Industrial method for simultaneously preparing propaldehyde and butyraldehyde by catalytic dry gas concentrating gas
An industrial method, the technology of propionaldehyde, applied in the direction of carbon monoxide reaction preparation, organic chemistry, etc., can solve problems such as static mixers that have not been seen
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Embodiment 1
[0028]The aqueous solution of the rhodium-phosphine complex catalyst with a rhodium content of 1×10-4 mole / liter to 1×10-2 mole / liter is sent into the static mixing reactor through a circulating pump, and the hot water at about 90°C is sent through static mixing The jacket of the reactor, the circulating liquid is preheated to 70 °C, and then the catalytic dry gas is enriched to enrich the mixed gas (85% ethylene, 8% propylene) to the molar ratio of ethylene and propylene to hydrogen and carbon monoxide at 1:1.05 : 1.05 mixed feed gas, sent to the static mixing reactor in the same direction as the circulating liquid, under the action of the catalyst, ethylene, propylene, hydrogen and carbon monoxide undergo hydroformylation reaction. While feeding the mixed gas, change the hot water passing into the static mixing reactor into cooling water, and control the temperature in the reactor to be stable at about 70°C. After the reaction, the gas-liquid mixture enters the circulation t...
Embodiment 2
[0034] The use of catalyzer, the content of raw material olefin and operating process are with embodiment 1, and processing condition and reaction result are as follows:
[0035] Reaction pressure: 2.0MPa Reaction temperature: 80°C
[0036] Ethylene, propylene: hydrogen: carbon monoxide: 1:1.10:1.05 (molar ratio)
[0037] The space velocity of the fluid in the static mixing reactor: 0.5m / s
[0038] The gas flow rate into the static mixing reactor
[0039] Ratio to circulating fluid flow rate (volume ratio): 320
[0040] Ethylene, propylene conversion rate: 97%
[0041] Ethylene, propylene selectivity: 94%
[0042] N-butyraldehyde: isobutyraldehyde: 16:1
Embodiment 3
[0044] The use of catalyzer, the content of raw material olefin and operating process are with embodiment 1, and processing condition and reaction result are as follows:
[0045] Reaction pressure: 2.0MPa Reaction temperature: 90°C
[0046] Ethylene, propylene: hydrogen: carbon monoxide: 1:1.10:1.05 (molar ratio)
[0047] The space velocity of the fluid in the static mixing reactor: 0.5m / s
[0048] The gas flow rate into the static mixing reactor
[0049] Ratio to circulating fluid flow rate (volume ratio): 320
[0050] Ethylene, propylene conversion rate: 98%
[0051] Ethylene, propylene selectivity: 93%
[0052] N-butyraldehyde: isobutyraldehyde: 13:1
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