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Catalysts for the synthesis of acrolein and acrylic acid

A technology of acrylic acid and acrolein, applied in the field of synthesis of acrolein and acrylic acid, can solve the problems of low catalyst activity and selectivity, and achieve the effect of good technical effect

Active Publication Date: 2020-12-29
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] One of the technical problems to be solved by the present invention is the problem of low catalyst activity and selectivity in the reaction of propylene oxidation to produce acrolein and acrylic acid in the prior art, and a catalyst is provided

Method used

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  • Catalysts for the synthesis of acrolein and acrylic acid
  • Catalysts for the synthesis of acrolein and acrylic acid
  • Catalysts for the synthesis of acrolein and acrylic acid

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0063] Add 200ml of deionized water (100°C) to the ingredient tank equipped with a stirring motor, and mix 200 grams of ammonium molybdate ((NH 4 ) 6 Mo 7 o 24 4H 2 O), 36.6 grams of bismuth nitrate (Bi(NO 3 ) 3 ·5H 2 O), 49.5 grams of cobalt nitrate (Co(NO 3 ) 2 ·6H 2 O), 46.2 grams of iron nitrate (Fe(NO 3 ) 3 9H 2 O), 69.3 grams of nickel nitrate (Ni(NO 3 ) 2 ·6H 2 (0), 0.51 g of potassium hydroxide (KOH) was dissolved and vigorously stirred, and the pH of the solution was adjusted to 5 with ammonia water to obtain an aqueous dispersion. Add 451.6g of macroporous Si-Al oxide carrier to the above water dispersion, and transfer it to a rotary evaporator until the water is evaporated to dryness, transfer it to an oven for overnight drying, and finally calcinate at 500°C for 2 hours to obtain the desired catalyst. The main preparation process and catalyst composition of the catalyst are listed in Table 1, and the investigation results of the catalyst are listed i...

Embodiment 2

[0065] Add 100ml of deionized water (100°C) to the ingredient tank equipped with a stirring motor, and mix 46.2 grams of iron nitrate (Fe(NO 3 ) 3 9H 2 O) and 10.1 g of ammonium molybdate ((NH 4 ) 6 Mo 7 o 24 4H 2 O) (molar ratio Mo:Fe=0.5) was dissolved in water, and the pH of the solution was adjusted to 5 with ammonia water to obtain aqueous solution I. Add 451.6g of macroporous Si-Al oxide carrier to the above aqueous solution, and pour it into a rotary evaporator until the aqueous solution I is completely evaporated to dryness, move it into an oven to dry overnight, and then roast it in a muffle furnace at 500°C for 2 hours to obtain a catalyst precursor.

[0066] Add 200ml of deionized water (100°C) to the ingredient tank equipped with a stirring motor, and mix 189.9 grams of ammonium molybdate ((NH 4 ) 6 Mo 7 o 24 4H 2 O), 36.6 grams of bismuth nitrate (Bi(NO 3 ) 3 ·5H 2 O), 49.5 grams of cobalt nitrate (Co(NO 3 ) 2 ·6H 2 O), 69.3 grams of nickel nitra...

Embodiment 3

[0068] Add 100ml of deionized water (100°C) to the ingredient tank equipped with a stirring motor, and mix 46.2 grams of iron nitrate (Fe(NO 3 ) 3 9H 2 O) and 20.2g of ammonium molybdate ((NH 4 ) 6 Mo 7 o 24 4H 2 O) (molar ratio Mo:Fe=1) was dissolved in water, and the pH of the solution was adjusted to 5 with ammonia water to obtain aqueous solution I. Add 451.6g of macroporous Si-Al oxide carrier to the above aqueous solution, and pour it into a rotary evaporator until the aqueous solution I is completely evaporated to dryness, move it into an oven to dry overnight, and then roast it in a muffle furnace at 500°C for 2 hours to obtain a catalyst precursor.

[0069] Add 200ml of deionized water (100°C) to the ingredient tank equipped with a stirring motor, and mix 179.8 grams of ammonium molybdate ((NH 4 ) 6 Mo 7 o 24 4H 2 O), 36.6 grams of bismuth nitrate (Bi(NO 3 ) 3 ·5H 2 O), 49.5 grams of cobalt nitrate (Co(NO 3 ) 2 ·6H 2 O), 69.3 grams of nickel nitrate ...

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Abstract

The invention relates to a catalyst for synthesizing acrolein and acrylic acid. The technical scheme of the invention is as follows: the catalyst for synthesizing the acrolein and the acrylic acid is prepared from the following components in parts by weight: 35-80 parts of macroporous Si-Al oxide carrier and 20-65 parts of active component supported on the macroporous Si-Al oxide carrier; the active component is expressed as Mo12BiaNicQsYeZfOx by atomicity, wherein Q is selected from at least one of Mg, Co, Ca, Be, Cu, Zn, Pb, Mn and Fe; Y is selected from at least one of K, Rb, Na, Li or Cs; Z is selected from at least one of La, Ce or Sm; a is an atomicity of Bi; c is an atomicity of Ni; s is an atomicity of Q; e is an atomicity of Y; f is an atomicity of Z; x is an total amount of oxygen atoms required for satisfying other element valences.

Description

technical field [0001] The present invention relates to a catalyst for synthesizing acrolein and acrylic acid, a preparation method of the catalyst, an application of the catalyst in synthesizing acrolein and acrylic acid, and a method for synthesizing acrolein and acrylic acid. Background technique [0002] Acrylic acid (CH 2 =CH-COOH) is the simplest unsaturated carboxylic acid, which is an important organic synthesis raw material and synthetic resin monomer. Acrylic acid is mainly used to synthesize advanced water-absorbent resins and water treatment agents, etc., and a part of acrylic acid is used for esterification to manufacture acrylates such as methyl acrylate, ethyl acrylate, n-butyl acrylate and 2-ethylhexyl acrylate, while Acrylate polymers are mainly used in adhesives, coatings, textiles, plastics, leather, paper and other fields. [0003] In recent years, acrylic acid and its series of products have developed rapidly. In 2013, the world's total output of acryl...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/887C07C27/14C07C45/35C07C47/22C07C51/25C07C57/05
CPCB01J23/002B01J23/8876B01J2523/00C07C45/35C07C51/252B01J2523/13B01J2523/31B01J2523/41B01J2523/54B01J2523/68B01J2523/842B01J2523/845B01J2523/847C07C47/22C07C57/04
Inventor 徐文杰汪国军杨斌奚美珍
Owner CHINA PETROLEUM & CHEM CORP