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TECHNICAL PAPERS: Gas Turbines: Advanced Energy Systems

Development of Methanol Steam Reformer for Chemical Recuperation

[+] Author and Article Information
T. Nakagaki, T. Ogawa, K. Murata, Y. Nakata

Toshiba Corporation Power and Industrial Systems Research and Development Center 1, Toshiba-cho, Fuchu-shi, Tokyo, 183-8511, Japan

J. Eng. Gas Turbines Power 123(4), 727-733 (Jan 11, 2000) (7 pages) doi:10.1115/1.1359238 History: Revised January 11, 2000; Received July 01, 2000
Copyright © 2001 by ASME
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References

Figures

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Effect of Tw on temperature and conversion profiles at P=10 atm,Tin=518 K,Xin=0 percent, and G=0.25 kg/(sm2)
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Effect of mass flux on temperature and conversion profiles at P=10 atm,Tw=548 K,Tin=518 K and Xin=0 percent
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Effect of Xin on temperature and conversion profiles at P=10 atm,Tw=548 K,Tin=518 K and G=0.25 kg/(sm2)
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Schematic illustration of geometry, boundary conditions, and coordinate system
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Temperature and methanol mole fraction profile at P=10 atm,Tw=548 K,Tin=518 K,G=0.25 kg/(sm2) and Xin=0 percent
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Influence of flow rate on reaction rate at T=513 K and Xin=0 percent
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Dependence of reaction rate on total pressure at G=0.25 kg/(sm2) and Xin=0 percent
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Effect of temperature on reaction rate at G=0.25 kg/(sm2) and Xin=0 percent
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Correlation between reaction rate and methanol mole fraction at G=0.25 kg/(sm2),T=513 K and Xin=0 percent
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Relation between reaction rate and methanol conversion at G=0.25 kg/(sm2)
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Effect of pressure on temperature and conversion profiles at Tw=548 K,Tin=518 K,Xin=0 percent and G=0.25 kg/(sm2)

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