Method for preparing alcohol through hydroformylation of olefin which is directly regenerated and reused by cobalt catalyst
A technology of olefin hydroformyl and cobalt catalysts, which is applied in the preparation of organic compounds, carbon monoxide reaction preparation, chemical instruments and methods, etc. It can solve the problems of low utilization rate of cobalt element, high cost, low recovery rate, etc., and achieve simplified production The effect of process flow, catalyst cost saving and equipment cost saving
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Embodiment 1
[0020] Initial reaction: Add 1.4L of raw material olefins into a 2L tank-type batch reactor, add 5g of cobalt(II) acetylacetonate, and 5g of tri-n-butylphosphine, vacuumize the system and replace it with nitrogen for 5 times, and add in a volume ratio of 1:2 Mix CO and hydrogen to a pressure of 7MPa, start stirring and raise the temperature to 180°C to start the reaction, and the pressure is about 9MPa at this time. Supplement the mixed gas of CO and hydrogen to ensure the pressure of the system at 8-9MPa, and maintain the volume ratio of the mixed gas of CO and hydrogen in the system at 1:2. After 6 hours of reaction, the pressure does not drop anymore, and the reaction ends.
[0021] After cooling down, the remaining gas was removed, and the reaction solution was taken out. The reaction solution was wine red with a small amount of black precipitation. After filtration, the reaction solution was directly distilled to obtain unreacted olefins, alcohol products and black heavy ...
Embodiment 2
[0027] Initial reaction: Add 1.4L of raw material olefin, 5g of cobalt(II) acetylacetonate, and 5g of tri-tert-butylphosphine into a 2L tank-type batch reactor. The system is vacuumed and replaced with nitrogen for 5 times, and supplemented at a volume ratio of 2:1. Mix CO and hydrogen to a pressure of 10MPa, start stirring and raise the temperature to 200°C to start the reaction. At this time, the pressure is about 12MPa. Supplement the mixed gas of CO and hydrogen to ensure that the system pressure is at 12MPa, and maintain the volume ratio of the mixed gas of CO and hydrogen in the system at 2:1. After 5 hours of reaction, the pressure does not drop any more, and the reaction ends.
[0028]After cooling down, the remaining gas was removed, and the reaction solution was taken out. The reaction solution was wine red with a small amount of black precipitation. After filtration, the reaction solution was directly distilled to obtain unreacted olefins, alcohol products and black...
Embodiment 3
[0034] Initial reaction: Add 1.4L of raw material olefins into a 2L tank-type batch reactor, add 5g of cobalt acetylacetonate and 5g of triisobutylphosphine phosphine, vacuumize the system and replace it with nitrogen for 5 times, supplement CO and Mix hydrogen gas to a pressure of 10MPa, start stirring and raise the temperature to 180°C to start the reaction. At this time, the pressure is about 12MPa. Supplement the mixed gas of CO and hydrogen to ensure the pressure of the system at 12MPa, and maintain the volume ratio of the mixed gas of CO and hydrogen in the system at 1:1. After 7 hours of reaction, the pressure will not drop and the reaction will end.
[0035] After cooling down, the remaining gas was removed, and the reaction solution was taken out. The reaction solution was wine red with a small amount of black precipitation. After filtration, the reaction solution was directly distilled to obtain unreacted olefins, alcohol products and black heavy components.
[0036...
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