FI80599B - FOERFARANDE FOER RENING AV MAENNISKOLEUKOCYTINTERFERON. - Google Patents

Description

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Method for purifying human leukocyte-derived interferon

FIELD OF THE INVENTION The invention relates to biochemical skills, and more particularly to methods for purifying human leukocyte-derived interferon.

Background of the invention

A method for purifying human leukocyte-10-derived interferon is known per se (see Cantell K.,

Hirvonen S., Interferon System, A Current Review to 1978, Ed. S. Baron, F. Dianzani, 1977, No. 35, page 138), which comprises precipitating proteins with potassium thiocyanate solution, separating the protein precipitate and recovering the desired product by multi-step extraction with ethanolic acidic medium.

This method allows the yield of the desired product with a specific activity of up to 10 .mu.g / mg protein.

However, the desired product having the above-mentioned specific activity can be achieved only if the pH of the medium is accurate to 0.01, which makes the commercial implementation of this method quite questionable.

In addition, the process is laborious because it involves seven to 25 steps of ethanol extraction in an acidic medium.

Also known per se is for the purification of human leukocyte-derived interferon (see Anfinsen CG, Proc. Natl. Acad. Sci., "The Process for Making Interferon", 1974, 71, 3139), which involves precipitation of the original proteins with ammonium sulphate, separation of the protein precipitate. , dissolving the separated precipitate and gel filtration of the desired product.

However, this method does not allow the high yield and high purity of the desired product to be achieved due to the aggregation of interferon with heavy proteins during gel filtration.

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Description of the invention

It is an object of the present invention to provide properly selected gel filtration conditions for a method of purifying human leukocyte-derived interferon so as to ensure a higher yield and higher purity of the desired product.

This intention is achieved by the method of purifying human leukocyte-derived interferon of the present invention, which consists of precipitating the original proteins with ammonium sulfate, separating the protein precipitate, dissolving the separated precipitate, and gel filtrating the desired product to a pH of 2.5 to 9. and containing an anti-aggregation agent, and adding the same amount of buffer equal to 3-5% of the column volume to the column before gel filtration.

Carrying out the precipitation steps of the precipitate in the presence of an anti-aggregating agent allows the degradation of protein complexes, which leads to a better purity and a higher yield of the desired product.

Interferon is unstable in media with pH values above 9.0 and below 2.5.

If the buffer used to dissolve the protein is added to the column before gel filtration in a volume less than 3% of the column volume, a partial reduction of protein complexes occurs during gel filtration, resulting in a lower degree of purity and waste of the desired product.

If more than 5% of the volume of the 30 columns is added to the column, the anti-aggregation agent will penetrate the desired product.

It is recommended to use urea as an anti-aggregation agent in buffer at a concentration of 2.0 to 8.0 M.

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When the urea concentration in the buffer is less than 2.0 M, complete degradation of the protein complexes occurs, resulting in a lower degree of purification of the desired product and its reduced yield.

5 When the urea concentration in the buffer is more than 8.0, a urea precipitate forms.

In another aspect of the present invention, guanidine chloride can be used as an anti-aggregation agent in a buffer at a concentration of 1.0 to 6.0 M.

When the amount of guanidine chloride in the buffer falls below 1.0 M, complete degradation of the protein complexes does not occur, which reduces the degree of purification and yield of the desired product.

As the amount of guanidine chloride in the buffer rises above 6.0 M, precipitation of guanidine chloride occurs.

Best Mode for Carrying Out the Invention

The method of the present invention is carried out as follows.

Ammonium sulfate 20 is added to the original interferon to a concentration of at least 70% saturation to precipitate leukocyte-derived interferon and other proteins. The precipitate is separated by centrifugation. The recovered protein residue is dissolved in a 0.1 M buffer solution having a pH of 2.5 to 9.0 and containing an anti-aggregation agent.

Prior to gel filtration, 3-5% of the volume of the column is added to the gel-containing column with the same anti-aggregation agent.

Gel filtration is performed on a gel with a protein-30 separation range based on molecular weight of 5-70 kD.

As the gel, an ultra gel or any other gel that is relatively stable to the anti-aggregation agent is used to allow efficient separation of proteins with a molecular weight of 5-70 kD.

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Elution of interferon from the column is performed with 0.1-0.2 M buffer at pH 2.5-9.0.

The amount of anti-aggregation agent in the buffer solution and in the gel-filled column is selected on the basis of the specific properties of the starting materials used.

Example 1 4405 g of ammonium sulphate are added to 8810 ml of original interferon (2000 IU / ml, 2 mg / ml protein). The protein precipitate formed is separated by centrifugation.

The recovered protein precipitate is dissolved in 0.1 M phosphate

to a buffer of pH 2.5 containing 8M urea in solution. The K 100/100 column packed with ultra gel is equilibrated with 0.1 M phosphate buffer pH 2.5 and 240 ml (3% of the column volume) of 8 M

15 urea solutions in the same buffer. Immediately thereafter, an interferon solution is added to the column and eluted with 0.1 M phosphate buffer, pH 2.5. The volume of the active fraction collected is 700 ml. The purified product has a specific activity of 500,000 IU / mg protein, a volumetric activity of 100,000 IU / ml and a total activity of 7x10 IU.

Example 2 To 8585 ml of the original interferon (3000 IU / ml, 2 mg / ml protein) is added 4292 g of ammonium sulphate. The protein precipitate formed is separated by centrifugation.

The recovered protein precipitate is dissolved in 0.1 M phosphate drop buffer, pH 6.0, containing 6 M urea. The K 100/100 column packed with ultra gel is equilibrated with 0.1 M phosphate buffer, pH 6.0, and 400 ml (5% of the column volume) of 6 M urea solution in the same buffer are added. Immediately thereafter, an interferon solution is added to the column and eluted with 0.1 M phosphate buffer, pH 6.0. The volume of active fraction collected is 1360 ml. The purified product has a specific activity of 300,000 IU / mg protein, a volumetric activity of 75,000 IU / ml and a total activity of 9.7x10 IU.

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Example 3 To 8270 ml of the original interferon (2480 IU / ml, 1 mg / ml protein) is added 4135 g of ammonium sulphate. The protein precipitate formed is separated by centrifugation.

The recovered protein precipitate is dissolved in 0.1 M phosphate buffer, pH 9.0, containing 4 M urea. The K 100/100 column packed with ultragel is equilibrated with 0.1 M phosphate buffer, pH 9.0, and 320 ml (4% of the column volume) of 4 M urea solution in the same 10 buffers are added. Immediately thereafter, an interferon solution is added to the column and eluted with 0.1 M phosphate buffer, pH 9.0. The volume of active fraction collected is 900 ml. The purified product has a specific activity of 50,000 IU / mg protein, a volume activity of 20,000 IU / ml 7 and a total activity of 1.8x10 IU.

Example 4 To 8980 ml of the original interferon (4960 IU / ml, 3 mg / ml protein) is added 4490 g of ammonium sulphate. The protein precipitate formed is separated by centrifugation.

The recovered protein precipitate is dissolved in 0.1 M phosphate buffer, pH 7.0, containing 2.0 M urea. The K 100/100 column packed with ultra gel is equilibrated with 0.1 M phosphate buffer pH 7.0 and 300 ml (3.75% of the column volume) of a 2 M urea solution in the same buffer are added. Immediately thereafter, an interferon solution is added to the column and eluted with 0.1 M phosphate buffer, pH 7.0. The volume of active fraction collected is 1280 ml. The purified product has a specific activity of 400,000 IU / mg protein, a volumetric activity of 70,000 IU / ml and a total activity of 9.4x10 IU.

Example 5 To 750 ml of the original interferon (3500 IU / ml, 3.3 mg / ml protein) is added 308 g of ammonium sulphate. The protein precipitate formed is separated by centrifugation.

The recovered protein precipitate is dissolved in 0.1 M phosphate-6,80599 dropper buffer containing 1 M guanidine chloride. The K 50/100 column packed with ultra gel is equilibrated with 0.1 M phosphate buffer pH 7.0 and 80 ml (4% of the column volume) of 1M guanidine chloride 5 in the same buffer is added. Immediately thereafter, an interferon solution is added to the column and eluted with 0.1 M phosphate buffer, pH 7.0. The volume of active fraction collected is 200 ml. The purified product has a specific activity of 30,000 IU / mg protein, a volume activity of 10,000,000 IU / ml and a total activity of 6x10 IU.

Example 6 To 760 ml of the original interferon (3500 IU / ml, 3.3 mg / ml protein) is added 310 g of ammonium sulphate. The protein precipitate formed is separated by centrifugation. The recovered protein precipitate is dissolved in 0.1 M phosphate dropper buffer, pH 7.0, containing 6 M guanidine chloride. The K 50/100 column packed with ultra gel is equilibrated with 0.1 M phosphate buffer, pH 7.0, and 60 ml (3% of the column volume) of 20 6 M guanidine chloride in the same buffer are added. Immediately thereafter, an interferon solution is added to the column and eluted with 0.1 M phosphate buffer, pH 7.0. The volume of active fraction collected is 220 ml. The purified product has a specific activity of 35,000 IU / mg of protein, a volume activity of 15,000 IU / ml and a total activity of 6.2x10 10 IU.

Example 7 To 935 ml of the original interferon (2000 IU / ml, 2.0 mg / ml protein) is added 466 g of ammonium sulphate.

The protein precipitate formed is separated by centrifugation.

The recovered protein precipitate is dissolved in 0.1 M phosphate buffer, pH 3, containing 3 M guanidine chloride. The K 50/100 column packed with ultra gel is equilibrated with 0.1 M phosphate buffer pH 3.0 to 35 and 60 ml (3% of the column volume) of 3 M

7 80599 guanidine chloride in the same buffer. Immediately thereafter, an interferon solution is added to the column and eluted with 0.1 M phosphate buffer, pH 3.0. The volume of active fraction collected is 240 ml. The purified product-5a has a specific activity of 96,000 IU / mg protein, a volume activity of 32,000 IU / ml and a total activity of 7.7 x 10 6 IU.

Example 8 To 1230 ml of the original interferon (7000 IU / ml, 3.5 mg / ml protein) is added 613 g of ammonium sulfate.

The protein precipitate formed is separated by centrifugation. The recovered protein precipitate is dissolved in 0.1 M phosphate buffer, pH 8.0, containing 4 M guanidine chloride. The K 50/100 column packed with ultrogel is equilibrated with 0.1 M phosphate buffer pH 8.0 and 60 ml (3% of the column volume) of 4 M guanidine chloride in the same buffer is added. Immediately thereafter, an interferon solution is added to the column and eluted with 0.1 M phosphate buffer, pH 8.0. The volume of the 20 active fractions collected is 250 ml. The purified product has a specific activity of 20,000 IU / mg protein, a volume activity of 10,000 IU / ml and a total activity of 5x106 IU.

Industrial Applicability The present invention can be most successfully used in the pharmaceutical industry according to any method for purifying human leukocyte-derived interferon derived from donor or body blood leukocytes.

Claims (3)

A process for purifying human leukocyte interferon, by precipitating native proteins with ammonium sulfate, separating the protein precipitate, dissolving the separated precipitate, and gel filtration of the desired final product, characterized in that the precipitate is dissolved in a buffer solution having a pH value of 2.5 to 9, and containing an aggregation preventing agent, and that before the gel filtration is started, the same buffer solution is added to the column in an amount of 3-5% calculated on the volume of the column. 2. A process according to claim 1, characterized in that as an aggregation preventing agent in the buffer solution, urea is used in a range of 2-8 mol / l. 3. A process according to claim 1, characterized in that as an aggregation preventing agent in the buffer solution, guanidine chloride is used in a range of 1-6 mol / l.