阅读说明：本技术 四种血液来源蛋白的纯化方法 (Purification method of four blood-derived proteins ) 是由 易维京 朱攀 任燕斌 赵威 赵忠颢 于 2020-08-13 设计创作，主要内容包括：本发明公开了四种血液来源蛋白的制备方法,采用阴/阳离子交换层析和亲和层析相配合的纯化方法,从同一份血液样本中,同时纯化出α1-抗胰蛋白酶(AAT)、转铁蛋白(TRF)、α1-酸性糖蛋白(AAG)和结合珠蛋白(HP)四种蛋白,本发明公开的制备方法操作简单,所得到的目的蛋白活性稳定、纯度高、收率高,适合用于工业生产和临床应用。(The invention discloses a preparation method of four blood source proteins, which adopts a purification method combining anion/cation exchange chromatography and affinity chromatography to simultaneously purify four proteins of alpha 1-antitrypsin (AAT), Transferrin (TRF), alpha 1-acid glycoprotein (AAG) and Haptoglobin (HP) from the same blood sample.)

1. The purification method of four blood-derived proteins is characterized by comprising the following steps:

a. dialyzing the serum into a chromatography buffer solution with the pH value of 4.2 to 4.8 to obtain a dialyzed sample, purifying the sample by anion exchange chromatography, and collecting a flow-through solution I and an eluent I;

b. purifying the eluent I by affinity chromatography to obtain flow-through liquid II and HP protein;

c. dialyzing the flow-through solution II into a chromatography buffer solution with the pH value of 3.0-3.8, purifying by anion exchange chromatography, and collecting AAG protein;

d. adjusting pH of the flow-through solution I to 5.0-5.8, purifying by cation exchange chromatography, and collecting flow-through solution III and eluent II;

e. purifying the flow-through liquid III by affinity chromatography to obtain AAT protein;

f. dialyzing the eluate II into a chromatography buffer solution with pH of 5.3-5.8, and purifying by anion exchange chromatography to obtain TRF protein.

2. The method of claim 1, wherein the anion/cation exchange chromatography and the affinity chromatography each comprise four processes of equilibration, loading, flow-through and elution.

3. The method according to claim 1 or 2, wherein the chromatography buffer is selected from the group consisting of sodium acetate buffer, phosphate buffer, hydrochloric acid buffer, and carbonate buffer.

4. The method of claim 2, wherein during the equilibration, the reagent for anion/cation exchange chromatography is a chromatography buffer, and the reagent for affinity chromatography is an equilibration buffer.

5. The method of claim 4, wherein the equilibration buffer is selected from PBS, PB, or Tris buffers.

6. The method according to claim 2, wherein an elution reagent A is used in the steps a, c, d and f during the elution, and the elution reagent A comprises: sodium acetate buffer and NaCl.

7. The method according to claim 2, wherein the elution is carried out using a glycine buffer as the reagent in step b.

8. The method of claim 2, wherein the elution is performed using reagents comprising Tris and MgCl in step e₂。

9. The production method according to claim 1 or 2, wherein the filler for anion exchange chromatography is a filler for strong anion exchange chromatography (Q) or a filler for weak anion exchange chromatography (DEAE).

10. The method according to claim 1 or 2, wherein the packing for cation exchange chromatography is a packing for strong cation exchange chromatography (SP) or a packing for weak cation exchange Chromatography (CM).

Technical Field

The invention relates to separation and purification of proteins, in particular to a purification method of four blood-derived proteins.

Background

In the age of rapid development of biomedicine, the blood product industry has become an important component of the biomedicine and diagnostic industry. At present, blood products (plasma protein drugs) derived from plasma mainly comprise four types of albumin, immunoglobulin, blood coagulation factors and protease inhibitors, and blood product enterprises in developed countries can obtain more than 20 plasma protein drugs from plasma. However, under the restriction of talents, technology, clinical cognitive level and other factors, at most, no more than 10 products can be obtained by domestic blood product enterprises, and mainly the products separated and purified based on the low-temperature ethanol precipitation process comprise human serum albumin, immunoglobulin, blood coagulation factor VIII products and the like. At present, the domestic medicament for mainly purifying the plasma protein is still based on the low-temperature ethanol method invented by Cohn and others in the decades of the twentieth century, and is separated by adjusting the ethanol concentration, the salt concentration, the temperature and the pH value and depending on the different solubilities of the plasma protein.

The alpha 1-antitrypsin (AAT) preparation can be used for treating emphysema, acute lung injury, cystic fibrosis, adult respiratory distress syndrome and other diseases caused by congenital or acquired AAT deficiency, and has high clinical application value.

Transferrin (TRF) numerous studies have demonstrated that transferrin has an antibacterial function and is also a growth factor essential for cell growth and proliferation. However, conventional purification methods for preparing transferrin (such as cold ethanol precipitation, ammonium sulfate precipitation, rivanol precipitation, etc.) have failed to meet the demands for transferrin at the present stage due to low production efficiency, complicated production process, and low purity of products.

Haptoglobin (HP) haptoglobin is an acute phase response protein. Can be used for treating hemolytic disease, and can prevent Hb urine after administration of HP. Furthermore, HP may also be of value in the treatment of life threatening infections caused by bacteria of the Hb iron. With the progress of modern medical treatment, the demand for HP is increasing.

Alpha 1-acid glycoprotein (AAG) is a major acute phase reaction protein, is increased in acute inflammation, and is involved in immune defense functions. With the development of various kits, the demand of AAG proteins, whether as research target proteins or as validation standards, has increased year by year, so the purification and preparation of AAG proteins are of great importance.

With the progress of modern medical treatment, the requirements of ATT, TRF, HP and AAG are increasing day by day, but due to different properties, the single purification in serum has the problems of low purity, low yield, unfavorable amplification and the like. In the prior art, simultaneous purification of a plurality of proteins is difficult to achieve, and because proteins treated by organic solvents or high salt are low in activity, subsequent use is seriously influenced. Therefore, a method for simultaneously preparing ATT, TRF, HP and AAG is required.

Disclosure of Invention

In order to solve the problem that a plurality of proteins are difficult to purify, the invention provides a purification method of four blood-derived proteins, which simultaneously purifies the four proteins by using the same sample, reduces the cost and obtains four proteins with high purity and high yield.

The four purified proteins are ATT, TRF, HP and AAG, and the four proteins are separated and purified by ion exchange chromatography and affinity chromatography.

The method has the advantages of simple operation, low cost, high product purity, strong stability and large processing capacity, and is suitable for large-scale production.

The method specifically comprises the following steps:

a. dialyzing the serum into a chromatography buffer solution with the pH value of 4.2 to 4.8 to obtain a dialyzed sample, purifying the sample by anion exchange chromatography, and collecting a flow-through solution I and an eluent I;

b. purifying the eluent I by affinity chromatography to obtain flow-through liquid II and HP protein;

c. dialyzing the flow-through liquid II into a chromatography buffer solution with the pH value of 3.0-3.8 to obtain dialyzed flow-through liquid II, purifying the dialyzed flow-through liquid II by anion exchange chromatography, and collecting AAG protein;

d. adjusting pH of the flow-through solution I to 5.0-5.8, purifying by cation exchange chromatography, and collecting flow-through solution III and eluent II;

e. purifying the flow-through liquid III by affinity chromatography to obtain AAT protein;

f. dialyzing the eluent II into a chromatography buffer solution with the pH value of 5.3-5.8 to obtain a dialyzed eluent II, and purifying the dialyzed eluent II by anion exchange chromatography to obtain TRF protein.

Preferably, the anion/cation exchange chromatography and the affinity chromatography each comprise four processes of equilibration, loading, flow-through and elution.

Preferably, the chromatography buffer is an acidic buffer, and can be selected from an acetic acid buffer, a phosphate buffer, a hydrochloric acid buffer and a carbonic acid buffer; more preferably an acetate buffer.

Preferably, during the equilibration, the reagent for anion/cation exchange chromatography is a chromatography buffer, and the reagent for affinity chromatography is an equilibration buffer.

More preferably, the equilibration buffer is selected from PBS, PB or Tris buffers.

Preferably, during the elution, elution reagent a is used in steps a, c, d, f, and the elution reagent a comprises: sodium acetate buffer and NaCl.

Preferably, in the anion/cation exchange chromatography process, the elution process adopts a gradient elution of 0-100% elution reagent A.

The 0-100% elution reagent A of the invention is: when the elution is started, the reagent in the filler is a complete chromatographic buffer solution, namely the elution reagent A is 0%, the gradient of the elution reagent A is continuously added to gradually displace the chromatographic buffer solution in the filler, and finally the solution in the filler is the elution reagent A, namely the elution reagent A is 100%.

Preferably, the elution process is performed with glycine buffer as the reagent used in step b.

Preferably, during said elution, the reagents used in step e comprise Tris and MgCl₂。

Preferably, the filler of anion exchange chromatography is a strong anion exchange chromatography filler (Q) or a weak anion exchange chromatography filler (DEAE); the strong anion exchange chromatography filler can be selected from Unigel-30Q, UniGel-50Q, NanoGel-50Q, and the weak anion exchange chromatography filler can be selected from Unigel-DEAE, Unicore-DEAE, DEAE-Sepharose F.F, DEAE-Sepharose CL-6B.

Preferably, the packing for cation exchange chromatography is strong cation exchange packing (SP) or weak cation exchange packing (CM); the filler of the strong cation exchange chromatography filler can be selected from Unigel-30SP, Unigel-80SP, Sepharose-SP and Nanogel-50SP, and the weak cation exchange filler can be selected from Unigel-30CM, Unigel-80CM, Unicore-CM and CM-Sepharose F.F.

Preferably, the chromatography buffer in step a is 10-50mM sodium acetate buffer, pH4.5-4.8, and the elution reagent A comprises: 10-50mM sodium acetate buffer solution and 0.5-1M NaCl, pH 4.5-4.8; eluent I is collected from the conductivity of 8 ms/cm.

In the step c, the chromatography buffer is 10-50mM sodium acetate buffer, and the pH is 3.0-3.8, and the elution reagent a comprises: 10-50mM sodium acetate buffer and 0.5-1M NaCl, pH 3.0-3.8; the AAG peak of interest begins to collect at a conductance of 9ms/cm, and only 1 protein peak is produced throughout the elution process.

In the step d, the chromatography buffer is 10-50mM sodium acetate buffer, and the pH is 5.0-5.8, and the elution reagent a includes: 10-50mM sodium acetate buffer and 0.5-1M NaCl, pH 5.0-5.8.

Preferably, the ion exchange chromatography used in the present invention: the chromatographic column is XK26(GE), the filler volume is 50ml, and the column packing height is 10 cm; the elution mode is gradient elution, and the flow rate is as follows: 15ml/min, linear elution volume 800 ml.

To ensure the purification effect, the elution process is performed after the flow-through process is completed.

Preferably, in step b, the buffer for affinity chromatography equilibration is PBS or PB, more preferably 5-40mM PBS.

In step b, the affinity chromatography steps are specifically as follows: after the affinity chromatography column is balanced by PBS buffer solution, eluent I is added for affinity chromatography, firstly, flow-through liquid II flows out, then, elution reagent B is added, and HP protein attached to the HP affinity column is eluted; the elution reagent B may be selected from glycine buffer, and the pH of the glycine buffer is preferably 2.7.

The buffer solution for balancing in the step e is PBS or 20-50mM Tris buffer solution, preferably 20-50mM Tris buffer solution, after the affinity chromatography column is balanced by Tris pH7.4 buffer solution, the flow-through solution III is added for affinity chromatography, firstly, the flow-through solution IV flows out, then, the elution reagent C is added, and the AAT protein attached to the AAT affinity column is eluted; the elution reagent C is: 25mM Tris, 2M MgCl₂The eluent IV preferably has a pH of 7.4.

The invention also provides another purification method, which comprises the following steps:

a. dialyzing the serum into a chromatography buffer solution with the pH value of 4.5-5.8 to obtain a dialyzed sample, purifying the sample by anion exchange chromatography, and collecting a flow-through solution I and an eluent I;

b. adjusting pH of the flow-through solution I to 5.2-5.5, purifying by cation exchange chromatography, adjusting pH to 5.3-5.5, and purifying by anion exchange chromatography to obtain TRF protein;

c. purifying the eluent I by affinity chromatography to obtain flow-through liquid II and HP protein;

d. carrying out affinity chromatography on the flow-through liquid II to obtain flow-through liquid III and AAT protein;

e. dialyzing the flow-through liquid III into a chromatography buffer solution with the pH value of 3.0-3.8 to obtain dialyzed flow-through liquid III, purifying the dialyzed flow-through liquid III by anion exchange chromatography, and collecting AAG.

Preferably, the anion/cation exchange chromatography and the affinity chromatography each comprise four processes of equilibration, loading, flow-through and elution.

Preferably, the chromatography buffer is an acidic buffer, and can be selected from an acetic acid buffer, a phosphate buffer, a hydrochloric acid buffer and a carbonic acid buffer; more preferably an acetate buffer.

Preferably, during the equilibration, the reagent for anion/cation exchange chromatography is a chromatography buffer, and the reagent for affinity chromatography is an equilibration buffer.

More preferably, the equilibration buffer is selected from PBS, PB or Tris buffers.

Preferably, in the elution process, elution reagent a is used in steps a, b and e, and the elution reagent a comprises: sodium acetate buffer and NaCl.

Preferably, the elution process is performed with glycine buffer as the reagent used in step c.

Preferably, the reagents used in step d include Tris and MgCl₂。

Preferably, the filler of anion exchange chromatography is a strong anion exchange chromatography filler (Q) or a weak anion exchange chromatography filler (DEAE).

Preferably, the packing for cation exchange chromatography is strong cation exchange chromatography packing (SP) or weak cation exchange chromatography packing (CM).

The invention also provides another purification method, which comprises the following steps:

a. dialyzing the serum into a chromatography buffer solution with pH of 4.2-5.0 to obtain a dialyzed sample, purifying the sample by cation exchange chromatography, and collecting a flow-through solution I and an eluent I.

b. Purifying the flow-through liquid I by affinity chromatography to obtain flow-through liquid II and HP protein;

c. purifying the eluent I by affinity chromatography to obtain flow-through liquid III and AAT protein;

d. dialyzing the flow-through liquid II into a chromatography buffer solution with the pH value of 3.0-3.8 to obtain a dialyzed flow-through liquid II, purifying the dialyzed flow-through liquid II by anion exchange chromatography, and collecting AAG protein;

e. dialyzing the flow-through liquid III into a chromatography buffer solution with the pH value of 5.3-5.5 to obtain dialyzed flow-through liquid III, and purifying the dialyzed flow-through liquid III by anion exchange chromatography to obtain TRF protein.

Preferably, the anion/cation exchange chromatography and the affinity chromatography each comprise four processes of equilibration, loading, flow-through and elution.

Preferably, the chromatography buffer is an acidic buffer, and can be selected from an acetic acid buffer, a phosphate buffer, a hydrochloric acid buffer and a carbonic acid buffer; more preferably an acetate buffer.

Preferably, during the equilibration, the reagent for anion/cation exchange chromatography is a chromatography buffer, and the reagent for affinity chromatography is an equilibration buffer.

More preferably, the equilibration buffer is selected from PBS, PB or Tris buffers.

Preferably, during the elution, elution reagent a is used in steps a, d, e, and the elution reagent a comprises: sodium acetate buffer and NaCl.

Preferably, the elution process is performed with glycine buffer as the reagent used in step b.

Preferably, the reagents used in step c include Tris and MgCl₂。

Preferably, the filler of anion exchange chromatography is a strong anion exchange chromatography filler (Q) or a weak anion exchange chromatography filler (DEAE).

Preferably, the packing for cation exchange chromatography is strong cation exchange chromatography packing (SP) or weak cation exchange chromatography packing (CM).

The invention also provides another purification method, which comprises the following steps:

a. dialyzing the serum into a chromatography buffer solution with the pH value of 3.5-4.0 to obtain a dialyzed sample, purifying the sample by cation exchange chromatography, and collecting a flow-through solution I and an eluent I;

b. dialyzing the eluent I into a chromatography buffer solution with the pH value of 3.0-3.8 to obtain a dialyzed eluent I, purifying the dialyzed eluent I by anion exchange chromatography, and collecting AAG protein;

c. affinity chromatography purification of the flow-through liquid I to obtain flow-through liquid II and HP protein;

d. affinity chromatography purification of the flow-through liquid II to obtain flow-through liquid III and AAT protein;

e. dialyzing the flow-through liquid III into a chromatography buffer solution with the pH value of 5.3-5.5 to obtain dialyzed flow-through liquid III, and purifying the dialyzed flow-through liquid III by anion exchange chromatography to obtain TRF protein.

Preferably, the anion/cation exchange chromatography and the affinity chromatography each comprise four processes of equilibration, loading, flow-through and elution.

Preferably, the chromatography buffer is an acidic buffer, and can be selected from an acetic acid buffer, a phosphate buffer, a hydrochloric acid buffer and a carbonic acid buffer; more preferably an acetate buffer.

Preferably, during the equilibration, the reagent for anion/cation exchange chromatography is a chromatography buffer, and the reagent for affinity chromatography is an equilibration buffer.

More preferably, the equilibration buffer is selected from PBS, PB or Tris buffers.

Preferably, in the elution process, elution reagent a is used in steps a, b and e, and the elution reagent a comprises: sodium acetate buffer and NaCl.

Preferably, the elution process is performed with glycine buffer as the reagent used in step c.

Preferably, the reagents used in step d include Tris and MgCl₂。

Preferably, the filler of anion exchange chromatography is a strong anion exchange chromatography filler (Q) or a weak anion exchange chromatography filler (DEAE).

Preferably, the packing for cation exchange chromatography is strong cation exchange chromatography packing (SP) or weak cation exchange chromatography packing (CM).

The technical effects are as follows:

1. realizes the extraction of protein with low content in blood with high purity and high yield. According to the previous experimental results, the protein is directly purified in the serum by an affinity chromatography mode, and the purified target protein has low purity and great influence on the yield because of a great amount of interfering substances; the target protein is enriched and decontaminated through ion exchange chromatography, and then purified through affinity/ion exchange chromatography and other modes, so that the problems of purity and yield can be effectively solved.

2. The simultaneous extraction of four desired proteins from the same sample is achieved. At present, there is no report that AAT, AAG, HP and TRF 4 proteins are purified simultaneously in the same human serum at home and abroad, most of the proteins are respectively purified on the basis of Cohn components IV, the purity and the activity of the proteins cannot be guaranteed, and the repeatability is low.

The invention reasonably designs an experimental scheme mainly according to the difference of isoelectric points of proteins, and purifies by combining anion-cation exchange packing with affinity chromatography; simple purification mode, mild purification condition, low cost and contribution to scale-up production. The obtained target protein has the characteristics of stable activity, high purity, high yield and the like. Therefore, the method has higher application value and potential.

Drawings

FIG. 1: HP, AAG, AAT, TRF enrichment gel map

FIG. 2: purification of HP

FIG. 3: purification of AAG

FIG. 4: purification of AAT

Detailed Description

In the examples of ion exchange chromatography, the volume of the used packing is 50ml, and the height of the packed column is 10 cm; the elution mode is as follows: elution with a gradient of 0-100% elution reagent a, flow rate: 15ml/min, linear elution volume 800 ml. The elution reagent A is: 20mM sodium acetate buffer and 0.5M NaCl.

The eluent and flow-through are not related in each example and are individually numbered.

Example 1: HP, AAG, AAT and TRF are separated and purified from human blood.

The fillers used for anion exchange chromatography are: Unicore-DEAE, and the filler used for cation exchange chromatography is: unigel-80 SP.

1. Dialyzing the sample human serum into a chromatography buffer solution (pH 4.7) to obtain a dialyzed sample, and purifying the dialyzed sample by anion exchange chromatography; the chromatography buffer solution is: 10-50mM sodium acetate buffer, pH 4.7, equilibrating the anion exchange chromatography column with chromatography buffer, then eluting with a gradient of 0-100% elution reagent A, pH 4.7 of 0-100% elution reagent A, collecting flow-through I and eluate I; at pH 4.7, flow-through I contained both TRF and AAT proteins and eluent I contained both HP and AAG proteins.

2. Balancing the HP affinity chromatographic column with 20mM PBS, loading the eluent I into the HP affinity chromatographic column for purification, and collecting the flow-through liquid II flowing out first, wherein the flow-through liquid II contains AAG protein; glycine buffer solution with pH 2.7 was added to elute HP attached to the affinity chromatography packing, and HP was collected.

3. Dialyzing the flow-through solution II into a chromatography buffer solution (pH 3.4) to obtain a dialyzed flow-through solution II, and purifying the dialyzed flow-through solution II by anion exchange chromatography, wherein the chromatography buffer solution is as follows: 10-50mM sodium acetate buffer solution, pH 3.4, balancing anion exchange chromatography column with chromatography buffer solution, then gradient-eluting with 0-100% elution reagent A, and collecting AAG; the pH of 0-100% elution reagent a was 3.4.

4. The pH of flow-through I was adjusted to 5.2 and purified by cation exchange chromatography with the following buffer: 10-50mM sodium acetate buffer, pH 5.2. Equilibrating the cation exchange chromatography column with a chromatography buffer, followed by gradient elution with 0-100% of an elution reagent a, the pH of 0-100% of elution reagent a being 5.2, collecting eluate II and flow-through III; eluent II contains TRF protein, and flow-through liquid III contains AAT protein.

5. Further purifying the flow-through III, equilibrating the affinity column with 25mM Tris pH7.4 buffer, adding the flow-through III to the AAT affinity column, removing the flow-through that had previously flowed out, adding 25mM Tris pH7.4 and 2M MgCl₂Eluting to obtain purified AAT protein;

6. further purifying the eluent II, dialyzing the eluent II into a chromatography buffer (pH 5.3) to obtain a dialyzed eluent II, and purifying the dialyzed eluent II by anion exchange chromatography, wherein the chromatography buffer is: and (3) balancing an anion exchange chromatography column by using a chromatography buffer solution with the pH value of 5.3 in a 10-50mM sodium acetate buffer solution, and then carrying out gradient elution by using 0-100% of an elution reagent A, wherein the pH value of 0-100% of the elution reagent A is 5.3, so as to obtain the TRF protein.

The results of purity and yield of the four proteins after purification are given in the table below, and it can be seen that with the process, a high quality protein sufficient for industrial production can be obtained.

Table one: yield and purity of alpha 1-antitrypsin, alpha 1-acid glycoprotein, haptoglobin and transferrin

Example 2: and separating and purifying AAT, AAG, HP and TRF from human blood.

The fillers used for anion exchange chromatography are: Unigel-30Q, and the filler used for cation exchange chromatography is: unigel-30 SP.

1. Dialyzing the sample human serum into a chromatography buffer solution (pH 5.0) to obtain a dialyzed sample, and purifying the dialyzed sample by anion exchange chromatography; the chromatography buffer solution is: equilibrating the anion exchange chromatography column with a chromatography buffer at pH 5.0 in 10-50mM sodium acetate buffer, followed by gradient elution with 0-100% elution reagent a at pH 5.0, collecting flow-through I and eluate I; at pH 5, flow-through I contained TRF protein and eluent I contained three proteins AAT, HP and AAG.

2. Adjusting the pH of the flow-through solution I to 5.3, and purifying by using cation exchange chromatography packing, wherein the chromatography buffer is: equilibrating the cation exchange chromatography column with a chromatography buffer at pH 5.3 in 10-50mM sodium acetate buffer, followed by gradient elution with 0-100% elution reagent a at pH 5.3, adjusting pH to 5.5 with acetic acid, and purifying by anion exchange chromatography with a chromatography buffer: and (3) balancing an anion exchange chromatography column by using a chromatography buffer solution with the pH value of 5.5 in a 10-50mM sodium acetate buffer solution, and then carrying out gradient elution by using 0-100% of an elution reagent A, wherein the pH value of 0-100% of the elution reagent A is 5.5, so as to obtain the TRF protein.

The results are shown in FIG. 1: m: marker, lane 1 is a sample, lane 2 is a TRF band passed through a cation exchange chromatography column, lane 3 is a TRF purified band after anion exchange chromatography, lane 4: lane 5 shows the removed main impurities, and it can be seen from the figure that the purified band is clean, the amount of protein is large, the purification effect is good, and the removed impurities are many, indicating that the purified protein has high purity.

3. Balancing affinity chromatography column with 20mM PBS, loading eluate I into HPT affinity chromatography column for purification, collecting first effluent flow-through liquid II containing AAG protein and AAT protein; glycine buffer solution with pH 2.7 was added to elute HP attached to the affinity chromatography packing, and HP was collected.

The results are shown in FIG. 2, where M: marker, lane 1: HP non-denatured gel band, lane 2: HP denaturation band. Since HP protein is a polymer mixture, the non-denatured glue has multiple bands of about 100KD, while the denatured glue picture has 3 electrophoretic bands, and since HP itself is a polymer, the result shows that the HP has good purification effect and no miscellaneous bands.

4. Further purifying the flow-through liquid II, balancing the affinity chromatography column by using 25mM Tris buffer solution with pH7.4, then adding the flow-through liquid II into the AAT affinity chromatography column, and collecting the flow-through liquid III, wherein the flow-through liquid III contains AAG protein; adding 25mM Tris pH7.4 and 2M MgCl₂And eluting to obtain the purified AAT protein.

The results are shown in FIG. 4, where M: marker, lanes 1 and 2 are AAT purified bands, which are clear, indicating that the purification effect is good.

5. Dialyzing the flow-through solution III into a chromatography buffer solution (pH 3.4) to obtain a dialyzed flow-through solution III, and purifying the dialyzed flow-through solution III by anion exchange chromatography, wherein the chromatography buffer solution is as follows: 10-50mM sodium acetate buffer, pH 3.4; performing gradient elution by using 0-100% of elution reagent A, and collecting AAG; the pH of 0-100% elution reagent a was 3.4.

The results are shown in FIG. 3, where M: marker, lanes 1 and 2 are AAG bands, and it can be seen from the figure that the bands are clean, indicating that the purification effect is good.

The purity and yield results of the four purified proteins are shown in table two below, and it can be seen that with the process, high quality proteins sufficient for industrial production can be obtained.

Table two: yield and purity of alpha 1-antitrypsin, alpha 1-acid glycoprotein, haptoglobin and transferrin

Example 3

The fillers used for anion exchange chromatography are: NanoGel-50Q, and the fillers used for cation exchange chromatography are: Unicore-CM.

1. Dialyzing the sample human serum into a chromatography buffer solution (pH 4.5) to obtain a dialyzed sample, and purifying the dialyzed sample by anion exchange chromatography; the chromatography buffer solution is: equilibrating the anion exchange chromatography column with a chromatography buffer at pH4.5 in 10-50mM sodium acetate buffer, followed by gradient elution with 0-100% elution reagent a at pH4.5, collecting flow-through I and eluate I; at pH4.5, flow-through I contained both HP and AAG proteins and eluent I contained both AAT and TRF proteins.

2. Balancing affinity chromatography column with 20mM PBS, loading the flow-through solution I into HPT affinity chromatography column for purification, collecting flow-through solution II flowing out first, wherein the flow-through solution II contains AAG protein; glycine buffer solution (pH 2.7) was added to elute HP adhered to the affinity column, and the HP was collected.

3. Balancing the AAT affinity chromatographic column by using 25mM Tris pH7.4 buffer solution, adding eluent I into the balanced affinity chromatographic column, and collecting flow-through liquid III, wherein the flow-through liquid III contains TRF protein; adding 25mM Tris pH7.4 and 2M MgCl₂And eluting to obtain the purified AAT protein.

4. The flow-through II was dialyzed into a chromatography buffer (pH 3.3), adjusted to pH3.3 with acetic acid, and purified by anion exchange chromatography, the chromatography buffer being: 10-50mM sodium acetate buffer, pH3.3, balancing anion exchange chromatography column with chromatography buffer, then gradient-eluting with 0-100% elution reagent A, collecting AAG; the pH of 0-100% elution reagent a was 3.3.

5. The flow-through III was dialyzed into chromatography buffer (pH 5.3) and purified by anion exchange chromatography, the chromatography buffer being: and (3) balancing an anion exchange chromatography column by using a chromatography buffer solution with the pH value of 5.3 in a 10-50mM sodium acetate buffer solution, and then carrying out gradient elution by using 0-100% of an elution reagent A, wherein the pH value of 0-100% of the elution reagent A is 5.3, so as to obtain the TRF protein.

The results of purity and yield of the four purified proteins are shown in table three below, and it can be seen that with the process, a high quality protein sufficient for industrial production can be obtained.

Table three: yield and purity of alpha 1-antitrypsin, alpha 1-acid glycoprotein, haptoglobin and transferrin

Example 4

The fillers used for anion exchange chromatography are: DEAE-sepharose f.f, the packing used for cation exchange chromatography was: Sepharose-SP.

1. The sample human serum was dialyzed into a chromatography buffer (pH 3.6) and the serum was purified by cation exchange chromatography. The chromatography buffer solution is: equilibrating the cation exchange chromatography column with a chromatography buffer at pH 3.6 in 10-50mM sodium acetate buffer, followed by gradient elution with 0-100% elution reagent a at pH 3.6, collecting flow-through I and eluate I; at a pH of 3.6, flow-through I contained three proteins, HP, TRF and AAT, and eluent I contained AAG protein.

2. The AAG protein was further purified by dialysis of eluent I into chromatography buffer (pH 3.5) and purification by anion exchange chromatography, the chromatography buffer being: 10-50mM sodium acetate buffer, pH3.5, using chromatography buffer to balance anion exchange chromatography column, then using 0-100% elution reagent A gradient elution, collecting AAG protein.

3. Balancing the flow-through liquid I with 20mM PBS, loading the balanced flow-through liquid into an HPT affinity chromatography filler for purification, and collecting a flow-through liquid II flowing out first, wherein the flow-through liquid II contains TRF and AAT proteins; glycine buffer solution with pH 2.7 was added to elute HP attached to the affinity chromatography packing, and HP was collected.

4. Equilibrating with 25mM Tris pH7.4 buffer, then adding flow-through II to AAT affinity chromatography packing, collecting flow-through III, which contains TRF protein; adding 25mM Tris pH7.4 and 2M MgCl₂And eluting to obtain the purified AAT protein.

5. The flow-through III was dialyzed into chromatography buffer (pH 5.5) and purified by anion exchange chromatography, the chromatography buffer being: and (3) balancing an anion exchange chromatography column by using a chromatography buffer solution with the pH value of 5.5 in a 10-50mM sodium acetate buffer solution, and then carrying out gradient elution by using 0-100% of an elution reagent A, wherein the pH value of 0-100% of the elution reagent A is 5.5, so as to obtain the TRF protein.

The results of purity and yield of the four purified proteins are shown in table four below, and it can be seen that with the process, a high quality protein sufficient for industrial production can be obtained.

Table four: yield and purity of alpha 1-antitrypsin, alpha 1-acid glycoprotein, haptoglobin and transferrin

Example 5 recovery rate experiments for HP, AAG, AAT, TRF

The method comprises the following steps: respectively taking 0.5g of the four purified and dried proteins, adding the four purified and dried proteins into 1L of human blood, purifying the human blood added by adopting the process method in the embodiment 1, and then calculating the recovery rates of the four proteins, wherein the recovery rate calculation formula is as follows: purification yield after sample addition-purification yield)/sample addition amount, and the experimental results are shown in table five.

Table five: sample-adding recovery rate of alpha 1-antitrypsin, alpha 1-acid glycoprotein, haptoglobin and transferrin

The results show that: the sample recovery rate ranges from 88% to 105%, which shows that the repeatability of the process method is good.

Example 6HP, AAG, AAT, TRF recovery test

The method comprises the following steps: 0.5g of the four purified and dried proteins are respectively added into 1L of human blood, the process method in the example 2 is adopted, the recovery rates of the four proteins are calculated, and the experimental results are shown in the table six.

Table six: sample-adding recovery rate of alpha 1-antitrypsin, alpha 1-acid glycoprotein, haptoglobin and transferrin

The results show that: the sample recovery rate ranges from 80% to 120%, which shows that the repeatability of the process method is good.

Example 7 recovery rate experiments for HP, AAG, AAT, TRF

The method comprises the following steps: 0.5g of the four purified and dried proteins are respectively added into 1L of human blood, the process method in the example 3 is adopted, the recovery rates of the four proteins are calculated, and the experimental results are shown in the seventh table.

TABLE VII: sample-adding recovery rate of alpha 1-antitrypsin, alpha 1-acid glycoprotein, haptoglobin and transferrin

The results show that: the sample recovery rate ranges from 84% to 103%, which shows that the repeatability of the process method is good.

Example 8 recovery rate experiments for HP, AAG, AAT, TRF

The method comprises the following steps: 0.5g of the four purified and dried proteins are respectively added into 1L of human blood, the process method in the example 4 is adopted, the recovery rates of the four proteins are calculated, and the experimental results are shown in the table eight.

Table eight: sample-adding recovery rate of alpha 1-antitrypsin, alpha 1-acid glycoprotein, haptoglobin and transferrin

The results show that: the sample recovery rate ranges from 84% to 110%, which shows that the repeatability of the process method is good.