Continuous synthetic method of p-phenylenediamine
A technology of p-phenylenediamine and its synthesis method, which is applied in chemical instruments and methods, preparation of amino compounds, preparation of organic compounds, etc., can solve the problems of high technical difficulty, difficult recovery, high price, etc., and achieve simple and easy process route The effect of control and easy availability of raw materials
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Embodiment 1
[0022] Add a supported nickel-based catalyst in a fixed-bed reactor, the solvent is methanol, the mass ratio of methanol to p-nitroaniline is 2:1, the ratio of hydrogen to p-nitroaniline is 5:1, and the reaction temperature is 45°C , the reaction pressure is 3 MPa, and the volume space velocity of p-nitroaniline is 0.8h -1 , the crude product of p-phenylenediamine is firstly decompressed to separate hydrogen, and p-phenylenediamine and methanol solvent are separated by continuous rectification process to separate methanol and high-purity p-phenylenediamine. Gas chromatography analysis showed that the purity of p-phenylenediamine was 99.99%, and the conversion rate of p-nitroaniline was 100%.
Embodiment 2
[0024] Add a supported nickel-based catalyst in a fixed-bed reactor, the solvent is methanol, the mass ratio of methanol to p-nitroaniline is 3:1, the ratio of hydrogen to p-nitroaniline is 10:1, and the reaction temperature is 50°C , the reaction pressure is 4 MPa, and the volume space velocity of p-nitroaniline is 1.0h -1 , the crude product of p-phenylenediamine is firstly decompressed to separate hydrogen, and p-phenylenediamine and methanol solvent are separated by continuous rectification process to separate methanol and high-purity p-phenylenediamine. Gas chromatography analysis showed that the purity of p-phenylenediamine was 99.99%, and the conversion rate of p-nitroaniline was 100%.
Embodiment 3
[0026] Add a supported nickel-based catalyst into a fixed-bed reactor, the solvent is ethanol, the mass ratio of ethanol to p-nitroaniline is 5:1, the ratio of hydrogen to p-nitroaniline is 15:1, and the reaction temperature is 55°C , the reaction pressure is 4.5MPa, and the volume space velocity of p-nitroaniline is 1.0h -1 , the crude product of p-phenylenediamine is firstly decompressed to separate hydrogen, and p-phenylenediamine and methanol solvent are separated by continuous rectification process to separate methanol and high-purity p-phenylenediamine. Gas chromatography analysis showed that the purity of p-phenylenediamine was 99.99%, and the conversion rate of p-nitroaniline was 100%.
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