2016
DOI: 10.1021/acscatal.6b00655
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Production of Linear Octenes from Oligomerization of 1-Butene over Carbon-Supported Cobalt Catalysts

Abstract: Linear octenes were produced in high (70–85%) selectivity from oligomerization of liquid 1-butene using carbon-supported cobalt oxide catalysts in a continuous flow reactor. The liquid products were characterized by two-dimensional gas chromatography–mass spectrometry. Above 95% of the oligomers were C8 olefins, with the other products primarily being branched C12 olefins. The linear octene products at a conversion of 9.77% decreased in selectivity according to 3-octene > trans-2-octene > cis-2-octene > 4-octe… Show more

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Cited by 29 publications
(39 citation statements)
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“…Figure S1 illustrates the typical step of the Reaction scheme in butene oligomerization. According to a previous report [53], oligomerization of light olefins is a cascade reaction. Traditionally, butene derivatives, C 8 (octenes), are produced by dimerization, and C 8 can further react with surplus butene to produce largely hydrocarbons.…”
Section: Catalytic Performancementioning
confidence: 97%
“…Figure S1 illustrates the typical step of the Reaction scheme in butene oligomerization. According to a previous report [53], oligomerization of light olefins is a cascade reaction. Traditionally, butene derivatives, C 8 (octenes), are produced by dimerization, and C 8 can further react with surplus butene to produce largely hydrocarbons.…”
Section: Catalytic Performancementioning
confidence: 97%
“…The 13 wt % cobalt on carbon catalyst was synthesized based on a wetness impregnation method previously described in the literature. , The catalyst is denoted as CoO X /N–C. The chromium-promoted cobalt on carbon catalyst was synthesized as follows: 2.00 g of sieved activated carbon (Norit, Darco MRXm-1721; BET surface area 600–800 m 2 /g; 250–600 μm particle size) was first treated with 1.8 mL of 30% NH 4 OH solution at room temperature.…”
Section: Methodsmentioning
confidence: 99%
“…The ethylene oligomerization reactions were conducted in a tubular down-flow fixed-bed reactor described elsewhere. , The length of the reactor tube is 30.5 cm long, and the catalyst bed is between 2.07 cm (0.5 g) and 8.29 cm (2.0 g). The temperature is measured by a built-in thermocouple touching the reactor wall at the center of the catalyst bed.…”
Section: Methodsmentioning
confidence: 99%
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“…Jet fuel is one of the most demanded transportation fuels. During the past few years, great efforts have been devoted to the synthesis of jet fuel range hydrocarbons by the C–C coupling reactions (such as aldol condensation, 3 hydroxyalkylation/alkylation, 4 alkylation, 5 Michael addition, 6 olefin oligomerization, 7 benzoic condensation, 8 Robinson annulation 9 and photo-catalyzed 2 + 2 cycloaddition 10 ) of lignocellulose derived platform compounds, followed by hydrodeoxygenation (HDO) or hydrogenation. However, most of the reported work was focused on the synthesis of jet fuel with cellulose and hemicellulose derived platform compounds.…”
Section: Introductionmentioning
confidence: 99%