An exchange structure, for example for biomedical equipment

Abstract: The structure comprises essentially a core (2) which may comprise a strand or braid, as well as a sheath (3) surrounding the core (2) and defining the exchange surface. Preferred applications are for biomedical equipment such as blood oxygenators and blood purification equipment.

Description: Field of the Invention The invention relates to exchange structures. The invention has been developed with particular concern for its possible use, for example, in the field of biomedical equipment. In this context not only are mass-exchange structures currently utilised (such as those present in devices for the oxygenation of blood or for the purification of blood), but also heat-exchange structures (for example for the production of heat exchangers usable together with blood oxygenators). Substantially similar structures can be utilised in industrial fields for various purposes, for example, for purification processes based on a reverse osmosis mechanism. A characteristic common to almost all these structures is that they provide for the arrangement, or the flow, of at least two media (usually fluids) in at least locally facing positions so as to cause an exchange - usually of mass and/or heat - between these two media by various mechanisms. Description of the Prior Art For mass transfer or exchange structures, such as blood oxygenators, (it should however be specified that the invention is not intended to be limited in any way to this specific context or application), at least four different types of configuration have been proposed and utilised in the art, that is to say: bubble oxygenators (see for example US-A-3 915 650 and US-A-4 428 934), film oxygenators (see for example US-A-3 070 092 and the description contained in the introductory part of US-A-5 244 930), flat membrane oxygenators (see for example US-A-4 698 207), and hollow fibre oxygenators (see for example EP-A-0 292 445). Film or bubble oxygenators have numerous elements which are critical in their operation, such as - for example - the problem of eliminating the bubbles of residual gas in the oxygenated blood before it is reintroduced into the patient's blood. Membrane oxygenators pose production problems, above all as regards the orientation of the membrane, which must be preserved as far as possible during use; this requirement imposes the need for extremely complex mechanical support structures. Hollow fibre oxygenators resolve many of the problems inherent in the other structures. They have, however, the disadvantage of becoming subject, during use, to phenomena of accumulation and condensation of water vapour and organic materials (typically proteins) which cause their operating efficiency to deteriorate gradually. This happens especially since the material of the fibres, originally hydrophobic, tends gradually to become hydrophilic. In general, -also, so that they can be self-supporting without risk of collapse or rupture as a result of the pressure gradients applied to them in use, the fibres must have a wall thickness (typically of the order of 25-50 micron in the case of microporous fibres for oxygenation) which cannot be considered optimum for the exchange mechanism, which is usually improved or is made easier by smaller wall thicknesses. Considerations generally similar to those given above also apply to the other exchange structures mentioned initially, for example for blood purification equipment (operating on various principles such as dialysis, haemofiltration, haemodiafiltration etc) and/or for heat exchangers. Specifically, the present invention relates to an exchange structure according to the preamble of Claim 1, which is known, e.g. from EP-A-0 341 979. This document also discloses a core constituted by a profiled body of generally lobed form. Substantially similar arrangements are known e.g. from EP-A-0 251 729 (D2), DATABASE WPI Week 8645, Derwent Publications Ltd.; AN 86-294614 & JP-A-61 215 710 (D3) and DATABASE WPI Week 8642, Derwent Publications Ltd.; AN 86-275600 & JP-A-61 201 007 (D4). Objects and Summary of the Invention The object of the invention is therefore to provide an exchange structure which, whilst in its essential parts resembling a conventional hollow fibre exchange structure, overcomes its disadvantages, particularly those discussed above, in a radical manner. According to the present invention, this object is achieved by an exchange structure having the further characteristics specifically set out in the following Claim 1. Detailed Description of the Invention The invention will now be described, purely by way of non-limitative example, with reference to the appended, drawings, in which: Figure 1 is a perspective view of a portion of an exchange structure formed according to a first possible embodiment of the invention; Figure 2 is a cross-section of the structure of Figure 1; Figure 3 shows a portion of an exchange structure according to another possible embodiment of the invention; Figure 4 is a cross-section of the exchange structure of Figure 3; Figures 5 and 6 illustrate two further possible embodiments of a portion of an exchange structure according to the invention; and Figure 7 is a cross-section common to both the embodiments of Figures 5 and 6. As already mentioned above, the exchange structure according to the invention is, to a certain extent, like a fibre structure in the sense that it lends itself to being made in the form of an elongate filamentary body of indefinite length of which Figures 1, 3, 5 and 6 show any portion whilst Figures 2, 4 and 7 show a section taken on any diametral plane (the longitudinal position in which this section is taken varies only the relative orientation of the elements considered). An exchange structure according to the invention, generally indicated 1, comprises essentially two elements, both of indefinite length and therefore capable of being cut to any desired length or wound in any manner entirely similar to those utilised for fibres, that is to say: a core 2, 2', 2"', 2''', which defines the general longitudinal development of the exchange structure 1, and a sheath or covering 3 of generally tubular form (although this configuration is not essential in itself) which surrounds the core 2, 2', 2'', 2''' tightly. In this connection it should be stated that, even though explicit reference will be made in the following description to an embodiment in which the core and the sheath are physically separate from one another, being constituted by two separate bodies, the invention also lends itself to being made with arrangements in which the core and the sheath are at least marginally connected together, for example because they are made simultaneously or almost simultaneously, for example by an extrusion, co-extrusion or like operation. Whatever specific constructional arrangement is adopted, the sheath 3 defines an exchange surface between at least one first medium, which can flow within the space between the internal surface of the sheath 3 and the outer surface of the core 2, 2', 2"', 2''', and at least one second medium which, in use, flows over the outer surface of the sheath 3 in a mechanism generally similar to that which regulates the functioning of hollow-fibre or tube exchange structures. In the embodiment of Figures 1 and 2, the core 2 is formed by two filamentary or fibre elements (here exemplified in the form of solid fibres) preferably wound, at least locally, in a generally helical configuration. A substantially similar arrangement is adopted for the core 2' of the embodiment of Figures 3 and 4, in which there are three filamentary elements 4 (here also shown in the form of solid fibres), preferably coupled in a generally stranded arrangement, also with a generally helical configuration in this case. In the embodiment of Figures 5 and 6, the core is constituted by a profiled body or 2''' 2"' with a lobed cross-section, for example with four substantially identical lobes equiangularly spaced at 90° about the longitudinal axis of the core. The difference between the embodiment of Figure 5 and the embodiment of Figure 6 lies in the fact that, whilst the core 2'' of Figure 5 has a generally rectilinear form, the core 2''' of Figure 6 is, so to say, twisted along its axis such that the lobes 5 are in a generally helical configuration. With regard to the embodiment illustrated in Figures 1, 3 and 6 it should be said that, in these drawings, the helical configuration of the core 2, 2', 2'', 2''' has been exaggerated (in order to illustrate the principal clearly) compared with the real situations currently considered preferable. A characteristic common to all the embodiments illustrated is the fact that the sheath 3 surrounds the core 2, 2'', 2''' in such a way as to leave spaces 6 between the core and the inner face of the sheath 3. These spaces define longitudinal flow channels within the exchange structure 1 for one of the media which is involved in the exchange process (of mass or heat) in use of the structure. For example, in the case of a blood oxygenator device, in a haemofilter or a haemodialiser, the spaces 6 define the flow channels for the oxygen, the blood filtrate or the dialysis solution, whilst the blood which is oxygenated or purified flows over the exterior of the sheath 3. In embodiments such as those of Figures 1 to 4, the spaces 6 have a cross-section which is generally V-shaped with rounded sides (defined by the outer surfaces of the fibres 4). To these is added, in the arrangements of Figures 3 and 4, a central channel or space 6' of approximately triangular shape. Not being exposed to the sheath 3 and therefore not being usable in the exchange mechanism, this central space 6' can be closed or utilised for other purposes (for example for the passage of a guide wire). It goes without saying that the arrangement described in Figures 1 to 4 can readily be extrapolated to the production of further variants of the invention (not illustrated here) in which the core is formed by a strand or braid of four or more filamentary or fibre elements 4. The provision of a plurality of fibres 4 in a generally helical arrangement enables the outer surface of the sheath 3 also to have a generally helically-ribbed shape if fitted around the core 2 or 2'. This particular conformation is advantageous in all those situations in which it is useful to promote a degree of turbulence in the medium which flows over the outer surface of the exchange structure in order to achieve effective exchange: for example, in the cases cited above, blood which is to be oxygenated or purified. Similar, substantial turbulence, or at least non-stagnation, of the medium which flows within the exchange structure 1 is promoted by the generally rough form of the channels 6. The above also applies essentially to the embodiments shown in Figures 5 to 7, especially for the embodiment of Figure 6 in which the core 2''' has a generally helical form. The variants of Figures 5 to 7 have the further advantage that the profiles of the connector surfaces, indicated 6a, interconnecting the lobes 5 can be modified selectively. The surfaces 6a, together with the inner surfaces of the portions of the sheath 3 facing them, define the cross-sectional profiles of the spaces or channels 6. Thus, for example, whilst the drawing of Figure 7 shows surfaces 6a of generally arcuate shape, these surfaces could have an L or V shape or a polygonal or more complex shape. All this within the recognised preference for shapes in those regions of the lobes 5 intended to come into contact with the sheath 3 which are generally rounded in order to support it: corners which are too sharp would in fact induce wear and possibly rupture of the sheath 3 itself. It will likewise be appreciated that, in all the embodiments illustrated, it is possible to make the channels 6 of such a shape that, in those regions in which the lobes 5 lie close to the sheath 3, corner regions with extremely small radii are formed. All this is for the purpose of causing, when liquids are present or flowing in the channels 6, capillary phenomena to occur which prevent the formation of gas-liquid fragmentation within the exchanger structure, according to the teachings provided in EP-A-0 521 430. As regards the choice of constituent materials the structure according to the invention is extremely flexible and can be varied according to specific fields of application. For example, for the production of mass-exchange structures (oxygenators, dialysers, structures for reverse osmosis etc), for the sheath 3 it is possible to use all materials conventionally utilised for the production of exchange membranes or fibres, for example, polymers, polyethylene, polypropylene, polyurethane, polysulphone, silicone, cellulose materials etc up to the use of metals in the case of heat-exchange structures, for example metals having a high thermal conductivity (copper, aluminium, steel etc). There is also the possibility, as far as the wall thickness of the sheath 3 is concerned, of using extremely small values, for example of the order of a few microns, which is optimum for the majority of the applications indicated above, and of making use of unified technologies (for example extrusion, spinning, co-extrusion etc) which do not impose particular overriding limitations as regards the dimensions of the structure. These can therefore be chosen according to the specific requirements of use, for example as far as the overall section of the channels 6 is concerned. By way of example, structures of the type illustrated in the appended drawings can be made with diameters of the order of 150-400 microns, from which it will easily be understood how, in the drawings, and in particular in the sections of Figures 2, 4 and 7, the thickness of the sheath 3, which is a thin-walled body, is shown with dimensions which are greatly enlarged with respect to the real relative dimensions for reasons of clarity of illustration. The above is also true in essence as regards the production of the cores 2, 2', 2", 2"'. Here, too, the choice of materials is just as wide, it being possible to range from very diverse types of polymer to metals (above all when it is desired to give the structure a certain longitudinal rigidity or strength, for example for the production of devices for catheterisation). All this can be achieved by the manufacturer with the use of known manufacturing techniques, such as, typically, extrusion, co-extrusion of the sheath on the core or fitting of heat-shrinkable sheaths and/or (in the case of structures such as those illustrated in Figures 1 and 3) spinning and winding techniques. As already mentioned, the sheath and the core may then consist equally well of two separate bodies or parts of a single body. This is regardless of whether they are made from the same material or are formed from different materials.

Claims: An exchange structure (1) capable of forming an exchange relationship between at least two media across at least one exchange surface, in use, including: a generally elongate core (2, 2', 2'', 2'''), and a sheath (3) defining the exchange surface and surrounding the core (2, 2', 2'', 2''') so as to define, with the core (2, 2', 2'', 2'''), at least one passage (6) for one of the two media characterised in that: the core (2, 2') comprises a plurality of filamentary elements (4) or is constituted by a profiled body (2'', 2''') of generally lobed form (5), and the sheath (3) is constituted by a thin-walled body which surrounds the core (2, 2', 2'', 2''') tightly, so that the outer surface of the sheath (3) over which the other of the media flows in use, exhibits, in cross section, straight portions bridging said filamentary elements (4) or the lobes of said profiled body (2'', 2'''). An exchange structure according to Claim 1, characterised in that the sheath (3) is of generally tubular structure. A structure according to Claim 1 or Claim 2, characterised in that the filamentary elements (4) are disposed in an arrangement in which they wrap around each other such that the sheath (3) has a generally ribbed external form. An exchange structure according to Claim 3, characterised in that the filamentary elements (4) are wound, at least locally, in a generally helical arrangement. An exchange structure according to Claim 1, characterised in that the core (2'', 2''') includes a plurality of equiangularly spaced lobes. An exchange structure according to Claim 1 or Claim 5, characterised in that the profiled body has, at least locally, a twisted form such that the lobes (5) extend in a generally helical form. An exchange structure according to any one of the preceding claims, characterised in that the core (2, 2', 2'', 2''') has a generally rounded form at least in the regions intended to come into contact with the said sheath (3). An exchange structure according to any one of the preceding claims, characterised in that, at least in the regions in which the profile of the core (2, 2', 2'', 2''') is close to the sheath (3), the core (2, 2', 2'', 2''') has a form such as to define corner zones with very small radii of curvature such as to induce capillary phenomena in a fluid which flows through these regions (6). An exchange structure according to any one of the preceding claims, characterised in that the core (2, 2', 2'', 2''') and the sheath (3) are made from different materials. An exchange structure according to any one of Claims 1 to 9, characterised in that the core (2, 2', 2'', 2''') and the sheath (3) are made from substantially the same material. An exchange structure according to any one of the preceding claims, characterised in that the core (2, 2', 2'', 2''') and the sheath (3) are separate bodies. An exchange structure according to any one of Claims 1 to 11, characterised in that the core (2, 2', 2'', 2''') and the sheath (3) are parts of a single body.

Inventors: FINI MASSIMO, PORRO GIAMPIERO, RINALDI STEFANO, VALLANA FRANCO, FINI, MASSIMO, PORRO, GIAMPIERO, RINALDI, STEFANO, VALLANA, FRANCO
Applicants: SORIN BIOMEDICA CARDIO SPA, SORIN BIOMEDICA CARDIO S.P.A.
Application year: 1995
Main classification: D01D5
IPC codes: B01D65, A61M1, B01D63, F28F13, F28F21