Method for producing pyromellitic dianhydride by continuous oxidation of durene at low temperature in liquid phase
A technology of pyromellitic dianhydride and pyromellitic acid, which is applied in the field of low-temperature liquid-phase continuous oxidation production technology, to achieve the effects of easy implementation, reduced corrosion, and reduced usage
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Embodiment 1
[0033] A method for producing pyromellitic dianhydride by low-temperature liquid-phase continuous oxidation of durene, comprising the steps of:
[0034] (1) The mixed solution of durene, acetic acid and cobalt-manganese-bromine-zirconium-guanidine catalyst is continuously poured into the oxidation reaction tower, and the cobalt-manganese-bromine-zirconium-guanidine catalyst includes cobalt acetate, manganese acetate, Tetrabromoethane, zirconium acetate and guanidine acetate, in the mixed liquor, acetic acid is as solvent, and mesylene is 223.35 kg, and acetic acid is 1272 kg, and catalyzer uses cobalt acetate 1.35 kg, manganese acetate 1.5kg, tetrabromoethane 0.825 kg, 0.48 kg of zirconium acetate and 0.495 kg of guanidine acetate, the corresponding weight contents of each substance are: 14.89% of durene, 84.8% of acetic acid, 0.09% of cobalt acetate, 0.1% of manganese acetate, and 0.055% of tetrabromoethane, Zirconium acetate is 0.032%, guanidine acetate is 0.033%; when the l...
Embodiment 2
[0040] A method for producing pyromellitic dianhydride by low-temperature liquid-phase continuous oxidation of durene, comprising the steps of:
[0041] (1) The mixed solution of durene, acetic acid and cobalt-manganese-bromine-zirconium-guanidine catalyst is continuously poured into the oxidation reaction tower, and the cobalt-manganese-bromine-zirconium-guanidine catalyst includes cobalt acetate, manganese acetate, Tetrabromoethane, zirconium acetate and guanidine acetate, in the mixed liquor, acetic acid is as solvent, and mesylene is 291 kg, and acetic acid is 1206 kg, and catalyst uses cobalt acetate 0.525 kg, manganese acetate 1.5kg, tetrabromoethane 0.375 kg, 0.105 kg of zirconium acetate and 0.495 kg of guanidine acetate, the corresponding weight contents of each substance are: 19.4% of durene, 80.4% of acetic acid, 0.035% of cobalt acetate, 0.1% of manganese acetate, and 0.025% of tetrabromoethane, Zirconium acetate is 0.007%, guanidine acetate is 0.033%; when the liq...
Embodiment 3
[0047] A method for producing pyromellitic dianhydride by low-temperature liquid-phase continuous oxidation of durene, comprising the steps of:
[0048] (1) The mixed solution of durene, acetic acid and cobalt-manganese-bromine-zirconium-guanidine catalyst is continuously poured into the oxidation reaction tower, and the cobalt-manganese-bromine-zirconium-guanidine catalyst includes cobalt acetate, manganese acetate, Tetrabromoethane, zirconium acetate and guanidine acetate, in the mixed liquor, acetic acid is used as solvent, and mesylene is 236.25 kg, and acetic acid is 1260.75 kg, and catalyst uses cobalt acetate 1.05 kg, manganese acetate 1.005 kg, tetrabromoethane 0.285 kg, 0.45 kg of zirconium acetate and 0.21 kg of guanidine acetate, the corresponding weight contents of each substance are: 15.75% of durene, 84.05% of acetic acid, 0.07% of cobalt acetate, 0.067% of manganese acetate, and 0.019% of tetrabromoethane, Zirconium acetate is 0.03%, guanidine acetate is 0.014%;...
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