referring to fig1 a schematic representation of a liver assist system 5 includes a conduit 6 made of disposable plastic tubing ( e . g ., pvc ) for circulating plasma through a bioartificial liver ( bal ) device 8 which contains liver cells . conduit 6 may include sections of tubing ( 11 , 13 , 70 , 74 ) used to connect liver assist system 5 to an external system , such as a plasma separation machine 100 . connected within conduit 6 , in a series arrangement , are a peristaltic pump 14 , optional charcoal filters 16 , 18 , an oxygenator / heat exchange unit 20 , the bal device 8 , and a reservoir bag 28 , each of which will be discussed in greater detail below . liver assist system 5 , in use , supports approximately 650 ml of fluid with about 120 ml disposed within conduit 6 . prior to introducing the plasma to liver assist system 5 , saline ( or other suitable fluid ) is used to entirely fill conduit 6 as well as the components of the system . reservoir bag 28 is also filled sufficiently to provide a buffer for incoming fluid and indicates when liver assist system is entirely filled and primed . this process is part of a cleansing process in which the system is rinsed and primed using a method described below . in general , plasma is provided to the liver assist system 5 at an in - port 10 via tubing 11 and is pumped through the system using pump 14 in the direction indicated by arrows . filters 16 , 18 prefilter the plasma of toxins while oxygenator / heat exchange unit 20 oxygenates and maintains the temperature of the plasma within a predetermined temperature range . the plasma is then received by the bal device 8 that has been seeded with liver cells which remove toxins from the plasma . the reservoir bag 28 receives the treated plasma before being recirculated back through the system . liver assist system 5 is generally used in conjunction with a cell inoculation device 200 ( described below ) which provides liver cells to the bal device . the liver cells remove or modify toxic substances from the plasma . in fig1 liver assist system 5 is shown as part of an on - line system that is connected to an external system ( e . g ., plasma separation machine 100 ) which supplies plasma to the liver assist system for treatment . the plasma from plasma separation machine 100 is provided to conduit 6 from tubing 11 and returned from liver assist system 5 via tubing 13 . the plasma separation machine 100 shown in fig1 separates plasma to be treated from whole blood of a human patient . in other on - line applications , the external system may be a patient and the whole blood of the patient is circulated and bioprocessed in liver assist system 5 . it is also important to note that liver assist system 5 may be used in an off - line operation in which a source of plasma to be treated is provided , for example , in a bag and connected to an in - port 10 of the liver assist system 5 . in this case , the untreated plasma is allowed to circulate through the liver assist system to be detoxified and then dispensed at an out - port of the system . disposed within the conduit 6 is pump 14 , which provide sufficient drive to force the plasma from tubing 11 to flow through the conduit 6 in the direction indicated by arrows . the plasma flows at a user selectable flow rate between 50 and 1000 ml / min , nominally 400 ml / min . the system optionally includes a pair of charcoal filters 16 , 18 for pre - filtering the plasma before it is provided to the bal device 8 . only one of the filters is in use at any given time , the other being available to allow continued use of the system when one of the filters needs to be replaced . clamps ( not shown ) are used to allow and / or restrict flow through one or the other of the filters . either of the charcoal filters 16 or 18 may be replaced with a length of tube 17 or 19 to provide a bypass path around the charcoal filter when system 5 is in use . plasma from the filters passes to oxygenator / heat exchange unit 20 having an oxygenator 22 which supplies oxygen to the plasma and a heater 24 . oxygenator 22 receives , at inlet 22a , pressurized sterile gas ( e . g ., 30 % o 2 , 5 % co 2 , 65 % n 2 ) from an external gas source ( not shown ). the plasma passes through semi - permeable hollow fibers disposed within the oxygenator 22 to collect oxygen needed by the liver cells inoculated within bal device 8 . an optional oxygen measurement system may be used to measure the difference between the oxygen content of the plasma entering and exiting bal device 8 to provide an indication of the effectiveness of the bal device . the pressurized gas provided to the oxygenator passes through hydrophobic membranes disposed respectively at inlet 22a and outlet 22b . plasma flowing through heater 24 is maintained at a predetermined temperature ( e . g ., 37 ° c .) by heat conduction as it flows past a heat exchanger within the oxygenator . heated water from an external water heater / recirculator ( not shown ) is received at inlet 24a of the heater and returned via outlet 24b for reheating . a bypass line 25 with a clamp ( not shown ) is provided to bypass oxygenator / heat exchange unit 20 and through the system to allow the cleaning or replacement of the oxygenator / heat exchange unit 20 . plasma from oxygenator / heat exchange unit 20 is received by the bioartificial liver device 8 ( e . g ., a replaceable hollow fiber cartridge inoculated with cells ). bal device 8 includes a bundle of hollow fibers . in one embodiment , the fibers are inoculated with liver cells so that toxic substances within the plasma are removed as the plasma passes between the fibers . alternatively , the plasma can pass along the axial length of the fibers with the liver cells introduced between the fibers . a bypass line 26 having a manual clamp is provided to bypass the bal device 8 , for example , when the bal device requires replacement , maintenance , or cleansing ( described below ). during operation of liver assist system 5 , tubing 29 attached to waste bags 31 , 33 ( described below ), is closed off from flow of plasma with pinch valve 27 . the treated plasma is then conveyed to the plasma reservoir bag 28 before being recirculated through the system with a portion also being returned to the plasma separation machine 100 . referring to fig2 reservoir bag 28 is made of a strong and pliable material , such as pvc plastic . reservoir bag 28 includes an inlet 30 and a pair of outlets 32 , 34 at the lower end of the bag . outlet 32 provides fluid back to bal device 8 for further treatment , while outlet 34 leads to the plasma separation machine 100 . a dividing partition 36 between inlet 30 and outlets 32 , 34 define a pair of compartments 38 , 40 . compartment 38 provides an inlet channel and compartment 40 provides an overflow reservoir for holding a volume ( e . g ., 100 ml ) of fluid . dividing partition 36 between compartments 38 , 40 ensures that particulate matter which may be in the plasma is trapped in compartment 38 and prevented from returning to the liver assist system 5 where it may cause clogging of conduit 6 and the components of the system . due to the increased cross - sectional area of compartment 38 ( with respect to the cross - sectional area of inlet 30 ), the velocity of the plasma entering reservoir bag 28 decreases . thus , the particulate matter is allowed to settle in the lower portion of compartment 38 . the plasma overflowing into compartment 40 is temporarily held before being recirculated to the liver assist system 5 or plasma separation system 100 . reservoir bag 28 also serves to accommodate surging of the plasma . reservoir bag 28 may include multiple compartments between inlet 30 and outlets 32 , 34 so that the particulate matter will settle in the bottom portions of each compartment as the plasma overflows from one compartment to the next . a vent 48 is provided at the top of reservoir bag 28 by a tube 50 which extends to a filter 52 ( e . g ., 0 . 2 micron ). vent 48 allows gas within the plasma , in the form of bubbles , to escape . one approach for forming reservoir bag 28 is to overlay two sheets of pvc plastic cut in the shape of the bag . rf energy is then applied to the periphery of the sheets to provide an air - tight edge 42 to the bag . support seams 44 , along the top portion of bag 28 , are provided where holes are punched for allowing the bag to be hung from a support . an additional support seam 45 at the side of the bag is provided along one side of bag 28 so that compartment 40 defines a reservoir of sufficient depth . support seams 44 and 45 , as well as dividing partition 36 , are formed also using the rf heat - sealing technique . the level of plasma in reservoir bag 28 can be visually observed by the operator of the system who can manually release or restrict flow of the plasma from the bag to maintain a proper level of plasma in the bag , for example , using line 15 . the level can also be maintained using an electronic device which controls pump 14 of the liver assist system and / or a pump of the plasma separation machine 100 . an optional filter 9 with a bypass 12 may be included within tubing 70 for filtering particulate matter from the plasma returning to the external system . filter 9 serves to capture and prevent the circulation of cells released into conduit 6 in the event of a catastrophic failure of the hollow fibers in bal device 8 . bypass 12 provides a flow path for the plasma if filter 9 becomes clogged or needs replacement . liver assist system 5 can also be used in a closed , off - line system operation , with reservoir bag 28 serving as the source of the plasma being introduced to the system . in this case , reservoir bag will generally be larger in size , for example , 2 liters . referring to the lower right inset of fig1 and fig3 a cell inoculation device 200 includes a flexible seeding bag 202 formed of plastic ( e . g . pvc ) in which harvested liver cells to be inoculated in the bal device 8 are held . cell inoculation device 200 includes an inlet 212 through which cell suspension is dispensed within seeding bag 202 and an outlet 206 which can be connected , for example , to an inlet tube 60 of the liver assist system 5 ( fig1 ). outlet 206 is connected to a tube 208 which extends to the bottom portion of seeding bag 202 to maximize the removal of cell suspension . the seeding bag 202 is easily attached / detached from liver assist system 5 and is also a convenient receptacle for transporting the cells . the liver cells are removed from seeding bag 202 into bal device 8 using a pressure mechanism device 210 attached to cell inoculation device 200 . in one embodiment , pressure mechanism device 210 may be a pressure cuff which is wrapped around seeding bag 202 . upon manual or automatic actuation , positive pressure is provided within the bag causing the cells to rise through tube 208 and out of outlet 206 . in another embodiment , a pressurized gas source may be used to provide positive pressure via inlet hose 204 to the inside of the bag causing the cells to rise through tube 208 . in still a further embodiment , the cells can be extracted from the bag by attaching a pump to outlet 206 of tube 208 to pump the cells out of the bag . a rinsing tube 214 is provided at the top of bag 202 for introducing a rinsing solution ( e . g ., saline ) to ensure the removal of residual cells that may settle within the bottom of bag . referring again to fig1 liver assist system 5 includes bypass conduits which allow flexibility of use and ensure safety in case of emergency . for example , the connection between the liver assist system 5 and the plasma separation system 100 ( or other external system ) includes tubing 70 which provides a path of flow for a portion of the treated plasma back to plasma separation machine 100 from outlet 34 of reservoir bag 28 . a bridge section 72 connects tubing 70 to tubing 74 which introduces the plasma to be treated to bal device 8 . when the plasma separation machine 100 is being used on - line with liver assist system 5 , a pinch valve 76 is closed to prevent flow of plasma through bridge section 72 so that all of the plasma returning along tubing 70 flows to plasma separation machine 100 . in the event of an emergency , when it becomes necessary to prevent interflow between the systems , pinch valves 78 , 80 are closed and pinch valve 76 is opened . in this arrangement , plasma from the plasma separation machine 100 can be made to flow through line 11 , through open pinch valve 76 , back to plasma separation machine 100 through line 13 . line 15 may be open to a plasma storage bag 47 within machine 100 . bag 47 may act as a compliant chamber to account for variations of the flow rate in and out of plasma separation machine 100 through bypass 72 . pressure transducers 82 , 84 are provided within conduit 6 to sense extreme or inadequate levels of pressure . in these situations , signals from transducers 82 , 84 are used to control pinch valves 76 , 78 , 80 and pump 14 , and may also be used to provide a visual or audible warning signal to alert the operator of the condition . sampling ports may also be provided along conduit 6 to examine the characteristics of the plasma . the liver assist system 5 provides the following features for rinsing and priming conduit 6 and its components ( i . e ., oxygenator , filters , and bioreactor unit ). tubing 92 , 93 , operating in conjunction with pinch valves 94 , 95 , allows the introduction of two separate solutions for priming and rinsing conduit 6 and the components disposed therein . one solution ( e . g ., saline ) is introduced through tubing 92 with the other solution ( e . g ., 5 % dextrose ) introduced through tubing 93 . bypass segments allow for flushing the components independently or in series . the components may be rinsed and primed in any order . tubing 92 , 93 for introducing priming solution and tubing 29 , 113 leading to integral waste bags 31 , 33 , 114 create a closed system and provide an aseptic method of rinsing and priming the liver assist system 5 . in a preferred configuration , tubing 29 , 92 , 93 may be sealed and removed to condense the liver assist system once it is ready to receive plasma . the use of pinch valves 27 and 98 allows the priming solution to be directed to waste bags 31 , 33 after one pass before flowing to the waste bags or recirculated through the liver assist system 5 . the hollow fiber cartridge of the bal device ( without inoculated cells ) is rinsed and primed along the fibers with the waste solution directed to waste bags 31 , 33 . a separate waste bag 114 is connected to bal device 8 at in - port 61 . the extra - capillary space between the bundle of fibers is primed , and pores of the fibers are rinsed , with the waste solution directed to waste bag 114 . when cleansing of bal device 8 is complete , bal device 8 is completely filled with saline and ready to receive cells . tubing 70 , 74 between liver assist system 5 and the plasma separation machine 100 is rinsed by opening valves 78 , 80 for a period of time to allow some of the saline to flow through the tubing . it is generally important that the liver assist system 5 be fully primed with the priming solution at the initiation of plasma processing . liver cells from cell inoculation device 200 are then introduced at inlet 60 of bal device 8 and the saline within the extra capillary space of the bal device is displaced into waste bag 31 , 33 . waste bags 31 , 33 , and 114 and lines 60 and 113 are then removed . in this condition , liver assist system 5 is considered to be primed and ready to receive plasma . from the above description , one skilled in the art can easily ascertain the essential characteristics of the present invention , and without departing from the spirit and scope thereof , can make various changes and modifications of the invention to adapt it to various usages and conditions . for example , liver assist system 5 , described above for use as an artificial liver , may be used in other medical applications . moreover , the concept may be applicable to industrial operations . thus , other embodiments are also within the claims .
the invention relates to the safe and effective biotreatment of circulating fluids . in one general aspect of the invention , an apparatus for circulating and bioprocessing a fluid includes a conduit for circulating the fluid , an oxygenator for supplying oxygen to the fluid , a pump adapted to circulate the fluid through the conduit , a bioreactor unit , connected within the conduit , adapted to process the fluid , and a container connected within the conduit for receiving and releasing a portion of the fluid .