A method for preparing α-hemihydrate gypsum with alcohol aqueous solution as crystallization medium
A technology of hemihydrate gypsum and alcohol aqueous solution, which is applied in the field of preparing α-hemihydrate gypsum by the normal pressure solution method, and achieves the effects of easy reuse, simple operation and low energy consumption
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Embodiment 1
[0035] according to figure 2 In the process flow shown, an ethanol aqueous solution with a mass concentration of 60% is prepared, and dihydrate gypsum is added and mixed to form a slurry with a solid mass concentration of 3%. Transport the slurry to the crystallization reactor, maintain the temperature of the slurry in the reactor at 80°C, and control the residence time of the slurry for 6.5 hours. After the conversion is completed, extract the slurry and send it to a vacuum belt filter for solid-liquid separation. The separated solid phase is washed with hot water at 50°C, and then sent to an oven to dry at 40°C, and it is α-hemihydrate gypsum after collection. The separated liquid phase is directly reused or combined with washing water for distillation to recover ethanol.
Embodiment 2
[0037] according to figure 2 As shown in the process flow, prepare ethanol-isopropanol-water solution with a mass concentration of 44%, wherein the mass ratio of ethanol to isopropanol is 1.0, add dihydrate gypsum and mix to form a slurry with a solid mass concentration of 36%. Transport the slurry to the crystallization reactor, maintain the temperature of the slurry in the reactor at 90°C, and control the residence time of the slurry for 4.3 hours. After the conversion is completed, extract the slurry and send it to a vacuum belt filter for solid-liquid separation. The separated solid phase was washed with hot water at 54°C, then sent to an oven for drying at 77°C, and the collected solid phase was α-hemihydrate gypsum. The separated liquid phase is directly reused or combined with washing water for distillation to recover ethanol and isopropanol.
Embodiment 3
[0039] according to figure 2 In the process flow shown, an aqueous solution of n-propanol with a mass concentration of 50% is prepared, and dihydrate gypsum is added and mixed to form a slurry with a solid mass concentration of 18%. Transport the slurry to the crystallization reactor, maintain the temperature of the slurry in the reactor at 82°C, and control the residence time of the slurry for 17.2 hours. After the conversion is completed, extract the slurry and send it to a plate and frame filter press for solid-liquid separation. The separated solid phase is washed with hot water at 70°C, and then sent to an airflow dryer to dry at 96°C. After collection, it is α-hemihydrate gypsum. The separated liquid phase is directly reused or combined with washing water for distillation to recover n-propanol.
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