Method for simultaneously extracting heparin sodium and intestinal membrane protein peptide based on enzymolysis method

A technology for intestinal membrane protein and heparin sodium, applied in the field of heparin sodium extraction, can solve the problems of high operating cost, long production cycle, large amount of waste water, etc., and achieves reduction of dosage and breakage rate, reduction of production input cost, and reduction of environmental pollution. Effect

Inactive Publication Date: 2020-11-27
无锡海思瑞科技有限公司
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  • Application Information

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Problems solved by technology

[0007] Large amount of wastewater: Traditional industrial production methods have a large amount of wastewater discharge and high salt content, especially the organic matter content in the discharge water of the enzymatic hydrolysis process is very high, the wastewater treatment is difficult and the operating cost is high;
[0008] A large amount of dangerous organic solvents are used: the traditional production method adopts ethanol precipitation and standing overnight to collect heparin, which has a long production cycle, high requirements for workshop level, strict operation and management requirements for ethanol recovery and storage, and high cost

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  • Method for simultaneously extracting heparin sodium and intestinal membrane protein peptide based on enzymolysis method

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Embodiment 1

[0039] Such as figure 1 As shown, a method for simultaneously extracting heparin sodium and intestinal membrane protein peptides based on an enzymatic hydrolysis method comprises the following steps:

[0040] S101, prepare intestinal mucosa mixture;

[0041] S102, preparing the intestinal mucosa mixed liquid into an enzymatic hydrolysis solution by enzymatic hydrolysis;

[0042] S103, filtering the enzymolysis solution to obtain a clarified filtrate and an enzymolysis concentrate;

[0043] S104, performing heparin adsorption on the clarified filtrate by using an ion exchange resin column, and obtaining an effluent at the same time;

[0044] S105. Remove the adsorbed and saturated ion-exchange resin column, first wash the resin in the ion-exchange resin column with washing brine, and then use desorption brine to elute the resin with heparin to obtain a heparin sodium eluent;

[0045] S106. Filtering, desalting and concentrating the heparin sodium eluate to obtain a second pe...

Embodiment 2

[0060] On the basis of the first embodiment above, the enzymatic hydrolysis concentrate in step S103 is returned to S101 for extraction again. Improve extraction rates.

Embodiment 3

[0062] On the basis of any one of the above embodiments, in step S104, no less than two ion exchange resin columns are used in series for adsorption.

[0063]The ion-exchange resin column is arranged in series in the form of "two-purpose and one-standby" with "saturated adsorption without leakage" or arranged in series with "one-use and one-standby". The resin column is separated from the process, and the rest of the ion exchange resin column continues to run, with high work efficiency. In the traditional process, due to the high content of impurities in the enzymolysis solution, it can only be adsorbed by sprinkling it into the adsorption tank, but the present invention adopts filtration and ion exchange resin column for adsorption, which greatly improves the adsorption rate And work efficiency, and can effectively reduce the broken rate of resin. Series connection can improve the extraction rate of heparin sodium, because the content of heparin sodium in the enzymatic hydro...

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Abstract

The invention relates to a method for simultaneously extracting heparin sodium and intestinal membrane protein peptide based on an enzymolysis method. The method comprises the following steps of: preparing an intestinal mucosa mixed solution; preparing enzymatic hydrolysate by adopting an enzymolysis method; filtering to obtain clarified filtrate and an enzymolysis concentrated solution; performing heparin adsorption on the filtrate through an ion exchange resin column, and obtaining effluent at the same time; taking down the adsorbed and saturated ion exchange resin column, firstly cleaning the resin in the ion exchange resin column by using cleaning saline water, and then performing heparin elution on the resin by using desorption saline water to obtain heparin sodium eluent; filtering,desalting and concentrating the heparin sodium eluent to obtain a heparin sodium concentrated solution; drying the heparin sodium concentrated solution to obtain crude heparin sodium; cooling the effluent, and then carrying out desalination and concentration to obtain a first concentrated solution; carrying out vacuum concentration on the first concentrated solution to obtain a protein peptide concentrated solution; and drying the protein peptide concentrated solution to obtain the protein peptide. The method is high in heparin sodium extraction rate, short in production period, capable of extracting protein peptide at the same time, low in cost and low in pollution.

Description

technical field [0001] The invention relates to a method for extracting heparin sodium, in particular to a method for simultaneously extracting heparin sodium and intestinal membrane protein peptides based on an enzymatic hydrolysis method. Background technique [0002] At present, there are two techniques for extracting heparin in China: salting-out method and enzymatic hydrolysis method. The salting-out method is to add salt and alkali to the intestinal mucosa to adjust the pH, raise the temperature to about 50°C and keep warm to dissolve the heparin and transfer it to water, then raise the temperature to 95°C to solidify the intestinal membrane protein, and then separate to obtain the by-product intestinal membrane slag (or called Intestinal membrane protein), and the separated supernatant is subjected to resin adsorption, analysis, alcohol precipitation, drying and other steps to obtain heparin. The enzymatic hydrolysis method is to add salt to the intestinal mucosa, ad...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08B37/10C12P21/06C07K1/34C07K1/18C07K1/14C07K1/36
CPCC08B37/0081C08B37/0003C12P21/06C07K1/34C07K1/18C07K1/14C07K1/36
Inventor 于淼
Owner 无锡海思瑞科技有限公司
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