FIELD: chemistry.
SUBSTANCE: invention relates to a method of increasing output of light olefin hydrocarbons from hydrocarbon material through catalytic cracking, involving (a) feeding hydrocarbon material in form of naphtha or kerosene and water vapour into a catalytic cracking furnace, where the hydrocarbon material undergoes a catalytic cracking reaction in the presence of a catalyst; (b) regenerating the catalyst used in the catalytic cracking reaction through continuous or periodic regeneration, and repeated use of (recycling) of the regenerated catalyst in the catalytic cracking furnace: (c) fast cooling, compression and separation of the catalytic cracking reaction product in order to separate and extract hydrogen, methane and C2-C3 olefin hydrocarbons and to separate into a stream containing C2-C3 paraffin hydrocarbons and a stream which contains C4+ hydrocarbons; (d) feeding the stream which contains C2-C3 paraffin hydrocarbons into the furnace for recycling, where the stream is converted to C2-C3 olefin hydrocarbons through a thermal cracking reaction, and recycling the converted C2-C3 olefin hydrocarbons to the fast cooling step; (e) recycling at least a portion of the C4-C5 hydrocarbons of the stream which contains C4+ hydrocarbons to the catalytic cracking reaction step, where the output of ethylene and propylene obtained through catalytic cracking of recycled C4-C5 hydrocarbons is higher than the output of ethylene and propylene obtained through catalytic cracking of naphtha or kerosene, wherein the catalytic cracking reaction is carried out at temperature 500-750°C and weight ratio of naphtha or kerosene to water vapour is equal to 0.01-10 and the dwell time of naphtha or kerosene is equal to 0.1-600 seconds and the weight ratio of the catalyst to naphtha or kerosene of the hydrocarbons is equal to 1-100.
EFFECT: high output of light olefins.
4 cl, 4 ex, 8 tbl, 2 dwg
Title | Year | Author | Number |
---|---|---|---|
METHOD FOR CATALYTIC CRACKING WITH FAST FLUIDISATION TO OBTAIN LIGHT OLEFINS FROM HYDROCARBON STARTING MATERIAL | 2006 |
|
RU2404152C2 |
METHOD AND INTEGRATED SYSTEM FOR PREPARATION OF LOWER OLEFIN PRODUCT | 2010 |
|
RU2560185C2 |
METHOD FOR OBTAINING LIGHT ALKENES FROM INITIAL HYDROCARBON RAW MATERIAL | 2006 |
|
RU2407776C2 |
METHOD OF ALKYLATING AROMATIC HYDROCARBONS IN PHASE | 2006 |
|
RU2409540C2 |
PRODUCING 1-BUTENE IN APPARATUS FOR CONVERTING OXYGEN-CONTAINING COMPOUNDS TO OLEFINS | 2011 |
|
RU2529855C2 |
OLEFIN PRODUCTION | 2003 |
|
RU2320704C2 |
PRODUCTION OF PROPYLENE IN PROCESS OF PARAPHASE CRACKING OF CARBOHYDRATES, IN PARTICULAR ETHANE | 2004 |
|
RU2383522C2 |
MIXING FEED RESERVOIR SYSTEM | 2013 |
|
RU2593996C2 |
PRODUCTION OF PETROL THROUGH POLYMERISATION OF OLEFIN WITH ALKYLATION OF AROMATIC COMPOUNDS | 2006 |
|
RU2409541C2 |
PRODUCTION OF PROPYLENE IN INSTALLATION OF CATALYTIC CRACKING WITH MOVABLE LAYER OF CATALYST | 2017 |
|
RU2673879C1 |
Authors
Dates
2011-04-20—Published
2006-05-19—Filed