| Budget Amount *help |
¥17,680,000 (Direct Cost: ¥13,600,000、Indirect Cost: ¥4,080,000)
Fiscal Year 2020: ¥2,860,000 (Direct Cost: ¥2,200,000、Indirect Cost: ¥660,000)
Fiscal Year 2019: ¥2,860,000 (Direct Cost: ¥2,200,000、Indirect Cost: ¥660,000)
Fiscal Year 2018: ¥2,860,000 (Direct Cost: ¥2,200,000、Indirect Cost: ¥660,000)
Fiscal Year 2017: ¥3,380,000 (Direct Cost: ¥2,600,000、Indirect Cost: ¥780,000)
Fiscal Year 2016: ¥5,720,000 (Direct Cost: ¥4,400,000、Indirect Cost: ¥1,320,000)
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| Outline of Final Research Achievements |
Alumina-supported silica monolayer catalyst with pore diameter > 6 nm (Si surface density of 8 nm-2) dealkylated to remove all the alkyl chains with >C3 length from approximately 100% of alkyl aromatics with two or more rings in practical vacuum gas oil under the optimized conditions. Liquid phase separation of aromatics and aliphatics was enabled, and parameters in the kinetics of separation, which controlled the performance, were clarified. For partial hydrogenation of naphthalene into tetralin, 100% of naphthalene was converted into tetralin with a 99% selectivity on a dispersed molybdenum oxide monolayer catalyst, derived from phosphomolybdic acid). For the decomposition of tetralin, molybdenum-added * BEA zeolite showed a tetralin conversion of 95% and selectivity into LPG / alkylbenzene of 85%.
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