Method for producing adipic acid by oxidizing cyclohexane by utilizing air based on gas-liquid-solid multiphase reaction and separation synchronization reactor
A multiphase reaction and air oxidation technology, which is applied in the direction of oxidative preparation of carboxylic acid, chemical instruments and methods, separation/purification of carboxylic acid compounds, etc., can solve the problem of increasing equipment investment and energy consumption, pollution of solvent environment, and reaction products Reduce selectivity and yield, increase the residence time of reaction products and other problems, achieve high-selectivity continuous production, prevent off-site excessive reaction, and solve the effects of complex equipment structure
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Embodiment 1
[0035] Attached figure 1 The shown gas-liquid-solid multiphase reaction separation synchronous reactor carries out the air oxidation of cyclohexane to prepare adipic acid products; wherein, the diameter-to-height ratio of the bubbling gravity reaction tower is 1:35; the ratio of the length of the gravity settling plate to the diameter of the tower is 1 : 1.2; the included angle of the gravity settling plate along the tower axis is 55°; there are two constant temperature settling towers, the constant temperature settling tower I and the constant temperature settling tower II; the outlet of the reaction liquid is 3 / 7 away from the height of the tower body .
[0036] Copper tetraphenylporphyrin (concentration: 30ppm) is added to the cyclohexane raw material as a catalyst, and the mixed solution enters the constant temperature settling tower I and the bubbling gravity reaction tower from the upper reaction material inlet of the constant temperature settling tower I, and is filled ...
Embodiment 2
[0040] Attached figure 1 The gas-liquid-solid multiphase reaction separation synchronous reactor is used to prepare adipic acid products by air oxidation of cyclohexane; wherein, the diameter-to-height ratio of the bubbling gravity reaction tower is 1:25; the ratio of the length of the gravity settling plate to the diameter of the tower is 1 : 1.1; the included angle of the gravity settling plate inclined along the tower axis is 65°; there are two constant temperature settling towers, the constant temperature settling tower Ⅰ and the constant temperature settling tower Ⅱ; .
[0041] Tetraphenylporphyrin iron μ-dimer (concentration: 20ppm) is added to the cyclohexane raw material as a catalyst, and the mixed solution enters the constant temperature settling tower I and the bubbling gravity reaction tower from the upper reaction material inlet of the constant temperature settling tower I, and is filled with In the oxidation zone of the constant temperature settling tower Ⅰ and ...
Embodiment 3
[0046] Attached figure 1 The gas-liquid-solid multiphase reaction separation synchronous reactor is used to prepare adipic acid products by air oxidation of cyclohexane; wherein, the diameter-to-height ratio of the bubbling gravity reaction tower is 1:32; the ratio of the length of the gravity settling plate to the diameter of the tower is 1 : 0.9; The included angle of the gravity settling plate along the tower axis is 50°; there are two constant temperature settling towers, the constant temperature settling tower I and the constant temperature settling tower II; .
[0047] Cobalt naphthenate (concentration: 100ppm) is added to the cyclohexane raw material as a catalyst, and the mixed liquid enters the constant temperature settling tower I and the bubbling gravity reaction tower from the upper reaction material inlet of the constant temperature settling tower I, and is filled with the constant temperature settling tower I and the bubbling gravity reaction tower. In the oxida...
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