Unlock instant, AI-driven research and patent intelligence for your innovation.

A kind of unsaturated aldehyde selective oxidation method

An aldehyde selective, unsaturated technology, applied in the field of selective oxidation of unsaturated aldehydes, can solve the problems of huge energy consumption, huge economic losses, difficult to control accurately, etc., to suppress hot spots, avoid the drop of bed temperature, long-term The effect of cycle stable production

Active Publication Date: 2015-11-18
PETROCHINA CO LTD
View PDF18 Cites 0 Cited by
  • 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
Tungsten bias on the surface side of the catalyst, and / or copper bias on the core side of the catalyst is difficult to accurately control

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • A kind of unsaturated aldehyde selective oxidation method
  • A kind of unsaturated aldehyde selective oxidation method
  • A kind of unsaturated aldehyde selective oxidation method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0040] Preparation of Catalyst 1

[0041] Step 1: Prepare catalyst inner layer matrix

[0042] (1) Preparation of active ingredient slurry (a)

[0043] Under stirring conditions, take 211.9 grams of ammonium molybdate and 46.8 grams of ammonium metavanadate and dissolve them in 500ml of pure water (water temperature above 65°C) to obtain slurry (1), then take 52.2 grams of ammonium paratungstate, 127.9 grams of copper nitrate, 14.5 grams Dissolve nickel nitrate, 48 grams of sodium stannate, and 5.8 grams of cesium nitrate in 1000 ml of pure water (water temperature above 65°C), stir well and mix evenly to obtain slurry (2). Then, the slurry (1) is mixed with the slurry (2) to obtain the slurry (3) to obtain the active ingredient slurry (a).

[0044] (2) Preparation of catalyst inner layer matrix

[0045] Add 90 grams of silicon dioxide and 1.4 grams of graphite to the active component slurry (a), stir vigorously at 80°C for co-precipitation reaction, heat and dry, heat-trea...

Embodiment 2

[0059] Preparation of Catalyst 2

[0060] Same as the preparation steps and the main raw materials of the catalyst 1 in Example 1, just add 16.2 grams of lanthanum nitrate, add 162 grams of silicon dioxide and 2.3 grams of silicon carbide in the inner layer, and extrude and roll granulate into a diameter of 2mm through an extruder. Spherical shape, adding 13.2 grams of silicon dioxide to the outer layer. The thickness of the coating is 0.5-2.0mm, and the catalyst 2 is obtained by roasting at 450° C. for 3 hours. The main composition of catalyst 2 inner layer matrix is: Mo 12 V 5 W 4 Cu 2 Ni 3.7 sn 0.6 La 0.5 Si 25.2 o x , the main composition of the outer layer is: Mo 12 V 5 W 4 Cu 2 Ni 3.7 sn 0.6 La 0.5 Si 2.2 o x , the element content of the outer layer is 0.8%~17.4% higher than that of the inner layer.

Embodiment 3

[0067] Same as the preparation steps and main raw materials of the catalyst 1 in Example 1, just add 11.8 grams of potassium manganate, add 174.6 grams of silicon dioxide and 1.6 grams of aluminum oxide in the inner layer; add 4.2 grams of silicon dioxide in the outer layer. The main composition of the catalyst 3 inner layer matrix is: Mo 12 V 2 W 6.7 Cu 1 Ni 1.2 sn 1.0 Si 20.5 mn 0.6 o x , the main composition of the outer layer is: Mo 12 V 2 W 6.7 Cu 1 Ni 1.2 sn 1.0 Si 0.7 mn 0.6 o x

[0068] The inner diameter of the fixed-bed single-tube reactor is 25 mm, and a thermocouple is installed inside, and 13 ml of CN201110265250.4 catalyst 3 (S 1 paragraph), 17ml of the above catalyst (S 2 section), heated in a salt bath, and the temperature of the salt bath was 253°C. From the entrance of the above reaction tube at a space velocity of 2000h -1 A mixed gas of 11% by volume of acrolein, 15% by volume of oxygen, 15% by volume of water vapor, and 59% by volume of...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

PropertyMeasurementUnit
thicknessaaaaaaaaaa
thicknessaaaaaaaaaa
Login to View More

Abstract

The invention relates to a preparation method for unsaturated acid from unsaturated aldehyde. A fixed bed reactor is employed; the part of the reactor from a reaction raw material inlet to an outlet is divided into a segment S1 and a segment S2; the segment S1 is filled with a Mo-Vi double-layer catalyst with inner layer concentration higher than external layer concentration; the segment S2 is filled with a catalyst (I) which has a double-layer structure; the catalyst (I) has the double-layer structure, and main composition of the catalyst is expressed by the general formula (I)--MoaVbWcCudNieSnfSigMhOx (I). The method is applicable to preparation of acrylic acid through selective oxidation of acrolein; bed temperature of the reactor is reasonably distributed; and the target product acrylic acid has high selectivity and yield.

Description

technical field [0001] The invention relates to a method for selective oxidation of unsaturated aldehydes, which is suitable for the selective oxidation of acrolein or methacrolein to produce corresponding unsaturated acids, and is especially suitable for catalyzing the selective oxidation of acrolein to produce acrylic acid. Background technique [0002] At present, acrylic acid is mainly prepared by two-step oxidation of propylene in industry. First, propylene is catalyzed in the gas phase to oxidize acrolein, and then acrolein is oxidized to acrylic acid. The oxidation reaction of acrolein is a strong exothermic reaction. Hot spots will be generated in the catalyst bed, and the heat accumulated instantaneously will continue to accumulate, which will lead to the loss and shedding of the active components of the catalyst, so that the activity of the catalyst will decrease, the life will be shortened, and the overheating will be caused. The oxidation reaction aggravates the ...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Patents(China)
IPC IPC(8): C07C51/25C07C57/055B01J23/888
CPCB01J23/002B01J23/8885B01J2523/00C07C51/252C07C57/04B01J2523/68B01J2523/55B01J2523/69B01J2523/17B01J2523/847B01J2523/43B01J2523/41B01J2523/15B01J2523/72B01J2523/3706
Inventor 王学丽张忠东李琰马艳萍何颖谢元李洁王玲玲白竟冰刘晓兰李耀朱博张小齐
Owner PETROCHINA CO LTD