FIELD: oil processing.
SUBSTANCE: hydrocarbon raw material with boiling point between 200°C and 600°C is brought into contact with hydrogen over hydropurification catalyst at hydropurification conditions. Hydropurification effluent is cooled and brought into contact over hydropurification catalyst in afterpurification reactor at temperature sufficient to reduce polyaromatic hydrocarbon content.
EFFECT: process with simplified technology.
6 cl, 4 tbl, 1 dwg, 3 ex
Title | Year | Author | Number |
---|---|---|---|
HYDROPROCESSING LIGHT CYCLE OIL IN LIQUID-FULL REACTORS | 2013 |
|
RU2662434C2 |
HYDROCARBON COMPOSITION USED AS FUEL AND OBTAINED FROM OIL COMPONENTS AND BIOLOGIC COMPONENT | 2009 |
|
RU2505582C2 |
METHOD FOR CONFIGURING PRODUCTION OF PETROCHEMICAL RAW MATERIAL | 2021 |
|
RU2766508C1 |
METHOD OF CONVERTING HYDROCARBON STREAM AND, OPTIONALLY, OBTAINING PROCESSED DISTILLATE PRODUCT | 2013 |
|
RU2565048C1 |
DOUBLE-STAGE METHOD OF SATURATION OF AROMATIC DIESEL FUEL COMPOUNDS USING INTERMEDIATE STEAMING AND BASIC METAL CATALYST | 2014 |
|
RU2671978C2 |
TWO-STEP METHOD OF SATURATION OF AROMATIC COMPOUNDS OF DIESEL FUEL, USING CATALYST BASED ON NON-PRECIOUS METAL | 2014 |
|
RU2695377C2 |
DIRECTED PRE-TREATMENT AND SELECTIVE OPENING CYCLE IN REACTORS FILLED WITH LIQUID | 2012 |
|
RU2593758C2 |
AROMATIC COMPOUND AND OLEFIN HYDROGENATION WITH USING MESOPOROUS CATALYST | 2005 |
|
RU2351635C2 |
METHOD AND DEVICE FOR HYDROCONVERSION OF HYDROCARBONS | 2015 |
|
RU2705590C2 |
HYDROTREATMENT METHOD AND CATALYST | 2009 |
|
RU2495082C2 |
Authors
Dates
2005-04-27—Published
2001-01-24—Filed