Lactone production method

A production method and lactone technology, applied in chemical instruments and methods, molecular sieve catalysts, physical/chemical process catalysts, etc., can solve the problems of difficult purification, difficult to solve, high risk, etc., to overcome the complex production process and achieve good conversion. Rate and selectivity effects

Active Publication Date: 2012-05-16
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] At present, the industrialized production of ε-caprolactone mainly adopts the Baeyer-Villiger oxidation process of cyclohexanone and peroxycarboxylic acid, but peroxyacid oxidants also have relatively large disadvantages: (1) after the reaction, a large amount of Organic carboxylic acid (salt) waste has a greater impact on the environment, and it is more difficult to recycle or process; (2) the separation and purification of reaction products are more difficult, the selectivity is low, the atom economy is poor, and it does not meet the basic principles of green chemistry; ( 3) Organic peroxyacids need to use high-concentration hydrogen peroxide in the production process, which is unstable in nature, high in production costs, and dangerous in transportation, storage and operation, thus limiting its application in industrial production
However, metal oxide catalysts have inherent defects in such reactions, such as low catalytic efficiency and small reaction conversion frequency (TON), which are difficult to solve and cannot be industrialized.

Method used

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] Take by weighing 3.45 grams of hollow titanium-silicon molecular sieves (produced by Hunan Jianchang Petrochemical Company, brand HTS, analyzed by X-ray diffraction to be the titanium-silicon molecular sieve of MFI structure, the adsorption isotherm and the desorption isotherm of the low-temperature nitrogen adsorption of this molecular sieve are between There is a hysteresis ring, the grains are hollow grains and the radial length of the cavity part is 15-180 nanometers; the molecular sieve sample is at 25°C, P / P 0 =0.10, the benzene adsorption measured under the condition of adsorption time 1 hour is 78 mg / g, the same below) is installed in the 100ml three-necked flask, then adds magnetic stirrer, 16.83 gram cyclopentanone, 3.6 gram water and 23ml concentration is 30% hydrogen peroxide, and the molar ratio of cyclopentanone and hydrogen peroxide is 1:1 at this moment. The three-necked flask is placed on a temperature-controlled magnetic stirrer, and the upper part of ...

Embodiment 2

[0032] Weigh 4.88 grams of hollow titanium-silicon molecular sieves and put them in a 100ml three-necked flask, then add a magnetic stirrer, 16.83 grams of cyclopentanone, 6.4 grams of methanol and 46ml of 30% hydrogen peroxide. At this time, cyclohexanone and hydrogen peroxide The molar ratio is 1:2. The three-necked flask is placed on a temperature-controlled magnetic stirrer, and the upper part of the three-necked flask is condensed and refluxed with a condenser, and the magnetic stirrer and heating device are started to start the reaction. The reaction temperature was controlled at about 60° C., and after 1 hour of reaction, the conversion rate of cyclopentanone was 15.08%, and the selectivity of forming δ-cyclopentanolactone was 63.64%.

Embodiment 3

[0034] Take 2.65 grams of hollow titanium-silicon molecular sieves and put them in a 100ml three-necked flask, then add a magnetic stirrer, 19.63 grams of cyclohexanone, 7.41 grams of tert-butanol, 6.4 grams of methanol and 23ml of hydrogen peroxide with a concentration of 30%. The molar ratio of hexanone to hydrogen peroxide is 1:1. The three-necked flask is placed on a temperature-controlled magnetic stirrer, and the upper part of the three-necked flask is condensed and refluxed with a condenser, and the magnetic stirrer and heating device are started to start the reaction. The reaction temperature was controlled at about 55°C. After 3 hours of reaction, the conversion rate of cyclohexanone was 38.57%, and the selectivity to ε-caprolactone was 45.69%.

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Abstract

A lactone production method is characterized in that a reaction is performed in the presence of a catalyst with a molar ratio of cyclic ketone, a solvent, and hydrogen peroxide of 1:(0-80):(0.2-20) and a mass ratio of the catalyst and the cyclic ketone of 1:1-100 at a temperature of 5-75 DEG C and a pressure of 0.1-6.0 MPa, and lactone is obtained through recovery; the catalyst comprises a molecular sieve which is a titanium silicon molecular sieve with a MFI crystal structure; the crystal grain has a hollow structure, and the cavity part of the hollow crystal grain has a radial length of 5-300 nanometers; the molecular sieve sample has a benzene adsorption quantity of at least 70 mg / g under a condition with a temperature of 25 DEG C, P / P0 of 0.10, and adsorption time of 1 hour, and as for the low temperature nitrogen adsorption of the molecular sieve, a hysteresis loop exists between an adsorption isotherm and a desorption isotherm. Compared with the prior art, the invention overcomes the disadvantages of complex production process, equipment corrosion, potential safety hazard existence, and severe environment pollution for traditional peroxy acid oxidation methods.

Description

technical field [0001] The present invention relates to a production method of lactone, more specifically to a method for producing lactone, especially ε-caprolactone, through Baeyer-Villiger oxidation of cyclic ketone and hydrogen peroxide. Background technique [0002] ε-caprolactone has the advantages of low viscosity, easy processing, and low VOC content. It is used as oligomer and denaturant in the process, which can improve the toughness, low temperature characteristics and reactivity and other functionalities; in terms of coatings, it is used as an improvement in solvents and latex coatings for automotive primers, surface coatings and various building materials. It can improve the toughness of the coating film, improve the low-temperature characteristics, reactivity, and increase the crosslinking density; in terms of adhesives, it can be used to improve the bonding properties of hot-melt adhesives and solvent-based adhesives; in resin modification On the one hand, it...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07D313/04C07D309/30C07D313/10B01J29/89
Inventor 林民夏长久朱斌史春风龙立华舒兴田邹飞艳汝迎春
Owner CHINA PETROLEUM & CHEM CORP
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