Method for purifying deoxyribose
A deoxyribose and supercritical fluid technology, applied in the directions of deoxy/unsaturated sugar, chemical instruments and methods, sugar derivatives, etc., can solve the problems of unsatisfactory product purity, poor control of cooling temperature, low yield, etc. , to achieve the effect of improving crystallization safety, easy control of operating parameters, and fast dissolution
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Embodiment 1
[0020] (1) Use the raw material pump to spray the neutralized deoxyribose solution A containing impurities at 90° C. from the top of the extraction column E, and at the same time pass the supercritical fluid CO at the bottom of the extraction column E. 2 C, control the temperature of the supercritical fluid to be 33°C, the pressure to be 9Mpa, and the flow rate to be 15m 3 / min, so that deoxyribose dissolves in supercritical fluid CO 2 C;
[0021] (2) High pressure supercritical fluid CO containing dissolved deoxyribose 2 B is depressurized to lower than the supercritical fluid CO through the throttle valve D 2 Enter the separation kettle F below the critical pressure; supercritical fluid CO 2 The solubility drops sharply to separate out the solute, which is separated into two parts, the deoxyribose solution H and the supercritical fluid gas, the former is the process product, which is regularly discharged from the bottom of the separation kettle F, and the latter is the ci...
Embodiment 2
[0024] (1) Use the raw material pump to spray the neutralized deoxyribose solution A containing impurities at 90° C. from the top of the extraction column E, and at the same time pass the supercritical fluid CO at the bottom of the extraction column E. 2 C, control the temperature of the supercritical fluid to be 34°C, the pressure to be 10Mpa, and the flow rate to be 17m 3 / min, so that deoxyribose dissolves in supercritical fluid CO 2 C;
[0025] (2) High pressure supercritical fluid CO containing dissolved deoxyribose 2 B is depressurized to lower than the supercritical fluid CO through the throttle valve D 2 Enter the separation kettle F below the critical pressure; supercritical fluid CO 2 The solubility drops sharply to separate out the solute, which is separated into two parts, the deoxyribose solution H and the supercritical fluid gas, the former is the process product, which is regularly discharged from the bottom of the separation kettle F, and the latter is the c...
Embodiment 3
[0028] (1) Use the raw material pump to spray the neutralized deoxyribose solution A containing impurities at 90° C. from the top of the extraction column E, and at the same time pass the supercritical fluid CO at the bottom of the extraction column E. 2 C, control the temperature of the supercritical fluid to be 36°C, the pressure to be 11Mpa, and the flow rate to be 20m 3 / min, so that deoxyribose dissolves in supercritical fluid CO 2 C;
[0029] (2) High pressure supercritical fluid CO containing dissolved deoxyribose 2 B is depressurized to lower than the supercritical fluid CO through the throttle valve D 2 Enter the separation kettle F below the critical pressure; supercritical fluid CO 2 The solubility drops sharply to separate out the solute, which is separated into two parts, the deoxyribose solution H and the supercritical fluid gas, the former is the process product, which is regularly discharged from the bottom of the separation kettle F, and the latter is the c...
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Abstract
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