Hydrogen-iodide decomposition over Pd-CeO2 nanocatalyst for hydrogen production in sulfur iodine thermochemical cycle

被引:24
作者
Singhania, Amit [1 ]
Krishnan, Venkatesan V. [2 ]
Bhaskarwar, Ashok N. [1 ]
Bhargava, Bharat [3 ]
Parvatalu, Damaraju [3 ]
机构
[1] Indian Inst Technol, Dept Chem Engn, New Delhi 110016, India
[2] Teesside Univ, Sch Sci & Engn, Middlesbrough TS1 3BA, Cleveland, England
[3] ONGC Energy Ctr, 2nd Floor,Core 2, New Delhi 110092, India
关键词
Hydrogen-iodide decomposition; Palladium; Ceria; Catalytic activity; Hydrogen production; Sulfur-iodine cycle; HI DECOMPOSITION; ACTIVE-CARBON; CO OXIDATION; CERIA CATALYSTS; NANOPARTICLES; TEMPERATURE; PARTICLES; NANOTUBES; KINETICS; ZIRCONIA;
D O I
10.1016/j.ijhydene.2017.07.088
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
A highly active and stable catalyst for hydrogen-iodide decomposition reaction in sulfur iodine (SI) cycle has been prepared in the form of Pd-CeO2 nanocatalyst by sol-gel method with different calcination temperatures (300 degrees C, 500 degrees C, and 700 degrees C). XRD and TEM confirmed a size around 6-8 nm for Pd-CeO2 particles calcined at 300 degrees C. Raman study revealed large number oxygen vacancies in Pd-CeO2-300 when compared to Pd-CeO2-500 and Pd-CeO2-700. With increase in calcination temperature, the average particle size increased whereas the specific surface area and number of oxygen vacancies decreased. Hydrogen-iodide catalytic-decomposition was carried out in the temperature range of 400 degrees C-550 degrees C in a quartz-tube, vertical, fixed-bed reactor with 55 wt % aqueous hydrogen-iodide feed over Pd-CeO2 catalyst using nitrogen as a carrier gas. Pd-CeO2-300 showed hydrogen-iodide conversion of 23.3%, which is close to the theoretical equilibrium conversion of 24%, at 550 degrees C. It also showed a reasonable stability with a time-on-stream of 5 h. (C) 2017 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:3886 / 3891
页数:6
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