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Refined crude benzene and method for extracting thiophene

A technology of crude benzene and thiophene, which is applied in extraction and purification/separation, treatment of hydrocarbon oil, organic chemistry, etc., can solve the problems of lower production material and process requirements, lower reaction pressure and temperature, and reduce the difficulty of making reactors. Reduced material and process requirements, reduced reaction pressure and temperature, and reduced production difficulty

Inactive Publication Date: 2012-08-01
JIANGSU YONGPENG TECH INDAL
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] In order to overcome the defects of serious pollution, low yield, difficult post-treatment, complex process of hydrorefining method, large equipment investment, high energy consumption and low yield by using the pickling and refining method in the refining process of crude benzene, the present invention uses crude benzene as Raw materials, pure benzene, toluene, xylene, solvent oil and thiophene are produced through crude benzene de-heavy, primary hydrogenation, de-light, extraction, secondary hydrogenation and rectification. A series of advantages such as simplicity, short production cycle, and high product purity. Compared with the traditional process, not only the product quality is better, but also pollution-free, the reaction is mild, and the reaction pressure and temperature are greatly reduced. The reduction of reaction pressure and temperature is conducive to reducing The difficulty of making the reactor, the material and process requirements of the reactor have been greatly reduced, further reducing the production cost

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0016] Send a certain amount of crude benzene into the two-benzene tower and then send it into steam to start the temperature-raising distillation, (the theoretical plate number of the two-benzene tower is not less than 45, the pressure is controlled at -30Kpa--40KPa, the temperature at the top of the tower is controlled at 120°C, the tower The temperature of the kettle is controlled at >190°C, and the reflux ratio is 0.2-0.3.) The part with a distillation range greater than 210°C is used as a heavy benzene product and sent to storage equipment for storage; the part with a distillation range less than 210°C is sent to the next step as light benzene Grade equipment evaporator. Send light benzene into the evaporator and heat it to 100°C to change into gas phase, then send it into the first-stage hydrogenation reactor, the hydrogen purity in the hydrogenation reactor is kept above 90%, and at the same time add the catalyst NI-MO, the molar ratio of the amount of hydrogen is : NI-...

Embodiment 2

[0018]Send a certain amount of crude benzene into the two-benzene tower and then send it into steam to start the temperature-raising distillation, (the theoretical plate number of the two-benzene tower is not less than 45, the pressure is controlled at -30Kpa--40KPa, the temperature at the top of the tower is controlled at 120°C, the tower The temperature of the kettle is controlled at >190°C, and the reflux ratio is 0.2-0.3.) The part with a distillation range greater than 210°C is used as a heavy benzene product and sent to storage equipment for storage; the part with a distillation range less than 210°C is sent to the next step as light benzene Grade equipment evaporator. Send light benzene into the evaporator and heat it to 110°C to change into gas phase, then send it into the first-stage hydrogenation reactor, the hydrogen purity in the hydrogenation reactor is kept above 90%, and at the same time add the catalyst NI-MO, the molar ratio of the amount of hydrogen is : NI-M...

Embodiment 3

[0020] Send a certain amount of crude benzene into the two-benzene tower and then send it into steam to start the temperature-raising distillation, (the theoretical plate number of the two-benzene tower is not less than 45, the pressure is controlled at -30Kpa--40KPa, the temperature at the top of the tower is controlled at 120°C, the tower The temperature of the kettle is controlled at >190°C, and the reflux ratio is 0.2-0.3.) The part with a distillation range greater than 210°C is used as a heavy benzene product and sent to storage equipment for storage; the part with a distillation range less than 210°C is sent to the next step as light benzene Grade equipment evaporator. Send light benzene into the evaporator and heat it to 120°C to change into gas phase, then send it to the first-stage hydrogenation reactor, the hydrogen purity in the hydrogenation reactor is kept above 90%, and at the same time add the catalyst NI-MO, the molar ratio of the amount of hydrogen is : NI-MO...

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Abstract

The invention discloses refined crude benzene and a method for extracting thiophene, which belongs to the chemical field. According to the invention, crude benzene is taken as a main raw material, hydrogen, a catalyst NI-MO and an extract N-formylmorpholine as auxiliary materials, two benzene towers, an evaporator, a section of hydrogenation reactor, a lightness-removing tower, an extraction tower, a regeneration tower, two section of hydrogenation reactor and a fractionate tower as equipments, benzene series products and thiophene can be prepared by an extraction method; the method has the advantages that the reaction of whole production process is mild, the pressure and the temperature are low, the reduction of reaction pressure and temperature is in favor of reducing the making difficulty of the reactor, The making material and technology requirements of the reactor are greatly reduced, thereby the investment cost can be further reduced, The yield and the purity of the benzene series products are high, compared with other technology, thiophene products with high added value can be obtained.

Description

Technical field: [0001] The invention belongs to the field of chemical industry, and is characterized in that it relates to a method for refining crude benzene and extracting thiophene therefrom. Background technique: [0002] Crude benzene is one of the products in the crude gas generated during the coal coking process. The coke oven gas after deamination contains benzene, toluene, xylene, trimethylbenzene, thiophene, indene and other aromatics, in addition to unsaturated compounds, Sulfur-containing compounds, aliphatic hydrocarbons, naphthalene, phenols and pyridine compounds are called crude benzene. Crude benzene is a light yellow transparent liquid, lighter than water, insoluble in water, and forms a resinous substance due to oxidation and polymerization of unsaturated compounds during storage. Soluble in crude benzene, the color becomes dark. Due to the large number of coking industries in my country, a large amount of crude benzene is produced annually, and the dire...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C15/04C07C15/06C07C15/08C07C7/04C07C7/10C07D333/10C10G67/14
CPCY02P20/52
Inventor 彭宏王晋勇林鹏增
Owner JIANGSU YONGPENG TECH INDAL