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Supported copper catalyst, preparation method and application thereof, and method for preparing propylene oxide by oxidation of propylene

A copper catalyst and catalyst technology, applied in chemical instruments and methods, physical/chemical process catalysts, organic compound/hydride/coordination complex catalysts, etc., can solve problems such as unsatisfactory PO selectivity and decreased PO selectivity. , to achieve the effect of good stability, high activity and good selectivity

Active Publication Date: 2019-05-03
CHNA ENERGY INVESTMENT CORP LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0014] At present, the PO selectivity of the direct oxidation process of propylene molecular oxygen using copper catalysts (including copper catalysts modified by alkaline earth metal salts or oxides) is still unsatisfactory, generally only at extremely low propylene conversion rates (1- 5%), the relatively high PO selectivity (20-50%) can be obtained, and with the increase of propylene conversion (increasing the reaction temperature), the PO selectivity drops sharply

Method used

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  • Supported copper catalyst, preparation method and application thereof, and method for preparing propylene oxide by oxidation of propylene
  • Supported copper catalyst, preparation method and application thereof, and method for preparing propylene oxide by oxidation of propylene
  • Supported copper catalyst, preparation method and application thereof, and method for preparing propylene oxide by oxidation of propylene

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preparation example Construction

[0054] According to the preparation method of the present invention, the phosphorus-containing organic ligands that meet the aforementioned requirements include, but are not limited to, compounds selected from phosphoric acid esters and / or phosphite esters, preferably selected from aromatic phosphoric acid esters or aromatic compounds having the following structure: One or more of group phosphites:

[0055]

[0056] Where R 1 , R 2 , R 3 , R 4 , R 5 Each is a substituted or unsubstituted aryl group; R 6 , R 7 , R 8 , R 9 , R 10 , R 11 Each is a substituted or unsubstituted arylene group, R 12 , R 13 Is C 1 -C 6 The alkylene group or a substituted or unsubstituted arylene group, R 14 , R 15 , R 16 , R 17 Each is a substituted or unsubstituted aryl group.

[0057] Preferably, R 1 , R 2 , R 3 , R 4 , R 5 Each substituted C 6 -C 10 The aryl group or unsubstituted aryl group; R 6 , R 7 , R 8 , R 9 , R 10 , R 11 Each substituted C 6 -C 10 The arylene group or unsubstituted arylene group, ...

Embodiment 1

[0099] Prepare 5 wt% Cu / SiO 2 / DOPO(P / Cu=1(mol / mol)) catalyst

[0100] SiO 2 Carrier (Grvisil Grade 62, specific surface area is 380m 2 / g, the pore size is 15 nanometers, 60-200 mesh) before use, activated at 250 ℃ for 4 hours, 5.56 grams of CuCl 2 ·H 2 O was dissolved in 77.7 g of deionized water, and the solution was added dropwise to 36 g of SiO 2 In the carrier, continue to stir the carrier during the dripping process to make the solution uniformly absorbed. After the solution is dripped, the carrier particles are completely wetted by the solution, but there is no free-flowing solution. The obtained solid is dried at 120°C for 4 hours and then at 300°C in an air atmosphere Calcined in medium for 4 hours to obtain a copper oxide-loaded carrier;

[0101] Take 0.3758 grams of 9,10-dihydro-9-oxa-10-phosphaphenanthrene-10-oxide (DOPO) was dissolved in 30 mL of toluene, 2.0 g of the aforementioned copper oxide-loaded carrier was added, stirred at 50°C for 4 hours, then the solvent w...

Embodiment 2

[0106] Prepare 5 wt% Cu / Al 2 O 3 / TPP(P / Cu=0.5(mol / mol)) catalyst

[0107] Al 2 O 3 The carrier was activated at 350°C for 4 hours before use, and 7.72 g of CuCl 2 ·H 2 O is dissolved in 54 grams of deionized water, and the solution is added dropwise to 50 grams of Al 2 O 3 In the carrier, continue to stir the carrier during the dripping process to make the solution uniformly absorbed. After the solution is dripped, the carrier particles are completely wetted by the solution, but there is no free-flowing solution. The obtained solid is dried at 120°C for 4 hours and then at 300°C in an air atmosphere Calcined in medium for 4 hours to obtain a copper oxide-loaded carrier;

[0108] Dissolve 0.2836 g of triphenyl phosphate (TPP) in 30 mL of toluene, add 2.0 g of the roasted copper oxide-loaded carrier, stir at 50°C for 4 hours, and then rotate and evaporate to remove the solvent. The resulting solid is heated at 120°C. Dry for 4 hours to obtain a catalyst.

[0109] Temperature programm...

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Abstract

The invention provides a supported copper catalyst. The catalyst comprises a carrier and phosphorus-containing organic ligand modified copper supported on the carrier. At the atmosphere, the phosphorus-containing organic ligand is stable and will not be decomposed at 200 DEG C, more preferably at 250 DEG C and most preferably at 300 DEG C. The invention provides a preparation method of the supported copper catalyst. The method comprises the following step: the carrier supported with copper oxide contacts with the phosphorus-containing organic ligand. The invention provides an application of the catalyst in an oxidation reaction and a propylene oxidation preparation method of epoxypropane. The catalyst of the invention has good stability, high activity and good selectivity. Specifically in the reaction of preparing epoxypropane by propylene oxidation, when propylene conversion rate of the catalyst is 20-30%, selectivity of PO can reach 15-21% and selectivity of PO is enhanced with the increasing of the reaction temperature in a reasonable reaction interval.

Description

Technical field [0001] The invention relates to a supported copper catalyst and a preparation method and application of the supported copper catalyst, as well as a method for preparing propylene oxide by oxidation of propylene. Background technique [0002] Propylene oxide (PO) is an important basic organic chemical raw material, and it is the third largest product after polypropylene and acryl cyanide in propylene derivatives. With the development of my country's fine chemical and polyurethane industries, the demand for propylene oxide is increasing. [0003] At present, the industrial production methods of propylene oxide are mainly the chlorohydrin method and the co-oxidation method (Halcon method), and the indirect oxidation method of cumene hydroperoxide is supplemented. The research and development of efficient, economical and environmentally friendly propylene oxide production technology has always been a hot spot in the fine chemical industry. Among them, the successful ap...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J31/28C07D301/12C07D303/04
CPCY02P20/52
Inventor 刘长坤孙琦
Owner CHNA ENERGY INVESTMENT CORP LTD