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Bright oil preparation method

A bright oil and tail oil technology, which is applied in the treatment of hydrocarbon oil, petroleum industry, hydrotreating process, etc. The effect of increasing the rate, reducing the dewaxing temperature difference, and high yield

Active Publication Date: 2020-11-13
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] The purpose of the present invention is to overcome the problems of low bright oil yield, large dewaxing temperature difference and high energy consumption in the solvent dewaxing step when bright oil is produced in the prior art, and provides a bright oil preparation method. The method can increase the bright stock yield and simultaneously reduce the dewaxing temperature difference in the solvent dewaxing step, thereby saving energy and reducing consumption

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preparation example Construction

[0024] According to the present invention, the preparation method of described bright stock comprises the following steps:

[0025] (1) Under the condition of residual oil hydrotreating, hydrogen gas, residual oil raw material and catalyst are contacted and reacted, and a gas phase stream and a liquid phase stream are obtained from the hydrogenation reaction product, and the liquid phase stream includes light oil and hydrogenated Residue tail oil, the light oil includes naphtha and diesel oil, and the hydrogenated residue tail oil is further separated into vacuum wax oil and vacuum residue;

[0026] (2) Under solvent deasphalting conditions, the vacuum residue obtained in step (1) is contacted with a deasphalting solvent to carry out solvent extraction and separation to obtain light deasphalted oil, heavy deasphalted oil and deoiled asphalt respectively;

[0027] The first way:

[0028] Under solvent refining conditions, the light deasphalted oil obtained in step (2) is conta...

Embodiment 1

[0100] This example is used to illustrate the preparation method of the bright stock provided by the present invention.

[0101]The vacuum residue produced by the atmospheric and vacuum unit of Sinopec Jingmen Branch is used as the raw material. In the fixed bed hydrogenation test unit, the catalyst is the RCS-31 hydrogenation catalyst produced by Sinopec Catalyst Branch. The hydrogenation temperature is 350°C , hydrogen partial pressure 8.0MPa, volume space velocity 0.2h -1 , hydrogen oil volume ratio 1100Nm 3 / m 3 Under the conditions of the residue oil hydrogenation test, the 70°C refractive index of the vacuum residue of the >500°C component in the residue oil hydrogenation product is 1.5102, and the residue oil hydrogenation product is separated to obtain gas, naphtha, diesel oil and residue Hydrogenated tail oil. The residue hydrogenation tail oil was further cut by vacuum distillation to separate vacuum wax oil and vacuum residue. The cutting temperature of vacuum di...

Embodiment 2

[0111] This example is used to illustrate the preparation method of the bright stock provided by the present invention.

[0112] Using the vacuum residue produced by the atmospheric and vacuum unit of Sinopec Jingmen Branch as raw material, the catalyst is prepared according to the catalyst preparation method and composition described in the example of CN 105524657A on the fluidized bed hydrogenation test unit, and hydrogenated at 410°C Temperature, hydrogen partial pressure 18.0MPa, volumetric space velocity 1.2h -1 , Hydrogen oil volume ratio 900Nm 3 / m 3 Residue hydrogenation test was carried out under certain conditions. The 70°C refractive index of the vacuum residue of >500°C components in the residue hydrogenation product was 1.5328, and the residue hydrogenation product was separated to obtain gas, naphtha, diesel oil and residue Hydrogenated tail oil. The residue hydrogenation tail oil was further cut by vacuum distillation to separate vacuum wax oil and vacuum res...

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Abstract

The invention relates to the field of petrochemical engineering and discloses a preparation method of bright stock. The method includes: 1) residual oil hydrogenation, solvent deasphalting, solvent extraction, solvent dewaxing, and adsorbent finishing; or 2) residual oil hydrogenation, solvent deasphalting, solvent dewaxing, solvent extraction, and adsorbent finishing. In the first mode, during the solvent dewaxing step at a solvent dewaxing temperature, the ratio of the refractive index of a dewaxing diluting solvent to the refractive index of a mixture of liquid components, in the raffinateoil, and the dewaxing diluting solvent is 0.94-1, preferably 0.96-0.99; or in the second mode, during the solvent dewaxing step at the solvent dewaxing temperature, the ratio of the refractive index of the dewaxing diluting solvent to the refractive index of a mixture of liquid components, in the deasphalting oil, and the dewaxing diluting solvent is 0.92-1, preferably 0.95-0.99. The method can increase yield of the bright stock and meanwhile reduce dewaxing temperature difference in the solvent dewaxing step, thus saving energy and reducing consumption.

Description

technical field [0001] The invention relates to a preparation method of bright stock. Background technique [0002] Bright stock is a heavy lubricant base stock. Bright oil can be divided into 90BS according to the kinematic viscosity at 100°C (the kinematic viscosity at 100°C is 17mm 2 / s-22mm 2 / s), 120BS (100℃ kinematic viscosity at 22mm 2 / s-28mm 2 / s) and 150BS (100℃ kinematic viscosity at 28mm 2 / s-34mm 2 / s), mainly used to increase the high temperature viscosity of blended lubricating oil. Bright stock is generally made of light deasphalted oil (hereinafter referred to as light deasphalted oil) produced by propane deasphalting equipment from the vacuum residue of petroleum, and the refined lubricating oil base is supplemented by solvent extraction-solvent dewaxing-clay Heavy bright oil with a color not greater than No. 6.0 produced by the traditional production process, and light-colored heavy bright oil with a color not greater than No. 1.5 produced by solven...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G67/06
Inventor 管翠诗丁洛王玉章蔡晨陈国成
Owner CHINA PETROLEUM & CHEM CORP