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Pregled bibliografske jedinice broj: 295706

Effect of Operating Parameters on the Hydrocracking and Isomerization Reactions in the Naphtha Reforming


Sertić-Bionda, Katica; Vrbanović, Željko; Rukavina, V.; Zrnčević, Stanka
Effect of Operating Parameters on the Hydrocracking and Isomerization Reactions in the Naphtha Reforming // Chem.Biochem.Eng.Q., 6 (1992), 133-138 (podatak o recenziji nije dostupan, članak, znanstveni)


Naslov
Effect of Operating Parameters on the Hydrocracking and Isomerization Reactions in the Naphtha Reforming

Autori
Sertić-Bionda, Katica ; Vrbanović, Željko ; Rukavina, V. ; Zrnčević, Stanka

Izvornik
Chem.Biochem.Eng.Q. (0352-9568) 6 (1992); 133-138

Vrsta, podvrsta i kategorija rada
Radovi u časopisima, članak, znanstveni

Ključne riječi
Naphtha Reforming; Hydrocracking and Isomerization reactions; Pt-Re/Al2O3 Catalyst; Reaction Parameters

Sažetak
The influence of the operating parameters on the activity oftwo commercial Pt-Re/Al2O3 catalyst (R-62 and R-16G), onhydrocracking and isomerization reactions in naphtha reformingwas investigated. The reactions were performed in a fixed-bedreactor of 26 mm i.d. at space velocity from 2.7 to 5.4 1/h andat temperatures of 505 and 525 C. It has been found that the yield of liquid product at bothtemperatures increases with increasing space velosity but R- 62catalyst is more active than the R-16G. This means that R-16Gactivity is higher for hydrocracking reactions when the gaseousproducts are formed. It should also be noted that higher activityof R-16G for hydrocracking is not only influenced by the acidsites of alumina but also by the higher operating pressure (27bar). Catalyst R-62 has shown higher activity in dehydroisomerizationreactions of CyC5 naphthenes into aromatic hydrocarbons than theR-16G. This directly influences the quality of the products.

Izvorni jezik
Engleski

Znanstvena područja
Kemijsko inženjerstvo



POVEZANOST RADA


Projekt / tema
2-15-022

Ustanove
Fakultet kemijskog inženjerstva i tehnologije, Zagreb

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