Preparation method of sulphonation phthalein cobalt catalyst using activated carbon as carrier

A technology of sulfonated cobalt phthalocyanine catalyst and sulfonated cobalt phthalocyanine salt, which is applied in other fields, can solve the problems of low cobalt saturation adsorption, low cobalt loading on the catalyst, low cobalt loading, etc., and achieve short processing time , high content, not easy to fall off

Inactive Publication Date: 2009-02-04
承德绿世界活性炭有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the sulfonated cobalt phthalocyanine catalysts prepared by these two types of preparation methods all have the problem of low cobalt loading.
The main reason is that most of the current activated carbon products have a microporous structure, and the surface area of ​​the micropores with a pore diameter less than 2nm generally accounts for more than 80% of the total surface area; while the diameter of the sulfonated cobalt phthalocyanine ion is relatively large, even if it is maintained for a long time time, it is also difficult to adsorb on the inner surface through the micropores of activated carbon, and the adsorption only occurs on the outer surface and mesopores of activated carbon, so that the absolute majority of the inner pore surface is not fully utilized, and the cobalt saturation adsorption is low, so that The cobalt loading of the final catalyst is relatively low

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0015] Weigh 200 mg of sulfonated cobalt phthalocyanine and dissolve it in 200 mL of NaOH solution with a mass concentration of 8%. The emulsified solution formed after thorough stirring is used as catalyst impregnation solution, and placed in a closed container with nitrogen protection.

[0016] The commercially available fruit shell granular activated carbon is used as the catalyst carrier. The main properties of the activated carbon are: moisture content 4%, specific surface area 900m 2 / g, average pore diameter 1.0nm, iodine adsorption value 750mg / g, particle size 5mm, weigh 1g of this kind of activated carbon and place it in a tubular heating furnace. After ℃, quickly move the activated carbon to the airtight container containing the catalyst impregnation solution for 1-60 seconds. With the rapid drop of temperature, the sulfonated cobalt phthalocyanine in the catalyst impregnation solution is completely loaded on the activated carbon carrier, cooling After reaching room ...

Embodiment 2

[0018] Weigh 200 mg sulfonated cobalt phthalocyanine and dissolve it in 200 mL of NaOH solution with a mass concentration of 8%. The emulsified solution formed after thorough stirring is used as catalyst impregnation solution, and placed in a closed container with nitrogen protection.

[0019] Weigh 5g of commercially available nutshell granular carbonized material and place it in a tubular heating furnace. Under the protection of nitrogen, heat it to 850°C at a heating rate of 10°C-20°C / min, and turn on the steam valve of the steam generator to Put superheated steam into the inner tube of the heating furnace with carbonized material, and maintain the temperature of the heating inner tube at 800°C to 850°C for 10 minutes to activate the carbonized material. After the activation process is completed, stop heating and increase the nitrogen flow rate to cool down After the temperature of the inner tube of the heating furnace drops to 500°C, quickly move the activated carbon into a...

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PUM

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Abstract

The present invention discloses a preparation method of a sulfonated cobalt phthalocyanine catalyst which takes active carbon as a carrier. The preparation method comprises the treatment of the active carbon and the preparation of the aqueous solution or the alkaline solution of sulfonated cobalt phthalocyanine. The preparation method is characterized in that the temperature of the active carbon is controlled to be 300 DEG C to 500 DEG C; under the protection of inert gas, the active carbon is directly dipped in the aqueous solution or the alkaline solution dissolved with the sulfonated cobalt phthalocyanine; or the aqueous solution or the alkaline solution dissolved with the sulfonated cobalt phthalocyanine is directly sprayed and dipped at the high temperature active carbon with the protection of the inert gas; then the sulfonated cobalt phthalocyanine catalyst with high load is obtained after cooling treatment once more. The content of sulfonated cobalt phthalocyanine active component loaded by the present invention is high; cobalt loaded quantity can be more than 10 percent of the quality of active carbon framework; the time for dipping or spraying and dipping treatment is short and is just 1 to 60 seconds; catalyzing active component loaded at the active carbon does not falling off easily, and the preparation method can be combined with the traditional active carbon preparation technology to prepare a catalyst product at a time.

Description

Technical field: [0001] The invention relates to a method for directly loading the catalytic active components of sulfonated cobalt phthalocyanine on an activated carbon carrier to prepare a solid catalyst with high cobalt content, in particular to a sulfonated cobalt phthalocyanine catalyst with activated carbon as a carrier The preparation method of the product is mainly used for catalytic sweetening treatment of liquid petroleum gas, gasoline, naphtha, diesel oil and other oil products, so that the oil products can achieve the purpose of deodorization, desulfurization and increasing stability. Background technique: [0002] With the increasing shortage of crude oil resources and increasing mining depth, the mining and processing of high-sulfur crude oil is increasing. According to preliminary statistics, it has occupied more than 60% of the market, and the annual average ratio of The increase of high-sulfur crude oil not only increases the difficulty of oil processing, bu...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J31/22B01J31/28
Inventor 凌凤军祁项超刘连浦
Owner 承德绿世界活性炭有限公司
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