DK155606B - METHOD OF CLEANING HEPARIN - Google Patents

METHOD OF CLEANING HEPARIN Download PDF

Info

Publication number
DK155606B
DK155606B DK096077AA DK96077A DK155606B DK 155606 B DK155606 B DK 155606B DK 096077A A DK096077A A DK 096077AA DK 96077 A DK96077 A DK 96077A DK 155606 B DK155606 B DK 155606B
Authority
DK
Denmark
Prior art keywords
heparin
gel
antithrombin
bound
matrix
Prior art date
Application number
DK096077AA
Other languages
Danish (da)
Other versions
DK96077A (en
DK155606C (en
Inventor
Lars-Olov Andersson
Erik Yngve Holmer
Original Assignee
Kabi Ab
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kabi Ab filed Critical Kabi Ab
Publication of DK96077A publication Critical patent/DK96077A/en
Publication of DK155606B publication Critical patent/DK155606B/en
Application granted granted Critical
Publication of DK155606C publication Critical patent/DK155606C/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08BPOLYSACCHARIDES; DERIVATIVES THEREOF
    • C08B37/00Preparation of polysaccharides not provided for in groups C08B1/00 - C08B35/00; Derivatives thereof
    • C08B37/006Heteroglycans, i.e. polysaccharides having more than one sugar residue in the main chain in either alternating or less regular sequence; Gellans; Succinoglycans; Arabinogalactans; Tragacanth or gum tragacanth or traganth from Astragalus; Gum Karaya from Sterculia urens; Gum Ghatti from Anogeissus latifolia; Derivatives thereof
    • C08B37/0063Glycosaminoglycans or mucopolysaccharides, e.g. keratan sulfate; Derivatives thereof, e.g. fucoidan
    • C08B37/0075Heparin; Heparan sulfate; Derivatives thereof, e.g. heparosan; Purification or extraction methods thereof

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Polymers & Plastics (AREA)
  • Engineering & Computer Science (AREA)
  • Biochemistry (AREA)
  • Materials Engineering (AREA)
  • General Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Molecular Biology (AREA)
  • Organic Chemistry (AREA)
  • Medicines That Contain Protein Lipid Enzymes And Other Medicines (AREA)
  • Peptides Or Proteins (AREA)
  • Polysaccharides And Polysaccharide Derivatives (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
  • Treatment Of Liquids With Adsorbents In General (AREA)
  • Medicines Containing Material From Animals Or Micro-Organisms (AREA)

Description

DK 155606BDK 155606B

Den foreliggende opfindelse angår en fremgangsmåde til fremstilling af heparin med høj specifik aktivitet; fremgangsmåden ifølge opfindelsen er ejendommelig ved det i krav 1's kendetegnende del angivne.The present invention relates to a process for the preparation of heparin with high specific activity; the process according to the invention is characterized by the characterizing part of claim 1.

5 Heparin har været anvendt i lægekunsten i flere årtier. Det er et af de mest kendte antikoagulations-midler og anvendes i stort omfang bl.a. til at forhindre blodpropper. Heparin er et sulfateret polysakkarid som kan fremstilles ud fra animalsk tarmslim eller lunge ved 10 en forholdsvis kompliceret fremgangsmåde. De heparin- præparater som anvendes klinisk nu om stunder indeholder materiale af meget varierende molekylstørrelse, fra ca. 5000 op til ca. 35.000. Den specifikke aktivitet plejer at være ca. 130 enheder pr. mg. De for tiden til-15 gængelige kommercielle præparater er altså ganske heterogene. Hyppigheden af bivirkninger ved heparinterapi er ganske lav, men de tilfælde som forekommer giver problemer der er vanskelige at løse. En del af disse bivirkninger kan sandsynligvis henføres til forureninger i he-20 parinpræparatet.5 Heparin has been used in medicine for several decades. It is one of the best known anticoagulants and is widely used i.a. to prevent blood clots. Heparin is a sulfated polysaccharide that can be prepared from animal gut or lung by a relatively complicated process. The heparin preparations used clinically nowadays contain material of very varied molecular size, from ca. 5000 up to approx. 35,000. The specific activity is usually approx. 130 units per mg. The commercially available commercially available preparations are thus quite heterogeneous. The frequency of side effects with heparin therapy is quite low, but the cases that occur cause problems that are difficult to solve. Some of these side effects are probably attributable to contaminants in the heparin preparation.

Der er derfor gode grunde til at fremstille renere, mere specifikt virksomme heparinpræparater end de for tiden anvendte. I forbindelse med studier over anti-trombin, som er co-faktor til heparin, undersøgtes mu-25 ligheden for materixbinde proteinet. Det viste sig overraskende at matrixbundet (sakkarosebundet) antitrombin specifikt kunne binde den molekylfraktion i det som lægemiddel anvendte heparin, der er bærer af den klinisk værdifulde, tromboseprofylaktiske virkning af heparin.Therefore, there are good reasons to make cleaner, more specifically effective heparin preparations than those currently used. In connection with anti-thrombin co-factor to heparin studies, the possibility of the matrix binding protein was investigated. Surprisingly, it was found that matrix-bound (sucrose-bound) antithrombin could specifically bind the molecular fraction of the drug used as a drug, the carrier of the clinically valuable thrombosis prophylactic effect of heparin.

30 Gennem passende valg af adsorptionsbetingelsr og de- sorptionsbetingelser kan der fremstilles et overordnet-ligt rent heparin. De specifikke aktiviteter, der vandtes, var 200-270 enheder/mg, der skal sammenlignes med ca. 130 enheder/mg i udgangsmaterialet. Molekylvægtfor-35 delingen i det rensede heparin var meget snævrere end hos udgangsmaterialet. Udover heparins cofaktor-anti-trombin kan der også anvendes et heparinbindende proteinBy suitable choice of adsorption conditions and conditions, an exceptionally pure heparin can be prepared. The specific activities gained were 200-270 units / mg, which should be compared with approx. 130 units / mg in the starting material. The molecular weight distribution in the purified heparin was much narrower than that of the starting material. In addition to the cofactor anti-thrombin of heparin, a heparin-binding protein can also be used

DK 155606 BDK 155606 B

2 såsom inter-a-trypsin-inhibitor med molekylvægt ca.2, such as molecular weight inter-α-trypsin inhibitor, ca.

150.000, vundet under isolering af koagulationsfaktor IX (B-faktor). Det kvalitativt bedste heparin vandtes med matrixbundet antitrombin med specifikke aktiviteter 5 op til 270 enheder/mg.150,000, obtained during the isolation of coagulation factor IX (B factor). The best quality heparin was obtained with matrix-bound antithrombin with specific activities 5 up to 270 units / mg.

Heparin med overordentlig høj renhed og specifik aktivitet kan altså fremstilles på den her angivne måde. Processen er simpel og industrielt anvendelig til at fremstille heparin med højere specifik aktivitet end 10 eksisterende præparater. Bestemmelse af heparins specifikke aktivitet er udført i henhold til Denson og Bonnar (1975, Brit J Haematol, 30, side 139).Thus, heparin of extremely high purity and specific activity can be prepared in the manner set forth herein. The process is simple and industrially applicable to produce heparin with higher specific activity than 10 existing preparations. Determination of the specific activity of heparin has been performed according to Denson and Bonnar (1975, Brit J Haematol, 30, page 139).

Nogle eksempler tjener til nærmere belysning af fremgangsmåden ifølge opfindelsen.Some examples serve to elucidate the method of the invention.

1515

Eksempel 1Example 1

Rensning af heparin med matrixbundet antitrombin. Ko- lonnefremgangsmåde_ 2Q Geladsorbenset fremstilledes på følgende måde:Purification of heparin with matrix-bound antithrombin. Column Procedure_ 2Q The gel sorbent was prepared as follows:

Aktivering 3 g BrCN opløstes i 30 ml destilleret vand. Der sattes 50 ml agarose ("Sepharose'^ 4B) til BrCN-opløs-ningen. Blandingen afkøledes på et isbad under omrøring.Activation 3 g of BrCN was dissolved in 30 ml of distilled water. 50 ml of agarose ("Sepharose" 4B) was added to the BrCN solution. The mixture was cooled on an ice bath with stirring.

2^ Ved tilsætning af 4M NaOH hævedes pH til 11,2 og holdtes konstant der i 10 minutter. Derefter vaskedes gelen med koldt destilleret vand og 0,2M NaHCO^.2 By the addition of 4M NaOH, the pH was raised to 11.2 and kept constant there for 10 minutes. The gel was then washed with cold distilled water and 0.2 M NaHCO 3.

Kobling 2Q 200 mg antitrombin renset i henhold til Miller-Coupling 2Q 200 mg of antithrombin purified according to Miller-

Andersson et al. (1974, Thromb Res 5, side 439-452) og opløst i 50 ml 0,2M NaHCO^, pH 9,0, sattes til gelen. Proteinopløsningen og gelen omrørtes ved stuetemperatur i en nat og vaskedes derefter omhyggeligt med puffere 2^ med høj ionstyrke, skiftevis høj og lav pH.Andersson et al. (1974, Thromb Res 5, pages 439-452) and dissolved in 50 ml of 0.2M NaHCO 3, pH 9.0, was added to the gel. The protein solution and gel were stirred at room temperature for one night and then washed thoroughly with high ionic strength buffer 2, alternating high and low pH.

DK 155606BDK 155606B

33

HeparinrensningHeparinrensning

Geladsorbenset indeholdende matrixbundet anti- trombin pakkedes på en kolonne og bragtes i ligevægt med 0,05M tris, 0,15M NaCl, pH 7,4. 300 mg heparin (Vitruro, specifik aktivitet 130E/mg) opløstes i 20 ml 0,05M tris, 0,15M NaCl, pH 7,4 puffer og pumpedes gennem kolonnen.The gel sorbent containing matrix bound antithrombin was packed on a column and equilibrated with 0.05M Tris, 0.15M NaCl, pH 7.4. 300 mg of heparin (Vitruro, specific activity 130E / mg) was dissolved in 20 ml of 0.05M Tris, 0.15M NaCl, pH 7.4 buffer and pumped through the column.

Gelen vaskedes med ovennævnte puffer og det adsorberede heparin desorberedes derefter med 0,05M tris, 1,0M NaCl, pH 7,4 puffer. Det eluerede heparin befriedes fra saltThe gel was washed with the above buffer and the adsorbed heparin was then desorbed with 0.05M Tris, 1.0M NaCl, pH 7.4 buffer. The eluted heparin is freed from salt

ÆDAED

ved gelfiltrering på en kolonne pakket med "Sephadex"^ G-25 i destilleret vand og frysetørredes. Det rensede heparin havde en specifik aktivitet på 270 E/mg.by gel filtration on a column packed with "Sephadex" ^ G-25 in distilled water and freeze-dried. The purified heparin had a specific activity of 270 U / mg.

Undersøgelse af molekylvægtfordelingen for dette heparin viser at det har betydeligt snævrere molekylvægtfordeling end det som udgangsmateriale anvendte heparin.Examination of the molecular weight distribution of this heparin shows that it has significantly narrower molecular weight distribution than the starting heparin used.

Kulhydratanalyse ved gelfiltrering blev foretaget ved karbazol-^SO^-metoden.Carbohydrate analysis by gel filtration was done by the carbazole® SO 2 method.

Eksempel 2Example 2

Rensning af heparin på matrixbundet antitrombin. Batch- proces_Purification of heparin on matrix-bound antithrombin. Batch Process_

Antitrombinmatrixen fremstilledes som beskrevet i eksempel 1.The antithrombin matrix was prepared as described in Example 1.

Heparinrensning 500 mg heparin (Vitrum, specifik aktivitet 130 E/mg) opløstes i 300 ml 0,05M tris, 0,15M NaCl, pH 7,4 puffer. 300 ml sedimenteret antitrombin indeholdende gelabsorbens ækvilibreredes i ovennævnte puffer og blev suget tørt. Gelen sattes til heparinopløsningen efterfulgt af omrøring ved stuetemperatur i 1 time. Gelen blev suget tør på glasfilter og vaskedes med 10 x 200 ml 0,05M tris, 0,15 NaCl, pH 7,4 puffer. Det adsorberede heparin desorberedes derefter fra gelen med 3 x 200 ml 0,05M tris, 1,0M NaCl, pH 7,4. Det eluerede hepa-Heparin Purification 500 mg of heparin (Vitrum, specific activity 130 U / mg) was dissolved in 300 ml of 0.05M Tris, 0.15M NaCl, pH 7.4 buffer. 300 ml of sedimented antithrombin containing the gel absorbent was equilibrated in the above buffer and sucked dry. The gel was added to the heparin solution followed by stirring at room temperature for 1 hour. The gel was sucked dry on glass filter and washed with 10 x 200 ml 0.05M Tris, 0.15 NaCl, pH 7.4 buffer. The adsorbed heparin is then desorbed from the gel with 3 x 200 ml 0.05M Tris, 1.0M NaCl, pH 7.4. The eluted hepa-

DK 155606 BDK 155606 B

4 rin koncentreredes ved frysetørring. Tilbageværende salt fjernedes ved gelfiltrering på nSephadex,,,iy G 25 i destilleret vand efterfulgt af frysetørring. Det rensede heparins specifikke aktivitet var 250 E/mg.4 rinse was concentrated by freeze drying. Residual salt was removed by gel filtration on nSephadex, in G 25 in distilled water followed by freeze drying. The specific activity of the purified heparin was 250 U / mg.

55

Eksempel 3Example 3

Rensning af heparin på geladsorbens indeholdende matrix- bundet inter-a-trypsin-inhibitor_ 1q Fremstilling af geladsorbens I forbindelse med rensning af koagulationsfaktor IX (B-faktor) (L.-O. Andersson et al., 1975, Thromb Res, 7, side 451-459) vandtes det heparinbindende protein in-ter-a-trypsin-inhibitor. Dets molekylvægt er ca. 150.000.Purification of heparin on gelase sorb containing matrix-bound inter-α-trypsin inhibitor pages 451-459), the heparin-binding protein in-ter-α-trypsin inhibitor was obtained. Its molecular weight is approx. 150,000.

250 mg af dette protein opløstes i 200 ml 0,2M NaHCO^, pH 9,0 puffer og sattes derefter til 50 ml sedimenteret "Sepharose"® 4B som var aktiveret med BrCN som beskrevet i eksempel 1. Proteinopløsningen og gelen omrørtes ved stuetemperatur natten over. Gelen vaskedes derefter ana-2Q logt med gelen i eksempel 1.250 mg of this protein was dissolved in 200 ml of 0.2 M NaHCO 3, pH 9.0 buffer and then added to 50 ml of sedimented "Sepharose" ® 4B activated with BrCN as described in Example 1. The protein solution and gel were stirred at room temperature overnight. over. The gel was then washed ana-2Q log with the gel of Example 1.

HeparinrensningHeparinrensning

Geladsorbenset indeholdende det matrixbundet protein pakkedes på en kolonne. 300 mg heparin (Vitrum) op-2^ løst i 20 ml 0,05M tris, 0,15M NaCl, pH 7,4 puffer pumpedes ind i kolonnen. Gelen vaskedes med ovennævnte puffer og det adsorberede heparin desorberedes derefter med 0,05M tris, 1,OM NaCl, pH 7,4 puffer. Heparinet befrie-des fra salt ved gelfiltrering på "Sephadex,wy G 25 30 (tværbundet dextran) i destilleret vand og frysetørredes derefter. Det rensede heparins specifikke aktivitet var 230 E/mg.The gel sorbent containing the matrix bound protein was packed onto a column. 300 mg of heparin (Vitrum) dissolved in 20 ml of 0.05M Tris, 0.15M NaCl, pH 7.4 buffer was pumped into the column. The gel was washed with the above buffer and the adsorbed heparin was then desorbed with 0.05M Tris, 1 OM NaCl, pH 7.4 buffer. The heparin was liberated from salt by gel filtration on Sephadex, containing G 25 30 (crosslinked dextran) in distilled water and then lyophilized. The specific activity of the purified heparin was 230 U / mg.

3535

Claims (2)

1. Fremgangsmåde til fremstilling af heparin med høj specifik aktivitet, kendetegnet ved at der anvendes en vanduopløselig'. gelmatrix, til· hvilken 5 der er bundet antitrombin eller inter-a-trypsin-inhi-bitor med en molekylvægt på ca. 150.000, til at adsor-bere en heparinfraktion med specifik antitrombincofak-tor-aktivitet, hvorefter den gelbundne heparinfaktor desorberes.A process for the preparation of heparin with high specific activity, characterized by the use of a water-insoluble '. gel matrix to which 5 is bound antithrombin or inter-α-trypsin inhibitor having a molecular weight of approx. 150,000 to adsorb a heparin fraction with specific antithrombin cofactor activity, after which the gel-bound heparin factor is desorbed. 2. Fremgangsmåde ifølge krav 1, kendeteg net ved at der anvendes en agarosegel som gelmatrix. 15 20 25 30 35Process according to claim 1, characterized in that an agarose gel is used as a gel matrix. 15 20 25 30 35
DK096077A 1976-03-05 1977-03-04 METHOD OF CLEANING HEPARIN DK155606C (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
SE7603040A SE431218B (en) 1976-03-05 1976-03-05 HEPARIN PURIFICATION PROCEDURE
SE7603040 1976-03-05

Publications (3)

Publication Number Publication Date
DK96077A DK96077A (en) 1977-09-06
DK155606B true DK155606B (en) 1989-04-24
DK155606C DK155606C (en) 1989-09-11

Family

ID=20327240

Family Applications (1)

Application Number Title Priority Date Filing Date
DK096077A DK155606C (en) 1976-03-05 1977-03-04 METHOD OF CLEANING HEPARIN

Country Status (21)

Country Link
JP (1) JPS52108012A (en)
AT (1) AT356818B (en)
AU (1) AU508430B2 (en)
CA (1) CA1079272A (en)
CS (1) CS196349B2 (en)
DE (1) DE2709500C2 (en)
DK (1) DK155606C (en)
ES (1) ES456196A1 (en)
FI (1) FI62103C (en)
FR (1) FR2342991A1 (en)
GB (1) GB1539332A (en)
HU (1) HU176811B (en)
IE (1) IE44907B1 (en)
IL (1) IL51346A (en)
NL (1) NL186385C (en)
NO (1) NO144388C (en)
NZ (1) NZ183480A (en)
PL (1) PL103049B1 (en)
SE (1) SE431218B (en)
SU (1) SU736860A3 (en)
ZA (1) ZA771267B (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SE449753B (en) * 1978-11-06 1987-05-18 Choay Sa MUCOPOLYSACCARIDE COMPOSITION WITH REGULATORY EFFECTS ON COAGULATION, MEDICINAL CONTAINING ITS SAME AND PROCEDURE FOR PREPARING THEREOF
GB2164346B (en) * 1984-08-31 1988-03-30 Nicolas Huberto Behrens A non-thrombogenic heparin and a process for its obtention
WO2015112121A1 (en) * 2014-01-21 2015-07-30 The Board Of Trustees Of The University Of Arkansas Heparin affinity tag for use in protein purification

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2623001A (en) * 1949-04-07 1952-12-23 Bengt E G V Sylven Preparing heparin
DE1195010B (en) * 1962-05-12 1965-06-16 Ormonoterapia Richter S P A Method for purifying heparin by the chromatographic method

Also Published As

Publication number Publication date
FI770491A (en) 1977-09-06
GB1539332A (en) 1979-01-31
DE2709500A1 (en) 1977-09-08
NL186385B (en) 1990-06-18
NO144388C (en) 1981-08-19
NL186385C (en) 1990-11-16
NZ183480A (en) 1979-08-31
IL51346A (en) 1979-11-30
SU736860A3 (en) 1980-05-25
IL51346A0 (en) 1977-03-31
PL103049B1 (en) 1979-05-31
FR2342991A1 (en) 1977-09-30
FR2342991B1 (en) 1981-10-30
NO144388B (en) 1981-05-11
CS196349B2 (en) 1980-03-31
HU176811B (en) 1981-05-28
ES456196A1 (en) 1978-07-01
SE431218B (en) 1984-01-23
FI62103C (en) 1982-11-10
JPS52108012A (en) 1977-09-10
IE44907B1 (en) 1982-05-19
ATA144577A (en) 1979-10-15
NO770764L (en) 1977-09-06
AT356818B (en) 1980-05-27
ZA771267B (en) 1978-01-25
CA1079272A (en) 1980-06-10
DK96077A (en) 1977-09-06
NL7701882A (en) 1977-09-07
SE7603040L (en) 1977-09-06
AU508430B2 (en) 1980-03-20
AU2295377A (en) 1978-09-07
IE44907L (en) 1977-09-05
FI62103B (en) 1982-07-30
DE2709500C2 (en) 1986-09-18
DK155606C (en) 1989-09-11

Similar Documents

Publication Publication Date Title
DK141274B (en) Method for isolating the blood coagulation factors.
US5324823A (en) Adsorbent for cellular fibronectin and a method for fractional purification of fibronectin
US5104860A (en) Heparin derivatives and process for their preparation
FI95136C (en) Procedure for cleaning annexins
CA2024667C (en) Process for preparing a concentrate of blood coagulation factor viii-von willebrand factor complex from total plasma
US4119774A (en) Heparin purification method
EP0058993A2 (en) Process for heat treatment of aqueous solution containing cold insoluble globulin
JP2726275B2 (en) Purification of glycosaminoglycan degrading enzyme
US4314994A (en) Process for obtaining a plasminogen activator
US4510084A (en) Method of producing an antithrombin III-heparin concentrate or antithrombin III-heparinoid concentrate
US4689323A (en) Covalently bound heparin--antithrombin-III complex
US3879369A (en) Anti-coagulant isolation from malayan pit viper using affinity chromatography
JP3471379B2 (en) Method for preparing human antithrombin-III
DK155606B (en) METHOD OF CLEANING HEPARIN
KR970001810B1 (en) Process for the purification of the placenta tissue protein pp4
CA1283073C (en) Adsorbent for purification of blood coagulation factor viii and process for purification of blood coagulation factor viii using the same
JPH0423751B2 (en)
JP2006089632A (en) Method for preparing heparin-like substance by using marine organism
JPH09286797A (en) Heparin cofactor ii and its purification
JP2903251B2 (en) Carrier for affinity chromatography and method for purifying antithrombin III
CN107674868B (en) Method for extracting thrombin from pig blood
RU2749424C1 (en) Method for obtaining drug with anti-coagulant activity
JP2000103800A (en) Purification of immunoglobulin a
RU1799599C (en) Method of lectin preparation
JP2753686B2 (en) Blood coagulation inhibitors and functional foods

Legal Events

Date Code Title Description
PUP Patent expired