| (19) |
 |
|
(11) |
EP 0 104 807 A3 |
| (12) |
EUROPEAN PATENT APPLICATION |
| (88) |
Date of publication A3: |
|
13.08.1986 Bulletin 1986/33 |
| (43) |
Date of publication A2: |
|
04.04.1984 Bulletin 1984/14 |
| (22) |
Date of filing: 05.09.1983 |
|
|
| (84) |
Designated Contracting States: |
|
BE DE FR GB IT NL |
| (30) |
Priority: |
28.09.1982 US 425842
|
| (71) |
Applicant: MOBIL OIL CORPORATION |
|
() |
|
| (72) |
Inventors: |
|
- Tabak, Samuel Allen
()
- Shih, Stuart Shan-San
()
|
|
| |
|
| (54) |
Use of high pressure to improve product quality and increase cycle length in catalytic
lube dewaxing |
(57) A process for preparing high quality lube base stock oil from waxy crude oil is provided
which comprises separating from the waxy crude a distillate fraction thereof having
an initial boiling point of at least 232°C (450°F) and a final boiling point labs
than 566°C (1050°F), extracting the distillate fraction with a solvent selective for
aromatic hydrocarbons to yield a raffinate from which undesirable compounds have been
removed, catalytically dewaxing the raffinate in the presence of hydrogen to a pour
point not higher than -1°C (+30°F) by contacting the raffinate at a temperature of
260°C to 385°C (500° to 725°F) at a hydrogen partial pressure of above 10350 kPa (1500
psia) in the absence of hydrotreating catalyst with a dewaxing catalyst comprising
an aluminosilicate zeolite having a silica/alumina ratio above 12 and a constraint
index of from 1 to 12 thereby forming dewaxed raffinate and lower boiling hydrocarbons,
and topping the raffinate subsequent to dewaxing to remove therefrom the lower boiling
hydrocarbons; thereby directly recovering substantially all of the remainder of the
dewaxed raffinate, the remainder having a pour point not higher than -1°C (+30°F).
