Abstract
Noble metal based catalysts being 0.8 wt.%Pd and 0.35 wt.%Pt supported on HZSM-5 zeolite were subjected to the investigation. Physico-chemical characteristics of catalysts were determined by the methods of nitrogen physi-sorption, SEM, XRD, TEM, NH3-TPD, TPR, and Hydrogen Pulse Chemi-sorption (HPC). Activity of catalysts in the isomerization of n-C6 and n-C5 + n-C6 mixture was studied in a micro-flow reactor in the temperature range of 225 − 325 oC at pressure of 0.1 MPa and 0.7 MPa; the molar ratio H2/ hydrocarbon: 5.92, concentration of n-C5 or n-C6: 4.6 mol.%, GHSV 2698 h-1. The stability of catalysts was also determined. The obtained catalysts expressed high acid density, good reducing property, and high metal dispersion with the cluster size in the range of nanometer. They were an excellent contact for isomerization of n-hexane or n-C5 + n-C6 mixture with high conversion, selectivity, and yield. At optimal temperature, n-paraffin conversions were as high as 57 – 63 % and selectivity was 90 %. Pressure had the positive effect to the catalyst conversion, selectivity, and stability. At 0.7 MPa, both catalysts produced 66- 69 RON liquid product containing friendly environmental iso-paraffins which is superior blending stock for green gasoline.
Highlights
The production of gasoline for automobiles has been becoming challenged in the aspect of environmental concerns
This work dealt with Pd and Pt catalysts supported on HZSM-5 for hydroisomerization of the mixture of n-pentane and nhexane
The impregnation of Pd or Pt onto HZSM-5 did not change the peak position but slightly increased the intensity of the peaks and the crystallinity of HZSM-5 due to the elimination of distorted aluminum sites [1]. These results indicated that Pd or Pt may interact with defect sites stabilizing the crystalline structure of HZSM-5 and making framework structure to be more ordered
Summary
The production of gasoline for automobiles has been becoming challenged in the aspect of environmental concerns. Finding out new catalyst with superior H2 spillover effect is evaluable for isomerization reaction. This work dealt with Pd and Pt catalysts supported on HZSM-5 for hydroisomerization of the mixture of n-pentane and nhexane. This study was conducted in order to study the actual effect of pressure to the catalyst activity and stability.
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