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- W35593227 abstract "In this paper, a catalytic microchannel reactor integrated with highly efficient heat exchangers was used to demonstrate the significantly improved Fischer-Tropsch (FT) productivity by minimizing heat and mass transfer limitations in this three phase reaction system. A factor of up to 15 process intensification can be achieved for FT synthesis using microchannel reactors. In order to achieve high yields of naphtha and diesel range of hydrocarbons (C 5 -C 1 9 ), we have developed a unique structured catalyst system suitable for the deployment in microchannel reactor applications. This engineered catalyst structure is based on metallic monolith supports, uniformly coated with an improved catalyst formula. Such an ordered catalyst structure has the advantages of higher thermal conductivity and more reduced mass transfer resistance compared to the conventional catalysts. By tailoring the mass transfer limitations, we have demonstrated that this engineered catalyst produces hydrocarbons with narrower carbon distributions (mainly < C 2 5 ) than a conventional particulate catalyst at similar conversion and methane selectivity. In particular, majority of the synthesis products fall into the gasoline and diesel range. This unique product distribution, in turn, has a positive impact on process economics since a milder or no hydrocracker will be required in downstream product processing." @default.
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- W35593227 date "2005-07-23" @default.
- W35593227 modified "2023-09-27" @default.
- W35593227 title "Microchannel Catalytic Processes for Converting Biomass-Derived Syngas to Transportation Fuels" @default.
- W35593227 doi "https://doi.org/10.1021/bk-2005-0914.ch017" @default.
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