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Process for production of purified terephthalic acid

A technology of terephthalic acid and p-toluic acid, which is used in the preparation of carboxylate, the preparation of organic compounds, and the preparation of carboxylic acid by oxidation, to achieve the effect of reducing the number of crystallizers, simplifying the crystallization process, and reducing the size

Inactive Publication Date: 2004-07-14
GRUPO PETROTEMEX DE C V
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

There is a constraint in the study of methods for the separation of refined terephthalic acid from hydrogenated liquid solutions that the final product should have acceptable levels of 4-CBA and p-toluic acid

Method used

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  • Process for production of purified terephthalic acid
  • Process for production of purified terephthalic acid

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0070] This example illustrates the ability to refine crude terephthalic acid having a p-toluic acid concentration of 429 ppmw below the acceptable purity limit (150 ppm) for purified terephthalic acid. It is also illustrated that this requirement can be met by isolating terephthalic acid at temperatures below the boiling point of the solvent.

[0071] The autoclave was charged with water (solvent) and crude terephthalic acid in the amounts listed in Table I, Experiments 1, 2 and 3. These amounts represent an approximate 30% aqueous solution of terephthalic acid. On a solid basis, the content of p-toluic acid in the crude terephthalic acid was 429.37 ppmw. The autoclave charge was heated to 280°C and held at this temperature for one hour to ensure that all solids dissolved. To simulate multiple crystallizers in series, the autoclave feed was cooled to room temperature at a rate of 30 °C per hour. The autoclave charge was then reheated to 60°C and the charge was maintained a...

Embodiment 2

[0075] In this example, which illustrates the effect of separation temperature on the purity of the final product, a portion of the room temperature autoclave feed from Experiments 1, 2 and 3 of Example 1, respectively, was placed into a well mixing vessel. Instead of reheating to 60°C as done in Example 1, in Example 2 the portions were reheated to 95°C and held at this temperature for 1 hour. Solid-liquid separation was performed at 95°C to obtain a solid sample, and the sample was analyzed for p-toluic acid concentration. The results are also listed in Table I. As we can see, the separation at the higher 95°C resulted in a product with a lower p-toluic acid concentration than the material isolated at the lower 60°C. Raising the separation temperature from 60°C while still keeping the solid-liquid separation temperature below the boiling point of the solvent can improve product purity.

Embodiment 3

[0077] The autoclave was charged with water and crude terephthalic acid in the amounts listed in Experiments 4 and 5 of Table II. These samples represent an approximate 20% aqueous solution of crude terephthalic acid. The concentration of p-toluic acid in the crude terephthalic acid was 429.37 ppmw. The sample was heated to 280°C and held at this temperature for one hour to ensure that all solids were dissolved. The sample was cooled to room temperature at a rate of 30°C per hour. Then, following the procedure of Examples 1 and 2, a portion of each sample was heated to 60°C and separated at this temperature, and a portion of each sample was heated to 95°C and separated at this temperature. The p-toluic acid concentrations of the resulting solids are listed in Table II.

[0078] substance

Experiment 4

Experiment 5

Crude terephthalic acid (parts)

25.0104

25.0017

water (parts)

99.9537

100.2292

p-toluic acid ...

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Abstract

Disclosed is a process for the production of terephthalic acid by a plurality of process steps including the catalyst oxidation of a dialkylbenzene compound, a second oxidation, a hydrogenation of the product of the second oxidation, and crystallization of the hydrogenation terephthalic acid using a plurality of series-connected crystallizers.

Description

field of invention [0001] The present invention relates to a novel process for the preparation of refined terephthalic acid by a novel combination of steps starting from the oxidation of dialkylbenzene compounds such as p-xylene. More specifically, the present invention relates to the preparation of refined terephthalic acid by an oxidation process in which a dialkylbenzene compound is first oxidized to terephthalic acid by a two-stage process under certain conditions to obtain a product of increased purity. Terephthalic acid, which is then purified by hydrogenation and recovered by a novel crystallization method. Background of the invention [0002] Aromatic dicarboxylic acids such as terephthalic acid and isophthalic acid are of commercial importance and are widely used in the preparation of various polyester polymers such as fiber-forming polyesters and molding-grade polyesters. Terephthalic acid (TPA) is a basic building block for making linear polyester resins used to ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D9/02C07B61/00C07C51/265C07C51/43C07C51/487C07C63/26
CPCC07C51/265C07C51/43C07C51/487C07C63/26C07C51/16
Inventor R·林R·S·奥梅德拉R·B·舍帕德
Owner GRUPO PETROTEMEX DE C V