Improved simulated moving bed separation method
A technology for simulating moving bed and separation methods, applied in separation methods, chemical instruments and methods, solid adsorbent liquid separation, etc., can solve problems such as increasing system operating pressure and solvent consumption, and achieve the goal of reducing consumption and system operating pressure Effect
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Embodiment 1
[0041] Improved Simulated Moving Bed Separation Method A
[0042] use as figure 2 In the separation system shown, prepare a saturated racemic omeprazole raw material solution with a concentration of 2 mg / mL with n-hexane / absolute ethanol (volume ratio 80 / 20), and inject it at a flow rate of 17.5 mL / min. The pump P1 is directly pumped into the III area formed by the chromatographic column 5 and the chromatographic column 6, and then flows through the IV area formed by the chromatographic column 7, 8 and the IV area circulation pump P2, and normal hexane / dehydrated alcohol (volume ratio is 80 / 20) At a flow rate of 7mL / min, pump the eluent through the eluent pump P3 from the eluent inlet between the IV zone and the I zone composed of chromatographic columns 1 and 2, and then flow through the chromatographic column 3, 4 and II zone circulation pump Zone II composed of P4. The flow rates in areas I to IV were set at 23, 14.5, 17.5, and 12 mL / min, respectively. According to the...
Embodiment 2
[0045] Improved Simulated Moving Bed Separation Method B
[0046] use as image 3 In the separation system shown, prepare a saturated racemic omeprazole raw material solution with a concentration of 2 mg / mL with n-hexane / absolute ethanol (volume ratio 80 / 20), and inject it at a flow rate of 17.5 mL / min. Pump P1 directly pumps into the III area composed of chromatographic column 5 and chromatographic column 6, and then flows through the IV area composed of chromatographic column 7, 8 and IV area circulation pump P2, and flows pure absolute ethanol from The eluent inlet is directly pumped into zone I composed of chromatographic column 1 and chromatographic column 2 through eluent pump P3, and then flows through zone II composed of chromatographic column 3, 4 and zone II circulation pump P4. The flow rates in areas I to IV were set at 3.1, 2.4, 17.5, and 12 mL / min, respectively. According to the material balance of the mobile phase, the flow rates of the extract and raffinate w...
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