Integrated reactor for ionic liquid alkylation using bio-ethylene feedstock

An alkylation process is described. The process involves alkylation of isobutane and ethylene in a loop reactor using an ionic liquid catalyst as a continuous phase. The alkylate typically has a research octane number of at least about 93, and the olefin conversion is typically at least about 95%.

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Bibliographische Detailangaben
Hauptverfasser: Chang, Bong-Kyu, Timken, Hye-Kyung Cho, Luo, Huping
Format: Patent
Sprache:eng
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Zusammenfassung:An alkylation process is described. The process involves alkylation of isobutane and ethylene in a loop reactor using an ionic liquid catalyst as a continuous phase. The alkylate typically has a research octane number of at least about 93, and the olefin conversion is typically at least about 95%.