FIELD: petroleum processing. SUBSTANCE: straight-run gasoline fraction 85-180 C is subjected to catalytic reforming at 480-530 C, pressure 4 MPa, feedstock volumetric flow rate 1.5 h-1, and circulating factor of hydrogen-containing gas 1500 cu.m/cu/m/ Reforming products are subjected to rectification to give first fraction with dry point 120 C and below and second fraction starting to boil at 120 C and higher. First fraction contacts with alumina-supported catalyst containing 13- 20% tungsten trioxide and 0.9-6% nickel dioxide at 160-250 C and pressure 1.8-4.2 MPa. Contact product of the first fraction is combined with the second reforming products fraction. EFFECT: improved quality of product due to reduced content of aromatic hydrocarbons, including benzene (most toxic and undesired component). 2 tbl, 5 ex
Title | Year | Author | Number |
---|---|---|---|
HIGH-OCTANE GASOLINE PRODUCTION PROCESS | 2001 |
|
RU2206600C1 |
HIGH-OCTANE GASOLINE PRODUCTION PROCESS | 2004 |
|
RU2280063C2 |
HIGH-OCTANE GASOLINE PRODUCTION PROCESS | 1998 |
|
RU2145627C1 |
HIGH-OCTANE GASOLINE PRODUCTION PROCESS | 1997 |
|
RU2131908C1 |
BENZENE AND TOLUENE PRODUCTION PROCESS | 2001 |
|
RU2194740C1 |
HIGH-OCTANE GASOLINE PRODUCTION PROCESS | 2003 |
|
RU2240340C1 |
METHOD FOR PRODUCING HIGH-OCTANE GASOLINE | 2021 |
|
RU2773285C1 |
METHOD OF PRODUCING ENVIRONMENTALLY SAFE HIGH-OCTANE GASOLINE | 1998 |
|
RU2131909C1 |
CRACKED GASOLINE PURIFICATION PROCESS | 2003 |
|
RU2241019C1 |
METHOD OF PRODUCING AIRCRAFT MOTOR GASOLINE | 1997 |
|
RU2120467C1 |
Authors
Dates
2004-05-20—Published
2003-07-03—Filed