"BIOSTABILΠΎ OF POLYMERIC STRUCTURES"
This invention relates to biostable biocompatible polymeric structures suitable for long term implantation within a living human body and as a suitable substratum for cell growth technologies.
Background of the Invention
Extensive investigations have been undertaken over many years to find materials that will be biologically and chemically stable towards body fluids and body tissue. This area of research has become increasingly important with the development of various objects and articles which can be implanted into a living body, such as pacemaker leads, vascular grafts, mammary prostheses, pacemaker bodies, probes, catheters and the like. Polyurethanes have become crucial to many of these devices .
Flexible polyurethane foams have been manufactured for more than thirty years from polyisocyanates and polymeric polyols. They have been used in the production of elastomers, flexible and rigid foams, coatings, adhesives and many other products in the industrial sector. The most commonly used polyisocyanate has been TDI (Toluene Diisocyanate) but in recent years this has been replaced with MDI (Diphenylmethane Diisocyanates). Isocyanate polyurethane prepolymers obtained by reacting a stoichiometric excess of a polyisocyanate with an organic polyol are well known in the field of polyurethanes.
The production of foamed materials based on polyurethane and other polymer systems derived from organic polysiloxanes in industrial applications is also well established. The formulation and processing conditions used during manufacture affects the properties of the foam product. They can vary in texture from soft flexible foams used in cushioning applications to hard rigid materials used as
insulating or structural materials. The density and strength of the material can also be affected by the formulation.
While there are some polymeric materials available for use in medical implant technologies there is a need for an improved technology for producing polymeric materials with enhanced biostability and biocompatibility.
Statements of Invention
According to the invention there is provided a method for manufacturing a biostable biocompatible polymeric material comprising the step of forming a three dimensional cross linked structure of the polymeric material and treating the structure to remove impurities.
In a particularly preferred embodiment of the invention the structure is treated by solvent extraction.
Ideally the solubility parameter of the solvent extraction system is selected for compatibility with the solubility parameter of the polymeric material or its phases. Preferably the solubility parameter of the solvent extraction system is within ± 8
MPa Λ of the solubility parameter of the polymer or its phases.
In a preferred embodiment of the invention the method includes the step of removing residual solvent from the structure, after solvent extraction. Preferably residual solvent is removed by treatment with water.
The biostable biocompatible material may for example be a polyether polyurethane or a polycarbonate urethane or polycarbonate urethane urea or a polydimethylsiloxane urethane urea.
In one case the material is in the form of a medical implant. The implant may be a septal defect occluder, a vessel occluder, a vessel defect occluder, a mammary prosthesis, a muscle bulking agent, a gynecological implant or an embolic filter.
The material may be in the form of a substratum for tissue and/ or cell growth.
Ideally the material forms a cell matrix for cell growth technologies, tissue repair and in drug delivery applications.
In the case of a biostable polyether polyurethane article the article may be formed from an organic diisocyanate, a polyether polyol, a chain extender and a blowing agent.
The blowing agent is preferably water.
The density of the article is preferably less than 1200kg/m3, ideally less than 200kg/m3.
The ratios of the reaction components are selected to promote the formation of a three dimensional porous molecular structure of polyether urethane biomaterial.
The article may be processed by a metering and mixing process, wherein the chemical components are aggressively mixed and dispensed into a vessel and chain extension and blowing reactions occur substantially simultaneously.
Typically the article is processed by a reactive moulding process, wherein the chemical components are mixed and dispensed into a vessel wherein chain extension occurs.
The article may be processed in two stages, a first stage involving a reaction process in which the number of isocyanate linkages in the reaction vessel is approximately equal to the number of active hydrogens in the vessel.
The article may also be processed by a reactive blowing process, in which the chemical components are aggressively mixed and dispensed substantially continuously and expand and chain extend substantially simultaneously to form a continuous block of foam which is subsequently cut or machined into a desired geometry.
The density of the article is preferably controlled by controlling the pressure in the reaction vessel.
Preferably the biostable polyether polyurethane article has a pore size of from 10 microns to 900 microns. Ideally the biostable polyether polyurethane article according to claim 25 having a pore size of between 35 microns to 200 microns.
In one aspect the invention provides a biostable polyether polyurethane wherein the urea linkages are derived from a water isocyanate reaction present in the hard segment phase. Preferably the percentage of urea linkages in the hard segment phase is greater than 0.5%.
In another aspect the invention provides a biostable polyether polyurethane wherein biuret linkages exist in the hard segment phase.
In a further aspect the invention provides a biostable polyether polyurethane wherein aliphatic linkages exist in the hard segment phase.
Further details of the invention are set out in claims 31 to 53.
Detailed Description
The biostable polyurethane devices of this invention are derived from organic diisocyanates and polyether polyols, polyether copolymer polyols or combinations thereof and are chain extended with either diamine, diol, water or mixtures of the above chain extenders. The reaction step converts the chemical precursors into a 3 dimensional molecular cross-linked structure, simultaneously forming a low density porous material. A 3 dimensional network of this kind is insoluble and intractable. Manufacturing the article by this method produces a material with minimal internal stress, enhancing biostability.
The fact that the polyether biomaterial is a three dimensional structure at a molecular level allows it to be processed aggressively to remove residual chemicals from the process. Low molecular weight chemicals have the potential to leach from the article and result in toxic reactions in living cells. The downstream processing of the article expands the biomaterials volume at a molecular level. This expansion aids in the removal of leachables such as catalyts, oligomers and free monomers. The solvent extraction process also reduces any internal stresses within the material. The solvent expands the material when it penetrates between the molecular chains. The 3-dimensional cross links provides the materials with molecular memory and prevents the molecular structure being soluble in the solvent. However, the molecular chains in this state can orient themselves into a preferred relaxed conformation, thereby relieving the material of any internal stresses.
This process enhances the material biocompatible for use as an implantable medical device or as a 3 dimensional matrix for use as a cell scaffold in tissue engineering applications. Altering the chemical precursors and the processing conditions of the material may alter the pore size and the density of the material, as required, to meet the requirements of the application.
The biostable polyurethanes of this invention are useful for the manufacture of catheters, vascular grafts, septal occluders, vessel occluders, embolisation devices, mammary prosthesis, pacemaker leads and other such implant, blood contacting devices and as cell scaffolds to support cell growth.
The biostable polyurethanes of this invention are based on organic diisocyanates, polyether copolymer polyols, polyether homopolymers and diol, diamine or water chain extenders and combinations thereof.
The product of this invention has applications in the medical device and tissue engineering sectors, however the material can also be used as a cell scaffold to support cell growth.
This material is suitable for these applications since it was designed such that an aggressive solvent extraction process can be applied to remove potential leachables from the material. Typically it is these leachables that are responsible for cytotoxic responses to polyurethane materials. The solvent extraction system detailed in this invention allows the use of solvents with a solubility parameter similar to that of the polymer, allowing the polymer to swell and the leachables to be removed by the solvent from the material.
Linear polymer systems cannot be subjected to such an aggressive solvent extraction since the use of a solvent with a similar solubility parameter will cause both the polymer and it's leachables to dissolve. It is the 3 dimensional structure of the biomaterial of this invention that permits the use of a solvent of a similar solubility parameter since the 3 dimensional structure of the material gives it inherent molecular memory allowing it to return to it's original configuration.
Swelling the 3 dimensional polymer with similar solvents opens up the structure and allows extraction of chemical species impossible to extract in linear systems by conventional dissimilar solvents.
To manufacture and process linear polymers into required geometries, normally requires the use of additives and catalysts, which cannot be removed completely by conventional solvent extraction. The 3 dimensional material , detailed in this invention can be laser machined into the required geometries.
Details on the chemistry of the invention are as follows;
The organic diisocyanates are of the general formula: R-(NCO)n
R is an aliphatic, aromatic, cycloaliphatic, or an aliphatic-aromatic hydrocarbon entity containing between 4 and 24 carbon atoms and "n" varies between 1.85 and 3. More preferably, R contains between 4 and 13 carbon atoms. Where n is 2, a polymer with a linear molecular structure may be produced. A three dimensional molecular network may be produced where n varies from 1.85 to 3. Ideally n should be between 1.9 and 2.2.
Examples of suitable isocyanates include: p-phenylene diisocyanate, tetramethylene diisocyanate, cyclohexane 1, 2-diisocyanate, m-tetramethylxylene diisocyanate, hexamethylene diisocyanate, 2,4 diphenylmethane diisocyanate, 4,4 diphenylmethane diisocyanate, 2,4 toluene diisocyanate, 2, 6 toluene diisocyanate, cyclohexane 1,4 diisocyanate, isophorone diisocyanate, 4,4 - dicyclohexylmethane diisocyanate, 4,4 -dicyclohexylmethane diisocyanate, and mixtures of the above.
More ideally the following isocyanates can be used to manufacture suitable materials; 2,4 diphenylmethane diisocyanate, 4,4 diphenylmethane diisocyanate, 2,4 toluene diisocyanate, 2, 6 toluene diisocyanate, cyclohexane 1,4 diisocyanate, isophorone diisocyanate, 4,4 -dicyclohexylmethane diisocyanate, and mixtures of the above.
Even more ideally, the following diisocyanates can be used to manufacture suitable polyurethanes: 2,4 diphenylmethane diisocyanate, 4,4 diphenylmethane diisocyanate, 4,4 -dicyclohexylmethane diisocyanate.
Polyether polyols that may be used include products obtained by the polymerisation of cyclic oxide, for example, ethylene oxide, propylene oxide, butylene oxide, or tetrahydrofuran in the presence of polyfunctional initiators. Suitable initiator compounds contain plurality of active hydrogen atoms including water and polyols, e.g., ethylene glycol, propylene glycol, diethylene glycol, resorcinol, bisphenol A, cyclohexane dimethanol, gylcerol, trimethylolpropane,
1,2,6, - heaxanetriol or pentaerythriol.
Useful polyether polyols include polytetramethylene glycols obtained by the polymerisation of tetrahydrofuran. The polytetramethylene glycols used in this invention having varying molecular weights of between 600 and 3000. Polyols of differing molecular weights can be used together in a single formulation.
The polyether polyurethanes of this invention are based on diol, diamine, alkanolamine, water chain extenders or mixtures of these. Diol chain extenders react with isocyanate to generate urethane linkages. Diamine and water generate urea linkages and alkanol amines can generate both urethane and urea linkages. The use of water as a chain extender in low density, three dimensional biomedical polyurethanes is unusual as with most conventional biomedical polyurethanes water is viewed as an impurity. The water chain extension reactions generate urea linkages in the hard segment and carbon dioxide is given off as a by-product.
The presence of significant quantities of urea linkages in the hard segment has the following important effects:
• Polyureas in the hard segment generate significant levels of hydrogen bonding that causes the hard segment to be strong and this adds to the ultimate properties of the material.
• It also promotes phase separation of the hard isocyanate/chain extender phase and the soft polyol phase. Phase separation is beneficial to the elastomeric and biocompatibility properties of the material.
• The presence of significant concentrations of urea linkages in the hard segment make linear polyurethanes difficult to process by thermomechanical techniques.
• The carbon dioxide generated from the water isocyanate reaction series can be used to influence the density of the material by generating a cellular structure.
Polyurethanes with a high concentration of urea linkages in the hard phase tend to be strong elastomers with good flex lives.
The carbon dioxide generated as a by-product of the isocyanate-water-isocyanate reaction series can be employed to generate a cell structure in the material. With the use of a surfactant, the size and porosity of this cell structure can be controlled. The manufacturing control over the pore size of the material has important implications in the application of the article. In cell growth technology the pore sizes can be modified to accommodate cells and modify the cell to surface ratio.
The level of water used in the reaction determines the amount of carbon dioxide generated and the hard segment content of the polymer. The amount of carbon dioxide generated plays an important role in the density of the polyurethane. By this invention, the density can be controlled independently of the hard segment content by controlling the pressure of the reaction/forming chamber. Thus, biostable polyurethanes of this invention can be manufactured with densities ranging from 15kg/m3 to 1200kg/m3 virtually independent of the hard segment content. Low density articles used in medical applications are desirable since the wrapping profile of the article is reduced and the delivery device profile is minimised, giving rise to a wider range of applications.
The polymerisation of biostable polyurethanes of this invention involves the reaction of -OH groups from the polyol with -NCO groups from the diisocyanate to form urethane linkages. These chemical groups are reacted in approximately equivalent ratios for the generation of linear polymers and with slight excess for a crosslinked (three-dimensional) molecular structure.
For the generation of biostable foams, water is used as the primary chain extender. Secondary chain extenders may be employed to alter the hard segment content or to alter specific properties. Manufacturing foams of the lowest densities per this invention is carried out by a combination of a water blown reaction, in a depressurised reactive/forming vessel and the incorporation of a physical blowing agent into the formulation. Secondary chain extenders can be either diamine, diol or alkanol amine based and should have a functionality of two or greater. Diol chain extenders are preferred.
Most diols or diamines make suitable chain extenders. Examples of such chain extenders include, ethylene glycol, 1,4 butanediol, diethylene glycol, triethylene glycol, 1,2 propane diol, 1,3 propane diol, 1,5 pentane diol, ethylene diamine, 1,4 diaminobutane, 1,6 diaminohexane, 1,7 diaminoheptane, 1,8 diaminooctane, and 1,5 diaminopentane.
Depending on the specific isocyanate reactive compounds used, the use of catalysts may be preferred or not. Using polyols as isocyanate reactive compounds, it is preferred to use catalysts for urethane formation. Catalysts for polyurethane formation that may be used are compounds, which promote the reaction between isocyanate and hydroxyl groups.
Such catalysts are widely available in the marketplace and include organic and inorganic salts of bismuth, lead, tin, iron, antimony, cadmium, cobalt, aluminum, mercury, zinc, cerium, molybdenum, vanadium, copper, manganese and zirconium, as well as phosphines and tertiary amines.
Tertiary amines are an important class of catalyst in which the nitrogen atom is not directly attached to an aromatic ring. Examples of tertiary amines are: triethylamine, N,N,N',N'-tetramemylenediamine, N-N,N',N'-tetramethyl-l,3- butanediamine, bis-2-dimethylaminoethyl ether, N,N-dimethylcyclohexylamine, N,N-dimethylbenzylamine, N-methylmorpholine, N-ethylmorpholine, 1,4- diazabicyclo-[2.2.2] octane and the like.
Biostable articles of this invention can be chemically prepared via the following methods: The one shot process in which the diisocyanate, the polyol and the chain extender are mixed and reacted in one step.
The prepolymer method wherein an isocyanate-terminated prepolymer is first prepared and then the system is chain extended. An experienced person knowing the isocyanate content of the isocyanate composition and the functionality and molecular weight of the isocyanate- reactive compound, can calculate the relative amounts of reactants to be delivered to the reaction vessel in order to provide a prepolymer having any desired NCO content.
The quasiprepolymer system wherein some of the polyol is reacted with the isocyanate to generate an isocyanate terminated prepolymer in an excess of isocyanate. The remaining polyol and chain extenders are subsequently added to facilitate chain extension.
Biostable articles of this invention may be processed by any of the following techniques: • Reactive blow moulding process, wherein the chemical ingredients for this invention are fed though two or three lines to a mixing head where it is aggressively mixed and dispensed into a mould and chain extension and blowing reactions occur simultaneously. This process is suitable for the manufacture of a three dimensional molecular structure and is suited to the manufacture of low density porous and non-porous articles. The shot size
used in this invention is 0.5g to lOg producing a three dimensional low density porous foam.
• Reactive blowing process, wherein the chemical ingredients are aggressively mixed and dispensed in a continuous fashion and expand and chain extend simultaneously to form a continuous block of foam which is subsequently cut or machined into useful shapes. This process is suitable for the manufacture of a three dimensional molecular structure and is suited to the manufacture of low density porous and non-porous articles.
The biostable polyurethane of this invention is solvent extracted to enhance the biocompatibility of the polyurethane article. This process can be applied to all polyurethane materials. The material of this invention has a structure that is three dimensional and crosslinked at a molecular level. This allows for use of more aggressive solvents with similar solubility parameters without destroying the integrity of the material. The process allows any internal stresses to be relieved, enhancing bio stability.
Biocompatibility of a material in contact with bodily fluids is a primary function of two variables :
• Surface chemistry of the implant : for polyurethanes it is widely accepted that the surface that displays alternating, well phase separated hydrophobic and hydrophilic domains provides optimum biocompatibility.
• Leachables with the implant : the severity of the inflammation of the surrounding tissue is strongly dependant on the type and quantity of products which can migrate from the implant to the surrounding tissue. Leachables can be removed from the foam via solvent extraction.
Different solvents are available for carrying out this process. The solubility and hydrogen bonding parameters of the solvent will affect the suitability of the solvent. The solubility of polyurethane foams is typically in the region of 17 -28
MPaI/2. The solvent system used for the extract system should have a solubility parameter close to in the same range as the foam.
Solvent that may be used are : methylethyl ketone, tetrahydrofuran, dimethylformamide, 1,2 - dichloroethane, n-heptane, diethylether, acetonitrile, propan-2-ol, methanol and combinations of the above.
On immersion of the foam into the chosen solvent system the leachables from the polymer are drawn into the solvent if the leachables are soluble in the solvent system.
If the solubility parameter of the solvent system is close to that of the volume of the polymer will extend and allow extraction of low molecular weight species. It is important to maintain the integrity of the foam during this process. The residual solvent is removed from the structure using a water extraction step. The molecular memory allows it to return to its original configuration.
Cleaning the foam in such a manner removes all leachables and makes the foam suitable for long term implantation in the human body and as a cell scaffold to promote cell growth in tissue engineering applications.
The article may be used as a cell scaffold to provide a substratum to promote the growth of adherent cell lines. Cells may be seeded onto the material, attach to the cell scaffold and replicate in a physiologically suitable environment. The nature of the article provides a large surface: area ratio, to enable cells infiltrate the material. The nature of the 3 dimensional material also allows the diffusion of nutrients and oxygen into the media and the diffusion of waste metabolites and carbon dioxide gas to leach from the three dimensional structure of the article. The cells can also secrete proteins as determined by the genetic make up of the cell. As a result of the open cell structure of the material, cell - cell interactions can take place forming the basis of tissue formation.
This article has a number of applications in the field of cell growth/tissue engineering not limited to
• The use of the article as an implantable medical device to promote the growth of new tissues.
• The use of the article seeded with a specific cell type, implanted to promote the growth of new tissues.
• The use of the article in in vitro cell culture technologies and related applications.
It will be appreciated that the treatment of polymeric structures to remove impurities may be applied to any suitable polymeric material. In particular the invention may be applied to the polycarbonate urethane material described in or co-pending PCT application No IE 98/00091, filed November 9, 1998, the entire contents of which are incorporated herein by reference.
The invention is not limited to the embodiments hereinbefore described which may be varied in detail.