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Control and Impact of Metal Loading Heterogeneities at the Nanoscale on the Performance of Pt/Zeolite Y Catalysts for Alkane Hydroconversion

[Image: see text] The preparation of zeolite-based bifunctional catalysts with low noble metal loadings while maintaining optimal performance has been studied. We have deposited 0.03 to 1.0 wt % Pt on zeolite H-USY (Si/Al ∼ 30 at./at.) using either platinum(II) tetraammine nitrate (PTA, Pt(NH(3))(4)...

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Autores principales: van der Wal, Lars I., Oenema, Jogchum, Smulders, Luc C. J., Samplonius, Nonne J., Nandpersad, Karan R., Zečević, Jovana, de Jong, Krijn P.
Formato: Online Artículo Texto
Lenguaje:English
Publicado: American Chemical Society 2021
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC8022326/
https://www.ncbi.nlm.nih.gov/pubmed/33833901
http://dx.doi.org/10.1021/acscatal.1c00211
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author van der Wal, Lars I.
Oenema, Jogchum
Smulders, Luc C. J.
Samplonius, Nonne J.
Nandpersad, Karan R.
Zečević, Jovana
de Jong, Krijn P.
author_facet van der Wal, Lars I.
Oenema, Jogchum
Smulders, Luc C. J.
Samplonius, Nonne J.
Nandpersad, Karan R.
Zečević, Jovana
de Jong, Krijn P.
author_sort van der Wal, Lars I.
collection PubMed
description [Image: see text] The preparation of zeolite-based bifunctional catalysts with low noble metal loadings while maintaining optimal performance has been studied. We have deposited 0.03 to 1.0 wt % Pt on zeolite H-USY (Si/Al ∼ 30 at./at.) using either platinum(II) tetraammine nitrate (PTA, Pt(NH(3))(4)(NO(3))(2)) or hexachloroplatinic(IV) acid (CPA, H(2)PtCl(6)·6H(2)O) and studied the nanoscale Pt loading heterogeneities and global hydroconversion performance of the resulting Pt/Y catalysts. Pt/Y samples prepared with PTA and a global Pt loading as low as 0.3 wt % Pt (n(Pt)/n(A) = 0.08 mol/mol, where n(Pt) is the number of Pt surface sites and n(A) is the number of acid sites) maintained catalytic performance during n-heptane (T = 210–350 °C, P = 10 bar) as well as n-hexadecane (T = 170–280 °C, P = 5 bar) hydroisomerization similar to a 1.0 wt % Pt sample. For Pt/Y catalysts prepared with CPA, a loading of 0.3 wt % Pt (n(Pt)/n(A) = 0.08 mol/mol) sufficed for n-heptane hydroisomerization, whereas a detrimental effect on n-hexadecane hydroisomerization was observed, in particular undesired secondary cracking occurred to a significant extent. The differences between PTA and CPA are explained by differences in Pt loading per zeolite Y crystal (size ∼ 500 nm), shown from extensive transmission electron microscopy energy-dispersive X-ray spectroscopy experiments, whereby crystal-based n(Pt)/n(A) ratios could be determined. From earlier studies, it is known that the Al content per crystal of USY varied tremendously and that PTA preferentially is deposited on crystals with higher Al content due to ion-exchange with zeolite protons. Here, we show that this preferential deposition of PTA on Al-rich crystals led to a more constant value of n(Pt)/n(A) ratio from one zeolite crystal to another, which was beneficial for catalytic performance. Use of CPA led to a large variation of Pt loading independent of Al content, giving rise to larger variations of n(Pt)/n(A) ratio from crystal to crystal that negatively affected the catalytic performance. This study thus shows the impact of local metal loading variations at the zeolite crystal scale (nanoscale) caused by different interactions of metal precursors with the zeolite, which are essential to design and synthesize optimal catalysts, in particular at low noble metal loadings.
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spelling pubmed-80223262021-04-06 Control and Impact of Metal Loading Heterogeneities at the Nanoscale on the Performance of Pt/Zeolite Y Catalysts for Alkane Hydroconversion van der Wal, Lars I. Oenema, Jogchum Smulders, Luc C. J. Samplonius, Nonne J. Nandpersad, Karan R. Zečević, Jovana de Jong, Krijn P. ACS Catal [Image: see text] The preparation of zeolite-based bifunctional catalysts with low noble metal loadings while maintaining optimal performance has been studied. We have deposited 0.03 to 1.0 wt % Pt on zeolite H-USY (Si/Al ∼ 30 at./at.) using either platinum(II) tetraammine nitrate (PTA, Pt(NH(3))(4)(NO(3))(2)) or hexachloroplatinic(IV) acid (CPA, H(2)PtCl(6)·6H(2)O) and studied the nanoscale Pt loading heterogeneities and global hydroconversion performance of the resulting Pt/Y catalysts. Pt/Y samples prepared with PTA and a global Pt loading as low as 0.3 wt % Pt (n(Pt)/n(A) = 0.08 mol/mol, where n(Pt) is the number of Pt surface sites and n(A) is the number of acid sites) maintained catalytic performance during n-heptane (T = 210–350 °C, P = 10 bar) as well as n-hexadecane (T = 170–280 °C, P = 5 bar) hydroisomerization similar to a 1.0 wt % Pt sample. For Pt/Y catalysts prepared with CPA, a loading of 0.3 wt % Pt (n(Pt)/n(A) = 0.08 mol/mol) sufficed for n-heptane hydroisomerization, whereas a detrimental effect on n-hexadecane hydroisomerization was observed, in particular undesired secondary cracking occurred to a significant extent. The differences between PTA and CPA are explained by differences in Pt loading per zeolite Y crystal (size ∼ 500 nm), shown from extensive transmission electron microscopy energy-dispersive X-ray spectroscopy experiments, whereby crystal-based n(Pt)/n(A) ratios could be determined. From earlier studies, it is known that the Al content per crystal of USY varied tremendously and that PTA preferentially is deposited on crystals with higher Al content due to ion-exchange with zeolite protons. Here, we show that this preferential deposition of PTA on Al-rich crystals led to a more constant value of n(Pt)/n(A) ratio from one zeolite crystal to another, which was beneficial for catalytic performance. Use of CPA led to a large variation of Pt loading independent of Al content, giving rise to larger variations of n(Pt)/n(A) ratio from crystal to crystal that negatively affected the catalytic performance. This study thus shows the impact of local metal loading variations at the zeolite crystal scale (nanoscale) caused by different interactions of metal precursors with the zeolite, which are essential to design and synthesize optimal catalysts, in particular at low noble metal loadings. American Chemical Society 2021-03-12 2021-04-02 /pmc/articles/PMC8022326/ /pubmed/33833901 http://dx.doi.org/10.1021/acscatal.1c00211 Text en © 2021 The Authors. Published by American Chemical Society Permits non-commercial access and re-use, provided that author attribution and integrity are maintained; but does not permit creation of adaptations or other derivative works (https://creativecommons.org/licenses/by-nc-nd/4.0/).
spellingShingle van der Wal, Lars I.
Oenema, Jogchum
Smulders, Luc C. J.
Samplonius, Nonne J.
Nandpersad, Karan R.
Zečević, Jovana
de Jong, Krijn P.
Control and Impact of Metal Loading Heterogeneities at the Nanoscale on the Performance of Pt/Zeolite Y Catalysts for Alkane Hydroconversion
title Control and Impact of Metal Loading Heterogeneities at the Nanoscale on the Performance of Pt/Zeolite Y Catalysts for Alkane Hydroconversion
title_full Control and Impact of Metal Loading Heterogeneities at the Nanoscale on the Performance of Pt/Zeolite Y Catalysts for Alkane Hydroconversion
title_fullStr Control and Impact of Metal Loading Heterogeneities at the Nanoscale on the Performance of Pt/Zeolite Y Catalysts for Alkane Hydroconversion
title_full_unstemmed Control and Impact of Metal Loading Heterogeneities at the Nanoscale on the Performance of Pt/Zeolite Y Catalysts for Alkane Hydroconversion
title_short Control and Impact of Metal Loading Heterogeneities at the Nanoscale on the Performance of Pt/Zeolite Y Catalysts for Alkane Hydroconversion
title_sort control and impact of metal loading heterogeneities at the nanoscale on the performance of pt/zeolite y catalysts for alkane hydroconversion
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC8022326/
https://www.ncbi.nlm.nih.gov/pubmed/33833901
http://dx.doi.org/10.1021/acscatal.1c00211
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