doi: 10.3850/978-981-08-7614-2_IMPRES013


Hydrogen Production Through Ethanol Steam Reforming on Conducting Heating Alumite Catalysts


Ha Thi Khanh Nguyen, Daisuke Saitoh, Hideki Kawachi, Yu Guo, Makoto Sakurai and Hideo Kameyama

Department of Applied Chemistry, Tokyo University of Agriculture and Technology, Naka-chou 2-24-16 , Koganei-shi, Tokyo-to, Japan.

50010642317@st.tuat.ac.jp

ABSTRACT

The aim of this research is to investigate a hydrogen production system using low concentration of ethanol derived from biomass fermentation-renewable materials. By using a non-equilibrium box reactor containing CO2 absorption agent and alumite catalyst in plate type, CO2 and CO can be removed from the reaction field, without CO converting and dividing reactors. Due to insertion of CO2 absorbent, it helped to build up hydrogen selectivity and decrease carbon monoxide formation.

First, supporting method of the alumite catalysts was studied to increase the durability of the catalysts and prevent carbon formation. The durability of the CO2 absorption agent was also studied to improve the using times and prevent abrasion phenomenon. Then, the amount of hydrogen that was needed to feed in the 1kW class of household fuel cell was assumed. From this condition, required catalysts and CO2 absorbent were computed. After that, the box reactor was designed in order to introduce these plates adequately and calculation of the reactor volume was carried out.

Keywords: Ethanol, Non-equilibrium system, CO2 absorbent.



     Back to TOC

FULL TEXT(PDF)