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A vanadium-phosphorus-oxygen catalyst for producing maleic anhydride by n-butane oxidation and its preparation method

A catalyst, vanadium phosphorus oxide technology, applied in physical/chemical process catalysts, chemical instruments and methods, organic chemistry and other directions, can solve problems such as increasing the yield of maleic anhydride, and achieve the effects of improving selectivity, easy implementation and simple process

Active Publication Date: 2020-12-18
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although the current production route using n-butane as raw material occupies a dominant position in the production of maleic anhydride, the catalyst needs to further improve its activity and selectivity to increase the yield of maleic anhydride

Method used

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  • A vanadium-phosphorus-oxygen catalyst for producing maleic anhydride by n-butane oxidation and its preparation method
  • A vanadium-phosphorus-oxygen catalyst for producing maleic anhydride by n-butane oxidation and its preparation method
  • A vanadium-phosphorus-oxygen catalyst for producing maleic anhydride by n-butane oxidation and its preparation method

Examples

Experimental program
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Effect test

Embodiment 1

[0067] Into a 3L round bottom flask add 127.2g of V 2 o 5 A mixed solution of 1350mL isobutanol and 150mL benzyl alcohol was heated and stirred to reflux for 3 hours, 10.0g of polyethylene glycol with a molecular weight of 1500 was added thereto, 150g of phosphoric acid 105wt% was added dropwise and heated and stirred to reflux for 16 hours, The V / P feeding molar ratio is 1 / 1.15, and the resulting precipitate is centrifuged and washed with absolute ethanol and then dried at 120°C for 12 hours. Add the dried catalyst precursor powder to graphite with a mass ratio of 3 / 97 to the catalyst precursor powder, mix well and heat in air at 250°C for 5 hours, and then press the powder into a cylindrical structure with a height of 3mm and a diameter of 6mm object, the density of this structure is 1.2g / cm 3 , the obtained catalyst precursor structure was heated up to 375°C at a heating rate of 2.5°C / min in an air atmosphere, and then the atmosphere was replaced with a mixed atmosphere o...

Embodiment 2

[0071] Into a 3L round bottom flask add 127.2g of V 2 o 5 A mixed solution of 1250mL isobutanol and 250mL benzyl alcohol was heated and stirred to reflux for 3 hours, 20.0g of polyethylene glycol with a molecular weight of 2000 was added thereto, 156g of phosphoric acid 105wt% was added dropwise and heated and stirred to reflux for 20 hours, The V / P feeding molar ratio is 1 / 1.20, and the resulting precipitate is centrifuged and washed with absolute ethanol and then dried at 120°C for 12 hours. Add the dried catalyst precursor powder to graphite with a mass ratio of 3 / 97 to the catalyst precursor powder, mix well and heat in air at 250°C for 5 hours, and then press the powder into a cylindrical structure with a height of 3mm and a diameter of 13mm object, the density of this structure is 1.22g / cm 3 , the obtained catalyst precursor structure was heated up to 375°C at a heating rate of 2.5°C / min in an air atmosphere, and then the atmosphere was replaced with a mixed atmosphere...

Embodiment 3

[0075] Into a 3L round bottom flask add 127.2g of V 2 o 5 A mixed solution of 1250mL isobutanol and 250mL benzyl alcohol was heated and stirred to reflux for 3 hours, 10.0g of polyethylene glycol was added with a molecular weight of 6000, 130g of 105wt% phosphoric acid was added dropwise and heated and stirred to reflux for 10 hours, The V / P feeding molar ratio is 1 / 1, and the resulting precipitate is centrifuged and washed with absolute ethanol and then dried at 120°C for 12 hours. Add the dried catalyst precursor powder to graphite with a mass ratio of 5 / 95 to the catalyst precursor powder, mix well and heat in air at 250°C for 5 hours, and then press the powder into a cylindrical structure with a height of 3mm and a diameter of 6mm object, the density of this structure is 1.12g / cm 3 , the obtained catalyst precursor structure was heated up to 375°C at a heating rate of 2.5°C / min in an air atmosphere, and then the atmosphere was replaced with a mixed atmosphere of 50% wate...

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Abstract

The invention provides a vanadium phosphorus oxide catalyst for preparing maleic anhydride from n-butane through oxidation. The vanadium phosphorus oxide catalyst is prepared by treating a vanadium phosphorus oxide catalyst matrix with a pore-enlarging agent; the mass content of elemental vanadium in the catalyst is 28 to 35%; the mass content of elemental phosphorus in the catalyst is 15 to 25%;and the pore-enlarging agent comprises one or more selected from a group consisting of 1,1,1-trimethylolethane, trimethylolpropane, phthalic anhydride, maleic anhydride, tartaric acid, and citric acidor In many cases, and a mass ratio of the pore-enlarging agent to the vanadium phosphorus oxide catalyst matrix is (5-20): (80-95). According to the invention, the pore-enlarging agent is added and the removal process of the pore-enlarging agent is controlled in the post-treatment process of the catalyst, so the specific surface area and the pore structure of the treated catalyst can be controlled and improved; and thus, the activity of the catalyst in catalysis of the selective oxidation of butane and the selectivity of produced maleic anhydride are improved.

Description

technical field [0001] The invention belongs to the technical field of catalyst synthesis, and relates to a vanadium-phosphorus-oxygen catalyst for preparing maleic anhydride by n-butane oxidation and a preparation method thereof. The catalyst is suitable for the catalytic reaction process of n-butane oxidation for maleic anhydride, more specifically , the present invention relates to catalysts providing improved catalytic performance. Background technique [0002] Maleic anhydride (maleic anhydride) is an important organic chemical raw material and fine chemical product. It is the third largest anhydride in the world after phthalic anhydride and acetic anhydride. It is mainly used in the production of thermosetting resins and unsaturated polyesters. Resins are used in the fields of pesticides, medicines, coatings, inks, lubricating oil additives, paper chemicals, textile chemicals, textile finishing agents, food additives, and surfactants. In addition, a series of widely u...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J27/198C07D307/60
CPCB01J27/198C07D307/60
Inventor 师慧敏张明森张东顺贾雪飞冯晔张作峰苗小培
Owner CHINA PETROLEUM & CHEM CORP