Process for continuously removing quinoline insolubles in coal tar pitch

A technology of coal tar pitch and quinoline, which is applied in the new process field of removing quinoline insolubles from coal tar pitch, can solve the problems of small processing capacity, low solvent recovery rate, high QI content, etc., and achieve the reduction of clear liquid loss, The effect of high solvent recovery and low QI content

Active Publication Date: 2009-08-19
BAOWU CHARCOAL MATERIAL TECH CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The disadvantages of the above method are: 1, the purification effect of the static sedimentation separation method is poor, and the QI content in the asphalt after purification is more than 1%; 2, the centrifugal separation method equipment operation cost is high, and the processing capacity is small; 3, hot-melt filtration 4. Intermittent solvent static sedimentation method has better purification effect, but the solvent consumption is large, the process energy consumption is also large, and the interface between the two phases of oil residue is unclear Causes high difficulty in industrialization
The yield of the purification product of solvent extraction and solvent flocculation method is low; 5, the recovery rate of solvent in solvent centrifugation method is low
[0005] Invention patent application 200510136738.1 discloses a production method for purifying asphalt. The method is an intermittent solvent settling method, which uses a stirred tank as a mixing and QI settling equipment for raw materials and solvents, which causes the following problems: oil residue two-phase The unclear interface makes the QI content in the purified bitumen still relatively high; to realize industrial continuous operation, multiple stirring tanks must be switched and used, so that the investment in equipment is large; Contamination of the supernatant, when the supernatant of the stirring tank is drawn out, it is impossible to completely pump it out, so that the loss of the supernatant will be caused, thereby reducing the yield of the product

Method used

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  • Process for continuously removing quinoline insolubles in coal tar pitch
  • Process for continuously removing quinoline insolubles in coal tar pitch

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0019] The raw material is mixed soft asphalt.

[0020] The flow ratio of soft asphalt to solvent is 1:0.6. The solvent is a mixture of kerosene and aromatic hydrocarbons, and the ratio of kerosene to aromatic hydrocarbons is 0.7:1.

[0021] After fully mixing the returned soft asphalt and the solvent through the pipeline mixer, they continuously enter the lower part of the settling tank. The temperature of the settling tank was 130°C, and the residence time of the mixed material in the settling tank was 24 hours.

[0022] In the settling tank, the mixed material is divided into two phases of clear liquid and sediment. The clear liquid is continuously discharged from the upper part of the settling tank, and the sediment is sent out from the bottom of the settling tank. The clear liquid is processed by a solvent distillation tower to obtain a purified product, and the solvent is recovered. The solvent is recovered for recycling.

[0023] After testing, the product yield (p...

Embodiment 2

[0025] The raw material is mixed soft asphalt.

[0026] The flow ratio of soft asphalt to solvent is 1:2.

[0027] The solvent is a mixture of hexane and aromatic hydrocarbon, and the ratio of hexane to aromatic hydrocarbon is 0.7:1.

[0028] After fully mixing the returned soft asphalt and the solvent through the pipeline mixer, they continuously enter the lower part of the settling tank. The temperature of the settling tank is 60°C, and the residence time of the mixed material in the settling tank is 12 hours. Others are the same as embodiment 1.

[0029] After testing, the product yield (purified back-mixed soft asphalt / back-mixed soft asphalt) is 87.0%, the solvent recovery rate is 98.5%, and the content of quinoline insolubles (QI) in the purified back-mixed soft asphalt is 0.02%.

Embodiment 3

[0031] The raw material is mixed soft asphalt.

[0032] The flow ratio of soft asphalt to solvent is 1:2. The solvent is a mixture of heptane and aromatic hydrocarbons, and the ratio of heptane to aromatic hydrocarbons is 1:0.5.

[0033] After fully mixing the returned soft asphalt and the solvent through the pipeline mixer, they continuously enter the lower part of the settling tank. The temperature of the settling tank was 90°C, and the residence time of the mixed material in the settling tank was 3 hours. Others are the same as embodiment 1.

[0034] After testing, the product yield (purified back-mixed soft asphalt / back-mixed soft asphalt) is 89.0%, the solvent recovery rate is 97.0%, and the content of quinoline insolubles (QI) in the purified back-mixed soft asphalt is 0.06%.

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Abstract

The invention provides a process for continuously removing quinoline insolubles from coaltar asphalt. In the process, after a working procedure of mixing materials and solvent, the mixture continuously enters to the lower part of a settling tank; a mixture separating working procedure is carried out in the settling tank; clear solution separated from the mixture is continuously discharged from the upper part of the settling tank, and sediments are sent out from the bottom of the settling tank; the solvent consists of aliphatic hydrocarbon and aromatic hydrocarbon according to the proportion of 1 to 0.5-1 to 1.5; and the flow ratio of pit asphalt and the solvent in the materials is 1 to 0.6-1 to 2.0. The OI content in the purified asphalt is low, and the clear solution loss of the supernatant clear solution is reduced due to the continuous operation, thus the purified asphalt product has high yield coefficient and the solvent also has higher recovery coefficient.

Description

technical field [0001] The invention relates to a pitch purification process, in particular to a new continuous process for removing quinoline insolubles (QI) from coal tar pitch. Background technique [0002] Pitch is a by-product in the process of coal tar processing. Because of its high yield, its processing technology and the added value of its products directly affect the economic benefits of coking enterprises. The production and preparation of coal-based needle coke, coal tar pitch-based carbon fiber, coal tar pitch impregnating agent and mesophase pitch all require purified coal pitch raw materials with low quinoline insoluble (QI) content, while coal tar contains raw QI The representative impurity can seriously hinder the preparation of above-mentioned high-quality high value-added coal tar pitch product. At the same time, the impurities contained in coal tar can easily cause blockage of coal tar deep processing equipment, thereby affecting the quality of coal tar ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10C3/08
Inventor 许祥军张秀云李乃民刘春法刘正华胡翔周智旻严天祥唐寄云
Owner BAOWU CHARCOAL MATERIAL TECH CO LTD
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