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Study of Mass Transfer Resistant Effect during Syn Gas and Hydrogen Production through CO2/CH4 Dry Reforming on La/Mg Supported Co-Ni/MSU-S Zeolite


Article Information

Title: Study of Mass Transfer Resistant Effect during Syn Gas and Hydrogen Production through CO2/CH4 Dry Reforming on La/Mg Supported Co-Ni/MSU-S Zeolite

Authors: Roohul Amin, Bingsi Liu, Sana Ullah, Ploywarin Sangsomboon, Faiq Saeed

Journal: ˜The œLighthouse

HEC Recognition History
No recognition records found.

Year: 2022

Volume: 1

Issue: 2

Language: en

Keywords: mass transfer resistant effect,xLa/mgyCozNi/MSU-SH2 and syn gas synthesismethane dry reforminggreater stability and activist

Categories

Abstract

In this study five different catalysts xLa/MgyCo-7Ni /MSU-S are synthesized through sol-gel procedure and further tested for XRD, HRTEM, FT-IR, H2-TPR, CO2-TPD, and O2-TPO skills. The mass transfer resistant effect, stability and activity of the catalytic samples were observed for syn gas and H2gas synthesis at different reaction temperatures and various space velocities (GHSV) at atmospheric pressure. Space velocities of 2.4- 3.2 × 104 mL/g-1h-1 were used for the determination of mass transfer resistant effect, catalytic  performance and composition of the catalyst at different reaction temperatures (700-800 oC) retaining constant atmospheric pressure during CO2/CH4 dry reforming reaction. The reaction outcomes showed that nanoparticles of nickel are highly discreted upon the promotion of Mg, La & Co oxides over MSU-S (mesoporous zeolite) through firmly contact of metal ions with HO-Si-groups of zeolite. Oxides of La (La2O3) in 1-3LayCozNi/MSU-S, which showed greater catalytic activity than 1-3Mg supported such catalysts. Among all five catalysts the N-/MSU-S doped with 3%La and 2%Co confirmed the best active catalyst in all respects with stability up to 75 h at of 750 oC. The catalyst also showed less mass transfer resistant effect at (GHSV) of 24000 mL/g-1h-1 than 32000 mL/g-1h-1


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