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Evrim SAHIN
Submitted to Professor Vincenzo PALMA
Supervisor Ph.D. Antonio RICCA
*
*
• Indoor outdoor carpeting
• Propylene glycols for paints
household detergents
*
 Synthesis Of Isopropanol
 Detergents
 Copolymer For Polypropylene
 Used in Calibration Gas Mixtures for
Petrochemical Industry
 Environmental Emission Monitoring
 Trace Impurity Analyzers
*
 Steam Cracking
 FCC (Fluid Catalytic Cracking)
 Catalytic
Dehydrogenation
 Oleflex UOP
 Catofin ABB Lummus
 STAR (Philips Petroleum Company)
 FBD-4 Snamprogetti
*
 The Group VIII metals (mainly platinum with tin)
 Chromium oxides on alumina or zirconia
 Supported iron oxides, with promoters
 Gallium oxide as a supported or
included in zeolite structures
 Copper, for the dehydrogenation of alcohols to
aldehydes
*
*
*
*
*
*
*
The active metal precursor is dissolved in
an aqueous or organic solution


* Than dried and calcined catalysts were
crushed and sieved
* Catalyst characterization [temperature-programmed
reduction(TPR)] were performed in multipurpose
apparatus(oven reactor).
*
*
• heating rate of 10ºC/min up to 600°C
TPRPDH
*
*
*
*
*
*
*
*
• A not negligible homogeneous reactions contribute is observed, due to
the reactor configuration
• Minimization of reactants residence time at high temperature out
of the catalytic volume
• Platinum shows an evident contribute in catalyst activity
• Tin catalyst decreases catalyst deactivation rate
• A relevant coke formation was observed in all the catalytic
configurations
• Lower temperature tests shows a very lower propane conversion, but a
sensible improvement in propylene selectivity
*For your

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Presentazione

  • 1. Evrim SAHIN Submitted to Professor Vincenzo PALMA Supervisor Ph.D. Antonio RICCA *
  • 2.
  • 3. * • Indoor outdoor carpeting • Propylene glycols for paints household detergents
  • 4. *  Synthesis Of Isopropanol  Detergents  Copolymer For Polypropylene  Used in Calibration Gas Mixtures for Petrochemical Industry  Environmental Emission Monitoring  Trace Impurity Analyzers
  • 5. *  Steam Cracking  FCC (Fluid Catalytic Cracking)  Catalytic Dehydrogenation  Oleflex UOP  Catofin ABB Lummus  STAR (Philips Petroleum Company)  FBD-4 Snamprogetti
  • 6. *  The Group VIII metals (mainly platinum with tin)  Chromium oxides on alumina or zirconia  Supported iron oxides, with promoters  Gallium oxide as a supported or included in zeolite structures  Copper, for the dehydrogenation of alcohols to aldehydes
  • 7.
  • 8.
  • 10. * *
  • 11.
  • 12. * The active metal precursor is dissolved in an aqueous or organic solution  
  • 13. * Than dried and calcined catalysts were crushed and sieved * Catalyst characterization [temperature-programmed reduction(TPR)] were performed in multipurpose apparatus(oven reactor).
  • 14. *
  • 15. * • heating rate of 10ºC/min up to 600°C TPRPDH
  • 16.
  • 17. *
  • 18. *
  • 19. *
  • 20. *
  • 21. *
  • 22. *
  • 23. *
  • 24. * • A not negligible homogeneous reactions contribute is observed, due to the reactor configuration • Minimization of reactants residence time at high temperature out of the catalytic volume • Platinum shows an evident contribute in catalyst activity • Tin catalyst decreases catalyst deactivation rate • A relevant coke formation was observed in all the catalytic configurations • Lower temperature tests shows a very lower propane conversion, but a sensible improvement in propylene selectivity