Well‐Defined RhO <sub>4</sub> Species Confined in Self‐Pillared Pentasil Zeolite as Efficient Nano Reactors for Hydroformylation of Higher Olefins

W Weili Jiang (State Key Laboratory of Heavy Oil Processing College of New Energy and Materials China University of Petroleum Beijing Beijing China) C Cheng Huang M Minghao Huang (Key Laboratory of Green Chemistry & Technology of Ministry of Education, College of Chemistry) W Wei Ding Z Ziqi Wang (Division of Advanced Materials) J Jicong Li (State Key Laboratory of Heavy Oil Processing College of New Energy and Materials China University of Petroleum Beijing Beijing China) H Haochen Xu C Congying Yue (State Key Laboratory of Heavy Oil Processing College of New Energy and Materials China University of Petroleum Beijing Beijing China) B Baodian Zhou (State Key Laboratory of Heavy Oil Processing College of New Energy and Materials China University of Petroleum Beijing Beijing China) G Guanglin Zhou H Hongjun Zhou (State Key Laboratory of Heavy Oil Processing College of New Energy and Materials China University of Petroleum Beijing Beijing China) C Chunming Xu (State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Chang Ping, Beijing 102249, China)

Abstract

ABSTRACT Heterogeneous catalytic hydroformylation of higher olefins often suffers from substrate diffusion limitations and unclear active species. We overcame both challenges using a self‐pillared MFI zeolite anchoring Rh single atoms. By controlling reaction and calcination conditions, we synthesized catalyst Rh 1 @SPP‐MFI (Rh 1 @SPP‐S‐1, Rh 1 @SPP‐ZSM‐5, Rh 1 @SPP‐TS‐1) using a one‐pot method. Extended x‐ray absorption analysis combined with cs‐corrected high‐angle annular dark field scanning transmission electron microscopy (HAADF‐STEM) confirmed each Rh atom coordinated with four O atoms as a well‐defined Rh 1.5+ ‐O 4 structure confined in zeolite cages. The thickness of the zeolite nanosheets was approximately 1.5 b ‐axis unit cells, interlayer spacing ∼ 3.0 nm, making them ideal as nanoreactors. At 353 K and 2.5 MPa, the catalyst achieved a turnover frequency (TOF) of 7074 h −1 for 1‐octene to nonanal, outperforming most homogeneous/heterogeneous catalysts under comparable conditions. Over five cycles (36 h), each Rh atom processed ∼6881 olefin molecules per hour. Density functional theory (DFT) revealed evident electron transfer from O to Rh in the RhO 4 unit, and the flexible Rh‐O bonds mitigated steric hindrance during hydroformylation. This work reveals the microstructure and working mechanism of supported Rh catalysts, and correlates them with the classical homogeneous catalytic mechanism.

Article Details

Volume / Issue Vol. 1, Issue 1
Published July 21, 2026
ISSN 1433-7851
Publisher Wiley

Journal Info

Angewandte Chemie International Edition

Wiley

ISSN: 1433-7851 Physical Sciences

Authors (12)

W

Weili Jiang

State Key Laboratory of Heavy Oil Processing College of New Energy and Materials China University of Petroleum Beijing Beijing China

C

Cheng Huang

M

Minghao Huang

Key Laboratory of Green Chemistry & Technology of Ministry of Education, College of Chemistry

W

Wei Ding

Z

Ziqi Wang

Division of Advanced Materials

J

Jicong Li

State Key Laboratory of Heavy Oil Processing College of New Energy and Materials China University of Petroleum Beijing Beijing China

H

Haochen Xu

C

Congying Yue

State Key Laboratory of Heavy Oil Processing College of New Energy and Materials China University of Petroleum Beijing Beijing China

B

Baodian Zhou

State Key Laboratory of Heavy Oil Processing College of New Energy and Materials China University of Petroleum Beijing Beijing China

G

Guanglin Zhou

H

Hongjun Zhou

State Key Laboratory of Heavy Oil Processing College of New Energy and Materials China University of Petroleum Beijing Beijing China

C

Chunming Xu

State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Chang Ping, Beijing 102249, China