4.8 Article

Desulfurization of liquid fuels by extraction and sulfoxidation using H2O2 and [CpMo(CO)3R] as catalysts

Journal

APPLIED CATALYSIS B-ENVIRONMENTAL
Volume 230, Issue -, Pages 177-183

Publisher

ELSEVIER
DOI: 10.1016/j.apcatb.2018.02.036

Keywords

Oxidative desulfurization; Extraction; Ionic liquid; Hydrogen peroxide; Cyclopentadienyl molybdenum complexes

Funding

  1. project REQUIMTE-LAQV (FCT, Fundacao para a Ciencia e a Tecnologia) [POCI-01-0145-FEDER-007265, UID/QUI/50006/2013]
  2. CICECO - Aveiro Institute of Materials (FCT) - national funds through the FCT/MEC [POCI-01-0145-FEDER-007679, UID/CTM/50011/2013]
  3. FEDER (Fundo Europeu de Desenvolvimento Regional)
  4. FCT - MCTES [SFRH/BD/102783/2014, SFRH/BPD/108541/2015]
  5. European Union - MCTES [SFRH/BD/102783/2014, SFRH/BPD/108541/2015]
  6. European Social Fund through the program POPH of QREN
  7. Fundação para a Ciência e a Tecnologia [SFRH/BD/102783/2014] Funding Source: FCT

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Efficient and recyclable liquid-liquid extraction and catalytic oxidative desulfurization (ECODS) systems for the removal of refractory sulfur compounds from liquid fuels are reported that use the cyclopentadienyl molybdenum tricarbonyl complexes [CpMo(CO)(3)Me] (1), [CpMo(CO)(3)(CH2-PC6H4-CO2Me] (2) and [CpMo(CO)(3)CH2COOH] (3) as catalyst precursors. An ionic liquid, 1-butyl-3-methylimidazolium hexafluorophosphate, was used as both extractant and reaction medium, entrapping the active homogeneous Mo-VI catalysts that are formed in situ under the operating catalytic conditions (aqueous H2O2 as oxidant, 50 degrees C). The high sulfoxidation activity of the catalyst formed from 1 was largely responsible for enabling > 99% desulfurization within 1 h of a model oil containing 1-benzothiophene, dibenzothiophene, 4-methyldibenzothiophene and 4,6-dimethyldibenzothiophene (2000 ppm S). The IL/catalyst phase could be repeatedly recycled with no loss of desulfurization efficiency. By sequentially performing extractive desulfurization and ECODS steps, 83-84% sulfur removal was achieved for untreated real diesel and jet fuel samples with initial sulfur contents of ca. 2300 and 1100 ppm, respectively.

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