Method for processing sucralfate crystal mother solution and obtaining by-product sucrose octasulphate by nanofiltration membrane technology and application thereof
A technology of sucrose octasulfate and crystallization mother liquor, applied in chemical instruments and methods, osmotic/dialysis water/sewage treatment, sugar derivatives, etc., can solve problems such as large pollution, restrict the development of sucralfate, pollute the environment, etc. Good economic value and social value, conducive to sustainable development, the effect of solving environmental problems
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Embodiment 1
[0028] Add acid to the sucralfate mother liquor in the storage tank to adjust the pH to 3.0, pass through a 0.5μm filter to the circulation tank, and then inject it into the three-stage nanofiltration membrane cooperative concentration circulation device by the pressure pump, the interception of the first-stage nanofiltration membrane The molecular weight is 1400-1500 Daltons, the molecular weight cut-off of the second-stage nanofiltration membrane is 800-1000 Daltons, the molecular weight cut-off of the second-stage nanofiltration membrane is 500-600 Daltons, and the molecular weight cut-off of the third-stage nanofiltration membrane is The operating conditions are the same: the operating pressure is 0.5Mpa, and the operating temperature is 30°C; after concentration by nanofiltration, a concentrated solution with a sucrose octasulfate content of 4.5% is obtained, the rejection rate is 97.0%, and the COD value of the solution obtained by dialysis is 438.5mg / L .
Embodiment 2
[0030] Add acid to the sucralfate mother liquor in the storage tank to adjust the pH to 3.0, pass through a 0.5μm filter to the circulation tank, and then inject it into the three-stage nanofiltration membrane cooperative concentration circulation device by the pressure pump, the interception of the first-stage nanofiltration membrane The molecular weight is 1400-1500 Daltons, the operating pressure is 0.5Mpa, and the operating temperature is 10°C; the molecular weight cut-off of the second-stage nanofiltration membrane is 800-1000 Daltons, the operating pressure is 0.8Mpa, and the operating temperature is 30°C; The molecular weight cut-off of the third-stage nanofiltration membrane is 500-600 Daltons, the operating pressure is 1.0Mpa, and the operating temperature is 40°C; after being concentrated by the third-stage nanofiltration, a concentrated solution with a sucrose octasulfate content of 5.0% is obtained, and the rejection rate 99.0%, the COD value of the solution obtaine...
Embodiment 3
[0032] Add acid to the sucralfate mother liquor in the storage tank to adjust the pH to 3.0, pass through a 0.5μm filter to the circulation tank, and then inject it into the three-stage nanofiltration membrane cooperative concentration circulation device by the pressure pump, the interception of the first-stage nanofiltration membrane The molecular weight is 1000-1100 Daltons, the operating pressure is 0.5Mpa, and the operating temperature is 20°C; the molecular weight cut-off of the second-stage nanofiltration membrane is 800-1000 Daltons, the operating pressure is 1.0Mpa, and the operating temperature is 30°C; The molecular weight cut-off of the third-stage nanofiltration membrane is 500-600 Daltons, the operating pressure is 2.0Mpa, and the operating temperature is 40°C; after concentration by the third-stage nanofiltration, a dope with a sucrose octasulfate content of 5.0% is obtained, and the rejection rate 99.5%, the COD value of the solution obtained by dialysis is 415.5...
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