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Method for processing inferior residual oil

A residual oil, inferior technology, applied in hydrotreating process, petroleum industry, treatment of hydrocarbon oil, etc., can solve the problems of high residual carbon value, increased feed saturation of coking unit, poor economy, etc., to increase the added value, The effect of high volatilization temperature and good quality

Active Publication Date: 2021-05-04
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] However, the anode paste produced by using medium-temperature asphalt as raw material produces relatively large flue gas due to high volatile content during use, which pollutes the environment; when using high-temperature asphalt as raw material , due to the high sulfur content, high metal content and high carbon residue value in high-temperature asphalt, it is easy to generate shot coke during coke formation, and the produced coke emits SOx during use, which affects the environment
[0008] CN1349955A discloses a production method of clean anode coke, which proposes to mix the raw material petroleum coke and medium-temperature pitch evenly, use an electromagnetic separator to remove impurities, grind, Forming, roasting at 1000-1300°C for 12-24 hours, and the mature anode coke is cooled by a cooling tower to obtain a clean anode coke product; while the electromagnetic separator only has the effect of separating free metal impurities, and is effective for metal compounds or sulfur, etc. no separation effect
[0009] At present, there is no suitable process to treat the vacuum residue with poor properties, so that it can be used as a raw material for the production of high-quality anode coke: fixed bed residue can be removed by hydrogenation Sulfur and metals in the vacuum residue, but considering the construction cost of the hydrogenation unit, hydrogen consumption, and the service life of the catalyst, its economy is poor
In addition, the vacuum residue is used as coking feed after hydrogenation, and the saturation of the feed to the coking unit is greatly increased. The volatile carbon-containing substances, stack ratio, and moldability of the anode coke produced are difficult to meet the quality requirements of the anode coke.

Method used

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  • Method for processing inferior residual oil
  • Method for processing inferior residual oil
  • Method for processing inferior residual oil

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0068] The first solvent and the second solvent used in this embodiment are the same as n-butane, and the first solvent and the second solvent come from the same solvent storage unit, and are only controlled through different pipelines with valves.

[0069] The hydroprocessing device in this embodiment is a fixed-bed hydrogenation reactor.

[0070] The catalytic cracking device in this embodiment is a riser reactor, wherein the catalytic cracking catalyst is the catalyst CDOS-WH.

[0071] The first tower still stream extracted from the bottom of the first separator is blended with base asphalt (properties are listed in Table 8) in the asphalt blending device to obtain hard asphalt, the properties of which are shown in Table 9.

[0072] The specific reaction conditions involved in the above examples are shown in Table 2, the composition and properties of the first tower still stream, the second tower still stream and the second tower overhead stream are shown in Table 3, the co...

Embodiment 2

[0074] This example is carried out using the same process flow as Example 1, only some specific parameters involved in the process are different from Example 1, and the specific parameters and results are shown in the following table.

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Abstract

The invention relates to the field of residual oil processing, and discloses a method for processing inferior residual oil, which comprises the following steps: vacuum residual oil is introduced into a first separator for countercurrent contact with a solvent contained in the vacuum residual oil, and a first tower top material flow and a first tower kettle material flow are respectively obtained; the first tower top material flow is introduced into a second separator to be in countercurrent contact with a solvent contained in the second separator, and a second tower top material flow and a second tower kettle material flow are obtained respectively; hydrotreating is carried out on the second tower kettle material flow to obtain a hydrogenated material flow; and delayed coking treatment is carried out on the hydrogenation material flow to obtain an anode coke product. According to the method, efficient utilization of the inferior residual oil is achieved, the utilization rate and the utilization value of the inferior residual oil are improved to the maximum extent, and the anode coke obtained through production has high quality.

Description

technical field [0001] The invention relates to the field of hydrocarbon oil processing, in particular to a method for processing inferior residue oil. Background technique [0002] With the rapid development of the electrolytic aluminum industry, the demand for aluminum prebaked anode coke has risen sharply, and the aluminum prebaked anode coke industry has gradually become a new investment growth point. [0003] Generally speaking, when the sulfur content of petroleum coke is relatively low, the anode consumption decreases with the increase of sulfur content, because sulfur increases the coking rate of asphalt and reduces the porosity of asphalt coking; at the same time, sulfur is also combined with metal impurities, reducing The catalytic effect of metal impurities, but if the sulfur content is too high, the thermal brittleness of the carbon anode will be increased, and because the sulfur is mainly converted into the gas phase in the form of oxides during the electrolysis...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G69/06C10G69/00
CPCC10G69/06C10G69/00C10G2300/1077C10G2300/107C10G2300/70C10G2400/02C10G2400/04C10G2400/26
Inventor 王翠红申海平王红刘自宾廖志新范启明佘玉成
Owner CHINA PETROLEUM & CHEM CORP