Reactive distillation method and device for low-pressure carbonylation of butyraldehyde
A technology of carbonylation and reactive distillation tower, which is applied in the field of reactive distillation of low-pressure carbonylation of butyraldehyde, can solve the problems of no relevant patents, etc., and achieve the effect of reducing operating costs and saving equipment investment
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Embodiment 1
[0022]In this example, the pressure of the reactive distillation tower is 1.7Mpa, the temperature of the reaction section is 110°C, the catalyst is rhodium-triphenylphosphine, the solvent is the trimer of butyraldehyde, the mass fraction of rhodium in the reaction solution is 250ppm, and the triphenylphosphine The mass fraction of phosphine is 8%, the molar ratio of feed composition propylene and synthesis gas is 1:2; the pressure of flash tower is 1Mpa; the pressure of absorption tower is 0.6Mpa; the pressure of stripper is 3Mpa, the crude butyraldehyde solution and synthesis gas The molar ratio is 1:1. Finally, the recovery rate of propylene in the non-condensable gas at the top of the reactive distillation column was 92%, and the mass purity of mixed butyraldehyde was 99%.
Embodiment 2
[0024] In this example, the pressure of the reactive distillation tower is 1.9Mpa, the temperature of the reaction section is 80°C, the catalyst is rhodium-triphenylphosphine, the solvent is a trimer of butyraldehyde, the mass fraction of rhodium in the reaction solution is 350ppm, and the triphenylphosphine The mass fraction of phosphine is 12%, the molar ratio of feed composition propylene and synthesis gas is 1:3; the pressure of the flash tower is 0.1Mpa; the pressure of the absorption tower is 1Mpa; The gas molar ratio is 1:1. Finally, the recovery rate of propylene in the non-condensable gas at the top of the reactive distillation column was 93%, and the mass purity of mixed butyraldehyde was 99.5%.
Embodiment 3
[0026] In this example, the pressure of the reactive distillation column is 1.8Mpa, the temperature of the reaction section is 100°C, the catalyst is rhodium-triphenylphosphine, the solvent is a trimer of butyraldehyde, the mass fraction of rhodium in the reaction solution is 450ppm, and the triphenylphosphine The mass fraction of phosphine is 10%, the molar ratio of feed composition propylene to synthesis gas is 1:2.5; the pressure of flash tower is 0.5Mpa; the pressure of absorption tower is 0.1Mpa; the pressure of stripping tower is 1Mpa, the crude butyraldehyde solution and synthesis The gas molar ratio is 1:1. Finally, the recovery rate of propylene in the non-condensable gas at the top of the reactive distillation column is 90%, and the mass purity of mixed butyraldehyde is 99.2%.
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