Preparation method of 1, 4-cyclohexanedicarboxylic acid

A technology of cyclohexanedicarboxylic acid and terephthalic acid, which is applied in chemical instruments and methods, preparation of carboxylic acids by ozone oxidation, catalysts for physical/chemical processes, etc., can solve problems such as poor activity and selectivity, and achieve long service life, High hydrogenation activity and cost reduction effect

Active Publication Date: 2022-04-29
浙江清和新材料科技有限公司
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  • Abstract
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  • Claims
  • Application Information

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Problems solved by technology

Other patents have also proposed to adopt relatively low-priced Ru as an active component, and Ru / C of activated carbon carrier is used for this reaction, such as U.S. Patent US3027398 and US4654064 reported this reaction; However, the activity of Ru / C catalyst for this reaction and poor selectivity

Method used

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  • Preparation method of 1, 4-cyclohexanedicarboxylic acid
  • Preparation method of 1, 4-cyclohexanedicarboxylic acid

Examples

Experimental program
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Embodiment A1

[0025] Example A1: The columnar activated carbon carrier was pretreated with a nitric acid solution, the nitric acid concentration was 5.0 wt%, the mass ratio of the activated carbon carrier to the nitric acid solution was 1:5, the treatment temperature was 90°C, and the treatment time was 3h. After nitric acid pretreatment, the activated carbon carrier was washed with purified water until the filtrate was neutral, and dried at 110 °C for 4 h.

[0026] The catalyst was prepared by an equal volume impregnation method. Palladium chloride and ruthenium chloride solutions (dissolved in hydrochloric acid) were prepared according to the theoretical loading, and the activated carbon carrier treated with the above nitric acid was added, impregnated for 24 hours, and dried at 110 °C for 4 hours. Using hydrogen reduction, the reduction temperature is 300 ℃. The theoretical loading of metal Pd is 0.35 wt %, and the theoretical loading of metal Ru is 0.15 wt %.

[0027] In Examples A2 to...

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Abstract

The present invention provides a 1, 4-cyclohexanedicarboxylic acid preparation method, which comprises that terephthalic acid is subjected to a hydrogenation reaction in the presence of a catalyst to prepare 1, 4-cyclohexanedicarboxylic acid, and the mass fraction of the active component Pd in the catalyst is 0.25-1.0 wt%; the mass fraction of the auxiliary agent Ru is 0.05-0.30 wt%, the loading capacity of the metal Pd is greater than that of the Ru, and both the Pd and the Ru are loaded on the carrier columnar activated carbon; the reaction comprises the following steps: dissolving the raw material terephthalic acid by using water, dissolving the raw material terephthalic acid by using the product 1, 4-cyclohexanedicarboxylic acid, and carrying out continuous hydrogenation reaction in a fixed bed reactor. According to the method, the conversion rate of the raw material terephthalic acid and the selectivity of the target product 1, 4-cyclohexanedicarboxylic acid can stably reach 99.5% or above, the service life of the catalyst is long, and the catalyst does not have an obvious inactivation phenomenon after one-way operation for 3000 h or above; therefore, the method has a good industrial application prospect.

Description

technical field [0001] The invention belongs to the field of fine chemicals, and in particular relates to a method for preparing 1,4-cyclohexanedicarboxylic acid by continuous hydrogenation of terephthalic acid. Background technique [0002] 1,4-Cyclohexanedicarboxylic acid (CHDA for short) brings many unique properties to polyester resins and glass fiber reinforced plastics for high performance coatings, products used in automotive, transportation, industrial maintenance, aerospace, buildings , equipment and general metal and gel coat coatings and other aspects. In addition, in medicine, CHDA can also be used to synthesize peptic ulcer medicine. CHDA is prepared by hydrogenation of terephthalic acid (PTA). US patent US 6291706 uses Pd / C catalyst, which is installed in the autoclave hanging basket, and the PTA concentration is 5% under continuous stirring at 200 ° C and 4.5 MPa. 45 minutes of the aqueous solution, and then contacted and reacted with the catalyst for 3 hour...

Claims

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Application Information

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IPC IPC(8): C07C51/36C07C61/09B01J23/46
CPCC07C51/36B01J23/462C07C2601/14C07C61/09Y02P20/52
Inventor 徐铁勇杨荣强李显明洪俊杰林桂海
Owner 浙江清和新材料科技有限公司
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