LIQUID-GAS BUBBLE SEPARATOR

Abstract: A liquid-gas bubble separator comprising a container (11) having an inlet (13) for a fluid which includes liquid and gas bubbles, an outlet (15) and upstream and downstream vents (17, 19). A filter element (21) is provided in the container between the inlet (13) and the outlet (15). The filter element (21) permits the passage of the liquid and inhibits the passage of the gas bubbles. The filter element (21) is between the upstream and downstream vents (17, 19) so that gas bubbles which do not pass through the filter element (21) can be vented through the upstream vent (17), and any gas bubbles down­ stream of the filter element (21) can be vented through the downstream vent (19). A bypass (71) is provided around the filter element (21). A portion of the filtered fluid is recirculated through the bypass passage (71) to prevent forward flow through the bypass passage (71) when the filter element (21) is clean, and such recirculating flow is terminated when the filter element (21) is clogged to a predetermined degree to thereby open the bypass passage (71) for forward flow. The separator is particularly suitable for use as a venous reservoir bag.

Description: This invention relates to liquid-gas bubble separators and especially to such a separator for use as a venous reservoir bag. A venous reservoir bag is commonly used in a cardiopulmonary bypass loop. A reservoir bag provides an accumulator function in that it allows for variations in blood volume when cardiopulmonary bypass is conducted with a membrane oxygenator. In addition, the reservoir bag separates bubbles from the venous blood or prime solution circulated in the bypass loop and vents the gas to atmosphere. Gas bubbles may enter the cardiopulmonary loop as a result of air or other gases being in the lines before priming or being entrapped in the venous blood at the operating site. One prior art reservoir bag has a blood inlet and a blood outlet along the lower edge of the bag and an air vent at the top of the bag. As blood flows through the bag from the inlet to the outlet, gas bubbles rise and are vented through the vent. Unfortunately, prior art bags of this type do not remove all of the gas bubbles from the blood, particularly when blood flow rates are high, the gas bubbles are relatively small and there is a low liquid volume in the bag. Although the oxygenator will remove some of the gas bubbles, the primary gas removal occurs in the venous reservoir bag. It is important that all of the gas be removed because gas emboli in the cardiovascular system of the patient can be fatal. Siposs US-A-4,344,777 shows a bubble trap for arterial blood in which a filter element is used to assist in the separation of the gas bubbles from the blood. Although a porous filter element can be quite effective in this separation function, there is a danger that the filter element can become clogged, in which event, blood flow to the patient would be terminated. In an attempt to deal with the clogging problem, the patentee provides a bypass outlet for use in those cases where the filter element is clogged up but system flow must continue. The bypass outlet is connected by a flexible tube to the regular outlet tube, and a clamp normally closes the bypass outlet. This requires that the attendant immediately observe the clogged condition of the filter element and manually open the clamp in order to prevent blood flow back to the patient. It is also known to provide an elastic, pressure-sensitive valve between an inlet and one outlet of a filter so that undesired pressure building at the inlet results in at least some of the liquid to be filtered passing from the inlet directly to the outlet. This filter, which is shown in Shaldon et al US-A-4,498,990 does not remove gas emboli from blood. According to the invention, a liquid-gas bubble separator comprises a container, having an inlet, an outlet, and a flow channel, extending between the inlet and the outlet; a filter element in said container between the inlet and the outlet, and permitting the passage of the liquid and inhibiting the passage of the gas bubbles; vent means, leading from the interior of the container to the exterior of the container for exhausting the gas bubbles from the container; and a bypass passage allowing liquid to bypass the filter element, if the filter element becomes blocked, wherein the filter element extends only part way across the flow channel and the bypass passage is formed by part of the flow channel around the filter element, and the inlet is being arranged to direct incoming flow toward the filter element. This invention solves the problems discussed in connection with the prior art and provides a number of other significant advantages. With this invention, a filter element is used to assist in separation of the liquid gas bubbles, and a bypass passage is provided around the filter element for bypassing the liquid around the filter element when the latter is at least partly clogged. However, unlike the prior art, the bypass passage is normally closed for forward flow by the presence of fluid in the bypass passage. When the filter element becomes clogged to a predetermined degree, so that flow through the filter element is reduced forward flow through the bypass passage and around the filter element can occur. Thus, this invention uses the fluid itself to automatically control the effective opening and closing of the bypass passage. Preferably the flow of fluid through the bypass passage is controlled by recirculating a portion of the filtered fluid that passes through the filter element through the bypass passage to the upstream side of the filter element, at least when the filter element is clean. The recirculating serves as valve means for opening and closing the bypass passage. This produces significant advantages. For example, no mechanical bypass valve is required, and consequently, there are no mechanical valve components which can stick, leak, or otherwise fail to function properly. As a result, reliability is increased, assembly is facilitated, and cost is reduced. In addition, the recirculation of the filtered fluid provides a second stage filtering action for the recirculated fluid to further assure the absence of any gas bubbles in the liquid discharged from the container. Another important advantage of this invention is that no separate pressure sensors are required for sensing when the filter element is clogged. In this regard, the recirculation of the filtered fluid responds automatically to a predetermined pressure drop across the filter element to allow at least some forward flow of unfiltered liquid through the bypass passage. Thus, reduction of the percent of open area through the filter element automatically opens the bypass passage for forward flow. Recirculation of filtered fluid through the bypass passage can be accomplished in different ways. For example, a swirling or vortex-like flow can be provided in the liquid upstream of the filter element. The swirling flow can be induced in any suitable way, such as by directing the incoming fluid stream along the surface of the filter element rather than directly against the filter element at a 90-deree angle. Recirculation can also be provided or assisted by directing incoming fluid in a direction extending generally across the bypass passage into the flow channel on the upstream side of the filter media. This tends to induce a lower pressure at the upstream end of the bypass passage to help draw filtered liquid through the bypass passage in the reverse direction. When the filter becomes clogged to a predetermined degree, forward flow of unfiltered fluid through the bypass passage is forced to occur due to the higher resistance to flow through the filter element. The invention is particularly adapted to separate gas bubbles from liquid in a medical fluid, such as blood or a priming solution. However, the invention is more broadly adapted to carry out liquid-gas bubble separation of fluids generally. To provide for separation of the gas bubbles from the liquid downstream of the filter element in a clogged filter element condition, a second vent is preferably provided which leads from the downstream side of the filter element to the exterior of the container. This also provides for a second-stage venting of any gas bubbles that may exist downstream of the filter element when the filter element is unclogged. Although the filter element can take different forms, in a preferred construction, it includes a generally tubular filter element having an opening at one end facing the by pass passage and the inlet, and the upstream vent extends into the tubular filter element. Although the filter element can be of different types and materials, it can advantageously take the form of a porous filter screen. To aid in forming the vortex-like flow, a portion of the end of the tubular filter element containing the opening is closed. The container can be rigid or flexible and in virtually any configuration, including a bag, pipe-like conduit, etc. The tubular filter element can be joined to the container along the opposite sides of the opening in the tubular filter element. With this arrangement, if the container is flexible, the bag expands as it is filled, and the opening of the tubular filter element is pulled open to insure that none of the liquid can escape without passing through the filter element so long as the filter element is unclogged. Forward flow from the bypass passage is preferably directed toward the downstream vent to give any gas bubbles ample opportunity to be vented. In this regard, the blood inlet and blood outlet can advantageously be located along the lower side of the flow channel, and the vents preferably lead from the upper side of the flow channel. The invention, together with additional features and advantages thereof, may best be understood by reference to the following description taken in connection with the accompanying illustrative drawing. In the drawings : Fig. 1 is an isometric view of a venous reservoir bag constructed in accordance with the teachings of this invention. Fig. 2 is an isometric view of one form of filter element. Fig. 3 is a front elevational view of the venous reservoir bag, with the front layer of the bag removed. Fig. 4 is a sectional view taken generally along line 4-4 of Fig. 3. Figs. 5-7 are sectional views taken generally along lines 5-5, 6-6 and 7-7, respectively, of Fig. 1. Fig. 1 shows a liquid-gas separator in the form of a venous reservoir bag 10 which comprises a container 11, an inlet tube 13, an outlet tube 15, an upstream vent tube 17, a downstream vent tube 19 and filter element 21. Although the container 11 may be rigid, in this embodiment, it is in the form of a flexible transparent bag, and it comprises two layers 23 and 25 (Fig. 5) of a suitable biocompatible plastic material heat sealed together along their peripheral edges. To facilitate hanging of the container 11 from a suitable support, such as an IV pole, tear resistant strips 27 and 29 (Figs. 1, 3 and 4) are held captive in elongated clots formed between the layers 23 and 25 by heat seals 31 (Fig. 3) between such layers. The layers 23 and 25 and the strips 27 and 29 have openings 33 from which the container can be suspended. As best shown in Fig. 3, the layers 23 and 25 are heat sealed together by a double heat seal 35 and 37 along their opposite side edges and are heat sealed together by a relatively wade heat seal 39 along their lower edges. The heat seal 39 is interrupted at its opposite ends at the lower corners of the container 11 by the inlet tube 13 and the outlet tube 15 which define an inlet 41 and an outlet 43, respectively, for the venous reservoir bag 10. The heat seal 39 is thickened intermediate its ends to form a ridge 45 (Fig. 3) for a purpose described hereinbelow. The container 11 has a flow channel 47 extending between the inlet 41 and the outlet 43. The vent tubes 17 and 19 lead from the flow channel 47 through the heat seals 31 along the upper edge of the container 11 and define upstream and downstream vents 49 and 51, respectively. The inlet tube 13, the outlet tube 15 and the vent tubes 17 and 19 can be mounted on the container 11 in any suitable manner, such as by an adhesive. Although various different kinds of filter elements 21 can be used, in the embodiment illustrated, the filter element is in the form of a porous filter screen having a pore size of between 50 and 300 microns. The filter screen may be constructed of, for example, plain weave or twill weave nylon or polyester material having 50 percent open area or a depth filter material. Single or multiple layers of the filter screen can be employed. The filter screen is preferably coated with a blood compatible coating, such as heparin. The filter screen will separate gas bubbles, such as air bubbles, from blood, but will not separate the dissolved blood gases from the blood. Although the filter element 21 can be arranged in various different geometric configurations, it is preferably tubular as shown in Fig. 2. The filter element 21 has an opening 53 at its lower end. To form the tubular configuration, the filter screen material is folded along a side edge 55 (Fig. 2) and then heat sealed together along the full length of its upper edge 57 and of the opposite side edge 59. A portion of the bottom edge of the filter element adjacent the edge 55 is closed by a heat seal 61. The opening 53 extends from the edge 59 to the heat seal 61 and, in this embodiment, is longer than the heat seal 61. Although the filter element 21 can be mounted in the flow channel 47 in various different ways, in the embodiment illustrated, it is heat sealed to the container 11 by a heat seal 63 (Fig. 1) extending along the top edge of the filter element and a heat seal 65 extending along the left edge of the filter element as viewed in Fig. 1. Heat seals 67 and 69 (Figs. 1 and 5) which extend from the edge 59 of the filter element along a major length of the opening 53 join the opposite sides of the opening 53 of the filter element to the layers 23 and 25. Because the filter element 21 is heat sealed to the container 11 along the heat seals 67 and 69, inflation of the container with a fluid enlarges the opening 53 as shown in Fig. 5. With the filter element 21 mounted in the flow channel 47 in this manner, the filter element extends from the top of the flow channel only part way across the flow channel to define a bypass passage 71 (Figs. 1, 3, 6 and 7) which bypasses the filter element in extending from the upstream side of the filter element to the downstream side thereof. The bypass passage 71 is directed upwardly generally toward the vent 51 by the ridge 45 so that flow exiting the bypass passage downstream of the filter element 21 is directed generally toward the downstream vent. The opening 53 faces the bypass passage 71 and the inlet 41. The upstream vent 49 extends into the tubular filter element 21, and the downstream vent 51 is downstream of the filter element. In use, the reservoir bag 10 is adapted to be connected into an extracorporeal circuit during cardiopulmonary bypass surgery. When coupled in this circuit, the venous reservoir bag 10 receives blood from the patient through the inlet tube 13. The inlet tube 13 directs the incoming blood through the inlet 41 in a direction extending generally across the bypass passage 71 and into the flow channel 47 on the upstream side of the filter element 21. More particularly, blood flow is directed through the opening 53 into the interior of the tubular filter element 21. This tends to create a slight negative pressure in the bypass passage 71 near the inlet 41. The flow is directed generally upwardly such that it is generally along the interior surface of the filter element 21 rather than being directed transversely through the filter element. As blood volume within the container 11 expands the container, the heat seals 67 and 69 progressively open the opening 53 to assure that the incoming blood stream will enter the tubular filter element 21. Blood flow within the container 11 is generally toward the upstream vent 49, and any gas bubbles within the blood tend to rise toward the upstream vent and be vented to atmosphere. The filter element 21 permits the passage of the blood and inhibits the passage of gas bubbles, and this further tends to separate the gas bubbles from the blood and allow the gas to pass out of the container 11 through the upstream vent 49. The blood that passes through the filter element 21, which may be considered as filtered blood, flows toward the outlet 43, and if any gas bubbles are present, they tend to rise to the surface and be vented through the downstream vent 51 which provides, in effect, a second-stage vent. Some of the blood within the tubular filter element 21 does not immediately pass through the filter element but rather is directed down along the edge 55 within the tubular filter element toward the heat seal 61. The heat seal 61 redirects this flow toward the incoming flow at the opening 53. This creates a swirl or vortex-like flow within the tubular filter element 21 which combines with the negative pressure in the bypass passage 71 resulting from the incoming flow from the inlet 41 to draw in a small percent of the filtered blood from downstream of the filter element 21 through the bypass passage 71. Thus, with the filter element 21 unclogged, flow through the bypass passage 71 is in the reverse direction, i.e., from downstream of the filter element 21 toward the upstream side of the filter element as shown by the arrows in Fig. 1. This serves as a valve to close the bypass passage 71 for forward flow, i.e., from upstream of the filter element 21 to downstream of the filter element 21 or as recirculating means for recirculating a portion of the filtered blood. The recirculation of some of the filtered blood, not only, closes the bypass passage 71, but also provides for passing a mixture of filtered and unfiltered blood through the filter element 21 to further assure elimination of all gas bubbles from the blood returning to the patient. If the filter element 21 becomes clogged to a certain degree, the recirculation of filtered blood through the bypass passage 71 terminates due to the tendency of the blood to take the path of least resistance so that some blood flow through the bypass passage in the forward direction occurs. Of course, at some greater degree of clogging of the filter element 21, all of the incoming blood from the inlet 41 flows through the bypass passage 71 into the flow channel 47 downstream of the filter element. The ridge 45 directs the flow exiting the bypass passage 71 generally toward the downstream vent 51 so that gas bubbles can separate from the blood and be vented through the downstream vent. The bypass passage 71 opens for forward flow when the resistance to flow through the filter element reaches a certain magnitude. Although this increased resistance to flow will ordinarily be brought about by clogging of the filter, under certain conditions, it may be brought about by a high volume of gas bubbles in the container 11 which would reduce the open area of the filter available for the passage of liquid.

Claims: A liquid-gas bubble separator comprising: a container (11), having an inlet 41, an outlet (45), and a flow channel (47), extending between the inlet (41) and the outlet (45); a filter element (21) in said container (11) between the inlet (41) and the outlet (43), said filter element (21) permitting the, passage of the liquid and inhibiting the passage of the gas bubbles; vent means (49), leading from the interior of the container (11) to the exterior of the container (11) for exhausting the gas bubbles from the container (11); and a bypass passage (71) allowing liquid to bypass the filter element (21), if the filter element (21) becomes blocked, characterised in that the filter element (21) extends only part way across the flow channel (47) and the bypass passage (71) is formed by part of the flow channel (47) around the filter element (21), the inlet (41) being arranged to direct incoming flow toward the filter element (21). A separator according to claim 1 wherein the container (11) comprises a flexible bag and the filter element (21) comprises a generally tubular structure having an opening at one end (53), said opening (53) being adjacent and spaced from the inlet (41). A separator according to claim 2 wherein the filter element (21) is flexible and on opposite sides of its opening (53) is joined to the walls of the bag so that inflation of the bag by passage of liquid thereinto pulls open the opening (53) of the filter element (21). A separator according to claim 2 or claim 3 wherein said opening (53) of the filter element (21) extends only partially across the filter element (21), the remainder (61) of said end of the filter element (21) being closed, the bypass passage (71) being defined at least partially by said closed portion (61) of the tubular filter element (21) and the walls of the bag in the region of said closed portion (61). A separator according to any one of claims 1 to 4 wherein said container (11) is generally rectangular and is arranged to be suspended from one edge, with the inlet (41) and the outlet (43) on the lower edge, the bypass passage (71) along the lower edge and with the vent means (49) on the upper edge. A separator according to any one of claims 2 to 4 wherein the inlet (41) is arranged to direct incoming flow into the filter element (21) in a direction generally across the bypass passage (71). A separator according to any one of claims 1 to 6 wherein the interior of the container (11) is structured to provide swirling flow on the upstream, side of the filter element (21) to recirculate a part of the filtered liquid back through the bypass passage (71) to block the bypass passage (71) to forward flow. A separator according to any one of claims 1 to 7, wherein said vent means (49) extends into the filter element. A separator according to any one of claims 1 to 8, including a second vent means (51) downstream of the filter element (21). A separator according to claim 9, wherein the interior of the container is structured to direct forward flow through the bypass passage (71) towards said second vent means (51).

Inventors: BALDING, DAVID, CLARKE, ROLF
Applicants: BAXTER INTERNATIONAL INC. (A DELAWARE CORPORATION)
Application year: 1986
Main classification: A61M1
IPC codes: B01D19, A61M1