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Propylene oxidation catalyst and preparation method

A technology of propylene oxidation and catalyst, which is applied in the preparation of carbon-based compounds, chemical instruments and methods, and the preparation of organic compounds, etc. It can solve the problems of reduced reaction efficiency, loss of active components, and large cost expenditures.

Active Publication Date: 2015-10-28
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

There are more than 50,000 reaction tubes, and it is difficult to ensure that the catalyst is not filled empty. If the catalyst is sintered quickly because the hot spot is too high, and the catalyst is replaced in a short period of time, it can be expected that the economic loss will be huge; in addition, for propylene The production of aldehyde and acrylic acid should be carried out under low temperature conditions as much as possible, because the reaction needs to be heated in a salt bath, and the energy consumption for maintaining production is also a huge expense; due to the generation of hot spots, high temperature resistance is required for the reaction tube, and for tens of thousands For the reaction tube, the cost of the tube is a very large cost
CN1672790A provides a kind of catalyst that catalyzes the gas-phase oxidation of acrolein to produce acrylic acid. The catalyst contains molybdenum and vanadium, and also contains at least one volatile catalyst poisoning component. Reduce the temperature of the superheated part, and suppress the reduction of the reaction efficiency of thermal degradation
The scouring of the mixed flow of propylene, air and water vapor will also cause the loss of some active components in the catalyst

Method used

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  • Propylene oxidation catalyst and preparation method
  • Propylene oxidation catalyst and preparation method
  • Propylene oxidation catalyst and preparation method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0035] Preparation of Catalyst 1

[0036] Step 1: Prepare catalyst inner layer matrix

[0037] (1) Preparation of active ingredient slurry (a)

[0038] Under stirring conditions, take 197 grams of ammonium molybdate and dissolve in 1000 ml of pure water (water temperature above 65°C) to obtain slurry (1), then take 73 grams of cobalt nitrate, 1.88 grams of potassium nitrate, 112.7 grams of iron nitrate, and 15.1 grams of lanthanum nitrate Dissolve in 500ml of purified water (water temperature above 65°C), stir and mix well to obtain slurry (2). Another 45.1 g of bismuth nitrate was taken and dissolved in dilute nitric acid with stirring to obtain a slurry (3). Then, the slurry (1) is mixed with the slurry (2) to obtain the slurry (4), and then the slurry (3) is added to the slurry (4) to obtain the active ingredient slurry (a).

[0039] (2) Preparation of catalyst inner layer matrix

[0040] Add 61.4 grams of silica powder and 2.5 grams of alumina to the active component s...

Embodiment 2

[0053] Preparation of Catalyst 2

[0054] Same as the preparation steps and main raw materials of catalyst 1 in Example 1, 35.7 grams of silicon dioxide were added to the inner layer, extruded by an extruder, rolled and granulated into a spherical shape with a diameter of 2 mm, and 6.7 grams of silicon dioxide was added to the outer layer and 3.1 grams of silicon carbide. The thickness of the coating is 0.5-2.0 mm, and the catalyst 2 is obtained by roasting at 550° C. for 3 hours. The main composition of catalyst 2 inner layer matrix is: Mo 12 Bi 5 Fe 5 co 6 W 3 K 2 Si 6.4 B 0.5 o x , the main composition of the outer layer is: Mo 12 Bi 5 Fe 5 co 6 W 3 K 2 Si 1.2 B 0.5 o x . The element content of the outer layer is 0.2% to 4.6% higher than that of the inner layer.

Embodiment 3

[0060] Same as the preparation steps and main raw materials of the catalyst 1 in Example 1, 57.5 grams of silicon dioxide and 2.3 grams of silicon carbide were added to the inner layer, which were extruded into hollow columnar particles of φ 5 × 5 mm through an extruder, and 28.5 grams of SiO2 were added to the outer layer. silicon oxide. The thickness of the coating is 0.1-1.5 mm, and the catalyst 3 is obtained by calcining at 400° C. for 6 hours. The main composition of the catalyst 3 inner layer matrix is: Mo 12 Bi 7 Fe 1 co 8 W 0.3 K 3.2 Si 10.3 mn 1.8 o x , the main composition of the outer layer is:

[0061] Mo 12 Bi 7 Fe 1 co 8 W 0.3 K 3.2 Si 5.1 mn 1.8 o x

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Abstract

The invention relates to a multi-metal oxide catalyst. The multi-metal oxide catalyst has a general formula of MoaBibFecCodWeKfSigAhBiOx (I). In the general formula of MoaBibFecCodWeKfSigAhBiOx (I), silicon is used as a carrier in the catalyst, A represents at least one of titanium, manganese, boron and lanthanum, B represents at least one of alkaline-earth metals, and O represents oxygen. The multi-metal oxide catalyst is used for propylene selective-oxidation reaction and has the characteristics of high reaction activity, high selectivity and long service life.

Description

technical field [0001] The invention relates to a multi-metal oxide catalyst for the selective oxidation of propylene to produce acrolein and a preparation method thereof. Background technique [0002] The gas-phase catalytic oxidation reaction of propylene to prepare acrolein and acrylic acid is a strong exothermic reaction, and a large amount of reaction heat is accumulated in the reactor instantaneously, forming local hot spots. If the reaction heat cannot be removed in time and effectively, the instantaneously accumulated heat will continue to accumulate, which will lead to catalyst The loss and detachment of active components lead to a decrease in catalyst activity and shortened life, and lead to the formation of by-products due to excessive oxidation reactions, thereby reducing the yield of acrolein and acrylic acid. It even causes a runaway reaction and sinters the catalyst. [0003] "Research Progress on Oxidative Synthesis of Acrylic Acid Process and Catalyst" (Pet...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/888C07C47/22C07C45/35
Inventor 王学丽龚光碧李琰李慧文郭珺李洁史蓉巩红光高阳光常晓昕颉伟张慧杨珊珊高杜娟
Owner PETROCHINA CO LTD