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Coking benzene deep desulfuration purification method

A technology for deep desulfurization and coking of benzene, applied in chemical instruments and methods, organic chemistry, hydrocarbons, etc., can solve the problems of inability to completely remove thiophene, short regeneration cycle of adsorbents, harsh reaction conditions, etc. Mild conditions, low environmental pollution, and low equipment corrosion

Inactive Publication Date: 2013-03-20
BEIJING INSTITUTE OF PETROCHEMICAL TECHNOLOGY
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AI Technical Summary

Problems solved by technology

At present, the catalytic hydrogenation method is used for the treatment of large-tonnage coking benzene. This method generally uses Co-Mo and Ni-W series catalysts to hydrogenate and saturate thiophene into hydrogen sulfide for removal under high temperature and high pressure conditions. After hydrogenation treatment The sulfide index in the final benzene product can reach the standard of petroleum benzene. Because the reaction conditions of this method are very harsh, the desulfurization process consumes hydrogen, and the process is very complicated. Therefore, the cost of producing sulfur-free benzene from coking benzene is generally high, and the process Suitable for large tonnage coking benzene treatment
For the vast majority of small and medium-sized coking enterprises and iron and steel enterprises, the traditional pickling method is still adopted, that is, thiophene in coking benzene reacts with sulfuric acid to generate thiophene sulfonic acid, and under the catalytic action of sulfuric acid, thiophene reacts with unsaturated olefins in coking benzene. The process is simple, the production cost is low, and the technology is very mature. Therefore, most coking benzene products in my country are produced by this method, but this process cannot completely remove the coking benzene. Thiophene, especially for coking benzene with relatively high thiophene content, even after two-stage pickling process, coking benzene still contains a small amount of thiophene impurities (generally, the concentration of thiophene is about 300 mg / L), and these small amounts of thiophene impurities will also It affects the subsequent production process related to the catalytic process (such as the process of coking benzene to catalyze the oxidation of maleic anhydride and the process of nitration to produce nitrobenzene and hydrogenation to produce aniline), so it must also be deeply desulfurized
There are many methods for deep desulfurization of coking benzene, and the representative one is to use adsorbent to selectively adsorb trace thiophene impurities in coking benzene, such as using A, X, Y, ZSM-5 and their modified zeolites for coking benzene adsorption desulfurization, The adsorption capacity reported in the research is generally low, and the regeneration cycle of the adsorbent is short, especially for the coking benzene adsorption desulfurization process with high thiophene content, and the regeneration process needs to be regenerated by high-temperature hot nitrogen purge or roasting. This desulfurization method has not been reported on industrial application so far, and the development trend is to develop adsorbents with large adsorption capacity.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0022] Take industrial water glass (modulus is 3.3, Na 2 O%=8.3, SiO 2 %=26-28) is silicon source, sodium aluminate is aluminum source, cetyltrimethyl amine bromide (CTAB) is template agent, molar ratio is SiO 2 :Al 2 O 3 :CTAB:H 2 O=60:1:5:1200, MCM-41 is synthesized by traditional hydrothermal method, after roasting, 0.4mol / LNH 4 NO 3 The HMCM-41 zeolite molecular sieve was prepared by three-time ion exchange of the solution, which was impregnated and modified with 0.8 mol / L sulfuric acid aqueous solution, and dried and calcined to obtain a solid acid catalyst. Using coking benzene containing 500mg / L thiophene (about 0.05%wt) as the raw material, isoamylene as the alkylating agent, the coking benzene solution containing 5%wt isoamyl at a reaction temperature of 200℃, 2.0MPa 2.33h -1 The flow rate is passed into the fixed bed reactor for the thiophene alkylation reaction, and the thiophene in benzene is almost completely converted into Cpentaalkylthiophene product. The reaction...

Embodiment 2

[0024] The raw material coking benzene comes from industrial raw materials after acid washing. The content of thiophene is 235mg / L, the bromine index is 65mgBr / 100g, the acidic zeolite molecular sieve HMCM-41 (Si / Al=60) is the catalyst, and isobutylene is the alkylating agent. , When the reaction temperature is 85℃, normal pressure, the feed weight space velocity of raw material coking benzene is 2.4h -1 , Isobutylene gas (mixed with nitrogen in a 1:1 molar ratio) with a flow rate of 2mL / min, and a 150-hour reaction comprehensive sample is rectified to remove the heavy component alkylthiophene by a rectification tower with a theoretical plate of 15. The thiophene content in the resulting benzene product Below 4mg / L, the alkylation rate of thiophene is as high as 98.3%, and the activity of the catalyst does not show a significant downward trend.

[0025] The benzene product after alkylation desulfurization is at room temperature, atmospheric pressure, and the raw material liquid ma...

Embodiment 3

[0027] Use coking light benzene containing 3350mg / L thiophene (from the benzene-toluene-xylene mixed fraction of crude benzene treated by the pre-fractionation unit, which contains 80.7% of benzene, 15.4% of toluene, and 3.5% of xylene) as raw material, N -Methylpyrrolidone is the extractant, the actual number of plates in the distillation tower is 45, the solvent ratio is 3 (that is, the ratio of the volume flow rate of the extractant to the raw coking light benzene), and the reflux ratio is 3, and the top of the tower is controlled When the temperature is 78-80℃, and the temperature of the bottom of the tower is 159-165℃, the concentration of thiophene in the coking benzene in the top fraction of the extractive distillation column is reduced to about 189mg / L. The coking benzene product is mixed with concentrated sulfuric acid at a ratio of 10:1 (volume ratio of coking benzene to concentrated sulfuric acid). After pickling for 15 minutes at a temperature of 50℃ and vigorous sti...

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Abstract

The invention discloses a method of coking benzene deep desulfurizing refined method, which comprises the following steps: adopting catalytic alkylthiophene desulfuration and selective adsorption desulfurizing associated craft; generating alkylthiophene with higher boiling point; rebuilding alkylthiophene through rectifying abscission; selective-adsorbing with desulfurizer; stripping excess un-reaction thiophene; reaching the demand of deep purifying harmful sulfur impurities in coking benzene. This invention possesses small corrosion, low cost and high earning rate, which is a better method for deep processing by-product of steel company and coking plant.

Description

Technical field [0001] The invention relates to a refining method for removing a small amount of thiophene in coked benzene, in particular to a combined method of catalytic thiophene alkylation desulfurization and selective adsorption desulfurization. Background technique [0002] Coking benzene is a by-product of iron and steel enterprises and coking enterprises, and it is also a valuable resource for the development of organic chemicals and fine chemicals. However, because it contains a certain amount of thiophene impurities, its comprehensive development and utilization are largely restricted, especially in the field of catalysis. For a long time, the deep processing and utilization of this coking by-product has not been greatly developed. Removal of sulfide in coking benzene is the key to rational development of this resource. At present, the catalytic hydrogenation method is adopted for the treatment of large-tonnage coking benzene. The method generally adopts Co-Mo and Ni...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C7/00C07C7/163C07C15/04
Inventor 罗国华徐新
Owner BEIJING INSTITUTE OF PETROCHEMICAL TECHNOLOGY
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