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Iron-based spinel composite oxide catalyst and its application

A composite oxide and catalyst technology, applied in physical/chemical process catalysts, hydrocarbons, hydrocarbons, etc., can solve the problem of low conversion rate of butene, low yield of butadiene, and high generation rate of alkyne by-products problem, to achieve the effect of enhanced activation

Active Publication Date: 2017-07-14
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] One of the technical problems to be solved by the present invention is that the prior art has the problems of low conversion rate of butene, low yield of butadiene, and high production rate of alkyne by-products. A new iron-based spinel composite oxide is provided catalyst

Method used

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  • Iron-based spinel composite oxide catalyst and its application
  • Iron-based spinel composite oxide catalyst and its application
  • Iron-based spinel composite oxide catalyst and its application

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0050] Get 236.0g ferric nitrate (Fe(NO 3 ) 3 9H 2 O), 128.2g magnesium nitrate (Mg(NO 3 ) 2 6H 2 O), 29.4g zinc nitrate (Zn(NO 3 ) 2 6H 2 O) and 3.3g manganese nitrate (Mn(NO 3 ) 2 ) was dissolved in 400ml of deionized water, then 3.0g of glucose was added to dissolve, and then at 60°C, under vigorous stirring, slowly added dropwise ammonia water (20%) containing 0.62g of ammonium sulfide to the mixed aqueous solution, and the pH value was controlled to be 9.5 , a precipitate was formed, which was aged at room temperature for 6 hours and then filtered. The filtered solid was then washed 5 times with deionized water, adding 1.1 g of HO during the last wash 3 PO 4 , dried at 120°C, pulverized, sieved, and calcined at 700°C for 6 hours to obtain composite oxide catalyst A. Catalyst A is composed of oxides and its chemical formula is:

[0051] 59.0%Fe 2 O 3 0.8%FeS 25.7%MgO 1.0%P 2 O 5 11.5%ZnO 2.0%MnO 2

[0052] XRD diffraction spectrum proves that it conta...

Embodiment 2

[0056] Get 130.4g ferric nitrate (Fe(NO 3 ) 3 9H 2 O), 51.3g magnesium nitrate (Mg(NO 3 ) 2 6H 2 O), 36.7g zinc nitrate (Zn(NO 3 ) 2 6H 2 O) and 2.1g manganese nitrate (Mn(NO 3 ) 2 ) was dissolved in 400ml of deionized water, then 3.0g of polyvinyl alcohol was added to dissolve, and then at room temperature, under vigorous stirring, the mixed aqueous solution was slowly added dropwise to 12% ammonia water (containing 1.54g of ammonium sulfide), and the pH was controlled to be 8.0, a precipitate was formed, aged at room temperature for 6 hours, and then filtered. The filtered solid was then washed 5 times with deionized water, adding 2.8 g of H during the last wash 3 PO 4 , dried at 110°C, pulverized, sieved, and calcined at 700°C for 6 hours to obtain composite oxide catalyst B. Catalyst B is composed of oxides and its chemical formula is:

[0057] 52.3%Fe 2 O 3 2.0%FeS 17.4%MgO 4.4%P 2 O 5 21.8%ZnO 2.2%MnO 2

[0058] XRD diffraction spectrum proves that ...

Embodiment 3

[0062] Get 189.7g ferric nitrate (Fe(NO 3 ) 3 9H 2 O), 51.3g magnesium nitrate (Mg(NO 3 ) 2 6H 2 O), 40.5g zinc nitrate (Zn(NO 3 ) 2 6H 2 O) and 1.7g manganese nitrate (Mn(NO 3 ) 2 ) was dissolved in 400ml of deionized water, then 5.0g of polyvinylpyrrolidone was added to dissolve, and then the mixed aqueous solution and 18% ammonia water (containing 1.16g of ammonium sulfide) were added dropwise at 60°C under vigorous stirring, and the pH was controlled to be 9.0, a precipitate formed, aged at room temperature for 6 hours, and then filtered. The filtered solid was then washed 5 times with deionized water, adding 2.1 g of H during the last wash 3 PO 4 , dried at 120°C, pulverized, sieved, and calcined at 700°C for 6 hours to obtain composite oxide catalyst C. Catalyst C is composed of oxides and its chemical formula is:

[0063] 62.0%Fe 2 O 3 1.5%FeS 13.7%MgO 18.8%ZnO 2.6%P 2 O 5 1.4%MnO

[0064] XRD diffraction spectrum proves that it contains spinel, α-F...

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Abstract

The invention relates to an iron-based spinel composite oxide catalyst and its application, which mainly solves the problems of low butene conversion rate, low butadiene yield and high alkyne by-product generation rate in the prior art. The catalyst of the invention includes FeS active crystal phase, has unique XRD diffraction data, and can be used in the industrial production of butadiene prepared by oxidative dehydrogenation of butene.

Description

technical field [0001] The present invention relates to an iron-based spinel composite oxide catalyst and its application. Background technique [0002] Butadiene is the basic raw material of petrochemical industry and an important monomer for the production of polymer synthetic materials. It can be copolymerized with various compounds to form various synthetic rubbers and synthetic resins. At present, there are two main production methods for butadiene: refinery steam cracking to ethylene co-production C4 extraction and separation and butene oxidation. Almost all butadiene in my country comes from the extraction and separation of C4. This process has economic advantages, but it is obtained as a by-product of the cracker in the refinery. With the increase in the demand for butadiene production in the rubber industry, the cracker The production of butadiene has been difficult to meet the needs. Oxidative dehydrogenation of butene is a process in which butadiene is the target...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J27/187B01J27/185B01J27/188B01J27/198C07C11/167C07C5/48
Inventor 吴文海缪长喜樊志贵曾铁强
Owner CHINA PETROLEUM & CHEM CORP