The present application is related to the following commonly-assigned, issued U.S. patents, which are incorporated herein by reference in their entirety: U.S. Pat. No. RE36,386 (ABBOTT et al.) Nov. 9, 1999, U.S. Pat. No. 5,573,502 (LECOCQ et al.) Nov. 12, 1996, U.S. Pat. No. 5,638,737 (MATTSON et al.) Jun. 17, 1997, and U.S. Pat. No. 5,645,531 (THOMPSON et al.) Jul. 8, 1997.
1. Technical Field
The present invention relates generally to equipment used to deliver fluids to a patient during surgery. Specifically, the present invention is directed to a device for delivering cardioplegia solution during open-heart surgery and other surgical procedures requiring myocardial protection.
2. Background Art
Heart surgery is among the most complex of surgical fields. Because under normal conditions, the heart muscle is in a constant state of motion, special techniques must be used to make the heart sufficiently stationary to allow a surgeon to operate on it. Although some surgical procedures may be performed on a beating heart, the majority of open-heart and closed-heart procedures, including coronary artery bypass surgery, require that the heart be slowed or stopped and the aorta clamped before the cardiac portion of the surgery may begin. In such procedures, external equipment is used to form an extracorporeal circuit in the patient's circulatory system. Electric/mechanical pumps are used to pump the blood to an artificial oxygenator, then back into the patient, so as to temporarily replace the patient's heart and lungs during the procedure. This technique is known as a “cardiopulmonary bypass,” and it allows the surgical team to stop the heart, while still keeping the patient alive.
The heart muscle (myocardium), no less than any other organ of the body, must also be kept alive during the procedure. Indeed, the myocardium has a very low tolerance for ischemia (reduction in blood supply), due to its high oxygen requirements. Thus, special techniques are employed to protect the myocardium during a cardiopulmonary bypass.
Modern surgical teams often use induced cardioplegia to both stop the heart and protect it from the effects of ischemia. A potassium-based cardioplegic solution is infused into the coronary arteries, usually at a low temperature. The potassium infusion causes an immediate cardiac arrest, while the typically low temperature of the solution reduces the heart's rate of oxygen consumption. There are two commonly-employed cardioplegic methods, blood cardioplegia and crystalloid cardioplegia. Blood cardioplegia is a solution that is mixed with oxygenated blood from the extracorporeal circuit. Crystalloid cardioplegic solution is a non-cellular solution with a saline or balanced electrolyte base such as Ringer's solution. Nowadays, cardioplegia may bedelivered through antegrade (that is, directly through the coronary arteries) or retrograde (through the coronary sinus vein) routes.
During cardiopulmonary bypass, both blood and cardioplegia solution must be circulated through the patient's body. Since the heart is no longer available to maintain the patient's circulation, artificial pump means must be employed. The most commonly employed pump is the DeBakey roller pump, which is described in U.S. Pat. No. 2,018,998 (DEBAKEY et al.) Oct. 29, 1935. The DeBakey pump uses a pair of rollers to create a peristaltic action against a flexible tube. Centrifugal pumps are also employed. Both of these types of pumps produce a relatively constant rate of flow.
Recent research, however, suggests that better cardiac perfusion is obtained with a pulsatile flow than with a constant-rate flow. The heart, after all, is a reciprocating pump and delivers a pulsatile flow. A number of designs have been developed to introduce a pulsatile component to extracorporeal circulation. These designs generally fall into two categories. A first category consists of those devices that combine a roller or centrifugal pump with an additional device that periodically compresses the tube through which the blood or cardioplegia flows. Examples of these devices include U.S. Pat. No. 4,116,589 (RISHTON) Sep. 26, 1978, and U.S. Pat. No. 6,620,121 (MCCOTTER) Sep. 16, 2003.
A second category consists of devices in which the pump itself is used to produce a pulsatile flow. In one type of pump, such as that in U.S. Pat. No. 5,702,358, the number of revolutions per minute (RPM) of a centrifugal pump is varied in a periodic fashion to achieve a roughly pulsatile flow. In U.S. Pat. No. 5,300,015 (RUNGE) Apr. 5, 1994, a type of peristaltic pump is described, which achieves a pulsatile flow. Both of these types of designs, however, are limited in their ability to produce a pulsatile flow of desired characteristics while still maintaining a desired average flow rate.
What is needed, therefore, is an apparatus for extracorporeal circulation that produces a significantly pulsatile flow, while still-maintaining a user-specified average flow rate. The present invention provides a solution to this and other problems, and offers other advantages over previous solutions.
A preferred embodiment of the present invention provides a system for delivering blood, cardioplegia solution, and other medications or fluids in a pulsatile flow to a patient during cardiopulmonary bypass. In one embodiment, a dual chambered pumping apparatus is utilized in which a pumping action is achieved by compressing one of the chambers with a piston mechanism, while allowing the other chamber to fill with fluid by retracting its respective piston. The instantaneous flow rate of either of the chambers is determined by the speed of the piston. In another embodiment, a single chambered pumping apparatus is used. In this embodiment, the piston can be delivering fluid during a stroke while at the same time filling the chamber on the opposite side of the piston. In a preferred embodiment, a pulsatile flow of fluid is achieved by cyclically alternating the velocity of the piston between two different speeds. A desired average flow rate is maintained by adjusting the alternating velocities and a duty cycle for the flow rate alternation. The calculations necessary to obtain a desired average flow rate are performed by a microprocessor, which also controls the movement of the pistons.
The foregoing is a summary and thus contains, by necessity, simplifications, generalizations, and omissions of detail; consequently, those skilled in the art will appreciate that the summary is illustrative only and is not intended to be in any way limiting. Other aspects, inventive features, and advantages of the present invention, as defined solely by the claims, will become apparent in the non-limiting detailed description set forth below.
The present invention may be better understood, and its numerous objects, features, and advantages made apparent to those skilled in the art by referencing the accompanying drawings, wherein:
The following is intended to provide a detailed description of an example of the invention and should not be taken to be limiting of the invention itself. Rather, any number of variations may fall within the scope of the invention, which is defined in the claims following the description.
A preferred embodiment of the present invention is directed to a system for delivering a pulsatile flow of blood and crystalloid cardioplegia solution to a patient undergoing open-heart surgery. In particular, a preferred embodiment of the present invention allows a perfusionist or surgeon to select between two different delivery modes, one in which fluids are delivered to the patient in a pulsatile flow and another in which fluids are delivered to the patient in a nonpulsatile flow. The two different modes of operation are supported by software, which controls the mechanical operation of the pump. The electromechanical components utilized in both modes are the same, the only difference between the two modes being the software processes used to control the electromechanical components of the system.
Turning now to
A crystalloid solution is stored in container 124 for combination with blood flowing in line 112 in a disposable pumping cassette 130a. The output of cassette 130a is supplied through line 128 to a heat exchanger 135. Pump cassette 130a is controlled by an electromechanical pump mechanism 130 in which cassette 130a is mounted. A second pump 131 controls cassette 131a containing potassium solution supplies its output to line 128 downstream from the pump cassette 131a. A third pump 132 controls cassette 132a containing any additional drug supplies its output to line 128 downstream from the pump cassette 132a.
In heat exchanger 135, the cardioplegic solution is juxtaposed with a circulating temperature controlled fluid to adjust the temperature of the solution prior to forwarding the solution to the heart through line 118. Preferably pump 133 circulates temperature controlled fluid through heat exchanger 135 either by push or pull.
The system includes patient monitoring of myocardial temperature along the signal path 142 and heart pressure along signal path 144 communicating to a central microprocessor control section 146. In addition, the pressure and temperature of the cardioplegic solution in delivery line 118 is sensed via sensors 160 and the data is forwarded along signal paths 148 and 150 to control microprocessor 146. Data input to microprocessor 146 through control panel 152 may include an advantageous combination of the following parameters: desired overall volumetric flow rate, desired blood/crystalloid ratio to be forwarded, desired potassium concentration to be established by pump 131, desired supplemental drug concentration to be established by pump 132, desired temperature of solution in cardioplegia delivery line 118, and safety parameters such as the pressure of the cardioplegia solution in the system or in the patient.
In response to the data input through the control panel 152 and the monitored conditions along signal paths 142, 144, 148 and 150, microprocessor control section 146 controls the operation of pump mechanism 130, via signal path 154, and of potassium pump 131 by way of a signal along path 156. In addition, microprocessor control section 146 controls the circulation of fluid in the heat exchanger circulation path along signal path 158 either for obtaining a desired patient temperature or a desired output solution temperature. Further, the safety parameters such as pressure limits for a particular procedure or a particular patient may be controlled based upon input settings or based upon preset standards, as for example, one range of acceptable pressure limits for antegrade and another range for retrograde cardioplegia.
In accordance with a preferred embodiment of the invention, microprocessor controller section 146 controls the pump mechanism 130 to combine crystalloid from container 124 and blood from line 112 in any selected ratio over a broad range of blood/crystalloid ratios. Controller 146 may command the pump mechanism 130 to deliver blood without crystalloid addition. The blood/crystalloid ratio can be adjusted from an all blood mixture to an all crystalloid mixture, with multiple ratios in between. The rate of flow produced by the pump mechanism 130 of the combined output from disposable pump cassette 126 is preferably variable from 0 to 999 milliliters per minute. Potassium pump 131 is automatically controlled to maintain a constant potassium solution concentration. In other words, if the blood pump flow rate is increased, the potassium pump flow rate is automatically increased.
The cassette 220 includes a first fluid inlet 222 and a second fluid inlet 224. In a preferred embodiment, the first fluid inlet 222 accommodates blood and the second fluid inlet accommodates a crystalloid fluid typically used during open heart surgery. Fluid entry paths 223, 225 run respectively from inlets 222, 224 to a common inlet path 226, which bifurcates to form inlet flow paths 228a and 228b. Inlet flow paths 228a and 228b respectively terminate in pump chambers 230a, 230b.
Outlet paths 232a, 232b, forming the respective output pathways from pump chambers 230a, 230b, join at a common outlet path 235. The outlet path 235 is the gateway for passage of the first and second fluid mixture to other portions of the fluid delivery system.
As shown in
As shown in
In the preferred embodiment, each spline 244 has a thickness substantially equal to that of each rib 254. Therefore, when the base 250 receives the piston 240 there exists limited and tightly controlled clearance between any rib-spline interface, thereby preventing the opportunity for the cassette material to become pinched or positioned between the elements during operation. The piston 240 may be manufactured from a lubricated material such as acetyl fluoropolymer (for example, Delrin AF from DuPont, Co., Wilmington, Del.), and the base 250 from a glass reinforced polycarbonate (for example, a 10% glass material Lexan 500 from GE Plastics, Pittsfield, Mass.), to permit largely unrestricted motion of the piston 240 relative to the base 250 despite the potential for repeated contact between two elements. The number of splines 244 and ribs 254 should be such that the space 245 between each spline 244 and the space 255 between each rib 254 (such being substantially equivalent if the thickness of each spline 244 is substantially equivalent to the thickness of each rib 254) is of such a distance to enable the adjacent splines (or ribs as the case may be) to support the cassette 220 across the spaces 245, 255.
The complementary shaping of the piston 240 and the base 250 enables a resting cassette pumping chamber 230 to be supported by a constant surface area throughout an entire stroke of the piston 240, thereby foreclosing the opportunity for the cassette material to be stretched, unsupported or pinched during movement of the piston 240. Furthermore, the geometric relation between the elements permits a mathematical relation to be established. In the preferred embodiment, for example, the diameter of the piston 240 linearly decreases, relative to the interior of the pumping chamber 230, with the retraction of piston 240. A similar relation exists for the advancement of piston 240. Thus, during retraction of the piston 240, an enclosed volume is created which increases as a quadratic function of the piston's 240 movement. The relation can be used to maintain a constant fluid flow rate because the rate of piston movement can be controlled to achieve a predetermined flow rate.
Although the preferred embodiment defines a base 250 having a receiving surface 258 with a 45-degree angular displacement along the plurality of ribs 254, the angular displacement may measure from 30 to 60 degrees. Notwithstanding, the preferred embodiment ensures (i) a relatively significant pumping chamber volume, (ii) full support of the cassette pumping chamber 230 through an entire pumping stroke, and (iii) avoidance of trapped air within the pumping chamber 230.
Referring to both
For pumping mechanism 130, inlet valves 284a, 284b, 286a, 286b control the introduction of fluid into the pumping chambers 230a, 230b. The inlet valves 284a, 284b, 286a, 286b act on the cassette 220 at valve locations 234a, 234b, 236a and 236b, respectively. Outlet valves 288a, 288b control the flow of fluid from the pumping chambers 230a, 230b by acting on cassette valve locations 238a, 238b. As an example, in preparation of filling pumping chamber 230b, valve 286a (valve location 236a) is actuated to close inlet flow path 228a, while valve 288b (valve location 238b) also occludes outlet path 232b to permit the accumulation of fluid within the pumping chamber 230b. During filling, valves 284a, 284b and 286b (valve locations 234a, 234b and 236b, respectively) open and close in a predetermined synchronized pattern to permit a ratio of the first and second fluids to enter the pumping chamber 230b. Upon completion of the fill, valves 286b and 288a respectively occlude flow paths 228b and 232a, and valve 288b is de-actuated to permit fluid to flow from the pumping chamber 230b. Fluid movement, whether filling or being expelled from the pumping chambers 230a, 230b, is initiated through the movement of the mechanism's pump assemblies 210a, 210b.
Referring to
When the cassette 220 is operatively positioned in the pump mechanism 130, the cassette pumping chambers 230a, 230b align with and rest upon the pump assemblies 210a, 210b. The retaining door 274 effectively constrains the cassette 220 during operation. The formed volume of the paths and chambers of the cassette 220 may be slightly greater or less than the nominal constraining volume defined by the rigid constituents of the pump mechanism 130. Practically, the firm restraints of the pump mechanism 130 permit the development of relatively high fluid pressures within the cassette 220 without significant or detrimental deformation of the cassette material. Indeed, constraining the cassette 220 over effectively the entire cassette surface creates an inherently non-compliant system. Such non-compliance contributes to the ability of the pump mechanism 130 to produce consistent, accurate volumetric fluid delivery.
In the preferred embodiment, the cassette pumping chambers 230a, 230b do not rest directly upon the supporting surfaces of the piston 240 and/or base 250. Instead, a resilient material 278, attached about the upper portion of the base 250, operates to conform to the supporting surface of the piston assembly 210 without regard to whether the piston 240 is fully advanced, retracted or in some intermediate position. The resilient material 278 protects the pump mechanism 130 from fluid intrusion in the event any liquid is spilled on the device operational environment. The resilient material 278 also acts to further protect the cassette 220 from damage that could inadvertently occur through the operation and movement of the piston assembly 210.
In an alternative embodiment, the resilient material 278 could include reinforcement means to provide additional rigidity to the resilient material 278. As an example, reinforcement means could include a fine metal mesh or cloth embedded within the material used to fabricate the resilient material 278. Alternatively, the resilient material 278 could include a spiral wire which is capable of concentric expansion to provide facial and lateral support for a resting cassette 220 about the interior of the base 250 (when piston 240 is in a retracted position) or about the piston 240 (when piston 240 is in an advanced position). Lastly, the material 278 could be formed of cloth altogether to eliminate any elasticity. This alternative embodiment, and its variations, could permit the use of fewer rib/splines or provide greater reliability in applications that require the piston assembly 130 to operate in larger applications, in the presence of greater fluid pressures or both.
Returning to
In addition to providing substantially continuous flow, the pump mechanism 130 of the present embodiment incorporates a four-step filling protocol, which is in parallel to the expulsion of fluid from the other pump chamber, to ensure the volumetric accuracy of the delivered fluid. First, valve 288a is actuated and a first fluid is introduced into the pumping chamber 230a through the synchronized operation of the inlet valves. The pump motor 272a retracts a predefined amount to admit a volumetric quantity of the first fluid that, relative to the total volume of the pumping chamber 230a, satisfies a predefined fluid mixture ratio. Second, the system tests the volumetric accuracy of the first fluid within the pump chamber 230a. As a prelude to performing the test, valve 286a is actuated to occlude inlet path 228a. The pump motor 272a is advanced a few steps to increase the pressure within the pumping chamber 230a to a predetermined level. Based upon both the relative position of the piston 240a and the measured chamber pressure, the fluid delivery system determines whether a sufficient quantity of fluid was delivered to the pumping chamber 230a. Third, a second fluid is introduced into the pumping chamber 230a through the synchronized operation of the inlet valves. Lastly, the accuracy of the total fluid volume is tested in accordance with the procedure above. Upon determining that the pump chamber has filled properly, the fill protocol is completed.
As should be gained from this operational description, the piston assembly 210 reduces the opportunity for damage to blood or blood-fluid mixtures in the pumping process. Specifically, the pump assembly 210 does not possess those features that (i) facilitate the trapping of blood in or about the pumping chamber 230 or (ii) subject the blood to damaging compressive forces (roller pumps) or shearing forces (centrifugal pumps).
From the relationship correlating piston position to pumping chamber volume, one will appreciate that various fluids may be mixed at definable ratios through simply controlling the number of steps the pumping motors 272a, 272b move for each fill stage. As well, the total volumetric flow rate delivered by the pump mechanism 130 is dependent upon the user-defined, flow rate.
Thus, at the commencement of the
The valves 284a and 284b controlling inlet of blood and crystalloid to common inlet path 226, and the inlet valve for chamber 230a (inlet valve 286a) are sequentially opened and closed during the filling protocol for bladder 230a, which occupies the time period during which bladder 230b is delivering fluid to line 128 (
In the 4-step filling protocol for chamber 230a, illustrated at the outset of the diagram, valves 284a and 286a are initially open, and valve 284b closed. Thus, an open flow path for entry of blood to chamber 230a is provided through inlet 222, common inlet path 226, and pump chamber inlet path 228a, while crystalloid is occluded at valve 284b. Pump motor 272a (shown in
The total volumetric flow rate from the cassette is varied pursuant to operator request simply by compressing or expanding the time for a cycle to be completed. Of course, if intermittent operation is desired, this may be provided as well. No matter what changes may be made to the blood/crystalloid flow rate, microprocessor 146 preferably automatically controls potassium pump 132 to deliver at a concentration which provides the requested potassium concentration.
Turning now to
Period 302 comprises partial-cycles 308a, 308b, 308c during which the piston is moved at a lower velocity, so as to achieve a lower flow rate. During partial-cycles 310a, 310b, 310c the piston is moved at a higher velocity, thus achieving a higher flow rate. The portion of period 302 during which the higher velocity is applied is referred to as the “duty cycle”. This velocity characteristic (which also represents the instantaneous flow rate) is a square- or rectangle-wave. Due to compliance in the tubing connecting the cardioplegia delivery system to the patient, the actual flow rate characteristic and actual fluid pressure characteristic experienced by the patient is more sinusoidal in nature, as shown at the top of
The upper and lower velocities, corresponding to upper and lower flow rates, respectively, are selected so as to achieve a desired average flow rate over time given a particular amplitude and duty cycle for the pulsatile flow. The difference in pressure obtained during the upper flow rate and that obtained during the lower flow rate is called the “pulse pressure.” An operator may also specify a particular frequency, corresponding to a simulated heart rate, at which the operator wishes the pulsatile flow to run. In order to simulate normal physiological conditions, a frequency of between 50-90 beats per minute is typically used. As shown in
Given a desired average flow rate, a desired amplitude, and a desired duty cycle, the microprocessor control of a preferred embodiment of the present invention calculates an appropriate upper and lower flow rate.
For safety purposes, one embodiment of the present invention supports a maximum upper flow rate of 750 mL/min. Therefore, if the upper flow rate calculated in block 402 exceeds 750 mL/min (block 404:Yes), then the upper flow rate is set to 750 mL/min. Then the amplitude is adjusted to be 750 mL/min./Avg. flow rate (block 406), and the process cycles back to block 408. The lower flow rate is calculated as
If this lower flow rate is less than 10 mL/min. (block 410: Yes), the lower flow rate is set to 10 ml/min. Then the amplitude is adjusted to be
and the process cycles back to block 414.
If the lower flow rate is greater than the minimum value of 10 mL/min. (block 410:No), then a cyclic flow profile, such as that depicted in
One of the preferred implementations of the invention is a client application, namely, a set of instructions (program code) or other functional descriptive material in a code module that may, for example, be resident in the random access memory of a microprocessor, microcontroller, or other computer (e.g., microprocessor control section 146 in
While particular embodiments of the present invention have been shown and described, it will be obvious to those skilled in the art that, based upon the teachings herein, changes and modifications may be made without departing from this invention and its broader aspects. Therefore, the appended claims are to encompass within their scope all such changes and modifications as are within the true spirit and scope of this invention. Furthermore, it is to be understood that the invention is solely defined by the appended claims. It will be understood by those with skill in the art that if a specific number of an introduced claim element is intended, such intent will be explicitly recited in the claim, and in the absence of such recitation no such limitation is present. For non-limiting example, as an aid to understanding, the following appended claims contain usage of the introductory phrases “at least one” and “one or more” to introduce claim elements. However, the use of such phrases should not be construed to imply that the introduction of a claim element by the indefinite articles “a” or “an” limits any particular claim containing such introduced claim element to inventions containing only one such element, even when the same claim includes the introductory phrases “one or more” or “at least one” and indefinite articles such as “a” or “an;” the same holds true for the use in the claims of definite articles.
Number | Name | Date | Kind |
---|---|---|---|
2018998 | DeBakey | Oct 1935 | A |
3597766 | Buck | Aug 1971 | A |
4116589 | Rishton | Sep 1978 | A |
4376312 | Robinson et al. | Mar 1983 | A |
5300015 | Runge | Apr 1994 | A |
5520652 | Peterson | May 1996 | A |
5573502 | LeCocq et al. | Nov 1996 | A |
5638737 | Mattson et al. | Jun 1997 | A |
5645531 | Thompson et al. | Jul 1997 | A |
5702358 | Witherspoon et al. | Dec 1997 | A |
5941891 | Walen | Aug 1999 | A |
RE36386 | Abbott et al. | Nov 1999 | E |
6083198 | Afzal | Jul 2000 | A |
6174144 | van Hamme et al. | Jan 2001 | B1 |
6422990 | Prem | Jul 2002 | B1 |
6620121 | McCotter | Sep 2003 | B1 |
20030088238 | Poulsen et al. | May 2003 | A1 |
20040015042 | Vincent et al. | Jan 2004 | A1 |
Number | Date | Country | |
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20070134101 A1 | Jun 2007 | US |