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Fuel oil oxidative desulfurization method based on silica gel loaded with cesium salt catalyst of heteropoly acid

A technology for loading heteropolyacids and oxidative desulfurization, which is applied in chemical instruments and methods, physical/chemical process catalysts, chemical/physical processes, etc., and can solve problems such as difficult recycling of catalysts, large consumption of oxidants, and difficulty in ensuring safety. , to achieve the effects of easy recycling and reuse, short reaction time, and shortened reaction time

Inactive Publication Date: 2011-07-20
SHANDONG UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, such processes have problems such as difficult recycling of catalysts or certain toxicity, large consumption of oxidants, difficulty in ensuring safety, and high costs, which fundamentally limit industrial production applications.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0021] Embodiment 1: Thiophene (TH)-n-octane simulation system

[0022] Taking thiophene (TH), which is difficult to remove in hydrodesulfurization, as a representative, dissolve a certain amount of TH in 60ml of n-octane to prepare a simulation system with a sulfur content of 350ppm, add 60ml of acetonitrile, and heat to 60°C with magnetic stirring . Calculate H by O / S (molar ratio) = 15 2 o 2 Adding amount, 50% Cs calculated by 1% n-octane mass 2.5 h 0.5 PW 12 o 40 / SiO 2 The amount added, the H 2 o 2 with 50% Cs 2.5 h 0.5 PW 12 o 40 / SiO 2 After mixing and contacting for 10 minutes, it was added to the above simulation system, and the content of TH in n-octane decreased by 84.5% after 2 hours of reaction.

[0023] The silica gel loaded heteropolyacid cesium salt 50%Cs 2.5 h 0.5 PW 12 o 40 / SiO 2 Obtained by the following preparation methods: (1) pretreatment of silica gel carrier: silica gel is soaked at room temperature for 12 hours with 5% hydrochloric ...

Embodiment 2

[0024] Embodiment 2: the simulation system of thiophene (TH)-n-octane

[0025] Taking thiophene (TH), which is difficult to remove in hydrodesulfurization, as a representative, dissolve a certain amount of TH in 60ml of n-octane to prepare a simulation system with a sulfur content of 350ppm, add 60ml of acetonitrile, and heat to 60°C with magnetic stirring . Calculate H by O / S (molar ratio) = 15 2 o 2 Adding amount, 20% Cs calculated by 0.1% n-octane mass 2.5 h 0.5 PW 12 o 40 / SiO 2 The amount of catalyst added, the H 2 o 2 with 20% Cs 2.5 h 0.5 PW 12 o 40 / SiO 2 After mixing and contacting for 10 minutes, it was added to the above simulation system. After 3 hours of reaction, the content of TH in n-octane dropped by 88.1%.

[0026] The silica gel loaded heteropolyacid cesium salt 20%Cs 2.5 h 0.5 PW 12 o 40 / SiO 2Obtained by the following preparation methods: (1) pretreatment of silica gel carrier: silica gel is soaked at room temperature for 12 hours with 5...

Embodiment 3

[0027] Embodiment 3: the simulation system of thiophene (TH)-n-octane

[0028] Taking thiophene (TH), which is difficult to remove in hydrodesulfurization, as a representative, dissolve a certain amount of TH in 60ml of n-octane to prepare a simulation system with a sulfur content of 350ppm, add 60ml of acetonitrile, and heat to 60°C with magnetic stirring . Calculate H by O / S (molar ratio) = 15 2 o 2 Adding amount, 20% Cs calculated by 1% n-octane mass 2.5 h 0.5 PW 12 o 40 / SiO 2 The amount of catalyst added, the H 2 o 2 with 20% Cs 2.5 h 0.5 PW 12 o 40 / SiO 2 After mixing and contacting for 5 minutes, it was added to the above simulation system. After 2 hours of reaction, the content of TH in n-octane decreased by 88.5%.

[0029] The silica gel loaded heteropolyacid cesium salt 20%Cs 2.5 h 0.5 PW 12 o 40 / SiO 2 The preparation method is with embodiment 2.

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Abstract

The invention discloses an oil desulfurization method of the silica gel loaded with cesium salt catalyst of heteropoly acid and the method uses hydrogen peroxide as oxidant and the silica gel loaded with cesium salt of heteropoly acid as catalyst. The method comprises the following steps: oi and acetonitrile used as solvent are mixed according to a certain ratio, the mixture of the oxidant and the catalyst are added in the mixed solution at a certain temperature under the atmospheric pressure, the mixture is cooled to the room temperature after the reaction, then the reaction fluid is layered naturally, the upper oil phase is desulfurized oil, the lower layer is acetonitrile phase with the product and the catalyst, and the catalyst performs solid-liquid separation and is cleaned with acetonitrile, thus the catalyst can be recycled and reused. The catalyst used in the method has simple and safe preparation process, is non-toxic and harmless, has no pollution and can be recycled and reused. Compared with the traditional process, the process is simple, the catalyst can be recycled and directly reused, the desulfurization efficiency is high, the dosage of the oxidant is low and the method is suitable for industrial popularization and application.

Description

technical field [0001] The invention relates to a fuel oil oxidative desulfurization method based on a silica gel-loaded heteropolyacid cesium salt catalyst, and belongs to the interdisciplinary field of fuel oil deep processing and environmental protection technologies in the petrochemical industry. Background technique [0002] In recent years, with the increasingly stringent environmental protection requirements, the fuel sulfur content standards stipulated by countries around the world are also rapidly increasing. For example, according to the requirements of the US Environmental Protection Agency, from June 2006, refineries need to reduce the mass fraction of sulfur in gasoline from 400×10 -6 down to 30×10 -6 , the mass fraction of sulfur in highway diesel oil is from 500×10 -6 down to 15×10 -6 ; Other countries such as Australia, India and South Korea have also proposed roughly the same sulfur standards. At present, the mass fraction of sulfur in gasoline in my cou...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G53/14B01J27/188
Inventor 王睿王寒于凤丽杨烽
Owner SHANDONG UNIV
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