Method for separating chiral compound metalaxyl by adopting simulated moving bed in fourth region
A technology for simulating moving bed and metalaxyl, applied in the field of simulated moving bed chromatographic separation of metalaxyl, can solve problems such as being in the analysis stage, and achieve the effects of stable product quality, continuous automation of production, and simple process
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[0029] 1. Preparation of cellulose-tris(3,5-dimethylphenylcarbamate) filler
[0030] Prepare according to the method of literature (Okamoto Y, Kawashima M, Hatada K J . Chromatogr.1986,363:173~186). Cellulose and phenyl isohydrogen were reacted in pyrrole solution at 100° C. for 24 hours, and the methanol-insoluble product obtained from the reaction was cellulose-tris(3,5-dimethylphenylcarbamate). Cellulose-tris(3,5-dimethylphenylcarbamate) was dissolved in tetrahydrofuran, and aminopropyl silica gel was added to the solution, and electromagnetically stirred until the tetrahydrofuran was volatilized, and repeated 3 times to obtain cellulose- Tris(3,5-dimethylphenylcarbamate) coated chiral stationary phase. Wherein the weight ratio of cellulose-three (3,5-dimethylphenylcarbamate) to aminopropyl silica gel is 1:5;
[0031] 2. Selection of mobile phase
[0032] The composition of the mobile phase affects the separation of metalaxyl enantiomers, and also affects the productivit...
example 1
[0053] A operating conditions
[0054] Mobile phase: methanol: water = 15:85
[0055] Injection concentration: 7mg / ml
[0056] Injection liquid flow rate: 2.5 ml / min
[0057] Eluent flow rate: 1.0 ml / min
[0058] Extraction flow rate: 1.5 ml / min
[0059] Raffinate flow rate: 2.0 ml / min
[0060] Switching time: 6.8min
[0061] System temperature: 25°C
[0062] B finished product analysis
[0063] Analyzing the composition of the extract and raffinate with an analytical column, the purity of the extract is 99.3%, and the purity of the raffinate is 99.1%. Each kilogram of stationary phase can produce 0.3kg of R-metalaxyl and S-metalaxyl each day , the mobile phase consumption was 57L / kg, and the recovery rate was 95.2%;
example 2
[0065] A operating conditions
[0066] Mobile phase: methanol: water = 20:80
[0067] Injection concentration: 10mg / ml
[0068] Injection liquid flow rate: 6.0 ml / min
[0069]Eluent flow rate: 5.0 ml / min
[0070] Extraction flow rate: 4.0 ml / min
[0071] Raffinate flow rate: 6.0 ml / min
[0072] Switching time: 7.5min
[0073] System temperature: 20°C
[0074] B finished product analysis
[0075] Analyzing the composition of the extract and raffinate with an analytical column, the purity of the extract is 99.5%, and the purity of the raffinate is 99.3%. Each kilogram of stationary phase can produce 0.53kg of R-metalaxyl and S-metalaxyl each day , the mobile phase consumption was 83.3L / kg, and the recovery rate was 98.1%.
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