Application method of ultrafiltration membrane in continuous resolution of D-trans-DE chrysanthemic acid
An application method and ultrafiltration membrane technology are applied in the field of continuous separation of chiral right-trans DE chrysanthemic acid by ultrafiltration membranes, which can solve the problems of low utilization rate of resolution enzymes, increased cost, enzyme inactivation, etc., and achieve The effect of reducing the size of the splitting equipment, increasing the conversion rate, and good economic efficiency
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Embodiment 1
[0028] Three-stage series reactors, continuous to one-stage reaction according to ethyl chrysanthemum acid: 5% disodium hydrogen phosphate-sodium dihydrogen phosphate buffer: esterase (esterase concentrate) = 1:10:0.005 (0.05) ratio Addition, temperature 45°C, pH control 10.5, reaction residence time 60hr, resolution utilization rate of ethyl chrysanthemum acid 90%, split liquid standing still to obtain split water layer, roll-type ultrafiltration membrane, cut-off molecular weight 5000, membrane ultrafiltration The filtration start pressure is 0.2MPa, the ultrafiltration end pressure is 0.6MPa, the ultrafiltration temperature is 35-45°C, the concentration ratio is 15 times, and the esterase cut-off rate is 95%. The ultrafiltered water is subjected to acidification and extraction to obtain dextrapanthemic acid, e.e99%. The highly active esterase used in this example is EYN045 esterase commercially available from Sigma, USA.
Embodiment 2
[0030] Four-stage series reactors, continuous to one-stage reaction according to the ratio of ethyl chrysanthemum acid: 5% disodium hydrogen phosphate-sodium dihydrogen phosphate buffer: esterase (esterase concentrate) = 1:10:0.005 (0.05) Addition, temperature 40°C, pH control 10, reaction residence time 72hr, resolution utilization rate of ethyl chrysanthemum acid 95%, split liquid standing still to obtain split water layer, through 37-channel ceramic ultrafiltration membrane, cut-off pore size 10nm, membrane The ultrafiltration TMP pressure is 0.2MPa, the ultrafiltration temperature is 35-45°C, the concentration ratio is 10 times, and the esterase cut-off rate is 90%. The ultrafiltered water is subjected to acidification and extraction to obtain dextrapanthemic acid, e.e99%. The highly active esterase used in this example is a commercially available esterase from Sigma, USA: EYN065 esterase.
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