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Solid acid complex catalyst and its preparing process

A composite and catalyst technology, applied in the field of solid acid composite catalyst and its preparation, can solve the problems of easy loss, uneven distribution of acid centers, few active centers, etc., and achieves high acid strength, uniform distribution of acid centers, and preparation method. Simple and easy effects

Inactive Publication Date: 2005-01-26
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

But these two methods also have some disadvantages: in the former method, the liquid acid is difficult to immobilize, and it is very easy to lose; in the latter method, the acid center is unevenly distributed, the active center is few, and a higher reaction temperature is required, so in some Reactions that require strong acid or low temperature, such as the alkylation of isobutane butene, are currently difficult to replace liquid acids
In fact, in this type of reaction, although the acid strength of solid superacids is much higher than that of sulfuric acid, solid superacids still cannot reach the reactivity of liquid acids such as 95% sulfuric acid.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

example 1-6

[0048] These examples illustrate the preparation and catalytic performance of the liquid acid-perfluorosulfonic acid resin-silicon dioxide solid acid composite catalyst provided by the invention.

[0049] Mix orthosilicate and alcohol in a beaker, stir until the solution is clear, add sulfuric acid or phosphoric acid and a certain amount of perfluorosulfonic acid resin alcohol solution with a content of 5% by weight to the above mixed solution, and stir at a certain temperature until A gel is formed. Separate the formed gel, put it in a vacuum oven, and dry it at 50° C. for 48 hours under a vacuum of 10 mmHg to obtain the silicon-based solid acid composite catalyst provided by the present invention, and store it in a desiccator . The specific operating conditions of each example are shown in Table 6.

[0050] See Table 7 for the acid strength, surface acid content, and total acid content of the samples prepared in each example before and after the 8-hour alkylation evaluatio...

Embodiment 7-9

[0056] These examples illustrate the preparation and catalytic performance of the sulfuric acid-perfluorosulfonic acid resin-titanium dioxide solid acid composite catalyst provided by the invention.

[0057] Mix titanate and alcohol in a 100ml beaker, quickly add sulfuric acid aqueous solution to the above mixed solution, stir until the solution is clear, add a certain amount of perfluorosulfonic acid resin alcohol solution with a content of 5% by weight, and stir at a certain temperature to form a gel. Put the gel into a vacuum oven, and dry it at 50° C. for 48 hours under the condition of a vacuum degree of 10 mmHg to obtain the titanium-based solid acid composite catalyst provided by the present invention, which is stored in a desiccator. The specific operating conditions of each example are shown in Table 9.

[0058] See Table 10 for the acid strength, surface acid content, and total acid content of the samples prepared in each example before and after the 8-hour alkylati...

Embodiment 10-11

[0064] These examples illustrate the preparation and catalytic performance of the sulfuric acid-perfluorosulfonic acid resin-zirconia solid acid composite catalyst provided by the invention.

[0065] Mix zirconate and alcohol in a 100ml beaker, stir until the solution is clear, add sulfuric acid and a certain amount of perfluorosulfonic acid resin alcohol solution with a content of 5% by weight to the above mixed solution, and stir at a certain temperature until condensation is formed. glue. Put the gel into a vacuum oven, and dry it at 50° C. for 30 hours under the condition of a vacuum degree of 10 mmHg to obtain the zirconium-based solid acid composite catalyst provided by the present invention, which is stored in a desiccator. The specific operating conditions of each example are shown in Table 12.

[0066] See Table 13 for the acid strength, surface acid content, and total acid content of the samples prepared in each example before and after the 8-hour alkylation evaluat...

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PUM

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Abstract

The invention is a solid acid compound catalyst whose component is: 10-80% sulfuric acid or phosphoric acid, 1-10% fluosulfonic acid resin and oxide of silicon, aluminum, titanium or zirconium; the fluosulfonic acid resin the polymer of perfluoroethylene and sulfonated perfluoroethylene, its average molecular weight is 300-500 thousands, the sulfonating rate is 1-5%. The mol rate of carbon element and fluorin element is 1:2. The catalyst blends the liquid acid and solid acid into a compound evenly, it maintains the nature of the liquid acid and the solid acid, and it has higher acid intensity and acid center quantity, the distribution of the acid center is even, the liquid acid will not be lost in the reaction.

Description

technical field [0001] The invention relates to a solid acid composite catalyst and a preparation method thereof. More specifically, it relates to a solid acid composite catalyst composed of liquid acid, solid acid and inorganic oxide and its preparation method. technical background [0002] Sulfuric acid, phosphoric acid, hydrofluoric acid and aluminum trichloride are widely used acid catalysts in industry. Some important processes such as alkylation, esterification, isomerization, etc. have used these catalysts or are still using them today. Although these catalysts have good catalytic activity, because they are all used under homogeneous conditions, compared with heterogeneous phases, they have problems such as difficult to achieve continuous production in technology, difficult separation of catalysts from raw materials and products, and easy equipment. Corrosion and other disadvantages; in addition, in some important chemical processes, a large number of by-products wi...

Claims

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Application Information

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IPC IPC(8): B01J31/12B01J31/38
Inventor 辛秀兰谢文华付强舒兴田闵恩泽
Owner CHINA PETROLEUM & CHEM CORP
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