FIELD: processing of oil; regeneration of aluminium- platinum catalyst of reforming. SUBSTANCE: in the oxygen- containing gas medium coke is burned out at 200-500 C from the waste aluminium-platinum catalyst of reforming. Then the catalyst is treated by Freon in the circulating hydrogen- containing gas medium at 200-300 C, with consumption of Freon being 0.1-0.4 percent of fluorine mass. EFFECT: higher efficiency.
Title | Year | Author | Number |
---|---|---|---|
METHOD OF REACTIVATING FLUORINE-CONTAINING ALUMINA-PLATINUM REFORMING CATALYST | 1994 |
|
RU2070090C1 |
METHOD FOR REGENERATION ALUMINA- OR SULFURIZED ALUMINA-BASED REFORMING CATALYST | 1999 |
|
RU2157728C1 |
METHOD OF PRODUCING HIGH-OCTANE GASOLINE | 1993 |
|
RU2044760C1 |
METHOD FOR PROCESSING HYDROPURIFIED BENZINE HAVING COAL ORIGIN | 0 |
|
SU1798362A1 |
METHOD OF RESTORING ACTIVITY OF PLATINUM-CONTAINING REFORMING CATALYST | 1995 |
|
RU2096085C1 |
METHOD FOR REGENERATION OF REFORMING CATALYST | 0 |
|
SU752883A1 |
CATALYTIC REFORMING PROCESS | 2004 |
|
RU2267515C1 |
PROCESS FOR REACTIVATION OF PLATINUM-BEARING GASOLINE REFORMING CATALYST | 0 |
|
SU1720708A1 |
METHOD FOR CATALYTIC REFORMING OF BENZINE FRACTIONS | 1992 |
|
RU2032706C1 |
METHOD FOR PURIFICATION OF PRODUCTS OF CATALYTIC REFORMING AGAINST OLEFIN HYDROCARBONS | 1997 |
|
RU2117029C1 |
Authors
Dates
1995-05-20—Published
1992-06-18—Filed