Method for producing etidronic acid
A technology of hydroxyethylene diphosphonic acid and production method is applied in the field of process improvement of the production process of water treatment agent-hydroxyethylene diphosphonic acid, and can solve the problems of severe hydrolysis, unstable reaction, difficult control and the like, Achieve stable reaction, reduce side reactions, and reduce production costs
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Embodiment 1
[0030] 1): Add 75Kg of industrial glacial acetic acid and 62Kg of 31% industrial hydrochloric acid into the reaction kettle. The configuration of the reaction kettle is shown in the figure, start stirring, pass cooling water through the interlayer of the reaction kettle, slowly add 165Kg of phosphorus trichloride, control the addition speed, and maintain the internal temperature Not higher than 45°C. The hydrogen chloride gas produced by the reaction enters the multi-stage absorption tank for absorption after being cooled in series and washing towers.
[0031] 2): After adding phosphorus trichloride, stir and heat up to 45-60°C.
[0032] 3): Keep the acetyl chloride in a state of total reflux, and stir and react at 60-75°C for 3 hours.
[0033] 4): Raise the temperature to 70°C and then add 36Kg of excess acetyl chloride through the feeding tank to maintain a high reflux ratio state.
[0034] 5): Stir and react at 65-80°C for 3 hours, and distill off excess acetyl chloride t...
Embodiment 2
[0041] Add 40Kg of industrial glacial acetic acid, 100Kg of recovered washing solution containing 35.7% acetic acid and 21.4% hydrogen chloride into the reaction kettle, start stirring, and slowly add 165Kg of phosphorus trichloride. Other operation is the same as embodiment 1, reclaims acetyl chloride 32Kg in the reaction, obtains 50% product 230Kg after hydrolysis, 85% acetic acid 27.6Kg, dilute acetic acid-hydrochloric acid mixture: 77Kg, 30% hydrochloric acid 391Kg. Example 3
Embodiment 3
[0042] Add 48Kg of recovered 91% acetic acid, 91Kg of recovered washing solution containing 35.7% acetic acid and 21.4% hydrogen chloride into the reactor, start stirring, and slowly add 165Kg of phosphorus trichloride. Other operations were the same as in Example 1, and 31Kg of acetyl chloride was collected and hydrolyzed with water to obtain 228Kg of 50% HEDP product, 28Kg of 85% acetic acid solution, and 82Kg of acetic acid-hydrochloric acid mixture. Example 4
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