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Catalyst, preparation method thereof, and application of catalyst in preparation of beta-isophorone

A technology of isophorone and catalyst, which is applied in the field of isophorone preparation technology, can solve the problems of equipment corrosion by strong alkaline catalyst, low purity of β-isophorone, poor dispersibility of β-cyclodextrin, etc. Achieve the effect of improving reaction selectivity, using less catalyst, and increasing base value

Active Publication Date: 2020-06-02
WANHUA CHEM GRP CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] In view of the complex operation of the above-mentioned isomerization reaction, a large amount of research has been carried out on the catalyst in the prior art, in order to expect to improve the reaction yield:
[0005] U.S. Patent No. 4010205A uses triethanolamine as a catalyst for reactive distillation, and the reaction solution is washed with tartaric acid and brine to obtain β-isophorone; the disadvantage of this technical solution is that the purity of the obtained β-isophorone is relatively low and the The processing process is complex;
[0006] U.S. patents US5907065A and US6005147A use Co 3 o 4 , CaO, Fe 3 o 4 The oxide is used as a catalyst, and the isomerization reaction is carried out by vacuum distillation, and the purity of the obtained β-isophorone can reach more than 97%, but there are many by-products in the reaction and the space-time yield is low;
[0007] Chinese patents CN1288882 and CN1292374 use alkaline hydroxide (KOH, NaOH, etc.) as a catalyst to produce β-isophorone through isomerization reaction, although this technical scheme can obtain β-isophorone with higher purity , but the strong alkaline catalyst will seriously corrode the equipment;
However, the Schiff base-modified esterified β-cyclodextrin has poor dispersibility and exists in flocculent form in the reaction system, which affects the catalytic efficiency of the reaction. In addition, the preparation of the catalyst by this method is cumbersome, which brings difficulties for large-scale industrial application.

Method used

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  • Catalyst, preparation method thereof, and application of catalyst in preparation of beta-isophorone
  • Catalyst, preparation method thereof, and application of catalyst in preparation of beta-isophorone
  • Catalyst, preparation method thereof, and application of catalyst in preparation of beta-isophorone

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0044] Preparation of N-(2-hydroxyethyl)diethylenetriamine-benzaldehyde Schiff base

[0045]

[0046] Add 10.3g (0.1mol) diethylenetriamine, 21.2g (0.2mol) benzaldehyde, and 500g ethanol to a 1L reaction flask in sequence, stir at 50°C for 6h, add 4.4g (0.1mol) ethylene oxide, and Stirring was continued for 2 hours, the reaction solution was directly filtered, and dried in a vacuum oven (60°C, 2KPa) to obtain 35.4g of N-(2-hydroxyethyl)diethylenetriamine-benzaldehyde Schiff base catalyst, which was designated as Catalyst A.

[0047] Product HPLC purity is 99.5%, melting point is 167.9-168.6 ℃,

[0048] HNMR (DMSO, 400M): = 8.78 (S, 2H, ArH), 7.85 (d, 4H, ArH), 7.61 (dd, 2H, ArH), 7.50 (m, 4H, ArH), 3.80 (S, 1H, -OH), 3.56-3.66 (m, 6H), 2.2-2.5 (m, 6H).

[0049] Add α-isophorone containing 0.005wt% catalyst A to the tower still of a plate tower reactor with 20 plates, and carry out refining under the conditions of 180°C, absolute pressure 0.05MPa, and reflux ratio of 30:1. ...

Embodiment 2

[0052] Preparation of N-(2-hydroxyethyl)diethylenetriamine-o-hydroxybenzaldehyde Schiff base

[0053]

[0054] Add 10.3g (0.1mol) diethylenetriamine, 30.5g (0.25mol) o-hydroxybenzaldehyde, 500g ethanol to a 1L reaction flask in sequence, stir at 70°C for 5h, add 3.96g (0.09mol) ethylene oxide, 20 Stirring was continued for 10 h at °C, the reaction solution was directly filtered, and dried in a vacuum oven (60 °C, 2KPa) to obtain 37.4 g of catalyst, which was designated as Catalyst B.

[0055] Product HPLC purity is 99.5%, melting point is 147.1-148.2 ℃,

[0056] HNMR (DMSO, 400M): = 8.68 (S, 2H, ArH), 7.21-7.65 (m, 8H, ArH), 5.81 (s, 2H, Ar-OH), 3.76 (S, 1H, -OH), 3.52 -3.61 (m, 6H), 2.21-2.50 (m, 6H).

[0057] Add α-isophorone containing 0.01wt% catalyst B to the tower still of a plate tower reactor with 25 plates, and carry out refining under the conditions of 230°C, absolute pressure 0.1MPa, and reflux ratio of 30:1. Distillation reaction, isomerization reaction occur...

Embodiment 3

[0059] Preparation of N-(2-hydroxyethyl)diethylenetriamine-furfuraldehyde Schiff base

[0060]

[0061] Add 10.3g (0.1mol) diethylenetriamine, 15.4g (0.16mol) furfuraldehyde, 500g ethanol to a 1L reaction flask in sequence, stir at 20°C for 10h, add 4.8g (0.11mol) ethylene oxide, and Continue to stir for 0.5h, filter the reaction solution directly, and dry it in a vacuum oven (60°C, 2KPa) to obtain 30.2g of N-(2-hydroxyethyl)diethylenetriamine-furanformaldehyde Schiff base catalyst, denoted as Catalyst C .

[0062] Product HPLC purity is 99.8%, melting point is 133.6-134.2 ℃,

[0063] HNMR (DMSO, 400M): = 7.68 (d, 2H, ArH), 7.38 (d, 2H, CH), 6.51-6.68 (m, 4H, ArH), 3.56 (S, 1H, -OH), 3.42-3.51 (m, 8H), 1.6-1.69 (m, 4H).

[0064] Add α-isophorone containing 1wt% catalyst A to the still of a plate tower reactor with 30 plates, and carry out rectification at 280°C, absolute pressure 0.2MPa, and reflux ratio of 3:1 reaction, an isomerization reaction occurs.

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Abstract

The invention provides an N-(2-hydroxyethyl)diethylenetriamine Schiff base catalyst, a preparation method thereof, and an application of the catalyst in the preparation of beta-isophorone. The preparation method of the catalyst comprises the following steps: 1) reacting diethylenetriamine with aromatic aldehyde to prepare a bis-Schiff base; and 2) reacting the bis-Schiff base compound with ethylene oxide to obtain the N-(2-hydroxyethyl)diethylenetriamine Schiff base. The invention also provides a method for preparing beta-isophorone from alpha-isophorone through an isomerization reaction underthe action of the Schiff base. The catalyst is simple to prepare and easy to industrialize. The prepared N-(2-hydroxyethyl)diethylenetriamine Schiff base has the advantages of high selectivity and high yield for the reaction of isomerizing alpha-isophorone to generate beta-isophorone, low generation possibility of byproducts, easiness in industrial production, and no corrosion to equipment.

Description

technical field [0001] The present invention relates to a kind of preparation process of isophorone, relate in particular to a kind of N-(2-hydroxyethyl)diethylenetriamine Schiff base catalyst, the preparation method of the catalyst and its use in the preparation of β-isophorone The application of the invention belongs to the technical field of preparation of isophorone and catalyst. Background technique [0002] β-isophorone (3,5,5-trimethylcyclohex-3-en-1-one, β-IP) is an important intermediate for the synthesis of vitamin E, carotenoids, astaxanthin and various spices body, and is the main raw material for the synthesis of tea aroma ketone (2,6,6-trimethyl-2-cyclohexene-1,4-dione, KIP). [0003] The conventional preparation method of β-isophorone is to use α-isophorone (3,5,5-trimethylcyclohex-2-en-1-one) as a raw material, through isomerization under the action of a catalyst The chemical reaction is obtained. α-isophorone and β-isophorone are a pair of isomers, and th...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J31/02C07C49/603C07C45/67C07C249/02C07C251/24
CPCB01J31/0241C07C45/67C07C249/02C07C49/603C07C251/24Y02P20/10
Inventor 刘英瑞宋明焱张涛吕英东郭劲资李莉宋军伟孙媛媛刘阳王子豪张弈宇黎源
Owner WANHUA CHEM GRP CO LTD
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