Oxygenator of organic fluids
11617818 · 2023-04-04
Assignee
Inventors
Cpc classification
B01D61/00
PERFORMING OPERATIONS; TRANSPORTING
B01D2313/26
PERFORMING OPERATIONS; TRANSPORTING
B01D2313/08
PERFORMING OPERATIONS; TRANSPORTING
A61M1/3623
HUMAN NECESSITIES
B01D61/36
PERFORMING OPERATIONS; TRANSPORTING
A61M1/1698
HUMAN NECESSITIES
International classification
B01D61/36
PERFORMING OPERATIONS; TRANSPORTING
Abstract
The oxygenator of organic fluids comprises: a container body having a longitudinal axis; a first inlet opening for the oxygen and a second outlet opening for an exhaust gas obtained in the container body; a third inlet opening for an organic fluid to be oxygenated and a fourth outlet opening for oxygenated organic fluid obtained in the container body; an oxygenation chamber of the fluid to be oxygenated that is defined inside the container body; a distribution pre-chamber of the fluid to be oxygenated fitted between the third inlet opening and the oxygenation chamber; a mass of capillary fibers that are impermeable to liquids and porous to gasses, designed to be lapped by the organic fluid and arranged inside the oxygenation chamber according with a common parallel direction; dynamic distribution means supported in the distribution pre-chamber by support means.
Claims
1. An oxygenator of organic fluids comprising: a container body having a longitudinal axis; a first inlet opening for the oxygen and a second outlet opening for an exhaust gas obtained in said container body; a third inlet opening for an organic fluid to be oxygenated and a fourth outlet opening for oxygenated organic fluid obtained in said container body; an oxygenation chamber of said organic fluid to be oxygenated that is defined inside said container body; a distribution pre-chamber of said organic fluid to be oxygenated fitted between third inlet opening and said oxygenation chamber; a mass of capillary fibers that are impermeable to liquids and porous to gases, designed to be lapped by said organic fluid and clamped by clamping means inside said oxygenation chamber according with a common parallel direction, said fibers being arranged in a package comprising loops of contiguous layers of fibers, transversally positioned with respect to said longitudinal axis and contained between at least two containing pierced plates which are housed reciprocally parallel in said oxygenation chamber; and dynamic distribution means supported in said distribution pre-chamber by support means, wherein spacing members comprising sheets of bi-adhesive material are interposed between said contiguous layers, said spacing members being fully encapsulated in a plastic-polymeric element; wherein between said contiguous layers at least a central cylindrical usable section is perpendicularly defined, coaxial to said longitudinal axis, designed to be passed through by said organic fluid.
2. The oxygenator as claimed in claim 1, wherein said dynamic distribution means comprise at least a fan that is supported freely rotatable by said support means inside said pre-chamber, said at least one fan including a central stem and a plurality of radial blades.
3. The oxygenator as claimed in claim 2, wherein said central stem is coaxial to said longitudinal axis.
4. The oxygenator as claimed in claim 2, wherein said support means comprise at least one bearing that is fixed in an opposing end of a mouth, coaxially to said longitudinal axis, and which supports said central stem, at least one end of said central stem extending in said mouth with a shaker portion.
5. The oxygenator as claimed in claim 1, wherein said distribution pre-chamber includes a fifth discharge opening outside said oxygenator.
6. The oxygenator as claimed in claim 5, wherein said fifth opening is obtained coaxially to said longitudinal axis and shapes a mouth having an extended end toward an outside of said container body and an opposing end emerging in said distribution pre-chamber, said support means being housed in said opposing end.
7. The oxygenator as claimed in claim 6, wherein said support means comprise at least one bearing that is fixed in said opposing end of said mouth, coaxially to said longitudinal axis, and which supports a central stem, at least one end of said central stem extending in said mouth with a shaker portion.
8. The oxygenator as claimed in claim 1, wherein said clamping means comprise at least one plastic-polymeric element, having two opposing walls encapsulating corresponding homologous opposing ends of said fibers and housed in said oxygenation chamber.
9. The oxygenator as claimed in claim 8, wherein said opposing walls have a rounded profile.
10. The oxygenator as claimed in claim 8, wherein between said at least one plastic-polymeric element and said container body at least an oxygen amassing chamber wherein first homologous ends of said fibers end and an exhaust gas amassing chamber wherein second ends of said fibers end are defined.
11. The oxygenator as claimed in claim 1, wherein between said distribution pre-chamber and said oxygenation chamber a thermoregulation chamber of said organic fluid to be oxygenated is defined, wherein a thermoregulated fluid flows in a flowing circuit arranged in said thermoregulation chamber.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) Other characteristics and advantages of the present invention will become apparent from the detailed description of a preferential but non-restrictive embodiment of an oxygenator of organic fluids, shown by way of non-restrictive example with reference to the attached drawings wherein:
(2)
(3)
(4)
(5)
(6)
(7)
(8)
(9)
(10)
(11)
(12)
(13)
(14)
(15)
(16)
DETAILED DESCRIPTION OF A PREFERRED EMBODIMENT
(17) With reference to the drawings cited, the number 1 indicates in its entirety an oxygenator of organic fluids, in a first possible embodiment, which has a container body 2 defining a longitudinal axis “A”.
(18) In the body 2 a first opening 3 is made from which the oxygen enters, and a second outlet opening 4 from which the exhausted oxygen exits, when, after the oxygenation process is complete, it is mixed with carbon dioxide released by the blood during the gas exchange, as will be described hereafter.
(19) Also in the body 2 there is a third inlet opening 5 from which an organic fluid to be oxygenated enters, in this specific case blood, and a fourth outlet opening 6 from which the blood exits after being oxygenated.
(20) With reference to
(21) In the oxygenation chamber 7 a mass of elements are housed, suitable to perform the gas exchange and which consist of a multitude of hollow fibers 8 which are all joined together in parallel positions and which are associated in the form of a skein consisting of closely adjacent and substantially laminar layers.
(22) As seen in
(23) With reference to
(24) With reference to
(25) As can be seen in
(26) In the preferred embodiment, the spacers 11 consist of sheets 12 of bi-adhesive material and each sheet 12 forms a through circular hole 13 at its center.
(27) When all the holes of all the sheets 12 are superimposed on each other substantially concentrically, a central cylindrical through section “Ω” is formed, intended to be subsequently entirely incorporated in an element of plastic-polymeric material, indicated by 28 and typically known by the term “potting”, defining a central cylindrical through section “Ω1” and coaxial to the previous “Ω” section through which the blood can flow during the gas exchange step, as will be described in detail hereafter.
(28) As can be seen in
(29) As can be seen in the drawings, all the openings 3, 4, 5, 6 are equipped with respective mouths which have a standardized profile to allow to attach connectors for pipes that transport blood and oxygen and which extend toward the outside of the oxygenator.
(30) In the body 2, specifically on the portion 2A considered the upper portion thereof, another fifth opening 18 is also provided which, like the others, is provided with a mouth in relief facing toward the outside, substantially cylindrical in shape, coaxial to the axis “A” and perimetrically equipped with a thread 19 to screw in a closing cap, not shown.
(31) With reference to
(32) Around the central portion 21 through openings 22 are provided which put the fifth opening 18 and the pre-chamber 17 in communication with each other.
(33) The central portion 21 supports a central stem 23 which is coaxial with the axis “A” and which at the base forms dynamic distribution means 24 which are free to rotate inside the pre-chamber 17.
(34) As can be seen in the drawings, the dynamic distribution means 24 are preferably made in the form of a fan having radial blades 25 which occupy a considerable part of the pre-chamber 17.
(35) In detail, the stem 23 has an apical portion 26 which has a shaped profile which forms three radial fins 27, as can be seen in detail in
(36) The radial fins 27 are suitable to keep the flows of blood in an agitated and moderately turbulent regime, in which there may be some undesired embolus of air which could accumulate at this point of the oxygenator 1, which is geometrically the highest inside the inlet chamber of the device, during use in the oxygenation step, to be expelled through the fifth opening 18, preventing the formation in the latter of accumulations and thrombi which, with time, would cause the occlusion thereof, rendering the oxygenator 1 unusable.
(37) With reference to
(38) With reference to
(39) In this drawing, the common elements have been indicated with the same numerical references as in the previous version.
(40) In detail, the oxygenator, indicated by 100, again comprises a body 2 which is equipped with inlet and outlet openings for a gas, in this specific case oxygen, however not visible in the drawing, and with openings for the inlet and outlet of an organic fluid which is to be oxygenated, in this specific case blood: of these last openings, only the fourth outlet 6 of the oxygenated blood is visible.
(41) Also in this second version, the body 2 defines inside it an oxygenation chamber 7 (or also gas exchange chamber in general), in which a mass of hollow fibers 8 organized in the form of a skein formed by laminar layers “S” of hollow fibers 8 parallel to each other is arranged.
(42) As in the previously described version, spacers are interposed between the layers “S”, which in
(43) The mass of hollow fibers 8 is interposed between two laminar plates 14 and 15 which are pierced to allow the blood to pass through them.
(44) The substantial difference between this second version of the oxygenator 100 compared with the first version is that in this second version, between the distribution pre-chamber 17 and the oxygenation chamber 7, another thermoregulation chamber 30 is obtained in which capillaries 31 are housed, open and parallel to each other.
(45) More in detail, the thermoregulation chamber 30 is defined between the laminar plate 15 and another laminar plate 30A, parallel to the laminar plate 15, which is mounted in correspondence with the distribution pre-chamber 17.
(46) The ends of the capillaries 31 end in corresponding lateral chambers 32 and 33 which are obtained in the body 2 and which are provided with openings 34A and 34B, also in this case provided with corresponding extension mouths, which communicate with the outside of the body 2.
(47) Precisely, the two chambers 32 and 33 are obtained by applying two respective lids 35 and 36 in a sealed manner on external and opposite faces 2B and 2C of the body 2.
(48) Typically, from one of the openings 34 a thermoregulated fluid can enter, that is, heated or cooled with respect to the body temperature of a patient, while the thermoregulated fluid can exit from the other opening 34.
(49) The two lateral chambers 32 and 33 are in communication with the thermo-regulation chamber 30 to allow the thermo-regulated fluid to pass inside the capillaries 31, so that the organic fluid to be subjected to oxygenation is heated or cooled as required, during its passage through the oxygenator 100.
(50) With reference to
(51) This characteristic allows to reduce the thickness “Z” of the “potting” 28, especially in the zones in which it incorporates the ends of the hollow fibers 8.
(52) This reduction in thickness allows to significantly reduce the formation of condensation inside the ends of the hollow fibers 8, since the difference in temperature is reduced between the zones in which the blood flows passing through the useful section “Ω1”, lapping the median portions of the hollow fibers 8 and the temperature of the ends of the latter.
DESCRIPTION OF FUNCTIONING
(53) The oxygenator of organic fluids according to the first implementation version functions as follows: the organic fluid to be oxygenated, in this specific case blood, is thrust by a pump that, through an extracorporeal circuit, takes it from a patient, directly or through the interposition of a venous blood collection tank, sends it to the oxygenator 1 and, from this, recirculates it to the patient.
(54) The blood, in detail, enters through the third opening 5, flows into and occupies the pre-chamber 17 in which the dynamic distribution means 24, in practice a fan 24 which rotates and has radial blades 25, thrust by the flow of the blood itself, and is evenly distributed on the surface of the pierced plate 15.
(55) The blood passes through the pierced plate 15 and penetrates inside the oxygenation chamber 7, lapping the external surfaces of the hollow fibers 8 grouped together in a skein.
(56) The blood passes in the cylindrical useful section “Ω1” which is defined between the layers “S” which form the skein of hollow fibers 8.
(57) At the same time, an oxygen flow is introduced into the oxygenator 1 through the first opening 3, accumulating in the chamber 2B in which concurrent ends of the hollow fibers 8 end.
(58) The oxygen then flows inside the hollow fibers 8 during the lapping of the latter by part of the blood.
(59) The porous nature of the hollow fibers 8 to gasses allows to obtain the gas exchange between oxygen and the blood which, in turn, gives up carbon dioxide which is collected inside the hollow fibers 8.
(60) The oxygenated blood then collects in the collection chamber 16 and from here is thrust toward the patient through the fourth outlet opening 6.
(61) The carbon dioxide present in the hollow fibers 8 after the gas exchange is collected in the chamber 2C and from there is sent toward the outside through the second outlet opening 4.
(62) When the blood to be oxygenated enters the oxygenator 1, occupying the pre-chamber 17, it releases possible air bubbles which are expelled through the fifth opening 18, after removal of the closing lid with which it is normally provided.
(63) The rotation of the fan 24 and of the shaft 23 keep the lumen of the fifth opening 18 constantly pervious by means of the dynamic action of the fins 27 which are formed at the end of the shaft 23, preventing harmful and undesirable accumulations and clots of blood inside the lumen of the fifth opening 18.
(64) When the blood flows inside the oxygenation chamber 7, it flows, as we said before, inside the useful passage section “Ω1” which has the overall shape of a pervious cylinder.
(65) The circular sections of the holes 13A which, aligned and substantially coaxial with each other, form the useful section “Ω1”, prevent the formation of angles and/or recesses which, being present in known oxygenators, create preferential paths of the blood flows and, as a consequence, distinct zones in which the speeds of the blood flow may be different from each other, in particular they create zones in which accumulations and clots can arise due to the strong slowing down of the flow speeds.
(66) In the alternative implementation version, the oxygenator 100, in the gas exchange step, functions in the same way as described above for the first version.
(67) The substantive difference is that in the second version, the blood, during its passage inside the oxygenator 100, can also be thermoregulated.
(68) Thermoregulation, which can be performed both to increase the temperature and also to decrease it, is performed by introducing a previously thermoregulated liquid, typically water, with known thermoregulation means, through the opening 34A, first by accumulating it in the lateral chamber 32, then by making it flow inside the capillaries 31 which are housed in the thermoregulation chamber 30, and then collecting it in the lateral chamber 33, before making it exit through the opening 34B.
(69) In the preferred embodiment, the capillaries 31 of the thermoregulation chamber 30 are preferably oriented at a right angle to the hollow fibers 8 of the oxygenation chamber 7.
(70) In this way, the blood, flowing from the pre-chamber 17 toward the oxygenation chamber 7, passes through the other laminar plate 30A, laps the capillaries 31 perimetrically, heating up or cooling down due to contact until it reaches a desired temperature.
(71) The presence of the spacers 11 between the layers “S” of hollow fibers 8 which form each of these allows to prevent crushing in a transverse direction of each hollow fiber 8, keeping the axial lumen pervious and, in short, leaving the entire external circumferential surface thereof completely free, allowing the passage of oxygen and carbon dioxide without any physical obstacle during the gas exchange process.
(72) It is also to be stressed that the particular rounded shape of the perimeter walls of the “potting” 28 considerably attenuates the formation of condensation inside the lumens of the hollow fibers 8, thus maintaining them pervious for the passage of oxygen.
(73) In practice it has been found that the invention achieves the intended purposes.
(74) The invention as conceived is susceptible to modifications and variants, all of which come within the inventive concept.
(75) Furthermore, all the details can be replaced by other technically equivalent elements.
(76) In its practical implementation, the materials used as well as the shapes and sizes may be any whatsoever, according to requirements, without departing from the field of protection defined by the following claims.