Optimization of Cu/MnO <sub>2</sub> catalyst for enhanced methane bi-reforming: a response surface methodology approach for sustainable syngas production-Reference-Cited by-同舟云学术

Optimization of Cu/MnO ₂ catalyst for enhanced methane bi-reforming: a response surface methodology approach for sustainable syngas production

Published:2024-08-04 Issue:11 Volume:211 Page:1713-1732
ISSN:0098-6445
Container-title:Chemical Engineering Communications
language:en
Short-container-title:Chemical Engineering Communications

Author:

Ibrahim Irna Haslina¹,Shafiqah Mohd-Nasir Nor¹,Suhaimi Nuremirah Syafiqah¹,Li Maoshuai²,Van Cuong Nguyen³,Zainal Abidin Sumaiya⁴³

Affiliation:

1. Faculty of Chemical and Process Engineering Technology, Universiti Malaysia Pahang Al-Sultan Abdullah, Kuantan, Pahang, Malaysia

2. School of Chemical Engineering and Technology, Key Laboratory for Green Chemical Technology of Ministry of Education, Collaborative Innovation Center of Chemical Science and Engineering, National Industry-Education Integration Platform of Energy Storage, Tianjin University, Tianjin, China

3. Faculty of Chemical Engineering, Industrial University of Ho Chi Minh City, Ho Chi Minh City, Vietnam

4. Centre for Research in Advanced Fluid & Processes (FLUID CENTRE), Universiti Malaysia Pahang Al-Sultan Abdullah, Kuantan, Pahang, Malaysia

Funder

Universiti Malaysia Pahang Al-Sultan Abdullah

UMPSA Distinguished Research

Publisher

Informa UK Limited

Link

https://www.tandfonline.com/doi/pdf/10.1080/00986445.2024.2383577

Reference51 articles.

1. CO2-reforming of methane to produce syngas over Co-Ni/SBA-15 catalyst: Effect of support modifiers (Mg, La and Sc) on catalytic stability

2. Tailoring strontium-promoted alumina-zirconia supported Ni-catalysts for enhanced CO2 utilization via dry reforming of methane: Sr loading effects and process optimization

3. Process Optimization for Syngas Production from the Dry Reforming of Methane over 5Ni+3Sr/10Zr+Al Catalyst Using Multiple Response Surface Methodology

4. Combined steam and CO2 reforming of methane (CSCRM) over Ni–Pd/Al2O3 catalyst for syngas formation

5. Ni/Y2O3–ZrO2 catalyst for hydrogen production through the glycerol steam reforming reaction