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A method for purifying clavulanic acid from fermentation broth

A technology of clavulanic acid and fermentation broth, applied in the direction of organic chemistry, etc., can solve the problems of emulsification, low purity of clavulanic acid solution, slow concentration rate, etc.

Active Publication Date: 2014-10-29
安徽普朗膜技术有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although this scheme can prepare or extract clavulanic acid or its pharmaceutically acceptable salt or ester, in the whole scheme, microfiltration and ultrafiltration (10-30 kilodaltons) are used to purify the fermentation broth, Although the suspended solids in the fermented liquid can be removed, the pigments, proteins and sugar components with smaller molecular weights contained in the fermented liquid cannot be removed, so the purity of the obtained clavulanic acid solution is low, containing a small amount of pigments, sugars Part and protein, there will be serious emulsification in the subsequent extraction process, which will affect the subsequent operations such as the separation and salt formation of clavulanate. At the same time, it is necessary to use activated carbon to further depigmentation treatment in the subsequent operations; Or it uses reverse osmosis to concentrate the fermentation broth, which has high energy consumption and slow concentration rate, and the whole production process takes a long time

Method used

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  • A method for purifying clavulanic acid from fermentation broth

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0016] Dilute the fermented broth containing crude clavulanic acid, mycelium, and other solid suspensions with water, adjust the pH value of the fermented broth to 4.8-5.5, and remove it through a tubular ultrafiltration membrane at a temperature of 4-10°C Suspended solids and some pigments are used to obtain permeate A. The selected tubular ultrafiltration membrane is polytetrafluoroethylene membrane, and the molecular cut-off is 10-200 kilodaltons. The flow rate of permeate A is controlled at 20-40L / m 2 .h; adjust the temperature of the permeate A to 4-10°C, and the pH value to be between 4.8 and 5.5, perform a first-level nanofiltration treatment on it through a first-level nanofiltration device, and remove the remaining pigment, protein and sugar to obtain the permeate B , the selected nanofiltration membrane is a polyamide membrane, the molecular cut-off is 200-1000 Daltons, and the flow rate of the permeate B is controlled to be 10-30L / m 2 .h; Finally, the permeate B i...

Embodiment 2

[0018] Dilute the fermented broth containing crude clavulanic acid, mycelia, and other solid suspensions with water, adjust the pH of the fermented broth to 5.5-6.2, and remove it through a tubular ultrafiltration membrane at a temperature of 10-15°C Suspended solids and some pigments are used to obtain permeate A. The selected tubular ultrafiltration membrane is polytetrafluoroethylene membrane, and the molecular cut-off is 10-200 kilodaltons. The flow rate of permeate A is controlled at 60-80L / m 2 .h; adjust the temperature of permeate A to 10-15°C, and perform primary nanofiltration treatment on it through primary nanofiltration equipment under the condition of pH 5.5-6.2, and remove the remaining pigment, protein and sugar to obtain permeate B , the selected nanofiltration membrane is a polyamide membrane, the molecular cut-off is 200-1000 Daltons, and the flow rate of the permeate B is controlled to be 20-30L / m 2 .h; Finally, the permeate B is subjected to secondary nan...

Embodiment 3

[0020] Dilute the fermented broth containing crude clavulanic acid, mycelia, and other solid suspensions with water, adjust the pH to 4.8-5.5, and remove the fermented broth through a tubular ultrafiltration membrane at a temperature of 4-10°C. Suspended solids and some pigments are used to obtain permeate A, the selected tubular ultrafiltration membrane is polytetrafluoroethylene membrane, the molecular cut-off is 10-200 kilodaltons, and the flow rate of permeate A is controlled to be 40-60L / m 2 .h; adjust the temperature of permeate A to 4-10°C, control the pH value to 4.8-5.5, pass permeate A through primary nanofiltration equipment for primary nanofiltration treatment, remove remaining pigment, protein and sugar to obtain permeate B. The selected nanofiltration membrane is a polyamide membrane, the molecular cut-off is 200-1000 Daltons, and the flow rate of the permeate B is controlled to be 20-30L / m 2 .h; Finally, the permeate B is subjected to secondary nanofiltration ...

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Abstract

The invention discloses a method for purifying clavulanic acid from fermentation liquor. The method comprises the steps of performing ultrafiltration treatment on the fermentation liquor and removing solids and partial coloring matters in the fermentation liquor to obtain penetrating fluid A; performing first stage nanofiltration treatment on the penetrating fluid A and removing proteins and surplus coloring matters in the penetrating fluid A to obtain penetrating fluid B; performing second stage nanofiltration treatment on the penetrating fluid B and removing partial water in the penetrating fluid B to obtain intercepted concentrated liquor C; and performing extraction separation on the concentrated liquor C to prepare purification liquid of the clavulanic acid. Solid bodies, the proteins, sugars and the coloring matters in the fermentation liquor can be effectively removed through the ultrafiltration treatment and the first stage nanofiltration treatment, so that the concentrated liquor C can be easily layered in a subsequent extraction separation process, excessive emulsion can be avoided, high speed centrifugation treatment is not needed, and investment cost of equipment can be greatly reduced.

Description

technical field [0001] The invention relates to a method for purifying clavulanic acid from fermentation broth. Background technique [0002] Clavulanic acid is also known as clavulanic acid, chemical name (2R,5R,Z)~30(2~hydroxyethylene)~7~oxo~4~oxa~1~azabicyclo[3.2.0]heptane Alkane ~ 2 ~ carboxylic acid, the molecular formula is: [0003] [0004] It is an irreversible competitive β-lactamase inhibitor produced by Streptomyces, which is effective against Staphylococcus aureus, Escherichia coli, Klebsiella, Shigella, Pseudomonas and influenza The β-lactamase of various pathogenic bacteria such as blood bacteria has a strong inhibitory effect. Because clavulanic acid can increase the antibacterial activity spectrum of antibiotics, its combined use with penicillins and cephalosporins can increase the efficacy by several times or even ten times, and at the same time restore the sensitivity to drug-resistant strains, so it has a high Medicinal value. [0005] At present, ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07D503/18C07D503/02
Inventor 俞经福
Owner 安徽普朗膜技术有限公司
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