3D‐Printed Bioinspired Meta‐Structural Perovskite Catalysts for Dry Reforming of CH <sub>4</sub> and CO <sub>2</sub>

C Cunbao Huo (State Key Laboratory for Manufacturing Systems Engineering Xi'an Jiaotong University No. 28 Xian Ning West Road Xi'an 710049 China) S Shuwang Wu (State Key Laboratory for Manufacturing Systems Engineering Xi'an Jiaotong University No. 28 Xian Ning West Road Xi'an 710049 China) R Rongjiang Zhang (College of Chemical Engineering Xi'an Jiaotong University No. 28 Xian Ning West Road Xi'an 710049 China) Z Zhiqiang Wu X Xiaoyong Tian (State Key Laboratory for Manufacturing Systems Engineering Xi'an Jiaotong University Xi'an China) L Lei Tan K Kexin Li Y Yao Yang B Baojie Wang (Lanzhou Petrochemical Research Center Petrochemical Research Institute PetroChina Company Limited No.1 Heshui North Road Lanzhou 730060 China) Z Zhun Hu (College of Chemical Engineering Xi'an Jiaotong University No. 28 Xian Ning West Road Xi'an 710049 China) L Lingling Wu D Dichen Li

Abstract

Abstract Conventional packed‐bed catalysts suffer from single‐scale porosity, insufficient mechanical strength, and suboptimal mass transfer efficiency. Inspired by the fractal structure of the lung bronchi, a design and 3D printing method for gradient meta‐structural catalysts is proposed by integrating synthesized LaFe 0.5 Ni 0.5 O 3 (LFN) perovskite with pseudo‐boehmite, achieving ultralow pressure drop and high catalytic efficiency. Computational fluid dynamics and reaction simulations guide the design of uniform and gradient‐structured catalysts with hierarchical woodpile channels (0.5–3 mm). Compared with homogeneous catalysts, the gradient design theoretically exhibits 1.5‐fold and 1.1‐fold increases in flow velocity and hydrogen production, respectively. Meta‐structural catalysts are fabricated with gradient multi‐peak pore distribution (9.32 nm, 103.75 nm) by regionally modulating unit cell sizes and LFN content (11–35%) combined with the dehydroxylation of pseudo‐boehmite. 3D‐printed perovskite catalysts demonstrate a 78.7‐fold increase in specific surface area (102.26 m 2 g −1 ) and compressive strength of 8.48 MPa. In dry reforming of methane (DRM) tests, it achieves 82.13% CH 4 conversion, and 9.69 mmol g −1 syngas yield, outperforming conventional powder‐packed beds by 10% efficiency. This study achieves mass transfer and catalytic performance coupling by tuning gradient hierarchical pores and tailoring flow dynamics, offering a paradigm for robust, high‐efficiency catalyst design across diverse applications.

Article Details

Volume / Issue Vol. 37, Issue 44
Published November 01, 2025
ISSN 0935-9648
Publisher Unknown Publisher

Journal Info

Advanced Materials

Unknown Publisher

ISSN: 0935-9648 Physical Sciences

Authors (12)

C

Cunbao Huo

State Key Laboratory for Manufacturing Systems Engineering Xi'an Jiaotong University No. 28 Xian Ning West Road Xi'an 710049 China

S

Shuwang Wu

State Key Laboratory for Manufacturing Systems Engineering Xi'an Jiaotong University No. 28 Xian Ning West Road Xi'an 710049 China

R

Rongjiang Zhang

College of Chemical Engineering Xi'an Jiaotong University No. 28 Xian Ning West Road Xi'an 710049 China

Z

Zhiqiang Wu

X

Xiaoyong Tian

State Key Laboratory for Manufacturing Systems Engineering Xi'an Jiaotong University Xi'an China

L

Lei Tan

K

Kexin Li

Y

Yao Yang

B

Baojie Wang

Lanzhou Petrochemical Research Center Petrochemical Research Institute PetroChina Company Limited No.1 Heshui North Road Lanzhou 730060 China

Z

Zhun Hu

College of Chemical Engineering Xi'an Jiaotong University No. 28 Xian Ning West Road Xi'an 710049 China

L

Lingling Wu

D

Dichen Li