FIELD: petrochemical processes.
SUBSTANCE: propylene is subjected to oligomerization in presence of phosphoric acid catalyst at elevated temperature and pressure. Propylene dimer fraction is separated from oligomerizate and returned into oligomerization process simultaneously normal α-olefin fraction and fraction containing C6 and C8-olefins. Weight ratio of the two fraction is (4-1):(1-4), respectively.
EFFECT: increased yield of propylene trimers and tetramers and enabled controlling proportions and yields thereof.
3 cl, 1 tbl, 6 ex
| Title | Year | Author | Number | 
|---|---|---|---|
| PROPYLENE TRIMER AND TETRAMER PRODUCTION PROCESS | 2000 | 
									
  | 
                RU2161600C1 | 
| PROPYLENE TRIMER AND TETRAMER ISOLATION PROCESS | 2004 | 
									
  | 
                RU2263655C1 | 
| METHOD OF PREPARING PROPYLENE TRIMERS AND TETRAMERS | 1998 | 
									
  | 
                RU2136642C1 | 
| METHOD FOR OBTAINING TRIMERS AND TETRAMERS OF PROPYLENE | 0 | 
									
  | 
                SU1641798A1 | 
| METHOD OF OLIGOMERIZATION OF PETROL WITHOUT ADDITIONAL REFINING | 2013 | 
									
  | 
                RU2639160C2 | 
| METHOD OF PRODUCING DIESEL FUEL USING GASOLINE OLIGOMERIZATION | 2013 | 
									
  | 
                RU2638933C2 | 
| PROPYLENE TRIMER AND TETRAMER PRODUCTION PROCESS | 2001 | 
									
  | 
                RU2200725C1 | 
| METHOD OF PRODUCING OLIGOMERS OF HIGHER LINEAR ALPHA-OLEFINS | 2011 | 
									
  | 
                RU2483052C2 | 
| OLEFIN DIMMER AND OLIGOMER PRODUCTION PROCESS | 2001 | 
									
  | 
                RU2184720C1 | 
| METHOD OF PRODUCING OLIGOMERS OF HIGHER LINEAR α-OLEFINS | 2011 | 
									
  | 
                RU2483053C2 | 
Authors
Dates
2005-06-27—Published
2004-03-18—Filed