Method for removing dicyclopentadiene from ethylene cracked carbon 9 fraction

A technology for dicyclopentadiene and carbon nine fractions, which is applied in the directions of distillation purification/separation, fractionation, vacuum distillation, etc., can solve the problems of dark color, not widely used, and blocked equipment, and achieve simple processing technology, reduce production costs, The effect of eliminating potential safety hazards

Active Publication Date: 2017-09-08
TIANJIN CLEANTECH TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] Among them, the third type of components in the C9 fraction of ethylene cracking, especially dicyclopentadiene (DCPD) has a high activity and is the main factor affecting the hue of the resin. Foreign countries have strict requirements on it, and the general requirement is not more than 2%. The DCPD content in the C9 fraction is relatively high, generally as high as 15%, which leads to the fact that there are not many C9 petroleum resin grades in my country, the color is darker, and there is no uniform quality index. The application is not yet widespread. At the same time, it affects the application in high-grade paint. There are also some applications in additives, low-grade inks, and adhesives in rubber shoe factories
[0005] The boiling point of DPCD and methyl styrene, which affects the quality of C9 petroleum resin, is only 0.6 degrees, and the composition of the cracked C9 fraction is extremely complex, and the boiling point is very close. It is impossible to remove DCPD by ordinary distillation. Therefore, ...

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0026] The first step, the removal of dicyclopentadiene in the ethylene cracking carbon nine fraction (the selection diameter is 30mm, and the glass rectification tower that is 1.5m high is the operation tower):

[0027] Add 200ml ethylene cracking C9 fraction and 200ml benzaldehyde into the tower kettle, control the operating pressure inside the tower to 30kpa, heat to reflux, at this time, the kettle temperature is 83.4°C, the top temperature is 62.8°C, and pump the ethylene cracking C9 fraction from the middle of the tower And benzaldehyde, wherein the feed rate of ethylene cracking carbon nine fraction is 150ml / hr, and the benzaldehyde feed rate is 60ml / hr, and the tower top reflux ratio is 10:1, and the extraction fraction at the top of the tower is containing 48% benzaldehyde Dicyclopentadiene, the residue of dicyclopentadiene in the tower still liquid is 0.56%;

[0028] The second step, the removal of benzaldehyde in the overhead fraction (the selection diameter is 30mm...

Embodiment 2

[0034] The first step, the removal of dicyclopentadiene in the ethylene cracking carbon nine fraction (the selection diameter is 30mm, and the glass rectification tower that is 1.5m high is the operation tower):

[0035] Add 200ml ethylene cracking C9 fraction and 200ml benzaldehyde to the tower kettle, control the operating pressure inside the tower to 30kpa, heat to reflux, at this time, the temperature of the kettle is 83.4°C, the top temperature is 62.8°C, and pump the ethylene cracking C9 fraction from the middle of the tower And benzaldehyde, wherein the feed rate of ethylene cracking carbon nine fraction is 150ml / hr, and the benzaldehyde feed rate is 60ml / hr, and the tower top reflux ratio is 3:1, and the extraction fraction at the top of the tower is containing benzaldehyde 51%. Dicyclopentadiene, the residue of dicyclopentadiene in the tower still liquid is 0.48%;

[0036] The second step, the removal of benzaldehyde in the overhead fraction (the selection diameter is...

Embodiment 3

[0042] The first step, the removal of dicyclopentadiene in the ethylene cracking carbon nine fraction (the selection diameter is 30mm, and the glass rectification tower that is 1.5m high is the operation tower):

[0043] Add 200ml ethylene cracking C9 fraction and 200ml furfural to the tower kettle, control the operating pressure in the tower to 30kpa, heat to reflux, at this time, the temperature of the kettle is 83.4°C, the top temperature is 62.8°C, and pump the ethylene cracking C9 fraction and Furfural, wherein the feed rate of the ethylene cracking carbon nine fraction is 150ml / hr, the furfural feed rate is 60ml / hr, the tower top reflux ratio is 3:1, and the tower top extraction fraction is dicyclopentadiene containing 50.36% furfural , the dicyclopentadiene residual content in the tower still liquid is 0.48%;

[0044] The second step, the removal of benzaldehyde in the overhead fraction (the selection diameter is 30mm, and the glass rectification tower that is 1.5m high...

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PUM

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Abstract

The invention provides a method for removing dicyclopentadiene from ethylene cracked carbon 9 fraction. The method includes: adding a selective solvent to the ethylene cracked carbon 9 fraction to carry out distillation under reduced pressure, selectively separating the dicyclopentadiene from the carbon 9 fraction extremely complex in component, approximate in boiling point and difficult to separate with common distillation methods, further treating the removed dicyclopentadiene containing the selective solvent, and then recycling the separated selective solvent to obtain the high-purity dicyclopentadiene. The selective solvent is utilized to highly selectively separate the dicyclopentadiene, content of the dicyclopentadiene in the carbon 9 fraction can be lowered to below 1%, and the influence of the residual of the dicyclopentadiene on the quality of the subsequent petroleum resin is removed; the problem that active components in the high temperature cracking method are prone to implosion resulting in blockage to equipment is avoided, potential risks brought by frequent cleaning are completely eradicated, production cost is lowered, and long-cycle, continuous and stable production is realized.

Description

technical field [0001] The invention belongs to the technical field of chemical separation, and in particular relates to a method for removing dicyclopentadiene from ethylene cracking carbon nine fractions. Background technique [0002] The C9 aromatics fraction (referred to as cracked C9) produced by the ethylene plant is the remaining fraction after separating the C5 fraction and the C6-C8 fraction (by hydrogenation to produce BTX) from pyrolysis gasoline, accounting for 10% to 20% of the total ethylene production. %, for the C9 and C9+ components of ethylene by-products, its most important feature is that it is rich in diolefins and vinyl aromatics, and has high reactivity. In addition to producing solvent oil, extracting heavy aromatics components and increasing the production of light aromatics, currently The most important way is to produce C9 petroleum resin, which is widely used in chemical industries such as paints, inks, coatings, and adhesives, and is an important...

Claims

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Application Information

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IPC IPC(8): B01D3/10B01D3/14C08F240/00C07C7/04C07C13/61
CPCB01D3/10B01D3/14C07C7/04C08F240/00C07C13/61
Inventor 张学岗刘通
Owner TIANJIN CLEANTECH TECH
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