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A kind of chlorine-free cuy catalyst for synthesizing dimethyl carbonate and its preparation method and application

A technology of dimethyl carbonate and catalyst, which is applied in the field of catalyst and preparation, can solve problems such as catalyst deactivation, equipment corrosion, and environmental pollution, and achieve the effects of overcoming catalyst deactivation, good catalytic performance, and avoiding the use of a large amount of solvents

Inactive Publication Date: 2017-05-10
TAIYUAN UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] Based on the above analysis, the preparation of CuY catalysts by solid-state ion exchange method is based on CuCl or CuCl 2 As a copper source, CuCl needs to be purified, and the carrier needs to be converted from NaY to NH 4 During the treatment process from Y to HY, a certain amount of Cl will still remain in the catalyst, and the loss of Cl will cause catalyst deactivation, equipment corrosion, and environmental pollution; while the solution ion exchange method has complicated procedures and uses a large amount of solvents, polluting the environment

Method used

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  • A kind of chlorine-free cuy catalyst for synthesizing dimethyl carbonate and its preparation method and application
  • A kind of chlorine-free cuy catalyst for synthesizing dimethyl carbonate and its preparation method and application
  • A kind of chlorine-free cuy catalyst for synthesizing dimethyl carbonate and its preparation method and application

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0032] (1) take by weighing the NaY molecular sieve (SiO 2 / Al 2 o 3 =5.3, specific surface area 810m 2 / g, pore volume 1.1cm 3 g -1 ) 5g and 0.5mol / L ammonium nitrate solution 50mL, exchange at 80°C for 12h, repeat the exchange twice, wash, filter with suction, and dry at 100°C to obtain NH 4 Y molecular sieve, its exchange degree reaches 78%.

[0033] (2) Weigh 3gNH 4 Y and 1.227 g of copper acetylacetonate were uniformly mixed mechanically, and steam impregnation was carried out at 150° C. for 24 hours to obtain a catalyst precursor.

[0034] (3) Weigh 3 g of the catalyst precursor, raise the temperature to 400° C. for 18 hours in the air at a heating rate of 3° C. / min and activate for 18 hours to obtain a catalyst. The loading amount of Cu is 10 wt % in terms of metal.

[0035] See attached table 1 for the reaction conditions and reactivity evaluation results of direct vapor-phase oxidative carbonylation of methanol to dimethyl carbonate by the catalyst. The specifi...

Embodiment 2

[0038] (1) take by weighing the NaY molecular sieve (SiO 2 / Al 2 o 3 =4.8, specific surface area 760m 2 / g, pore volume 1.2cm 3 g -1 ) 5g and 0.2mol / L ammonium nitrate solution 50mL, exchanged at 30°C for 4h, repeated the exchange once, washed, suction filtered, and dried at 100°C to obtain NH 4 Y molecular sieve, its exchange degree reaches 32%. (2) Weigh 3gNH 4 Y and 0.982 g of copper acetylacetonate were uniformly mixed mechanically, sublimated and impregnated at 250° C. for 8 hours to obtain a catalyst precursor.

[0039] (3) Weigh 3g of catalyst precursor, in 50vol%N 2 +50vol%O 2 In the atmosphere, the temperature was raised to 700° C. for 8 hours at a heating rate of 3° C. / min for activation to obtain a catalyst, and the loading amount of Cu was 8 wt % in terms of metal.

[0040] Catalyst in direct vapor phase oxidative carbonylation of methanol to synthesize dimethyl carbonate The reaction conditions and activity evaluation activity are shown in attached table ...

Embodiment 3

[0042] (1) Weigh the NaY molecular sieve (SiO 2 / Al 2 o 3 =11, the specific surface area is 655m 2 / g, pore volume 0.8cm 3 g -1 ) 5g and 0.1mol / L ammonium nitrate solution 50mL, exchanged at 40°C for 8h, repeated the exchange twice, washed, suction filtered, and dried at 100°C to obtain NH 4 Y molecular sieve, its exchange degree reaches 42%.

[0043] (2) Weigh 3gNH 4 Y and 0.736 g of copper acetylacetonate were uniformly mixed mechanically, sublimated and impregnated at 250° C. for 4 hours to obtain a catalyst precursor.

[0044] (3) Weigh 3 g of the catalyst precursor, heat it up to 750° C. for 4 hours in Ar at a heating rate of 5° C. / min, and activate it for 4 hours to obtain a catalyst. In terms of metal, the Cu loading is 6 wt%.

[0045] Catalyst in direct vapor phase oxidative carbonylation of methanol to synthesize dimethyl carbonate The reaction conditions and activity evaluation activity are shown in attached table 1, and the specific steps are shown in Example...

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Abstract

The invention discloses a synthetic dimethyl carbonate chloride-free CuY catalyst, which is prepared from 5.0%-30.0wt% of an active component Cu and the balance being a Y molecular sieve on the basis of metal. The synthetic dimethyl carbonate chloride-free CuY catalyst has the advantages of high catalytic activity, free of chloride and free of pollution.

Description

technical field [0001] The invention belongs to a catalyst and its preparation method and application, and in particular relates to a completely chlorine-free supported copper-based catalyst, its preparation method and its application in the direct gas-phase oxidative carbonylation of methanol to synthesize dimethyl carbonate. Background technique [0002] Dimethyl carbonate (dimethyl carbonate, DMC) contains various functional groups such as methyl group, methoxyl group and carbonyl group, and is an important chemical intermediate; in addition, due to its high oxygen content of 53% and good blending It can replace methyl tert-butyl ether to increase the octane number of gasoline. Therefore, the demand for DMC has greatly increased. It was first synthesized by the toxic phosgene method, which has been eliminated; and the raw material of the transesterification method, ethylene oxide or propylene oxide, is affected by the petrochemical industry, and the cost is relatively hig...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/14C07C69/96C07C68/00
Inventor 王玉春李忠郑华艳
Owner TAIYUAN UNIV OF TECH