4.4 Article Proceedings Paper

Sustainable Desulfurization Processes Catalyzed by Titanium-Polyoxometalate@TM-SBA-15

Journal

TOPICS IN CATALYSIS
Volume 60, Issue 15-16, Pages 1140-1150

Publisher

SPRINGER/PLENUM PUBLISHERS
DOI: 10.1007/s11244-017-0801-5

Keywords

mu-Hydroxo dimeric titanium; Polyoxometalate; SBA-15; Oxidative desulfurization; Hydrogen peroxide

Funding

  1. national projects REQUIMTE-LAQV [FCT (Fundacao para a Ciencia e a Tecnologia)] [UID/QUI/50006/2013]
  2. FEDER (Fundo Europeu de Desenvolvimento Regional) under the PT Partnership Agreement
  3. FCT - Ministerio da Ciencia, Tecnologia e Ensino Superior (MCTES) [SFRH/BD/95571/2013, SFRH/BPD/73191/2010]
  4. European Union - Ministerio da Ciencia, Tecnologia e Ensino Superior (MCTES) [SFRH/BD/95571/2013, SFRH/BPD/73191/2010]
  5. European Social Fund through the program POPH of QREN
  6. Fundação para a Ciência e a Tecnologia [SFRH/BPD/73191/2010, SFRH/BD/95571/2013] Funding Source: FCT

Ask authors/readers for more resources

A titanium-polyoxometalate with a mu-hydroxo dimeric structure [(PW11O39Ti)(2)OH](7-) ((PW11Ti)(2)OH) was used efficiently for the desulfurization of a model diesel containing a mixture of various refractory sulfur compounds present in real fuels. The catalytic performance of the mu-hydroxo dimeric compound was compared in its homogeneous form and also when immobilized in the trimethylammonium-functionalized SBA-15 ((PW11Ti)(2)OH@TM-SBA-15). An optimization study was performed using the homogeneous and heterogeneous catalysts to obtain high catalytic efficiency, sustainability and cost-effectiveness of the system. Different optimized conditions were found using the homogeneous and heterogeneous catalysts. Lower amounts of solvent extraction (MeCN, 175 mu L), catalyst (0.5 mu mol of active center) and oxidant (50 mu L) were used to produce sulfur-free model diesel after 2 h at 70 degrees C, using the heterogeneous (PW11Ti)(2)OH@TM-SBA-15 catalyst. On the other hand, complete desulfurization was achieved with homogeneous (PW11Ti)(2)OH catalyst after only 40 min, although higher amounts of MeCN (750 mu L), catalyst (1.5 mu mol) and oxidant (75 mu L) were used. Both systems combined liquid-liquid extraction and catalytic oxidation. Using the heterogeneous catalyst, adsorption of oxidized-sulfur compound was also observed. Both homogeneous and heterogeneous desulfurization systems presented a high capacity to be reused/recycled for consecutive desulfurization cycles.

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