WO2008006925A2 - Process for depolymerisation of heparin using glycidol molecules - Google Patents

Process for depolymerisation of heparin using glycidol molecules Download PDF

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WO2008006925A2
WO2008006925A2 PCT/ES2007/000423 ES2007000423W WO2008006925A2 WO 2008006925 A2 WO2008006925 A2 WO 2008006925A2 ES 2007000423 W ES2007000423 W ES 2007000423W WO 2008006925 A2 WO2008006925 A2 WO 2008006925A2
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heparin
glycidol
per gram
hours
molecules
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PCT/ES2007/000423
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French (fr)
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WO2008006925A3 (en
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Jean Sarkis Mardiguian
Ochoa Maria Teresa Gomez
Gregorio Roncero Andres
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Laboratorios Farmaceuticos Rovi S. A.
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Publication of WO2008006925A3 publication Critical patent/WO2008006925A3/en

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    • 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
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61PSPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P7/00Drugs for disorders of the blood or the extracellular fluid
    • A61P7/02Antithrombotic agents; Anticoagulants; Platelet aggregation inhibitors

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  • the present invention falls within the field of biochemistry.
  • the present invention relates to a new method of depolymerization of heparin.
  • the present invention thus provides a new simple and economical process that poses an alternative to the known methods of depolymerization of heparins.
  • Heparin is a mucopolysaccharide that is composed of polymers of alternating derivatives of D-glucosamine (N-sulfated or N-acetylated) and uric acids (L-iduronic or D-glucuronic acids), linked by glycosidic bonds, in varying proportions. Heparin has, among other properties, the prolongation of blood clotting time, mainly through the formation of an intermediate compound with plasma antithrombin. This enhances thrombin inactivation and inhibits other proteases that act in the coagulation process such as Activated Factor X. The limiting step in the cascade reaction is the activation of Factor X, which is involved in the extrinsic and intrinsic pathways.
  • Heparin in combination with Antithrombin III inhibit thrombosis by deactivating Factor X and inhibiting the conversion of prothrombin to thrombin. This bases its use in prophylaxis with Heparin in small doses. Once the active thrombosis has developed, larger amounts of Heparin can inhibit new coagulations by inactivating the thrombin by preventing the conversion of fibrinogen to fibrin. In combination with Antithrombin III, Heparin inactivates Factors IXa, Xa, XIa, XIIa and thrombin, inhibiting the transformation of fibrinogen to fibrin.
  • Heparin also prevents the formation of a stable fibrin clot by inhibiting the activation of Factor XIII (the fibrin stabilizing factor). Heparin surprisingly inhibits the reactions that lead to coagulation, but does not significantly alter the levels of coagulation factors in the blood. Heparin has no fibrinolytic activity; It does not cause lysis of existing clots, but it can prevent the spread of existing clots. Heparin also increases the release of lipoprotein lipases, which eliminates circulating lipids from the plasma, increases the amount of circulating free fatty acids and reduces lipoprotein levels.
  • Factor XIII the fibrin stabilizing factor
  • heparin is a sulfated mucopolysaccharide formed by units of uronic acid (U) (D-glucuronic or L-iduronic) alternated with units (Gl) of D-glucosamine, as shown by the compound of formula general I:
  • the uronic acid (U) is normally 2-sulfated and the glucosamine (Gl) can be N-sulfated or 6-sulfated, but also N-acetylated or 3-sulfated.
  • Heparin is used in the form of sodium salt (sodium heparin), but it can also be in the form of calcium salt (calcium heparin) or magnesium.
  • the depolymerization of heparin can be carried out enzymatically by heparinases [FR20020011724; WO1996US15593; US19950004622P] or chemical route [RU19970117697; JP19830159102; JP19810046288; JP19800051602; JP19760159896; JP19800051601] either for structure studies or to prepare low molecular weight heparins that are used in antithrombotic therapy.
  • the chemical depolymerization processes in aqueous medium use sodium nitrite in acidic medium or peroxides, or the alkaline treatment of the benzyl ester of heparin.
  • a benzyl ester can be treated with a base or directly a quaternary ammonium salt of heparin with a strong base.
  • the present invention provides a practical solution and an alternative to the heparin depolymerization methods employed so far.
  • a novel solution that includes the novel use of glycidol molecules for the first time in heparin depolymerization processes, a simple and substantially economical process is obtained, since being more selective entails fewer reaction steps.
  • the present invention relates to a new method of depolymerization of heparin. It is a simple and economical procedure, which consists of treating an aqueous solution of heparin with a certain amount of glycidol of at least 0.4 ml per gram of heparin, at a temperature of 40 ° C to 80 ° C, for a period of 4 to 24 hours.
  • the procedure described in the present invention comes from beta-elimination, with formation of an enopyranosyluronic moiety.
  • R H or SO 3
  • the reaction may eventually be accompanied by the formation of residues of a compound of general formula A in small amounts. However, by optimizing working conditions, this secondary reaction can be minimized, and even avoided.
  • the present invention relates to a heparin depolymerization process in which an aqueous solution of heparin of a concentration range between 10% and 40% is treated with glycidol in a proportion of at least 0, 4 ml per gram of heparin, at a temperature range of 40 ° C to 80 ° C, for a period of 4 to 24 hours.
  • the present invention relates to a heparin depolymerization process in which an aqueous solution of heparin of a concentration range between 20% and 40% is treated with an amount of glycidol in a proportion between 0 , 4 ml to 2 ml per gram of heparin, at a temperature range of 40 ° C to 50 ° C, for a period of 6 to 24 hours.
  • the present invention relates to the use of glycidol molecules to depolymerize heparin, in which glycidol is used in a proportion of at least 0.4 ml per gram of heparin.
  • the products obtained have a characteristic absorption spectrum in the ultraviolet, with a maximum of approximately 232 nm. Its average molecular weight was determined by the method of the European Pharmacopoeia (Ph. Eur. 5 Edition).
  • heparin 20 g are dissolved in 80 ml of water and 12 ml of glycidol are added. The solution is brought to 50 ° C for 24 hours. After cooling, 19.5 g of depolymerized heparin are isolated as in the previous examples.

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Abstract

The present invention relates to a simple and economic procedure for depolymerising heparin using glycidol molecules that offers an alternative to known heparin depolymerisation methods.

Description

PROCEDIMIENTO NUEVO DE DESPOLIMERIZACIÓN DE LA HEPARINA NEW PROCEDURE FOR DEPOLIMERIZATION OF HEPARINE
CAMPO DE LA INVENCIÓN:FIELD OF THE INVENTION:
La presente invención se engloba dentro del campo de Ia bioquímica. La presente invención se refiere a un nuevo procedimiento de despolimerización de heparina. La presente invención proporciona, por tanto un nuevo procedimiento sencillo y económico que plantea una alternativa a los procedimientos conocidos de despolimerización de heparinas.The present invention falls within the field of biochemistry. The present invention relates to a new method of depolymerization of heparin. The present invention thus provides a new simple and economical process that poses an alternative to the known methods of depolymerization of heparins.
ESTADO DE LA TÉCNICASTATE OF THE TECHNIQUE
La heparina es un mucopolisacárido que se compone de polímeros de derivados alternados de D-glucosamina (N-sulfatados o N-acetilados) y ácidos uránicos (ácidos L- idurónico o D-glucurónico), unidos por enlaces glicosídicos, en proporciones variables. La heparina tiene, entre otras propiedades, Ia de prolongar el tiempo de coagulación de Ia sangre, principalmente a través de Ia formación de un compuesto intermedio con Ia Antitrombina del plasma. Esto potencia Ia inactivación de Trombina e inhibe otras proteasas que actúan en el proceso de coagulación tal como el Factor X Activado. El paso limitante en Ia reacción en cascada es Ia activación del Factor X, que está involucrado en las vías extrínseca e intrínseca. Pequeñas cantidades de Heparina en combinación con Antitrombina III inhiben Ia trombosis al desactivar el Factor X e inhibir Ia conversión de protrombina a trombina. Esto fundamenta su uso en Ia profilaxis con Heparina en dosis pequeñas. Una vez que Ia trombosis activa se ha desarrollado, cantidades mayores de Heparina pueden inhibir nuevas coagulaciones al inactivar Ia trombina previniendo Ia conversión de fibrinógeno en fibrina. En combinación con Antitrombina III, Heparina inactiva los Factores IXa, Xa, XIa, XIIa y Ia trombina, inhibiendo Ia transformación de fibrinógeno a fibrina. La heparina también previene Ia formación de un coágulo estable de fibrina al inhibir Ia activación del Factor XIII (el factor estabilizante de fibrina). La heparina, sorprendentemente inhibe las reacciones que llevan a Ia coagulación, pero no altera significativamente los niveles de los factores de coagulación en Ia sangre. La heparina no tiene actividad fibrinolítica; no causa lisis de los coágulos existentes, pero puede prevenir Ia extensión de coágulos existentes. La heparina también incrementa Ia liberación de lipoproteinlipasas, que elimina lípidos circulantes del plasma, incrementa Ia cantidad de ácidos grasos libres circulantes y reduce los niveles de lipoproteína. De acuerdo con su estructura molecular, Ia heparina es un mucopolisacárido sulfatado formado por unidades de ácido urónico (U) (D- glucurónico o L-idurónico) alternado con unidades (Gl) de D-glucosamina, tal y como muestra el compuesto de fórmula general I:Heparin is a mucopolysaccharide that is composed of polymers of alternating derivatives of D-glucosamine (N-sulfated or N-acetylated) and uric acids (L-iduronic or D-glucuronic acids), linked by glycosidic bonds, in varying proportions. Heparin has, among other properties, the prolongation of blood clotting time, mainly through the formation of an intermediate compound with plasma antithrombin. This enhances thrombin inactivation and inhibits other proteases that act in the coagulation process such as Activated Factor X. The limiting step in the cascade reaction is the activation of Factor X, which is involved in the extrinsic and intrinsic pathways. Small amounts of Heparin in combination with Antithrombin III inhibit thrombosis by deactivating Factor X and inhibiting the conversion of prothrombin to thrombin. This bases its use in prophylaxis with Heparin in small doses. Once the active thrombosis has developed, larger amounts of Heparin can inhibit new coagulations by inactivating the thrombin by preventing the conversion of fibrinogen to fibrin. In combination with Antithrombin III, Heparin inactivates Factors IXa, Xa, XIa, XIIa and thrombin, inhibiting the transformation of fibrinogen to fibrin. Heparin also prevents the formation of a stable fibrin clot by inhibiting the activation of Factor XIII (the fibrin stabilizing factor). Heparin surprisingly inhibits the reactions that lead to coagulation, but does not significantly alter the levels of coagulation factors in the blood. Heparin has no fibrinolytic activity; It does not cause lysis of existing clots, but it can prevent the spread of existing clots. Heparin also increases the release of lipoprotein lipases, which eliminates circulating lipids from the plasma, increases the amount of circulating free fatty acids and reduces lipoprotein levels. According to its molecular structure, heparin is a sulfated mucopolysaccharide formed by units of uronic acid (U) (D-glucuronic or L-iduronic) alternated with units (Gl) of D-glucosamine, as shown by the compound of formula general I:
U - Gl - U - Gl - UU - Gl - U - Gl - U
Compuesto de fómula general ICompound of general formula I
El ácido urónico (U) normalmente está 2-sulfatado y Ia glucosamina (Gl) puede estar N-sulfatada o 6-sulfatada, pero también N-acetilada o 3-sulfatada.The uronic acid (U) is normally 2-sulfated and the glucosamine (Gl) can be N-sulfated or 6-sulfated, but also N-acetylated or 3-sulfated.
La heparina se usa en forma de sal de sodio (heparina sódica), pero también puede estar en forma de sal de calcio (heparina calcica) o de magnesio.Heparin is used in the form of sodium salt (sodium heparin), but it can also be in the form of calcium salt (calcium heparin) or magnesium.
La despolimerización de Ia heparina se puede realizar vía enzimática mediante heparinasas [FR20020011724; WO1996US15593; US19950004622P] o vía química [RU19970117697; JP19830159102; JP19810046288; JP19800051602; JP19760159896; JP19800051601] ya sea para los estudios de estructura o bien sea para preparar heparinas de bajo peso molecular que se usan en Ia terapia antitrombótica. Los procedimientos de despolimerización por vía química en medio acuoso usan nitrito sódico en medio ácido o peróxidos, o el tratamiento alcalino del éster bencílico de Ia heparina. En medio no acuoso se puede tratar un éster bencílico con una base o directamente una sal de amonio cuaternario de heparina con una base fuerte.The depolymerization of heparin can be carried out enzymatically by heparinases [FR20020011724; WO1996US15593; US19950004622P] or chemical route [RU19970117697; JP19830159102; JP19810046288; JP19800051602; JP19760159896; JP19800051601] either for structure studies or to prepare low molecular weight heparins that are used in antithrombotic therapy. The chemical depolymerization processes in aqueous medium use sodium nitrite in acidic medium or peroxides, or the alkaline treatment of the benzyl ester of heparin. In a non-aqueous medium, a benzyl ester can be treated with a base or directly a quaternary ammonium salt of heparin with a strong base.
Durante el curso de los últimos años, se han utilizado diferentes métodos químicos para despolimerizar Ia heparina, tales como:During the course of recent years, different chemical methods have been used to depolymerize heparin, such as:
- tratamiento con nitrito de sodio en medio ácido - tratamiento alcalino de esteres uso de radicales libres generados en presencia de peróxido de hidrógeno- treatment with sodium nitrite in acid medium - alkaline treatment of esters use of free radicals generated in the presence of hydrogen peroxide
- tratamiento de una sal de amonio cuaternario de heparina en medio no acuoso con una base fuerte de acuerdo a un mecanismo de beta- eliminación, etc. Estos métodos permiten obtener, con rendimientos variables, mezclas de fragmentos de heparina en las cuales el peso molecular promedio y Ia actividad anticoagulante varía de acuerdo al procedimiento y a las condiciones de operación [E99500184; P9901671; P8700020].- treatment of a quaternary ammonium salt of heparin in a non-aqueous medium with a strong base according to a beta-elimination mechanism, etc. These methods allow, with variable yields, to obtain mixtures of heparin fragments in which the average molecular weight and the anticoagulant activity varies according to the procedure and the operating conditions [E99500184; P9901671; P8700020].
En el estado de Ia técnica existe también un método selectivo y específico de despolimerización de heparina, protegido por el titular de Ia presente invención, que se realiza en un medio no acuoso con una base fuerte. El proceso comienza sometiendo a Ia heparina no fraccionada al tratamiento con amonio cuaternario. Así se forma una sal de heparina que protege particularmente los grupos claves de Ia molécula de HNF. A continuación se despolimeriza y fracciona Ia cadena por los lugares no protegidos, obteniéndose hasta un 75% de fragmentos homogéneos, de peso molecular comprendido entre los 2.000 y 6.000 daltons. Tras Ia despolimerización controlada se procede al proceso de purificación y liofilización, con el que se obtienen distintas Heparinas de Bajo Peso Molecular, entre ellas Bemiparina, HBPM de 2a generación, de 3.600 daltons de PM medio [P9901671].In the state of the art there is also a selective and specific method of depolymerization of heparin, protected by the holder of the present invention, which is carried out in a non-aqueous medium with a strong base. The process begins by subjecting the unfractionated heparin to the quaternary ammonium treatment. Thus, a heparin salt is formed that particularly protects the key groups of the HNF molecule. The chain is then depolymerized and fractionated by unprotected sites, obtaining up to 75% of homogeneous fragments, of molecular weight between 2,000 and 6,000 daltons. After the controlled depolymerization process proceeds to purification and freeze drying with which different LMWH Weight including Bemiparina LMWH 2 to generation 3,600 daltons medium PM [P9901671] are obtained.
DESCRIPCIÓN DE LA INVENCIÓNDESCRIPTION OF THE INVENTION
Normalmente todos estos procedimientos tienen una serie de desventajas e implican varias etapas entre las que destaca una etapa adicional de purificación final delicada. Además, estos procedimientos necesitan un control estricto de las condiciones de trabajo.Normally all these procedures have a number of disadvantages and involve several stages, among which an additional stage of delicate final purification stands out. In addition, these procedures need strict control of working conditions.
La presente invención proporciona una solución práctica y una alternativa a los métodos de despolimerización de heparina empleados hasta el momento. Mediante una solución novedosa que incluye Ia utilización novedosa de moléculas de glicidol por primera vez en procesos de despolimerización de heparina, se obtiene un procedimiento sencillo y sustancialmente económico, ya que al ser más selectivo conlleva menos etapas de reacción.The present invention provides a practical solution and an alternative to the heparin depolymerization methods employed so far. By means of a novel solution that includes the novel use of glycidol molecules for the first time in heparin depolymerization processes, a simple and substantially economical process is obtained, since being more selective entails fewer reaction steps.
La presente invención se refiere a un nuevo procedimiento de despolimerización de Ia heparina. Se trata de un procedimiento sencillo y económico, que consiste en tratar una solución acuosa de heparina con una cantidad determinada de glicidol de al menos 0,4 mi por gramo de heparina, a una temperatura de 40° C a 80° C, durante un periodo de 4 a 24 horas.The present invention relates to a new method of depolymerization of heparin. It is a simple and economical procedure, which consists of treating an aqueous solution of heparin with a certain amount of glycidol of at least 0.4 ml per gram of heparin, at a temperature of 40 ° C to 80 ° C, for a period of 4 to 24 hours.
CH2 — CH — CH2OHCH 2 - CH - CH 2 OH
GlicidolGlycidol
De este modo se consigue aislar los productos formados, por precipitación o por cualquier otro procedimiento del estado de Ia técnica.In this way it is possible to isolate the products formed, by precipitation or by any other procedure of the state of the art.
El procedimiento descrito en Ia presente invención procede de una beta- eliminación, con formación de un resto enopiranosilurónico.The procedure described in the present invention comes from beta-elimination, with formation of an enopyranosyluronic moiety.
Figure imgf000005_0001
Figure imgf000005_0001
R= H o SO3 R = H or SO 3
Resto enopiranosilurónicoEnopyranosyluronic rest
La reacción eventualmente puede venir acompañada de Ia formación de restos de un compuesto de fórmula general A en pequeñas cantidades. No obstante, optimizando las condiciones de trabajo, se puede minimizar esta reacción secundaria, e incluso evitarla.The reaction may eventually be accompanied by the formation of residues of a compound of general formula A in small amounts. However, by optimizing working conditions, this secondary reaction can be minimized, and even avoided.
— O— CH2 — CH-CH2OH- O— CH 2 - CH-CH 2 OH
OHOH
Restos de fórmula general A También se puede limitar el ataque del glicidol al sitio de unión a Ia antitrombina de Ia heparina, que es responsable de su actividad anticoagulante, trabajando con una solución concentrada de heparina, a 40-50° C.Remains of general formula A It is also possible to limit the attack of glycidol to the antithrombin binding site of heparin, which is responsible for its anticoagulant activity, working with a concentrated solution of heparin, at 40-50 ° C.
De forma más general, se pueden usar otras moléculas definidas por Ia fórmula general B, pero parece que el glicidol es el más reactivo.More generally, other molecules defined by the general formula B can be used, but it seems that glycidol is the most reactive.
CH2 — CH — CH2 — RCH 2 - CH - CH 2 - R
\/\ /
Restos de fórmula general BRemains of general formula B
De acuerdo con un primer aspecto, Ia presente invención se refiere a un procedimiento de despolimerización de heparina en el que se trata una solución acuosa de heparina de un intervalo de concentración entre 10% y 40% con glicidol en una proporción de al menos 0,4 mi por gramo de heparina, a un intervalo de temperatura de 40° C a 80° C, durante un periodo de 4 a 24 horas.In accordance with a first aspect, the present invention relates to a heparin depolymerization process in which an aqueous solution of heparin of a concentration range between 10% and 40% is treated with glycidol in a proportion of at least 0, 4 ml per gram of heparin, at a temperature range of 40 ° C to 80 ° C, for a period of 4 to 24 hours.
De acuerdo con otro aspecto importante, Ia presente invención se refiere a un procedimiento de despolimerización de heparina en el que se trata una solución acuosa de heparina de un intervalo de concentración entre 20% y 40% con una cantidad de glicidol en una proporción entre 0,4 mi a 2 mi por gramo de heparina, a un intervalo de temperatura de 40° C a 50° C, durante un periodo de 6 a 24 horas.According to another important aspect, the present invention relates to a heparin depolymerization process in which an aqueous solution of heparin of a concentration range between 20% and 40% is treated with an amount of glycidol in a proportion between 0 , 4 ml to 2 ml per gram of heparin, at a temperature range of 40 ° C to 50 ° C, for a period of 6 to 24 hours.
Según un segundo aspecto importante, Ia presente invención se refiere al uso de moléculas de glicidol para despolimerizar heparina, en el que el glicidol se utiliza en una proporción de al menos 0,4 mi por gramo de heparina. EJEMPLOS DE REALIZACIÓN:According to a second important aspect, the present invention relates to the use of glycidol molecules to depolymerize heparin, in which glycidol is used in a proportion of at least 0.4 ml per gram of heparin. EXAMPLES OF REALIZATION:
Los siguientes ejemplos específicos que se proporcionan en este documento de patente sirven para ilustrar Ia naturaleza de Ia presente invención. Estos ejemplos se incluyen solamente con fines ilustrativos y no han de ser interpretados como limitaciones a Ia invención que aquí se reivindica. Por tanto, los ejemplos descritos más adelante ilustran Ia invención sin limitar el campo de aplicación de Ia misma. Los productos descritos se han obtenido a partir de heparina de origen porcino (ejemplos 3 y 4) o bovino (ejemplos 1 y 2) de calidad farmacéutica. Se han aislado por precipitación en alcohol, por adición de metanol a Ia solución acuosa que contiene cloruro sódico al 10%, y después filtración del precipitado y secado.The following specific examples provided in this patent document serve to illustrate the nature of the present invention. These examples are included for illustrative purposes only and should not be construed as limitations to the invention claimed herein. Therefore, the examples described below illustrate the invention without limiting its scope of application. The products described have been obtained from heparin of porcine origin (examples 3 and 4) or bovine (examples 1 and 2) of pharmaceutical quality. They have been isolated by precipitation in alcohol, by adding methanol to the aqueous solution containing 10% sodium chloride, and then filtration of the precipitate and drying.
Los productos obtenidos presentan un espectro de absorción característico en el ultravioleta, con un máximo aproximadamente a 232 nm. Su masa molecular media se ha determinado por el procedimiento de Ia Farmacopea Europea (Ph. Eur. 5a Edición).The products obtained have a characteristic absorption spectrum in the ultraviolet, with a maximum of approximately 232 nm. Its average molecular weight was determined by the method of the European Pharmacopoeia (Ph. Eur. 5 Edition).
Se ha medido su actividad antifactor Xa según un método cromogénico (Ph. Eur. 5a Its anti-factor Xa activity has been measured according to a chromogenic method (Ph. Eur. 5 a
Edición) y se ha expresado en unidades internacionales por mg.Edition) and has been expressed in international units per mg.
Ejemplo 1Example 1
Se disuelven 20 g de heparina en 80 mi de agua, después se añaden 24 mi de glicidol, se lleva Ia solución a 50° C durante 24 horas y después se enfría y se deja que vuelva a Ia temperatura ambiente, y mediante Ia precipitación en alcohol habitual se aislan 13,2 g de heparina despolimerizada.20 g of heparin are dissolved in 80 ml of water, then 24 ml of glycidol are added, the solution is brought to 50 ° C for 24 hours and then cooled and allowed to return to room temperature, and by precipitation in Usual alcohol is isolated 13.2 g of depolymerized heparin.
Ejemplo 2Example 2
Se disuelven 5 g de heparina en 20 mi de agua, se añaden 6 mi de glicidol y se lleva Ia solución a 40° C durante 24 horas. Después de enfriar y devolver a Ia temperatura ambiente, mediante Ia precipitación en alcohol se obtienen 4 g de heparina despolimerizada. Ejemplo 35 g of heparin are dissolved in 20 ml of water, 6 ml of glycidol are added and the solution is brought to 40 ° C for 24 hours. After cooling and returning to room temperature, by precipitation in alcohol, 4 g of depolymerized heparin are obtained. Example 3
Se disuelven 20 g de heparina en 80 mi de agua y se añaden 12 mi de glicidol. La solución se lleva a 50° C durante 24 horas. Después de enfriar se aislan como en los ejemplos anteriores 19,5 g de heparina despolimerizada.20 g of heparin are dissolved in 80 ml of water and 12 ml of glycidol are added. The solution is brought to 50 ° C for 24 hours. After cooling, 19.5 g of depolymerized heparin are isolated as in the previous examples.
Ejemplo 4Example 4
Se disuelven 10 g de heparina en 40 mi de agua y se añaden 12 mi de glicidol. La solución se lleva a 50° C durante 4 horas y después se enfría hasta temperatura ambiente. Se obtienen 8,9 g de heparina despolimerizada.10 g of heparin are dissolved in 40 ml of water and 12 ml of glycidol are added. The solution is brought to 50 ° C for 4 hours and then cooled to room temperature. 8.9 g of depolymerized heparin are obtained.
Características de los productos descritos (ver figura 1 ):Characteristics of the products described (see figure 1):
PM (1) Actividad (2) Espectro UV (3)PM (1) Activity (2) UV spectrum (3)
Ejemplo 1 2757 60 máx. a 232 nmExample 1 2757 60 max. at 232 nm
Ejemplo 2 3594 65 máx. a 232 nmExample 2 3594 65 max. at 232 nm
Ejemplo 3 4427 73 máx. a 232 nmExample 3 4427 73 max. at 232 nm
Ejemplo 4 5467 83 máx. a 232 nmExample 4 5467 83 max. at 232 nm
(1) masa molecular media (daltons)(1) average molecular mass (daltons)
(2) actividad anti-Xa (Ul/mg)(2) anti-Xa activity (Ul / mg)
(3) espectro UV en HCI 0,01 N (3) UV spectrum in 0.01 N HCI

Claims

REIVINDICACIONES
1. Procedimiento de despolimerización de heparina caracterizado porque se trata una solución acuosa de heparina de un intervalo de concentración entre 10% y1. Heparin depolymerization process characterized in that an aqueous solution of heparin of a concentration range between 10% and
40% con glicidol en una proporción de al menos 0,4 mi por gramo de heparina, a un intervalo de temperatura de 40° C a 80° C, durante un periodo de 4 a 24 horas.40% with glycidol at a rate of at least 0.4 ml per gram of heparin, at a temperature range of 40 ° C to 80 ° C, for a period of 4 to 24 hours.
2. Procedimiento de despolimerización de heparina según Ia reivindicación 1 , caracterizado porque se trata una solución acuosa de heparina de un intervalo de concentración entre 20% y 40% con una cantidad de glicidol en una proporción menor o igual a 2 mi por gramo de heparina, a un intervalo de temperatura de 40° C a 50° C1 durante un periodo de 6 a 24 horas.2. Heparin depolymerization process according to claim 1, characterized in that an aqueous solution of heparin of a concentration range between 20% and 40% is treated with an amount of glycidol in a proportion less than or equal to 2 ml per gram of heparin at a temperature range of 40 ° C to 50 ° C for a period of 1 6 to 24 hours.
3. Procedimiento de despolimerización de heparina según Ia reivindicación 2, caracterizado porque Ia heparina tratada es heparina sódica.3. Heparin depolymerization process according to claim 2, characterized in that the heparin treated is sodium heparin.
4. Procedimiento según Ia reivindicación 1 , en el que Ia heparina está en forma de sal de calcio o de magnesio.4. Method according to claim 1, wherein the heparin is in the form of calcium or magnesium salt.
5. Procedimiento de despolimerización de heparina según cualquiera de las reivindicaciones 2 y 3 caracterizado porque Ia estructura de los oligosacáridos obtenidos tiene un resto enopiranosilurónico y una actividad anti-factor Xa residual superior a 40 Ul/mg.5. Heparin depolymerization process according to any of claims 2 and 3 characterized in that the structure of the oligosaccharides obtained has an enopyranosyluronic moiety and a residual anti-factor Xa activity greater than 40 Ul / mg.
6. Uso de moléculas de glicidol para despolimerizar heparina.6. Use of glycidol molecules to depolymerize heparin.
7. Uso de moléculas de glicidol para despolimerizar heparina según reivindicación 6, en una proporción de al menos 0,4 mi por gramo de heparina. 7. Use of glycidol molecules to depolymerize heparin according to claim 6, in a proportion of at least 0.4 ml per gram of heparin.
PCT/ES2007/000423 2006-07-14 2007-07-13 Process for depolymerisation of heparin using glycidol molecules WO2008006925A2 (en)

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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2960498A (en) * 1956-04-02 1960-11-15 Burke Oliver W Jun Partial glycerol esters of pectic substances and preparation thereof
EP0544592A2 (en) * 1991-11-28 1993-06-02 Sanofi High molecular weight N,O-sulfated heparosans, process for producing the same and pharmaceutical compositions containing them
WO1995019176A1 (en) * 1994-01-12 1995-07-20 Glycomed Incorporated Non-anticoagulant chemically modified heparinoids for treating hypovolemic shock and related shock syndromes

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4351938A (en) * 1980-05-19 1982-09-28 Riker Laboratories, Inc. Anticoagulant substance

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2960498A (en) * 1956-04-02 1960-11-15 Burke Oliver W Jun Partial glycerol esters of pectic substances and preparation thereof
EP0544592A2 (en) * 1991-11-28 1993-06-02 Sanofi High molecular weight N,O-sulfated heparosans, process for producing the same and pharmaceutical compositions containing them
WO1995019176A1 (en) * 1994-01-12 1995-07-20 Glycomed Incorporated Non-anticoagulant chemically modified heparinoids for treating hypovolemic shock and related shock syndromes

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