FIELD: petroleum refinery, in particular method for catalytic refinement of petroleum light hydrocarbon cuts.
SUBSTANCE: petroleum light cuts are fed into catalyst cracking reaction; brought into contact with regenerated catalyst at temperature of 200-450°C, pressure of 0.1-0.5 MPa for 1-20 s followed by separation of reaction products. Stripped catalyst is regenerated for 10-50 min at temperature of 400-600°C and pressure of 0.1-0.6 MPa. Regenerated catalyst is recycled into reactor.
EFFECT: gasoline with decreased olefin content; diesel fuel with increased cetane number and partially decreased sulfur and nitrogen content.
10 cl, 6 tbl, 1 dwg, 4 ex
Title | Year | Author | Number |
---|---|---|---|
METHOD FOR CATALYTIC CONVERSION (VERSIONS) | 2008 |
|
RU2464298C2 |
METHOD, REACTOR AND SYSTEM FOR CATALYTIC CRACKING OF LIQUID OIL PRODUCTS | 2019 |
|
RU2797245C2 |
METHOD OF CATALYTIC CONVERSION WITH INCREASED OUTPUT OF DIESEL FUEL WITH HIGH CETANE NUMBER | 2010 |
|
RU2547152C2 |
METHOD, REACTOR AND SYSTEM FOR CATALYTIC CRACKING OF LIQUID OIL PRODUCTS | 2019 |
|
RU2793541C2 |
METHOD AND APPARATUS FOR CATALYTIC CRACKING FOR PRODUCING PROPYLENE | 2012 |
|
RU2580829C2 |
EQUIPMENT AND METHOD OF CATALYTIC CRACKING | 2010 |
|
RU2535675C2 |
METHOD AND SYSTEM FOR PRODUCING LIGHT OLEFINS FROM LOW-QUALITY PETROLEUM PRODUCTS | 2020 |
|
RU2803815C2 |
METHOD FOR CONVERSION OF LOW-GRADE RAW FEEDSTOCK TO HIGH-QUALITY OIL FUEL | 2009 |
|
RU2497933C2 |
METHOD AND SYSTEM FOR TREATMENT OF CATALYTIC CRACKING REACTION PRODUCT AND THEIR APPLICATION | 2020 |
|
RU2802626C1 |
METHOD OF CATALYST REGENERATION | 2010 |
|
RU2529021C2 |
Authors
Dates
2006-05-10—Published
2002-05-29—Filed