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Method of preparing formaldehyde by catalytic selection oxidation of ethylene

A technology of selective oxidation and catalytic oxidation, applied in the field of formaldehyde

Inactive Publication Date: 2009-05-20
XIAMEN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

But so far, the method for preparing formaldehyde from direct selective oxidation of ethylene has not been seen in any report

Method used

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  • Method of preparing formaldehyde by catalytic selection oxidation of ethylene
  • Method of preparing formaldehyde by catalytic selection oxidation of ethylene

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0029] Weigh 0.50g of ammonium heptamolybdate and dissolve it completely in 30ml of deionized water, weigh 1.63g of mesoporous molecular sieve SBA-15 according to the proportion, add it to the above solution, stir at room temperature for 8h, stand for 10h, and steam in a 70℃ water bath until viscous paste, dried in a vacuum oven at 50°C for 20h, fully ground and then added to 1°C mlin -1 The heating rate was increased to 600 °C for 6 h, and 20wt% MoO was obtained. 3 / SBA-15 catalyst. The calcined solid powder is pressed into tablets, pulverized and sieved, and the solid particles of 30-60 meshes are taken as the catalyst for the catalytic selective oxidation reaction of ethylene.

[0030] The catalytic reaction was carried out in a fixed-bed reactor at atmospheric pressure (inner diameter of quartz reaction tube was 8 mm), and 0.20 g of 30-60 mesh 20wt% MoO was weighed 3 / SBA-15 catalyst was loaded into the reaction tube, at N 2 :O 2 =1:1, the total flow rate is 20ml min ...

Embodiment 2

[0034] The specific steps of catalyst preparation are the same as those in Example 1.

[0035] The catalytic reaction was carried out in a fixed-bed reactor at atmospheric pressure (inner diameter of quartz reaction tube was 8 mm), and 0.20 g of 30-60 mesh 20wt% MoO was weighed 3 / SBA-15 catalyst was loaded into the reaction tube. in N 2 :O 2 =1:1, the total flow rate is 20ml min -1The temperature was programmed to 600 °C for 30 min under the atmosphere, and the reaction was started after purging with nitrogen for 20 min. Reaction conditions: N 2 :O 2 :C 2 H 4 =8:1:1 (volume ratio), the total flow rate is 150ml min -1 , normal pressure, the reaction temperature is 590 ℃. The product was analyzed online by gas chromatography. The results of the catalytic reaction are listed in Table 2.

[0036] Table 2 20wt% MoO 3 Catalytic performance of / SBA-15 catalyst (T=590℃)

[0037] Conversion rate of ethylene (%) 47.3 Selectivity to formaldehyde (%) 61.2 ...

Embodiment 3

[0039] Weigh 0.09g of ammonium metavanadate and dissolve it completely in 30ml of deionized water, weigh 1.33g of mesoporous molecular sieve SBA-15 according to the proportion, add it to the above solution, stir at room temperature for 8h, stand for 10h, and steam in a water bath at 70°C until viscous paste, dried in a vacuum oven at 50°C for 20h, fully ground at 1°C min -1 The heating rate was increased to 600 °C for 6 h, and 5 wt% V was obtained. 2 O 5 / SBA-15 catalyst. The calcined solid powder is pressed into tablets, pulverized and sieved, and the solid particles of 30-60 meshes are taken as the catalyst for the catalytic selective oxidation reaction of ethylene.

[0040] The catalytic reaction was carried out in a fixed-bed reactor at atmospheric pressure (inner diameter of quartz reaction tube was 8 mm), and 0.20 g of 30-60 mesh 5wt% V was weighed. 2 O 5 / SBA-15 catalyst was loaded into the reaction tube. in N 2 :O 2 =1:1, the total flow rate is 20ml min -1 The ...

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Abstract

The present invention relates to a method for preparing formaldehyde by using ethylene as raw material, using oxygen gas or air as oxygen source and adopting gas-solid multi-phase catalytic selective oxidation reaction. The chemical composition of solid catalyst is nMoO3 / SiO2 or mV2O5 / SiO2, and said method includes catalyst pretreatment and catalytic reaction. Besides, said invention also provides the concrete steps and requirements of said catalyst pretreatment and catalytic reaction.

Description

technical field [0001] The present invention relates to a formaldehyde, in particular to a new method for directly producing formaldehyde by using ethylene as a raw material, on a solid catalyst, and the catalytic selective oxidation reaction of ethylene and oxygen or air, and a related solid catalyst. Background technique [0002] Formaldehyde is an important organic chemical raw material. Using formaldehyde as raw material, it can produce a variety of chemical products such as: urea-formaldehyde, phenolic, melamine and other resins, resin glue, plastics and polyoxymethylene engineering plastics, urotropine, pentaerythritol, phenolic resin paint, etc. In addition, formaldehyde is also used to produce some dyes, pesticides, disinfectants, etc. In 2002, the domestic demand for formaldehyde exceeded 2.6 million tons, and the annual growth rate of formaldehyde consumption in recent years is about 13%. [0003] At present, the main production route of formaldehyde is methanol ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C47/04C07C45/34B01J23/22B01J23/28B01J21/08
Inventor 王野楼银川张庆红王惠纯
Owner XIAMEN UNIV