Method for continuous synthesis of ligustral in fixed bed reactor
A technology of fixed bed reactor and privet aldehyde, which is applied in chemical instruments and methods, preparation of organic compounds, preparation of carbon-based compounds, etc., can solve problems such as reaction temperature, high pressure, acrolein polymerization, difficult temperature control, etc. Achieve the effect of avoiding polymerization, low pressure and avoiding violent reaction
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Embodiment 1
[0039] The method for continuously synthesizing privetal in a kind of fixed-bed reactor of embodiment 1
[0040] Include the following steps:
[0041] (1) Mixing of raw materials
[0042] 165.1g (2.01mol) 2-methyl-1,3-pentadiene and 114.9g (2.05mol) acrolein are mixed, and the molar ratio of 2-methyl-1,3-pentadiene and acrolein in the mixture is 1:1.02, put the mixed solution in the raw material solution 1 storage tank.
[0043] (2) Air replacement, preheating
[0044]The fixed-bed reactor 4 passes nitrogen from the nitrogen buffer tank 3 to replace the air, and the temperature is raised for preheating.
[0045] (3) Continuous response
[0046] When the temperature of the catalyst bed in the reactor reaches the reaction temperature, feed the raw material liquid 1 into the reactor through the double-plunger micrometering pump 2, and fill the fixed bed reactor 4 with phosphomolybdic acid modified Al 2 o 3 Catalyst, catalyst loading is 15g, reaction temperature is 36°C, rea...
Embodiment 2
[0049] The method for continuously synthesizing privetal in a kind of fixed-bed reactor of embodiment 2
[0050] Include the following steps:
[0051] (1) Mixing of raw materials
[0052] 165.1g (2.01mol) 2-methyl-1,3-pentadiene and 129.6g (2.31mol) acrolein are mixed, and the molar ratio of 2-methyl-1,3-pentadiene and acrolein in the mixture is 1:1.15, put the mixed solution in the raw material solution 1 storage tank.
[0053] (2) Air replacement, preheating
[0054] The fixed-bed reactor 4 passes nitrogen from the nitrogen buffer tank 3 to replace the air, and the temperature is raised for preheating.
[0055] (3) Continuous response
[0056] When the temperature of the catalyst bed in the reactor reaches the reaction temperature, feed the raw material liquid 1 into the reactor through the double-plunger micrometering pump 2, and fill the fixed bed reactor 4 with phosphomolybdic acid modified Al 2 o 3 Catalyst, catalyst loading is 20g, reaction temperature is 40°C, re...
Embodiment 3
[0059] The method for continuously synthesizing privetal in a kind of fixed-bed reactor of embodiment 3
[0060] Include the following steps:
[0061] (1) Mixing of raw materials
[0062] 165.1g (2.01mol) 2-methyl-1,3-pentadiene and 123.9g (2.21mol) acrolein are mixed, and the molar ratio of 2-methyl-1,3-pentadiene and acrolein in the mixture is 1:1.10, put the mixed solution in the raw material solution 1 storage tank.
[0063] (2) Air replacement, preheating
[0064] The fixed-bed reactor 4 passes nitrogen from the nitrogen buffer tank 3 to replace the air, and the temperature is raised for preheating.
[0065] (3) Continuous response
[0066] When the temperature of the catalyst bed in the reactor reaches the reaction temperature, feed the raw material liquid 1 into the reactor through the double plunger micro metering pump 2, and fill the fixed bed reactor 4 with phosphotungstic acid modified Al 2 o 3 Catalyst, catalyst loading is 20g, reaction temperature is 40°C, r...
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