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Preparation method and application of a copper phosphotungstate/attapulgite clay composite oxidation desulfurization catalyst

A technology of attapulgite clay and desulfurization catalyst, which is applied in the field of copper phosphotungstic acid oxidation desulfurization catalyst, which can solve the problems of unsuitability for large-scale industrial application, difficult control of cooling and crystallization steps, high relative proportion of pure phosphotungstic acid, etc., and achieve repeated utilization High efficiency, low safety cost, simple and clear preparation process

Active Publication Date: 2017-01-18
CHANGZHOU UNIV
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

The patent with application number 201210249959 introduces the application of a double-effect copper phosphotungstic acid catalyst in oil desulfurization, but the relative proportion of pure phosphotungstic acid used in its preparation method is relatively high, and the cooling crystallization step is under laboratory conditions Difficult to control, not suitable for large-scale industrial applications

Method used

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  • Preparation method and application of a copper phosphotungstate/attapulgite clay composite oxidation desulfurization catalyst
  • Preparation method and application of a copper phosphotungstate/attapulgite clay composite oxidation desulfurization catalyst
  • Preparation method and application of a copper phosphotungstate/attapulgite clay composite oxidation desulfurization catalyst

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preparation example Construction

[0018] 1. Preparation of copper phosphotungstate / attapulgite clay catalyst.

[0019] Measure 20mL of 0.1mol / L sodium hydroxide solution, add 10mL of 0.1mol / L copper nitrate dropwise to it, a blue flocculent precipitates, stir for 5min to make the reaction complete. Wash with deionized water several times during suction filtration, and then vacuum dry at 40°C for 1 hour to obtain copper hydroxide powder. Weigh 0.2g of copper hydroxide powder, add it to 10mL of water, and disperse it evenly by ultrasonic vibration; weigh 3.0g of phosphotungstic acid (H 3 PW 12 o 40 14H 2 (2) was dissolved in 20mL water to obtain a phosphotungstic acid solution; then, the phosphotungstic acid solution and 30mL 3g / 10mL attapulgite slurry were added dropwise to the uniform dispersion system while stirring until the blue precipitate in the system disappeared completely. The total volume of the mixed solution is 50mL~60mL, stirred at room temperature for 10min, and dried at 100°C for 2h to obtain...

Embodiment 1

[0021] Add 0.1g catalyst to 50mL simulated oil with sulfur content of 200ppm prepared by mixing 0.3g benzothiophene (BT) and 500mL n-octane, add 0.12mL H 2 o 2 and 0.1 g of cetyltrimethylammonium bromide (CTAB), magnetically stirred in a water bath at 40° C. for 1 h, the reaction mixture was cooled to room temperature, and the layers were separated. Add 25mL of N-N-dimethylformamide (DMF) and continue to stir for 5min, statically separate the layers, separate the oil phase, measure the sulfur content and calculate the desulfurization rate to be 64.84%.

[0022] The catalyst in the mixed system was recovered by suction filtration, dried at 70°C for 1 hour, washed with water several times, and reused according to the above method after drying.

[0023] In the above method, benzothiophene was replaced by dibenzothiophene (DBT), and other conditions remained unchanged, and the desulfurization rate was measured, see Table 1 for details.

Embodiment 2

[0025] Add 0.2g catalyst to 50mL simulated oil with sulfur content of 200ppm prepared by mixing 0.3g benzothiophene (BT) and 500mL n-octane, add 0.12mL H 2 o 2 and 0.1 g of cetyltrimethylammonium bromide (CTAB), magnetically stirred in a water bath at 40° C. for 1 h, the reaction mixture was cooled to room temperature, and the layers were separated. Add 25mL of N-N-dimethylformamide (DMF) and continue to stir for 5min, statically separate the layers, separate the oil phase, measure the sulfur content and calculate the desulfurization rate to be 75.26%.

[0026] The catalyst in the mixed system was recovered by suction filtration, dried at 70°C for 1 hour, washed with water several times, and reused according to the above method after drying.

[0027] In the above method, benzothiophene was replaced by dibenzothiophene, and other conditions remained unchanged, and the desulfurization rate was measured, see Table 1 for details.

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Abstract

The invention belongs to the field of fuel oxidation desulfurization, and particularly relates to a copper phosphotungstate oxidation desulfurization catalyst. The technical scheme is as follows: a preparation method of the copper phosphotungstate / attapulgite clay composite oxidation desulfurization catalyst comprises steps as follows: deionized water is added to copper hydroxide, a phosphotungstic acid solution and attapulgite clay slip are slowly dropwise added to the copper hydroxide while stirring, stirring is performed continuously until blue floccule precipitate just disappears, and addition is stopped; then a copper phosphotungstate / attapulgite clay composite is obtained through aging and drying. Insoluble copper hydroxide floccule is used as a raw material, insoluble copper salt molecules and attapulgite clay molecules are bonded together, phosphotungstic acid reacts with copper salt, and the composition is firmer; operation conditions are mild, the recycling efficiency is high, the efficiency of removal of benzothiophene compounds which are difficult to remove through catalytic hydrogenation is higher, and the application prospect is bright.

Description

technical field [0001] The invention belongs to the field of oxidative desulfurization of fuel oil, in particular to a catalyst for oxidative desulfurization of copper phosphotungstate. Background technique [0002] With the rapid development of the automobile industry, people's awareness of the social environment is strengthening, and the fuel sulfur content standards stipulated by countries around the world are also rapidly increasing. The United States and the European Union limit the sulfur content of oil products to no more than 15ppm and 10ppm respectively. my country's Beijing and Shanghai have formulated local standards in 2007 and 2009 respectively, limiting the sulfur content of gasoline and diesel to below 50ppm. From 00:00 on May 31, 2012, Beijing will implement two new local standards for vehicle gasoline and diesel, that is, the "Beijing V" fuel standard. European standards at the same stage are basically in line. Hydrodesulfurization (HDS) is usually used i...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J31/26C10G27/12
Inventor 姚超吕新刚李霞章左士祥刘文杰魏科年罗士平
Owner CHANGZHOU UNIV