| Budget Amount *help |
¥19,500,000 (Direct Cost: ¥15,000,000、Indirect Cost: ¥4,500,000)
Fiscal Year 2012: ¥4,290,000 (Direct Cost: ¥3,300,000、Indirect Cost: ¥990,000)
Fiscal Year 2011: ¥5,460,000 (Direct Cost: ¥4,200,000、Indirect Cost: ¥1,260,000)
Fiscal Year 2010: ¥9,750,000 (Direct Cost: ¥7,500,000、Indirect Cost: ¥2,250,000)
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| Research Abstract |
In order to construct a novel hydrogen production system, a honeycomb-type nickel-based catalyst systemwas constructed by a combination technique consisting of a sol-gel method and an electroless plating on a stainless steel substrate. The constructed system demonstrated high reforming property of methane steam reforming and high hydrogen production ability close to the equilibrium conversion. The multifunctional reforming system, which combined with a catalytic combustion through the reactor wall, was also constructed. This combined reforming system enabled a rapid supply of thermal energy to reactive zone by conductive heat transfer and produced an improvement of a great advance of hydrogen production ability.
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