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Nickel-based catalysts for synthesizing methyl isobutyl ketone and by-producing isopropanol

A methyl isobutyl ketone, nickel-based catalyst technology, applied in heterogeneous catalyst chemical elements, physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, etc., can solve problems such as single product , to achieve the effect of simple preparation process, increased anti-loss ability and low cost

Active Publication Date: 2018-04-20
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] Throughout the literature and reports, the current industrialized catalyst is still Pd / resin catalyst, and the life-span of the catalyst is 9-12 months, and the product produced by this catalyst has only methyl isobutyl ketone, and the product is single
Other catalysts have not been reported on industrialization

Method used

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  • Nickel-based catalysts for synthesizing methyl isobutyl ketone and by-producing isopropanol

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0035] In a beaker, 148.6 grams of nickel nitrate, 204.7 grams of zinc nitrate, 13.9 grams of cerium nitrate and 3.4 grams of boric acid were dissolved in 860 grams of water to make aqueous solution I. Under stirring and at 70°C, titrate to the reaction solution with 30wt% sodium carbonate aqueous solution The pH value is 7.0. Then add 295 grams of pseudo-boehmite powder. Pseudoboehmite is produced by Jiangsu Sanji Industrial Co., Ltd., with a specific surface area of ​​306m 2 / g, the pore volume is 1.08mL / g.

[0036] Then aged at 75° C. for 3 hours, then suction filtered and washed until the sodium ion content was lower than 0.05%. The wet filter cake was dried, granulated, and then roasted and decomposed at 420°C. Finally, it is sliced ​​into granules, and the particle size is

[0037] Then, the catalyst was reduced with hydrogen in a temperature-programmed manner, and the highest reduction temperature was 480°C. Constant temperature reduction at 480°C for 2 hours. A...

Embodiment 2

[0042] In a beaker, 89.1 grams of nickel nitrate, 136.5 grams of zinc nitrate, 32.5 grams of cerium nitrate and 1.7 grams of boric acid were dissolved in 600 grams of water to make aqueous solution I. Under stirring and at 75°C, titrate to the reaction solution with 30wt% sodium carbonate aqueous solution The pH value is 7.5. Then add 330 grams of pseudo-boehmite powder. Pseudoboehmite is produced by Jiangsu Sanji Industrial Co., Ltd., with a specific surface area of ​​290m 2 / g, the pore volume is 0.99mL / g.

[0043] Then aged at 75° C. for 3 hours, then suction filtered and washed until the sodium ion content was lower than 0.05%. The wet filter cake is dried, granulated, and then roasted and decomposed at 380°C. Finally, it is sliced ​​into granules, and the particle size is

[0044] Then, the catalyst was reduced with hydrogen in a temperature-programmed manner, and the highest reduction temperature was 450°C. Constant temperature reduction at 450°C for 2 hours. Aft...

Embodiment 3

[0047] In a beaker, 178.3 grams of nickel nitrate, 109.2 grams of zinc nitrate, 8.4 grams of cerium nitrate and 34.3 grams of boric acid were dissolved in 770 grams of water to make aqueous solution I, which was titrated to the reaction solution with stirring and at 75°C. The pH value is 7.2. Then add 302 grams of pseudo-boehmite powder. Pseudoboehmite is produced by Jiangsu Sanji Industrial Co., Ltd., with a specific surface area of ​​275m 2 / g, the pore volume is 1.12mL / g.

[0048] Then aged at 75° C. for 3 hours, then suction filtered and washed until the sodium ion content was lower than 0.05%. The wet filter cake is dried, granulated, and then roasted and decomposed at 360°C. Finally, it is sliced ​​into granules, and the particle size is

[0049] Then, the catalyst was reduced with hydrogen in a temperature-programmed manner, and the highest reduction temperature was 450°C. Constant temperature reduction at 450°C for 4 hours. After cooling down, the catalyst of t...

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Abstract

The invention relates to a catalyst, and belongs to the technical field of applications and development of acetone downstream products, wherein nickel and zinc are used as main active components, boron and cerium are used as auxiliary components, aluminum oxide, silicon oxide or an aluminum oxide-silicon oxide composite carrier with rich pH value is selected to promote a reaction, the catalyst isused under a mild reaction condition, an acetone one-step production process is used, the yield of methyl isobutyl ketone in the application of the catalyst of the present invention is higher than theyield of methyl isobutyl ketone in the application of the palladium / resin catalyst used in the current industrial apparatus, and isopropanol is by-produced. According to the present invention, the obtained catalyst has the ideal stability, has the cost significantly lower than the cost of the existing palladium catalyst, and has good economic benefits.

Description

technical field [0001] The invention relates to a catalyst for ketone condensation, more specifically, relates to a catalyst for synthesizing methyl isobutyl ketone and co-producing isopropanol by using acetone as a raw material through a one-step method. Background technique [0002] Methyl isobutyl ketone (MIBK for short) is an important solvent and chemical intermediate. It has attracted much attention because of its excellent performance. It has an aromatic ketone smell, is colorless and transparent, and has a medium boiling point. It has a very strong solvency. It can be miscible with many organic solvents such as alcohol, benzene, ether, etc., and can be used as paint, ethyl cellulose, nitrocellulose, audio and video tapes, paraffin, various natural or synthetic resin solvents, dewaxing agents, rare earth metal extraction agents, polymerization The raw materials of reaction initiators, surfactants, medicines, pesticide extractants and rubber anti-aging agents are current...

Claims

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Application Information

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IPC IPC(8): B01J23/83C07C29/145C07C31/10C07C45/73C07C49/04
CPCB01J23/002B01J23/83B01J2523/00C07C29/145C07C45/73B01J2523/27B01J2523/305B01J2523/3712C07C31/10C07C49/04
Inventor 杨溢唐国旗田保亮李宝芹
Owner CHINA PETROLEUM & CHEM CORP