO2 During Reverse Water‐Gas Shift Reaction: Formation of Atomically Dispersed Pd
  • Citing Article
  • June 2020

Angewandte Chemie

... Previous work by Sharafi et al. using Raman and X-ray photo-emission spectroscopy (XPS) revealed the existence of thick layers (∼5-10 nm) of Li 2 CO 3 on the Li 7 La 3 Zr 2 O 12 surfaces, upon exposure to air. 21,23 The same authors also detected LiOH on the Li 7 makes it potentially relevant for the water-gas shift reaction, 44,45 while the strong chemisorption of CO 2 makes Li 7 La 3 Zr 2 O 12 a promising dual functional material for CO 2 capture and conversion. 46,47 Hence, in the context of catalysis, Li 7 La 3 Zr 2 O 12 appears an excellent catalyst support to investigate reactions of CO 2 activation and water splitting, respectively. ...

Heterolytic Hydrogen Activation: Understanding Support Effects in Water–Gas Shift, Hydrodeoxygenation, and CO Oxidation Catalysis
  • Citing Article
  • April 2020

ACS Catalysis

... However, precisely regulating the stoichiometric balance between defect sites and hydroxyl groups in MOH•••M catalysts remains challenging. Additionally, the ubiquitous reaction between CO 2 and surface hydroxyl groups on metal (hydro)oxides often leads to the undesirable formation of bicarbonate [19][20][21] . Although previous studies have achieved some control over the reactivity of SFLPs on metal oxides 22 , achieving the fine-tuning of SFLPs with optimized Lewis acidic and basic properties continues to pose considerable difficulty. ...

Carboxyl intermediate formation via an in situ-generated metastable active site during water-gas shift catalysis