Blood Processing Systems And Methods That Employ An In-Line Flexible Leukofilter
Systems and methods separate pump the blood cells through an in-line leukofilter to a blood cell storage container. The leukofilter has a filtration medium enclosed within a flexile housing. The systems and methods can employ a fixture to restrain expansion of the flexible filter housing during operation of the pump.
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This application is a continuation of co-pending U.S. application Ser. No. 09/976,833, filed Oct. 13, 2001, and entitled Blood Separation Systems and Methods that Employ an In-Line Leukofilter Mounted in a Restraining Fixture,” which is a continuation-in-part of U.S. patent application Ser. No. 09/389,504, filed Sep. 3, 1999, and entitled “Blood Separation Systems and Methods Using a Multiple Function Pump Station to Perform Different On-Line Processing Tasks,” which is incorporated herein by reference.
FIELD OF THE INVENTIONThis invention relates to systems and methods for processing and collecting blood, blood constituents, or other suspensions of cellular material.
BACKGROUND OF THE INVENTIONToday people routinely separate whole blood, usually by centrifugation, into its various therapeutic components, such as red blood cells, platelets, and plasma.
Conventional blood processing methods use durable centrifuge equipment in association with single use, sterile processing systems, typically made of plastic. The operator loads the disposable systems upon the centrifuge before processing and removes them afterwards.
Conventional blood centrifuges are of a size that does not permit easy transport between collection sites. Furthermore, loading and unloading operations can sometimes be time consuming and tedious.
In addition, a need exists for further improved systems and methods for collecting blood components in a way that lends itself to use in high volume, on line blood collection environments, where higher yields of critically needed cellular blood components, like plasma, red blood cells, and platelets, can be realized in reasonable short processing times.
The operational and performance demands upon such fluid processing systems become more complex and sophisticated, even as the demand for smaller and more portable systems intensifies. The need therefore exists for automated blood processing controllers that can gather and generate more detailed information and control signals to aid the operator in maximizing processing and separation efficiencies.
SUMMARY OF THE INVENTIONThe invention provides systems and methods for processing blood and blood constituents that lend themselves to portable, flexible processing platforms equipped with straightforward and accurate control functions.
One aspect of the invention provides blood processing systems and methods comprising a blood processing set that includes a source of blood cells and a blood component collection flow channel coupled to the source of blood cells. The blood component collection flow channel includes a blood cell storage container and an in-line filter to remove leukocytes from the blood cells before entering the blood cell storage container. The in-line filter including a fibrous filter medium, first and second flexible housings, and a unitary, continuous peripheral seal. The peripheral seal is characterized by being formed by application of pressure and radio-frequency heating in a single process, to join the first and second flexible housings to each other, as well as join the fibrous filtration medium to the first and second flexible housings. The blood processing system further includes a pump station adapted to be placed into communication with the blood component collection flow channel to pump blood into the blood cell storage container through the in-line filter.
In one embodiment, the blood processing system further includes a fixture to restrain expansion of the first and second filter housings as a result of pressure applied during operation of the pump station.
In one embodiment, the source of blood cells includes a donor flow channel including a blood separation device to separate blood cells from donor whole blood. Other features and advantages of the inventions are set forth in the following specification and attached drawings.
The invention may be embodied in several forms without departing from its spirit or essential characteristics. The scope of the invention is defined in the appended claims, rather than in the specific description preceding them. All embodiments that fall within the meaning and range of equivalency of the claims are therefore intended to be embraced by the claims.
DESCRIPTION OF THE PREFERRED EMBODIMENTSThe system 10 is particularly well suited for processing whole blood and other suspensions of biological cellular materials. Accordingly, the illustrated embodiment shows the system 10 used for this purpose.
I. System OverviewThe system 10 includes three principal components. These are: (i) a liquid and blood flow set 12 (shown schematically in
A. The Processing Device and Controller
The blood processing device 14 and controller 16 are intended to be durable items capable of long term use. In the illustrated and preferred embodiment, the blood processing device 14 and controller 16 are mounted inside a portable housing or case 36. The case 36 presents a compact footprint, suited for set up and operation upon a table top or other relatively small surface. The case 36 is also intended to be transported easily to a collection site.
The case 36 includes a base 38 and a hinged lid 40, which opens for use (as
The case 36 can be formed into a desired configuration, e.g., by molding. The case 36 is preferably made from a lightweight, yet durable, plastic material.
The controller 16 carries out process control and monitoring functions for the system 10. The controller 16 comprises a main processing unit (MPU), which can comprise, e.g., a Pentium™ type microprocessor made by Intel Corporation, although other types of conventional microprocessors can be used. The MPU can be mounted inside the lid 40 of the case 36.
Preferably, the controller 16 also includes an interactive user interface 260, which allows the operator to view and comprehend information regarding the operation of the system 10. In the illustrated embodiment, the interface 260 includes an interface screen carried in the lid 40, which displays information for viewing by the operator in alpha□numeric format and as graphical images.
Further details of the controller 16 can be found in Nayak et al, U.S. Pat. No. 6,261,065, which is incorporated herein by reference. Further details of the interface can be found in Lyle et al, U.S. Pat. No. 5,581,687, which is also incorporated herein by reference.
As
B. The Flow Set
The flow set 12 (see
The flow set 12 can take various forms. In the illustrated embodiment (see
As
The centrifuge station 20 rotates the processing chamber 18. When rotated, the processing chamber 18 centrifugally separates whole blood received from a donor into component parts, e.g., red blood cells, plasma, and platelets.
In the illustrated embodiment, the set 12 also includes a fluid pressure actuated cassette 28 (see
The cassette 28 can take various forms. In a preferred embodiment (see
As
As
Further details of the cassette 28 and the operation of the pump and valve station 30 can be found in Nayak et al, U.S. Pat. No. 6,261,065, which is incorporated herein by reference.
Referred back to
In the illustrated embodiment, the flow set 16 is arranged to support the centrifugal collection of two units of red blood cells (about 360 ml), and to filter the red blood cells to reduce the number of leukocytes prior to storage. During this procedure, whole blood from a donor is centrifugally processed in the chamber 18 into red blood cells (in which a majority of the leukocytes resides) and a plasma constituent (in which a majority of the platelets resides). The plasma constituent is returned to the donor, while the targeted volume of red blood cells is collected, filtered to reduce the population of leukocytes, and placed into containers for storage mixed with a red blood cell storage solution.
In this configuration (see
As
An anticoagulant tube 270 is coupled to the phlebotomy needle 268. The anticoagulant tube 270 is coupled to another cassette port. A container 276 holding anticoagulant is coupled via a tube 274 to another cassette port.
A container 288 holding saline is coupled via a tube 284 to another cassette port.
The set 16 further includes tubes 290, 292, 294, which extend to an umbilicus 296. When installed in the processing station, the umbilicus 296 links the rotating processing chamber 18 with the cassette 28 without need for rotating seals. In a preferred embodiment, the umbilicus 296 is made from rotational-stress-resistant Hytrel® copolyester elastomers (DuPont). Further details of the construction of the umbilicus 296 will be provided later.
The tubes 290, 292, and 294 are coupled, respectively, to other cassette ports. The tube 290 conveys whole blood into the processing chamber 18. The tube 292 conveys plasma constituent from the processing chamber 18. The tube 294 conveys red blood cells from processing chamber 18.
A plasma collection reservoir 304 is coupled by a tube 302 to a cassette port. The collection reservoir 304 is intended, in use, to serve as a reservoir for the plasma constituent during processing prior to its return to the donor.
A red blood cell collection reservoir 308 is coupled by a tube 306 to a cassette port. The collection reservoir 308 is intended, in use, to receive red blood cells during processing. for storage.
Two red blood cell storage containers 307 and 309 are coupled by a tube 311 to another cassette port. A leukocyte reduction filter 313 is carried in line by the tube 311. During processing, red blood cells are transferred from the red blood cell collection reservoir 308 through the filter 313 into the storage containers 307 and 309.
A container 208 holding a red blood cell storage or additive solution is coupled via a tube 278 to another cassette port. The red blood cell storage solution is metered into the red blood cells as they are conveyed from the container 308, through the filter 313, into the storage containers 307 and 309. Further details of this aspect of the collection process will be described later.
A whole blood reservoir 312 is coupled by a tube 310 to a cassette port. The collection container 312 is intended, in use, to serve as a reservoir for whole blood during processing.
In the illustrated embodiment, the set 16 further includes a fixture 338 (see
As
The fixture 338 gathers the tubes 292 and 294 in a compact, organized, side-by-side array, to be placed and removed as a group in association with the sensing station 332. In the illustrated embodiment, the fixture 338 also holds the tube 290, which conveys whole blood into the processing chamber 18, even though no associated sensor is provided. The fixture 338 serves to gather and hold all tubes 290, 292, and 294 that are coupled to the umbilicus 296 in a compact and easily handled bundle.
The fixture 338 can be an integral part of the umbilicus 296, formed, e.g., by over molding. Alternatively, the fixture 338 can be a separately fabricated part, which snap fits about the tubes 290, 292, and 294 for use.
As
In the illustrated embodiment, the weigh station 238 comprises a series of container hangers/weigh sensors 246 arranged along the top of the lid 40. In use, the containers 304, 308, 312 are suspended on the hangers/weigh sensors 246.
The holding trays 212 comprise molded recesses in the base 38. The trays 212 accommodate the containers 276 (containing anticoagulant) and 208 (containing the red blood cell additive solution). In the illustrated embodiment, an additional swing-out side hanger 248 is also provided on the side of the lid 40. The hanger 248 (see
In the illustrated embodiment, the tray 212 holding the container 276 and the hanger 248 also include weigh sensors 246.
As blood or liquids are received into and/or dispensed from the containers during processing, the weigh sensors 246 provide output reflecting weight changes over time. This output is conveyed to the controller 16. The controller 16 processes the incremental weight changes to derive fluid processing volumes. The controller generates signals to control processing events based, in part, upon the derived processing volumes. Further details of the operation of the controller to control processing events can be found in Nayak et al, U.S. Pat. No. 6,261,065, which is incorporated herein by reference.
C. The Centrifugal Processing Chamber
In one arrangement, the chamber 18 can be fabricated in two separately molded pieces; namely (as
The top of the channel 126 is closed by the separately molded; flat lid 150 (which is shown separated in
All contours, ports, channels, and walls that affect the blood separation process may be preformed in the base 388 in a single, injection molded operation, during which molding mandrels are inserted and removed through the open end of the base 388 (shown in
The contours, ports, channels, and walls that are preformed in the base 388 may create surfaces within the base 388 that do not readily permit the insertion and removal of molding mandrels through a single end of the base 388. In this arrangement, the base 388 can be formed by separate molded parts, either by nesting cup shaped subassemblies or two symmetric halves.
Alternatively, molding mandrels can be inserted and removed from both ends of the base 388. In this arrangement (see
The contours, ports, channels, and walls that are preformed in the base 388 can vary.
As seen in
In this embodiment (as
Additional molded interior walls divide the region 134 into three passages 142, 144, and 146. The passages 142, 144, and 146 extend from the hub 120 and communicate with the channel 126 on opposite sides of the terminus wall 136. Blood and other fluids are directed from the hub 120 into and out of the channel 126 through these passages 142, 144, and 146.
The underside of the base 388 (see
The mount 178 is desirably made from a material that can withstand considerable flexing and twisting, to which the mount 178 can be subjected during use, e.g., Hytrel® 3078 copolyester elastomer (DuPont). The dimensions of the shaped receptacle 179 and the shaped mount 178 are preferably selected to provide a tight, dry press fit, to thereby avoid the need for solvent bonding or ultrasonic welding techniques between the mount 178 and the base 388 (which can therefore be formed from an incompatible material, such as ABS plastic).
D. The Centrifuge Assembly
The centrifuge station 20 (see
As illustrated (see
A rotor plate 166 (see
As
The configuration of the latching assembly 382 can vary. In the illustrated embodiment (see
In the retaining position (see
In the releasing position (see
In the illustrated embodiment, the latching assembly 382 includes a sliding pawl 72 carried in a radial track 74 on the top of the rotor plate. In the track 74, the pawl 72 slides radially toward and away from the latch arm 66.
When the latch arm 66 is in its retaining position and the pawl 72 is located in a radial position adjacent the latch arm 66 (see
A spring 80 within the pawl 72 normally biases the pawl 72 toward this radial position adjacent the latch arm 66, where engagement between the pawl finger 76 and latch arm cam recess 78 can occur. The latch arm 66 is thereby normally held by the pawl 72 in a locked, retaining position, to hold the processing chamber 18 during use.
The pawl 72 can be manually moved against the bias of the spring 80 radially away from its position adjacent the latch arm 66 (see
In the illustrated embodiment (see
As
The interference between the collar sidewall 84 and the key element 88 of the pawl 72 prevents manual movement of the pawl 72 away from the latch arm 66, to unlock the latch arm 66 for movement into its releasing position, unless the open region 86 and the key element 88 register. The open region 86 is aligned on the yoke 154 so that this registration between the open region 86 and the key element 88 occurs only when the rotor plate 166 is in a prescribed rotational position relative to the yoke 154. In this position (see
This arrangement makes possible a straightforward sequence of acts to load the processing chamber 18 for use and to unload the processing chamber 18 after use (see
A sheath 182 on the near end of the umbilicus 296 fits into a preformed, recessed pocket 184 in the centrifuge station 20. The pocket 184 holds the near end of the umbilicus 296 in a non□rotating stationary position aligned with the mutually aligned rotational axes 64 of the yoke 154 and rotor plate 166.
The preformed pocket 184 is also shaped to accommodate loading of the fixture 338 at the same time the sheath 182 is inserted. The tubes 290, 292, and 294 are thereby placed and removed as a group in association with the sensing station 332, which is located within the pocket 184.
Umbilicus support members 186 and 187 (see
As
The other member 187 receives the upper portion of the umbilicus 296. The member 187 includes a surface 190 against which the upper portion of the umbilicus 296 rests. The surface 190 forms a channel inclined toward the top wall 158 of the yoke 154. The surface 190 guides the upper portion of the umbilicus 296 toward the recessed pocket 184, which is located axially above the top wall 158 of the yoke 154, where the umbilicus sheath 182 and fixture 338 are fitted. Like the surface 188, the surface 190 inhibits travel of the upper portion of the umbilicus 296 in radial directions toward and away from the rotational axis 64. However, like the surface 188, the surface 190 permits rotation or twisting of the umbilicus 296 about its own axis.
Closing the centrifuge station door 20 positions a holding bracket 90 on the underside of the door 20 in registry with the sheath 182 (see
During operation of the centrifuge assembly 48 (see
The relative rotation of the yoke 154 at a one omega rotational speed and the rotor plate 166 at a two omega rotational speed, keeps the umbilicus 296 untwisted, avoiding the need for rotating seals. The illustrated arrangement also allows a single drive motor 164 to impart rotation, through the umbilicus 296, to the mutually rotating yoke 154 and processing chamber 18 carried on the rotor plate 166. Further details of this arrangement are disclosed in Brown et al U.S. Pat. No. 4,120,449, which is incorporated herein by reference.
The umbilicus 296 can stretch in response to the rotational forces it encounters. The dimensions of a given umbilicus 296 are also subject to normal manufacturing tolerances. These factors affect the flight radius of the umbilicus 296 during use; as well as the stress encountered by the mount 178 at the far end of the umbilicus 296, which serves as the two omega torque transmitter to drive the processing chamber 18; as well as the lateral loads acting on the centrifuge and motor bearings.
As
The support members 186 and 187 make possible a bearing-less umbilicus assembly with no moving parts, while leading to reduced stress at the two omega torque region, where stresses tend to be greatest. The surfaces 188 and 190 of the support members 186 and 187 can be formed and oriented to accommodate rotation of the umbilicus 296 and the driving of the processing chamber 18 in either clockwise or counterclockwise directions.
In the illustrated embodiment, the surfaces 188 and 190 of the support members 186 and 187 are preferably fabricated from a low friction material, to thereby eliminate the need for external lubrication or rotating bearings on the umbilicus 296 itself. The material used can, e.g., comprise Teflon® polytetrafluoroethylene material (DuPont) or an ultra high molecular weight polyethylene. Made from such materials, the surfaces 188 and 190 minimize umbilicus drive friction and the presence of particulate matter due to umbilicus wear.
In a representative embodiment (see
In this arrangement, the outside layer 98 of Hytrel® 3078 copolyester elastomer serves as a compatible interface to accommodate over-molding of the zero omega sheath 182 and the two omega mount 178, which may comprise the same Hytrel® 3078 material or an otherwise compatible material. Absent material compatibility, solvents (e.g., methylene chloride) or other forms of surface treatment may be required to facilitate a robust bond between these elements and the umbilicus. Hytrel® 3078 material is desired for the sheath 182, and the mount 178 because it can withstand considerable flexing and twisting forces, to which these regions of the umbilicus are subjected during use.
The core layer 96 of Hytrel® 4056 copolyester elastomer can be readily solvent bonded to conventional flexible medical grade polyvinyl tubing, from which the tubes 290, 292, and 294 are desirably made.
II. Double Red Blood Cell Collection ProcedureUse of the set 12 in association with the device 14 and controller 16 to conduct a typical double unit red blood cell collection procedure will now be described for illustrative purposes.
A. The Cassette
The cassette 28 used for a procedure of this type desirably includes dual pneumatic pump chambers PP3 and PP4 (see
The cassette 28 also desirably includes a pneumatic pump chamber PP5, which serves as a dedicated anticoagulant pump, to draw anticoagulant from the container 276 and meter the anticoagulant into the blood drawn from the donor.
The cassette 28 also desirably includes a pneumatic pump chamber PP1 that serves as a dedicated in-process whole blood pump, to convey whole blood from the reservoir 312 into the processing chamber 18. The dedicated function of the pump chamber PP1 frees the donor interface pump chambers PP3 and PP4 from the added function of supplying whole blood to the processing chamber 18. Thus, the in-process whole blood pump chamber PP1 can maintain a continuous supply of blood to the processing chamber 18, while the donor interface pump chambers PP3 and PP4 operate in tandem to simultaneously draw and return blood to the donor through the single phlebotomy needle. Processing time is thereby minimized.
The cassette 28 also desirably includes a pneumatic pump chamber PP2 that serves as a plasma pump, to convey plasma from the processing chamber 18. The ability to dedicate separate pumping functions provides a continuous flow of blood into and out of the processing chamber 18, as well as to and from the donor.
B. Capacitive Flow Sensing
The controller 16 desirably includes means for monitoring fluid flow through the pump chambers PP1 to PP5. In the illustrated embodiment, the pump and valve station 30 carries electrode circuits 206 associated with each pump chamber PP1 to PP5. The electrode circuits 206 can be located, e.g., within the pneumatic actuator ports 204 in the pump and valve station 30 (see
The passage of electrical energy through each electrode circuit 206 creates an electrical field within the respective pump chamber PP1 to PP5. Cyclic deflection of the diaphragm associated with a given pump chamber to draw fluid into and expel fluid from the pump chamber PP1 to PP5 changes the electrical field, resulting in a change in total capacitance of the circuit through the electrode. Capacitance increases as fluid is draw into the pump chamber PP1 to PP5, and capacitance decreases as fluid is expelled from pump chamber PP1 to PP5.
In the arrangement, the electrode circuits 206 each includes a capacitive sensor (e.g., a Qprox E2S). The capacitive sensor registers changes in capacitance for the electrode circuit 206 for each pump chamber PP1 to PP5. The capacitance signal for a given electrode circuit 206 has a high signal magnitude when the pump chamber is filled with liquid, has a low signal magnitude signal when the pump chamber is empty of fluid, and has a range of intermediate signal magnitudes when the diaphragm occupies intermediate positions.
At the outset of a blood processing procedure, the controller 16 can calibrate the difference between the high and low signal magnitudes for each sensor to the maximum stroke volume of the respective pump chamber. The controller 16 can then relate the difference between sensed maximum and minimum signal values during subsequent draw and expel cycles to fluid volume drawn and expelled through the pump chamber. The controller 16 can sum the fluid volumes pumped over a sample time period to yield an actual flow rate.
The controller 16 can compare the actual flow rate to a desired flow rate. If a deviance exists, the controller 16 can vary pneumatic pressure pulses delivered to the actuators for the pump chambers PP1 to PP5 to minimize the deviance.
The controller 16 can also operate to detect abnormal operating conditions based upon the variations in the electric field and to generate corresponding alarm outputs. The controller 16 can, e.g., monitor for an increase in the magnitude of the low signal magnitude over time. The increase in magnitude reflects the presence of air inside a pump chamber.
For example, the controller 16 can generate a derivative of the signal output of the sensor 426. Changes in the derivative, or the absence of a derivative, reflects a partial or complete occlusion of flow through the pump chamber PP1 to PP5. The derivative itself also varies in a distinct fashion depending upon whether the occlusion occurs at the inlet or outlet of the pump chamber PP1 to PP5.
1. Monitoring Vein Flow Conditions
By using capacitive sensing and by also counting pump strokes (i.e., the application of negative pressure upon the diaphragm of a given pump chamber to draw fluid into the chamber), the controller 16 can also monitor vein flow conditions, and, in particular, assess and respond to real or potential vein occlusion conditions.
When blood is pumped from the donor, the donor's vein may show difficulties in keeping up with the commanded draw rate that operation of the donor pump chambers PP3/PP4 imposes. In the case of restricted blood flow from the donor, the donor pumps PP3 and PP4 do not fill properly in response to the commanded sequence of pump strokes. The controller 16 attempts to assess and mediate blood supply interruptions due to vein problems before generating a vein occlusion alarm, which suspends processing.
For example, the controller 16 can count the number of consecutive attempted pump strokes for which no blood flow into the pump chambers PP3 and PP4 occurs (which blood flow or absence of blood flow can be detected by capacitive sensing, as above described). A potential donor draw occlusion condition can be deemed to occur when a prescribed number (e.g., 3) of consecutive incomplete fill donor pump strokes takes place.
When a potential donor draw occlusion condition is detected, the controller 16 attempts to rectify the condition by increasing pressure of the pressure cuff 58 and/or decreasing the commanded draw rate, before generating a processing-halting vein occlusion alarm.
More particularly, in a representative implementation, when a donor draw occlusion condition is detected, the controller 16 executes a potential draw occlusion condition function (in shorthand, the “Potential Occlusion Function”). The Potential Occlusion Function first suspends the draw for a period of time (e.g. upwards to 20 seconds, and desirably about 10 seconds) to rest the vein. While the vein rests, the controller 16 also increases the pressure cuff pressure by a preset increment (e.g., upwards to 25 mmHg, and desirably about 10 mmHg), unless cuff pressure, when adjusted, exceeds a prescribed maximum (e.g., upwards to 100 mmHg, desirably about 70 mmHg). If the prescribed maximum cuff pressure condition exists, no incremental changes to the cuff pressure are made during the prescribed vein rest interval.
After the prescribed vein rest interval, the Potential Occlusion Function resets the attempted pump stroke counter to zero and resumes the draw cycle. The controller 16 monitors the initial series of consecutive pump strokes during the resumed draw cycle, up to a first threshold number of pump strokes (e.g., 5). The magnitude of the first threshold number is larger that the number of consecutive incomplete fill donor pump strokes (i.e., 3) that indicate a potential donor draw occlusion condition. The magnitude of the first threshold number is selected to accurate assess, after a potential donor draw occlusion condition arises, whether a true donor draw occlusion exists. In the illustrated embodiment, if within the first five pump strokes (or whatever the first threshold number is), three consecutive incomplete fill donor pump strokes take place, the controller 16 assumes that a true donor draw occlusion exists, and thus generates an occlusion alarm. With the generation of an occlusion alarm, the controller 16 suspends processing, until the operator can establish that it is safe to resume.
If within the first threshold number of pump strokes, three consecutive incomplete fill donor pump strokes do not take place, the controller 16 assumes that a true vein occlusion may not exists and that the potential occluded flow condition was either transient, or at least capable of correction short of suspending the procedure. In this event, the Potential Occlusion Function allows the resumed draw cycle to continue beyond the first threshold number of pump strokes up to a second threshold number of pump strokes (e.g., 20 to 100, and desirable about 50).
If at any time between the first threshold number of pump strokes and the second threshold number of pump strokes, three consecutive incomplete fill donor pump strokes take place, the Potential Occlusion Function institutes another vein rest interval (e.g. upwards to 20 seconds, and desirably about 10 seconds). While the vein rests, the Potential Occlusion Function also again increases the pressure cuff pressure by a preset increment (e.g., upwards to 25 mmHg, and desirably about 10 mmHg). While the vein rests, the Potential Occlusion Function also lowers the draw rate by a preset decrement (e.g., upwards to 20 ml/min, and desirably about 10 ml/min). If the draw rate, when lowered, is less than a prescribed minimum draw rate (e.g., 70 to 90 ml/min), the controller 16 generates an occlusion alarm. Otherwise, the Potential Occlusion Function resets the attempted pump stroke counter to zero, and resumes the draw cycle at the increased cuff pressure and decreased draw rate.
The controller 16 again monitors the initial series of consecutive pump strokes during the resumed draw cycle, up to the first threshold number of pump strokes (e.g., 5). If within the first threshold number of pump strokes, three consecutive incomplete fill donor pump strokes take place, the controller 16 assumes that a true donor draw occlusion exists, and thus generates an occlusion alarm and also suspends processing.
However, if within the first threshold number of pump strokes, three consecutive incomplete fill donor pump strokes do not take place, the controller 16 allows the resumed draw cycle to continue beyond the first threshold number of pump strokes up to the second threshold number of pump strokes (e.g., 20 to 100, and desirable about 50). If at any time between the first threshold number of pump strokes and the second threshold number of pump strokes, three consecutive incomplete fill donor pump strokes take place, the Potential Occlusion Function again institutes another vein rest interval (e.g. upwards to 20 seconds, and desirably about 10 seconds). While the vein rests, the Potential Occlusion Function also again increases the pressure cuff pressure by a preset increment (e.g., upwards to 25 mmHg, and desirably about 10 mmHg). While the vein rests, the Potential Occlusion Function also again lowers the draw rate by a preset decrement (e.g., upwards to 20 ml/min, and desirably about 10 ml/min), unless the draw rate, when lowered, is less than a prescribed minimum draw rate (e.g., 70 to 90 ml/min), in which case the controller 16 generates an occlusion alarm. Otherwise, the Potential Occlusion Function resets the attempted pump stroke counter to zero, and resumes the draw cycle at the increased cuff pressure and decreased draw rate.
The controller 16 continues to repeat the steps of the Potential Occlusion Function, using the first and second pump stroke number thresholds to gage whether a true vein occlusion exists, and either generating an occlusion alarm if it does, or continuing to attempt remedial action (by increasing cuff pressure and/or decreasing draw rate), or cancelling the potential donor draw occlusion condition when three consecutive incomplete fill donor pump strokes are not observed during either the first or second threshold periods following a potential donor occlusion condition.
If no three consecutive incomplete fill donor pump strokes take place within the second threshold number of strokes following a potential donor draw occlusion condition, the controller 16 assumes that a true vein occlusion does not exist. The draw cycle continues, and the controller 16 continues to count pump strokes. If the prescribed number (e.g., 3) of consecutive incomplete fill donor pump strokes subsequently takes place, the controller 16 assumes that this event is unrelated to any previous occlusion event condition, and generates a new potential donor draw occlusion condition, executing the Potential Occlusion Function from the start.
It should be appreciated that the Potential Occlusion Function, as just described, can be used with any blood processing device that has means for detecting when a draw blood pumping command does not result in blood flow through the pump.
C. Blood Processing Cycles
Prior to undertaking the double unit red blood cell collection procedure, as well as any blood collection procedure, the controller 16 conducts an appropriate integrity check of the cassette 28, to determine whether there are any leaks in the cassette 28. Once the cassette integrity check is complete and no leaks are found, the controller 16 begins the desired blood collection procedure.
In general, using the processing chamber shown in
The whole blood separates as a result of centrifugal forces. Red blood cells are driven toward the high□G wall 124, while lighter plasma constituent is displaced toward the low□G wall 122. In this flow pattern, a dam 384 projects into the channel 126 toward the high-G wall 124. The dam 384 prevents passage of plasma, while allowing passage of red blood cells into a channel 386 recessed in the high-G wall 124. The channel 386 directs the red blood cells into the umbilicus 296 through the radial passage 144. The plasma constituent is conveyed from the channel 126 through the radial passage 142 into umbilicus 296.
1. Collection Cycle
During a typical collection cycle of the double unit red blood cell collection procedure, whole blood drawn from the donor is processed to collect two units of red blood cells, while returning plasma to the donor. The donor interface pumps PP3/PP4 in the cassette, the anticoagulant pump PS in the cassette, the in-process pump PP1 in the cassette, and the plasma pump PP2 in the cassette are pneumatically driven by the controller 16, in conjunction with associated pneumatic valves, to draw anticoagulated blood into the in-process container 312, while conveying the blood from the in-process container 312 into the processing chamber 18 for separation. This arrangement also removes plasma from the processing chamber into the plasma container 304, while removing red blood cells from the processing chamber into the red blood cell container 308. This phase continues until an incremental volume of plasma is collected in the plasma collection container 304 (as monitored by a weigh sensor) or until a targeted volume of red blood cells is collected in the red blood cell collection container (as monitored by a weigh sensor).
If the volume of whole blood in the in-process container 312 reaches a predetermined maximum threshold before the targeted volume of either plasma or red blood cells is collected, the controller 16 terminates operation of the donor interface pumps PP3/PP4 to terminate collection of whole blood in the in-process container 312, while still continuing blood separation. If the volume of whole blood reaches a predetermined minimum threshold in the in-process container 312 during blood separation, but before the targeted volume of either plasma or red blood cells is collected, the controller 16 returns to drawing whole blood to thereby allow whole blood to enter the in-process container 312. The controller toggles between these two conditions according to the high and low volume thresholds for the in-process container 312, until the requisite volume of plasma has been collected, or until the target volume of red blood cells has been collected, whichever occurs first.
2. Return Cycle
During a typical return cycle (when the targeted volume of red blood cells has not been collected), the controller 16 operates the donor interface pumps PP3/PP4 within the cassette 28, the in-process pump PP1 within the cassette, and the plasma pump PP2 within the cassette, in conjunction with associated pneumatic valves, to convey anticoagulated whole blood from the in-process container 312 into the processing chamber 18 for separation, while removing plasma into the plasma container 304 and red blood cells into the red blood cell container 308. This arrangement also conveys plasma from the plasma container 304 to the donor, while also mixing saline from the container 288 in line with the returned plasma. The in line mixing of saline with plasma raises the saline temperature and improves donor comfort. This phase continues until the plasma container 304 is empty, as monitored by the weigh sensor.
If the volume of whole blood in the in-process container 312 reaches a specified low threshold before the plasma container 304 empties, the controller 16 terminates operation of the in-process pump PP1 to terminate blood separation. The phase continues until the plasma container 304 empties.
Upon emptying the plasma container 304, the controller 16 conducts another collection cycle. The controller 16 operates in successive collection and return cycles until the weigh sensor indicates that a desired volume of red blood cells have been collected in the red blood cell collection container 308. The controller 16 terminates the supply and removal of blood to and from the processing chamber, while operating the donor interface pumps PP3/PP4 in the cassette 28 to convey plasma remaining in the plasma container 304 to the donor. The controller 16 next operates the donor interface pumps PP3/PP4 in the cassette to convey the blood contents remaining in the in-process container 312 to the donor as well as convey saline to the donor, until a prescribed replacement volume amount is infused, as monitored by a weigh sensor.
3. In-Line Leukofiltration Cycle
When the collection of red blood cells and the return of plasma and residual blood components has been completed, the controller 16 switches, either automatically or after prompting the operator, to an in-line leukofiltration cycle. During this cycle, red blood cells are removed from the red blood cell collection reservoir 308 and conveyed into the red blood cell storage containers 307 and 308 through the leukocyte removal filter 313. At the same time, a desired volume of red blood cell storage solution from the container 208 is mixed with the red blood cells.
In the first stage of this cycle, the controller 16 operates donor interface pumps PP3/PP4 in the cassette to draw air from the red blood cell storage containers 307 and 309, the filter 313, and the line 311, and to transfer this air into the red blood cell collection reservoir 308. This stage minimizes the volume of air residing in the red blood cell storage containers 307 and 309 before the leukocyte removal process begins. The stage also provides a volume of air in the red blood cell collection container 308 that can be used purge red blood cells from the filter 313 into the red blood cell collection containers 307 and 309 once the leukocyte removal process is completed.
In the next stage, the controller 16 operates the donor interface pumps PP3/PP4 in the cassette 28 to draw a priming volume of storage solution from the solution container 208 into the red blood cell collection reservoir 308. This stage primes the tubing 278 between the container 208 and the cassette 28, to minimize the volume of air pumped into the final red blood cell storage containers 307 and 309.
In the next stage, the controller 16 operates the donor interface pumps PP3/PP4 in the cassette 28 to alternate pumping red blood cells from the red blood cell collection reservoir 308 into the red blood cell collection containers 307 and 309 (through the filter 313), with pumping of red blood cell storage solution from the container 208 into the red blood cell collection containers 307 and 309 (also through the filter 313). This alternating process mixes the storage solution with the red blood cells. The controller 16 counts the pneumatic pump strokes for red blood cells and the storage solution to obtain a desired ratio of red cell volume to storage solution volume (e.g., five pump strokes for red blood cells, followed by two pump strokes for storage solution, and repeating the alternating sequence). This alternating supply of red blood cells and storage solution continues until the weigh scale for the red blood cell collection reservoir 308 indicates that the reservoir 308 is empty.
When the red blood cell collection reservoir 308 is empty, the controller 16 operates the donor interface pumps PP3/PP4 to pump additional storage solution through the filter 313 and into the red blood storage containers 307 and 309, to ensure that a desired ratio between storage solution volume and red blood cell volume exists.
This also rinses residual red blood cells from the filter 313 into the red blood cell storage containers 307 and 309 to maximize post-filtration percent red blood cell recovery.
The controlled ratio of pump strokes for red blood cells and for storage solution that the controller 16 achieves ensures that the storage solution is always metered in at a constant ratio. Therefore, regardless of the volume of red blood cells collected, the final red blood cell/storage solution hematocrit can be constant.
The alternating supply of red blood cells and storage solution through the filter 313 eliminates the need to first drain the storage solution into the red blood cell collection reservoir 308, which lessens the overall procedure time.
The alternating supply of red blood cells and storage solution through the filter 313 also eliminates the need to manually agitate a red blood cell/storage solution mixture prior to leukofiltration. Due to density differences, when concentrated red blood cells are added to a preservation solution, or vice versa, the preservation solution floats to the top. Poorly mixed, high hematocrit, high viscosity red blood cells lead to reduced flow rates during leukofiltration. Poorly mixed, high hematocrit, high viscosity red blood cell conditions can also lead to hemolysis. By alternating passage of red blood cells and storage solution through the filter 313, mixing occurs automatically without operator involvement.
The alternating supply of red blood cells and storage solution through the filter 313 also eliminates the need to gravity drain the red blood cell product through the leukofilter 313. As a result, filtration can occur in about half the time required for a gravity-drain procedure.
If desired, the controller 16 can monitor weight changes relating to the red blood cell collection reservoir 308 and the red blood cell storage containers 307 and 309, to derive a value reflecting the percent of red blood cells that are recovered after passage through the leukofilter 313. This value can be communicated to the operator, e.g., on the display screen of user the user interface.
The following expression can be used to derive the percent recovery value:
% Recovery=[(Bag A Vol+Bag B Vol)/RBC Vol+Adsol)]*100
where:
Bag A Vol represents the volume of red blood cells collected the container 307, calculated as follows:
(Wt of Container 307 containing red blood cells(in g)−Container 307 Tare)/1.062 g/ml
Bag B Vol represents the volume of red blood cells collected the container 309, calculated as follows:
(Wt of Container 309 containing red blood cells(in g)−Container 309 Tare)/1.062 g/ml
RBC Vol represents the volume of red blood cells collected in the red blood cell collection reservoir 308, which the controller 16 determines by weight sensing at the end of the procedure.
Adsol represents the volume of red blood cell storage solution added to the during leukofiltration, which is determined by the controller 16 by capacitive sensing during processing.
a. The Leukofilter
The leukofilter 313 can be variously constructed. In the embodiment illustrated in
The housing 100 can comprise rigid plastic plates sealed about their peripheries. In the illustrated embodiment, the housing 100 comprises first and second flexible sheets 104 of medical grade plastic material, such as polyvinyl chloride plasticized with di-2-ethylhexyl-phthalate (PVC-DEHP). Other medical grade plastic materials can be used that are not PVC and/or are DEHP-free.
In the illustrated embodiment, a unitary, continuous peripheral seal 106 (see
The filter 313 also includes inlet and outlet ports 108. The ports 108 can comprise tubes made of medical grade plastic material, like PVC-DEHP. In the embodiment shown in
In the illustrated embodiment (as
The fixture 110 can take various forms. In the illustrated embodiment, the fixture 110 comprises two plates 112 coupled by a hinge 114. The fixture 110 can be placed in an open condition (as
The plates 112 maintain a desired gap clearance, thereby restraining expansion of the filter 313 during use. The gap clearance is selected to maintain a desired blood flow rate at a desired minimum blood volume.
The plates 112 desirably include indentations 118 in which the ports 108 of the filter 313 rest in a non-occluded condition when the fixture 110 is closed. The interior surfaces of the plates 112 may be roughed or scored with a finish to aid blood flow through the filter 313 when the fixture 110 is closed.
The fixture 110 can be made as a stand-alone item that can be separately stored prior to use. It can be stored in association with the device 14 during transport and prior to use, e.g., in a receptacle 128 formed on the exterior of the lid 40 of the device 14 (see
It should be appreciated that pump-assisted leukofiltration of red blood cells, whole blood, or other blood cell products, wherein blood flow through a leukofilter is not driven strictly by gravity flow, can be carried out using manual or automated systems having configurations different than those shown in this Specification. For example, external peristaltic or fluid actuated pumping devices can be used to transfer whole blood or manually processed blood products from separation bags into processing or storage containers through intermediate leukofiltration devices. It should also be appreciated that a filter restraining fixture of the type shown in
The many features of the invention have been demonstrated by describing their use in separating whole blood into component parts for storage and blood component therapy. This is because the invention is well adapted for use in carrying out these blood processing procedures. It should be appreciated, however, that the features of the invention equally lend themselves to use in other blood processing procedures.
For example, the systems and methods described, which make use of a programmable cassette in association with a blood processing chamber, can be used for the purpose of washing or salvaging blood cells during surgery, or for the purpose of conducting therapeutic plasma exchange, or in any other procedure where blood is circulated in an extracorporeal path for treatment.
Features of the invention are set forth in the following claims.
Claims
1-8. (canceled)
9. A blood processing system comprising
- a blood processing set including a source of blood cells, and a blood component collection flow channel coupled to the source of blood cells including a blood cell storage container and an in-line filter to remove leukocytes from the blood cells before entering the blood cell storage container, the in-line filter including a leukocyte removal filter medium and first and second flexible housings, wherein the flexible housings are comprised of DEHP-free plastic material, and
- a pump station adapted to be placed into communication with the blood component collection flow channel to pump blood into the blood cell storage container through the in-line filter.
10. The blood processing system of claim 9 wherein said leukocyte removal filter medium comprises a plurality of layers.
11. The blood processing system of claim 9 wherein said leukocyte removal filter medium comprises a leukocyte-exclusion filter medium including a membrane.
12. The blood processing system of claim 9 wherein said leukocyte removal filter medium comprises a depth filtration filter comprising a fibrous filter medium.
13. In a method of filtering a liquid using a filter comprising a flexible housing having an inlet port and outlet port for the liquid and a sheet-like filter element for removing undesired components from the liquid, with the inlet port being separated from the outlet port by the filter element, a method characterized by maintaining the pressure at the outlet side of the filter at a positive pressure above atmospheric pressure by controlling a feed rate per unit time of a feed pump installed in an upstream flow channel of the filter.
14. The method according to claim 13, wherein the filter does not comprise a spacer for securing a flow channel at the outlet side of the filter.
15. The method according to claim 13 or claim 14 wherein a filter of which the outlet side flexible housing has not been processed to provide irregularity as a spacer for securing a flow channel at the filter outlet side and/or a filter in which a tube is not inserted between the outlet side flexible housing and the sheet-like filter as a spacer for securing a flow channel at the filter outlet side are/is used.
16. The method according to claim 13, wherein the liquid to be filtered is blood.
17. The method according to claim 14, wherein the liquid to be filtered is blood.
18. The method according to claim 15, wherein the liquid to be filtered is blood.
19. The method according to claim 16, wherein the liquid to be filtered is blood.
20. The method according to claim 17, wherein the filter is used for removal of leukocytes.
21. The method according to claim 18, wherein the filter is used for removal of leukocytes.
22. In a filtering system for a liquid comprising a filter comprising a flexible housing having an inlet port and outlet port for the liquid, a sheet-like filter element for removing undesired components from the liquid, with the liquid inlet port and the outlet port separated from each other by the filter element, an upstream side flow channel connected to the filter inlet port, a filtered liquid recovery bag, a downstream side flow channel connecting the filter outlet port with the recovery bag, and a feed pump installed in the upstream side flow channel, a filtering system wherein the feed rate per unit time of a feed pump installed in an upstream flow channel of the filter can be controlled so that the pressure at the outlet side of the filter is maintained at a positive pressure above atmospheric pressure.
23. The system according to claim 22 comprising the filter without a spacer for securing a flow channel at the outlet side of the filter.
24. The system according to claim 22 or claim 23, wherein a filter of which the outlet side flexible housing has not been processed to provide irregularity as a spacer for securing a flow channel at the filter outlet port and/or a filter in which a tube is not inserted between the outlet side flexible housing and the sheet-like filter as a spacer for securing a flow channel at the filter outlet side are/is used.
25. The system according to claim 22, wherein the liquid to be filtered is blood.
26. The system according to claim 23, wherein the liquid to be filtered is blood.
27. The system according to claim 24, wherein the liquid to be filtered is blood.
28. The system according to claim 25, wherein the filter is used for removal of leukocytes.
29. The system according to claim 26, wherein the filter is used for removal of leukocytes.
30. The system according to claim 27, wherein the filter is used for removal of leukocytes.
31. A liquid filtering method using the system according to claim 22.
32. A liquid filtering method using the system according to claim 23.
33. A liquid filtering method using the system according to claim 24.
34. A liquid filtering method using the system according to claim 25.
35. A liquid filtering method using the system according to claim 26.
36. A liquid filtering method using the system according to claim 27.
37. A liquid filtering method using the system according to claim 28.
38. A liquid filtering method using the system according to claim 29.
39. A liquid filtering method using the system according to claim 30.
40. In a method of filtering blood or blood components using a filter comprising a flexible housing having an inlet port and outlet port, said inlet port being separated from the outlet port by a sheet-like filter element, said sheet-like filter element removing undesired elements from the blood, the method including:
- connecting the inlet port to a source of blood or blood components;
- connecting the outlet port to a container;
- pumping the blood from the source to the filter by a pump station communicating with a blood or blood component flow channel;
- adjusting at least one filtration parameter so that a pressure at an outlet side of the filter is above atmospheric pressure;
- maintaining a pressure at the outlet side of the filter above atmospheric pressure throughout filtration by adjusting said at least one filtration parameter; and
- collecting filtered blood or blood components in the container.
41. The method according to claim 40 wherein the pressure at the outlet side of the filter is maintained above atmospheric pressure by controlling a feed rate per unit time of a feed pump installed in an upstream flow channel of the filter.
42. The method according to claim 40 wherein the pressure at the outlet side of the filter is maintained above atmospheric pressure by restraining expansion of the inlet side flexible housing and the outlet side flexible housing by contacting an outer surface of each of said flexible housings with a separate restraining structure to restrain the outward expansion of said flexible housings under pressure applied during operation of a feed pump.
43. The method according to claim 40, wherein the filter does not comprise a spacer for securing a flow channel at the outlet side of the filter.
44. The method according to claim 40 wherein a filter of which the outlet side flexible housing has not been processed to provide irregularity as a spacer for securing a flow channel at the filter outlet side and/or a filter in which a tube is not inserted between the outlet side flexible housing and the sheet-like filter as a spacer for securing a flow channel at the filter outlet side are/is used.
45. The method according to claim 40, wherein the filter is used for removal of leukocytes.
Type: Application
Filed: Feb 25, 2009
Publication Date: Aug 6, 2009
Applicant: Baxter International Inc. (Deerfield, IL)
Inventors: Mark R. Vandlik (Hawthorn Woods, IL), Michael J Kast (Evanston, IL), Kelly B. Smith (Stroudsburg, PA), Tom Westberg (Gurnee, IL), Rohit Vishnoi (Deerfield, IL)
Application Number: 12/392,769
International Classification: A61M 1/36 (20060101); B01D 61/30 (20060101);