US3293236A - Process for isolating alpha1-antitrypsin - Google Patents
Process for isolating alpha1-antitrypsin Download PDFInfo
- Publication number
- US3293236A US3293236A US375424A US37542464A US3293236A US 3293236 A US3293236 A US 3293236A US 375424 A US375424 A US 375424A US 37542464 A US37542464 A US 37542464A US 3293236 A US3293236 A US 3293236A
- Authority
- US
- United States
- Prior art keywords
- antitrypsin
- solution
- serum
- exchanger
- buffer
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07K—PEPTIDES
- C07K14/00—Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof
- C07K14/81—Protease inhibitors
- C07K14/8107—Endopeptidase (E.C. 3.4.21-99) inhibitors
- C07K14/811—Serine protease (E.C. 3.4.21) inhibitors
- C07K14/8121—Serpins
- C07K14/8125—Alpha-1-antitrypsin
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J47/00—Ion-exchange processes in general; Apparatus therefor
- B01J47/014—Ion-exchange processes in general; Apparatus therefor in which the adsorbent properties of the ion-exchanger are involved, e.g. recovery of proteins or other high-molecular compounds
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K38/00—Medicinal preparations containing peptides
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S530/00—Chemistry: natural resins or derivatives; peptides or proteins; lignins or reaction products thereof
- Y10S530/827—Proteins from mammals or birds
- Y10S530/829—Blood
- Y10S530/83—Plasma; serum
Definitions
- the present invention relates to a process for isolating o -antitrypsin, in particular from hum-an or animal body fluids, with exchangers which contain carboxymethyl groups.
- the electrophoresis of serum globulins in an alkaline medium produces three principal fractions, the most mobile of which is identified as aglobulin and is in turn comprised of two further mate-rials identified as oqand ri -globulin respectively.
- the 4x globulin fraction contains a -antitrypsinz u antitrypsin is found in the or -globulin.
- u -antitrypsin can be isolated in a simple manner by adjusting an a -antitrypsin-containing solution to a pH-value in the range from 5.0 to 5.5 with a buffer salt molarity of 0.005 to 0.05, treating the said solution with an exchanger containing carboxymethyl groups, separating the a -antitrypsin-containing solution from the exchanger, if desired or required removing in known manner the buffer salt from the solution obtained and isolating a -antitrypsin in known manner.
- human or animal body fluids in particular human serum, animal sera and ascitic fluids which have been adjusted to a pH-value in the range of 5.5 and 5 .0 and comprise a butter salt molarity of 0.005 to 0.05 can 'be used according to the invention.
- the adjustment can be made, for example, by dialyzing the fluid against a 0.005 to 0.05 molar, preferably 0.01 molar, bufier solution having a pH-value ranging from 5.5 to 5 .0, preferably 5.3, by diluting 'with a buffer solution having a pH-value ranging from 5 .0 to 5.5, preferably 5.3, to a buffer salt molarity of 0.005 to 0.05, by using a cationic exchanger, or by removing undesired low molecular Weight substances using the process described in French Patent 1,300,388, with the addition of a 0.005 to 0.05 molar, preferably 0.01 molar, buffer solution having a pH-value in the range from 5.0 to 5.5, preferably 5.3.
- Suitable buffer solutions are, for example, phosphate buffer or acetate bulfer, but preferably an about 0.01 molar citrate buffer having a pH-value of 5.3 is used.
- the adjustment of the solutions to the desired pH-value and to the desired molarity is advantageously carried out at temperatures below room temperature, preferably at temperatures in the range of '0 and C., and dialysis is carried out with stirring.
- dialysis it has proved advantageous to maintain a volume ratio of a -antitrypsin solution to buffer solution of 1:25 to 1:200, preferably 1:50 to 1:100.
- dialysis is carried out for about 4 to 6 hours.
- the active substance may also be isolated by the process of the present invention from impure oq-antitrypsin solutions prepared according to the processes described earlier herein.
- the process of the present invention is advantageously carried out by treating the aqueous a -antitrypsin-containing solutions which have been dialyzed and adjusted to a pH of 5.0 to 5.5 and a buffer salt molarity of 0.005 to 0.05 as described above with an exchanger containing carboxymethyl groups by chromatographing the solution in a column charged with the exchanger.
- the latter is advantageously Wetted with buffer solution, for example with the buffer used for dialysis.
- the socalled batch process may be used, in which the solution is brought into mechanical contact with the adsorbing agent, preferably with stirring.
- all exchangers may be used, provided they contain carboxymethyl groups.
- carboxyrnethylpolysaccharides for example, carboxymethyl cellulose
- Cross-linked dextrans which are etherified with carboxymethyl groups, obtainable by the process described in US. Patent 3,042,667, proved particularly advantageous.
- the accompanying substances are bound by the adsorbing agent, whereas the a aant-itrypsin is not adsorbed.
- the purified a -antitrypsin solution runs off at the bottom of the column and is collected there. It is advantageous to wash the column with a buffer solution having the same composition as that used for dialysis.
- the aqueous phase is separated in known manner, for example by filtration or centrifugation.
- the buffer salts can then be eliminated from the solution in known manner, for example by dialysis.
- the dialyzed solution is suitably lyophilized.
- the process of the present invention offers the advantage that it can be carried out rapidly and under mild, but above all under sterile, conditions and that it permits the isolation of a -antitrypsin in good yields even from crude serum.
- the biological activity is fully maintained in the process of the present invention.
- a further particular advantage of the present process is that when using serum as starting material, the other biologically valuable serum proteins such as gamma globulin, albumin and others can be eluted from the exchanger and recovered.
- the product obtained by the process is immuno-eleo trophoretically uniform against anti-human-serums from rabbits.
- the a -antitrypsin obtained according to the present in vention binds trypsin, plasmin or chymotrypsin and there by inhibits the activity of trypsin, pl asmin or chymotrypsin.
- a -antitrypsin is therapeutically important in cases of pancreatitis and burns, since it is able to inhibit the enzymatic activity of trypsin. (Plasmin is present in the blood and plays a role in blood coagulation.)
- the product of the present invention serves for the preparation of antisera which are of interest for diagnostic purposes. It is, namely, possible to diagnose by means of the antisera the a antitrypsin concentration in sera, particularly a reduction or increase of the a -antitrypsin content in the serum of patients.
- a -antitrypsin dissolved in a 0.85% sodium chloride solution, is injected in increasing antibodies against the injected material. These antibodies are contained in the serum recovered from the blood of the rabbits.
- the a -antitrypsin which normally is present in' the blood in a certain concentration, of the human serum reacts with the antibodies contained in the rabbit serum.
- a precipitate forms in the mixture of both sera, which precipitate appears, for example, in the test tube in the form of flakes or may be made visible in the agar in the form of a white bent line.
- Morbus haemolyticus meanatorum Rheumatic diseases Liver diseases The indicated method represents the most specific test for the detection of a antitrypsin and is an important support for the diagnosis of the above-mentioned diseases.
- Example 1 A column for chromatography, having an internal diameter of 2.3 cm. and a length of 40 cm., is charged up to a height of 30 cm. with a cross-linked dextran etheritied with carboxymethyl groups (CM-Sephadex C-50), hereinafter designated as CMD, equilibrated with a 0.01 molar sodium citrate butter having a pH-value of 5.25 and is then charged with 12 ml. of human serum which had been dialyzed against 1200 ml. of the equilibration bufier for 5 hours at C. with stirring. The column is then washed with 100 ml. of a 0.01 molar sodium citrate buffer having a pH-value of 5.25.
- CMD carboxymethyl groups
- the a -antitrypsin-containing solution is subsequently dialyzed against water at a pH-value of 7 and finally freeze-dried.
- the yield from 12 ml. of human serum amounts to 38 mg. of pure a -antitrypsin.
- Example 2 Into a column (2.3 x 50 cm.) charged with CMD and equilibrated as described in Example 1, there are introduced 20 ml. of fresh human serum which had been dialyzed against 2 liters of 0.01 molar sodium cit-rate buffer having a pH-value of 5.3, for hours at 0 C. and while stirring. The yield of immuno-electrophoretically uniform a antitrypsin is 66 mg.
- Example 2 A column (34x23 cm.) filled with CMD-andequilibrated as described in Example 1 is charged with 10 ml. of a 3.6% serum protein solution obtained by fractionation with ammonium sulfate from human serum and which had been dialyzed against 500 ml. of a 0.01 molar sodium citrate buffer having a pH of 5.3. The operation is carried out as described in Example 1. The yield of oi -antitrypsin is 45 mg.
- Example 4 g. of CMD impregnated with a 0.01 molar sodium citrate buflfer having a pH-value of 5.3 are added to 15 ml. of human serum previously di-alyzed at 0 C. with stirring against 1500 ml. of 0.01 molar sodium citrate buffer; the mixture is stirred for 20 minutes and the Ol antitrypsin containing solution is recovered by centrifugation. The s-oltuion is then dialyzred and freeze-dried as described in Example 1. The yield is 33 mg. of u -antitrypsin.
- a process for isolating a -antitrypsin from a solution comprising human or animal body fluids which process consists solely of 'bufiering said body fluids at a pH between 5.0 and 5.5 with a buffer salt to give a solution containing buffer salt at a molarity between 0.005 and 0.05, contacting the bufiered solution with an exchanger containing carboxymethyl groups to adsorb dissolved serum substances other than a -antitrypsin therefrom and then recovering a -antitrypsin from the solution contacted with said exchanger.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Gastroenterology & Hepatology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Biophysics (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Genetics & Genomics (AREA)
- Medicinal Chemistry (AREA)
- Molecular Biology (AREA)
- Proteomics, Peptides & Aminoacids (AREA)
- Peptides Or Proteins (AREA)
- Medicines That Contain Protein Lipid Enzymes And Other Medicines (AREA)
- Medicines Containing Material From Animals Or Micro-Organisms (AREA)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DEB72263A DE1189674B (de) | 1963-06-12 | 1963-06-12 | Verfahren zur Isolierung von alpha-Antitrypsin |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3293236A true US3293236A (en) | 1966-12-20 |
Family
ID=6977373
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US375424A Expired - Lifetime US3293236A (en) | 1963-06-12 | 1964-06-11 | Process for isolating alpha1-antitrypsin |
Country Status (7)
| Country | Link |
|---|---|
| US (1) | US3293236A (de) |
| AT (1) | AT255027B (de) |
| BE (1) | BE649238A (de) |
| CH (1) | CH443561A (de) |
| DE (1) | DE1189674B (de) |
| GB (1) | GB1062434A (de) |
| NL (1) | NL6406622A (de) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0035204A3 (en) * | 1980-03-05 | 1982-11-10 | Miles Laboratories, Inc. | Pasteurized therapeutically active protein compositions |
| EP0698615A1 (de) * | 1994-08-24 | 1996-02-28 | Bayer Corporation | Reinigung von Alpha-l-proteinaseinhibitor mittels neuen chromatographischen Trennungsbedingungen |
| WO1997009350A1 (en) * | 1995-09-07 | 1997-03-13 | Ppl Therapeutics (Scotland) Ltd. | Purification of alpha-1 proteinase inhibitor |
| US6093804A (en) * | 1998-09-24 | 2000-07-25 | American National Red Cross | Method for purification of alpha-1 proteinase inhibitor |
| US6462180B1 (en) | 1999-11-24 | 2002-10-08 | Bayer Corporation | Method of preparing α-1 proteinase inhibitor |
| EP2295126A1 (de) | 2002-12-31 | 2011-03-16 | CSL Behring LLC | Verfahren zur Reinigung von Alpha-1-Antitrypsin |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3271827D1 (en) * | 1981-05-01 | 1986-07-31 | Medical Research Inst Of San F | Method for isolating alpha-1-antitrypsin |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3002823A (en) * | 1958-04-16 | 1961-10-03 | Pharmacia Ab | Process of separating materials having different molecular weights and dimensions |
| US3042667A (en) * | 1959-03-10 | 1962-07-03 | Pharmacia Ab | Process for producing dextran derivatives and products resulting therefrom |
-
1963
- 1963-06-12 DE DEB72263A patent/DE1189674B/de active Pending
-
1964
- 1964-06-09 CH CH752564A patent/CH443561A/de unknown
- 1964-06-10 AT AT498564A patent/AT255027B/de active
- 1964-06-11 NL NL6406622A patent/NL6406622A/xx unknown
- 1964-06-11 US US375424A patent/US3293236A/en not_active Expired - Lifetime
- 1964-06-12 BE BE649238A patent/BE649238A/xx unknown
- 1964-06-12 GB GB24601/64A patent/GB1062434A/en not_active Expired
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3002823A (en) * | 1958-04-16 | 1961-10-03 | Pharmacia Ab | Process of separating materials having different molecular weights and dimensions |
| US3042667A (en) * | 1959-03-10 | 1962-07-03 | Pharmacia Ab | Process for producing dextran derivatives and products resulting therefrom |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0035204A3 (en) * | 1980-03-05 | 1982-11-10 | Miles Laboratories, Inc. | Pasteurized therapeutically active protein compositions |
| DK156698B (da) * | 1980-03-05 | 1989-09-25 | Miles Inc | Fremgangsmaade til pasteurisering af et materiale indeholdende et termisk foelsomt, terapeutisk aktivtprotein valgt blandt alfa-l-antitrypsin, antithrombin-iii, praekallikrein, antihaemofil faktor (faktorviii) og fibronectin |
| EP0698615A1 (de) * | 1994-08-24 | 1996-02-28 | Bayer Corporation | Reinigung von Alpha-l-proteinaseinhibitor mittels neuen chromatographischen Trennungsbedingungen |
| US5610285A (en) * | 1994-08-24 | 1997-03-11 | Bayer Corporation | Purification of α-1 proteinase inhibitor using novel chromatographic separation conditions |
| US6194553B1 (en) | 1995-09-07 | 2001-02-27 | Ppl Therapeutics (Scotland) Limited | Purification of alpha-1 proteinase inhibitor |
| WO1997009350A1 (en) * | 1995-09-07 | 1997-03-13 | Ppl Therapeutics (Scotland) Ltd. | Purification of alpha-1 proteinase inhibitor |
| US6525176B1 (en) | 1995-09-07 | 2003-02-25 | Ppl (Holdings) Limited | Purification of alpha-1 proteinase inhibitor |
| EP1736483A3 (de) * | 1995-09-07 | 2008-07-30 | Pharming Intellectual Property BV | Reinigung von Alpha-l-Proteinaseinhibitor |
| US6093804A (en) * | 1998-09-24 | 2000-07-25 | American National Red Cross | Method for purification of alpha-1 proteinase inhibitor |
| US6462180B1 (en) | 1999-11-24 | 2002-10-08 | Bayer Corporation | Method of preparing α-1 proteinase inhibitor |
| EP2295126A1 (de) | 2002-12-31 | 2011-03-16 | CSL Behring LLC | Verfahren zur Reinigung von Alpha-1-Antitrypsin |
| EP3006462A1 (de) | 2002-12-31 | 2016-04-13 | CSL Behring LLC | Verfahren zur reinigung von alpha-1-antitrypsin |
| EP3543254A1 (de) | 2002-12-31 | 2019-09-25 | CSL Behring LLC | Verfahren zur reinigung von alpha-1-antitrypsin |
Also Published As
| Publication number | Publication date |
|---|---|
| NL6406622A (de) | 1964-12-14 |
| GB1062434A (en) | 1967-03-22 |
| BE649238A (de) | 1964-12-14 |
| AT255027B (de) | 1967-06-26 |
| DE1189674B (de) | 1965-03-25 |
| CH443561A (de) | 1967-09-15 |
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