PAO20 base oil and preparation method thereof
A technology of base oil and heavy oil, applied in the direction of base material, petroleum industry, lubricating composition, etc., can solve the problems of high preparation cost, high reaction conditions, low product yield, etc., and achieve simple operation, less side reactions, Response to easily controlled effects
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
preparation example Construction
[0019] The first aspect of the present invention provides a kind of preparation method of PAO20 base oil, comprising:
[0020] (I) Cut the Fischer-Tropsch stable heavy oil into fractions to obtain 8 -C 12 distillate streams of hydrocarbons;
[0021] (II) subjecting the distillate stream to removal of oxygenated compounds to obtain a deoxygenated distillate stream;
[0022] (III) In the presence of a catalyst and a solvent, subjecting the deoxygenated distillate stream to a polymerization reaction to obtain a product system, and post-processing the product system to obtain a primary product;
[0023] (IV) Distilling the initial product to obtain PAO20 base oil.
[0024] According to the present invention, the Fischer-Tropsch stable heavy oil is obtained from a medium-temperature Fischer-Tropsch synthesis process and contains α-olefins, alkanes and oxygenates. 8 -C 20 Heavy product. The medium temperature Fischer-Tropsch synthesis process refers to the synthesis gas (mainl...
Embodiment 1
[0065] (I) Fischer-Tropsch stabilized heavy oil is introduced into the first rectification column for fraction cutting (the reflux ratio is 20, the tower top temperature is 170°C, and the tower top pressure is normal pressure), to obtain C 10 A distillate stream of hydrocarbons (based on the total amount of said distillate stream, said distillate stream has an alpha-olefin content of 61.2% by weight);
[0066] (II) adding column chromatography silica gel to the distillate stream (column chromatography silica gel: the weight ratio of the distillate stream is 1:5), stirring for 1h for adsorption, repeating the above adsorption process twice to obtain the deoxygenated distillate stream (based on The total amount of the deoxygenated distillate stream, the content of oxygen-containing compounds in the deoxygenated distillate stream is 800ppm);
[0067] (III) AlCl 3 Powder and n-heptane are added in the reaction vessel, and nitrogen gas is passed into, and then the deoxygenated dis...
Embodiment 2
[0072] (I) Fischer-Tropsch stabilized heavy oil is introduced into the first rectification tower for fraction cutting (the reflux ratio is 20, the tower top temperature is 150°C-170°C, and the tower top pressure is normal pressure), to obtain C 9 -C 10 A distillate stream of hydrocarbons (based on the total amount of said distillate stream, said distillate stream has an alpha-olefin content of 63.5% by weight);
[0073] (II) adding column chromatography silica gel to the distillate stream (column chromatography silica gel: the weight ratio of the distillate stream is 1:5), stirring for 1h for adsorption, repeating the above adsorption process twice to obtain the deoxygenated distillate stream (based on The total amount of the deoxygenated distillate stream, the content of oxygen-containing compounds in the deoxygenated distillate stream is 800ppm);
[0074] (III) AlCl 3 Add the powder and n-heptane solvent into the reaction vessel, feed nitrogen, and then use a constant pres...
PUM
| Property | Measurement | Unit |
|---|---|---|
| Particle size | aaaaa | aaaaa |
| Pour point | aaaaa | aaaaa |
| Flash point | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More 

