Preparation of nitrile compounds
A compound and organic compound technology, which is applied in the field of preparation of polynitrile compounds, can solve the problems of single-flow yield drop, low reaction rate, and reduced productivity of nitrile compounds, and achieve the goals of suppressing side reactions, reducing losses, and high yields Effect
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Embodiment 1
[0040] The ammoxidation reaction of m-xylene was carried out using the ammoxidation reactor shown in FIG. 1 . 2.3 tons of the above-prepared mobile catalyst were filled in an ammoxidation reactor, and air, m-xylene (MX), and ammonia gas were preheated at 180°C and supplied to the reactor. Supply rate is MX 266kg / hr, MTN 40.0kg / hr, ammonia 412kg / hr, air 1570Nm 3 / hr. The reaction is carried out at a reaction pressure of 0.08Mpa to obtain isophthalonitrile (IPN). The reaction temperature was set at 427°C. The freshly supplied MX (new supply flow) was substantially the same as the comparative example, 241.8 kg / hr, the circulating supply flow MX was 24.2 kg / hr, and the MTN was 40.0 kg / hr. The molar ratio of the flow rate of the mononitrile compound at the reactor outlet to the total flow rate of the poly-substituted organic compound and the mononitrile compound supplied to the reactor was 12.0 mol%.
[0041] The reaction gas was analyzed, containing MX 24.2kg / hr, IPN 257.2kg / h...
Embodiment 2
[0044] The ammoxidation reaction of m-xylene was carried out using the ammoxidation reactor shown in FIG. 1 . 2.3 tons of the above-prepared mobile catalyst were filled in an ammoxidation reactor, and air, m-xylene (MX), and ammonia gas were preheated at 180°C and supplied to the reactor. Supply rate is MX245.6kg / hr, MTN 10.7kg / hr, ammonia 350kg / hr, air 1320Nm 3 / hr. The reaction is carried out at a reaction pressure of 0.08Mpa to obtain isophthalonitrile (IPN). The reaction temperature was set at 427°C. The freshly supplied MX (new supply flow) was 242 kg / hr as in the comparative example, the circulating supply flow MX was 3.6 kg / hr, and the MTN was 10.7 kg / hr. The molar ratio of the flow rate of the mononitrile compound at the reactor outlet to the total flow rate of the MX poly-substituted organic compound and the mononitrile compound supplied to the reactor was 3.8 mol%.
[0045] The reaction gas was analyzed, containing MX 3.6kg / hr, IPN 247kg / hr, MTN 10.7kg / hr.
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