Synthesis of Mesoporous Nickel-Ceria Catalyst Using Tri-Block Co-Polymer Template for Low–Temperature Water-Gas-Shift Reaction

Monday, November 17, 2008: 4:55 PM
Room 203-A (Pennsylvania Convention Center)

Jiann-Horng Lin, Department of Chemical and Materials Engineering, University of Cincinnati, Cincinnati, OH
Prakash Biswas, Department of Chemical and Materials Engineering, University of Cincinnati, Cincinnati, OH
Vadim V. Guliants, Department of Chemical and Materials Engineering, University of Cincinnati, Cincinnati, OH

Abstract:

Recently, the water-gas shift reaction has become very important because of its potential use in conjunction with fuel cell power generation and production of high purity H2

. It has been reported that novel metal supported on ceria is a superior catalyst for the water-gas shift reaction. Ceria is also a crucial component of automotive three-way emission control catalysts. Self-assembly of block copolymers provides a versatile approach to the creation of nanostructured materials. Mesoporous inorganic materials, templated by tri-block copolymer self assemblies usually have high surface areas, which promising for catalytic applications.

Mesoporous cerium oxide and nickel-loaded cerium oxide catalysts were synthesized by evaporation-induced self-assembly (EISA) followed by direct calcination to remove the polymer template. A novel tri-block copolymer of different length ratio was used as a template directing agent. Nickel was added to the mesoporous cerium oxide support by incipient wetness impregnation method. Lanthanum (10 at. %) was used as a stabilizing agent of cerium oxide support. The catalysts were characterized by scanning electron microscopy, transmission electron microscopy, X-ray diffraction, thermogravimetric analysis and N2 physisorption. The BET results showed that the surface areas of the catalysts significantly increased due to the addition of lanthanum to the nickel-cerium oxide. The X-ray diffraction revealed that the crystal size and structure were extremely sensitive to the conditions of heat treatment. The catalytic activity for the low temperature water-gas shift reaction was evaluated over nickel-doped and undoped cerium-lanthanum oxide catalysts in a tubular flow reactor. The temperature of the reaction was varied from 150 to 350oC

. The flow rate and other reaction condition were optimized. The experimental results showed that the catalytic activities of cerium-lanthanum oxide catalysts were significantly increased by the addition of small amount of nickel.

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See more of this Session: Catalytic Hydrogen Generation - General III
See more of this Group/Topical: Catalysis and Reaction Engineering Division