Method for preparing nonanal by adopting loop reactor and venturi ejector for preparing nonanal
A technology of loop reactor and injector, which is applied in the direction of carbon monoxide reaction preparation, chemical instruments and methods, catalytic reaction, etc., can solve the problems of poor industrial application prospects, stay in the research stage, catalyst loss, etc., and reduce the loss of precious metal rhodium content efficiency, reduce catalyst cost, and increase the effect of interfacial contact
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Embodiment 1
[0036] In the loop reactor of 5L (reactor volume 5L), add TPPTS and RhCl 3 ·3H 2 The catalyst solution (water phase) formed by dissolving O in water and the reaction raw material 1-octene (organic phase), the volume ratio of the catalyst water phase and the reactant organic phase is controlled to be 1.3:1, and the molar ratio of TPPTS to Rh element is 50 :1, the molar ratio of reactant 1-octene to Rh element is 2000:1. The total volume of materials in the reactor is 4025ml, and the liquid level in the reactor of the loop reactor is 75±2% of the height of the entire reactor.
[0037] Feed synthesis gas (hydrogen to carbon monoxide volume ratio 1:1) into the reactor to a system pressure of 1 MPa, turn on the circulation pump 4 to allow the liquid in the kettle to flow slowly, vent, repeat 6 times to replace the air in the loop reactor, and heat up (heating time About 15 minutes) to the preset reaction temperature of 110°C, immediately fill the synthesis gas to the reaction pre...
Embodiment 2
[0041] In the loop reactor of 5L (reactor volume 5L), add TPPTS and RhCl 3 ·3H 2 The catalyst solution (water phase) formed by dissolving O in water and the reaction raw material 1-octene (organic phase), the volume ratio of the catalyst water phase and the reactant organic phase is 2.1:1, and the molar ratio of TPPTS to Rh element is 70: 1. The molar ratio of reactant 1-octene to Rh element is 1450:1. The total volume of materials in the reactor is 4025ml, and the liquid level in the reactor of the loop reactor is 75±2% of the height of the entire reactor.
[0042] Feed synthesis gas (hydrogen to carbon monoxide volume ratio 1:1) into the reactor to a system pressure of 1 MPa, turn on the circulation pump 4 to allow the liquid in the kettle to flow slowly, vent, repeat 6 times to replace the air in the loop reactor, and heat up (heating time About 15 minutes) to the preset reaction temperature of 90°C, immediately fill the synthesis gas to the reaction pressure of 2.3MPa, a...
Embodiment 3
[0046] In the loop reactor of 5L (reactor volume 5L), add TPPTS and RhCl 3 ·3H 2 The catalyst solution (water phase) formed by dissolving O in water and the reaction raw material 1-octene (organic phase), the volume ratio of the catalyst water phase and the reactant organic phase is 0.7:1, and the molar ratio of TPPTS to Rh element is 28: 1. The molar ratio of reactant 1-octene to Rh element is 2230:1. The total volume of materials in the reactor is 4025ml, and the liquid level in the reactor of the loop reactor is 75±2% of the height of the entire reactor.
[0047] Feed synthesis gas (hydrogen to carbon monoxide volume ratio 1:1) into the reactor to a system pressure of 1 MPa, turn on the circulation pump 4 to allow the liquid in the kettle to flow slowly, vent, repeat 6 times to replace the air in the loop reactor, and heat up (heating time About 15 minutes) to the preset reaction temperature of 90°C, immediately fill the synthesis gas to the reaction pressure of 1.6MPa, a...
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