A kind of fumaric acid production process
A production process, technology of fumaric acid, applied in the direction of carboxylate preparation, organic compound/hydride/coordination complex catalyst, organic compound preparation, etc., can solve the problem of yellow color of finished fumaric acid and difficult Degradation, wastewater treatment and discharge difficulties, etc., to achieve the effect of reducing individual costs
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Embodiment 1
[0021] ①, set the volume to 6M 3 The maleic acid aqueous solution is added in the decolorization kettle, and the active carbon that is 0.1% by weight relative to the maleic acid aqueous solution is added simultaneously for stirring and decolorization, and the decolorization time is 20 minutes;
[0022] ②. Filter the decolorized maleic acid aqueous solution to remove activated carbon and impurities, and then pump it into the reaction kettle;
[0023] ③. Measure the volume of acid water in the reactor, calculate the maleic acid content according to the measured acid water concentration, and control the acid water concentration at 35%;
[0024] 4. Stir and heat the reaction kettle, when the temperature is at 45°C, add urea with a relative acidic maleic acid weight of 0.5%, and the reaction time is 10 minutes;
[0025] ⑤. After continuing to raise the temperature by 2°C, add diammonium hydrogen phosphate with a maleic acid weight of 0.6 relative to acid water, close the steam val...
Embodiment 2
[0030] ① Set the volume to 9M 3 The maleic acid aqueous solution is added in the decolorization kettle, and the active carbon that is 0.3% relative to the maleic acid aqueous solution weight ratio is added simultaneously for stirring and decolorization, and the decolorization time is 40 minutes;
[0031] ②. Filter the decolorized maleic acid aqueous solution to remove activated carbon and impurities, and then pump it into the reaction kettle;
[0032] ③. Measure the volume of acid water in the reactor, calculate the maleic acid content according to the measured acid water concentration, and control the acid water concentration at 40%;
[0033] 4. Stir and heat the reaction kettle, when the temperature is at 65°C, add urea with a maleic acid weight of 1.8% in relative acid water, and the reaction time is 20 minutes;
[0034] 5. After continuing to heat up 8°C, add diammonium hydrogen phosphate with a weight of 2% maleic acid in relative acid water, close the steam valve, and t...
Embodiment 3
[0039] ① Set the volume to 9M 3 The maleic acid aqueous solution is added in the decolorization kettle, and the active carbon that is 0.3% relative to the maleic acid aqueous solution weight ratio is added simultaneously for stirring and decolorization, and the decolorization time is 40 minutes;
[0040] ②. Filter the decolorized maleic acid aqueous solution to remove activated carbon and impurities, and then pump it into the reaction kettle;
[0041] ③. Measure the volume of acid water in the reactor, calculate the maleic acid content according to the measured acid water concentration, and control the acid water concentration at 38%;
[0042] 4. Stir and heat the reaction kettle, when the temperature is at 60°C, add urea with a relative acidic maleic acid weight of 1.5%, and the reaction time is 18 minutes;
[0043] 5. After continuing to raise the temperature by 8°C, add diammonium hydrogen phosphate whose weight of maleic acid is 1.8% in relative acid water, close the stea...
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