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VPO catalyst and preparation and application thereof in preparation of acrolein by reaction of methanol and ethanol

A catalyst and acrolein technology, applied in the preparation of carbon-based compounds, organic compounds, physical/chemical process catalysts, etc., can solve problems such as difficult large-scale commercialization, unstable raw material prices, and scale-up, and achieve good hydrothermal Stability, the reaction process is simple, controllable and easy to operate, and the effect of good stability

Active Publication Date: 2020-10-13
DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, these methods are practically difficult to commercialize on a large scale due to the instability of raw material prices and the problem of scale-up.

Method used

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  • VPO catalyst and preparation and application thereof in preparation of acrolein by reaction of methanol and ethanol
  • VPO catalyst and preparation and application thereof in preparation of acrolein by reaction of methanol and ethanol

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0021] Vanadium pentoxide is placed in the mixed alcohol solution of benzyl alcohol and isobutanol (5g V 2 o 5 and 100mL alcohol solution), the volume ratio of benzyl alcohol to isobutanol is 3:1, heat and reflux at 120°C for 3h, then add phosphoric acid with a mass fraction of 85% and continue to reflux for 12h, the amount of phosphoric acid added is based on phosphoric acid and di Vanadium was added at a P / V molar ratio of 1.0. At the same time, surfactant PVP-K30 (concentration: 10 mg / mL) was added. The obtained solid was suction-filtered, air-dried at 100°C for 6 hours, calcined in air at 400°C for 12 hours, and activated in 0.5% butane-air mixture for 4 hours before use.

[0022] The obtained sample was pressed into tablets to 20-40 mesh, mechanically mixed with the same mass of silicon dioxide of the same mesh, and then loaded into a stainless steel tube fixed bed reactor (fixed bed inner diameter 8mm). Methanol-ethanol mixture (molar ratio 1:1), reaction temperature ...

Embodiment 2

[0024] Vanadium pentoxide is placed in the mixed alcohol solution of benzyl alcohol and isobutanol (10g V 2 o 5 and 100mL alcohol solution), the volume ratio of benzyl alcohol to isobutanol is 1:1, heat and reflux at 130°C for 3h, then add phosphoric acid with a mass fraction of 45% and continue to reflux for 12h, the amount of phosphoric acid added is based on phosphoric acid and di The P / V molar ratio in vanadium is 1.2. At the same time, surfactant PVP-K90 (concentration: 10 mg / mL) was added. The obtained solid was suction-filtered, air-dried at 120°C for 6 hours, roasted in nitrogen at 600°C for 12 hours, activated in 1.5% butane-air mixture for 4 hours before use.

[0025] The obtained sample was pressed into tablets to 40-60 mesh, mechanically mixed with the same mass of silicon dioxide of the same mesh, and then loaded into a stainless steel tube fixed bed reactor (fixed bed inner diameter 8mm). Methanol-ethanol mixture (molar ratio 5:1), reaction temperature 300°C, ...

Embodiment 3

[0027] Vanadium pentoxide is placed in the mixed alcohol solution of benzyl alcohol and isobutanol (5g V 2 o 5 and 100mL alcohol solution), the volume ratio of benzyl alcohol to isobutanol is 1:3, heat and reflux at 140°C for 3h, then add phosphoric acid with a mass fraction of 85% and continue to reflux for 12h. The P / V molar ratio of vanadium is added at 1.6. At the same time, surfactant PVP-K150 (concentration: 10 mg / mL) was added. The obtained solid was suction-filtered, vacuum-dried at 140°C for 6 hours, calcined and reduced with hydrogen at 800°C for 4 hours, activated in 3.0% butane-air mixture for 4 hours before use.

[0028] The obtained sample was pressed into tablets to 60-80 mesh, mechanically mixed with the same mass of silicon dioxide of the same mesh, and then loaded into a stainless steel tube fixed bed reactor (fixed bed inner diameter 8mm). Methanol-ethanol mixture (molar ratio 10:1), reaction temperature 400°C, pressure 0.1MPa, methanol: ethanol: oxygen: ...

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Abstract

The invention relates to a preparation method of acrolein, in particular to preparation of a VPO catalyst and preparation of acrolein by catalyzing a methanol and ethanol mixed solution (or a mixed aqueous solution) through oxidative condensation. The catalytic system has good catalytic activity and hydrothermal stability. The catalytic reaction is carried out in a solid bed reactor, the reactionliquid reacts in an oxygen-containing atmosphere, the yield of acrolein can reach 40% at most, and the selectivity can reach 85%.

Description

technical field [0001] The invention relates to a preparation method for preparing a VPO catalyst and its application in the reaction of methanol and ethanol to prepare acrolein, in particular to the preparation of acrolein by the oxidative condensation of methanol and ethanol catalyzed by the VPO catalyst. Background technique [0002] Acrolein is the simplest unsaturated aldehyde and has a wide range of applications in the chemical industry. One of the most important applications is the production of acrylic acid. Acrylic acid is mainly used in the production of coating resins, polyacrylic acid thickeners, superabsorbent materials, detergents, etc. Acrolein is also used to produce methionine, an important amino acid used in cattle feed and chemical agriculture. [0003] At present, the main production method of acrolein is the oxidation of propylene using bismuth molybdate and bismuth phosphomolybdate catalysts. With the continuous improvement of environmental protectio...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J27/198C07C45/74C07C47/22
CPCB01J27/198C07C45/38C07C45/74C07C47/04C07C47/06C07C47/22
Inventor 王峰张志鑫王业红李书双张健
Owner DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI