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Hydrocracking method for producing lube base oil

A lubricating base oil and hydrocracking technology, which is applied in lubricating compositions, hydrotreating process, petroleum industry, etc., can solve the problems of large investment, increased enterprise investment, and large manpower consumption, and achieve low overall investment and high process efficiency. The effect of simplified process and low labor consumption

Active Publication Date: 2012-05-23
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The content of saturated hydrocarbons in the tail oil is very high, the content of aromatics is very low, and the content of sulfur and nitrogen is very low, so it is a good raw material for producing high-quality lubricating oil base oil, but the content of paraffins is high, which is difficult to meet the requirements of lubricating oil. Therefore, the use of hydrocracking tail oil through hydroisomerization process can produce light lubricating oil base oil to meet the needs of the lubricating oil market
[0004] At present, the main methods for preparing high-quality lubricating oil base oils from hydrocracking tail oils are: using hydrocracking-tail oil isomerization dewaxing combined process to prepare lubricating oil base oils, which includes hydrocracking and tail oil Two units of shape-selective isomerization, the tail oil of the hydrocracking unit is directly supplied to the shape-selective isomerization unit as raw material, and high-quality lubricating oil base oil is produced after shape-selective isomerization; although this method can produce lubricating oil, However, it is necessary to increase the tail oil shape-selective isomerization device, which increases the investment of the enterprise and increases the consumption of manpower and material resources.
Using a hydrocracking catalyst with isomerism depressing characteristics, the tail oil can be directly produced as a lubricating base oil under the condition of a relatively high conversion rate. Although this method can directly produce the tail oil as a lubricating oil base oil, there are limitations on the catalyst, The requirements for process conditions are relatively high. For industrial production, it is difficult to ensure long-term stable operation.
[0005] CN93110073.9 discloses a method for producing lubricating base oil by hydrodewaxing. Although high-quality lubricating oil with low freezing point can be produced, a shape-selective catalyst is required for one-stage hydrodewaxing, which consumes a lot of manpower and material resources.
[0006] CN98119809.0 introduces a method for preparing lubricating base oil. Under the condition of non-hydrogenation, a molecular sieve catalyst is selected to carry out shape-selective cracking of hydrocracking tail oil, so that hydrocracking tail oil is selectively cracked, thereby reducing the amount of base oil Freezing point, but shape-selective cracking is also required, the investment is large, and the yield of base oil is low

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment approach

[0025] Such as figure 1 As shown, an implementation of the hydrocracking flexible cutting scheme of the present invention is as follows:

[0026] The fresh raw material 1 is mixed with the circulating intermediate tail oil 22, the obtained raw material oil 2 is mixed with hydrogen gas 9, and then enters the hydrocracking unit 3, the reaction effluent 4 enters the separation system 5, and the obtained gas 6 passes through the circulating hydrogen compressor 7 , and mixed with new hydrogen 8 to obtain hydrogen 9, which is recycled to the reactor inlet or used as quenched hydrogen at the same time; the liquid 10 obtained by the separation system 5 enters the stripping tower 11, and the top part of the tower gives out the top gas 12, and the bottom of the stripping tower The liquid phase 13 obtained enters the atmospheric fractionation tower 14, and light naphtha 15, heavy naphtha 16 and aviation kerosene 17 are sequentially fractionated from top to bottom, and the liquid phase 18...

Embodiment 1

[0031] use figure 1 As shown in the process flow, the cutting scheme of the decompression part of the fractionation system is flexibly adjusted, the tail oil 1 is cut into three different components of light, medium and heavy, and the middle tail oil (415℃~445℃) is recycled back to In the reaction part, light tail oil and heavy tail oil are mixed into tail oil 2.

[0032]The properties of the catalysts used in the examples are listed in Table 1. The catalyst is a commercial catalyst developed and produced by Fushun Petrochemical Research Institute. The properties of the raw oil are shown in Table 2, and the operating conditions of the hydrogenation process are shown in Table 3.

Embodiment 2

[0036] The raw material oil is the mixed raw material oil of VGO and DAO in the Middle East, the intermediate tail oil (430℃~460℃) is recycled to the reaction part, and the light tail oil and heavy tail oil are mixed into tail oil 4. Other conditions are with embodiment 1

[0037] Table 1 Main physicochemical properties of the catalyst

[0038] project

[0039] Table 2 Raw Oil Properties Table

[0040] project

[0041] Table 3 reaction conditions

[0042] Example 1

[0043] Table 4

[0044] Comparative example 1

[0045] It can be seen from the above examples that the biggest feature of the hydrocracking method of the present invention is that, compared with the conventional product cutting method, the pour point of the tail oil can be lowered by 4-5°C, so that the downstream shape-selective isomerization can be eliminated It can directly produce high-quality low-point lubricating base oil and improve the economic benefits of th...

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Abstract

The invention discloses a hydrocracking method for producing lube base oil. The method comprises the steps of: firstly performing hydrocracking on raw oil, feeding oil generated after the hydrocracking into an atmospheric tower for fractionation, feeding obtained atmospheric tail oil into a vacuum tower for fractionation to obtain light tail oil, intermediate tail oil and heavy tail oil, and mixing the light tail oil and the heavy tail oil to obtain the lube base oil. In the hydrocracking method disclosed by the invention, by means of flexible segmentation treatment to the hydrocracked tail oil, a tail oil component with high condensation point is separated from the tail oil on the premise of not influencing the quality of other products, so that the lube base oil with low condensation point is obtained. According to the hydrocracking method, by means of only performing slighter reformation on the hydrocracking tower, the lube base oil with higher added value can be produced while light fuel oil is obtained, meanwhile, a downstream tail oil isodewaxing device can be omitted. The hydrocracking method has the advantages of simplified process flow, low operation cost, low material consumption, low energy consumption, low manpower consumption, low total investment and the like.

Description

technical field [0001] The invention relates to a hydrocracking method, in particular to a method for producing high-quality lubricating oil base oil by utilizing the hydrocracking process. Background technique [0002] In the international market, 70% to 99% of finished lubricants are base oils. Conventional solvent refining technology for lubricating base oil production has been used industrially for more than 50 years. Although there have been some technical improvements in recent years, the main reasons are energy saving and production cost reduction, and only low-quality lubricating oil can be produced, with little improvement in product properties. With the development of the modern automobile industry, the quality requirements for automotive lubricating oils are getting higher and higher, and correspondingly higher requirements are put forward for base oils. They have higher performance in terms of low-temperature fluidity, viscosity and oxidation stability. Requirem...

Claims

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Application Information

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IPC IPC(8): C10G67/02C10M177/00
Inventor 王仲义彭冲刘继华石友良刘涛黄新露孙士可
Owner CHINA PETROLEUM & CHEM CORP
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