Supported ruthenium-pyrrolidine ionic liquid catalyst as well as preparation method and application thereof
A technology of ionic liquid and pyrrolidine, which is applied in the field of catalysts for the addition reaction of acetylene and hydrogen chloride, can solve the problems of catalyst deactivation and carbon deposition
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Embodiment 1
[0025] Example 1. A supported ruthenium-pyrrolidine ionic liquid catalyst, the catalyst is composed of RuCl3, pyrrolidine ionic liquid and carrier activated carbon.
[0026] Described catalyst, by weight, contains RuCl in every one hundred parts 3 0.001-1 part, the content of pyrrolidine ionic liquid is 1-20 parts per hundred parts, and the balance is carrier activated carbon.
[0027] The pyrrolidine ionic liquid is N-butyl-N-methylpyrrolidine bromide.
[0028] Better yet, the catalyst, in parts by weight, contains RuCl in every hundred parts 3 0.01-0.5 parts, the content of pyrrolidine ionic liquid is 5-15 parts per hundred parts, and the balance is carrier activated carbon.
[0029] A kind of preparation method of supported ruthenium-pyrrolidine ionic liquid catalyst, is prepared by impregnating-drying method, RuCl 3 and pyrrolidine ionic liquids are uniformly mixed to obtain a solution, then activated carbon is added into the solution, the impregnation temperature is 5...
Embodiment 2
[0033] Example 2. A kind of supported ruthenium-pyrrolidine ionic liquid catalyst, described catalyst, by weight, contains RuCl in every hundred parts 3 0.3 parts, the content of pyrrolidine ionic liquid N-butyl-N-methylpyrrolidinium bromide is 18 parts in every hundred parts, the balance is carrier activated carbon, and the catalyst is prepared by impregnation-drying method, and RuCl 3 and pyrrolidine ionic liquids are uniformly mixed to obtain a solution, then activated carbon is added into the solution, the impregnating temperature is 70° C., and dried after impregnating. The obtained catalyst is used for the addition reaction of acetylene and hydrogen chloride. The conditions for the addition reaction of acetylene and hydrogen chloride are: temperature 90-200°C, molar ratio of acetylene to hydrogen chloride is 1:1.05, and the space velocity of acetylene is 25h -1, the conversion rate of acetylene is 99.7%, and the selectivity of vinyl chloride is 99.8%.
Embodiment 3
[0034] Example 3. A kind of supported ruthenium-pyrrolidine ionic liquid catalyst, described catalyst, by weight, contains RuCl in every hundred parts 3 0.25 parts, the content of pyrrolidine ionic liquid N-butyl-N-methylpyrrolidinium bromide is 16.5 parts per hundred parts, and the balance is carrier activated carbon. The catalyst is prepared by impregnation-drying method, and RuCl 3 and pyrrolidine ionic liquids are uniformly mixed to obtain a solution, then activated carbon is added into the solution, the impregnation temperature is 60°C, and the impregnation is dried. The obtained catalyst is used for the addition reaction of acetylene and hydrogen chloride. The conditions for the addition reaction of acetylene and hydrogen chloride are: temperature 90-200°C, molar ratio of acetylene to hydrogen chloride is 1:1.05, and the space velocity of acetylene is 23h -1 , the conversion rate of acetylene is 99.8%, and the selectivity of vinyl chloride is 99.8%.
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