Abstract
In the present work, zeolite Y has been synthesized successfully by sol-gel
method.Zeolite was synthesized by crystallization of the final gel which consist from
seeding and feed stock gels at 85 oC. HY zeolite was prepared by an ion exchange
process with ammonium chloride solution and then loaded with different percentages
of platinum and titanium by the wet - impregnation method.
X-ray Diffraction (XRD), X-ray Florescence (XRF), Scanning Electron
Microscopy (SEM), BET surface area and, Crushing strength were used to
characterize the synthesized and prepared catalysts . Results showed high crystallinity
90% with silica to alumina ratio 5 for HY, high surface area of 600 m2
/g and pore
volume of 0.38 cm3
/g.
The activity of the prepared zeolite was investigated using a pilot plant unit for
the catalytic reforming of Iraqi heavy naphtha. All prepared catalysts were
investigated at temperatures of 490,500 and 510oC ,pressure of 20 bar, H2 /HC ratio 3
and LHSV 1.4.hr-1
.
Reformate was produced with 86 RON and 94% yield at 510ºC and 20 bar
using 0.13 wt.% Pt - 0.75 wt.% Ti loaded on synthesized HY.
method.Zeolite was synthesized by crystallization of the final gel which consist from
seeding and feed stock gels at 85 oC. HY zeolite was prepared by an ion exchange
process with ammonium chloride solution and then loaded with different percentages
of platinum and titanium by the wet - impregnation method.
X-ray Diffraction (XRD), X-ray Florescence (XRF), Scanning Electron
Microscopy (SEM), BET surface area and, Crushing strength were used to
characterize the synthesized and prepared catalysts . Results showed high crystallinity
90% with silica to alumina ratio 5 for HY, high surface area of 600 m2
/g and pore
volume of 0.38 cm3
/g.
The activity of the prepared zeolite was investigated using a pilot plant unit for
the catalytic reforming of Iraqi heavy naphtha. All prepared catalysts were
investigated at temperatures of 490,500 and 510oC ,pressure of 20 bar, H2 /HC ratio 3
and LHSV 1.4.hr-1
.
Reformate was produced with 86 RON and 94% yield at 510ºC and 20 bar
using 0.13 wt.% Pt - 0.75 wt.% Ti loaded on synthesized HY.
Keywords
Naphtha catalytic reforming
Sol-gel method.
Zeolite Y