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Fluid bed catalyst in use for oxidizing reaction of olefin ammonia

A technology of fluidized bed catalyst and oxidation reaction, which is applied in the direction of metal/metal oxide/metal hydroxide catalyst, preparation of hydrocarbon ammoxidation, physical/chemical process catalyst, etc. Reduce and reduce active sites and other problems, and achieve the effects of improved wear resistance, long service life and excellent catalytic performance

Inactive Publication Date: 2005-03-30
CHINA PETROLEUM & CHEM CORP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, for supported catalysts, although the carrier itself has no catalytic activity, the physical properties of the carrier have a great influence on the catalytic performance of the catalyst. Especially for supported fluidized bed catalysts, the wear resistance of the carrier directly affects the catalytic performance of the catalyst. service life
In the prior art, it is proposed that adding sodium to the catalyst can improve the wear resistance of the catalyst, but it is generally believed that the introduction of sodium will cause the catalyst to be poisoned in the later stage of use, resulting in a rapid decrease in the late activity of the catalyst
Another conventional method is to improve the wear resistance of the catalyst by increasing the content of the carrier in the catalyst. However, this method is generally considered to be a negative method, because the increase of the carrier content means that the content of the active component of the catalyst is reduced. Reduction, that is, the reduction of the active site of the unit catalyst, which must reduce the olefin load of the catalyst, which means a reduction in the production capacity of the reactor in production

Method used

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  • Fluid bed catalyst in use for oxidizing reaction of olefin ammonia
  • Fluid bed catalyst in use for oxidizing reaction of olefin ammonia
  • Fluid bed catalyst in use for oxidizing reaction of olefin ammonia

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0037] 425.4 g (NH 4 ) 6 Mo 7 o 24 4H 2 O was added to 325 grams of warm water at 70°C, stirred to make it all dissolve, and then 11.6 grams of solid silicon dioxide was added with a particle size of 5 to 20 nanometers. After the slurry was uniform, 1401 grams of 40 wt% silicon dioxide was added. Silica sol, make material A.

[0038] 178.3 g Fe(NO 3 ) 3 9H 2 O was added to 170 g of 70°C hot water, stirred and dissolved, and then 129.0 g of Bi(NO 3 ) 3 ·5H 2 O, 62.4 g Ce(NO 3 ) 3 ·nH 2 O, 105.7 g Mg(NO 3 ) 3 ·6H 2 O, 312.8 g Ni(NO 3 ) 3 ·6H 2 O and 18.1 g Co(NO 3 ) 3 ·6H 2 O is stirred and dissolved to make material B.

[0039] Add 1.5 grams of KNO to 20 grams of water 3 , 1.7 g LiNO 3 and 2.4 g CsNO 3 After dissolution it was added to feed B to form feed C.

[0040] Material C was added dropwise to material A under rapid stirring, and the obtained material was aged at 70°C for 3 hours, then spray-dried into granules, and the obtained granules were roa...

Embodiment 2~10

[0042] Change the starting material of the active component and the amount thereof, change the content of the carrier silica in the total amount of the catalyst and the amount of solid silica in the carrier, and the rest are the same as in Example 1. The finished catalyst was evaluated using the above-mentioned investigation and evaluation conditions.

Embodiment 2

[0048] Example 2 Mo 11.2 Bi 0.45 Fe 2 Ni 5.2 Mg 2 La 0.3 Rb 0.06 K 0.09 W 0.46 V 0.3 P 0.04 o x

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Abstract

A fluidized-bed catalyst for the ammoxidation reaction of olefin is composed of the carrier consisting of nano-SiO2 and silica sol, and the active component Mo(12-g)BiaFebNicXdZfOgOx, where X is chosen from Mg, Co, Ca, Be, Cu, Zn, Pb, Sb, Mn and Cr, Y is chosen from La, Ce and Sm, Z is chosen from Li, K, Rb, Na and Cs, Q is chosen from B, W, P and V, a=0.1-6, b=0.01-10, c=0.01-10, d=0.01-10, e=0.01-10, g=0-2 and f is more than (0-0.5).

Description

technical field [0001] The invention relates to an ammoxidation catalyst for preparing unsaturated nitrile from olefin, and its active component contains multiple metal oxides such as molybdenum, bismuth and iron. Background technique [0002] α or β unsaturated nitriles can be prepared from olefins through ammoxidation, and the most typical industrial acrylonitrile or methacrylonitrile is prepared from propylene or isobutylene through ammoxidation. This type of ammoxidation reaction is usually carried out in a fluidized bed reactor, and the catalysts used are mostly supported catalysts, the most mature and widely used of which are molybdenum-bismuth-iron catalysts, which use silica as a carrier and support The active component contains molybdenum, bismuth, iron and other metal oxides, as introduced in Chinese patents ZL91100078.X and ZL97106771.6. Since the birth of this type of catalyst, people have paid more attention to the improvement of the active components. Through ...

Claims

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Application Information

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IPC IPC(8): B01J23/88B01J23/889B01J27/18C07C253/24
Inventor 黄新汉姜家乐严胜宏杨斌
Owner CHINA PETROLEUM & CHEM CORP
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