The method is used for derivation of high-octane components through catalytical reforming of oil fractions in the presence of various catalysts. Through it, the petroleum raw material is much better utilized, increases the output and improves the octane characteristics of the products from the catalytical reforming. It creates conditions for more rational exploitation of the installations and for additional spending of raw material at the expense of milder regimes for carrying out of the catalytical reforming. Under the method, the received after the separation of the liquid product poor in hydrogen hydrocarbon gases are subject to additional catalitical transformation on rich in silicon zeolite catalysts, at which a high-octane liquid product is derived and then added to the reform.
申请公布号
BG49664(A1)
申请公布日期
1992.01.15
申请号
BG19890087254
申请日期
1989.02.15
申请人
TEKHNOLOGICHEN NEFTOKHIMICHESKI KOMBINAT
发明人
KANAZIREV, VLADISLAV I.;KHRISTOV, VESELIN KH.;ATANASOV, ATANAS G.;DANCHEV, NIKOLAJ M.;DESHKOV, VASKO I.;KOZALIEVA, TOTKA L.;PENCHEV, VLADIMIR ZH.;KOZOVA, LJUBKA R.