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Chinese Journal of Materials Research  2026, Vol. 40 Issue (1): 1-12    DOI: 10.11901/1005.3093.2025.096
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Synthesis of Hierarchical ZSM-22 Zeolite and its Catalytic Performance for Hydrogenation Isomerization of n-Dodecane
HAN Yang1,2, LI Mengchen3,4, YU Hongyue3, QIAO Liang3, SHEN Yuge3, GAO Shanbin3, JIAO Yilai2(), CHI Kebin3()
1.School of Materials Science and Engineering, University of Science and Technology of China, Shenyang 110016, China
2.Shenyang National Laboratory for Materials Science, Institute of Metal Research, Chinese Academy of Sciences, Shenyang 110016, China
3.Petrochemical Research Institute, PetroChina Company Limited, Beijing 102206, China
4.Department of Chemical Engineering, Tsinghua University, Beijing 100084, China
Cite this article: 

HAN Yang, LI Mengchen, YU Hongyue, QIAO Liang, SHEN Yuge, GAO Shanbin, JIAO Yilai, CHI Kebin. Synthesis of Hierarchical ZSM-22 Zeolite and its Catalytic Performance for Hydrogenation Isomerization of n-Dodecane. Chinese Journal of Materials Research, 2026, 40(1): 1-12.

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Abstract  

The zeolite ZSM-22 with different grain length and pore structure was synthesized by hydrothermal synthesis with TDPA as mesoporous template agent. The synthesized material was characterized using XRD, XRF, SEM, TEM, NH3-TPD, N2 adsorption/desorption, solid-state NMR, and Py-IR. The results indicated that the incorporation of TDPA is beneficial for the formation of the mesoporous structure and the optimization of the acidity distribution for the prepared ZSM-22 zeolite. Then, a novel bifunctional noble metal catalyst was prepared with the acquired hierarchical ZSM-22 zeolite as support, meanwhile the performance of catalyst in the hydrogenation isomerization of n-dodecane was evaluated. The results revealed that with a molar ratio of nTDPA/SiO2 of 0.0170, the synthesized ZSM-22 zeolite presented proper pore structure and acidic performance, with an average crystal grain length lowered to 200 nm and an optimal distribution of acid strength and acid sites. For the n-dodecane conversion rate of 83%, the isomer selectivity increased to 68%, representing a 10-percentage-point improvement compared to the conventional blank ZSM-22 catalyst (58%). This study provides a new approach for developing highly efficient hydroisomerization catalyst through the in-situ synthesis of ZSM-22 zeolites with mesoporous structures.

Key words:  inorganic non-metallic materials      molecular sieves      hydroisomerization      mesoporous      porous structure      acidity      ZSM-22     
Received:  04 March 2025     
ZTFLH:  TE65  
Fund: National Key Research and Development Program of China(2023YFB3810600);National Natural Science Foundation of China(22378407)
Corresponding Authors:  JIAO Yilai, Tel: (024)23971936, E-mail: yljiao@imr.ac.cn;
CHI Kebin, Tel: (010)80165536, E-mail: ckb459@petrochina.com.cn

URL: 

https://www.cjmr.org/EN/10.11901/1005.3093.2025.096     OR     https://www.cjmr.org/EN/Y2026/V40/I1/1

Fig.1  Fixed-bed catalyst evaluation apparatus
Fig.2  XRD patterns and relative crystallinity of ZSM-22 zeolite with different TDPA additive amounts
SamplesSBET / m2·g-1Smicro / m2·g-1Sext / m2·g-1Vtotal / cm3·g-1Vmicro / cm3·g-1Vmeso / cm3·g-1
Z22-0265232330.1800.0890.091
Z22-0.0068287245420.2700.0930.158
Z22-0.0119289244450.2630.0930.170
Z22-0.0170288242460.2470.0920.177
Z22-0.0221281240410.2300.0910.154
Z22-0.0272237198390.2300.0760.139
Z22-0-5L237206310.160.0810.079
Z22-0.0068-5L265229360.270.0870.183
Z22-0.0170-5L270235350.300.0890.212
Z22-0.0272-5L184151330.260.0580.203
Table 1  Results of synthetic products with different TDPA additive amounts by BET analysis
Fig.3  Texture properties of synthetic products (a) N2 adsorption-desorption isotherm curves of products synthesized with different TDPA addition, (b) BJH aperture distribution, (c) H-K micropore size distribution, (d) H-K cumulative pore size distribution
Fig.4  SEM images of the synthesized products with different TDPA addition amounts and its grain length frequency distribution (a) Z22-0, (b) Z22-0.0068, (c) Z22-0.0119, (d) Z22-0.0170, (e) Z22-0.0221, (f) Z22-0.0272
Fig.5  TEM images (a) Z22-0, (b) Z22-0.0170
Fig.6  NMR spectra of the synthesized products with different TDPA addition amounts (a) 27Al NMR spectra, (b) 29Si NMR spectra
SamplesSiO2/Al2O3 (XRF)Weak acidStrong acidTotal NH3 uptake / μmol·g-1
Temperature / oCNH3 uptake / μmol·g-1Temperature / oCNH3 uptake / μmol·g-1
Z22-063.34225275435206481
Z22-0.006860.63227310447247557
Z22-0.011958.77230309448249558
Z22-0.017058.37231317452258575
Z22-0.022161.32229302451248550
Z22-0.027286.72218195431145340
Z22-0-5L61.63221279443258537
Z22-0.0068-5L58.72224290448268558
Z22-0.0170-5L54.08227312452303615
Z22-0.0272-5L75.26223258439243501
Table 2  Concentration of acid sites determined by NH3-TPD and SiO2/Al2O3 determined by XRF
Fig.7  Acidity characterization of products synthesized with different TDPA addition (a) NH3-TPD, (b) Py-IR spectra at 200 oC
SamplesBrønsted acidity / μmol·g-1Lewis acidity / μmol·g-1Total acidity / μmol·g-1
Z22-043.9333.2477.17
Z22-0.006845.3636.6482.00
Z22-0.011948.4140.3388.74
Z22-0.017052.8948.36101.25
Z22-0.022136.3042.1578.45
Z22-0.027219.7044.7964.49
Table 3  Py-IR analysis results of the synthesized products with different TDPA addition amounts
Fig.8  Comprehensive electron microscopy analysis results of Pt/Z22-0.0170-5L (a) SEM-EDS surface scanning mapping, (b) TEM image, (c) STEM image
Fig.9  Evaluation results of n-dodecane hydroisomerization (a) iso-hexadecane yield, (b) iso-hexadecane selectivity
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