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Aromatic aldehyde selective hydrogenation catalyst for refining terephthalic acid

A technology of terephthalic acid and hydrogenation catalyst, applied in metal/metal oxide/metal hydroxide catalyst, physical/chemical process catalyst, carboxylate preparation, etc., can solve the problem of low selectivity of 4-HMBA , to achieve the effect of simplifying the process, enhancing hydrophilic properties, reducing operating costs and energy consumption

Active Publication Date: 2010-07-07
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] The technical problem to be solved by the present invention is the problem of low selectivity of 4-HMBA generated by hydrogenation of 4-CBA existing in the prior art, and a new catalyst for the selective hydrogenation of aromatic aldehydes for the purification of terephthalic acid is provided

Method used

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  • Aromatic aldehyde selective hydrogenation catalyst for refining terephthalic acid
  • Aromatic aldehyde selective hydrogenation catalyst for refining terephthalic acid
  • Aromatic aldehyde selective hydrogenation catalyst for refining terephthalic acid

Examples

Experimental program
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Effect test

Embodiment 1

[0029] Weigh 50 grams of 4-8 mesh, flaky coconut shell activated carbon, the specific surface is 1078 square meters per gram, and the pore volume is 0.47 milliliters per gram. After removing the dust adsorbed on the carbon surface and the loose parts on the surface, oxidize it with 0.5 mol / L nitric acid in a washing tank at a temperature of 60°C for 3 hours, and then wash it with deionized water until neutral. and dried at 120° C. for 2 hours before use. Take by weighing 0.5 gram of palladium-containing 20% ​​chloropalladic acid solution, then add 4.05 gram of NiCl 2 ·6H 2 O, then add an appropriate amount of surfactant and sodium carbonate, and finally add deionized water to dilute to the amount of the solution just submerged gac carrier is advisable. The carrier was impregnated with the catalyst active component solution, aged for 24 hours, then reduced with hydrogen, then washed with pure water until neutral and dried to obtain the catalyst product. The physical propertie...

Embodiment 2~9

[0031] Catalysts were prepared according to the steps and operating conditions of Example 1, except that the type, concentration, temperature, time, and type, precursor, and content of the active component were changed. See Table 1 for details.

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Abstract

The invention relates to an aromatic aldehyde selective hydrogenation catalyst for refining terephthalic acid, which mainly solves the problem of the prior art that hydrogenation of p-Eormylbenzoic acid (short for 4-CBA) mainly generates p-methyl benzoic acid (short for P-TA), and the product of p-Eormylbenzoic acid (short for 4-CBA) has low selectivity. Through adopting the technical scheme that the active carbon modified by oxidant is taken as carrier to carry one or more than one of palladium, ruthenium, nickel, zinc, copper and the like, the invention can better solve the problem and can be applied to the industrial production of terephthalic acid hydrofining.

Description

technical field [0001] The invention relates to an aromatic aldehyde selective hydrogenation catalyst used for refining terephthalic acid. Background technique [0002] The supported palladium / carbon catalyst is suitable for the purification of crude terephthalic acid. Impurities such as 4-CBA in crude terephthalic acid are converted into other compounds by hydrogenation, and then separated and purified by crystallization. In industrial production, the hydrogenation of 4-CBA in crude terephthalic acid mainly produces P-TA and contains a very small amount of 4-HMBA. [0003] As an important monomer, 4-HMBA is used in the synthesis of the corresponding homopolymer, poly-tere-benzoate or the corresponding ester, polymethyl-para-hydroxymethyl-benzoate (mep-HMB). Because 4-HMBA is more soluble in solvent water than PT acid, it is easy to separate from PTA, and the hydrogenation of each carbonyl to alcohol only consumes one molecule of active hydrogen. And hydrogenolysis into hy...

Claims

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Application Information

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IPC IPC(8): B01J23/89B01J23/60C07C65/01C07C51/367
CPCY02P20/52
Inventor 姜瑞霞畅延青孙广斌朱小丽
Owner CHINA PETROLEUM & CHEM CORP