Conversion of Alcohols to Hydrocarbons Using a Dual Catalyst System
A catalyst and alcohol conversion technology, applied in the direction of catalysts, heterogeneous catalyst chemical elements, molecular sieve catalysts, etc., to reduce the problem of coke formation and improve stability
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[0115] To achieve the desired aromatics levels (less than 35 vol%) and benzene content (ie well below 1 vol%), gasoline is produced from bioethanol using a two-stage reactor system (two reactor beds in series). The reactors contain two different catalysts whereby two or more reactors are maintained at different temperatures. In the first reactor, the temperature range should be in the range of 300°C to 550°C (the first reactor was operated at 400°C unless otherwise specified). Higher temperatures may promote undesired coke formation. 300°C to 550°C temperature range for use with Si 2 o 2 -Al 2 o 3 Ni on (selective to ethylene) and Cu on MgO-modified SBA-15 (selective mainly to butadiene some ethylene), selectively producing olefinic mixtures; still other geological types of materials can be used.
[0116] e.g. Ni / SiO 2 -Al 2 o 3 Ethylene was selectively produced (95%) over long reaction times. In the case of Cu-MgO / SBA-15, the catalyst selectively produced butadiene a...
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