Method for preparing taurine through solid isethionic acid sodium salt
A technology of sodium isethionate and taurine, which is applied in the fields of sulfonic acid preparation, sulfonate preparation, organic chemistry, etc., and can solve problems such as environmental pollution
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Embodiment 1
[0025] will be 6.0m 3 , 42wt% of the addition liquid is transported to the first-effect evaporator and concentrated to 5m 3 , 47 wt%, into the second effect evaporator, concentrated to 4.2m 3 , 55 wt%, into the three-effect evaporator, concentrated to 3.0m 3 , 70%, and then enter the continuous crystallizer. After 1~3h, the solid sodium hydroxide 2.8T is separated by a fully automatic centrifuge at 50~60°C. Put 2.8T solid sodium hydroxide into 5 m 3 In the batching tank, add 3.5 m 3 Dilute ammonia water, the total volume of the material is 4.8 m 3 , will be 4.8 m 3 The material is transported to the ammonia reactor, replenished with water and ammonia until the ammonia content is 20 wt%, and the total volume of the material after the ammonia is 20 m 3 . The material after the ammonia pass through 5 m 3 The flow rate of / h enters the high temperature and high pressure synthesis tower, the tower temperature is controlled at 252°C, and the pressure is controlled at 20.0MP...
Embodiment 2
[0029] will be 3.2m 3 , 43wt% of the addition liquid is transported to the first-effect evaporator and concentrated to 2.6m 3 , 48 wt%, into the second effect evaporator, concentrated to 2.2m 3 , 56 wt%, into the three-effect evaporator, concentrated to 1.6m 3 , 72%, and then enter the continuous crystallizer, after 1~3h, at 50~60℃, the solid sodium hydroxide 1.5T is separated by a fully automatic centrifuge. Put 1.5T solid sodium hydroxide into 3m 3 In the batching tank, add 1.8m 3 Dilute ammonia water, the total volume of the material is 2.6m 3 , will be 2.6 m 3 The material is transported to the ammonia reactor, replenished with water and ammonia until the ammonia content is 21 wt%, and the total volume of the material after the ammonia is 10 m 3 . The material after the ammonia pass through 5m 3 The flow rate of / h enters the high temperature and high pressure synthesis tower, the tower temperature is controlled at 256°C, and the pressure is controlled at 21.0MPa....
Embodiment 3
[0033] will be 3.2m 3 , 40wt% of the addition liquid is transported to the first-effect evaporator and concentrated to 2.6m 3 , 47 wt%, into the second effect evaporator, concentrated to 2.2m 3 , 55 wt%, into the three-effect evaporator, concentrated to 1.6m 3 , 70%, and then enter the continuous crystallizer, after 1~3h, at 50~60℃, the solid sodium hydroxide 1.5T is separated by a fully automatic centrifuge. Put 1.5T solid sodium hydroxide into 3 m 3 In the batching tank, add 1.8 m 3 dilute ammonia, the total volume of the material is 2.6 m 3 , will be 2.6 m 3 The material is transported to the ammonia reactor, replenished with water and ammonia until the ammonia content is 20 wt%, and the total volume of the material after the ammonia is 10 m 3 . The material after the ammonia pass through 4.5 m 3 The flow rate of / h enters the high temperature and high pressure synthesis tower, the tower temperature is controlled at 258°C, and the pressure is controlled at 21.0MPa....
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