Preparation of Pt/Al2O3-Cl Catalyst and Investigation of Operating Variables Effects on Isomerization Reaction

A high chlorinated alumina catalyst obtained by treating Pt/γ-Al2O3 (0.25 wt. % Pt) samples with two mixtures of CCl4/N2 and CCl4/N2/H2 was tested for the hydroisomerization of C6 alkane. The conversion of n-hexane feed was diluted with hydrogen performed with different H2/HC ratios at various tempe...

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Published in:Journal of chemical and petroleum engineering (Online) Vol. 52; no. 1; pp. 13 - 21
Main Authors: Mansour Jahangiri, Fatollah Salehirad, Shahram Alijani
Format: Journal Article
Language:English
Published: University of Tehran 01-06-2018
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Abstract A high chlorinated alumina catalyst obtained by treating Pt/γ-Al2O3 (0.25 wt. % Pt) samples with two mixtures of CCl4/N2 and CCl4/N2/H2 was tested for the hydroisomerization of C6 alkane. The conversion of n-hexane feed was diluted with hydrogen performed with different H2/HC ratios at various temperatures, liquid hourly space velocities (LHSVs) and 3MPa total pressure. The catalyst introduced in the reactor displayed a fairly high initial activity, but conversion slowly declined with time on stream. Adding CCl4 to the hexane feed could not improve the stability with time on stream. The effects of temperature on conversion and isomer selectivity were studied at various H2/HC ratios and LHSVs. Superior conversion and selectivity were found for the catalyst at 160 ˚C and 120 ˚C at LHSV 1.2 h-1. Furthermore, effects of LHSV and low temperature were studied on conversion and product octane number derived from hexane isomerization, respectively. The highest octane number was observed at the low space velocity (1.2 h-1).
AbstractList A high chlorinated alumina catalyst obtained by treating Pt/γ-Al2O3 (0.25 wt. % Pt) samples with two mixtures of CCl4/N2 and CCl4/N2/H2 was tested for the hydroisomerization of C6 alkane. The conversion of n-hexane feed was diluted with hydrogen performed with different H2/HC ratios at various temperatures, liquid hourly space velocities (LHSVs) and 3MPa total pressure. The catalyst introduced in the reactor displayed a fairly high initial activity, but conversion slowly declined with time on stream. Adding CCl4 to the hexane feed could not improve the stability with time on stream. The effects of temperature on conversion and isomer selectivity were studied at various H2/HC ratios and LHSVs. Superior conversion and selectivity were found for the catalyst at 160 ˚C and 120 ˚C at LHSV 1.2 h-1. Furthermore, effects of LHSV and low temperature were studied on conversion and product octane number derived from hexane isomerization, respectively. The highest octane number was observed at the low space velocity (1.2 h-1).
Author Mansour Jahangiri
Fatollah Salehirad
Shahram Alijani
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  organization: Faculty of Chemical, Petroleum and Gas Eng., Semnan University, Semnan, Iran
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  fullname: Fatollah Salehirad
  organization: Research Institute of Petroleum Industry (RIPI), Tehran, Iran
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  fullname: Shahram Alijani
  organization: Research Institute of Petroleum Industry (RIPI), Tehran, Iran
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Snippet A high chlorinated alumina catalyst obtained by treating Pt/γ-Al2O3 (0.25 wt. % Pt) samples with two mixtures of CCl4/N2 and CCl4/N2/H2 was tested for the...
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SubjectTerms Catalyst
Chlorinated alumina
Isomerization
Light naphtha
Normal hexane
Title Preparation of Pt/Al2O3-Cl Catalyst and Investigation of Operating Variables Effects on Isomerization Reaction
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