Chinese Journal of Catalysis ›› 2025, Vol. 78: 156-169.DOI: 10.1016/S1872-2067(25)64795-4
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Siquan Fenga,1, Cunyao Lia,1, Yuxuan Zhoub,1, Xiangen Songa,*(
), Miao Jianga, HuFei Daib, Shangsheng Songa, Benhan Fana, Yutong Caia,c, Bin Lia, Qiao Yuana,c, Xingju Lia, Lei Zhua, Yue Zhanga, Weimiao Chena, Tao Liua, Li Yana,*(
), Xueqing Gongd,*(
), Yunjie Dinga,e,*(
)
Received:2025-05-20
Accepted:2025-07-03
Online:2025-11-18
Published:2025-10-14
Contact:
*E-mail: xiangensong@dicp.ac.cn (X. Song), yanli@dicp.ac.cn (L. Yan), xqgong@sjtu.edu.cn (X. Gong), dyj@dicp.ac.cn (Y. Ding).
About author:1Contributed equally to this work.
Supported by:Siquan Feng, Cunyao Li, Yuxuan Zhou, Xiangen Song, Miao Jiang, HuFei Dai, Shangsheng Song, Benhan Fan, Yutong Cai, Bin Li, Qiao Yuan, Xingju Li, Lei Zhu, Yue Zhang, Weimiao Chen, Tao Liu, Li Yan, Xueqing Gong, Yunjie Ding. Regulating microenvironment of heterogeneous Rh mononuclear complex via sulfur-phosphine co-coordination to enhance the performance of hydroformylation of olefins[J]. Chinese Journal of Catalysis, 2025, 78: 156-169.
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URL: https://www.cjcatal.com/EN/10.1016/S1872-2067(25)64795-4
Fig. 1. The industrial plant of 50000 tons/year ethylene hydroformylation based on heterogeneous mononuclear Rh1/POPs-PPh3 catalyst at Ningbo Juhua Chemical & Science Co., Ltd., Zhejiang, China in the 2020s, which was developed by Ding’s group of Dalian Institute of Chemical Physicals, Chinese Academy of Science.
Fig. 2. The activity of heterogeneous mononuclear Rh1/POPs-PPh3 and Rh1/POPs-PPh3&S for olefin hydroformylation. (a) Preparation of sulfur- -coordinated Rh-PPh3 (Rh1/POPs-PPh3&S) catalyst. (b) Effect of ratios of sulfur with phosphine on the activity of Rh1/POPs-PPh3&S for propene hydroformylation; 80 °C, 2.0 h, autoclave, C3H6/CO/H2 = 1:1:1, 1.0 MPa, 600 rpm; the ratio of olefin to rhodium is approximately 1500. (c) The activity conversion, n/i values and TOF comparison between Rh1/POPs-PPh3 and Rh1/POPs-PPh3&S for C5H10, C6H12, C7H14, C8H16 hydroformylation; 80 °C, 2.0 h, autoclave, CO/H2 = 1:1, 1.0 MPa; C5H10, C6H12, C7H14, C8H16, 1.0 g, 600 rpm; the ratios of olefin to rhodium are approximately 5868, 4892, 4194 and 3668, respectively. (d) The stability test of Rh1/POPs-PPh3&S for propylene hydroformylation, 120 °C, C3H6/CO/H2 = 1:1:1, 1.0 MPa. (e) The apparent activation energy comparison of the Rh1/POPs-PPh3 and Rh1/POPs-PPh3&S catalysts.
Fig. 3. The HAADF-STEM images of spent Rh?/POPs-PPh3 and Rh1/POPs-PPh3&S catalysts, the EXAFS Fourier transform in R space, as well as the wavelet transform. (a) The HAADF-STEM image of spent Rh?/POPs-PPh3t, and (b) Rh1/POPs-PPh3&S. (c) The 31P magic angle spinning solid-state NMR of Rh?/POPs-PPh3 and Rh1/POPs-PPh3&S. (d) The Fourier transform of the EXAFS data in R space of Rh foil, spent Rh?/POPs-PPh3 and Rh1/POPs-PPh3&S. The first shell coordination paths fitting of (e) Rh1/POPs-PPh3&S, and (f) Rh1/POPs-PPh3. The wavelet transforms of (g) Rh1/POPs-PPh3&S, (h) Rh1/POPs-PPh3, and (i) Rh foil.
Fig. 4. The molecular structure identification of the spent Rh1/POPs-PPh3 and Rh1/POPs-PPh3&S (a) The in-situ CO-TPD of Rh1/POPs-PPh3 and Rh1/POPs-PPh3&S catalysts after treatment with CO/H2, (b) In-situ DRIFTS spectra of Rh1/POPs-PPh3 and Rh1/POPs-PPh3&S catalysts. (c) The XANES comparison of Rh foil, Rh2O3, spent Rh1/POPs-PPh3 and Rh1/POPs-PPh3&S catalysts. (d-f) The Rh 3d5/2, P 2p3/2, S 2p3/2 XPS spectra of spent Rh1/POPs-PPh3 and Rh1/POPs-PPh3&S catalysts. (g-i) In-situ TPSR-MS signals of m/z = 42 (C3H6), m/z = 28 (CO), and m/z = 2 (H2) from Rh1/POPs-PPh3 and Rh1/POPs-PPh3&S catalysts during propylene hydroformylation.
Fig. 5. The reaction process exploration on Rh1/POPs-PPh3 and Rh1/POPs-PPh3&S catalysts for propene hydroformylation. (a-c) In-situ TPSR-MS signals of m/z = 72 (C4H8O), m/z = 43 (C3H7) and m/z = 44 (C3H8) from Rh1/POPs-PPh3 and Rh1/POPs-PPh3&S catalysts during propylene hydroformylation. (d) The in-situ DRIFTS spectra of propene hydroformylation on Rh1/POPs-PPh3 and Rh1/POPs-PPh3&S catalysts.
Fig. 6. The DFT calculated the relative energy of different reaction coordination on the mononuclear Rh1/POPs-PPh3 and Rh1/POPs-PPh3&S catalysts catalyst for propylene hydroformylation.
Fig. 7. The DFT calculation Bader electron analysis. (a) The single-site Rh Bader electron analysis of mononuclear Rh1/POPs-PPh3 and Rh1/POPs-PPh3&S during the reaction pathway (1, 2, 4, 6, 8 are intermediates, and 3, 5, 7, 9 are the corresponding transition states, corresponding olefin insertion, CO carbonyl insertion, H2 oxidative addition and acyl hydrogenolysis, respectively). The all-atom Bader charge analysis of mononuclear Rh1/POPs-PPh3&S (b) and Rh1/POPs-PPh3 (c) catalysts with the intermediate species of 2 and its corresponding transition state 3 in Fig. 6. C* refers to the carbon in CO, and the C** refers to the carbon in propylene (C3H6).
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