ISOMERIZATION OF PARAFFIN HYDROCARBONS AT LOW TEMPERATURE.

J. Hancsók, G. Gaordos, J. Perger

Research output: Contribution to journalArticle

3 Citations (Scopus)

Abstract

The isomerization reaction of n-pentane and n-hexane was studied at low temperature (100-150 degree C) and at a total pressure of 20 bar on aluminum-oxide supported platinum catalyst modified by chlorination. It was found that, in contrast to the high temperature process using a IP-62 type catalyst, the amount of isomers can be significantly increased and the results obtained approach BP and UOP data. The process is economic and a considerable increase in capacity can be obtained. The octane number of the product mixture is higher by 5-10 times than that of the traditional process.

Original languageEnglish
Pages (from-to)309-316
Number of pages8
JournalHungarian Journal of Industrial Chemistry
Volume15
Issue number3
Publication statusPublished - 1987

Fingerprint

Isomerization
Hydrocarbons
Paraffin
Paraffins
Catalysts
Antiknock rating
Aluminum Oxide
Chlorination
Platinum
Hexane
Isomers
Aluminum
Temperature
Economics
Oxides
n-hexane
pentane

ASJC Scopus subject areas

  • Chemical Engineering(all)
  • Chemistry(all)
  • Chemistry (miscellaneous)

Cite this

ISOMERIZATION OF PARAFFIN HYDROCARBONS AT LOW TEMPERATURE. / Hancsók, J.; Gaordos, G.; Perger, J.

In: Hungarian Journal of Industrial Chemistry, Vol. 15, No. 3, 1987, p. 309-316.

Research output: Contribution to journalArticle

@article{887e46cee70f44aca6a4bda8596ddbbf,
title = "ISOMERIZATION OF PARAFFIN HYDROCARBONS AT LOW TEMPERATURE.",
abstract = "The isomerization reaction of n-pentane and n-hexane was studied at low temperature (100-150 degree C) and at a total pressure of 20 bar on aluminum-oxide supported platinum catalyst modified by chlorination. It was found that, in contrast to the high temperature process using a IP-62 type catalyst, the amount of isomers can be significantly increased and the results obtained approach BP and UOP data. The process is economic and a considerable increase in capacity can be obtained. The octane number of the product mixture is higher by 5-10 times than that of the traditional process.",
author = "J. Hancs{\'o}k and G. Gaordos and J. Perger",
year = "1987",
language = "English",
volume = "15",
pages = "309--316",
journal = "Hungarian Journal of Industrial Chemistry",
issn = "0133-0276",
publisher = "University of Veszprem",
number = "3",

}

TY - JOUR

T1 - ISOMERIZATION OF PARAFFIN HYDROCARBONS AT LOW TEMPERATURE.

AU - Hancsók, J.

AU - Gaordos, G.

AU - Perger, J.

PY - 1987

Y1 - 1987

N2 - The isomerization reaction of n-pentane and n-hexane was studied at low temperature (100-150 degree C) and at a total pressure of 20 bar on aluminum-oxide supported platinum catalyst modified by chlorination. It was found that, in contrast to the high temperature process using a IP-62 type catalyst, the amount of isomers can be significantly increased and the results obtained approach BP and UOP data. The process is economic and a considerable increase in capacity can be obtained. The octane number of the product mixture is higher by 5-10 times than that of the traditional process.

AB - The isomerization reaction of n-pentane and n-hexane was studied at low temperature (100-150 degree C) and at a total pressure of 20 bar on aluminum-oxide supported platinum catalyst modified by chlorination. It was found that, in contrast to the high temperature process using a IP-62 type catalyst, the amount of isomers can be significantly increased and the results obtained approach BP and UOP data. The process is economic and a considerable increase in capacity can be obtained. The octane number of the product mixture is higher by 5-10 times than that of the traditional process.

UR - http://www.scopus.com/inward/record.url?scp=0023568641&partnerID=8YFLogxK

UR - http://www.scopus.com/inward/citedby.url?scp=0023568641&partnerID=8YFLogxK

M3 - Article

AN - SCOPUS:0023568641

VL - 15

SP - 309

EP - 316

JO - Hungarian Journal of Industrial Chemistry

JF - Hungarian Journal of Industrial Chemistry

SN - 0133-0276

IS - 3

ER -