A kind of preparation method of cpc sodium salt
A technology of sodium salt and organic solvent is applied in the field of preparation of CPC sodium salt, which can solve the problems of insufficient purity of CPC sodium salt, affecting the quality of cephalosporins, etc., and achieve the effects of low cost and simple operation.
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
Embodiment 1
[0022] Embodiment 1, the preparation of CPC sodium salt of the present invention
[0023] Take 50L of CPC feed solution with a potency of 21500u / ml, and further concentrate it to 10L with a potency of 96300u / ml on a nanofiltration concentrator in the laboratory. The concentrated solution was adjusted to neutral pH with 4% sodium hydroxide solution,
[0024] Use Rohm and Haas FPA-65 ion exchange resin to decolorize the concentrated solution in a dynamic decolorization mode (resin loading capacity is 1.4L, feed flow rate is 2BV / h, decolorization process temperature is 0-5°C), and the decolorization solution uses G4 Sand core funnel filter. Slowly add 30L of acetone to the filtered decolorizing solution at 5°C for crystallization at a feeding rate of 2BV / h. The cake was washed twice with acetone and drained to obtain 832 grams of CPC sodium salt crude product.
[0025] Add 8L of purified water to dissolve the dried crude CPC sodium salt, and use Rohm and Haas FPA-65 exchange r...
Embodiment 2
[0026] Embodiment 2, the preparation of CPC sodium salt of the present invention
[0027] Take 60L CPC nanofiltration concentrate with a potency of 22500u / ml, and further concentrate it to 13L with a potency of 92763u / ml on a nanofiltration concentrator in the laboratory. The concentrated solution is adjusted to neutral pH with 4% sodium hydroxide solution, and the concentrated solution is decolorized in a dynamic decolorization mode using Rohm and Haas FPA-65 ion exchange resin (resin loading capacity 1.3L, feed flow rate is 1BV / h , the decolorization process temperature is 0-5°C), and the decolorization solution is filtered with a G4 sand core funnel. Slowly add 30L of acetone to the filtered decolorizing solution at 5°C for crystallization at a feeding rate of 2BV / h. The cake was washed twice with acetone and drained to obtain 950 g of the crude product of CPC sodium salt.
[0028] Add 1.5L of purified water to dissolve 150g of the dried CPC sodium salt crude product, and...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More