NON-ANTICOAGULANT HEPARAN SULFATE, PROCESS FOR EXTRACTION FROM ORGANS, AND PHARMACEUTICAL COMPOSITIONS THEREOF

Abstract: A process for the extraction of heparan sulfate from animal organs and tissues, such as spleen, pancreas, kidney, mucosa. The process comprises preparation of a complex of heparan sulfate with macroporous basic resins, decomplexation with salts of appropriate ionic strength and purification on resins. The obtained heparan sulfate has a low sulfur content, a SO3/-COO<-> ratio lower than 1, antithrombotic activity higher or equal to that of heparin and substantially no anticoagulant activity.

Description: . . - - Non-anticoagulant heparan sulfate, process for extraction from organs, and pharmaceutical compositions thereof. The present invention relates to a novel heparan sulfate having high antithrombotic activity, high bio-av¬ ailability, no anticoagulant activity; to a process for the extraction thereof from organs and tissues and to the relating pharmaceutical compositions. Heparan sulfate has a hibrid structure which could be represented by an average recurrent unity, which is intermediate between the acetylated disaccharide: (1— ■ > 4 )-0-2-acetamido-2-deoxy- ( -D-glucopyranosyl-(1 ■ >4)-0- β-D-glucopyranosyl uronic acid and the trisulfated disac¬ charide: (1 > ■ 4)-0-2-deoxy-2-sulfamino-C^-D-glucopyra- nosyl-6-sulfate-(1 —-> 4)-O-0(-L-idopyranosyl uronic acid-2- -sulfate. However, the sequence in which said disaccharides are bound, as well as the existence of successions of particularly functionalized disaccharides, able to sel¬ ectively interact with biologically important factors, are not known. Nevertheless, some variability in the composition of heparans from different organs and tissues seems to exist. All the up to now described heparan sulfates, extr¬ acted from mucosa, lung, aorta, myocardium, liver, are characterized in having a sulfur content higher than 6.5%, equal to a -SO /COO ratio higher than 1, corresponding to an uronic acids/hexosamines/-SO molar ratio = 1/1 1. Heparan sulfate, being mainly situated on cellular and parietal membranes, plays a physiological role of paramount importance. Reticuloendothelial system, under normal conditions, is rich in receptors carrying heparan sulfate which, due to the its electric charges, markedly contributes to the preservation of superficial electroneg¬ ative potential. As long as said electronegative charge condition lasts, any thrombogenesis"phenomenon is prevent- ed (Sawyer P.N. et al., "7th Europ. Conf. on Microcircul- ation", Karger, Basel 1973). Moreover, complex interaction mechanisms between endogenous heparanic structures and hexogenous and endogenous heparinic structures have been evidenced at the parietal level (Dawes J. and Witt J., "Heparin: New -Biochemical and Medical aspects", W. DeGruyter and Co., Berlin 1982 p.45). Said mechanisms consist in the possibility that endogenous or hexogenous circulating glucosaminoglycans preserve parietal glucos- aminoglyeans, by means of a mainly competitive mechanism, preventing LDL, PF and other atherogenic or thrombogenic proteins from depositing therein, or favouring the rem- otion of said proteins or causing the transformation thereof through the activation of lipolytic enzymes, which are latent on parietal heparanic structures. Endothelial wall is thereby kept "clean". Thus, a natural heparan sulfate, administered for therapeutical or prophylactic purposes, should have an undoubted pharmacologic value, since it can take part in the above mentioned mechanism. Recently, heparan sulfate has been proposed as a fibrinolytic antithrombotic, due to its therapeutic power, especially to its well-known poor anticoagulant activity._ Prolonged use of this kind of drugs is allowed only prov¬ ided they have poor or no anticoagulant activity as well as poor or no bleeding effect. Antithrombotic activity of the up to now charact¬ erized heparan sulfates has always been related to re¬ sidual anticoagulant activity, which in its turn always proved to depend on the antithrombin III (AT III) affinity (Hub ' bard A.R. et al. , Thromb. Res., 35_, 567, 1984). The pattern of the different activities of heparan sulfates was compared with heparin activities: a stru¬ cture-activity relationship was always evidenced, in which a closer structural likeness was connected with a higher pharmacological activity and a higher "SO group content corresponded to a more marked lipasemic activity (Casu B. et al. Arznei . Forsch., 33, I, 135, 1983), to a higher anticoagulant activity (Fransson L.A. et al., Em. J. Biochem., 106, 59, 1980) and to an increased uptake by endothelial cells (Barzu T. et al., Nouv. Rev. Hemat. , 2_6 243, 1984.) . All the heparans hitherto described have a high sulfur average content, since the uronic acids/hexos- amines/-Sθ " molar ratio can range from 1/1/1 up to .1/1/1.9 (Johnson E.A., Thromb. Res., _35, 583, 1984) or from 1/1/1 up to 1/1/2 (Casu B. et al., Arzneim. Forsch., _3_3, 1, 140, 1983). EP-A-0.097.625 discloses a process for the extr¬ action of heparan sulfate (HS) from bovine mucosa, which process consists in fractional precipitations of glucos- aminoglycans with salts and purification of HS with cond- roitinase ABC, to remove condroitin sulfates and dermatan sulfate which are always present with heparan sulfate. Availability of pure condroitinase ABC is an important problem, all the more on industrial scale. Therefore, purification of heparan sulfate by means of condroitinase ABC is practically impossible. EP-A-0.199.033 discloses a process for the extr¬ action of HS from aorta and myocardium, through the fol¬ lowing steps " : micronization, cell lysis with high salt concentrations, ultrafiltration, remotion of nucleic acids with activated earths, precipitation with solvents, purif¬ ication on cationic resins, fractional precipitation of dermatan sulfate and heparan sulfate in form of calcium salts, purification and transformation of HS into sodium salt. The obtained product has the following characterist¬ ics: Molecular weight in the range 5:30Kd, sulfation degree: -SO /hexosamines = 1.2/1, iduronic acid = 30-40%, electrophoresis: Rf 1.9-1.96, according to Cappelletti et al.. Anal. Bioch., J9_9, 311, (1979). Analytic indications do not define biunivocally an heparane sulfate. The used electrophoreltic system does not distinguish between HS and fast heparin, neither specific rotations are reported. The process according to the invention relates to the extraction of heparan sulfate from bovine spleen, pancreas, kidney and from other organs and tissues. The process consists in the following operations: - grinding the organs - enzymatic treatment with proteolytic enzymes (papain, alcalase , superase ) - filtration - concentration of the filtrate by reverse osmosis, fol¬ lowed by percolation on a macroporous strong anion exch¬ ange resin, in form of Cl or acetate or OH (such as Lewatit MP 500A, or Amberlite IRA 904). Heparan sulfate is eluted from the resin with a 0.7 - 0.9 M sodium chloride solution. - treatment of the eluate from the column with solvents such as methanol, ethanol or acetone, to precipitate a surprisingly pure product. Alternatively, the reverse osmosis concentrated solution is treated with 30% am¬ monium sulfate. The protein precipitate is filtered off. - dilution of the filtrate 1 5 with water and treatment with a quaternary ammonium salt, such as benzetonium chloride or cetrimonium bromide. - decomplexation of the obtained precipitate with a sodium chloride solution of appropriate molarity, from which polysaccharides are precipitated with water miscible solvents, such as alcohols or acetone. - purification of the polysaccharide mixture on a macropo- rous strong basic resin, from which HS is obtained in pure form by elution with a sodium chloride solution of molarity 0.5 to 0.9, or on a macroporous weak basic resin from which HS is eluted with a 0.15 r 0.3 M sodium chloride solution. The obtained product has the following characteristics: - -20° -.-. _c^J ~~~ — +70 on dry matter -SO~ / C00~ < 1; N-sulfatation abundance= N-Sθ " /(N-SO~ + N-Ac ) ≤ 0.5 (cal- 13 culated for C-NMR); 0-sulfatation abundance in C of aminosugar: 6 C,. - OSO / ( C,- -OSO~+ C -OH ) ≤ 0 . 3 ; 6 3 6 3 6 _ 2-0-sulfated iduronic acid abundance = C -OSO /Total uronic acids .£ 0.2; Average Molecular Weight comprised from 15 to 30 Kd (det- er inated by HPLC) ; Anti-factor Xa activity --? 3 ^ U/mg; Anticoagulant activity = 0 U.I./ mg. Absent. APTT ≤ 0.5 U/mg. - The compound of the invention surprisingly displays antithrombotic activity higher or equal to that of heparin in all the experimental thrombosis patterns. The present invention also applies to all the indu¬ strial aspects related to the use of the products obtained by the process of the invention in human therapy, as an- tithrombotic and fibrinolytic agents, with poor or no anticoagulant activity; to this purpose, the compounds of the invention are formulated with conventional techniques and excipients, in pharmaceutical compositions suited for oral and parenteral administration. Examples of formulations for parenteral administr¬ ation are sterile solutions in vials. Examples of formul¬ ations for oral administration are capsules, tablets, syrups, in which the active ingredient can optionally by vehiculated in form of liposomes or micells. Examples of topical formulations are ointments and creams comprising the conventional excipients. The following examples illustrate in more detail the invention, without limiting the spirit and scope thereof. EXAMPLE 1 1.1 2700 kg of bovine spleen were ground, introduced into a reactor with 2100 1 of water, heated to 60°C, added with 6.4 kg of papain 1:350 and stirred for 2 5 hours at 60°C, then heated for some minutes to 78°C and filtered on filter press. The filtrate was subjected to reverse osmosis on polysulfone spiral membranes • with cut off 20.000. The solution was concentrated to 900 1. 1.2 25% Ammonium sulfate was added to the solution. The ,10 protein precipitate was filtered off. The filtrate was diluted 1:5 with water, added with 10 1 of a 50% dime- thylethyl-cetyl ammonium chloride solution. The obtained precipitate was recovered by centrifugation and immedi¬ ately redissolved in 50 1 of a 1.3 M sodium chloride sol- 15 ution, from which polysaccharides were precipitated with two volumes of methanol. The dried precipitate yielded 1.140 kg of crude product (OP 509). Discontinue electr- ophoresis on agarose (Bianchini et al., J. Chromat., 196, 455, 1980) evidenced: HS, dermatan sulfate and condroitin 20 sulfate A in a 35%, 30%, 30% ratio respectively to each other. 1.3 300 g of the obtained precipitate was dissolved in 5 1 of water added with 150 g of calcium chloride hydrate and 0.3 volumes of ethanol. The precipitate was filtered off. 25 The solution was eluted on a column (0 8 cm, height 30 cm) of a Dowex 50 W-X8, resin, in H form, the eluate was adjusted to pH 5.8, added with 300 g of sodium acetate and 2 volumes of methanol. After filtration and drying, 224 g of the OP 511 product was obtained, having the following 30 composition:HS 45%, dermatan sulfate 22%, condroitin sulf- ate 33% . 1.4. The all- powder was redissolved in 3 1 of water and eluted on a column of Lewatit MP 500 A resin (in acetate form, ft 10 cm,h 100 cm). The column was washed with water and HS was eluted with 1 volume of a 0.7 M sodium chloride solution. The eluate was added with 20 1 of methanol, HS precipitated which was recovered and dried. 100 g of a highly pure product was obtained, having the following characteristics: ^i n =+72, Sulfur= 5.05%, uronic Acids = 31%, -SO /-COO~ =0.92, In vitro activity UAPTT= 0.5 U/mg, UAXa= 1.9 U/mg. Experimental thrombosis by lig- a ion of vena cava in the rat (Reyers S., et al., Thromb. Res., .18,.699, 1980) ED50=0.4 mg/kg. EXAMPLE 2 2.1. 50 kg. of ground bovine spleen was introduced into a reactor containing 75 1 of water. 1.2 kg of sodium chlor¬ ide, sodium hydroxide to pH 8 and 37 kg of Alcalase to 2.4 L Units were added thereto. The mixture was stirred at 50°C for 1.5 hours, then heated to 75°C for 5 minutes and filtered. The filtrate was concentrated by reverse osmosis to 25 liters. The solution was eluted on a column (j 10 cm, h 115 cm) of a macroporous strong basic resin Amberli- te IRA 904, in form of acetate, at a rate of 2 BV/h. The column was washed with 2 volumes of water. Eluate and washings were removed, then the resin was eluted with 2 volumes of a 1.2 M sodium chloride solution at a rate of 3 BV/h, then with 20 1 of water. Eluate and washings were diluted to 100 1 with water and added with 100 g of benze- thonium chloride. The precipitate was recovered by filtra- tion, washed on the filter and suspended in 3 1 of a 1.5 M calcium chloride solution, with stirring for 1 hour. The solution was filtered with 4% filter aid. The filtrate was treated with 2 volumes of methanol. After filtration and drying, 16.1 g of crude product was obtained. 2.2. Said product was redissolved in 300 ml of water and eluted on a column of a cation exchange resin, then dire¬ ctly on a 300 ml column of Lewatit MP 500A (in the OH form) . The eluate was discarded. The resin was eluted with 1200 ml of a 0.75 M sodium chloride solution. HS was pre- cipitated from the solution by means of 2 volumes of methanol. After filtration and drying, 7.6 g of pure HS, coded OP 495075, was obtained, having the following char- 20° — — acteristics: f ] * +76, Sulfur = 4.5%,-SO /-COO = 0.91, UAPTT = 0.5 U/mg, UAXa = 2.3 U/mg. Average molecular weight: 21 Kd. Electrophoresis on agarose gel: (J. of Chromat. , .196, 455, 1980) single band. C.NMR (TMS as the external reference and methanol as the inner reference with chemical shifts 51.75 ppm) : S ppm, 105 (C glucuronic acid), 101 (2-0-sulfated iduronic acid), 97.87 (C, N-acetylated glucosamine) , 67.53 (C. 1 6 6-0-sulfated glucosamine), 60.93 (C 6.OH glucosamine), 6 57.18 (C N-sulfated glucosamine), 54.46 (C N-acetylated glucosamine), 23.4 (acetyl). EXAMPLE 3 3.1. 21.5 kg of bovine kidney was ground and placed in 25 1 of water with 2.5 kg of sodium chloride and 65 g of moxatase at pH 6.3 with sodium hydroxide. The mixture was heated to 50°C for 3.5 hours, then to 95°C for 5 minutes. The solid part was filtered off, filtrate was diluted to 280 1 with water, pH was adjusted to 8.3 with sodium hydr- oxide, then 600 ml of 50% cetrimonium bromide was added. Precipitate was collected and added to 3 1 of a 3 M sodium chloride solution. The mixture was filtered and the filtrate was treated with 2 volumes of methanol. After filtration and drying, 35 g of crude product was obtained. 3.2. The crude product was dissolved in 800 ml of water, added with 8 g of zinc hydride and 40 g of filtration aid. After filtration, the filtrate was treated with 3 volumes of methanol. The precipitate was collected and dried to obtain 15.7 g of an intermediate product, which was puri¬ fied as described in Example 2, point 2.2, but using a macroporous weak basic resin Amberlite IRA-93 SP and HS was eluted in the pure form with a 0.2 M sodium chloride solution. 6.1 g of HS was obtained, having the following characteristics: Sulfur = 4.9%, -SO /-COO = 0.78 and sin¬ gle band on all the electrophoretic systems. ED50 = 0.54 mg/kg on venous thrombosis. EXAMPLE 4 By extraction from pancreas, following a process similar to that described in Example 3, and purification on Lewatit MP 500A resin, compound 436.437 was obtained hav¬ ing the following characteristics: Sulfur = 3.6%, Uronic acids = 34.9%, -SO /-COO =0.62. Ionic band on an electro- phoretic system with acid buffer (Wessler E., Anal. Bioch. 41, 67, 1971), having R related to slow moving heparin = 0.7 and R related to Dermatan=0.77. 13C.NMR: see Figure 1. Pharmacological activity Product OP 436.437 gave the following in vitro values: UAPTT=0.5 U/mg, UAXa=3 U/mg (by chromogenic method), U.I.= 1 U/mg. In venous thrombosis in vivo in the rat (according to Reyers S. et al. , Throm. Res., 33, 699, 1980), ED50=0.3 mg/kg intravenously (i.v.). In venous thrombosis induced by prothrombin concentrated complex (PCC) on rabbit jugular (Fareed J. et al. "Seminars in Throm. Haemost., 11, 2, 155, 1985) ED50=0.053 mg/kg i.v. and ED50=0.50 mg/kg subcutaneous (s.c). 2123.3M Heparin respectively had ED50=0.055 mg/kg ' i.v. and " ED50 >> 1 mg/kg s.c. In the venous thrombosis pattern induced by PCC and Russel viper venom (RVV) in the rabbit the following activities were obtained: ED50=0.069 mg/kg i.v. and ED50=0.7 mg/kg s.c. In the same experimental thrombosis pattern, heparin has ED50=0.05 mg/kg i.v. and ED50=1.1 mg/kg s.c, respective- ly. HS obtained according to the present process proved to be surprisingly active on thrombosis patterns induced by thrombogenic agents such as prothrombin complex (PCC) and phospholipase A obtained from RW, which give raise to thrombin and respectively act on coagulation and platelet aggregation. Since HS turned out to be 4.2x10 times less 3 active than heparin on thrombin and 2.8x10 times less 2 active than heparin and 1.5x10 times less active than dermatan sulfate on heparin cofactor II (HCII), it should be assumed that HS acts by means of an hitherto unknown and surprising mechanism.

Claims: CLAIMS 1. A process for the preparation of pure heparan sulf- ate from animal organs and tissues, which process consists of the following steps: - grinding and mild treatment with protelytic enzymes"; - concentration of the filtrate by reverse osmosis; - formation of an unsoluble heparane complex, which can be extracted from the reaction solution; - remotion of the proteins from the solution by selective precipitation; - decomplexation of the heparan complex with saline solut¬ ions of appropriate ionic strenght; - remotion by selective precipitation of nucleic acids which pollute heparane, - purification of heparan sulfate on macroporous basic resins. 2. A process according to claim1=, in which enzymes are papain, alcalase, superase, moxatase. 3. A process accoding to claim 1, in which the mem¬ branes for reverse osmosis have a 20 Kd cut off. 4. A process according to claim 1, in which the unsol¬ uble complex consists of heparan sulfate and a macroporous strong basic resin, such as Lewatit MP 500A or Amberlite IRA 904, or a macroporous weak basic resin, such as Amber- lite IRA 93 SP, or a quaternary ammonium salt, such as benzethonium chloride or cetrimonium bromide. 5. A process according to claim 1, in which ammonium sulfate is used for selective precipitation of proteins. 6. A process according to claim 1, in which heparan decomplexation is carried out with sodium, potassium or calcium chlorides or acetates. 7. A process according to claim 1, in which nucleic acids are selectively removed by precipitation as calcium or zinc salts. 8. A process according to claim 1, in which heparan sulfate is purified on macroporous basic resins of the kind Lewatit . MP 500A-, Amberlite IRA 904 o Amberlite IRA 93 SP. 9. Pure heparan sulfate obtained according to claims 1 to 8, which heparan sulfate has the following character¬ istics: 70° >_ d V = - +70° on dry matter Sulfate to carboxy groups ratio: -SO / COO :-- ■ -: 1; N-sulfatation abundance= N-Sθ7/(N-SO~ ' + N-Ac) -≤. 0.5 osugar: 2-0-sulfated iduronic acid abundance = C -OSO ~ /Total uronic acids ----: 0.2; Average Molecular Weight~ 20 Kd; Anti-factor Xa activity -≤k 3 U/mg; Anticoagulant activity = 0 U.I./ mg. Absent. Antithrombotic activity higher or equal to that of heparin in all the studied experimental patterns. 10. Pharmaceutical compositions for oral, parenteral and topical administration, containing heparan sulfate obtained according to claims 1 to 9.

Inventors: BIANCHINI PIETRO, MASCELLANI GIUSEPPE, BIANCHINI, PIETRO, MASCELLANI, GIUSEPPE
Applicants: OPOCRIN SPA, OPOCRIN S.P.A. LABORATORIO FARMACOBIOLOGICO
Application year: 1988
Main classification: C08B37
IPC codes: C08B37