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Title: Multi-scale simulation of reaction, transport and deactivation in a SBA-16 supported catalyst for the conversion of ethanol to butadiene

Abstract

Effective design of heterogeneous catalytic systems requires careful coordination of physiochemical phenomena that span orders or magnitude in length and time scales. Multiscale modeling and simulation tools can provide useful insight for understanding and improving the performance of such systems. Mesoporous silica catalyst support materials present a versatile platform wherein support attributes may be tuned to control transport phenomena throughout the system. In this study we develop an integrated multiscale modeling approach for the conversion of ethanol to butadiene over an SBA-16 mesoporous silica supported catalyst. We use molecular dynamics simulations to calculate domain specific diffusivities of reactants and products in the various domains of SBA-16’s nanostructure. This is used to calculate a resultant effective diffusivity (Deff) through its microstructure using finite element method (FEM) models of the tessellated unit cell. The resultant effective diffusivity enables the development of a reduced-order reactor level FEM model that is able to implicitly account for the SBA-16’s transport effects without the explicit consideration of its detailed geometry. Experimental bench-scale conversion data for the ethanol to butadiene process over SBA-16 is used to extract intrinsic kinetic rate constants for a simplified reaction mechanism using this reduced order bench-scale reactor FEM model. The model ismore » able to reproduce experimental trends in conversion and activity lifetimes. The impact of varying key support attributes such as pore-size and particle size on catalytic activity lifetimes is then explored. We demonstrate the utility of this multi-scale modelling strategy in guiding catalyst design for the development of rational strategies to improve the performance of heterogeneous supported catalytic systems.« less

Authors:
ORCiD logo [1]; ORCiD logo [1];  [1];  [2];  [2]; ORCiD logo [1]
  1. National Renewable Energy Lab. (NREL), Golden, CO (United States)
  2. Pacific Northwest National Lab. (PNNL), Richland, WA (United States)
Publication Date:
Research Org.:
National Renewable Energy Lab. (NREL), Golden, CO (United States); Pacific Northwest National Lab. (PNNL), Richland, WA (United States)
Sponsoring Org.:
USDOE Office of Energy Efficiency and Renewable Energy (EERE), Sustainable Transportation Office. Bioenergy Technologies Office
OSTI Identifier:
1525763
Alternate Identifier(s):
OSTI ID: 1573020
Report Number(s):
NREL/JA-2700-74122; PNNL-SA-139387
Journal ID: ISSN 0920-5861
Grant/Contract Number:  
AC36-08GO28308; AC05-76RL01830
Resource Type:
Accepted Manuscript
Journal Name:
Catalysis Today
Additional Journal Information:
Journal Volume: 338; Journal Issue: C; Journal ID: ISSN 0920-5861
Publisher:
Elsevier
Country of Publication:
United States
Language:
English
Subject:
09 BIOMASS FUELS; 37 INORGANIC, ORGANIC, PHYSICAL, AND ANALYTICAL CHEMISTRY; multi-scale catalysis; finite element method; molecular dynamics; reaction; diffusion; deactivation; catalyst design

Citation Formats

Bharadwaj, Vivek S., Pecha, Michael B., Bu, Lintao, Dagle, Vanessa Lebarbier, Dagle, Robert A., and Ciesielski, Peter N. Multi-scale simulation of reaction, transport and deactivation in a SBA-16 supported catalyst for the conversion of ethanol to butadiene. United States: N. p., 2019. Web. doi:10.1016/j.cattod.2019.05.042.
Bharadwaj, Vivek S., Pecha, Michael B., Bu, Lintao, Dagle, Vanessa Lebarbier, Dagle, Robert A., & Ciesielski, Peter N. Multi-scale simulation of reaction, transport and deactivation in a SBA-16 supported catalyst for the conversion of ethanol to butadiene. United States. https://doi.org/10.1016/j.cattod.2019.05.042
Bharadwaj, Vivek S., Pecha, Michael B., Bu, Lintao, Dagle, Vanessa Lebarbier, Dagle, Robert A., and Ciesielski, Peter N. Thu . "Multi-scale simulation of reaction, transport and deactivation in a SBA-16 supported catalyst for the conversion of ethanol to butadiene". United States. https://doi.org/10.1016/j.cattod.2019.05.042. https://www.osti.gov/servlets/purl/1525763.
@article{osti_1525763,
title = {Multi-scale simulation of reaction, transport and deactivation in a SBA-16 supported catalyst for the conversion of ethanol to butadiene},
author = {Bharadwaj, Vivek S. and Pecha, Michael B. and Bu, Lintao and Dagle, Vanessa Lebarbier and Dagle, Robert A. and Ciesielski, Peter N.},
abstractNote = {Effective design of heterogeneous catalytic systems requires careful coordination of physiochemical phenomena that span orders or magnitude in length and time scales. Multiscale modeling and simulation tools can provide useful insight for understanding and improving the performance of such systems. Mesoporous silica catalyst support materials present a versatile platform wherein support attributes may be tuned to control transport phenomena throughout the system. In this study we develop an integrated multiscale modeling approach for the conversion of ethanol to butadiene over an SBA-16 mesoporous silica supported catalyst. We use molecular dynamics simulations to calculate domain specific diffusivities of reactants and products in the various domains of SBA-16’s nanostructure. This is used to calculate a resultant effective diffusivity (Deff) through its microstructure using finite element method (FEM) models of the tessellated unit cell. The resultant effective diffusivity enables the development of a reduced-order reactor level FEM model that is able to implicitly account for the SBA-16’s transport effects without the explicit consideration of its detailed geometry. Experimental bench-scale conversion data for the ethanol to butadiene process over SBA-16 is used to extract intrinsic kinetic rate constants for a simplified reaction mechanism using this reduced order bench-scale reactor FEM model. The model is able to reproduce experimental trends in conversion and activity lifetimes. The impact of varying key support attributes such as pore-size and particle size on catalytic activity lifetimes is then explored. We demonstrate the utility of this multi-scale modelling strategy in guiding catalyst design for the development of rational strategies to improve the performance of heterogeneous supported catalytic systems.},
doi = {10.1016/j.cattod.2019.05.042},
journal = {Catalysis Today},
number = C,
volume = 338,
place = {United States},
year = {Thu May 23 00:00:00 EDT 2019},
month = {Thu May 23 00:00:00 EDT 2019}
}

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Works referencing / citing this record:

Hierarchically Structured CeO2 Catalyst Particles From Nanocellulose/Alginate Templates for Upgrading of Fast Pyrolysis Vapors
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