METHOD FOR ISOLATING ALPHA-1-ANTITRYPSIN

Abstract: Alpha-1-antitrypsin is isolated from solutions of protein containing alpha-1-antitrypsin, such as human plasma. Isola­ tion is accomplished by breaking sufficient disulfide bonds in the proteins to destabilize them. Reducing agents such as dithiothreitol are used to break the disulfide bonds. The destabilized proteins may be precipitated by salting out. Alpha-1-antitrypsin is not stabilized by disulfide bonds, is therefore not destabilized by the treatment, and can be recovered from the supernatant by chromatographic separa­ tion. Other suitable proteins such as antichymotrypsin may be similarly isolated.

Description: METHOD FOR ISOLATING AL;5HA-1-ANTITRYP SIN BACKGROUND OF THE INVENTION Field of the.fnvention This invention relates to methods for isolating alpha-l-antitrypsin from sources in which it occurs. Other suitable proteins such as antichymotrypsin may be similarly isolated. Suitable proteins include those with disulfide bonds which are not involved in stabilization (as in alpha l-antitrypsin), proteins with stabilizing disulfide bonds which are not chemically accessible to the reagents used for breaking the bonds, and proteins containing no disulfide bonds. In the preferred embodiment, the invention relates to a method for isolating alpha-l-antitrypsin from Cohn fraction IV-I, a subfraction obtained from pooled human plasma. Alpha-l-antitrypsin is a major inhibitor of proteolytic enzymes in human serum. There are about 70,000 to 80,000 people who have a genetic deficiency which results in serum levels of alpha-l-antitrypsin that are only 10-15% of normal. These individuals are strongly disposed to pulmonary emphysema. The lung damage results from the digestive action of improperly regulated enzymes due to the alpha-l-antitrypsin deficiency. There are a number of other acute clinical conditions, including sepsis, pancreatitis, respiratory failure, and cardiopulmonary bypass, where there are indications that excessive proteolysis may be an important contributing factor. The present invention provides a process for obtaining purified alpha-l-antitrypsin for treatment of these disease states. The process produces the desired product through a sequence of steps which are collectively inexpensive, simple, reproducible, and which create a relatively pure product in high yield that is safe for therapeutic use and applicable to large scale industrial processing. Brief Description of the Prior Art "Isolation and Characterization of Alpha-l-Anti- trypsin from the Cohn Fraction IV-I of Human Plasma", by Charles B. Glaser, Lucy Karic and Robert Fallat, Preparative BiochemistrY, 5(4), 1975 pages 333-348, describes the isolation of alpha-l-antitrypsin from pooled human plasma utilizing ion exchange, biospecific affinity and gel exclusion chromatographic procedures. "Evaluation of Alpha-l-Antitrypsin as a Potential Therapeutic Agent", by Allen B. Cohen and Harold James, DHEW Publication &num;(NIH)78-1422, pages 326-388, describes a method for isolating alpha-l-antitrypsin and its potential therapeutic utility. Purification of alpha-l-antitrypsin by chromatographic techniques utilizing the do sulfide group in alphal-antitrypsin is disclosed in "Thiol-Disulfide Interchange Chromatography Using Sepharose-Linked Thiol Compounds to Separate Plasma Proteins", by C.-B. Laurell, Eva Thulin and R.P. Bywater, Analytical Biochemistry, 81 (1977), pages 336-345, and in "Purification of Alpha-l-Antitrypsin from Plasma through Thiol-Disulfide Interchange", by C.-B. Laurell, J. Pierce, U. Persson and F. Thulin, Eur. J. Biochem., 57 (1975) pages 107-113. "Improved Identification of Antitrypsin Phenotypes Through Isoelectric Focusing with Dithioerythritol", by John A. Pierce and Bibiana G. Eradio, J. Lab. Clin. Med., December 1979, pages 826-831, describes the use of dithiothreitol and dithioerythritol for identifying antitrypsin phenotypes through isoelectric focusing. SUMMARY OF THE INVENTION In accordance with the present invention there is provided a method for isolating alpha-l-antitrypsin from a mixture of blood plasma proteins in solution comprising: (a) breaking sufficient disulfide bonds in said proteins to destabilize them, (b) precipitating the destabilized proteins, (c) and recovering non-precipitated alpha-l-antitrypsin from said solution. The term "destabilize" is used in a relative sense and refers to the solubility of the proteins in the solution being treated. A destabilized protein is rendered less soluble than the protein being isolated (alpha-l-antitrypsin in the preferred embodiment) and can therefore be selectively precipitated by appropriate adjustment of the solution conditions, as will be discussed. It will be appreciated that all disulfide bonds present need not be broken to obtain this relative instability. The process contemplates breaking a sufficient number of the bonds so that the desired selective precipitation is obtained. In the preferred embodiment the precipitated proteins are separated first before recovering alpha-lantitrypsin from the supernatant solution. The disulfide bonds are preferably broken with an effective concentration of any suitable reducing agent that is strong enough to reduce protein disulfide bonds, but not reduce other protein bonds such as peptide linkages or other groups which would cause a fragmentation of the protein. Typical reducing agents which might be utilized are monothiols such as 2-mercaptoethanol, mercaptoacetic acid, and cysteine. Suitable nonthiol reducing agents are exemplified by sodium borohydride. Preferably the reducing agent is a dithiol such as dithiothreitol or its stereoisomer dithioerythritol. The dithiols are more effective in this process, forming a ring structure upon reducing a disulfide group to sulfhydryls. This ring formation drives the reaction to completion via favorable entropic effects. Accordingly, sterically favorable dithiols can be used at a concentration of about .01M or higher, usually about .03-.1M. The less effective reducing agents such as monothiols require a minimum concentration of about .lM, usually about .5M-1.5M. The protein solution is preferably adjusted with a buffer to a pH of about 6.0-8.5. Suitable buffers include phosphate and tris. At higher pHs the protein becomes less stable but the higher pHs could be utilized if desired. At pHs below about 6 the alpha-l-antitrypsin tends to denature and aggregate and therefore such lower pHs would usually be less satisfactory. In the protein precipitation step any agent that may lower the solubility of proteins may be utilized such as polyethylene glycol, alcohols such as ethyl alcohol, guanidine, and urea. In the preferred embodiment the protein is salted out with the addition of sufficient salts which may be those typically used for precipitating proteins and preferably will be a divalent salt such as a sulfate. The precipitated proteins may then be separated from the supernatant by any suitable technique such as centrifuging. Alpha-l-antitrypsin is recovered from the supernatant by any one of several methods. Ultrafiltration with hollow fibers may provide acceptable results in many cases. Best results have thus far been obtained by chromatographic separation particularly with DEAE-cellulose columns, although other ion exchange resins or other chromatographic means may be used (gel filtration, hydroxyapatite, immunoadsorbant, affinity columns containing cibacron blue, concanavalin A, DNA, etc.). By selecting a chromatographic column and solvent conditions includng pH and ion concentration under which alpha-l-antitrypsin binds more strongly than the other proteins, protein concentrations in excess of the binding capacity of the column can be introduced. The alpha-l-antitrypsin will bind to the column while the more weakly binding proteins pass through. The alpha-l-antitrypsin can then be eluted with an appropriate stronger solvent. This technique permits the loading of larger amounts of protein onto the column that would otherwise be possible. The present method is particularly effective in that it utilizes the disulfide bond which is present in most known plasma proteins. The reducing agent such as dithiothreitol effectively reduces many of these protein disulfide bonds even in the absence of other denaturants. A primary function of the disulfide bonds is to stabilize the protein structure. Consequently when disulfide bonds are broken the proteins become destabilized in solution. The destabilized proteins may then be readily precipitated by suitable techniques such as salting, heating, change in pH, addition of solvents and the like. The process is presently believed to be effective because alpha-l-antitrypsin has only a single disulfide bond and this bond is not involved in stabilizing the protein chain. The alpha-l-antitrypsin is not thus destabilized with the reduction step and remains in the supernatant solution. If desired, this single disulfide bond can be reconstituted after the reduction step. In the usual case the protein remaining in solution such as alpha-l-antitrypsin is the protein desired and is the one that is recovered for further use. However, the process can also be utilized to separate the precipitated proteins from those in solution when it is desired to recover the precipitated proteins for use in their denatured form or for conversion to some other form. A potential collateral benefit is obtained from use of the present method. The reducing conditions that may be used also serve to effectively destroy the infective properties of any hepatitis virus in the protein source. It is thought that, because the viral coat contains various disulfide containing proteins, it will be denatured under the process conditions and the virus will thereby lose its infectivity. In the preferred embodiment human blood plasma is utilized as the protein solution. Preferably the present process utilizes the Cohn IV-I fraction of blood plasma as a starting material because it is enriched in alpha-l-antitrypsin (6-10% of the protein) and is currently a relatively unused side fraction during the production of albumin and gamma globulin. Cohn IV-I paste contains approximately 25-35% protein, 30-35% alcohol, 30-40% H2O and consists of at least the following proteins: albumin (-15-20%), alpha-l-antitrypsin (-6-10%), alpha-l-antichymotrypsin (-4-6%), ceruloplasmin (2.5%), haptoglobulin (-2%), antithrombin III (-1%), transferrin (-7%), hemopexin, alpha-2-plasmin inhibitor, alpha-l-lipoprotein, plasminogen, fibrinogen, C2, C3, alphal-acid glycoprotein, C1 esterase inhibitor, inter-alphatrypsin inhibitor, C1 esterase inactivator. Regardless of the source, it is preferable that the protein solution used in the process be diluted so that it contains less than about 50mg/ml of protein. Where the concentration is appreciably higher, excessive alpha-i-anti- trypsin may be lost through occlusion in the precipitated proteins. EXPERIMENTAL Materials and Methods Cohn Fraction IV-I was obtained as a frozen, homogenized paste from Cutter Laboratories, Berkeley, California. The trypsin inhibitory capacity (TIC) was determined against crystallized, salt-free, bovine trypsin (Worthington Chemical Company, Freehold, New Jersey) using benzoyl-DL-arginine-p-nitroanilide as a substrate. The percentage of active trypsin was determined by titration with p-nitrophenyl p'-guanidinobenzoate. The concentration of alpha-l-antitrypsin was determined by the radial immunodiffusion method (RID) using rabbit anti-serum to human alpha-l-antitrypsin (Kallestad Labs, Chaska, Minnesota). Specific activity was estimated by dividing the TIC in mg/ml by the protein concentration as determined by the method of Lowry, et al., or by the weight of lyophilized protein (with a 15% moisture correction). The extinction coefficient of alpha-l-antitrypsin is 0.1% E = 0.50 1 cm, 280 nm and was used as a measure of protein concentration and specific activity for purified products. The final product was phenotyped by starch gel electrophoresis with an acidic, discontinuous buffer system, followed by crossed antigen-antibody electrophoresis. Analytical SDS acrylamide gel electrophoresis was performed in 9% gels by the method of Laemmli (1970). Immunoelectrophoresis was carried out by standard procedures on an LKB system. Cohn fraction IV-I paste may be activated by solubilizing in 0.1M buffer at pH 8.5 (phosphate, tris) and dialyzing against 0.01M buffer, pH 7.6 which serves the purpose of removing the alcohol. As will be shown below in Example 1, dialysis to remove alcohol is not essential. Throughout the examples the analytical methods referred to are as described in the following references: TIC = B.F. Erlanger, N. Kokowsky and W. Cohen, Arch. Biochem. Biophys., 95, 271-278 (1961). RID = M. Mancini, A.P. Carbonara and J.F. Heremans, Immunochemistry, 29, 235-254 (1965). Lowry = O.H. Lowry, N.L. Rosebrough, A.J. Farr and H. J. Randall, J. Biol. Chem., 193, 265-272 (1951). Example 1: Activation and Salting Out of Alpha-l-Antitrypsin 100 gm of Cohn IV-I was dissolved in 1.0 liter of 0.1M phosphate at pH 8.5 and the solution was stirred for 3 hours. Undissolved material was removed by filtration. The solution was divided into four aliquots as follows: One aliquot (A) was concentrated directly to 20mg/ml. A second aliquot (B) was first dialysed against 0.01M phosphate, pH 8.5 using a DC-2 Amicon hollow fiber with a 10,000 M.W. cutoff, and then concentrated to 20mg/ml. A third aliquot (C) was concentrated by ultrafiltration to -50mg/ml. The fourth aliquot (D) was dialyzed against 0.01M phosphate at pH 8.5 and then concentrated to 50mg/ml. Four 10ml aliquots of each of these alpha-l-antitrypsin solutions (A-D) were prepared. Half of the solutions were treated with 0.1M dithiothreitol (DTT) for either 3 or 24 hours at 250C, and all samples were then salted out to a final concentration of 50% (NH4)2SO4 at 50C and stirred overnight. This was followed by centrifugation at 3000rpm for 2 hours. The precipitate was washed with 50% (NH4)2SO4 and the supernatants combined. The initial and final trypsin inhibitory capacity were determined for each sample by the TIC assay, as well as the protein content by the method of Lowry. The results are summarized in Table 1. TABLE I Initial Final Specific alpha-1- TIC mg alpha-1- anti- Trypsin antitrypain trypsin inhibited DTT Reduction Initial Final Protein (by TIC) Recovery mg Purifi Reduction Time Protein Protein Recovery (mg) (by TIC) protein cation 0.1 M) (Hrs.) (mg) (mg) (%) corrected** (%) Initial Final Factor A) 20.2 mg.ml + 3 202.0 14.0* * 12.1 6.0* * .06 .43 7.2 no + 24 202.0 20.0 10.0 12.1 9.1 75 .06 .46 7.7 dialysis - 3 202.0 70.0 35.0 12.1 9.0 74 .06 .11 2.2 - 24 202.0 77.0 38.0 12.1 9.1 75 .06 .12 2.0 B) 21.2 mg/ml + 3 212.0 28.0 13.2 12.0 10.9 91 .057 .39 6.8 after + 24 212.0 29.2 13.8 12.0 10.0 84 .057 .34 6.0 dialysis - 3 212.0 72.8 34.3 12.0 11.5 96 .057 .16 2.8 - 24 212.0 91.0 43.0 12.0 9.4 79 .057 .10 1.8 C) 48.7 mg/and + 3 487 57.6 11.8 24.1 20.8 86 .050 .36 7.2 no dialysis + 24 487 48.0 9.9 24.1 18.4 77 .050 .38 7.6 - 3 487 154. 32.0 24.1 19.3 80 .050 .13 2.6 - 24 487 72.6 15.0 24.1 18.7 78 .050 .26 5.2 D) 49.5 mg/ml + 3 497 70.5 14.2 24.6 19.0 77 .050 .27 5.4 after + 24 495 46.0 9.3 24.6 16.2 66 .050 .35 7.0 dialysis - 3 495 158.0 32.0 24.6 16.8 68 .050 .11 2.2 - 24 495 144.0 29.1 24.6 17.2 70 .050 .12 2.4 * Lost some of protein prior to dialysis. ** Corrected for trypsin activity (69%) and for factor 2.17 (obtained by using M.W. of 50,000 for alpha-1-antitrypsin/M.W. of 23,000 for trypsin). Conclusions 1. Dialysis of Cohn IV-I solutions to remove alcohol prior to salting out is not necessary. 2. DTT is highly effective in providing a medium for protein precipitation without adversely affecting the alpha-l-antitrypsin recovery in the supernatant. 3. Protein concentrations in the range of 20-50mg/ml are selectively salted out similarly and quite effectivelt Example 2: To maximize the recovery of antitrypsin, Cohn IV-I was activated as described in Example 1 above without dialysis. The activated solution contained 27.75mg/ml of protein as determined by the Lowry method. The following DTT concentrations were used: 0, 0.2M, 0.03M, 0.05M, 0.01M, 0.20M. For each DTT concentration, separate incubation was performed for 3, 8 and 24 hours. After reduction, each 10ml aliquot was precipitated with lOml of saturated (NH4)2SO4 to a final concentration of 50% at 50C and incubated for 24 hours, then centrifuged, washed, recentrifuged. The supernatants were dialysed against 1 x 4 liter 0.01M phosphate buffer, pH 7.6 containing 0.01M cysteine to reform the disulfide bridge with alpha-l-antitrypsin. A final dialysis against 3 x 4 liter 0.01M phosphate buffer was used to remove excess cysteine. Conclusions The results are seen in Figs. 1 and 2 and indicate: 1. Reduction with dithiothreitol (DTT), followed by precipitation with (NH4)2S04 (50%) is highly effective in removing contaminating proteins from alpha-l-antitrypsin containing protein solutions of Cohn IV-I. 2. The effectiveness of the method is dependent on the concentration of reductant and on the time of reduction. 0.05M DTT treatment for 8 hours is highly effective, giving a purification factor > 8.0 (as compared to 3.0 for the control). Higher levels of DTT are somewhat better, but at an increased cost factor and with only modest improvement. 3. Albumin is completely removed by this treatment. 4. The recovery of alpha-l-antitrypsin activity is 75-80% as determined by TIC, and this closely parallels the recovery found in the absence of DTT. 5. The recovery of immunological activity (radial immunodiffusion) is ¯55-60%. (Note: This is the result of some aggregated alpha-l-antitrypsin in the original Cohn IV-I solution, as will be demonstrated in Example 3. Example 3 To determine whether any antitrypsin aggregate is present in Cohn IV-I, an aliquot of 0.6ml of Cohn IV-I solution, containing 25.3mg/ml of protein and 1.7mg/ml of alpha-l-antitrypsin (determined by TIC), was applied onto a Sephadex G-150 column (1.5 x 91cm) which had been equilibrated with 0.10M NH4HC03. Based on a TIC assay on the eluants, fractions 18-29 had only traces of inhibitory activity, and these were pooled (peak A). Fractions 30-40 containing most of the activity were combined (peak B). TABLE II Total Total alpha- Total alpha Protein l-antitrypsin l-antitrypsin (Lowry) (RID) (TIC-corr.) mg mg mg RID/TIC Peak A 8.4 0.258 0.137 1.90 Peak B 3.6 0.554 0.582 0.95 RID(A) and + RID(B) = 100 0.258 % aggregate = 0.258 + .554 x 100 = 32% Conclusions It appears that Cohn IV-I contains approximately 32% aggregate. This is only an approximation for two reasons: 1) The radial immuno-diffusion assay (RID) will not distinguish between monomeric and polymeric alpha-I- antitrypsin. Polymeric alpha-l-antitrypsin will diffuse less in the agar gel and its concentration will be underestimated. 2) Since the column was not optimal, some monomer could be eluting in peak A, and this would tend to overestimate the alpha-l-antitrypsin polymer. Alternatively, the limited trypsin inhibiting activity seen in peak A may be the result of other higher MW inhibitors known to be present in Cohn IV-I, i.e., alpha-2-macroglobulin, interalpha trypsin inhibitor. Example 4 To test the effect of reduction and salting out on the antitrypsin aggregate, supernatant from reduced-salted out Cohn IV-I was dialysed against 0. iM NH4HCO3 and a one ml aliquot containing 19.lmg of protein and 9.6mg alpha-l-antitrypsin was applied into the Sephadex G-150 column (1.5 x 91cm) equilibrated in the same buffer. The fractions were pooled and labeled A (aggregate peak) and B, and analyzed by various assays as indicated by the summary below. TABLE 111 Total Total alpha-l-antitrypsin alpha-l-antitrypsin RID TIC (corrected) mg mg A O 0 B 4.42 5.5 In conclusion, it seems clear that treatment of Cohn IV-I with DTT followed by (NH4)2S04 salting out effectively removes all aggregated alpha-l-antitrypsin. Example 5 To further determine whether the time of reduction and/or the molarity of reducing agent could be decreased in the salting out scheme, the process was run at 370C. Activated Cohn IV-I was divided into 9.5my aliquots containing 31.9mg/ml protein and treated at 370C for 2, 4 or 8 hours with various concentrations of DTT, or cysteine. Control solutions containing no reductant were also included. All aliquots were then treated to a final concentration of 50% (NH4)2SO4, incubated for 24 hours at 50C, centrifuged at 10,000rpm and the precipitates washed with cold 50% (NH4)2S04. The combined supernatants were dialysed against 1 x 41 of 0.01M phosphate pH 7.6 containing 0.01M cysteine followed by 3 x 41 0.01M phosphate, pH 7.6 without cysteine. The assays performed were TIC, Lowry and albumin radial immunodiffusion. A summary of the results is given in Table IV. TABLE IV % alpha-l-anti- % Protein % Albumin Purifi trypsin Recovery Recovery Recovery cation (by TIC) (Lowry) (RID) Factor 2 Hours Control 88.3 33.0 99.5 3.0 0.01M DTT 78.6 17.0 2.0 5.3 0.05M DTT 78.6 11.3 0 7.3 0.1M DTT 70.9 10.3 0 7.5 0.1M cysteine 83.5 24.0 95.0 3.3 1.0M cysteine 73.3 16.0 21.0 5.0 4 Hours Control 89.0 31.5 99.5 3.0 0.01M DTT 74.2 13.0 7.7 6.3 0.05M DTT 68.0 10.8 0 6.8 0.1M DTT 74.2 9.6 0 8.5 0.1M cysteine 84.8 25.8 89.3 3.5 1.OM cysteine 74.2 12.9 1.5 6.3 8 Hours Control 94.8 32.0 100.0 3.3 0.01M DTT 76.8 13.0 1.0 6.3 0.05M DTT 80.0 11.3 0 7.5 0.1M DTT 73.8 9.4 0 8.5 0.1M cysteine 91.5 24.7 99.0 4.0 1.0M cysteine 79.8 14.9 0 5.8 Conclusions The purification factors obtained with DTT at 370C for 4-8 hours were similar to those at 250C for 24 hours. Cysteine, even at 1M, is not as effective as 0.05M DTT. Example 6 To test the effect of pH on salting out after reduction, Cohn IV-I was activated without the removal of ethanol. For this experiment, salting out was carried out at pH 6.0 and at pH 8.5. 80ml of Cohn IV-I in 0.1M phosphate pH 8.5 (15mg/ml protein by Lowry) was divided into two 40ml samples (A and B). Sample A was treated with 0.1M DTT for 24 hours at room temperature. Sample B was kept as a control (no DTT). Following reduction, sample A was divided into two equal aliquots A1 and A2. A1 was titrated under stirring with 1M HC1 to pH 6.0 (final volume 22.8m1). A2 was diluted with pH 8.5 in order to maintain the same protein concentration as A1. The control sample B was treated similarly. From each aliquot (A1, A2, B1, B2) 20 ml were removed and treated with (NH4)2S04 at 50C to a final concentration of 50% salt. After 24 hours of incubation, the solid ppts were centrifuged at 10,000 rpm, washed and dialyzed against 1 x 41 0.01M phosphate, pH 7.6 containing 0.01M cysteine and 3 x 41 0.01M phosphate pH 7.6 TABLE V alpha-l- Protein Purifi- Albumin pH for antitrypsin Recovery cation Recovery DTT Salting Out Recovery % (Lowry) % Factor RID) % A1 + 6.0 64 8 8 0 A2 + 8.5 85 10 8 0 B1 - 6.0 70 27 2.5 90 B2 - 8.5 83 30 2.8 90 Conclusions Adjustment of the pH to 6 prior to salting out leads to somewhat greater precipitation of overall protein; however the precipitation of alpha-l-antitrypsin is also increased. The net effect is that the purification factor is approximately the same at pH 6 and 8.5. Since the loss of alpha-l-antitrypsin is greater at pH 6, salting out at pH 8.5 seems preferable. Example 7 To determine the purification factor achievable by reduction and salting out in plasma, citrated plasma was diluted 2, 4 or 6-fold, and each solution divided into two equal parts. One part was reduced with 0.1M DTT for 24 hours at 250C and then salted out to 50% (NH4)2SO4. The second part of each diluted plasma was incubated and salted out, but not reduced. The reduced aliquots A, B, C had insoluble protein which were readily removed by centrifugation at 10,000rpm (50C) for 20 minutes. The supernatants and washes were combined, treated to 50% (NH4)2SO4 saturation, incubated for 24 hours at 5 C and centrifuged as before. The controls were also similarly treated with (NH4)2S04, etc. Each solution was dialysed against 1 x 41 phosphate pH 7.6 containing 0.01M cysteine and then phosphate alone. TABLE VI Purifi 0.1M Protein (Lowry) t Recovery cation DTT Dilution Initial Final (Protein) (TIC) Factor A + 2-fold 501.0 46.2 9 61 6.66 B + 4-fold 250.5 17.9 7 68 9.60 C + 6-fold 167.0 10.6 6.3 72 11.40 D - 2-fold 501.0 307.8 61.0 65 1.07 E - 4-fold 250.5 161.0 64.0 78 1.22 F - 6-fold 167 121.6 73.0 81 1.12 Conclusions The reduction-salting out scheme gives a greatly enhanced purification factor in plasma. Dilute plasma solutions give better results. Albumin is essentially completely precipitated by the reduction protocol as was shown by radial-immunodiffusion. Example 8 To illustrate separation of alpha-l-antitrypsin from the supernatant, Cohn IV-I was activated, reduced and salted out essentially as described in the previous examples. The solution (770ml) obtained contained -2.77mg/ml of protein, of which -50% was alpha-1-antitrypsin. A 20ml DEAEcellulose column was packed and equilibrated with 0.01M phosphate, pH 7.6. TIC was used to monitor the eluant fractions for antitrypsin activity. 664m1 of solution were loaded corresponding to a maximum column capacity of 1.84gm of total protein or 92mg of protein/ml of resin. The resin was then washed with starting buffer to remove unbound protein, and then eluted with 400ml gradiant consisting of 0.OlM phosphate, pH 7.6 + O.0lM phsophate + 0.07M NaCl, pH 6.0. After monitoring OD and TIC, active fractions (60-115) were pooled. Approximately 597mg (-32) of the protein did not bind to the resin. A summary of the results is included below. TABLE VII Protein alpha-1 alpha-l Purifi (Lowry) antitrypsin Specific antitrypsin cation mg corr.(TIC) Activity Yield % Factor Cohn IV-1 26,500 1,709 0.064 DTT+(NH4)2SO4 2,132 1,115 0.523 65 8.15 DEAE 551 516 0.936 32 14.6 Conclusions The product obtained was quite pure (Spec. Activity 0.94mg antitrypsin/mg protein. This example also illustrates that an overloaded column can be effectively utilized. Example 9 The activation, reduction and salting out of Cohn IV-I was performed as described in the previous examples. A 23ml column of DEAE-cellulose was equilibrated with 0.01M phosphate buffer, pH 7.6, and 430 ml of protein solution, corresponding to 25.7mg of protein/ml of resin was passed through. The unbound proteins were washed out with starting buffer and column eluted with 500ml gradient consisting of 0.01M phosphate, pH = 7.6 > 0.01M phosphate + 0.1M NaCl, pH = 6.0. After obtaining a protein elution pattern and checking proteins for activity, tubes 175-210 were pooled. A summary of the results is found in Table VIII. TABLE VIII Protein alpha-l alpha-l Purifi (Lowry) antitrypsin Specific antitrypsin cation mg mg Activity Yield % Factor Cohn IV-1 6507 421.5 0.07 DTT+(NH4)2SO4 591.2 254.3 0.43 60 6.15 DEAE 198.8 212.7 1.07 50.5 15.3 Conclusions The non-overloaded DEAE procedure gives an excellent product of high purity and with 84% recovery based on the amount of alpha-l-antitrypsin loaded on the column. It is evident that significant quantities of antichymotrypsin bind tightly to this column and can be separated if desired. Example 10 Activation, reduction and salting out of Cohn IV-I solution was performed as desbribed in previous examples. 365ml of DTT/(NH4)2S04 treated protein solution in 0.01M phosphate, 0.01M cysteine pH 7.6 containing 16.3mg of protein/ml and 5.9mg alpha-1-antitrypsin/ml was concentrated by ultra-filtration to -250ml. The solution was diafiltered against 1980ml of 0.05M NH4HCO3 using a 100,000 M.W. cutoff hollow fiber. Both the filtrate and the solution remaining within the chamber were examined for alpha-l-antitrypsin content and purity, and compared to alpha-1-antitrypsin obtained from DEAE-cellulose. TABLE IX alpha-l-anti trypsin Purifi Protein Recov- Specific cation mg mg (TIC) ery % TICmg/mg Factor DTT (NH4)2S 4 5,949 2,156 0.362 Amicon ultrafiltration (Filtrate) 2,831 1,881 87 0.66 1.8 (Retained Solution) 2,825 304 14 0.109 DEAE-cellulose 91 0.894 2.4 Using Amicon ultrafiltration at 100,000 M.W. cutoff 87% of alpha-l-antitrypsin passed through the membrane and a 1.8-fold purification factor was obtained. An SDS-polyacrylamide gel of purified protein showed one major impurity of higher M.W., probably alpha-l-antitrypsin aggregate. On the other hand the material purified by DEAEcellulose appeared homogenous. Purity of the product was also examined by immunoelectrophoresis using antibodies to different plasma proteins. Inhibitor purified by DEAEcellulose showed contamination with antithrombin III and alpha-l-lipoprotein; the Amicon purified alpha-l-antitrypsin in addition to these impurities also contains alpha-l-antichymotrypsin, alpha-l-acid glycoprotein, and C1 S inactivator. Conclusions The DEAE-cellulose purification step appears superior to the ultrafiltration preparation by purity (89% vs. 70-75%) and recovery (91 vs. 87%). On the other hand, ultrafiltration purification is extremely rapid, simple, inexpensive and can be scaled up easily. Example 11 In a publication by Laurell, et al, (Eur. J. Biochem., 57:107-113, 1975) the authors treat plasma with 30mM beta-mercaptoethanol to prepare alpha-1-antitrypsin for thiol-disulfide exchange. They follow this step with ammonium sulfate fractionation to partially purify the alpha-lantitrypsin prior to the thiol chromatography step. This Example compares the effectiveness of beta-mercaptoethanol versus DTT as reductant using the conditions described by Laurell, et al., and those used in this application. Laurell, et al., incubated with 30mM beta-metcaptoethanol followed by fractionation with 50% saturated (NH4)2S04 at 250C; the present method involves incubation with lOOmM DTT for 24 hours followed by 50% saturated (No4)2 504 at 40C. The following matrix experiment was conducted: 4.0ml of reductant in aqueous solution were added to 2. Oml aliguots of plasma to yield the final reductant concentrations (30 or 100mM). These treated plasma samples were incubated for one hour or 24 hours at 250C, and then 6.0ml of 100% saturated (NH4)2S04 solutions were added at 250C or 40C, respectively. After sixteen hours, the samples were centrifuged at 3,000 x g for twenty minutes, washed with 50% saturated (NH4)2504 and recentrifuged. Supernatants were dialyzed against lOmM sodium phosphate (pH 7.6) buffer containing lOmM cysteine followed by lOmM phosphate (pH 7.6) alone. Lowry and TIC assays were done on the dialyzed supernatants and on a plasma control. The results are presented in Table X. TABLE X Comparison of Beta-Mercaptoethanol (BME) and DTT as Reductant in the Purification of Alpha-l-Antitrypsin from Plasma Purifi mg Alpha-l- mg Specific cation Sample Antitrypsin Protein Activity Factor Plasma Control 2.5 131.2 0.019 1 One-Hour Reduction No Reductant 1.95 66.8 0.029 1.5 30mM BME 2.17 72.5 0.030 1.6 30mM DTT 1.96 18.0 0.109 5.7 100mM BME 1.86 71.1 0.026 1.4 100mM DTT * 1.76 8.1 0.217 11.4 24-Hour Reduction No Reductant 2.08 72.0 0.029 1.5 30mM BME 1.96 71.3 0.027 1.4 30mM DTT 0.98 4.55 0.215 11.3 100mM MBE 1.88 53.0 0.035 1.8 100mM DTT 1.07 5.28 0.203 10.7 Conclusions The results of Table X imply the following conclusions: 1. With a one-hour incubation with reductant and salting out at 250C: a. DTT plus (NH4)2SO4 greatly enhances the purification of alpha-1-antitrypsin from plasma over the purification yielded by 50% saturated (NH4)2SO4 alone. 100mM DTT is more effective than 30mM DTT during the short incubation period. b. Beta-mercaptoethanol in conjunction with 50% saturated (NH4)2S04 yields no improvement in purification of alpha-l-antitrypsin over (NH4)2SO4 alone. Neither 100mM beta-mercapto ethanol nor 30mM beta-mercaptoethanol is effective. c. The conditions of Laurell, et al., (30mM beta-mercaptoethanol, 1 hour incubation, 50% saturated (NH4)2S04, at room temperature [-220C]) yield no improvement over (NH4)2SO4 alone in the purification of alpha-l-anti trypsin. The use of beta-mercaptoethanol in their procedure is to reduce alpha-l-anti trypsin for subsequent thiol exchange chroma tography, not to enhance the purification of alpha-1-antitrypsin by destabilizing contami nant proteins. 2. With 24 hours of incubation with reductant and salting out at 40C: a. DTT plus 50% saturated (NH4)2S04 greatly enhances the purification of alpha-1-anti trypsin from plasma over the purification yielded by (NH4)2SO4 alone. 30mM DTT is as effective as lOOmM DTT at this incubation time. b. Beta-mercaptoethanol plus 50% saturated (NH4)2SO4, even at 1 hour of reduction, yields substantially no improvement in puri fication of alpha-l-antitrypsin over (NH4)2SO4 alone, with a small improvement apparently commencing at 24 hours and 100mM. c. The yield of alpha-l-antitrypsin in the DTT-treated samples of three-fold diluted plasma incubated with reductant for 24 hours is 40%, due to the formation of a firm clot. This effect of DTT on alpha-l-antitrypsin yield is not noted in samples incubated for one hour nor, as shown in previous work, is it noted in six-fold diluted plasma. Example 12 A second matrix experiment was conducted to determine whether DTT alone is sufficient to affect a purification of alpha-l-antitrypsin from plasma comparable to the purification acheived by the reductive-salting out scheme. Pierce and Eradio (J. Lab. Clin. Med. 94:826-831, 1979) used DTT to remove albumin from plasma samples prior to phenotyping alpha-l-antitrypsin by isoelectric focusing. They found that 30mM DTT for one hour at 370C precipitated albumin in a firm clot. This experiment shows that the coupling of DTT and (NH4)2SO4 exhibits a greater alpha-l-antitrypsin purification than DTT alone, using 30 and 100mM concentrations of reductant. 0.2ml of reductant in aqueous solution were added to 2.0ml aliquots of plasma to yield the DTT concentrations given above. The reductant-treated plasma samples were incubated from one hour at 370C and then either were centrifuged at 3000 X g or were fractionated with 50% saturated (NH4)2SO4 and then centrifuged. The supernatants were dialyzed versus lOmM sodium phosphate (pH 7.6) + lOmM cysteine buffer followed by lOmM phosphate (pH 7.6). The samples, plus a plasma control, were assayed by Lowry and TIC with the results compiled in Table XI. TABLE XI Comparison of DTT alone and DTT Plus 50% Saturated (NH4)2SO4 in the Purification of Alpha-l-Antitrypsin from Plasma Purifi mg Alpha-l- mg Specific cation Sample Antitrypsin Protein Activity Factor No (NH4)2S 4 no DTT 1.62 88.9 0.018 1.0 30mM DTT 0.60 13.2 0.045 2.5 100mM DTT 0.64 14.9 0.043 2.4 + (NH4)2SO4 No DTT 1.55 44.6 0.035 1.9 30mM DTT 0.61 3.26 0.188 10.4 100mM DTT 0.49 3.17 0.155 8.6 Conclusions 1. DTT alone yields a slight purification of alpha-l-antitrypsin from undiluted plasma. 2. DTT plus 50% saturated (NH4)2SO4 improves the purification of alpha-l-antitrypsin -four-fold over the purification shown by DTT alone. 3. The conditions of Pierce and Eradio (30mM DTT, one hour at 370C) do not demonstrate the dramatic enhancement of alpha-l-antitrypsin purification shown by the combination of DTT reduction plus fractionation by 50% saturated (NH4)2S04- 4. The low yields of alpha-l-antitrypsin (30-40%) from undiluted plasma incubated with DTT results from clot formation. This effect of DTT, as shown previously, is not seen in six-fold diluted plasma. Example 13 To test whether Aerosil, a fumed silica product, can improve the purification of alpha-l-antitrypsin in the reduction salting out method, and to determine whether the product retains activity against elastase (in addition to trypsin) the following experiment was performed. Activation of alpha-1-antitrypsin in Cohn IV-I was accomplished by dissolving 50gm of Cohn IV-I paste in 0.5 1 of 0.1M Tris-HCl pH 8.5) and allowing the solution to stir overnight at 250C. Dithiothreitol at a concentration of 25mM was added to activated Cohn IV-I in the presence of 2.5% Aerosil 380 (Degussa, Inc., Teterboro, N.J.) at 250C with stirring for 24 hours. Aerosil 380 is a fumed-silica material reported to be effective in removing alpha- and beta-lipoproteins and other beta-glob-ulins from aqueous solutions. The dithiothreitol treated solution was salted out in 50% saturated ammonium sulfate (40C) and, after equilibration overnight, was centrifuged at 3000 x g for one hour. The precipitate was washed with 50% saturated (NH4)2SO4 and recentrifuged. The combined supernatants were dialyzed against lOmM sodium phosphate (pH 7.6), containing lOmM cysteine, followed by dialysis against lOmM sodium phosphate (pH 7.6). TABLE XII Purifi Protein alpha-l alpha-l-anti- cation (Lowry) antitrypsin mg trypsin yield (%) Factor mg TIC EIC* TIC EIC TIC EIC Cohn IV-I 15,200 735 634 - - - DTT + 764 512 447 69.6 70.5 13.7 13.9 (NH4 )2SO4 + Aerosil *The elastase inhibitory capacity (EIC) was determined against porcine pancreatic elastase (Calbiochem-Behring) using p-nitrophenyl-n-tert-butyloxycarbonyl-l-alanine as substrate. Visser, L., and Blout, E.R. (1972) Biochim. Biophys. Acta, 268; 257-260. Conclusions 1. The Aerosil method does appear to offer advantages in removing contaminant proteins to give a higher purification factor (-13.7, 13.9 versus 8.15 in Table VII). The recovery of alpha-l-antitrypsin was as good as experiments performed in the absence of Aerosil. 2. The product had an elastase inhibitory capacity which paralleled the trypsin inhibitory capacity.

Claims: Claims 1. A method for isolating alpha-l-antitrypsin from a mixture of blood plasma proteins in solution comprising: (a) breaking sufficient disulfide bonds in said proteins to destablize them, (b) precipitating the destabilized proteins, (c) and recovering non-precipitated alpha-l-antitrypsin from said solution. 2. A method for isolating alpha-l-antitrypsin in accordance with claim 1 wherein said disulfide bonds are broken by treating the solution with an effective concentration of a reducing agent having a reducing strength sufficient to reduce disulfide bonds but insufficient to reduce other protein bonds or groups so as to fragment-the protein. 3. A method for isolating alpha-l-antitrypsin in accordance with claim 2 wherein said reducing agent is selected from monothiols and dithiols. 4. A method for isolating alpha-l-antitrypsin in accordance with claim 3 wherein said monothiol is present in a concentration of about Ql-1.5M and said dithiol is present in a concentration of about QOlA lM. 5. A method for isolating alpha-l-antitrypsin in accordance with claim 2 wherein said reducing agent is selected from dithiothreitol and dithioerythritol. 6. A method for isolating alpha-1-antitrypsin in accordance with claim 5 wherein said reducing agent is added to the solution in a concentration of about 0.03 - 0.10M. 7. A method for isolating alpha-l-antitrypsin in accordance with claim 6 wherein the reduction reaction is executed at about 25 - 370C for about 2 - 24 hours. 8. A method for isolating alpha-1-antitrypsin in accordance with anyone of claims 1 - 7 wherein the destabilized proteins are precipitated by salting them out. 9. A method for isolating alpha-l-antitrypsin in accordance with anyone of claims 1 - 8 wherein said mixture of blood plasma proteins is a human plasma Cohn fraction IV-I. 10. The product obtained from the method of anyone of claims 1 to 9.

Inventors: GLASER, CHARLES BARRY
Applicants: MED RES INST SAN FRANCISCO
Application year: 1982
Main classification: A61K37
IPC codes: C07K14