Method for separating human serum albumin

A technology for the separation of human serum albumin, which is applied in the direction of albumin peptides, preparation methods of peptides, animal/human proteins, etc., can solve the problem of incomplete removal, low yield of protein components, and inability to accurately remove albumin components Unstable substances and other problems can be solved, and the effect of good product quality and high albumin yield can be achieved

Active Publication Date: 2008-12-31
NANYUE BIOPHARMING
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Problems solved by technology

[0003] The current low-temperature ethanol separation method to produce human serum albumin has the disadvantages of low yield of protein components and incomplete removal of unstable substances (such as lipoproteins) in the albumin component.
There are mainly two reasons for the above-mentioned defects. One is that the selection of process parameters such as ethanol concentration, temperature, and pH value is unreasonable, and the other is that the separation method is unscientific. At present, most of them use centrifugation. When the temperature rises, the miscellaneous proteins are dissolved but not removed, and the unstable substances in the albumin component cannot be removed accurately.

Method used

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Embodiment Construction

[0010] A method for separating human serum albumin, the specific process is:

[0011] (1), first separate component I:

[0012] Put the plasma into the reaction tank, measure, start stirring and circulating the refrigerated ethanol machine, slowly add 95% ethanol to the plasma until the volume concentration of ethanol is 8%, adjust the pH of the reaction solution to 7.1-7.3 with pH 4.0 acetic acid buffer, and react Afterwards, component I solid-liquid mixture is obtained;

[0013] (2), re-separation of component II+III:

[0014] Add 95% ethanol to the solid-liquid mixture of component I until the volume concentration of ethanol is 20%, adjust the pH of the reaction solution to 6.8 to 7.0 with pH 4.0 acetic acid buffer solution, and the temperature is -4 to -6°C to obtain component I after reaction +II+III solid-liquid mixture;

[0015] (3), pressure filtration separates component I+II+III:

[0016] Press filter the solid-liquid mixture of the above components I+II+III in t...

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Abstract

The invention relates to a protein separation and purification process method in the biological product technology, in particular to a human serum albumin separation method, comprising protein separation and purification process. The method is characterized in that the method takes plasma as raw material; first of all, composition I, composition II and composition III are respectively precipitated; then the composition I, II and III are separated together; finally compositions IV-1 and IV-4 are precipitated respectively and separated together; the solid-liquid separation uses a pressure filtration technology, with the fluid intake pressure no more than 0.2MPa. The method of the invention adopts the pressure filtration technology in the separation process, adjusts and controls the ethanol albumin concentration, temperature, pH value and other parameters in the albumin separation, and overcomes the disadvantages that the existing technology which produces human albumin through low-temperature ethanol separation has lower albumen composition yield and the unstable substances (such as lipoprotein) in the albumin composition are not completely removed. Compared with the low-temperature ethanol method, the method of the invention has high yield of albumin (not less than 2.9g / 100ml) and good product quality.

Description

technical field [0001] The invention relates to a protein separation and purification process in biological product technology, in particular to a separation method of human blood albumin. Background technique [0002] Human albumin is the most abundant macromolecular protein in human blood. Since Cohn et al. created the low-temperature ethanol human plasma protein separation technology in the 1940s, the industrialized production of plasma protein has made great progress. [0003] The current low-temperature ethanol separation method to produce human serum albumin has the disadvantages of low yield of protein components and incomplete removal of unstable substances (such as lipoproteins) in the albumin component. There are mainly two reasons for the above-mentioned defects. One is that the selection of process parameters such as ethanol concentration, temperature, and pH value is unreasonable, and the other is that the separation method is unscientific. At present, most of t...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07K1/30C07K14/76
Inventor 张翔陈治海周柏林岳跃飞单永红张秋声
Owner NANYUE BIOPHARMING
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