Dynamic operation of water gas shift reaction over Fe2O3/Cr2O3/CuO catalyst in Pd/Al2O3 membrane reactor

2nd international Tropical Renewable Energy Conference 2017

Budhi, Yogi Wibisono^1 ; Putri, Dhinny Dwi^1 ; Husna, Afifa^1 ; Irawan, Hans Kristian^1 ; Miyamoto, Manabu^2 ; Uemiya, Shigeyuki^2

Chemical Engineering Study Program, Institut Teknologi Bandung, Jl. Ganesha 10, Bandung, Indonesia^1

Department of Materials Science and Technology, Gifu University, 1-1 Yanagido, Gifu

501-1193, Japan^2

关键词: Dynamic operations;    Gas residence time;    Pressure swing adsorption;    Process intensification;    Production of hydrogen;    Technical specifications;    Water gas shift (WGS) reaction;    Water gas shift reactors;   

Others  :  https://iopscience.iop.org/article/10.1088/1755-1315/105/1/012020/pdf
DOI  :  10.1088/1755-1315/105/1/012020

来源: IOP

【 摘 要 】

Hydrogen has been considered as promising energy carrier that can be produced from renewable resources, such as biomass through gasification. This process results in producer gas containing CO, CO2, H2, N2, and CH4. The conventional enhancement of hydrogen is typically conducted using several unit operations such as water gas shift reactor (WGSR) and separation unit such as Pressure Swing Adsorption (PSA). Process intensification offers a new method to integrate both WGSR and separation unit into single membrane reactor. This research aimed to investigate the influence of dynamic operation on membrane reactor performance. The steady state fixed bed reactor and membrane reactor were used as base case to judge the performance of dynamic membrane reactor. The water gas shift reaction over Fe2O3/Cr2O3/CuO was carried out at 350°C and 1 atm by varying the feed composition and gas residence time. The feed composition ratio of H2O/CO consisted of 2 and 3 on mole basis, while the gas residence times were 1.2 s and 2.3 s. The membrane reactor consists of shell and tube sides made of Pd/Al2O3material with technical specification of 10 mm inner diameter, 20 μm Pd thickness supported by alumina, and 10 cm reactor length. The compositions of the feed gas and products were measured using gas analysers such CO gas detector (Bacharach PCA®3) and H2gas detector (Cosmos XP-3140). The dynamic operation was performed following the square wave perturbation of the feed gas at switching time of 15 s. The experiment results showed that increasing the feed composition ratio and gas residence time increased the conversion of CO and hydrogen production in the fixed bed reactor and membrane reactor. Higher production of hydrogen also improved the recovery of hydrogen in membrane reactor. The use of membrane reactor increased significantly the conversion of CO when compared to fixed bed reactor. Moreover, the dynamic membrane reactor would give much better performance in term of CO conversion and hydrogen recovery. The stability of the Pd/Al2O3membrane reactor was proven for at least 10 h operation.