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Method for refining carbonization crude benzole

A technology for coking crude benzene and a refining method, which is applied in distillation purification/separation and other directions, can solve the problems that thiophene cannot be completely removed, affect product purity, and the purification depth is not enough, so as to achieve low operating costs, avoid sulfonation losses, and save energy. The effect of investment costs

Inactive Publication Date: 2008-04-02
BEIJING INSTITUTE OF PETROCHEMICAL TECHNOLOGY
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  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The pickling process is simple, the production cost is low, and the technology is relatively mature, but the fatal defect of this process is that it produces a large amount of acid tar and waste sulfuric acid while removing impurities such as thiophene and unsaturated hydrocarbons, which causes serious pollution to the environment. Moreover, the purification depth of coking benzene and toluene is not enough in this process, and some saturated hydrocarbons whose relative volatility is close to that of benzene and toluene will enter the product as impurities, affecting the purity of the product. At the same time, the thiophene in benzene cannot be completely removed. In addition, these impurities will affect the subsequent production processes related to the catalytic process, such as the synthesis of cyclohexanone by coking benzene, the synthesis of maleic anhydride by oxidation of coked benzene, and the production of nitrobenzene by nitration and then hydrogenation to produce aniline. It must be deeply desulfurized
[0005] There are many methods for deep desulfurization of coking benzene. The typical one is to use adsorbents to selectively adsorb trace thiophene impurities in coking benzene. For example, zeolite molecular sieves such as A, 13X, and Y are used for adsorption and desulfurization of coking benzene through metal ion exchange modification. Currently reported The adsorption capacity of the adsorbent is generally low, the regeneration cycle is short, and the regeneration process often uses high-temperature hot nitrogen purge or roasting with oxygen-containing gas. Therefore, there is no report on the industrial application of the process of selectively adsorbing thiophene for deep purification of coked benzene.

Method used

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  • Method for refining carbonization crude benzole
  • Method for refining carbonization crude benzole
  • Method for refining carbonization crude benzole

Examples

Experimental program
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Effect test

Embodiment 1

[0047] Taking the coking crude benzene produced by the coking enterprise as the raw material (wherein the mass contents of benzene and toluene are 68.8% and 12.1%, respectively), after dehydration, filtering solid impurities, and preheating it, according to the crude benzene separation scheme A, from the two benzene The middle feed of column 1, the column is operated at atmospheric pressure and semi-continuously, and the crude benzene is divided into light benzene fractions below 150°C (wherein the concentration of thiophene is 3350 mg / L) and heavy benzene fractions above 150°C; The toluene front fraction (containing toluene fraction) is distilled from the top of the tower through the cutting tower 2, and the bottom fraction is rectified and separated by the xylene tower 3 to obtain the xylene fraction. The toluene front distillate obtained from the top of the cutting tower 2 is then passed through the benzene-toluene cutting tower to realize the separation of the benzene front...

Embodiment 2

[0054] The coking crude benzene produced by the coking enterprise is used as the raw material (wherein the mass content of benzene and toluene is 68.8% and 12.1% respectively), after dehydration, filtering solid impurities, and preheating it, according to the crude benzene separation scheme B, from the cutting tower. 1. The middle feed, the tower is operated continuously at normal pressure, and the control tower still temperature is 126 ° C, and the crude benzene is divided into a toluene front fraction (containing toluene fraction) and a toluene rear fraction; wherein the toluene front fraction passes through the benzene-toluene cutting tower again. The separation of benzene front fraction (containing benzene fraction) and toluene is realized, while the toluene rear fraction is separated from xylene through a xylene tower.

[0055] N-formyl morpholine was selected as solvent, the solvent ratio of the de-aromatic column was 3.5, the reflux ratio was 30, and other operating cond...

Embodiment 3

[0058] Taking the coking crude benzene produced by the coking enterprise as the raw material (wherein the mass contents of benzene and toluene are respectively 68.8% and 12.1%), dewatering and filtering the solid impurities, and preheating it, according to the crude benzene separation scheme C, from the tower 1 The middle feed, the tower is operated continuously at normal pressure, and the crude benzene is divided into benzene front fraction (containing benzene fraction) and distilled from the top of the tower; the bottom fraction is passed through the toluene tower 2 and the xylene tower 3, and the toluene and the xylene fraction are separated by toluene and xylene. seperate.

[0059]Sulfolane was selected as the solvent, the solvent ratio of the non-aromatics tower was 4.3, the operating pressure was 0.23 MPa, the temperature at the bottom of the tower was controlled at 162°C to 165°C, the feed temperature of the lean solvent was 105°C, and other operating conditions were the...

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Abstract

The present invention relates to a refining method of coking crude benzol. The method has four following sequential steps as follows: thepretreatment process of raw materials, the refining process of doffing non-arene and doffing othiophene, the deep desulfurization process of thiophene alkyl, and the refining process of toluene and xylene. The products of high-purity sulfur-free benzene, toluene and xylene can be made. The detailed technological process can be referred to the specification munual. Compared with the traditional pickling method, the present invention has the following advantages: the whole process has no production of acid tar, no serious pollution to the environment and no serious corrosion of equipment; at the same time, the present invention avoids sulfonate loss of arene, effectively improves the reclamation rate of arene and belongs to an environmental friendly technology. Besides, the products of coking benzene category are obviously superior in quality to the traditional pickling. Compared with the catalytic hydrogenation process, the process is simple and not only can save a substantial amount of investment costs, but also the operation cost of device is low. The quality of benzene products is equivalent to hydrogenated benzene. The present invention provides an environmentally protective and economical process for the reasonable development and utilization of coking benzene resources, and has quite broad application prospects.

Description

technical field [0001] The invention relates to the fields of chemical separation engineering and catalytic reaction engineering, in particular to an environment-friendly coking crude benzene refining method, which adopts extractive distillation technology to remove impurities such as non-aromatic hydrocarbons and thiophenes in coking benzene, Alkylation means deep desulfurization of coke benzene. Background technique [0002] Benzene and toluene are important basic organic chemical raw materials, and one of their important sources is coking crude benzene, a by-product of iron and steel enterprises and coking enterprises. Due to the complex composition of crude benzene and containing many impurities, especially thiophene and saturated alkanes, these impurities cannot be completely removed when crude benzene is purified by the traditional pickling process, thereby affecting the quality of coking aromatic products, especially Many quality indicators of coking benzene have a b...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C15/02C07C7/04
Inventor 罗国华徐新
Owner BEIJING INSTITUTE OF PETROCHEMICAL TECHNOLOGY
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