Core/yolk-shell nanoreactors for tandem catalysis

doi:10.1016/S1872-2067(23)64463-8

Chinese Journal of Catalysis ›› 2023, Vol. 50: 83-108.DOI: 10.1016/S1872-2067(23)64463-8

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Core/yolk-shell nanoreactors for tandem catalysis

Meng Zhao^a^,^b^,¹, Jing Xu^a^,^b^,¹, Shuyan Song^a^,^b^,^*(), Hongjie Zhang^a^,^b^,^c^,^*()

^aState Key Laboratory of Rare Earth Resource Utilization, Changchun Institute of Applied Chemistry, Chinese Academy of Sciences, Changchun 130022, Jilin, China
^bSchool of Applied Chemistry and Engineering, University of Science and Technology of China, Hefei 230026, Anhui, China
^cDepartment of Chemistry, Tsinghua University, Beijing 100084, China

Received:2023-02-28 Accepted:2023-05-16 Online:2023-07-18 Published:2023-07-25
Contact: *E-mail: songsy@ciac.ac.cn (S. Song), hongjie@ciac.ac.cn (H. Zhang).
About author:Shuyan Song received his BSc degree in Chemistry in 2003 and MSc in inorganic chemistry in 2006 both from Northeast Normal University. He joined the group of Prof. Hongjie Zhang at Changchun Institute of Applied Chemistry, Chinese Academy of Sciences (CAS), where he received his PhD in inorganic chemistry in 2009. He is working as a professor under the direction of Prof. Zhang at Changchun Institute of Applied Chemistry, CAS. His research focus is primarily on the development of porous functional materials for heterogeneous catalysis, proton conduction, chemical sensing and detection.
Hongjie Zhang received his BSc degree from Peking University in 1978. He then worked as a research assistant in Changchun Institute of Applied Chemistry, where he received his MSc degree in Inorganic Chemistry in 1985. Then, he worked as an assistant professor at the same institute from 1985-1989. He then studied at Universite de Bordeaux I, Laboratoire de Chimie du Solide du CNRS (France), where he received his PhD degree in Solid State Chemistry and Materials Sciences in 1993. He joined Changchun Institute of Applied Chemistry, CAS, as a professor in 1994. His current research interests include lanthanide organic-inorganic hybrid materials, electroluminescent devices, functional nanomaterials, and the structure and properties of rare earth magnesium alloys.
¹ Contributed equally to this work.
Supported by:
National Science and Technology Major Project of China(2021YFB3500700);National Natural Science Foundation of China(22020102003);National Natural Science Foundation of China(22025506);National Natural Science Foundation of China(22271274)

Abstract

Abstract:

Tandem catalysis is of great significance in industrial production. Among various catalysts, the core/yolk-shell nanoreactors have been regarded as one of the most promising ones. Their special hierarchical structure is an excellent platform for the deposition of various active sites, thus bringing strong interaction reactions. More importantly, their well-controlled shell structures can prudentially select the filterable components onto the inner cores, which facilitates the operation of tandem reaction steps. In this review, we systematically summarize the state-of-art encouraging progress of the core/yolk-shell tandem nanoreactors. Apart from their unique characteristics and attractive advantages, we also explored the innovative synthetic approaches as well as the potential application fields. Meanwhile, the specific tandem catalytic mechanism was discussed in-depth. Finally, we outlined the challenges and opportunities of this field to propose some promising development directions.

Key words: Tandem catalysis, Core shell catalyst, Yolk shell catalyst, Nanoreactor, Heterogeneous catalysis

Meng Zhao, Jing Xu, Shuyan Song, Hongjie Zhang. Core/yolk-shell nanoreactors for tandem catalysis[J]. Chinese Journal of Catalysis, 2023, 50: 83-108.

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Figures/Tables 15

Fig. 1. (a) Formation mechanism of the Al/Ni-Pt/Ti catalysts. Reprinted with permission from Ref. [25]. Copyright 2016, Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim. (b) Formation mechanism of the FeMn@HZSM-5 catalysts. Reprinted with permission from Ref. [27]. Copyright 2021, American Chemical Society. (c) Formation mechanism of the CuZnAl/SAPO11-PhyC catalysts. Reprinted with permission from Ref. [29]. Copyright 2015, Elsevier B. V.

Fig. 2. (a) Schematic diagram about the synthesis routes of UIO-66-Pt-Au and UIO-66-Pt/Au. (b) Schematic illustration of the specific tandem reaction routes. (c) Catalytic performance of different materials. Reprinted with permission from Ref. [48]. Copyright 2021, Springer Nature.

Fig. 3. (a) Schematic illustration of the step-by-step synthesis routes of Ni/SiO2@Ni-MOF-74. (b) The growth mechanism of Ni-MOF-74 on hollow Ni/SiO2 surface. (c) Illustration of the role of the Ni-MOF-74 shell in tandem catalysis. Reprinted with permission from Ref. [53]. Copyright 2019, American Chemical Society.

Fig. 4. (a) Scheme image of the GOx@ZIF-8@HRP@ZIF-8) synthetic process. (b) The regulation of distance of different enzymes by adjust the epitaxial growth period of ZIF-8. Reprinted with permission from Ref. [56]. Copyright 2022, Springer Nature. (c) Schematic illustration of the separate encapsulation of incompatible enzymes by MOF-Cs. (d) Schematic illustration of tandem catalytic process and corresponding catalytic performance and recyclability. Reprinted with permission from Ref. [57]. Copyright 2018, Wiley-VCH GmbH.

Fig. 5. (a) Schematic diagram of the Fe-Zn-Zr-T@H-ZSM-5 structure and reaction path for CO2 hydrogenation. (b) Possible tandem catalytic mechanism. (c?e) Catalytic performance of various catalysts with different components ratios. (d) Thermal stability of the Fe-Zn-Zr(0.1:1:1)-T@H-ZSM-5 catalysts. Reprinted with permission from Ref. [30]. Copyright 2021, American Chemical Society.

Fig. 6. (a) Schematic diagram of the Cu/ZnO@H-MOR core-shell catalysts preparation. (b) Reaction pathways of the ethanol synthesis. (c) Influence of shell thickness on the catalytic performance. (d) Proposed possible tandem catalytic mechanism. Reprinted with permission from Ref. [74]. Copyright 2020, American Chemical Society.

Fig. 7. (a) The synthesis strategy of Zn-Cr@SAPO-34 core-shell catalysts and corresponding STO process. (b) STO performance of various catalysts. Reprinted with permission from Ref. [34]. Copyright 2020, Royal Society of Chemistry. (c) FTS performance of FeMnK@H-S-1 core-shell like nanoreactors with different porous shells. (d) HF values of catalysts treated with different solution. (e) The relationship of HF value with light olefins selectivity. Reprinted with permission from Ref. [28]. Copyright 2021, Elsevier Ltd.

Fig. 8. (a) Schematic illustration of step-by-step synthesis process of MO@ZO materials. (b) Cross-sectional high resolution transmission electron microscopy (HRTEM) images of catalyst at the heating temperature of 400 °C and the enlarged HRTEM images and corresponding Fourier transform patterns of the enlarged three areas (l?n). (c) Catalytic performance of various catalysts in syngas conversion. (d) Illustration of reaction pathway of MO@ZO. Reprinted with permission from Ref. [82]. Copyright 2022, Springer Nature.

Fig. 9. (a) Schematic diagram of synthesis of CeO2-Pt@mSiO2. (b) Possible tandem catalytic mechanism of alkene hydroformylation. (c) Catalytic performance of CeO2-Pt@mSiO2, CeO2/Pt and Pt/mSiO2 at 150 °C respectively. (d) Catalytic performance comparison of CeO2-Pt@mSiO2 and single-step hydroformylation at different temperature. Reprinted with permission from Ref. [16]. Copyright 2016, American Chemical Society. (e) Synthesis of CeO2-Pt@mSiO2-Co tandem catalyst. (f) Catalytic performance of different catalysts as well as product distribution and CO2 conversion on various reaction conditions. Reprinted with permission from Ref. [17]. Copyright 2017, American Chemical Society.

Fig. 10. (a) Three kinds of tandem catalysts models. (b) Infrared spectra of adsorbed linear CO on catalysts treated with various temperature and in situ H2 DRIFTS spectra of different catalysts at same temperature. (c?e) Specific catalytic performance of model 1?3 in (a), respectively. (f) Comparison of catalytic performance over (Pt/Al2O3)@In2O3 with other state-of-art catalysts. Reprinted with permission from Ref. [22]. Copyright 2021, American Association for the Advancement of Science.

Fig. 11. (a) The tandem deacetalization-Knoevenagel reaction. (b) Scheme image of the synthetic process of the all-organic nanoreactor. (c) The specific tandem reaction steps in the core-shell catalyst. (d) Reaction kinetics plot. Reprinted with permission from Ref. [86]. Copyright 2020, Wiley-VCH GmbH.

Fig. 12. (a) The selectivity of the as-prepared catalysts. (b) Schematic diagram of the yolk-shell nanoreactors of Pd1@Fe1. (c) Diagram of ring-opening amination reaction scheme for epoxides. (d) The specific productivity and selectivity for a continuous recycled testing. Reprinted with permission n from Ref. [92]. Copyright 2021, Nature. (e) Synthesis procedure of Zn-N-C/Au@mSiO2. (f) Conversion and yield changes over time. (g) Reaction mechanism of styrene to styrene carbonate. (h) Catalytic performance comparison for styrene to styrene carbonate. Reprinted with permission from Ref. [18]. Copyright 2021, The Royal Society of Chemistry.

Fig. 13. (a) Schematic diagram of the preparation process of ZnCoSiOx with different structure. (b) Catalytic performance of ZnCoSiOx in CO2 hydrogenation at 390 °C. (c) The proposed CO2 conversion process over ZnCoSiOx. Reprinted with permission from Ref. [95]. Copyright 2021, Springer Nature Switzerland AG.

Fig. 14. (a) Comparison of catalytic activity with previous works. (b) Reaction scheme for Olefin pathway over the FeMn@MZ5. (c) TG curves of the catalysts after the stability test. (d) Rate of coke deposition on the catalyst during the stability test. Reprinted with permission from Ref. [27]. Copyright 2021, American Chemical Society. (e) Catalytic performance of different catalysts for CO2 hydrogenation. (f) TEM image of fresh Co@hsZSM5@Pt (5 wt%). (g) TEM image of spent Co@hsZSM5@Pt (5 wt%). (h) EDS elemental mapping of fresh Pt-Co/comZSM5. (i) EDS elemental mapping of spent Pt-Co/comZSM5. Reprinted with permission from Ref. [102]. Copyright 2020, The Royal Society of Chemistry.

Fig. 15. (a) FE of various reduction products of Ag@Cu2O-6.4 NCs at di?erent potentials measured in a flow-cell with 1 mol L?1 KOH electrolyte. (b) Operando Cu K-edge XANES spectra of Ag@Cu2O-6.4 NCs at different potential. (c) Linear scaling relations between *CO coverage and formation energy of *CHO and *COCOH on Cu (111) surface. (d) The reduction products and CO flux in Ag@Cu2O-x NCs with different radius of the Cu2O shell. Reprinted with permission from Ref. [104]. Copyright 2021 Wiley-VCH GmbH. (e) The faradaic efficiencies of reduction products from the CO2RR reaction of Au@Cu2O-MC. (f) Au@Cu2O Schematic diagram of intracavity tandem catalytic mechanism. Reprinted with permission from Ref. [106]. Copyright 2020, The Royal Society of Chemistry. (g) The catalytic activity of different catalysts. (h) The rate at which N2H4·H2O breaks down to H2. Reprinted with permission from Ref. [25]. Copyright 2016, WILEY-VCH Verlag GmbH & Co. KGaA, Weinheim. (i) The catalytic performance from the DKR of 1-phenylethylamine catalyzed by the Pd/NH2-MSN@BTME@enzyme/L-mesosilica and other catalysts. Reprinted with permission from Ref. [111]. Copyright 2017, The Royal Society of Chemistry.

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Core/yolk-shell nanoreactors for tandem catalysis

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