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Heterogeneous catalytic method for synthesis of isophorone from acetone

A heterogeneous catalysis and isophorone technology, applied in clean catalysis and green fields, can solve the problems of complex catalyst preparation process, low selectivity of isophorone, difficult regeneration, etc. Simple, Inexpensive Effects

Active Publication Date: 2010-11-03
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although the acetone gas-solid multiphase condensation method has many advantages, according to the current research results, the developed catalyst has disadvantages such as relatively complicated preparation process, high cost, short life, difficult regeneration and low isophorone selectivity.

Method used

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  • Heterogeneous catalytic method for synthesis of isophorone from acetone
  • Heterogeneous catalytic method for synthesis of isophorone from acetone
  • Heterogeneous catalytic method for synthesis of isophorone from acetone

Examples

Experimental program
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Effect test

Embodiment 1

[0024] Dissolve 23.08 g of magnesium nitrate hexahydrate and 56.27 g of aluminum nitrate nonahydrate in 2000 ml of deionized water, and add ammonia water dropwise at 38°C until the pH is 8.5. Aging at 70°C for 12 hours and standing for cooling for 1 hour. Filter and rinse the filter cake with deionized water until the pH of the filtrate is 7.0. Dry overnight at 80°C, and calcinate at 350°C for 7 hours in an air atmosphere to prepare the catalyst. Catalyst evaluation conditions were: normal pressure, 220°C, acetone feed rate of 0.33ml / mim, after 24 hours of reaction, samples were taken for analysis, the conversion rate of acetone was 20.3%, and the selectivity of isophorone was 86.5%.

Embodiment 2

[0026] Catalyst preparation is the same as embodiment 1. Catalyst evaluation conditions were: normal pressure, 250°C, acetone feed rate of 0.33ml / mim, after 24 hours of reaction, samples were taken for analysis, the conversion rate of acetone was 25.2%, and the selectivity of isophorone was 90.0%.

Embodiment 3

[0028] Catalyst preparation is the same as embodiment 1. Catalyst evaluation conditions were: normal pressure, 290°C, acetone feed rate of 0.33ml / mim, after 24 hours of reaction, samples were taken for analysis, the conversion rate of acetone was 34.5%, and the selectivity of isophorone was 90.2%.

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Abstract

The invention relates to a heterogeneous catalytic method for synthesis of isophorone from acetone. Acetone is used as a raw material, and a magnesium-aluminum composite oxide is used as a catalyst for carrying out catalytic synthesis to obtain isophorone; the magnesium-aluminum composite oxide comprises MgO, Al2O3 and MgAl2O4, the molar ratio of magnesium to aluminum is 0.3-3, the specific surface area is 80-150m<2> / g, and the pore volume is 0.2-0.3cm<3> / g; a fixed bed reactor is used for carrying out synthetic reaction, 20ml of 20 to 40-mesh catalyst is added into a stainless steel reactor of which the inner diameter is 10mm, the reactor is heated to the reaction temperature from the room temperature at the rate of 10 DED C / min after being qualified through an air-tight test, and then, the analytically pure acetone raw material is injected into the reactor by a duplex plunger pump through a preheater; the reaction temperature is 220-290 DEG C; the reaction pressure is normal pressure; and the air speed of the acetone liquid is 0.1-1.0 / h, the selectivity reaches 94.5%, the conversion rate reaches 44.8%, and the stability reaches 1000 hours.

Description

technical field [0001] The invention relates to the technical field of green and clean catalysis, and specifically refers to a heterogeneous catalytic method for synthesizing isophorone from acetone, wherein magnesium-aluminum composite oxide is used as a catalyst, and acetone gas-solid multiphase is carried out under mild reaction conditions Catalyzes condensation reactions. Background technique [0002] As one of the deep-processing products of acetone, isophorone has developed rapidly in developed countries such as the United States, Britain, Germany, and Japan. With the rapid development of the chemical industry, especially the synthetic resin industry, the demand for isophorone is also increasing rapidly. In the late 1980s and early 1990s, many foreign countries built or expanded isophorone production facilities. At present, the production and consumption of isophorone are mainly concentrated in western developed countries and regions. The main manufacturers are Rohm a...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C49/603C07C45/74B01J21/10B01J21/04
Inventor 李凯荣陈宵榕周玮马中义李正赵胤侯立波王宏伟蒋海洋
Owner PETROCHINA CO LTD
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