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A kind of catalyst for producing isobutanol by hydrogenation of methacrolein and preparation method thereof

A technology for producing methacrolein and isobutanol, which is applied in catalyst activation/preparation, hydroxyl compound preparation, chemical instruments and methods, etc., can solve problems such as low conversion rate and poor selectivity, and achieve extended life and simplified product separation. , to avoid the effect of side effects

Active Publication Date: 2021-08-06
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] The technical problem to be solved by the present invention is that the selectivity of the aldehyde hydrogenation catalyst to isobutanol is poor in the prior art, and the conversion rate is low, and the preparation method of the catalyst for the hydrogenation of methacrolein to produce isobutanol is provided

Method used

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  • A kind of catalyst for producing isobutanol by hydrogenation of methacrolein and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

example 1

[0019] Take 500mL of 1M copper nitrate solution and 747mL of 1M zirconium nitrate solution and mix them. Co-precipitate the mixed solution and NaOH solution in a sedimentation tank with stirring, control the precipitation temperature to about 80°C, and neutralize for 30 minutes. at 9. Then stir and age at 80°C for 30 minutes, weigh 260g of JN-30 silica sol and add it to the above slurry, stir at 80°C for 50 minutes, wash, filter, dry, and add modification additive Ce 2 o 3 2g, granulated, roasted at 350°C for 3 hours, added 6ml of water and 6g of graphite, and finally compressed into ¢3×3mm cylindrical tablets to obtain the usable catalyst (S1).

[0020] The catalyst has a copper oxide content of 20%, a zirconia content of 40%, a silicon dioxide content of 39%, and a modification additive content of 1%.

example 2

[0022] Take 562mL of 1M copper nitrate solution and 598mL of 1M zirconium nitrate solution and mix them. Co-precipitate the mixed solution and sodium bicarbonate solution in a sedimentation tank with stirring, control the precipitation temperature to about 80°C, and neutralize for 50 minutes. The value is controlled at 9.5. Then stir and age at 80°C for 40 minutes, weigh 296g of JN-30 silica sol and add it to the above slurry, stir at 80°C for 50 minutes, wash, filter, dry, and add modification additive Ce 2 o 3 1.6g, granulated, calcined at 380°C for 3 hours, added 6ml of water and 6g of graphite, and finally pressed into tablets into ¢3×3mm to obtain the usable catalyst (S2).

[0023] The catalyst has a copper oxide content of 23%, a zirconia content of 32%, a silicon dioxide content of 45%, and a modification additive content of 0.8%.

example 3

[0025] Take 625mL of 1M copper nitrate solution and 654mL of 1M zirconium nitrate solution and mix them. Co-precipitate the mixed solution and NaOH solution in a precipitation tank with stirring, control the precipitation temperature at about 85°C, and neutralize for 30 minutes. at 9. Then stir and age at 80°C for 40 minutes, weigh 260g of JN-30 silica sol and add it to the above slurry, stir at 90°C for 50 minutes, wash, filter, dry, and add modification additive La 2 o 3 1g, granulated, calcined at 370°C for 3 hours, added 6ml of water and 6g of graphite, and finally pressed into tablets into ¢3×3mm to obtain a usable catalyst (S3).

[0026] The catalyst has a copper oxide content of 25%, a zirconia content of 35%, a silicon dioxide content of 39%, and a modification additive content of 0.5%.

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Abstract

The invention belongs to the technical field of catalyst production and provides a catalyst preparation method for preparing isobutanol from methacrolein hydrogenation. The preparation of the catalyst adopts the method of co-precipitation. The specific preparation method is to mix copper nitrate solution and zirconium nitrate solution and add a certain amount of precipitant to precipitate and age, and then add silica sol to combine with the precipitate to form a stable and uniform slurry; washing, filtering , drying, adding modification additives, roasting, and finally tableting. The catalyst has the characteristics of high activity and high selectivity.

Description

technical field [0001] The invention belongs to the field of catalyst manufacture, and in particular relates to a catalyst preparation method for preparing isobutanol from methacrolein hydrogenation. Background technique [0002] Isobutanol is an important basic chemical raw material, which can be used to manufacture petroleum additives, antioxidants, plasticizers, synthetic rubber, artificial musk, fruit essential oils and synthetic drugs; its ester derivatives can be used as Used as a solvent, it can also be used to synthesize lubricants and hydraulic oils. [0003] At present, isobutanol mainly comes from the hydrogenation of isobutyraldehyde by-product of propylene carbonylation to butanol / octanol plant. However, with the development of propylene carbonylation to the low-pressure method (rhodium catalyst method), the normal isomerization ratio in the crude carbonylation liquid rises to more than 10:1, leading to an increasing source of isobutyraldehyde, the raw material...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/83C07C29/141C07C31/12
CPCB01J23/83B01J37/03B01J2523/00C07C29/141B01J2523/17B01J2523/3712B01J2523/41B01J2523/48B01J2523/3706C07C31/12
Inventor 孙远龙袁浩然孙中华吴结华张皓张觅
Owner CHINA PETROLEUM & CHEM CORP