Production method of lubricant base oil and naphthenic oil
A technology for lubricating base oils and production methods, which is applied in the production field of lubricating base oils and naphthenic oils, can solve problems such as high naphthenic content and low viscosity index of base oils, achieve high yields, and improve separation efficiency Effect
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0035] This example is used to illustrate the production method of lubricating oil base oil and naphthenic oil provided by the present invention.
[0036] The No. 4 base oil produced by the lubricating oil isomerization dewaxing unit of Sinopec Gaoqiao Branch has a carbon number of 15-25 and a pour point of -12°C as the raw material oil. The properties of the raw material oil are shown in Table 1. A mixture of benzene and butanone is used as a solvent, the content of benzene is 3% by weight, and the content of butanone is 97% by weight. The mass ratio of solvent to raw oil is 10:1. Solid-liquid separation and filtration temperature -30°C. The ratio of the refractive index of the solvent at the filtration temperature to the refractive index of the mixture of liquid components and solvent in the feedstock oil at the filtration temperature is 0.98. See Table 2 for the basic properties of the first component and the second component separated by this method, as well as the separ...
Embodiment 2
[0040] This example is used to illustrate the production method of lubricating oil base oil and naphthenic oil provided by the present invention.
[0041] The No. 10 base oil with a carbon number between 25-35 and a pour point of -12°C produced by Sinopec Jingmen Branch's fourth-line distillate oil through solvent extraction-hydrotreating-solvent dewaxing process is used as raw material. See Table 1 for oil properties. A mixture of cyclopentane and ethanol is used as a solvent, the content of cyclopentane in the solvent is 13% by weight, and the content of ethanol is 87% by weight. The mass ratio of solvent to raw oil is 15:1. Solid-liquid separation filtration temperature -40 ℃. The ratio of the refractive index of the solvent at the filtration temperature to the refractive index of the mixture of feedstock oil and solvent at the filtration temperature was 0.98. See Table 2 for the basic properties of the first component and the second component separated by this method, a...
Embodiment 3
[0043] This example is used to illustrate the production method of lubricating oil base oil and naphthenic oil provided by the present invention.
[0044] Using the >380°C distillate of hydrocracking tail oil produced by the hydrocracking unit of Sinopec Beijing Yanshan Branch as the raw material, the product with a carbon number of 20-40 and a pour point of -12°C after conventional solvent dewaxing is used as the raw material , the properties of raw oil are shown in Table 1. A mixture of n-octane and propanol is used as a solvent, the content of n-octane in the solvent is 10% by weight, and the content of propanol is 90%. The mass ratio of solvent to raw oil is 5:1. Solid-liquid separation and filtration temperature is -45°C. The ratio of the refractive index of the solvent at the filtration temperature to the refractive index of the mixture of feedstock oil and solvent at the filtration temperature was 0.97. See Table 2 for the basic properties of the first component and ...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 

