Patent Grant
11420165
The invention relates generally to the system and methods for mixing one liquid with dissolved gas into a second liquid in a bubble free manner to achieve gas enrichment in the second liquid and, more particularly, to the gas enrichment of a flowing liquid within a conduit.
Gas-enriched liquids are desirable in a wide variety of applications. However, at ambient pressure, the relatively low solubility of many gases, such as oxygen or nitrogen, within a liquid, such as water, produces a relatively low concentration of the dissolved gas in the liquid. One method of obtaining an increase in the gas concentration level without significant increase in liquid volume involves an injection and mixing of a gas-enriched liquid, such as a gas-supersaturated liquid, into a liquid flow path of interest. A liquid can be gas enriched at high pressure through various methods. However, when the gas-supersaturated liquid is delivered to the mixing site at ambient pressures, it has a propensity to form gas bubbles. Thus there is a need for a system and methods for mixing a highly gas enriched liquid into another liquid in a bubble free manner.
Oxygen-enriched liquids are desirable in a variety of medical applications. However, injection of the gas-supersaturated liquid directly into blood within a blood vessel without adequate mixing of the gas-supersaturated liquid and the blood may lead to localized pockets of the liquid having high levels of gas supersaturation. The presence of these pockets of the gas-supersaturated liquid within blood vessels may lead to nucleation of oxygen bubbles from the gas-supersaturated liquid with accompanying entrainment of undesirable bubbles in the blood stream. Gas bubbles may occlude the blood vessels and result in a gaseous local embolism that causes a decrease in local circulation, arterial hypoxemia, and systemic hypoxia. The inhibition of gaseous emboli formation is highly desirable for this application.
To solve this problem of gaseous emboli formation, conventional methods for the delivery of oxygenated blood or oxygen-enriched liquids to tissues and bodily liquids involve the use of extracorporeal circuits for blood oxygenation. Extracorporeal circuits require withdrawing blood from a patient, circulating the blood through an oxygenator to increase blood oxygen concentration, and then delivering the blood back to the patient. There are drawbacks, however, to the use of conventional oxygenators in an extracorporeal circuit. In general, they are not operated and monitored automatically, and the presence of a qualified perfusionist is typically required. Accordingly, such systems typically are costly, complex, and difficult to operate.
Conventional extracorporeal circuits also exhibit other drawbacks. For example, extracorporeal circuits typically have a relatively large priming volume. The priming volume is typically the volume of blood contained within the extracorporeal circuit, i.e., the total volume of blood that is outside of the patient's body at any given time. For example, it is not uncommon for the extracorporeal circuit to hold one to two liters of blood for a typical adult patient. Such large priming volumes are undesirable for many reasons. For example, in some cases a blood transfusion may be necessary to compensate for the blood temporarily lost to the extracorporeal circuit because of its large priming volume. Also, a heat exchanger must be used to maintain the temperature of the blood at an acceptable level as it travels through the extracorporeal circuit. Further, conventional extracorporeal circuits are relatively difficult to turn on and off. For instance, if the extracorporeal circuit is turned off, large stagnant pools of blood in the circuit might coagulate.
In addition to the drawbacks mentioned above, in extracorporeal circuits that include conventional blood oxygenators, there is a relatively high risk of inflammatory cell reaction and blood coagulation due to the relatively large blood contact surface area of the oxygenators. Conventional membrane-type blood oxygenators are gas-liquid contact devices, and require efficient surface contact between gas and blood. The exposure of blood to both solid surface and gas contact triggers a host of inflammatory processes, begins the process of protein denaturation, and acts to promote the coagulation cascade. For example, a blood contact surface area of about one to two square meters are not uncommon with conventional oxygenator systems. Thus, relatively aggressive anti-coagulation therapy, such as heparinization, is usually required as an adjunct to using the oxygenator. Anti-coagulation therapy increases the risk of bleeding.
An additional limitation of conventional gas-liquid membrane-based blood oxygenators is the maximum gas-enrichment that may be imparted to the blood; the gas concentration in the blood is expressed typically as an oxygen partial pressure, or pO2 level. Under optimal conditions, conventional blood oxygenation systems can elevate the arterial blood pO2 to a maximum level of approximately 500 mmHg. Thus, if the benefits of hyperbaric medicine are to be realized, i.e. with blood having pO2 levels at or above one atmosphere, or 760 mmHg, this result cannot be achieved with conventional oxygenators.
A new technology for producing hyperbaric blood pO2 levels has been developed as described in U.S. Pat. No. 6,387,324. This technology, referred to as Supersaturated Oxygen Therapy (SSO2 Therapy), develops higher oxygen concentrations than conventional means, but still requires that the fluid to be oxygenated be pumped to an oxygenation device to mix with a highly oxygen-enriched fluid, then be returned as an oxygenated fluid. In the case of oxygenating patient blood, this is defined as an extracorporeal circuit.
In view of these disadvantages of the conventional devices and methods for enriching liquids with high concentrations of dissolved gas, it is an object of the present invention to provide devices and methods for enriching a liquid within a conduit with a dissolved gas without use of external mixing circuits and in a manner which prevents or minimizes bubble formation.
This and other objects and advantages are achieved in the system of the present invention for enriching a flowing liquid inside a conduit with a dissolved gas. The system comprises two or more capillaries, each capillary delivering a stream of a gas-enriched liquid into the flowing liquid contained in the conduit. The first end (outlet) of each capillary is positioned inside the conduit in fluid communication with the flowing liquid. The first ends of the capillaries form an intersecting angle with respect to the effluent stream of other capillary such that these streams of gas-enriched liquid collide with each other upon exit from the first ends of the capillaries, effecting localized convective mixing within the larger liquid conduit before these gas-enriched streams are able to come into close contact with the boundary surfaces of the conduit. This localized convective mixing that is achieved by the geometric apposition of the streams acts to rapidly achieve a nearly homogeneous concentration (mixing cup concentration) in the surrounding liquid without exposing the localized ‘hot spots’ of high gas concentration to potential bubble nucleation from the boundary surfaces. In one embodiment, the capillaries are contained within a tip of a catheter adapted for positioning within the enclosed area in communication with the bodily liquid. The second ends of the capillaries are connected to a single tube within the catheter to be supplied with a source of gas-enriched fluid.
The gas-enriched liquid introduced through the capillaries may be water, physiologic solution, or biocompatible liquid-liquid emulsions; these gas-enriched liquids may advantageously contain ancillary therapeutic agents that are desirable to be delivered in combination with the gas-enriched liquid. In the case of liquid-liquid emulsions, a dispersed non-aqueous phase may be incorporated stably into the solution by conventional means in order to enhance gas solubility or incorporate water-immiscible therapeutic agents (such as perfluorocarbons or crystalloids). The bodily liquid may be blood, cerebrospinal fluid, or interstitial liquid. The gas may be oxygen, ozone, nitrogen, air, an inert gas, or a non-inert gas that is desired to add directly to the bodily liquid for therapeutic effect. The conduit may be an enclosed area such as a blood vessel.
The second ends of the capillaries (catheter inlet) may be operatively coupled to a cartridge, the source for the gas-enriched liquid. In one embodiment, the cartridge comprises a housing and an enrichment device disposed in the housing to form a gas-enriched liquid. The enrichment device may comprise an atomizing chamber adapted to receive the gas through a gas inlet and an atomizer disposed within the atomizing chamber. The atomizing chamber is pressurized with the gas that is to be dissolved into the liquid. The atomizer is adapted to receive a liquid from a fluid supply assembly (piston pump) and to atomize the liquid upon delivery into the atomizing chamber, exposing the liquid to the pressurized gas and dissolving the gas efficiently to form the gas-enriched liquid.
In another aspect, the present invention provides a method of operating a system for enriching a liquid with a dissolved gas inside a conduit. The method comprises: (a) providing two or more capillaries each having first and second ends for delivery of a gas-enriched liquid; (b) the first ends form an intersecting angle with respect to the effluent streams such that these streams of gas-enriched liquid collide with each other upon exit from the first ends of the capillaries, effecting localized convective mixing within the larger liquid conduit before these gas-enriched streams are able to come into close contact with the boundary surfaces of the conduit; and (c) operatively connecting the second ends of the capillaries to a source of the gas-enriched liquid.
In one embodiment, the step (a) further comprises: (a1) providing a single lumen polymer capillary tube; (a2) wrapping the tube around a curved tool with a known radius to form a capillary of a modified shape having a curved segment; and (a3) cutting and removing a part of the curved segment to form two capillaries with exposed lumen. Preferably, the cutting step (a3) is conducted in such a way that each of the obtained two capillaries has a curved portion, wherein the end of the curved portion is the first end of the capillary.
In another embodiment, the step (a) further comprises: (a1) providing a separate capillary tube for each capillary end; (a2) inserting each tube into a slot on a tip adapter in such a way as to produce the geometry for intersecting capillary jets; and (a3) holding each capillary in place with an outer sleeve that could be shrunk over the tip to lock the capillaries in place.
In another aspect, the present invention provides a method of enriching a liquid with a dissolved gas inside a conduit. The method comprises: (a) providing two or more capillaries for delivery of a gas-enriched liquid, each capillary having first and second ends, wherein the first ends form an intersecting angle with respect to the effluent streams such that these streams of gas-enriched liquid collide with each other upon exit from the first ends of the capillaries, effecting localized convective mixing within the larger liquid conduit before these gas-enriched streams are able to come into close contact with the boundary surfaces of the conduit; and (b) delivering the gas-enriched liquid through the capillaries and mixing it with a bodily liquid to form a gas-enriched bodily liquid.
Preferably, the mixing occurs without accompanying bubble formation. For example in one embodiment, evaluation of oxygen-enriched liquid mixing was performed, using a peristaltic pump in combination with a glass tube. Solutions of glycerin and water, and polyacrylamide and water were used in different concentrations to simulate a range of potential bodily liquid viscosities and viscoelastic behavior. In this experiment, the simulated bodily liquid solution was pumped at a fixed flow rate of 110 ml/min through the test circuit, while injecting 4.0 ml/min of oxygen-enriched liquid (with added dye for visual contrast enhancement) through the first ends of the dual capillaries, using a custom in vitro test system. The exit jets streams of the oxygen-enriched liquid were positioned at opposing 45° angles (90° included angle) to effect jet collision just distal to the exit ports of the first ends. The exit region and jet streams were observed and videotaped. When a 40% (v/v) glycerin and water simulated bodily liquid solution was used, video results showed that the colliding exit jet streams of oxygen-enriched liquid quickly dispersed, filling the glass tube (conduit). No evidence of nucleation on the distal outer surface of the capillaries, or in the mixed flow stream, was observed during the test.
The system and methods of the present invention have been found to provide an adequate mixing without production of significant bubbles within a blood vessel of a patient. In the present invention, the gas-enriched liquid may be created in the same manner as previously described in U.S. Pat. No. 6,613,280, entitled “System for Enriching a Bodily Fluid with a Gas,” which is incorporated herein by the reference. However, the present invention greatly simplifies the cartridge described in that Patent by entirely eliminating the necessity for extracorporeal mixing of the bodily liquid with the highly gas-enriched liquid. In effect, the present invention improves upon the previously disclosed ex vivo liquid-liquid oxygenation method and apparatus by creating an effective in vivo liquid-liquid oxygenation method and apparatus. Accordingly, the hardware component of the present invention is greatly simplified since many of the features described in U.S. Pat. No. 6,613,280 are not needed, including the blood pump, blood draw tubing, and extracorporeal blood circuit controls.
The aforementioned and other features of this invention and the manner of obtaining them will become more apparent, and will be best understood by reference to the following description, taken in conjunction with the accompanying drawings. These drawings depict only a typical embodiment of the invention and do not therefore limit its scope. They serve to add specificity and detail.
The present invention provides a system for enriching a bodily liquid with a dissolved gas inside an enclosed area 1 of a body. As shown in
Henry's Law describes the effect of pressure on the solubility of a gas in a liquid. The law states that the gas solubility at a fixed temperature is proportional to the partial pressure of the gas in phase equilibrium with the liquid. The simple equation for Henry's Law is pA=HxA, where pA represents the partial pressure of gas A, H is the Henry's Law constant for gas A in the specified liquid, and xA is the mole fraction of gas A dissolved in the liquid. For example, at sea level total atmospheric pressure is 760 mmHg and approximately 20.8 percent of this air is oxygen gas. Using the ideal gas law, the partial pressure of oxygen at sea level is 158 mmHg (760 mmHg×0.208=158.08 mmHg). The Henry's Law constant for oxygen solubility in water at 25° C.=4.55×104 atmosphere/mole fraction O2, or 3.45×107 mmHg/mole fraction O2, the details of which are described in A. X. Schmidt and H. L. List, Material and Energy Balances, Prentice-Hall, Englewood Cliffs, N J, 1962. Thus, the mole fraction of oxygen dissolved in water that is exposed to air at standard temperature and pressure (STP) xO2=pO2/H=158/(3.45×107)=4.57×10−6.
Liquids may be enriched with gas to obtain gas-enriched liquids containing concentrations of the gas that exceed its solubility at ambient pressure; this condition is necessary to have a gas-supersaturated liquid. For example, compression of a gas/liquid mixture at a high pressure may be used to achieve a high dissolved gas concentration. As per Henry's Law, the application of higher pressure will increase the partial pressure of the gas, and the solubility will increase proportionally. E.g., a gas-enriched liquid that has a greater dissolved oxygen concentration than 4.57×10-6 mole fraction in ambient conditions at STP must also have a higher equivalent partial pressure of oxygen than the ambient air level of about 158 mmHg. Such a liquid, for the purposes of the present invention, is defined as a “gas-enriched liquid”, meaning a liquid having a gaseous solute concentration that exceeds its equilibrium solubility limit in accordance with Henry's Law.
The gas-enriched liquid of the present application may contain one or more dissolved gases such as oxygen, ozone, an inert gas (for example, helium), nitrogen, nitrous oxide, carbon dioxide and air. In one embodiment, gas-enriched liquid is oxygen-supersaturated liquid that contains a dissolved oxygen concentration (expressed in units of STP gas volume per volume solvent) between 0.5 and 3 ml O2/ml solvent; expressed in terms of xO2, this range is 3.68×10−4 to 2.2×10−3. For this specific example, the solvent is aqueous in nature. Compared to the amount of oxygen contained in water under ambient conditions, the upper end of this achievable concentration range is (2.2×10−3)/(4.57×10−6)=483 times this level.
The oxygen-supersaturated liquid may be supplied to the capillaries at supply pressures from 100 to 10,000 psig, at any supersaturated concentration produced when saturating the fluid at the chosen supply pressure. The supply pressure (operating pressure) is controlled, and the total flow rate will vary depending upon the capillary diameter and length, number of capillaries, and liquid viscosity.
For physiologic applications, oxygen levels typically are described in terms of equivalent partial pressure of oxygen that is in equilibrium with the dissolved gas. Thus, measurements of oxygen concentration in the blood are reported as ‘pO2’ levels, in units of mmHg, even though the reported quantity is the dissolved gas concentration. For human arterial blood, normal oxygen levels, i.e., normoxia or (less commonly) normoxemia, range from 90 to 160 mmHg. Hypoxic blood, i.e., hypoxia or (less commonly) hypoxemia, is arterial blood with a pO2 less than 90 mmHg. Hyperoxemic blood, i.e., hyperoxia or hyperoxemia, is arterial blood with a pO2 greater than 160 mmHg. As used herein, hyperbaric blood is arterial blood with a pO2 greater than 160 mmHg, or the oxygen concentration of air at standard conditions. In one embodiment, the obtained gas-enriched bodily liquid is blood containing a hyperbaric concentration of oxygen.
For the purposes of the present invention, any gas-enriching device may be used to provide a gas-enriched liquid to the capillaries. For example, gas-enriched liquid may be prepared using apparatus and methods for preparing oxygen-supersaturated liquids disclosed in U.S. Pat. No. 5,407,426 to Spears entitled “Method and Apparatus for Delivering Oxygen into Blood”; U.S. Pat. No. 5,569,180 to Spears entitled “Method for Delivering a Gas-Supersaturated Fluid to a Gas-Depleted Site and Use Thereof”; U.S. Pat. No. 5,599,296 to Spears entitled “Apparatus and Method of Delivery of Gas-Supersaturated Liquids;” U.S. Pat. No. 5,797,874 to Spears entitled “Method of Delivery of Gas-Supersaturated Liquids;” U.S. Pat. No. 6,387,324 to Patterson entitled “Apparatus and Method for Blood Oxygenation”, and U.S. Pat. No. 6,613,280 to Myrick, entitled “System for Enriching a Bodily Fluid with a Gas,” each of which is incorporated herein in its entirety by reference.
The gas-enriched liquid introduced through the capillaries may be water, physiologic solution, or biocompatible liquid-liquid emulsions or microemulsions; these gas-enriched liquids may advantageously contain ancillary therapeutic agents that are desirable to be delivered in combination with the gas-enriched liquid. In the case of liquid-liquid emulsions or microemulsions (for example perflouorocarbons, or PFC's), a dispersed non-aqueous phase may be incorporated stably into the solution by conventional means in order to enhance gas solubility or incorporate non-aqueous therapeutic agents. Examples of physiologic solutions include ion-balanced salt solutions, such as those which contain calcium, sodium, magnesium, potassium, and mixtures thereof. It will also be appreciated that suitable physiologic solutions may include pH buffers selected from a group consisting of phosphates, bicarbonates, and mixtures thereof. Additionally, the physiologic solution may comprise a physiologically balanced salt solution and an oncotic agent selected from the group consisting of albumen, hydroxyethyl starch, and mixtures thereof. It may also be helpful to provide a physiologic solution including a balanced salt solution and a perfluorocarbon, for example. It will be readily apparent that other equivalent substitutes may be selected, but for brevity they are not specifically enumerated here.
The system of the present invention may be used with any bodily liquid. For example, the system may be used to enrich blood, cerebrospinal fluid, or interstitial liquid. For example, in one embodiment, the bodily liquid is blood and the enclosed area is the coronary vasculature. The enclosed area may be a blood vessel and the surfaces surrounding the enclosed area are walls of the blood vessel.
Preferably, the angle α between the first ends of the capillaries is such that the exit jets from the capillaries, which are laminar jets, collide and form an efficient mixing zone, enabling rapid elimination of concentration gradients and realization of a uniform mixing cup concentration. In one embodiment, the α is between 20° and 150°. In another embodiment, cc is between 30° and 120°. In still another embodiment, α is 90°.
In the preferred embodiment, no observable bubbles are formed in the gas-enriched bodily liquid. To help minimize or eliminate the formation of clinically significant bubbles, the blood contact surfaces of the capillaries are exposed to or coated with blood proteins for some brief time interval, usually at least several minutes, before initiating infusion of oxygen-supersaturated liquids. Exposure of the capillary surfaces to proteins is equivalent to providing a wettable surface-active coating, which acts to limit the potential for heterogeneous bubble nucleation from the surface. Similarly, other liquid contact surfaces are exposed to or pre-wetted with liquids and/or hydrophilic agents or coatings, e.g., saline, ethanol and benzalkonium heparin, before use. The liquid contact surfaces also do not include any substance which promotes such bubble formation, e.g., hydrophobic or non-water wettable surfaces that have low surface free energy and high observed contact angles with water, namely Teflon, Teflon-composite liners, silicone oils, etc. Hydrophilic liquid contact surfaces, achieved through judicious material selection or coating methods, are typically useful.
In the case of delivery of gas-enriched liquid to the vasculature, the system of the present invention may be used in conjunction with angiographic or guiding catheters, arterial sheaths, and/or other vascular access devices used in angioplasty and in other interventional cardiovascular procedures. In one embodiment depicted in
The first ends of the capillaries may be connected to each other in such a way that allows the effluent streams of the gas-enriched liquid to collide and convectively mix before exposing the boundary surfaces surrounding the enclosed area to highly supersaturated gas concentrations. Such an arrangement greatly improves lateral stability of the capillaries. For example, in embodiments shown in
In the embodiment shown in
In the embodiments shown in
Fluid Delivery Catheter
Typically, the fluid delivery catheter 500, as shown in
This oxygen-enriched saline is delivered from the fluid oxygenation device 54 to catheter 500 via the single lumen tube 40 and to the capillaries 10 and 11 via a transition 41. The catheter 500 is designed to create a relatively low pressure drop from the oxygenation device 54, through single lumen tube 40 and transition 41. Most of the pressure drop in the catheter occurs in capillaries 10 and 11.
In one embodiment, the capillaries in the catheter tip are also enclosed within a tip sleeve 16. Tip sleeve 16 may be attached to transition 41 by any suitable means. Methods of attachment of two elements are known by those skilled in the art and may include chemical adhesion or over molding. A tip cover 15 (not shown for clarity) could be adhesively attached, mechanically attached, or incorporated into the over molded tip sleeve 16. The internal form 17 aligns and supports the capillaries.
Alternatively, catheter 500 can form an integral catheter sleeve (not shown) with internal transition 41 from a single lumen tube 40 to the capillaries 10 and 11. The internal transition from single lumen tube 40 to multiple capillaries 10 and 11, can be achieved in a single, low profile transition 41. This transition would be joined to the capillaries 10 and 11, using chemical adhesives or solvent bonding.
Oxygenation Device (Cartridge)
Although, as discussed above, various gas-enriching devices may be suitable for supplying gas-enriched liquid to the capillaries, in one embodiment shown in
As mentioned previously, the oxygenation device 54 includes two chambers: a fluid supply chamber 58 and an atomization chamber 62. Although various relative positioning of two chambers is possible, in one embodiment, illustrated in
A liquid, such as physiologic liquid (or saline), is delivered from a suitable supply 56, such as an IV bag, to the fluid supply chamber 58 of the cartridge 54 under the control of a system controller (not shown). A suitable gas, such as oxygen, is delivered from a supply 60, such as a tank, to the atomization chamber 62 of the cartridge 54. Although the system of the present invention can operate with any gas, liquid, and bodily liquid, for clarity and simplicity the following description will refer to oxygen, saline, and blood, respectively. The saline from the fluid supply chamber 58 is pumped into the oxygen-pressurized atomization chamber 62 and atomized to create oxygen-enriched saline.
An appropriate delivery device, such as a tube 140, is coupled to a supply of physiologic liquid. In this example, the tube 140 is coupled at one end to an IV bag 56. The other end of the tube 140 is coupled to inlet port 142 of the fluid supply chamber 58. The inlet port 142 forms a fluid passageway that leads to the fluid supply chamber 58 through passageway 190. A check valve 146 is disposed in the inlet port 142 so that fluid may enter the passageway 190 through the inlet port 142, but fluid cannot exit through the inlet port 142.
As illustrated by
Referring to
Referring additionally to
In operation, the piston assembly 160 within the fluid supply chamber 58 acts as a piston pump. As the piston assembly 160 retracts, fluid is drawn into the chamber 58 from the fluid supply 56. No fluid can be drawn from passageway 190 because valve assembly is closed and a check valve 146 is closed in this direction. As the piston assembly 160 extends, the fluid within the chamber 58 is pressurized, typically to about 670 psi, and expelled from the fluid supply chamber 58 through the fluid passageway 190. The outlet of the fluid supply chamber 58 is coupled to an inlet of the atomization chamber 62 via an appropriate fluid passageway. Further shown in
As shown in
The nozzle 222 forms fluid droplets into which the oxygen within the atomization chamber 62 diffuses as the droplets travel within the atomization chamber 62 shown in
Since the atomizer 216 will not atomize properly if the level of the pool rises above the level of the nozzle 222, the level of the pool is controlled to ensure that the atomizer 216 continues to function properly. The system monitors a liquid level sensor (not shown) to maintain minimum level in atomization chamber 62. A second (Low) level sensor monitors if level is too low to safely operate, and can stop gas-enriched liquid delivery.
As shown in
Because it is desirable to control the extent to which the patient's blood is enriched with oxygen, it may be desirable to dilute the oxygen-supersaturated liquid to reduce its oxygen content. Any suitable valve arrangement and type of valve may be used. For example, in one embodiment, the valves are needle valves that are normally biased in the closed position. Details of these valves are described in U.S. Pat. No. 6,613,280, the relevant content of which is incorporated herein by reference. A representative needle valve 230 is shown in
Although an atomizing chamber provides a convenient mechanism for diffusing relatively large amounts of gas into a liquid in a relatively short period of time, it is not the only way of dissolving gas within a liquid. Indeed, other devices, such as membrane oxygenators, gas spargers, bubblers, and thin film oxygenation devices, may be used to perform this function as well. Furthermore, although a piston pump similarly provides a compact and efficient method of pressurizing liquid prior to sending it to an oxygenator, such as the atomizer, other types of pumps or methods of pressurization may be used as well. Therefore, although a piston pump and atomizer are utilized in the exemplary embodiment of the system of the present invention, other devices may perform these functions.
With these generalities in mind, as shown in
Also, all of the valves used to operate the oxygenation device 54 are integrated within its unitary structure. Thus, the valves and their associated fluid passageways are protected against external contamination, and users are protected against any contamination that may arise from the use of the various fluids as well. As a result, the oxygenation device 54 is a relatively contamination-free cartridge that may be used during a surgical procedure on a patient, and then removed and replaced prior to performing a surgical procedure on the next patient.
Finally, the oxygenation device 54 allows to create oxygen-enriched saline and deliver it directly to the patient's coronary vasculature through the fluid delivery catheter where it adequately mixes with the blood without creating bubbles.
Hardware Enclosure (Cartridge)
Although, as discussed above, various gas-enriching devices may be suitable for supplying gas-enriched liquid to the capillaries, in one embodiment shown in
Capillary Construction Methods
In another aspect, the present invention provides a method of assembling a system for enriching a flowing liquid with a dissolved gas inside a conduit. The method comprises: (a) providing two capillaries for delivery of a gas-enriched liquid, each with a first end and a second end; (b) positioning the first ends of the capillaries to form an intersecting angle with respect to the effluent streams such that these streams of gas-enriched liquid collide with each other upon exit from the first ends of the capillaries, effecting localized convective mixing within the larger liquid conduit before these gas-enriched streams are able to come into close contact with the boundary surfaces of the conduit; and (c) operatively connecting second ends of the capillaries to a source of the gas-enriched liquid.
In one embodiment shown in
In one embodiment, the step (a2) further comprises a step of fixing the modified shape of the capillary. On one embodiment, discussed in more detail in Examples that follow, the fixing is carried out by placing the form tool and capillary in an oven and baked them at approximately 350° F. for about 60 minutes to stress relieve the capillary.
For example, in one embodiment, a single lumen polymer capillary tube, made from polyetherimide, is formed approximately 180 around a tool with a known radius, of 0.100 inch or smaller. The form tool and tube are placed in an oven and baked at approximately 350° F. to stress relieve the capillary. Baking also allows the capillary to retain its shape during the bonding process at assembly. The formed capillary is placed into a trimming fixture, and a circular segment is cut from the apex of the capillary, exposing the inner lumen. The radius of the capillary and the depth of the trimmed segment control the angle of the exit jet streams; this angle is preferably 90 included. As a final step, the overall length of the capillary is trimmed to the final size.
As shown in
The obtained capillaries 10 and 11 each having a single lumen or a single capillary 400 may be positioned inside a catheter as shown in
In another aspect, the present invention provides a method of enriching a flowing liquid with a dissolved gas inside a conduit. The method comprises: (a) providing two capillaries for delivery of a gas-enriched liquid, the capillaries having first and second ends, wherein the first ends of the capillaries are positioned to form an intersecting angle with respect to the effluent streams such that these streams of gas-enriched liquid collide with each other upon exit from the first ends of the capillaries, effecting localized convective mixing within the larger liquid conduit before these gas-enriched streams are able to come into close contact with the boundary surfaces of the conduit; and (b) delivering the gas-enriched liquid through the capillaries to form a gas-enriched bodily liquid.
In one embodiment, the capillaries are contained within a tip of a catheter adapted for positioning within the body in a communication with the bodily liquid. The catheter may further comprises an aligning device. Then, the positioning step (b) of the above method further comprises a step of using the aligning device to position the catheter inside the body in a way that prevents a contact between the streams of the gas-enriched liquid with the surfaces surrounding the enclosed area prior to the mixing of the gas-enriched liquid with the bodily liquid.
The present invention may be embodied in other specific forms without departing from its essential characteristics. The described embodiments are to be considered in all respects only as illustrative and not as restrictive. The scope of the invention is, therefore, indicated by the appended claims rather than by the foregoing description. All changes which come within the meaning and range of the equivalence of the claims are to be embraced within their scope.
This application is a continuation of U.S. patent application Ser. No. 15/732,975, filed on Jan. 22, 2018, which is a divisional of U.S. patent application Ser. No. 13/986,361, filed on Apr. 23, 2013, which claims the benefit of U.S. Provisional Application No. 61/687,781, filed May 1, 2012.
| Number | Name | Date | Kind |
|---|---|---|---|
| 2901112 | Naftulin | Aug 1959 | A |
| 3862715 | Remenyik | Jan 1975 | A |
| 3963503 | Mackenzie | Jun 1976 | A |
| 4041180 | Wilson | Aug 1977 | A |
| 4445886 | Osterholm | May 1984 | A |
| 4450841 | Osterholm | May 1984 | A |
| 4664680 | Weber | May 1987 | A |
| 4808378 | Nakanishi | Feb 1989 | A |
| 4865836 | Long, Jr. | Sep 1989 | A |
| 4874509 | Bullock | Oct 1989 | A |
| 4927623 | Long, Jr. | May 1990 | A |
| 4963130 | Osterholm | Oct 1990 | A |
| 4965022 | Litz | Oct 1990 | A |
| 4973558 | Wilson | Nov 1990 | A |
| 5029579 | Trammell | Jul 1991 | A |
| 5072739 | John | Dec 1991 | A |
| 5080885 | Long, Jr. | Jan 1992 | A |
| 5084011 | Grady | Jan 1992 | A |
| 5086620 | Spears | Feb 1992 | A |
| 5108662 | Litz | Apr 1992 | A |
| 5261875 | Spears | Nov 1993 | A |
| 5324436 | John | Jun 1994 | A |
| 5344393 | Roth | Sep 1994 | A |
| 5393513 | Long, Jr. | Feb 1995 | A |
| 5407426 | Spears | Apr 1995 | A |
| 5527962 | Pavia | Jun 1996 | A |
| 5562608 | Sekins | Oct 1996 | A |
| 5569180 | Spears | Oct 1996 | A |
| 5591328 | Bodnaras | Jan 1997 | A |
| 5599296 | Spears | Feb 1997 | A |
| 5693017 | Spears | Dec 1997 | A |
| 5735934 | Spears | Apr 1998 | A |
| 5797874 | Spears | Aug 1998 | A |
| 6030357 | Daoud | Feb 2000 | A |
| 6180059 | Divino, Jr. | Jan 2001 | B1 |
| 6241802 | Spears | Jun 2001 | B1 |
| 6248087 | Spears | Jun 2001 | B1 |
| RE37379 | Spears | Sep 2001 | E |
| 6312647 | Spears | Nov 2001 | B1 |
| 6315942 | Spears | Nov 2001 | B1 |
| 6344489 | Spears | Feb 2002 | B1 |
| 6387324 | Patterson | May 2002 | B1 |
| 6454997 | Divino | Sep 2002 | B1 |
| 6555059 | Myrick | Apr 2003 | B1 |
| 6565807 | Patterson | May 2003 | B1 |
| 6576191 | Myrick | Jun 2003 | B1 |
| 6582387 | Derek | Jun 2003 | B2 |
| 6596235 | Divino, Jr. | Jul 2003 | B2 |
| 6602467 | Divino, Jr. | Aug 2003 | B1 |
| 6602468 | Patterson | Aug 2003 | B2 |
| 6607698 | Spears | Aug 2003 | B1 |
| 6613280 | Myrick | Sep 2003 | B2 |
| 6622542 | Derek | Sep 2003 | B2 |
| 6676900 | Divino, Jr. | Jan 2004 | B1 |
| 6746417 | Spears | Jun 2004 | B2 |
| 6759008 | Patterson | Jul 2004 | B1 |
| 6811750 | Patterson | Nov 2004 | B2 |
| 6843099 | Derek | Jan 2005 | B2 |
| 6849235 | Myrick | Feb 2005 | B2 |
| 6855291 | Patterson | Feb 2005 | B2 |
| 6890482 | Divino, Jr. | May 2005 | B2 |
| 6899847 | Myrick | May 2005 | B2 |
| 6936221 | Divino, Jr. | Aug 2005 | B1 |
| 6974435 | Daw | Dec 2005 | B2 |
| 7013703 | Derek | Mar 2006 | B2 |
| 7172727 | Patterson | Feb 2007 | B2 |
| 7820102 | Myrick | Oct 2010 | B2 |
| 8192384 | Myrick | Jun 2012 | B2 |
| 8246564 | Myrick | Aug 2012 | B2 |
| 9919276 | Myrick | Mar 2018 | B2 |
| 10960364 | Myrick | Mar 2021 | B2 |
| 20100143190 | Myrick | Jun 2010 | A1 |
| 20100143192 | Myrick | Jun 2010 | A1 |
| 20100145249 | Myrick | Jun 2010 | A1 |
| Number | Date | Country |
|---|---|---|
| 271787 | Sep 1912 | DE |
| 0692273 | Jan 1996 | EP |
| Number | Date | Country | |
|---|---|---|---|
| 20210252463 A1 | Aug 2021 | US |
| Number | Date | Country | |
|---|---|---|---|
| 61687781 | May 2012 | US |
| Number | Date | Country | |
|---|---|---|---|
| Parent | 13986361 | Apr 2013 | US |
| Child | 15732975 | US |
| Number | Date | Country | |
|---|---|---|---|
| Parent | 15732975 | Jan 2018 | US |
| Child | 17189054 | US |
