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Solid acid catalyst supporting methane sulfonic acid, preparation method and application of same

The technology of a solid acid catalyst and methanesulfonic acid, which is applied in the polyester synthesis industry, can solve the problems of limited use of liquid acid, waste of national mineral resources, and cumbersome operation process.

Inactive Publication Date: 2015-05-27
EAST CHINA UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] (1) Hydrogenation process, this process is very effective for reducing the bromine index, but the process operation requirements are high and difficult, and the use of hydrogen is also relatively dangerous, so the scope of use is limited;
[0005] (2) White clay refining process, which is very simple to operate and has a high safety factor, and is adopted by most refineries, but the white clay in this process is easily deactivated under the condition of high bromine index, which causes a large amount of solid waste emissions and waste of national mineral resources
[0006] In order to concentrate the strengths of the above two processes and abandon their shortcomings, many methods have been studied, such as various modifications to clay to prolong its service life, but the effect is still limited
[0007] In previous studies, it was found that liquid pure methanesulfonic acid has a good effect on catalyzing the alkylation reaction of aromatics and olefins, and methanesulfonic acid is an environmentally friendly organic acid, which can be used in natural environment for 28 days It is decomposed into carbon dioxide, water and sulfur dioxide, but as a liquid acid, its scope of use is obviously limited, and it is difficult to use it on an industrial scale in existing processes
[0008] At present, there have been some reports on the introduction of sulfonic acid groups into the surface of silica, but they either require the use of templates, or the precursors of oxidants or sulfonic acid groups, and need to be washed in the later stage, which makes the production process difficult. Environmental pollution, and the operation process is cumbersome, which is not conducive to practical use

Method used

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  • Solid acid catalyst supporting methane sulfonic acid, preparation method and application of same
  • Solid acid catalyst supporting methane sulfonic acid, preparation method and application of same
  • Solid acid catalyst supporting methane sulfonic acid, preparation method and application of same

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0052] Add 21 g of ethyl orthosilicate and 50 g of anhydrous formic acid into the stirring tank, and stir for 30 minutes to obtain a uniform mixed solution. Then, 0.7 g of methanesulfonic acid was added, the stirring intensity was increased, and the stirring was continued for 50 minutes to form a catalyst intermediate. The obtained catalyst intermediate was allowed to stand at 30°C for 6 hours, then transferred to a muffle furnace, and calcined at a temperature of 100°C for 6 hours to obtain a solid acid catalyst.

[0053] The solid acid catalyst samples prepared in this example were evaluated as follows:

[0054] (1)N 2 Adsorption-desorption isotherm,

[0055] (2) Pore size distribution diagram,

[0056] (3) XRD pattern.

[0057] N of the solid acid catalyst sample obtained in Example 1 2 The adsorption-desorption isotherm curve, pore size distribution diagram, XRD diagram are shown respectively Figure 1-Figure 3 :

[0058] Among them, the N2 adsorption-desorption isotherm shows tha...

Embodiment 2

[0062] Add 21 g of ethyl orthosilicate and 50 g of anhydrous formic acid into the stirring tank, and stir for 30 minutes to obtain a uniform mixed solution. Then, 0.7 g of methanesulfonic acid was added, the stirring intensity was increased, and the stirring was continued for 50 minutes to form a catalyst intermediate. The obtained catalyst intermediate was allowed to stand at 30°C for 6 hours, and then transferred to a muffle furnace and calcined at a temperature of 500°C for 6 hours to obtain a solid acid catalyst.

[0063] As described in Example 1, the solid acid catalyst obtained in Example 2 was evaluated by XRD.

[0064] From image 3 It can be seen from the curves b and c that the solid acid catalyst sample of Example 2 also has the same XRD characteristics of the pure (amorphous) silica support, indicating that the catalyst calcined at 500°C and loaded with methanesulfonic acid is the same as that of Example 1. Compared with the silica structure, the catalyst calcined at ...

Embodiment 3

[0066] Take 2ml of the solid acid catalyst loaded with methanesulfonic acid prepared in Example 1 and Example 2, and put it into a micro fixed bed reactor at a temperature of 100°C, a pressure of 1.0 MPa, and a weight space velocity of 30 h -1 Under the conditions, the reaction is 8 hours. Sampling and analysis are performed every hour, and the bromine index of the sample is analyzed with a bromine index instrument. The catalytic performance curve of the catalyst with the olefin removal rate as a measure is shown in Figure 4 .

[0067] This figure shows that the catalyst still has considerable catalytic performance after being calcined at 500°C, but the catalytic performance is slightly lower than that of the catalyst calcined at 100°C.

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Abstract

The invention relates to a solid acid catalyst supporting methane sulfonic acid, a preparation method and an application of the same. In particular, the invention provides a strong acidic solid acid catalyst for removing olefin components from aromatic hydrocarbon, wherein the strong acidic solid acid catalyst is in the form of an amorphous state and includes amorphous silicon dioxide and the methane sulfonic acid supported thereon. The strong acidic solid acid catalyst is prepared through following steps: (1) under a water-free condition, mixing tetraethoxysilane (TEOS) and anhydrous formic acid to obtain a homogeneous solution; (2) adding the methane sulfonic acid and mixing the mixture continuously to form a catalyst intermediate; and (3) roasting the intermediate to obtain the strong acidic solid acid catalyst. The invention also provides the preparation method and the application of the strong acidic solid acid catalyst. The strong acidic solid acid catalyst has an excellent catalytic performance. Successful preparation and application of the catalyst develops a new way of novel green industrialization.

Description

Technical field [0001] The invention relates to the polyester synthesis industry, in particular to a strong acid solid acid catalyst for removing aromatic hydrocarbons, especially olefin components in p-xylene. The strong acid solid acid catalyst is prepared under anhydrous conditions using ethyl orthosilicate (TEOS) as a silicon source, anhydrous formic acid as a hydrolysis catalyst, and methanesulfonic acid as an acid modifier. The invention also relates to a preparation method of the strong acid solid acid catalyst and the application of the strong acid solid acid catalyst for removing olefin components in the production of aromatic hydrocarbons, especially p-xylene. technical background [0002] In recent years, with the rapid development of my country's polyester industry and the vigorous intervention of private enterprises, my country's demand for terephthalic acid has continued to grow. As the direct upstream raw material of terephthalic acid, the demand for p-xylene is n...

Claims

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Application Information

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IPC IPC(8): B01J31/02C07C15/08C07C7/148
CPCY02P20/52
Inventor 施力刘乃旺濮鑫王昕
Owner EAST CHINA UNIV OF SCI & TECH
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