Method for separating and purifying glufosinate-ammonium solution
A purification method, the technology of glufosinate-ammonium, applied in the field of separation and purification of glufosinate-ammonium solution, can solve the problems of difficult separation, high resin price, unsafety, etc., and achieve the effect of automatic control, good product quality and low processing cost
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Embodiment 1
[0022] Using phosphorus trichloride or phosphite as the starting material, a glufosinate-ammonium solution is obtained at the end of the ammoniation reaction, the mass fraction of glufosinate-ammonium is 20%, the mass fraction of sodium chloride is 8%, and the solution pH=4 . Add 1 times of water to dilute and enter the first-level nanofiltration membrane separation device. The selected nanofiltration membrane is a roll-type nanofiltration membrane with a molecular weight cut-off of 150Da and a glufosinate-ammonium rejection rate of ≥90%. The control pressure is 1.0MPa and the temperature is 10 ℃ to obtain glufosinate-ammonium massfraction is 15%, sodium chloride massfraction is 0.5% solution A and glufosinate-ammonium massfraction is 0.01%, sodium chloride massfraction is 3% solution B;
[0023] Solution A enters the electrodialysis membrane separation device for separation. The selected electrodialysis membrane is a homogeneous membrane with a rejection rate of glufosinate ≥...
Embodiment 2
[0027] Using phosphorus trichloride or phosphite as the starting material, a glufosinate-ammonium solution is obtained at the end of the ammoniation reaction, the mass fraction of glufosinate-ammonium is 35%, the mass fraction of ammonium chloride is 20%, and the solution pH=7 , add 5 times of water to dilute, and enter the 4-stage nanofiltration membrane separation device. The selected nanofiltration membrane is a roll-type nanofiltration membrane with a molecular weight cut-off of 300Da and a glufosinate-ammonium rejection rate of ≥90%. The control pressure is 4.0MPa and the temperature is 45 DEG C obtain that glufosinate-ammonium massfraction is 30%, ammonium chloride massfraction is 4% solution A and glufosinate-ammonium massfraction is 0.1%, ammonium chloride massfraction is 8% solution B;
[0028] Solution A enters the electrodialysis membrane separation device for separation. The selected electrodialysis membrane is a heterogeneous membrane with a rejection rate of glufo...
Embodiment 3
[0032] Using phosphorus trichloride or phosphite as the starting material, a glufosinate-ammonium solution is obtained at the end of the ammoniation reaction, the mass fraction of glufosinate-ammonium is 35%, the mass fraction of ammonium chloride is 15%, and the solution pH=6 , add 3 times of water to dilute, and enter the 3-stage nanofiltration membrane separation device. The selected nanofiltration membrane is a roll-type nanofiltration membrane with a molecular weight cut-off of 200Da and a glufosinate-ammonium rejection rate of ≥90%. The control pressure is 3.0MPa and the temperature is 35 DEG C obtain that glufosinate-ammonium massfraction is 20%, ammonium chloride massfraction is 2% solution A and glufosinate-ammonium massfraction is 0.08%, ammonium chloride massfraction is 6% solution B;
[0033] Solution A enters the electrodialysis membrane separation device for separation. The selected electrodialysis membrane is a heterogeneous membrane with a rejection rate of gluf...
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