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Deep desulfurization of fuels catalyzed by surfactant-type decatungstates using H2O2as oxidant

Authors
Journal
Fuel
0016-2361
Publisher
Elsevier
Publication Date
Volume
88
Issue
3
Identifiers
DOI: 10.1016/j.fuel.2008.11.010
Keywords
  • Surfactant-Type Decatungstates
  • Catalytic Oxidation
  • Deep Desulfurization
  • Hydrogen Peroxide

Abstract

Abstract Oxidation of dibenzothiphene (DBT) in model oil with H 2O 2 using surfactant-type decatungstates Q 4W 10O 32 (Q = (CH 3) 3NC 16H 33, (CH 3) 3NC 14H 29, (CH 3) 3NC 12H 25 and (CH 3) 3NC 10H 21) as catalysts was studied. The surfactant-type decatungstates were synthesized and characterized. The suitable reaction condition of deep desulfurization was suggested: n(DBT): n(catalyst): n(H 2O 2) = 1:0.01:3, 60 °C for 0.5 h, under which the DBT conversion can reach 99.6% with [(CH 3) 3NC 16H 33] 4W 10O 32 as catalyst. The length of carbon chains of quaternary ammonium cations played a vital role in the catalytic activity of surfactant-type decatungstates, that is, the longer the carbon chain of quaternary ammonium cation of a catalyst was, the better the activity of this catalyst showed. [(CH 3) 3NC 16H 33] 4W 10O 32 exhibited the best catalytic performance and can be recycled for six times without significant decrease in catalytic activity. Using benzothiphene (BT) and 4,6-dimethyldibenzothiphene (4,6-DMDBT) as substrates in model oil, surfactant-type decatungstates also showed high catalytic activity. During desulfurization process, BT conversion can reach 99.6% at 3.25 h, while 99.4% of 4,6-DMDBT conversion reached at 1.25 h, with the temperature of 60 °C under atmospheric pressure. The sulfone can be separated from the oil using N, N-dimethylformamide (DMF) as an extractant, and the sulfur content can be lowered from 1000 to 4 ppm. For real diesel, the sulfur removal can reach 93.5% after five times extraction.

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