Method for preparing purified petroleum benzine and concentrating thiofuran by cruden benzol

A technology for thiophene and crude benzene, which is applied in the field of preparing pure benzene and concentrated thiophene from crude benzene, can solve problems such as harsh technical conditions, equipment corrosion, environmental pollution, etc., and achieves high product quality specifications, mild desulfurization conditions, and simple process flow. Effect

Inactive Publication Date: 2009-01-14
BEIJING INSTITUTE OF PETROCHEMICAL TECHNOLOGY
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Problems solved by technology

Although my country's coking industry is rich in thiophene resources, thiophene cannot be recovered due to the general use of pickling or hydrogenation processes in the processing process, resulting in a shortage of this raw material market. At present, it mainly relies on foreign imports, and the price is very expensive
[0004] The traditional sulfuric acid washing method to treat coking light benzene not only cannot guarantee product quality, but also causes serious corrosion of equipment during the refining process, produces a large amount of acid tar and regenerated acid that cannot be reused at present, and constitutes serious pollution to the environment. Benzene also has certain degree loss, the precious thiophene resource cannot be recovered
[0005] The traditional catalytic hydrogenation method has a large investment scale, harsh technical conditions, high catalyst production costs, and thiophene is completely destroyed during the hydrogenation process
In addition, this process is only suitable for processing large-tonnage coking benzene, and is not suitable for promotion in small and medium-sized enterprises
Therefore, a better method has not been found so far to prepare crude benzene into pure benzene and concentrated thiophene

Method used

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  • Method for preparing purified petroleum benzine and concentrating thiofuran by cruden benzol

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Embodiment 1

[0016] Use coked light benzene containing 3350mg / L thiophene, that is, the benzene-toluene-xylene mixed fraction from the crude benzene treated by the pre-fractionation unit as raw material, which contains 80.7% of benzene, 15.4% of toluene, 3.5% of xylene, N -Methylpyrrolidone is the extraction agent, the actual number of plates in the rectification tower is 45, the solvent ratio (i.e. the ratio of the volume flow rate of the extraction agent to the raw material coking light benzene) is 3, and the reflux ratio is under the condition of 3: 1, the control The temperature at the top of the tower is 78--80°C, and the temperature at the bottom of the tower is 159--165°C, then the concentration of thiophene in the coked benzene in the overhead fraction of the extractive distillation tower drops to about 189mg / L. The bottom liquid of the tower is taken out and enters the solvent recovery tower, and the concentrate of thiophene is obtained at the top of the recovery tower, and the ben...

Embodiment 2

[0018] Use the benzene-toluene system containing 4250mg / L thiophene, that is, the fraction obtained from crude benzene through the pre-fractionation unit and benzene cutting and separation as the raw material, which contains 87.2% of benzene, 12.4% of toluene, and N,N-dimethylformamide As the extraction agent, the actual number of plates in the rectification tower is 40, the solvent ratio (i.e. the ratio of the volume flow rate of the extraction agent to the raw material) is 3, and the reflux ratio is 3:1, the temperature at the top of the control tower is 78-- 80°C, and the temperature of the tower bottom is 149--155°C, the concentration of thiophene in the coked benzene in the overhead fraction of the extractive distillation tower will drop to about 165mg / L. The bottom liquid of the tower is taken out and enters the solvent recovery tower, and the concentrate of thiophene is obtained at the top of the recovery tower, and the benzene containing thiophene concentration of 2.12%...

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Abstract

A process for preparing high-purity benzene and concentrated thiophene from crude benzene features use of two-class extracting and rectification. Its advantages are simple process, low corrosion to equipment, low cost and high output rate.

Description

technical field [0001] The present invention relates to the deep processing and utilization of by-products (i.e. crude benzene) produced in the industrial production process of iron and steel enterprises and coking enterprises, in particular, to a kind of crude benzene as raw material, through pre-fractionation unit, two-stage extraction and rectification Process for unitary preparation of pure benzene and thiophene concentrates. Background technique [0002] Benzene is an important basic organic chemical raw material. The annual consumption of benzene as an intermediate in organic chemical and fine chemical raw materials in my country accounts for about 45%-50% of domestic benzene production. The domestic petroleum benzene raw material has been in short supply, and the price is relatively low. High, which makes coking benzene an important source of local fine chemical raw materials, and its demand is increasing year by year. [0003] Thiophene is a very expensive chemical r...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C15/04C07C7/04C07D333/10
Inventor 罗国华杨春育徐新
Owner BEIJING INSTITUTE OF PETROCHEMICAL TECHNOLOGY
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