CA1061251A - Method of removing hepatitis-associated antigen from protein fraction - Google Patents

Method of removing hepatitis-associated antigen from protein fraction

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CA1061251A
CA1061251A CA166,295A CA166295A CA1061251A CA 1061251 A CA1061251 A CA 1061251A CA 166295 A CA166295 A CA 166295A CA 1061251 A CA1061251 A CA 1061251A
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antigen
protein
precipitate
solution
haa
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Alan J. Johnson
Jack Newman
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    • C07ORGANIC CHEMISTRY
    • C07KPEPTIDES
    • C07K14/00Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof
    • C07K14/005Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof from viruses
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    • C12N2730/00Reverse transcribing DNA viruses
    • C12N2730/00011Details
    • C12N2730/10011Hepadnaviridae
    • C12N2730/10111Orthohepadnavirus, e.g. hepatitis B virus
    • C12N2730/10122New viral proteins or individual genes, new structural or functional aspects of known viral proteins or genes
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S530/00Chemistry: natural resins or derivatives; peptides or proteins; lignins or reaction products thereof
    • Y10S530/806Antigenic peptides or proteins
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S530/00Chemistry: natural resins or derivatives; peptides or proteins; lignins or reaction products thereof
    • Y10S530/827Proteins from mammals or birds
    • Y10S530/829Blood
    • Y10S530/83Plasma; serum
    • Y10S530/831Cohn fractions

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Abstract

ABSTRACT OF THE DISCLOSURE
Hepatitis-associated antigen is removed from a protein fraction containing same by solubilizing the protein in a sol-vent physiologically tolerable on injection, e.g., glycine-citrate-saline buffer; adding polyethylene glycol having a molecular weight of from about 200 to about 6,000 to a concen-tration of from about 12 to about 30 grams per 100 ml of solution to yield a precipitate and separating the precipitate. The protein fraction may be, for example, albumin, gamma globulin, coagulation factors II, V, VII, IX, X, XI and XIII, fibrinogen or plasminogen.

Description

BACKGROUND OF THE INVENT:I: ON
This invention relates to the separation of blood pro-teins, and more particularly this invention relates to the removal of hepatitis-associated antigen from other protein fractions.
Hepatitis is a relatively common disease, but the disease is sometimes difficult to diagnose and there is, as yet, no specific treatment. Even though as many as five percent of the reported cases become chronically ill and another two percent become cirrhotic, it has been estimated that three out of every thousand persons who be-come infected with the serum hepatitis virus do not become ill, but nevertheless carry the disease. For this reason hepatitis poses a serious problem in detecting blood donors who may transmit the disease.
The known methods for detecting serum hepatitis rely on detection of virus products in the body fluids but are time-consuming and burdensome as well as being relatively insensitive. In fact, it has been estimated that most of the prior art tests can detect only twenty to thirty percent of the carriers of the disease.
Moreover, prior tests have not been sensitive enough to detect anti-bodies that develop after a single exposure to hepatitis virus or primary hepatit~is infection.
A specific antigenr popularly known as Australia antigen has been found in the serum of many patients with serum hepatitis.
The exact pathogenic role of the Australia antigen is a current problem of great academic interest as well as urgency in view of the importance of recognizing the source and/or cause of hepatitis.
The Australia antigen is also known as hepatitis-associated antigen (HAA), which terminology will be used herein. Most of the common methods used for the detection of hepatitis rely on the presence of the HAA, or the antibody thereto, for their specificity.
At present, the neutralizing effect of immune serum/ that is, the serum of an individual who has recovered from hepatitis and ' .

c~ntains antibodies speciic against the disease, is used to diagnose hepatitis by various tests. In these tests HAA antibody is added to the sample, forming a precipitate or complex with the antigen present in the sample.
Existing techniques for detecting and diagnosing hepatitis - include: immunodiffusion, complement fixation, electrophoretlc modifications of precipitin techn:iques, radioimmunoassays, and hemagglutination procedures. Diffusion methods are the simplest but ; the least sensitive and slowest. The electrophoretic modifications a of precipitin techniques are rapid, as rapid as complement fixation,but not quite as sensitive. Of the available techniques, complement - fixation and hemagglutination procedures appear to be the most rapid and are also moderately sensitive. The complement fixation technique involves adding a biologic material such as blood or plasma to the 1 appropriate antibody for HAA. The reaction mixture is incubated with a predetermined amount of complement to fix the latter. The amount of HAA or antibody in the fluid can be determined through titrating the amount of remaining non-fixed complement by incubation with a standard cell solution. The complement fixation technique is only ¦ 2~ moderately sensitive for detecting antigen and antibody gives anti-complementary reactions with plasma fractions, and is not routinely available in many hospitals and blood banks. The various radio-immunoassays used are the most sensitive tests available at present but usually require at least one day to run, and the reproducibility is only fair. The hemagglutination test with antibody-coated red cells appears to combine both sensitivity and rapidity.
Bpidemiological surveys following transfusion therapy reveal a very high incidence of hepatitis, on the order of 0.12-12 percent with pooled plasma or whole blood. The incidence of hepatitis with fibrinogen transfusion has been variously estimated at nine percent to more than thirty-six percent, whereas one investigator believed the incidence was thirty-five times as high as with trans-fusion of blood or plasma fractions. The fibrinogen is con~idered to be contaminated because it is isolated from very large plasma pools (5000 or more units, some of which contain HAA) but probably contains only about one percent of the hepatitis-associated antigen present in the original plasma. The tendency to transmit hepatitis has severely limited the usefulness of fibrinogen or fibrinogen-containing fractions, e.g., when Fraction 1-0 containing sixty to eighty percent fibrinogen was used as a source of AHF in this country, it caused hepatitis in seventy-five percent of hemophiliacs not previo~sly given massive transfusions of fresh-frozen plasma and in fifty percent of those who were previously transfused. It is estimated that more than ten percent of patients who develop hepatitis die from its effects.
Prior screening of all blood donors by present assays will probably reduce the incidence by only twenty to thirty percent since the available assays for the antigen associated with serum hepatitis (HAA) are relatively insensitive and plasma with barely detectable HAA content by ln vitro assay usually produces overt disease. Furthermore, injection of a 1:1,000,000 dilution of such plasma may cause demonstrable viremia without icterus. Since pro~
fessional blood donors, who have a ten times higher incidence of he-patitis than volunteer blood donors, furnish almost half the country's blood supply, it would be very difficult to exclude them as donors and indeed would be unnecessary if the HAA could be re-moved during blood collection. Patients recaiving transfusions could be given ordinary gamma globulin but it has proved to be helpful only against infectious hepatitis; or they could be given high-titer immune gamma globulin from recovered hepatitis patients, but the supply is exceedingly limited and its usefulness in preventing clinical disease in pat ents infused with large amounts of HAA con-taminated plasma fractions has not yet been proved conclusively.
The HAA or serum hepatitis lSH) antigen probably partici-pates in the pathogenesis of serum hepatitis, and is viewed primarily as a marker in plasma for the disease. The HAA particles `~ ' ' ~ '' ' found in infected blood are predominantly of two morphologic types:
those about 22 m~ in diameter which seem to represent incomplete virions (empty capsids), and particles about 42 m~ in diameter which may represent the entire virus.
For many years the risk of hepatitis has prevented the widespread use of fractions such as fibrinogen and slowed the commercial production of a concentrate of Factors II, VII, IX and X
as well as Factor VIII (antihemophilic factor -~ AHF), from large pools of human blood. Because the Cohn procedure has been widely - 10 used for many years and little or no serum hepatitis develops after treatment with Cohn Fraction II and albumin, the method has been considered more or less "sacred" or "definitive".
These considerations have mitigated against the commercial use of new fractionation methods such as the zinc method XIII and DEAE adsorption in the purification of gamma globulin, and poly-- ethylene glycol (PEG) in the purification of serum albumin although these methods would undoubtedly result in products of higher purity and yield, lower aggregation potential and greater stability. Even new anticoagulants such as citrate-phosphate-dextrose (CPD) cannot be used without prior extensive clinical trials of each plasma fraction derived from blood collected with CPD and fractionated by the Cohn procedure, to ascertain its potential for transmitting hepatitis --a long, tedious, expensive and time-consuming process. Thus, in addition to demonstrating that new fractionation techni~ues or use of CPD blood r~sult in plasma fractions of higher purity and yield than the Cohn fractions, it is necessary to show that they are no more likely to cause hepatitis.
Some therapeutically valuable plasma fractions are often contaminated with HAA. In the hands of most investigators, commercially prepared concentrates of Factors II, VII, IX and X have been associated with a high incidence of hepatitis, at least seventeen percent, while one study reports forty to seventy percent.
This material is therefore reserved primarily for the treatment of a small group of bleeding patients with Factor IX deficiency and a history of multiple transfusions. Many other bleeding patients ` deficient in one or more of the four factors but with no history of transfusions would probably benefit greatly from therapy with plasma, plasma fractions, and whole blood free of HAA. This group includes patients with hepatitis, cirrhosis, liver poisoning or other parenchymal liver damage, or with dicumarol overdosage or biliary obstruction.
Possible H~A contamination of AHF concentrates and fibrinogen also seems to be a pressing problem. Recent emphasis on HAA by the Division of Biologics Standards (DBS) has pointed up the need for screening donors before the plas~a is fractionated as well as three months after blood collection to make sure that they are still free of the antigen. It is very difficult, however, to predict whether donors will develop HAA-positive blood six weeks to three months after giving blood. According to recent estimates, a fairly high percentage do so. It is also difficult to rule out circulating antigen-antibody complexes that give negative results with present HAA assays and may subsequently prove to be infective.
The high morbidity and mortality attending post-transfusion hepatitis can probably be reduced to some extent by modi-fying present plasma fractionation methods. About 50,000 units of unselected plasma were fractionated from 1966 to l9B9 to produce American National Red Cross (ANRC) intermediate-purity AHF which was used with other materials to treat 153 episodes in 96 patients with hemophilia A or von Willebrand's disease. Although some of them received very laxge amounts, only two developed hepatitis and they had also received large amounts of other ~actor VIII concentrates and plasma. Similarly, about 50,000 units of unselected plasma were processèd for the ANRC high-purity AHF which was used with other Factor VIII preparations to treat 92 episodes in 57 patients. One of these developed hepatitis and he, too, had received large amounts of other AHF-containing materials. Since other patients given intermediate or high-purity AHF from the same lots did not de-velop the disease, the level of any contaminating HAA present in the preparations seems to have been very low indeed.
In order to prevent transmission of hepatitis by blood donors, most transfusion centers are setting up one of the new assay methods for detecting HAA in the dono~'s blood. If it is found, the HAA-positive plasma is usually sterilized and discarded.
As mentioned above, these methods will detect the HAA in only 20 to 30 percent of the contaminated plasma units.

Polyethylene glycol in the_fractionatlon and concentration of proteins and viruses. Albertson used polyethylene glycol (PEG) to fractionate and concentrate cells, viruses, microsomes, proteins, nucleic acids, and antigen-antibody complexes in two-phase systems with dextrans or ammonium sulfate and water. This synthetic, non-reactive po~ymer has also been used as a vehicle for intramuscular and intravenous administration of various hormones. Polson et al.
fractionated albumin, gamma globulin and fibrinogen with PEG of 6000 molecular weight, and a procedure for the preparation of high-purity AHF with PEG of 4,000 and 6,000 m.w. is described and claimed by Johnson et al. in U.S. Patent No. 3,652,530. In general, PEG's mode of action is believed to be based on removal of water from the hydrophilic region of proteins; as a result, their hydrophobic bonds presumably interact causing aggregation and a decrease in solubility.

Extensive acute and chronic toxicity studies at the Mellon Institute from 1947 to 1970, principally with PEG-4000, further attested the nontoxic nature of the polymer. In animals, intra-venous doses as high as 16 Gm./kg. were given to four species without evidence of toxicity. In 52 hemophiliacs and von Willeb~and patients~

high-purity AHF precipitated with PEG was administered during 92 treatment episodes with no toxic effects~ PEG is rapidly excreted by the kidneys, with a glomerular clearance rate virtually the same ~ 3l~

as that of inulin and creatinine.
PE& has also been used by virologists to concentrate and purify a number of plant viruses, bacteriophages, and some animal organisms:
(a) Hebert precipitated partially purified soil-borne wheat mosaic virus (WMVJ from a growth medium with three percent PEG 6000 and centrifugation for ten minutes at 10,000 rpm. In other s~udies, he precipitated rod-shaped WMV particle~ in 0.1 M phosphate bu~fer at pH 7.5 with two percent PEG. Tobacco mosaic virus (TMV) was also precipitated from extracted, infected tobacco leaves by four percent PEG in 0.1 M NaCl and by two percent PEG in 0.3 M NaCl.
In contrast, eight percent PEG was required to precipitate two plant viruses with spherical particles: tobacco ringspot virus (precipitated by treating the juice with PEG in 0.3 M NaCl) and the bean pod mottled virus (precipitated in 0.2 M NaCl~.
(b) When purifying African horse-sickness virus for electronmicroscopy~, Polson and Deeks precipitated the virus from emulsified mouse brain tissue using three to four percent PEG-6~00 and 0.066 M phosphate buffer at pH 7Ø

(c) Leberman described precipitation of four highly purified viruses from solutions: turnip crinkle virus (TCV), turnip yellow mosaic :v~irus (TYMV), a nitrous acid mutant of tobacco mosaic virus (TMV), and bacteriophage T-4 with PEG-6000 at varying pH and NaCl concentrations. Similar studies were later carried out with only partially purified virus solutions. Precipitation with PEG
required a higher NaCl concentration as the pH was raised.

(d) In earlier studies, viruses with a nucleic acid core and a pxotein coat were precipitated with PE~. However, McSharry and Benziner applied the method to a virus with a lipoprotein coat:

vesicular stomatitis virus. The virus was effectively precipitated with a six to eight percent concentration of PEG-6000 and 0.5 M NaC1;
~hese researchers concluded that PEG precipitation concentrates and purifies representatives of all major vixus classes except the ,.

pox-virus and herpes~irus groups (not yet tested) without loss of infectivity.
(e) In experiments by Yamomoto et al., seven bacterio-phages were readily concentrated from crude lysates of infected bacteria by two to ten percent PEG-6000 and 0.5 M NaCl. The efficacy of the method was relatively unaffected by changes in pH
and ionic strength. They also showed that the asymmetric particles of T~ and bacteriophage fd were especially susceptible to PEG
and could easily be purified from the more symmetric phage particles at low PEG concentrations. In addition, they found that a relatively constant percentage of phage was precipitated by a fixed concentra-tion of PEG over a phage concentration range of nearly 10 8 and concluded that the exact mechanism of precipitation is unknown but a phase partition rather than a normal precipitation reaction seems to be involved (f) Juckes precipitated proteins with PEG-6000 in an effort to determine the mechanism(s) involved. He vari~d the pH, ionic strength, protein concentration, and temperature, and concluded that each variable had an effect on precipitability of tha proteins studied: carboxyhemoglobin, ovalbumin and bovine ser~um albumin, as well as bromegrass mosaic virus. He concluded that precipitability was related primarily to the molecular weight of the protein and the pH, as measured by differences in the Stokes radius of the proteins, but could not relate the other effects to changes in the Stokes xadius. These principles did not obtain when viruses and other pro-teins in low concentration and a low ionic strength were precipitated.
(g) Pert reported that antibody-antigen reactions can be enhanced with protein-precipitating agents such as PEG. In one phase of these experiments, he added eight percent PEG to eliminate fibri-nogen, alpha macroglobulin, cryoglobulins and some other large-molecular-weight proteins, then used twelve percent PEG to pre-cipitate and concentrate most of the HAA together with many oth~r moderate-sized proteins such as gamma globulin, alpha 1 and alpha 2 -globulins, beta globulins, and their associated lipoproteins.
SUMMARY OF` THE INVENTION
Since the hepatitis-associated antigen (H~A) has been associated with, and may be involved in the pathogenesis of, serum hepatitis, absence of the antigen has been interpreted as indicating relative freedom from the infectious agent causing serum hepatitis.
The primary object, therefore, is to provide a method to eliminate the antigen from protein fractions including most of the commercially useful plasma fractions -- albumin, gamma globulins, coagulation Factors II, V, VII, IX, X, XI, XII a~d XIII, fibrinogen, antihemo-philic factor (Factor VIII), plasminogen, ceruloplasmin, transferring, thyroxin-binding proteins, antithrombin III, ~ 1 anti~rypsin, Q~ 2 macroglobulin, Ci inactivator, inter-~trypsin inhibitor, as well as sewage -- by fractionation with polyethylene glycol (PEG).
It is another primary object of the pxesent invention to provide a method for removing the contaminating HAA from plasma fractions that have been partially purified.
It is stili another object of the present invention to provide a superior fractionation method using an agent which does not denature or combine with plasma proteins, but selectively con-centrates the HAA from albumin, gamma globulin, and fibrinogen, as well as concentrates of AHF and Factors II, VII, IX, and XO
Variations of thas method are used to remove the antigen from albumin, gamma globulin, fibrinogen, a concentrate of Factors II, VII, and IX, and a concentrate of Factor~ II, IX and X -- all prepared for therapeutic purposes.
In accordance with the foregoing objects, a method is provided which comprises the essential steps of: (1) maintaining the solubility of the HAA-containing protein fraction at a pH away from its isoelectric point, (2) adding polyethylene glycol with a molecular wei~ht ranging from about 200 to 6000 to a concentration of from about 12 to about 30 percent to thereby precipitate the HAA, and (3) separating the HAA from the protein.

The major factors that are varied to remove the HAA from the various fractions are the final PEG concentration of the mixture, the pH, the ionic strength, and the protein concentration.
The PEG concentration is varied from about 12-30 Gm./lO0 ml. of solution, depending on the molecular weight of the polymer. The pH
is adjusted so that it is removed as far as possible from the iso-electric point of the fraction remaining in solution, but without denaturing the protein and still within the precipitability range for the HAA. The pH is generally separated by l.0 or 2.0 pH units from the isoelectric point, which is well known from most of the protein fractia~s and in any event can be easily determined by one of - ordinary skill in the art, using known methods. As examples, the isoelectric point of fibrinogen is about 5.5, of gamma globulin from 6.5 to 7.5, nominally 7.2, of albumin about 4.9, of Factor IX about 4.3, and Factor II about 4.7.
The solutions are made with any suitable buffer or the like, provided that the small amounts which may be carried along in the fractionation procedure are physiologically tolerable on I.V. or I.P. injection. Typical suitable materials for these~solutions are a slycine-citrate buffer~ a phosphate buffer, a saline solution, a tris-citrate buffer with or without other additives such as urea, alone or in various combinations. The ionic strength may vary from 0.20 to 0.001.
After the HAA is precipitated, it is removed from the supernatant by any suitable procedure such as centrifugation or filtration or both. The filter should have pores of less than ~.6 m~, preferably between about 0.45 and 0.2 m~. Suitable filters are commer-cially supplied by Millipore or Cox.
TemperatUre is not a factor in the method of the present invention, although for practical purposes it may be conveniently practiced at room temperature or from about 15 to about 25C. At lower temperatures, lower concentrations of PEG are used.
While the method o the present invention is preferably .

. ' , ~. ' ~ ' . . ' ~ractised by selectively precipitating the HAA to remove it from a : solution of the same with another protein fraction, it should be understood that all the proteins could be precipitated by PEG and the fraction to be separated from the HAA then solubilized with a suitable buffer at the proper pH.
The foregoing objects of the present invention and other objects will in part be obvious and in part be pointed out as the : description of the invention proceeds.
DESCRIPTION OF THE PREFERRED EMBODIMENT

Concentration of HAA from fractions for assay. One milli-.
liter of serum or partially purified HAA (isolated and washed by centrifugation) with an HAA concentration barely detectable by counter-immunoelectrophoretic assay, was dilited up to 10,000 times with fibrinogen, albumin, or gamma globulin, prepared by Cohn methods 6, and 9, or purified concentrates of Factors II, VII, IX and ~ or Factor VIII. The added EL~A was precipitated from the plasma fraction by PEG, reconstituted to its original volume in buffer and assayed (Table l). Since only a minute amount of precipitate was obtained, it was collected by batch centrifugation at moderate speed -- about 10,000 relative centrifugal force (RCF)* or continuous flow (Sharples) at 13,000 RCF. In most cases, 0.3 mp - 0.2 mlu filters (Millipore or Cox) offer a useful back-up measure to remove any residual aggre-gated HAA.

~RCF = _4 (3-14162_ r ~ gravity wherein r ~ radius (in feet) of the rotor and n = revolutions per second = r60 ~// , .~. , ; :
. . ., ~ , ,.

q~

RECOVERY OF UNDETECTABLE* AMOUNTS OF HAA FROM ALBUMIN BY
PRECIPITATION AND CONCENTRATION WITH POLYETHYLENE GLYCOL (PEG~

.
PEG FRACTION PERCENT HAA RECOVERED

SUPERNATANT

~, (Containing Albumin) 0%
!

PRECIPITATE 100%

*One ml. of partially purified HAA, positive on counter-:
immuno-electrophoresis at a dilution of 1:35, proved negative by HAA assay when diluted with 2000 ml. of five percent human serum albumin.

lla . ~

:
~j Removal of HAA from fractions by PEG precipitation. In - . .
other experiments, H~A-rich serum or a serum fraction (complement-; fixation titer over 1000) or partially purified HAA (isolated and . washed by ultra-centrifugation) was mixed with a partially purified concentrate of Factors, II, VII, IX and X prepared by DEAE adsorp-tion of plasma and subsequent elu-tion, or with AHF prepared ~y cryoethanol precipitation, or with fibrinogen, albumin or gamma globulin prepared by Cohn methods 6 and 9. The added HAA was pre-cipitated from the plasma fraction by PEG, and the desired fraction 10 itself was then precipitated and concentrated by PEG. The yield of the plasma fraction was 90-100 percent for all except fibrinogen and AHF (Tables 2-4).

u Concentration of HAA from a Plasma_Fraction Containin~_Prothrombin .
Complex tFactors II, VII, IX and X~ and Preparation of the Fraction Free of Hepatitis-Assoclated Antigen (~AA) for Clinical Use The starting material commonly used for this procedure may be partially purified prothrombin complex obtained by DEAE-(trc~dcn~a r ) Sephadex or DEAE column chromatography or from calcium phosphate adsorption and elution methods. The ionic strength for an optimal yield of these fractions ranges from 0.15 to 0.001, and the protein concentration ranges from 3 to 27 mg./ml. at about neutral pH, with water and a suitable buffer, e.g., sodium citrate~sodium chloride.
The temperature of this solution is maintained at 15-25C. Poly-ethylene glycol (PEG), molecular weight 200-6000, is added to a final concentration of 12-30 grams per 100 ml. The exact percentage is - . . ~ ~ . , ~.0 f:ilZ5~L
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increased for PEG of low molecular weight and decreased for the high molecular weight material. After sufficient mixing to dissolve the PEG and precipitate the HAA, usually 30 minutes, the solution is centrifuged at room temperature for at least 10 minutes at a relative centrifugal force (RCF) of approximately 10,000, and the supernatant is separated cleanly from the precipitate by decantation or vacuum aspiration and reserved.
The HAA precipitate is reconstituted with three volumes of buffer or saline solution, and the walls of the centrifuge bottle are washed, bringing the total volume to about 10 percent of the starting material, or to a volume which readily permits transfer of the re-constituted precipitate from the large centrifuge tube to a small one.
The HAA is then reprecipitated from the buffer or saline solution with 12-30 percent PEG 200-6000 and centrifuged. Since the pre-cipitate contains the HAA, special care must be taken in this separation and in disposition of the precipitate after it has been reconsti~uted in 0.2-1.0 ml. of water or saline solution and assayed.
This optional procedure of redissolving and reprecipitating the H~A
provides a purified, concentrated HAA for assay.
If the II, VII, IX and X concentrate is for laboratory or clinical use, the reservad supernatant containing it is adjusted to a pH of about 5.2 and the PEG concentration is raised, according to the molecular weight of the PEG used, e.g., 30 grams per 100 ml. with PEG-4000. After sufficient mixing to dissolve the PEG and preci-pitate the concentrate, usually 30 minutes, the solution is sentri-fuged at about 10,000 RCF for 10 minutes at room temperature. The precipitate is collected, washed with 30 percent ethanol at -5C. in buffer or in water and dissolved at neutral pH in a suitable buffer, e.g., sodium citrate-sodium chloride. Alternatively, Soulier's method of precipitation and concentration with ethanol may be used instead of PEG in the second precipitation step, but the yield is moderately decreased with this procedure.

`~
X~PLE 2 Concentration of HAA from Gamma Globulin, and/or Preparation of . . _ .
Gamma Globulin Free of Hepatitis-Associated Antigen (HAA) for . . . _ .
Clinical Use The starting material for this procedure can be ~raction II+III (from Cohn Method VI), Fractions II-3, II-1,2 and II (from Method IX) or fractions obtained from similar or derivative techniques. The protein in these fractions is diluted in a suitable buffer, eOg., glycine-sodium citrate-sodium chloride at about neutral pH to a concentration of 12-22 mg./ml. The temperature is maintained at 15-25OC. The solution is adjusted to pH 3.0-3.7 by slowly adding acid, e.g., acetic, hydrochloric or citric acid, with mixing. Poly-ethylene glycol (PEG) , 200-6000 molecular weight, is added to a final concentration of 12-30 grams per 190 ml. of solution. The exact percentage is increased for PEG of low molecular weight and decreased for material of high molecular weight. After the PEG has been dissolved by mixing and the HAA has been precipitated, which usually requires 30 minutes, the solution is centrifuged at room temperature for at least 10 minutes at a relative centrifugal force of about 10,000, and the supernatant is separated cleanly from the HAA precipitate by decantation or vacuum aspiration and reserved.
The precipitate is reconstituted with three volumes of buffer or saline solution, and the walls of the centrifuge bottle are washed, bringing the total volume to about 10 percent of the starting material, or to a volume which readily permits transfer of the reconstituted precipitate from the large centrifuge tube to a small one. The HAA is then reprecipitated from the buffer or saline solution with 12-30 percent PEG 200-6000 and centrifuged. Since the precipitate contains the HAA, special care must be taken with this separation and with disposal of the precipitate after it has been reconstituted in 0.2 1.0 ml. water, saline, or buffer, and assayed.
This optional procedure of redissolving and reprecipitating the HAA
provides a purified, concentrated HAA for assay.

.
~ -- - . : . : ~ , 3~

If the gamma globulin recovered is for laboratory or clinical use, the reserved supernatant containing it is adjusted to about pH 7.0 by slowly adding a base, e.g., sodium hydroxide, with mixing. The precipitate is collected, washed with 20-40 percent ethanol at -5 to -10C in buffer or in water and then dissolved in buffer, usually a glycine-sodium citrate-saline buffer at pH 7Ø As an alternative, this procedure can be introduced into Method 6 after ~upernatant I has been collected and just before the precipitation of Fraction II-III, or introduced into Method 9 after collection of Supernatant III.

Concentration of HAA from Albumin and/or Preparation of Albumin .
F_ of Hepatitis-Associated Antigen tHA:A) for Clinical Use The starting material for this procedure can be Cohn supernatant V or Fraction V precipitate (from Method 6), or fractions obtained from derivative techniques or other methods. The protein in these fractions is diluted in a solven~, e.g., 0.9 percent sodium chloride, to a final concentration up to 50-60 mg./ml.
and adjusted to about pH 7.0 by slowly adding acid or base, e.g., hy-drochloric, citric or acetic acid, or sodium hydroxide. The tempera~
ture of this solution is maintained at 15-25C. Polyethylene glycol (PEG), molecular weight 200-6000, is added to a final concentration of 12-30 grams per 100 ml. The exact percentage is increased for the low-molecular-weight material. ~fter sufficient mixing to dissolve the PEG and precipitate the HAA,usually 30 minutes, the solution is centrifuged at room temperature for at least 10 minutes at a relative centrifugal force of about 10,000, and the supernatant is separated clear1~ from the HAA precipitate by decantation or vacuum aspiration and reserved.
The precipitate is reconstituted with three volumes of buffer or saline solution, and thé walls of the centrifuge bottle are washed, bringing the total volume to about 10 percent of the starting material, or to a volume which readily permits transfer lof the reconstituted precipitate from the large centrifuge tube to a small one. The HAA is then reprecipitated from the buffer or saline solution with 12-30 percent PEG 20t)-6000 and centrifuged. Since the precipitate contains the HAA, special care must be taken in this se-paration and in disposal of the precipitate after it has been recon-stituted in 0.2-l.0 ml. of water or saline solution and assayed.
This optional procedure of redissolving and reprecipitating the HAA
provides a purified, concentrated HAA for assay.
If the albumin is for laboratory or clinical use, the pH
of the reserved supernatant containing it is adjust~d to approximately 4.8 by slowly adding an acid, e.g., acetic, hydrochloric or citric acid. The precipitate is collected, washed with 40 percent ethanol in water or 0.9 percent saline at -5C, and a suitable solvent is added, e.g., water or 0.9 percent sodium chloride. As an alterna-tive, the Fraction V precipitate can be further fractionated by Method 6 and the resulting albumin can then be processed as described abo~e.

Concentration of HAA for Assay from Fibrinogen or AHF Concentrates _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ : n _ _ _ _ and/or Preparation of Fibrino n or AHF Concentrates-Free of _ _ _ ge ___ _ Hepatitis-Associated Antigen (HAA~ for Clinical U~e ... _ . . . .. . _ Freshly prepared, fresh frozen or lyophilized fibrinogen or AHF concentrate prepared for clinical use -- reconstituted in sterile water or a suitable buffer -- is diluted to a protein con-centration of 2-12 mg./ml. with physiologic saline solution, 0.02 M
tris-0.02 M citrate buffer, or other buffer. Urea is added to a final concentration of 2.0-5.0 M. The procedure may be carried out at a high pH or at a low pH.
High pH Method. The pH of the solution is adjusted to 9.8-10.5 with any suitable base. After the diluted fibrinogen or AHE
has been mixed for 30 minutes at pH 9.8-10.5 at room temperature, PEG
200-6000 molecular weight is added to a final concentration of 12-30 grams/ml. and mixing is continued for 30-120 minutes at room . - . :

temperature to dissolve the PEG and precipitate the HAA. The pH
must be adjusted at this stage to prevent any precipitation of the fibrinogen or AHP, or to dissolve any that has already precipitated.
Such precipitation may occur at pEI 10.0 or lower, but rarely above pH 10.3.
Low pH Method. The pH of the solution i~ adjusted to 3.0-.
4.5 with any suitable acid. After the diluted fibrinogen or AHF has been mixed for 30 minutes at a room temperature, PEG 200-6000 mole-cular weight is added to a final concentration of 12-30 grams/ml. and mixing is continued for 30-120 minutes at room temperature. The pH
must be adjusted at this stage to prevent any precipitation of the fibrinogen or AHF, or to dissolve any that has already precipitated.
Such precipitation may occur at a pH of 4.0 or more, but rarely below 4.2.
With either the high or low pH method, the mixture is then centrifuged for at least 10 minutes at about 10,000 RCF at 20C to bring down the HAA, and the supernatant is aspirated carefully to avoid disturbing any minute quantities of precipitate that may be visible at the hottom of the centrifuge cup or tube and reserved.
The precipitate is reconstituted with three volumes of buffer or saline solution, and the walls of the centrifuge bottle are washed, bringing the total volume to about 10 percent of the starting material, or to a volume which readily permits transfer of the re-constituted precipitate from the large centrifuge tube to a small one. The HAA is then reprecipitated from the buffer or saline solu-tion with 12-30 percent PFG 200-6000, and centrifuged at pH 9.8-10.5 for the high pH method and pH 3.0-4.5 for the low pH method, as descxibed above. The final precipitate is dissolved in 0.2-1.0 ml. of saline, water or tris-citrate or other buf~er for optimal concentra-tion and then assayed. This optimal procedure of redissolving and reprecipitating the HAA provides a purified, concentrated HAA for assay.
The fibrinogen or AHF in the aspirated reserved super~atant may be precipitated by adding sufficient NaOH or HCl to bring the pH to 6Ø The precipitate is collected, washed with 10 percent ethanol in water at -2C and a suitable solvent is added, e.g., 0.02 M tris citrate plus 0.1 M NaCl.

Concentration of HAA from a Plasma Fraction Containing Prothrombin Complex (Factors II, VII, IX and X) and Preparation-of the Fraction , Free of ~Iepatitis-Associated Antigen (HAA) for Clinical Use Partially purified prothrombin complex (500 mg.), ob-tained by DEAE column chromatography, was dissolved in 0.03 M
glycine - 0.0005 M sodium citrate - 0.01 percent sodium chloride buffer, pH 7.0, and diluted with additional buffer to an ionic strength of 0.003 and a protein concentration of 5.0 mg./ml. The temperature of this solution was maintained at 25C~ Polyethylene glycol (PEG) molecular weight 4000 was added to a final concentra-tion of 20 grams per 100 ml. After 30 minutes of mixing to dis-solve the PEG and precipitate the HAA, the solution was centrifuged at room temperature for at least 10 minutes at a relative centrifugal force of approximately 10,000, and the supernatant was separated cleanly from the HAA precipitate by vacuum aspiration and reserved.

The precipitate from Example 5 was reconstituted with three (10 ml.) volumes of saline, and the walls of the centrifuge bottle were washed with an additional 5 ml., bringing the total volume to 35 ml. -- all of which was pooled in a small test tube.
The HAA was then reprecipitated from the saline at pH 7.0 with 20 percent PEG-4000 and centrifuged. Since the precipitate contains the HAA, special care must be taken in this separation and in dis- -position of the precipitate after it has been reconstitu~ed in 0.2-1.0 ml. normal saline and assayed.

The reserved supernatant from Example 5 containing Factors II, VII~ IX and X was adjusted to a pH of 5.2 by adding 1 N

- ~ ~

A~P 3`.
; hydrochloric acid, and the PEG concentration was raised to 30 grams per 100 ml. with PEG-4000. After 30 minutes of mixing to dissolve the PEG and precipitate the HAA, t:he solution was centrifuged at a RCF of 10,000 for at least 10 minutes at room temperature. The pre-cipitate was collected, washed with 30 percent ethanol at -5 C in buffer (pH 5.2) and dissolved in 20 ml. of 0.3 M glycine - 0.005 M
sodium citrate - 0.1 percent sodium chloride buffer, at pH 7Ø

; Concentration of HAA from Gamma Globulin and/or Preparation of Gamma 10 Globulin Free of Hepatitis-Associated Antigen (HAA) for Clinical Use Fraction II-3 (500 ml.) from Cohn Method 9, containing 166 mg. protein/ml., was diluted in 0.3 M glycine - 0;.005 M sodium citrate - 0.1 percent sodium chloride buffer at pH 7.0 to a protein concentration of 22 mg./ml. The temperature was maintained at 25C.
15 The solution was adjusted to pH 3.5 by slowly adding l~,N hydrochloric , acid, with mixing. Polyethylene glycol (PEG), 4000 molecular weight, was added to a final concentration of 20 grams per 100 ml. of solution. After 30 minutes of mixing to dissolve the PEG and pre-` cipitate the HAA, the solution was centrifuged at room temperature ; 20 for at least 10 minutes at a relative centrifugal force of 10,000, and the supernatant was separated cleanly from the HAA precipitate by vacuum aspiration and reserved.

The pxecipitate from Example 8 was reconstituted with 25 three (10 ml.) volumes of saline solution, and the walls of the centrifuge bottle were washed with 5 ml. of saline bringing the volume to 35 ml. -- all of which was transferred to a small test tube. The pH was adjusted to 7.0 and the HAA was then reprecipitated from the saline solution with 20 percent PEG-4000. Since the precipitate 30 contàins the HAA, special care must be taken with this separation and the disposal of the precipitate after it has been reconstituted in 1.0 ml. saline solution and assayed.

The reserved supernatant from Example 8 containing gamma ~ globulin was adjusted to pH 7.0 by slowly adding 1 N sodium hydroxide, ; with mixing. The precipitate was collected/ washed with ethanol at -5C. in buffer and dissolved in 500 ml. of 0.3 M glycine -oaoo5 M
sodium citrate -0.1 percent buf~e:r, at pH 7Ø

Concentration of HAA from Albumin and/or Preparation of Albumin Free of Hepatitis-Associated Antigen ~HAA) for Clinical Use Fraction V precipitate (2.5 grams) from Cohn Method 6 was diluted in 0.9 percent sodium chloride, to a final protein con-centration of 50 mg./m-. and adjusted to pH 7.0 by slowly adding 1 N
hydrochloric acid. The temperature of this solution was maintained at 25C. Polyethylene glycol (PEG), molecular weight 4000, was added to a final concentration of 20 grams per 100 ml. After 30 minutes of mixing to dissolve the PEG and precipitate the HAA, the solution was centrifuged at room temperature for at least 10 minutes at a relative centrifugal force of 10,000, and the supernatant was separated cleanly from the HAA precipitate by vacuum aspiration and reserved.

The precipitate from Example 11 was reconstituted with three (10 ml.) volumes of saline, and the walls of the centrifuge bottle were washed with 5 ml. bringing the total volume to 35 ml. --all of which was then pooled in a small test tube. The pH wa~ ad-justed to 7.0 and the HAA was then reprecipitated from the saline with 20 percent PEG-4000 and centrifuged. Since the precipitate contains the HAA, special care must be taken in this separation and in the disposal of the precipitate after it has been reconstituted in 1.0 ml. of saline solution and assayed.

The pH of the reserved supernatant from Example 11 con-taining the albu~in was adjusted to 4.8 by slowly adding 1 N

, ~ . , . . :

hydrochloric acid, and the PEG concentration was raised to 30 grams per 100 ml. with PEG 4000. After 30 minutes of mixing to dissolve the PEG and precipitate the HAA, the solution was centrifuged at a RCF of 10,000 for at least 10 minutes at room temperature. The precipitate was collected, washed with 40 percent ehtanol in 0.9 percent saline at -5C, and dissolved in 500 ml. of 0.9 percent sodium chloride, at pH 7Ø

Concentration of HAA for Assay from Fibrinogen or AHF Concentrates and/or Preparation of Fibrinogen or AHF Concentrates Free of Hepatitis-Associated Antigen (HAA) for Clinical Use Lyophilized fibrinogen or fibrinogen-rich AHF concentrate prepared for clinical use (approximately 1 1/2 - 2 Gm.) was recon-stituted in 200 ml. of distilled water and diluted to a protein concentration of 2 mg./ml. with 0.02 M tris-0.02 M citrate buffer.
High pH Method. The pH of the solution was adjusted to 10.3 with 1 N NaOH. After the diluted fibrinogen or A~F had been mixed for 30 minutes at room temperature, PEG-4000 was added to a final concentration of 30 grams per 100 ml. and mixing was continued for 30 minutes. The pH was maintained at 10.3 throughout this stage to prevent any precipitation of the fibrinogen or AHF, and to dissolve any that had already precipitated.

Low pH Method. The procedure of Example 1~ ~was ollowed, but the pH was adjusted to 3.5 using 1 N HCl. After the diluted fibrinogen or AHF had been mixed for 30 minutes at room temperature, PEG-4000 was added to a final concentration of 20 grams per 100 ml.
and mixing was continued for 30 minutes at room temperature. The pH
was maintained at 3.5 throughout this stage to prevent any pre-cipitation of the fibrinogen or AHF, and to dissolve any that hadalready precipitated. Such precipitation may occur at a pH of 4.0 or more, but rarely below 4.2.

.. . .

3~.

' With both the high and low pH methods, of Examples 14 and 15, the mixture was then centrifuged for about oneehour at 10,000 ~CF at 20C. to bring down the HAA, and the supernatant was aspirated carefully to avoid disturbing any minute quantity of precipitate visible at the bottom of the centrifuge cup. The precipitate was reconstituted with three successive 10 ml. volumes of saline, and the walls of the centrifuge bottle were washed with an additional 5 ml. bringing the total volume to 35 ml. - all of which was pooled in a small test tube. The HAA was then reprecipitated from the saline solution with 30 percent PEG-4000, at pH 7.0 and centrifuged.
The final precipitate was dissolved in 1.0 ml. of 0.02 M tris-0.02 M citrate buffer for optimal concentration.
EXAMæLE 17 The fibrinogen or AHF in the aspirated supernatant from Example 16 was precipitated by adding sufficient 1 N NaOH for the low pH method or 1 N HCl for the high pH method to bring the pH to 6Ø
It was then centrifuged at an RCF of 10,000 for at lea~t 10 minutes at room temperature, the precipitate collected and washed with 10 percent ethanol in water at -2C. and dissolved in 200 ml. of 0.4 percent citrate - 0.9 percent NaCl, at pH 7Ø

Concentration of HAA from a Plasma Fraction Containing Prothrombln Complex (Factors_II, VII, IX ahd X) and Extractioh of the' F_action Free of Hepatitis-Associated Anti~en (HAA) for Clinical Use Precipitated or lyophilized partially pu~ified prothrom-bin complex (500 mg.), obtained by DEAE column chromatography, was dissolved in a 20 percent PEG-buffer solution of 0.03 M glycine-0.0005 M sodium citrate - 0.01 percent sodium chloride, p~ 7.0 (ionic strength of 0.003), to a protein concentration of 5.0 mg./ml.
The temperature of this solu~ion was maintained at 25C. After 30 minutes of mixing to extract the prothrombin complex and precipitate the HAA, the solution was centrif~d at room temperature for at least 10 minutes at a RCF of approximately 10,000, and the supernatant was separated cleanly from the HAA precipitate by vacuum aspiration and reserved.

The precipitate from Example 18 was reconstituted with three (10 ml.) volumes of saline, and the walls of the centrifuge bottle were washed with an additional 5 ml., bringing the total volume to 35 ml. -- all of which was pooled in a small test tube.
The HAA was then reprecipitated from the saline at pH 7~0 with 20 percent PEG-4000 and centrifuged. Since the precipitate contains the HAA, special care must be taken in this separation and in disposition of the precipitate after it has been reconstituted in 0.2-1.0 ml.
normal saline and assayed.

The reserved supernatant from Example 18 containing Factors II, VII, IX and X was ad~usted to a pH of 5.2 by adding 1 N
hydrochloric acid, and the PEG concentration was raised to 30 grams per 100 ml. with PEG-4000. After 30 minutes of mixing to dissolve the PEG and precipitate the HAA, the solution was centrifuged at a RCF of 10,000 for at least 10 minutes at room temperature. The pre-cipitate was collected, washed with 30 percent ethanol at -5C.
in buffer(pH 5.2) and dissolved in 20 ml. of 0.03 M glycine - 0.005 M
sodium citrate - 0.1 percent sodium chloride buffer, at pH 7Ø
It should be understood that reference to the isoelectric point of a substance mean5 the pH at which the net charge on a mole-cule in solution is 0. At this pH, amino acids exist almost entirely in the zwitterion state; that is, the positive and negative groups are equally ionized. A solution of proteins or amino acids at the isoelectric point exhibits minimum conductivity, osmvtic pressure, and viscosity.
It is also understood that "saline" solution, unless otherwise indicated, refers to physiologic saline solution.

It should be apparent from the foregoing detailed description that the objects set forth hereinabove have been successfully achieved. Moreover, while there is shown and described a present preferred embodiment of the invention, it is to be distinct-ly understood that the invention is not limited ~hereto but may be otherwise variously embodied and practiced within the scope of the ; following claims.

Claims (21)

THE EMBODIMENTS OF THE INVENTION IN WHICH AN EXCLUSIVE
PROPERTY OR PRIVILEGE IS CLAIMED ARE DEFINED AS FOLLOWS:
1. A method of removing hepatitis-associated antigen from a protein fraction containing the same comprising the steps of:
a) solubilizing said antigen-containing protein in a solvent which is physiologically tolerable on injection wherein solubility of said antigen-containing protein is maintained with a solvent having a pH removed as far as possible from isoelectric point of said protein without causing denaturation and still permitting preciptation of the antigen;
b) adding polyethylene glycol having a molecular weight of from about 200 to about 6,000 to a concentration of from about 12 to about 30 grams per 100 milliliters of solution to thereby obtain a precipitate containing said antigen; and c) separating said antigen from said protein.
2. A method as defined in Claim 1, wherein said polyethylene glycol precipitates said antigen and said protein, further comprising extracting said protein from said precipitate in a solvent having a pH removed from the isoelectric point of said protein.
3. A method as defined in Claim 1, wherein said poly-ethylene glycol has a molecular weight of about 4,000 and said concentration is from about 20 to 30 grams per 100 milliliters of solution.
4. A method as defined in Claim 1, wherein said steps are performed at a temperature of from about 15 to 25°C.
5. A method as defined in claim 4, wherein said steps are performed at room temperature.
6. A method as defined in Claim 1, wherein the pH is separated by 1.0 to 2.0 units from said isoelectric point.
7. A method as defined in Claim 6, wherein said solvent has an ionic strength between 0.001 and 0.2.
8. A method as defined in Claim 7, wherein said solvent is selected from the group consisting of glycine-citrate-saline buffer, tris (hydroxymethyl) aminomethane-citrate buffer, tris (hydroxymethyl) aminomethane-citrate-urea buffer, phosphate buffer, phosphate-saline buffer, ammonium or sodium acetate, sodiumbicarbonate-CO2, an amino acid, physiologic saline solution and water.
9. A method as defined in Claim 7, wherein said solvent is a buffer solution of a concentration suitable to provide a predetermined pH.
10. A method as defined in Claim 6, wherein said antigen is removed from said protein by centrifugation of filtration.
11. A method as defined in Claim 10, wherein said centrifugation varies from about 10,000 to 15,000 RCF for about 4 minutes to about one hour.
12. A method as defined in Claim 10, wherein said separation is by filtration using a filter having a pore size below about 0.6 mµ.
13. A method as defined in Claim 12, wherein said pore size is from about 0.45 to about 0.2 mµ.
14. A method as defined in Claim 6, further comprising purifying and concentrating said antigen by the steps of:
a) maintaining solubility of said antigen in a solvent at a pH of about 7;
b) adding polyethylene glycol having a molecular weight of about 4,000 to a concentration of about 20 percent to reprecipitate said antigen; and c) removing said reprecipitated antigen from the resulting supernatant.
15. A method as defined in Claim 6, further comprising concentrating said protein by:
a) adjusting the pH of said supernatant to near the isoelectric point of said protein to thereby precipitate said protein; and b) collecting said precipitated protein.
16. A method as defined in Claim 1, wherein said protein fraction is a member of the group consisting of albumin, gamma globulin, coagulation Factors II, V, VII, IX, X, XI and XIII, fibrinogen, antihemophilic factor, plasminogen, ceruloplasmin, transferring, thyroxin-binding protein, antithrombin III, .alpha. 1 antitrypsin,.alpha. 2 macroglobulin C? inactivator, inter .alpha. -trypsin inhibitor and mixtures thereof.
17. A method as defined in Claim 16, wherein said mixtures include prothrombin complex and sewage.
18. A method for separating Hepatitis-associated antigen from solutions of blood plasma and plasma fractions which contain plasma proteins and said antigen, comprising adding polyethylene glycol to said solution in an amount and at a molecular weight sufficient to precipitate substantially all of said antigen from said solution, and separating said precipitate containing said antigen from said solution.
19. A method for separating Hepatitis-associated antigen from solutions of blood plasma and plasma fractions which contain plasma proteins and said antigen, comprising adding to said solution per 100 milliliters of said solution about 12 to about 30 grams of polyethylene glycol having a molecular weight of from about 200 to 6000 so as to precipitate said antigen from said solution, and separating the resulting precipitate consisting essentially of said antigen from said solution containing said plasma proteins substantially free of said Hepatitis-associated antigen.
20. A method as defined in claim C1, wherein the pH
is separated by 1.0 to 1.8 units from said isoelectric point.
21. A method as defined in Claim C16, wherein said solvent has an ionic strength of 0.15.
CA166,295A 1972-03-16 1973-03-16 Method of removing hepatitis-associated antigen from protein fraction Expired CA1061251A (en)

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Publication number Priority date Publication date Assignee Title
US3951937A (en) * 1973-12-20 1976-04-20 The Community Blood Council Of Greater New York, Inc. Large scale purification of hepatitis type B antigen using polyethylene glycol
DE2602892A1 (en) * 1976-01-27 1977-07-28 Community Blood Council Highly purified hepatitis type B antigen from blood materials - by double pptn. with polyethylene glycol
DK25877A (en) * 1977-01-21 1978-08-15 Nordisk Insulinlab PROCEDURE FOR EXTRACTING PURE ALBUMIN FROM BLOOD PLASMA
US4197238A (en) * 1977-04-12 1980-04-08 The Green Cross Corporation Method of preparation of human albumin using polyethylene glycol
DE2750045A1 (en) * 1977-11-09 1979-05-10 Behringwerke Ag METHOD FOR REMOVING DETERGENTS FROM VIRUS ANTIGENS SUSPENSIONS
US4164496A (en) * 1978-08-23 1979-08-14 American National Red Cross Preparation of albumin using PEG and EDTA
US4395395A (en) * 1979-05-21 1983-07-26 The United States Of America As Represented By The Department Of Health And Human Services Detection of non-A, non-B hepatitis associated antigen
FR2483779A1 (en) * 1980-06-05 1981-12-11 Synthelabo PROCESS FOR ISOLATING VIRAL GLYCOPROTETIC ANTIGENS AND APPLICATION THEREOF TO VACCINE PREPARATION
US4835257A (en) * 1984-07-07 1989-05-30 Armour Pharma Gmbh Process for preparing gamma globulin suitable for intravenous administration using peg and a citrate buffer
US4683294A (en) * 1985-04-03 1987-07-28 Smith Kline Rit, S.A. Process for the extraction and purification of proteins from culture media producing them
US4684723A (en) * 1985-09-11 1987-08-04 Miles Laboratories, Inc. Method of separating proteins from aqueous solutions
US4833233A (en) * 1987-08-20 1989-05-23 The United States Of America As Represented By The Administrator Of The National Aeronautics And Space Administration Human serum albumin crystals and method of preparation
US5525519A (en) * 1992-01-07 1996-06-11 Middlesex Sciences, Inc. Method for isolating biomolecules from a biological sample with linear polymers
WO2008097581A1 (en) * 2007-02-06 2008-08-14 Incept, Llc Polymerization with precipitation of proteins for elution in physiological solution
EP2121753A2 (en) * 2007-02-14 2009-11-25 Amgen, Inc Method of isolating antibodies by precipitation

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