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Method of inclusion body protein renaturation and purification at the same time

A protein renaturation and inclusion body technology, applied in the field of inclusion body protein renaturation and simultaneous purification, can solve problems such as being unsuitable for industrial production, unsuitable for large-scale production, increasing operation steps and operation time, etc. Small active recovery, suitable for large-scale production, and the effect of saving operation time

Inactive Publication Date: 2003-04-16
INST OF PROCESS ENG CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The disadvantages of the general renaturation method are: mainly the low renaturation rate at low concentration, so that the whole process requires a large amount of buffer solution, a large volume of containers, and a large amount of operating time, which greatly reduces the production efficiency and increases the production efficiency. Cost of production
Dilution method is to directly dilute the inclusion body protein with refolding buffer to achieve the purpose of refolding. There are long refolding time, large amount of buffer, and large container volume, which are not suitable for large-scale production; and The refolding method of dialysis is to put the inclusion body protein in the dialysis bag, and gradually dialyze the deformation agent in the bag with the constantly changing refolding buffer to achieve the purpose of refolding. The disadvantage is that it is easy to cause protein and dialysis membrane The adsorption between the two methods, and because the refolding buffer needs to be replaced frequently, the operation steps and operation time are increased; both methods have a large buffer volume, which not only brings inconvenience to the subsequent purification process, but also increases the use of the buffer The production cost is increased, and the processing capacity of the equipment must be increased, which is not suitable for industrial production;
Washing the refolded protein with a buffer that does not contain a denaturant not only reduces the yield of refolding, but also some target proteins are adsorbed on the chromatographic medium and are not eluted from the column, resulting in a low quality recovery of the protein, and Contaminated column
Some people use this process to refold and denature the natural lysozyme protein, and the mass yield of the protein is only about 10%.

Method used

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  • Method of inclusion body protein renaturation and purification at the same time
  • Method of inclusion body protein renaturation and purification at the same time
  • Method of inclusion body protein renaturation and purification at the same time

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0032] Embodiment 1, the natural chicken egg white lysozyme of renaturation denaturation:

[0033] The ion-exchange chromatography column used in this example is a SP Sepharose Fast Flow prepacked column with a column volume of 5 mL;

[0034] The buffer solution for dissolving natural chicken egg white lysozyme is 0.05mol / L Tris-HCL, pH6.0, and contains 8mol / L urea and 0.1mol / L DTT;

[0035] Equilibrium, loading and washing buffer (mobile phase I) is 0.05mol / L Tris-HCL, pH6.0, and contains 6mol / L urea and 3mmol / L GSD, 0.3mmol / L GSSG;

[0036] The elution buffer (mobile phase II) is 0.1mol / L Tris-HCl, pH9.5, and contains 1mol / L urea, 0.3mol / L NaCl, 3mmol / L GSH, 0.3mmol / L GSSG;

[0037] Loading 8mg of denatured natural chicken egg white lysozyme, the flow rate used is 0.4mL / min, a gradient of one column volume (5mL); the gradient of urea concentration in the process of denaturation and purification (from 6mol / L to 1mol / L) and A pH gradient (pH increase from 6 to 9.5) achieved ...

Embodiment 2

[0038] Example 2, renaturation and simultaneous purification of inclusion body protein Fe-SOD

[0039] The ion-exchange chromatography column used in this example is a Q Sepharose Fast Flow prepacked column with a volume of 5 mL;

[0040] The buffer solution for dissolving inclusion body protein Fe-SOD is 0.05mol / L PBS buffer solution, pH8.5, and contains 10mol / L urea and 3% Triton X-100;

[0041] Equilibration and injection buffer (mobile phase I) is 0.05mol / L PBS, pH8.5, and contains 6mol / L urea, 0.01mol / L FeCl 3 and 3% Triton X-100;

[0042] Elution buffer (mobile phase II) is 0.1mol / L PBS, pH6.5, and contains 1mol / L urea, 0.01mol / L FeCl 3 , 0.2% Triton X-100, 0.2mol / L NaCl;

[0043] Load 4mg of inclusion body protein Fe-SOD refolding solution, flow rate of 0.3mL / min, gradient of two column volumes.

[0044] This process uses an elution buffer (mobile phase II) containing mixed denaturants (urea and Triton X-100), which increases the solubility of the inclusion body pro...

Embodiment 3

[0046] Example 3: Renaturation and Simultaneous Purification of Inclusion Body Protein Human Lysozyme

[0047] The ion exchange chromatography column used in this example is SP Sepharose Fast Flow 7mL;

[0048] The buffer solution for dissolving inclusion body protein is 0.05mol / L Tris-HCl, pH5.5, and contains 8mol / L urea and 0.1mol / L dithiothreitol (DTT);

[0049] Loading buffer (mobile phase I) is 0.05mol / L Tris-HCl, pH5.5, and contains 6mol / L urea, 3mmol / L GSH and 0.3mmol / L GSSG;

[0050] The elution buffer (mobile phase II) is 0.1mol / L Tris-HCl, pH10.0, and contains 1mol / L urea, 0.2mol / L (NH 4 ) 2 SO 4 , 3mmol / L GSH and 0.3mmol / L GSSG, the flow rate is 0.4mL / min, a gradient of one column volume, and 8mg of sample protein;

[0051] The average specific activity of the protein after renaturation is 42618U / mg, the protein yield is 98%, and the final protein concentration is 1-1.2mg / mL; the renaturation time is shortened from 8.5 hours for dilution renaturation to 2 hours ...

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Abstract

A process for renaturating and purifying the inclusion body protein includes such steps as dissolving the inclusion body protein in acidic / alkaline flowing phase or other solution, loading it in the ion-exchange chromatographic column, reversible adsorbing it by the chromatographic medium, and modifier concentration gradient elution. Its advantages are high concentration and activity of recovered protein and high purity.

Description

field of invention [0001] The invention belongs to the field of biotechnology, in particular to a method for refolding and simultaneously purifying inclusion body proteins. Background technique [0002] The development of biotechnology has made it possible to produce target proteins on a large scale. Some proteins that are rare and difficult to extract can be efficiently expressed in host cells through transgenic technology, and the most commonly used host cells are Escherichia coli. The expression of target protein in Escherichia coli has the advantages of rapidity, large quantity and low cost. However, the massive expression of foreign proteins in Escherichia coli often forms protein aggregates, namely inclusion bodies. Inclusion bodies are aggregates of randomly stretched peptide chains, without biological activity, and inclusion body proteins need to be dissolved and then refolded. [0003] The renaturation of protein is a difficult and hot...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07K1/18
Inventor 苏志国李明
Owner INST OF PROCESS ENG CHINESE ACAD OF SCI
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