Unlock instant, AI-driven research and patent intelligence for your innovation.

Method for preparing terephthalyl alcohol by hydrogenation of terephthalic acid

A technology of terephthalic acid and terephthalic acid, applied in chemical instruments and methods, preparation of organic compounds, metal/metal oxide/metal hydroxide catalysts, etc., can solve problems such as difficulty in hydrogenation reaction, and achieve Low cost of raw materials, favorable for large-scale industrial production, and high selectivity

Active Publication Date: 2010-01-27
SINOPEC SHANGHAI PETROCHEMICAL CO LTD
View PDF3 Cites 4 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] The invention provides a method for preparing terephthalic acid by hydrogenation of terephthalic acid. It uses a highly efficient hydrogenation catalyst to directly hydrogenate terephthalic acid to prepare terephthalic acid, which solves the problem of The technical problem of difficulty in the hydrogenation reaction of the carboxyl group of terephthalic acid

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Method for preparing terephthalyl alcohol by hydrogenation of terephthalic acid

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0016] 2.59gRuCl 3 ·3H 2 O was dissolved in 14 ml of deionized water, then 1.34 g of SnCl was added 2 2H 2 O dissolved, then add 20g carrier Al 2 o 3 Stir evenly to obtain a dark green paste, which is aged for 15 hours. Take 11.65g NaBH 4 Dissolve in 10ml of deionized water, add this solution dropwise to the above paste, let it stand for 30 minutes, filter and wash with deionized water three times, and dry at 70-90°C for 6 hours. After grinding, take particles with a particle size of 80-250 mesh as the catalyst precursor, heat and reduce with hydrogen for 2 hours, and the hydrogen flow rate is 150ml / min, and the finished catalyst for hydrogenation reaction is obtained.

Embodiment 2~8

[0018] Change the consumption of carrier and starting material in each catalyst, all the other are the same as embodiment 1.

[0019] The composition and content of the catalyst active components prepared in each embodiment are shown in Table 1.

[0020] Table 1

[0021]

[0022] 2. Hydrogenation reaction:

Embodiment 9

[0024] Adopt the catalyst that above-mentioned embodiment obtains to carry out the reaction that terephthalic acid hydrogenation prepares terephthalic acid dimethanol:

[0025] Add 15g of terephthalic acid and 150ml of water (solvent) into a 300ml autoclave at the same time, and add the required amount of catalyst in proportion. Close the reaction kettle, pump out the air in the kettle, replace it with hydrogen, stir and heat to the reaction temperature under 2.0MPa hydrogen pressure, then inject hydrogen to the reaction pressure, start the reaction timing, and maintain the required hydrogen pressure until the end of the reaction. After cooling, the catalyst was filtered off, and the product p-phenylenedimethanol in the reaction solution was analyzed by gas chromatography, and its concentration was calculated by the internal standard method.

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

PropertyMeasurementUnit
particle sizeaaaaaaaaaa
Login to View More

Abstract

The invention discloses a terephthalyl alcohol preparing method by hydrotreating terephthalic acid, which proceeds with the hydrogenation reaction in the accelerant and hydrogen gas condition. The reaction is made in the solvent water, wherein the proportion by weight of terephthalic acid and water is 1: (5-20), the reaction temperature is 180-300Deg. C, the hydrogen pressure is 5.0-10.0MPa, the reaction time is 3-8 hours, the accelerant regards AL2O3 as the carrier, and the load active component is Ru, Sn and B, the mole ratio of Ru and Sn is 1:(0.5-2.0), the total content of the active component Ru and Sn in the accelerant is 5-12wt%, the content of B is 5-20wt%, the grain size of the accelerant is 80-250 mesh size, the usage of the accelerant in the reaction system is 1-5wt%. The invention is provided with the low material cost, which is fit for the mass industry production.

Description

technical field [0001] The invention relates to a method for preparing terephthalmic alcohol by catalytic hydrogenation of terephthalic acid as a raw material. The catalyst used in the method is a supported catalyst with metal Ru, Sn and B as active components. Background technique [0002] Terephthalic alcohol is an important organic polymer intermediate. Because there are two active hydroxyl groups in its structure, it can react with compounds with α-active hydrogen such as hydroxyl, aldehyde, and carboxyl to form a variety of polymers. They are The main raw material for the production of plasticizers, synthetic fibers, synthetic resins and adhesives. At present, p-xylene is mainly produced from p-xylene, which is hydrolyzed after chlorination. For example, the technology disclosed in US Pat. No. 3,546,301 uses tetrahydrofuran as a solvent and anhydrous sodium carbonate as a catalyst to hydrolyze p-dichloromethylbenzene, and the yield of p-xylylenedimethanol is 73%. The ...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Patents(China)
IPC IPC(8): C07C39/08C07C37/00B01J23/62B01J21/02B01J21/04
Inventor 朱志庆吕自红郭世卓谢家明宋义伟
Owner SINOPEC SHANGHAI PETROCHEMICAL CO LTD