WO2012048298A2

WO2012048298A2 - Methods and systems of growing and harvesting cells in a hollow fiber bioreactor system with control conditions

Info

Publication number: WO2012048298A2
Application number: PCT/US2011/055482
Authority: WO
Inventors: Thomas G. Dilorenzo; Edward Allan Stanton Iv; Glen Delbert Antwiler; Michael E. Kinzie; Brian J. Nankervis; Monique Givens; Casey V. Medina; Jon A. Dodd
Original assignee: Terumo BCT Inc
Current assignee: Terumo BCT Inc
Priority date: 2010-10-08
Filing date: 2011-10-07
Publication date: 2012-04-12
Anticipated expiration: 2013-04-08
Also published as: WO2012048276A2; US20150079664A1; US10870827B2; EP2625263A2; US11746319B2; US20210024876A1; US11773363B2; US20200291346A1; EP2625264B1; US20170335270A1; EP2625577A2; WO2012048298A3; EP2625577B1; US11613727B2; US20120089930A1; US9677042B2; US9670451B2; US9725689B2; EP2625263B1; US8895291B2

Abstract

Embodiments described herein generally relate to methods and systems for using an air removal chamber as a control for a process in a cell expansion system. The air removal chamber may be mounted on a fluid conveyance assembly for use with the system. Fluid is pumped into a fluid containment chamber of the air removal chamber, in which the level of fluid in the fluid containment chamber may be monitored through the use of one or more sensors. The sensors are capable of detecting air, a lack of fluid, fluid, and/or a gas/fluid interface, e.g., an air/fluid interface, at measuring positions within the air removal chamber. Protocols for use with the system may include one or more stop conditions. In an embodiment, the stopping of a process is automated based on the detection of air, a lack of fluid, and/or a gas/fluid interface in the air removal chamber.

Description

METHODS AND SYSTEMS OF GROWING AND HARVESTING CELLS

IN A HOLLOW FIBER BIOREACTOR SYSTEM WITH CONTROL CONDITIONS

CROSS-REFERENCE TO RELATED APPLICATIONS

This application claims the benefit of U.S. Provisional Application Ser. No. 61/391,152, filed on October 8, 2010, and entitled, "Methods of Growing and Harvesting Cells in a Hollow Fiber

Bioreactor System" and of U.S. Provisional Application Ser. No. 61/434,726, filed on January 20, 2011, and entitled, "Methods of Growing and Harvesting Cells in a Hollow Fiber Bioreactor System." The disclosures of the above-identified applications are hereby incorporated by reference in their entireties as if set forth herein in full for all that they teach and for all purposes.

FDZLD

Embodiments of the present disclosure relate to cell growth in cell expansion systems.

BACKGROUND

The use of stem cells in a variety of medical treatments and therapies is receiving growing attention. Cell expansion systems can be used to grow stem cells, as well as other types of cells, such as bone marrow cells which may include stem cells. Stem cells which are expanded from donor cells can be used to repair or replace damaged or defective tissues and are considered for treating a wide range of diseases. Cell expansion systems (CESs) are used to expand cells and may be used to expand donor stem cells from bone marrow. Stem cells may be grown in hollow fiber bioreactors in a cell expansion system.

SUMMARY

Embodiments of the present disclosure generally relate to providing a control condition for stopping a process in a cell expansion system. Aspects of particular embodiments further provide for a stop condition involving an air removal chamber used in the cell expansion system. In embodiments, the stop condition is met when air, a lack of fluid, and/or a gas/fluid interface, e.g., an air/fluid interface, is detected in the air removal chamber.

The disclosure relates to a method of controlling a process in a cell expansion system. The method includes the steps of providing a fluid conveyance assembly, wherein the fluid conveyance assembly comprises a bioreactor; engaging the fluid conveyance assembly; providing an air removal chamber, wherein the air removal chamber is mounted on the fluid conveyance assembly, and wherein the air removal chamber comprises a fluid containment chamber, the fluid containment chamber comprising: a fluid entrance aperture, a fluid exit aperture, wherein the fluid exit aperture is coupled to a fluid exit tube, and a vent aperture, wherein the vent aperture is located above the fluid entrance aperture and the fluid exit aperture; providing a pump to pump a fluid through the fluid entrance aperture and into the fluid containment chamber of the air removal chamber; initiating the process, comprising operating the pump to pump the fluid through the fluid entrance aperture and into the fluid

containment chamber, wherein the fluid reaches a fluid level in the fluid containment chamber;

allowing the fluid to pass through the fluid exit aperture to enter the fluid exit tube; providing a sensor to detect the fluid level in the fluid containment chamber; detecting the fluid level using the sensor; providing a stop condition comprising meeting the stop condition when the fluid level in the fluid containment chamber reaches a predetermined level as detected by the sensor; and when the fluid level in the fluid containment chamber is at the predetermined level, stopping the process based on meeting the stop condition.

In at least one embodiment, providing the stop condition comprises meeting the stop condition when the sensor detects air. In at least one embodiment, providing the sensor comprises providing an ultrasonic sensor. In at least one embodiment, providing the sensor comprises providing an optical sensor. Γη at least one embodiment, the process comprises chasing the fluid from the air removal chamber. In at least one embodiment, when the fluid level in the fluid containment chamber is higher than the predetermined level, the method includes continuing to pump the fluid through the fluid entrance aperture and into the fluid containment chamber. In at least one embodiment, the process comprises loading media from a media bag into the bioreactor until the media bag is empty, in which the media is the fluid. In at least one embodiment, the process comprises loading cells, in which the media bag is a cell inlet bag. In at least one embodiment, the process comprises loading a reagent, wherein the media bag is a reagent bag. In at least one embodiment, the process comprises a step from a protocol, wherein the protocol comprises one of: loading cells into the bioreactor using a high flux cell load, loading cells into the bioreactor using a load with circulation, adding reagent, releasing adherent cells, or coating the bioreactor. In at least one embodiment, the method includes a second sensor to detect a top level of the fluid level in the fluid containment chamber.

The disclosure also relates to a method of operating a cell expansion system with a stop condition. The method includes the steps of selecting a protocol to load media into a bioreactor of the cell expansion system, wherein the protocol comprises a first process; determining whether a condition for the first process is set; when the condition for the first process is not set, setting the condition;

selecting the stop condition for the first process, wherein the stop condition comprises a detection of a gas/fluid interface in an air removal chamber; and selecting to execute the protocol.

In at least one embodiment, the protocol further comprises a second process, in which the first process comprises loading the media from a media bag into the cell expansion system until the media bag is empty, and the second process comprises chasing the media from the air removal chamber into a circulation loop of the cell expansion system. In at least one embodiment, the circulation loop comprises an intracapillary loop. In at least one embodiment, selecting a protocol to load media into the bioreactor comprises selecting the media, the media comprising one of: cells from a cell inlet bag or reagent from a reagent bag. In at least one embodiment, the one or more sensors detect the gas/fluid interface at a predetermined measuring position within the air removal chamber. In at least one embodiment, the one or more sensors comprise an ultrasonic sensor. In at least one embodiment, the protocol comprises one of: loading cells into the bioreactor using a high flux cell load, loading cells into the bioreactor using a load with circulation, adding reagent, releasing adherent cells, or coating the bioreactor.

The disclosure further relates to a cell expansion system comprising a capability to stop a process, in which the stopping of the process is automated. The system includes a fluid conveyance assembly comprising a bioreactor. The system also includes an air removal chamber comprising a fluid containment chamber. The fluid containment chamber comprises a fluid entrance aperture, a fluid exit aperture, and a vent aperture, wherein the vent aperture is located above the fluid entrance aperture and the fluid exit aperture. The system also includes at least one sensor for detecting a fluid in the fluid containment chamber and a controller in communication with the at least one sensor. The controller is operable to: signal to start the process, comprising signaling to start the one or more pumps for pumping the fluid through the fluid entrance aperture and into the fluid containment chamber of the air removal chamber; receive an indication from the at least one sensor when a lack of the fluid is detected by the at least one sensor; and in response to receiving the indication from the at least one sensor, altering the one or more pumps. In at least one embodiment, the altering the one or more pumps comprises stopping the one or more pumps to stop the process.

In at least one embodiment, the process comprises loading, by the one or more pumps, media from a media bag through the air removal chamber and into an intracapillary side of the bioreactor until the media bag is empty, wherein the media is the fluid. In at least one embodiment, the process comprises a step from a protocol, wherein the protocol comprises one of: loading cells into the bioreactor using a high flux cell load, loading cells into the bioreactor using a load with circulation, adding reagent, releasing adherent cells, or coating the bioreactor. In at least one embodiment, the at least one sensor is an ultrasonic sensor, and wherein the at least one sensor detects the lack of fluid by sensing air. This Summary is included to provide a selection of concepts in a simplified form, in which such concepts are further described below in the Detailed Description. This Summary is not intended to be used in any way to limit the claimed subject matter's scope. Features, including equivalents and variations thereof, may be included in addition to those provided herein.

BRIEF DESCRIPTION OF THE DRAWINGS

Embodiments of the present disclosure may be described by referencing the accompanying figures. In the figures, like numerals refer to like items.

FIG. 1 illustrates a perspective view of a hollow fiber bioreactor in accordance with embodiments of the present disclosure.

FIG. 2 depicts a schematic of one embodiment of a cell expansion system.

FIG. 3 illustrates a perspective view of the cell expansion system with a pre-mounted fluid conveyance device in accordance with embodiments of the present disclosure.

FIG. 4 depicts a perspective view of the housing of the cell expansion system in accordance with embodiments of the present disclosure.

FIG. 5 illustrates a perspective view of the pre-mounted fluid conveyance device in accordance with embodiments of the present disclosure.

FIG. 6 depicts a perspective view of the air removal chamber in accordance with embodiments of the present disclosure. DETATLED DESCRIPTION

The following Detailed Description provides a discussion of illustrative embodiments with reference to the accompanying drawings. The inclusion of specific embodiments herein should not be construed as limiting or restricting the present disclosure. Further, while language specific to features, acts, and/or structures, for example, may be used in describing embodiments herein, the claims are not limited to the features, acts, and/or structures described. A person of skill in the art will understand other embodiments, including improvements, that are within the spirit and scope of the present disclosure.

Embodiments of the present disclosure are generally directed to sterile methods for loading, growing, and harvesting cells in a hollow fiber cell growth chamber of a closed cell expansion system. In further embodiments, sterile methods are provided for loading, growing, and harvesting adherent cells, in particular mesenchymal stem cells, in the hollow fiber cell growth chamber of the closed cell expansion system. A closed system means that the contents of the system are not directly exposed to the atmosphere.

With reference now to Fig. 1, an example of a hollow fiber cell growth chamber 100 which may be used with the present disclosure is shown in front side elevation view. Cell growth chamber 100 has a longitudinal axis LA-LA and includes cell growth chamber housing 104. In at least one embodiment, cell growth chamber housing 104 includes four openings or ports: IC inlet port 108, IC outlet port 120, EC inlet port 128, and EC outlet port 132. It should be noted that like elements are represented by like numerals in all of the Figures.

According to embodiments of the present disclosure, fluid in a first circulation path enters cell growth chamber 100 through IC inlet port 108 at a first longitudinal end 112 of the cell growth chamber 100, passes into and through the intracapillary side (referred to in various embodiments as the

intracapillary ("IC") side or "IC space" of a hollow fiber membrane) of a plurality of hollow fibers 116, and out of cell growth chamber 100 through IC outlet port 120 located at a second longitudinal end 124 of the cell growth chamber 100. The fluid path between the IC inlet port 108 and the IC outlet port 120 defines the IC portion 126 of the cell growth chamber 100. Fluid in a second circulation path flows in the cell growth chamber 100 through EC inlet port 128, comes in contact with the extracapillary side or outside (referred to as the "EC side" or "EC space" of the membrane) of the hollow fibers 116, and exits cell growth chamber 100 via EC outlet port 132. The fluid path between the EC inlet port 128 and the EC outlet port 132 comprises the EC portion 136 of the cell growth chamber 100. Fluid entering cell growth chamber via the EC inlet port 128 is in contact with the outside of the hollow fibers 116. Small molecules (e.g., ions, water, oxygen, lactate, etc.) can diffuse through the hollow fibers from the interior or IC space of the hollow fiber to the exterior or EC space, or from the EC space to the IC space. Large molecular weight molecules such as growth factors are typically too large to pass through the hollow fiber membrane, and remain in the IC space of the hollow fibers. The media may be replaced as needed. Media may also be circulated through an oxygenator 232 (Fig. 2) to exchange gasses as needed. Cells can be contained within the first circulation path 202 and/or second circulation path 204 as described below, and can be on either the IC side and/or EC side of the membrane.

The material used to make the hollow fiber membrane may be any biocompatible polymeric material which is capable of being made into hollow fibers. One material which may be used is a synthetic polysulfone-based material, according to an embodiment of the present disclosure. In order for the cells to adhere to the surface of the hollow fibers, the surface may be modified in some way, either by coating at least the cell growth surface with a protein such as fibronectin or collagen, or by exposing the surface to radiation. A gamma irradiated polysulfone-based membrane for cell expansion is described in WO 2010/034466. Gamma treating the membrane surface allows for attachment of adherent cells without additionally coating the membrane with fibronectin or the like. Bioreactors made of gamma treated membranes can be reused. Referring now to Fig. 2, a schematic of one possible embodiment of a cell expansion system (CES) which may be used with the present disclosure is shown. In this embodiment and in all the examples or protocols below, the cells are grown in the IC space. CES 200 includes first fluid circulation path 202 (also referred to as the "intracapillary loop" or "IC loop") and second fluid circulation path 204 (also referred to as the "extracapillary loop" or "EC loop"). First fluid flow path 206 is fluidly associated with cell growth chamber 100 to form first fluid circulation path 202. Fluid flows into cell growth chamber 100 through IC inlet port 108, through hollow fibers in cell growth chamber 100, and exits via IC outlet port 120. Pressure gauge 210 measures the pressure of media leaving cell growth chamber 100. Media flows through IC circulation pump 212 which can be used to control the rate of media flow. IC circulation pump 212 may pump the fluid in a first direction or second direction opposite the first direction. Exit port 120 can be used as an inlet in the reverse direction. Media entering the IC loop may enter through valve 214. As those skilled in the art will appreciate, additional valves and/or other devices can be placed at various locations to isolate and/or measure characteristics of the media along portions of the fluid paths. Accordingly, it is to be understood that the schematic shown represents one possible configuration for various elements of the CES and modifications to the schematic shown are within the scope of the one or more present embodiments.

With regard to the IC loop, samples of media can be obtained from sample port 216 or sample coil 218 during operation. Pressure/temperature gauge 220 disposed in first fluid circulation path 202 allows detection of media pressure and temperature during operation. Media then returns to IC inlet port 108 to complete fluid circulation path 202. Cells grown/expanded in cell growth chamber 100 can be flushed out of cell growth chamber 100 into harvest bag 299 through valve 298 or redistributed within the hollow fibers for further growth. This will be described in more detail below. In this example, cells are grown in the IC space.

Fluid in second fluid circulation path 204 enters cell growth chamber 100 via EC inlet port 128, and leaves cell growth chamber 100 via EC outlet port 132. Media in the EC loop is in contact with the outside of the hollow fibers in the cell growth chamber 100, thereby allowing diffusion of small molecules into and out of the hollow fibers.

Pressure/temperature gauge 224 disposed in the second fluid circulation path 204 allows the pressure and temperature of media to be measured before the media enters the EC space of the cell growth chamber 100. Pressure gauge 226 allows the pressure of media in the second fluid circulation path 204 to be measured after it leaves the cell growth chamber 100. With regard to the EC loop, samples of media can be obtained from sample port 230 or a sample coil (not shown) during operation. After leaving EC outlet port 132 of cell growth chamber 100, fluid in second fluid circulation path 204 passes through EC circulation pump 228 to oxygenator 232. EC circulation pump 228 may also pump the fluid in opposing directions. Second fluid flow path 222 is fluidly associated with oxygenator 232 via oxygenator inlet port 234 and oxygenator outlet port 236. In operation, fluid media flows into oxygenator 232 via oxygenator inlet port 234, and exits oxygenator 232 via oxygenator outlet port 236. Oxygenator 232 adds oxygen to and removes bubbles from media in the CES. In various embodiments, media in second fluid circulation path 204 is in equilibrium with gas entering oxygenator 232. The oxygenator 232 can be any appropriately sized oxygenator or gas transfer device known in the art. Air or gas flows into oxygenator 232 via filter 238 and out of oxygenator or gas transfer device 232 through filter 240. Filters 238 and 240 reduce or prevent contamination of oxygenator 232 and associated media. Air or gas purged from the CES 200 during portions of a priming sequence can vent to the atmosphere via the oxygenator 232.

In the configuration depicted for CES 200, fluid media in first fluid circulation path 202 and second fluid circulation path 204 flows through cell growth chamber 100 in the same direction (a co-current configuration). The CES 200 can also be configured to flow in a counter-current conformation.

In accordance with at least one embodiment, media, such as cells (from bag 262), and fluid media from bag 246 can be introduced to first fluid circulation path 202 via first fluid flow path 206. Fluid containers, or media bags, 244 (e.g., Reagent) and 246 (e.g., IC Media) may be fluidly associated with either first fluid inlet path 242 via valves 248 and 250, respectively or second fluid inlet path 274 via valves 270 and 276. First and second sterile sealable input priming paths 208 and 209 are provided. Air removal chamber (ARC) 256 is fluidly associated with first circulation path 202. The air removal chamber 256 may include one or more ultrasonic sensors including an upper sensor 1268 and lower sensor 1264 to detect air, a lack of fluid, fluid, and/or a gas/fluid interface, e.g., an air/fluid interface, at certain measuring positions within the air removal chamber 256 (see Fig. 6), and to send a signal to the controller upon such detection, according to embodiments of the present disclosure. For example, ultrasonic sensors may be used near the bottom and/or near the top of the air removal chamber 256 to detect air, a lack of fluid, fluid, and/or an air/fluid interface at these locations. Embodiments provide for the use of numerous other types of sensors without departing from the spirit and scope of the present disclosure. For example, optical sensors may be used in accordance with embodiments of the present disclosure. Air or gas purged from the CES 200 during portions of the priming sequence or other protocols can vent to the atmosphere out air valve 260 via line 258 that is fluidly associated with air removal chamber 256.

Fluid container 262 (e.g., Cell Inlet Bag (or Saline Priming Fluid for priming air out of the system)) is fluidly associated with the first fluid circulation path 202 via valve 264. EC media (from bag 268) or wash solution (from bag 266) may be added to either the first or second fluid flow path. Fluid container 266 may be fluidly associated with valve 270 that is fluidly associated with first fluid circulation path 202 via distribution valve 272 and first fluid inlet path 242.

Alternatively, fluid container 266 can be fluidly associated with second fluid circulation path 204 via second fluid inlet path 274 and second fluid flow path 284 by opening valve 270 and closing distribution valve 272. Likewise, fluid container 268 is fluidly associated with valve 276 that may be fluidly associated with first fluid circulation path 202 via first fluid inlet path 242 and distribution valve 272. Alternatively, fluid container 268 may be fluidly associated with second fluid inlet path 274 by opening valve 276 and closing valve distribution 272.

An optional heat exchanger 252 may be provided for media reagent or wash solution introduction.

In the IC loop, fluid is initially advanced by the IC inlet pump 254. In the EC loop, fluid is initially advanced by the EC inlet pump 278. An air detector 280, such as an ultrasonic sensor, may also be associated with the EC inlet path 284.

In at least one embodiment, first and second fluid circulation paths 202 and 204 are connected to waste line 288. When valve 290 is opened, IC media can flow through waste line 288 and to waste bag 286. Likewise, when valve 292 is opened, EC media can flow through waste line 288 to waste bag 286.

Cells can be harvested via cell harvest path 296. Here, cells from cell growth chamber 100 can be harvested by pumping the IC media containing the cells through cell harvest path 296 and valve 298 to cell harvest bag 299.

Various components of the CES 200 can be contained or housed within an incubator machine or housing 304 (Fig. 3), wherein the incubator maintains cells and media at a desirable temperature. With reference now to Fig. 3, an embodiment of a CES 200 is shown. The CES 200 includes a cell expansion housing or machine 304 that comprises a hatch or closable door 308 for engagement with a back portion 312 of the cell expansion machine 200. An interior space 316 within the cell expansion machine 304 includes features adapted for receiving and engaging a premounted fluid conveyance assembly 320. The premounted fluid conveyance assembly 320 is detachably-attachable to the cell expansion machine 200 to facilitate relatively quick exchange of a new or unused premounted fluid conveyance assembly 320 at a cell expansion machine 200 for a used premounted fluid conveyance assembly 320 at the same cell expansion machine 200. Advantageously, a single cell expansion machine 304 can be operated to grow or expand a first set of cells using a first premounted fluid conveyance assembly 320, and thereafter, used to grow or expand a second set of cells using a second premounted fluid conveyance assembly 320 without needing to be sanitized between interchanging the first premounted fluid conveyance assembly 320 for the second premounted fluid conveyance assembly 320. The premounted fluid conveyance assembly includes the bioreactor 100 and the oxygenator 232. Tubing guide slots are shown as 612 for receiving various media tubing connected to premounted fluid conveyance assembly 320.

Referring now to Fig. 4, the back portion 312 of a cell expansion machine 304 is shown prior to detachably-attaching a premounted fluid conveyance assembly 320. For clarity, the closable door 308 (shown in Fig. 3) is omitted from Fig. 4. The back portion 312 of the cell expansion machine 304 includes a number of different structures for working in combination with elements of a premounted fluid conveyance assembly 320. More particularly, the back portion 312 of the cell expansion machine 304 includes a plurality of peristaltic pumps for cooperating with pump loops 404 (Fig. 5), including the IC circulation pump 212, the EC circulation pump 228, the IC inlet pump 254, and the EC inlet pump 278. In addition, the back portion 312 of the cell expansion machine 104 includes a plurality of valves, including the IC circulation valve 214, the reagent valve 248, the IC media valve 250, the air removal valve 260, the cell inlet valve 264, the wash valve 270, the distribution valve 272, the EC media valve 276, the IC waste valve 290, the EC waste valve 292, and the harvest valve 298. Several sensors are also associated with the back portion 312 of the cell expansion machine 304, including the IC outlet pressure sensor 210, the combination IC inlet pressure and temperature sensors 220, the combination EC inlet pressure and temperature sensors 224, and the EC outlet pressure sensor 226. Also shown is the optical sensor 616 for the air removal chamber 256. Referring still to Fig. 4, a shaft or rocker control 604 for rotating the bioreactor 100 is shown. Shaped fitting 608 associated with the shaft 604 allows for proper alignment of a shaft access aperture 324 (Fig. 5) of the tubing-organizer 300 of the premounted conveyance assembly with the back portion 312 of the cell expansion machine 304. Rotation of rocker control 604 imparts rotational movement to shaft fitting 508 (Fig. 5) and bioreactor 100. Thus, when an operator of the CES200 attaches a new or unused premounted fluid conveyance assembly 320 to the cell expansion machine 304, the alignment is a relatively simple matter of properly orienting the shaft access aperture 324 of the premounted fluid conveyance assembly 320 with the shaped fitting 608.

Referring now to Fig. 5, a perspective view of a detachably-attachable premounted fluid conveyance assembly 320 is shown. The premounted fluid conveyance assembly 320 is detachably-attachable to the cell expansion housing304 to facilitate relatively quick exchange of a new or unused premounted fluid conveyance assembly 320 at a cell expansion machine 304 for a used premounted fluid conveyance assembly 320 at the same cell expansion machine 304. As shown in Fig. 5, the bioreactor 100 is attached to a bioreactor coupling that includes a shaft fitting 508. The shaped fitting 508 includes one or more shaft fastening mechanisms, such as a biased arm or spring member 512 for engaging a shaft (shown in Fig. 4) of the cell expansion machine 304.

Referring still to Fig. 5, the premounted fluid conveyance assembly 320 typically includes tubing 408 and various tubing fittings 412 to provide the fluid paths shown in Fig. 2. Pump loops 404 are also provided for the pump. Although the various media are typically provided at the site where the cell expansion machine 304 is located, the premounted fluid conveyance assembly 320 typically includes sufficient tubing length to extend to the exterior of the cell expansion machine 304 and to enable welded connections to tubing associated with the media bags.

The air removal chamber or ARC will now be described with respect with Fig. 6. In accordance with at least one embodiment, the air removal chamber 256 is mounted in a substantially vertical orientation on the premounted fluid conveyance assembly 320, such that air or gas bubbles within the fluid rise upward away from the bottom 1212 toward the vent aperture 1224 preferably located at the top 1228 along the vertical direction of the air removal chamber 256, or at least vertically above the fluid entrance aperture 1220 and fluid exit aperture 1236.

Referring again to Fig. 6 in at least one embodiment a plurality of fluid level sensors is used in combination with the air removal chamber 256. In at least one embodiment, the sensors are located on the cell expansion machine 304 at 616. More particularly, while the air removal chamber 256 is connected to a premounted fluid conveyance assembly 320 that can be detachably-attached to the cell expansion machine 304, the fluid level sensors for the air removal chamber 256 form part of the cell expansion machine 304 along with a control for such.

In accordance with at least one embodiment, at least two sensors are used with the air removal chamber 256 to provide "high" and "low" fluid level sensing capability. Accordingly, operating protocol for the CES 100 includes monitoring the fluid level within the air removal chamber 256 and adjusting the pumping rate of the peristaltic pumps as necessary to maintain an appropriate fluid level within the fluid containment chamber 1208 of the air removal chamber. This operating protocol may include increasing or decreasing the pumping rates associated with pumps on either one or both the upstream and downstream sides of the air removal chamber 256. The ARC as described below also functions as a stop indication for various protocols. In embodiments using the ARC as a stop indication, the stopping of a process is automated based on the detection of air, a lack of fluid, and/or a gas/fluid interface in the air removal chamber. In at least one embodiment, a first fluid level sensor 1264 (or low level fluid sensor) is situated to detect a fluid level in the air removal chamber 256 at a level of approximately ¼ full, and a second fluid level sensor 1268 (or high level fluid sensor) is situated to detect a fluid level in the air removal chamber 256 at a level of approximately 3/4 full. The position of the fluid level sensors 1264 and 1268 allow the fluid level within the ah removal chamber 256 to be adjusted to ensure that air does not pass though the fluid exit aperture 1236 and enter the fluid exit tube 1240 at the bottom 1212 of the air removal chamber 256 because of too low a fluid level, and that fluid does not exit through vent aperture 1224 located at the top 1228 of the air removal chamber 256 because of too high a fluid level. As will be recognized by those of skill in the art, any number of fluid containers (e.g., media bags) can be fluidly associated with the CES in any combination.

Protocols will now be described with respect to the schematic described in Fig. 2, in accordance with embodiments of the present disclosure.

The following is a definition section for the Protocols described below. Points A through H on the schematic of Fig.2 are also described in the definition section below. Γη the protocols or examples described the definition section may be referenced for various descriptions.

Protocols Parameter Definitions

TcM 10 Time to equilibrate (condition) media

Note: For all examples the initial position of the bioreactor 100 to define rocker control motion is as shown in Fig. 3 or parallel to the horizon. Protocol 1 : High Flux Cell Load in Bioreactor Example

In an embodiment, this protocol is to load the cells from cell inlet bag 262 into bioreactor 100 until the bag 262 is empty. This is a high flux load at a medium flow rate. ic_BL is the volume from the bags such as cell inlet bag 262 to the IC loop 202. In this example, the VicBL is 29.3 mL assuming the volume of the air removal chamber (ARC) is 10 mL and the inlet bag 262 length, such as cell inlet bag 262, is 3 mL. For a high flux cell load, V_FT0 of air is needed in the cell inlet bag. V_FT0 is defined as (1 + LP%/100) * ic_BL + 5 mL. In this example, it is 40.2 mL. LP% is a percentage related to pump error volume and in this example may be 20%.

The High Flux Load Protocol conditions are:

1) Valve 264 is open.

2) Inlet Pump 254 pumps at 50 mL/min (can be within 20 to 100 mL/min range).

3) IC circulation pump 212 and EC inlet pump 278 are off.

4) EC circulation pump 228 is set at Q_ECCM which is a rate selected to keep EC loop well mixed which in this example is 30 mL/min.

5) IC Valve 290 is open to waste.

6) The bioreactor 100 is rotated using the rocker control from -90° to 180° with 1 second rest at end points to distribute cells. Alternatively the bioreactor can be fixed.

7) The high flux cell load is stopped when air is detected in the air removal chamber or ARC by the lower air sensor 1264.

8) ARC valve 260 is open to vent ARC air to atmosphere.

9) The ARC is then filled with media (either reagent, IC media or wash solution by pump 254 to upper senor 1268). IC media may be at least 60 mL of media with protein.

10) Cells are chased from the ARC by the fill media of item 9) above to the bioreactor 100 with larger chase volumes spreading the cells toward the IC outlet 120.

11) The chase is stopped at a selected IC volume which in this example is 47 mL.

The following is a brief summary of Protocol High Flux Load with chase step.

Protocol 1 High Flux Load

Purpose of protocol: Loads cells into the bioreactor from the cell inlet bag until the bag is empty. This protocol does not use IC circulation to distribute the cells. Step 1 : Load Bioreactor

Purpose of Step: Loads the cells from the cell inlet bag into the bioreactor.

Precondition: Need at least V_FT0 of air in cell inlet bag.

Step 2: Chase to Bioreactor

Purpose of Step: Chases the cells from the ARC to the bioreactor. Larger chase volumes spread the cells and move them towards the IC outlet.

Precondition: Fill ARC

Protocol 2: Load Cells into Bioreactor with Circulation Example

In an embodiment , this alternative protocol loads the cells from the IC inlet bag 262 until it is empty to the bioreactor 100. It uses the IC circulation loop 202 for the load. The cell inlet bag contains at least V_FTO of air. The IC circulation pump 212 permits load from both the inlet 108 and outlet 120 of bioreactor 100.

The conditions for the Protocol Load Cells into Bioreactor with Circulation are:

1) Valve 264 is open.

2) Inlet pump 254 operates at 50 mL/min within a range of 200 to 100 mL/min.

3) IC circulation rate using pump 212 is Vici/min - Q_ICA

Vic_L is the IC loop 202 volume or

VBRIC ⁺ 2 VBRICH + EF

V_BRIC is the volume of the IC side of bioreactor 100 excluding headers. V_BRICH is the volume of the headers. V_EF is the volume of the IC loop from E to F on Fig. 2 excluding the bioreactor. Q_ICA is the inlet pump rate. The range for the IC circulation rate is from 20 to 300 mL/min and depends on the IC inlet rate. In this example it is 139 mL/min.

4) EC inlet is O with default Q_ECCM in a range from 10 to 300 mL/min.

5) The EC circulation rate is Q_ECCM, for example 30 mL/min.

6) The outlet the EC waste through valve 292.

7) Rocker control for the bioreactor 100 is -90° to 180° for 1 second stops at the ends of rotation or optionally the bioreactor may be fixed.

8) The stop condition is air detection by the ARC by the lower air sensor 1264.

9) After stop condition ARC is filled with desired media to upper sensor 1268and chase liquid chases the cells from the ARC to the loop. The stop condition for chase is the IC volume (V_ARCA + V_ARCBS) * 2 in a range from 1 to 100. V_ARC_A is the volume from the ARC to point A on Fig. 2 and V_ARCBS is the volume of the ARC between sensors 1268 and 1264.

10) To load the cells from the IC loop the IC circulation rate is -V_ABO% of <¾_CA- -V_ABO % is V_ABO * 100 / V_ABI + V_ABO- _ABO i the volume from point A to the bioreactor 100 outlet (point F) and in this example is 42.1 mL. Q_ICA is the inlet pump rate as described above. V_ABI is the volume from point A to inlet 108 with V_ABO being the volume from point A to outlet 120.

11) The stop condition for the load is the IC volume 1.5 x V_EF- The range is 0.5 V_EF to 2.0 V_EF- V_EF is the volume of the IC loop 202 from point E to F excluding the bioreactor.

Below is a summary of the circulation load. Protocol 2 Load with Circulation

Purpose of protocol: Loads the cells into the bioreactor from the cell inlet bag until the bag is empty, and uses IC circulation to distribute the cells.

Step 1 : Load IC Loop

Purpose of Step: Loads the cells into the system.

Precondition: Need at least V_FTo of air in cell inlet bag.

EC Circulation Rate (mL/min) Default: Same as Step 1

Outlet EC Waste

Rocker Control Same as Step 1

Output: IC volume Volume as defined by Stop Condition

Output: EC volume N/A

Output: Remaining time of step Countdown in minutes or manual stop as defined by Stop Condition

Step 3: Load Bioreactor

Purpose of Step: Chases the cells from the IC loop into the bioreactor.

Protocol 3 : Bone Marrow Washout Example

In an embodiment, this protocol is to remove non-attached/non-adhered cells from the bioreactor. It is for 25mL to 62 mL bone marrow load though it could be used for load above 10 mL. The bone marrow washout generally follows bone marrow load. It can also be a wash out protocol when the bioreactor is packed with a large number of cells though this protocol is typically done after an initial load. The types of cells removed include red blood cells, platelets and non-adherent bone marrow cells.

The protocol includes the following:

1) IC media introduced through valve 250. This may be approximately 500 mL with protein.

Optionally wash or EC media could be introduced. 2) EC media is generally media without protein introduced through valve 276. Optionally wash or IC media could be introduced on EC side.

3) IC inlet rate (mL/min) through pump 254 is expressed as follows:

0, 0<t<ti

20 + ((^Q/₂)-20) x (t-ti) / _ti), _tl< t < t₂

0, t₃< t

In this example the maximum is 100 mL/min.

4) IC circulation rate is expressed as follows: -AB

VAB = volume from point A to B on Fig.2

IC loop volume

5) EC inlet rate (mL/min)

20 + ((^Q/₂)-20)x(t/_tl) 0<t<t_i

Q/2 ti<t≤t₂

( )-( )* ((*-¾/¾-¾)) t₂<t<t₃

0, t₃<t

6) The parameters for both the IC inlet and EC inlets rates are defined in the table following:

Parameter Equation

V User input - Total IC + EC volume to be pumped (mL).

Q User input - Maximum IC inlet rate (mL/min). Q > 40 mL/min.

ti (minutes)= _{V X} ((2 X(Q-40))/_{(3 X Q2}^_{0 X Q}_ ₁₆₀₀₎₎ t₂ (minutes)= 2 xt ! ; t₃ (minutes)= (⁵/₂) x ((Q-³²)/(Q.₄₀)) ¾

7) EC circulation rate (mL/min) = QECCM of a range from 10 to 300 mL/min. QECCM = rate to keep EC loop well mixed in this example 30mL/min.

8) Rocker control for bioreactor 100 is on with -90°, 180°, for 1 second pause at the ends.

9) The stop condition in this example is an inlet volume of 1000 mL with a range from 400 to 4000.

10) Maximum flow rate of output washout is 100 mL in range from 80 to 200.

Summary of the protocol is below. Protocol 3 Bone Marrow Washout

Purpose of protocol: Meant for use following a bone marrow load (25 mL to 62 mL) and attachment phase, this protocol is recommended to remove any non-attached/non-adhered cells from the bioreactor.

This is also a useful washout protocol for any occasion when the bioreactor is packed with a similar large number of cells. For bone marrow loads of 10 mL or less, Protocol Aggressive Washout is recommended. For bone marrow loads between 10 mL to 25 mL, this protocol is optional but may not be required.

Step 1 : Bone Marrow Washout

20 + ((^Q/₂) - 20) x (t / _ti) 0 < t≤ ti

Q/2 tl< t < t₂

EC Inlet Rate (rnL/min)

=

(^Q/₂) - (^Q/₂) x t₂< t≤t₃ o, t₃< t

EC Circulation Rate (mL/min) Default: Q_ECC_M

Range: 10 to 300 mL/min

Outlet IC Waste

Rocker On (-90°, 180°, 1 sec) Range: full range (deg, time)

Output: IC volume Volume as defined by stop condition

Output: EC volume Volume as defined by stop condition

Output: Remaining time of step Countdown in minutes as defined by stop condition

Parameter Equation

V User input - Total IC + EC volume to be pumped (mL).

Q User input - Maximum IC inlet rate (mL/min). Q > 40 mL/min.

ti (minutes)= V x ((2 * (Q-40)) _{/ (3 x Q 0 x Q}_ ₁₆₀₀₎₎ t₂ (minutes)= 2 x t i ; t₃ (minutes)= (⁵/₂) ^χ ((Q-³²)/(Q.₄₀)) X ¾

Protocol 4: Aggressive Washout for Bone Marrow Loads below 10 mL Example

In an embodiment, this protocol produces a small amount ultrafiltration into the hollow fiber of the bioreactor membrane 116 across the entire filter length. The purpose of the protocol is to remove non-adherent cells from the bioreactor.

The protocol includes:

1) IC source is IC media introduced through valve 250 by pump 254. Alternatively the IC source could be reagent, wash, or EC media. The IC media may be media with protein estimated in this example to be about 500 mL.

2) EC source is EC media introduced through valve 276 by pump 278. Alternatively the EC source could be reagent, IC media, or wash. This may be media without protein.

3) IC pump 254 is set at approximately 260 mL/min inlet rate from a range of 50 to 500 mL/min.

4) IC circulation rate is -AB% * Q_ICA, in this example, -45mL/min.

5) EC inlet rate is 40 mL/min from a range of 0 to 100 mL/min. 6) EC circulation rate is Q_ECCM or the rate to keep the loop well mixed from a range of 10 to 300 mL/min, in this example 30 mL/min.

7) The IC source goes to waste.

8) The rocker control for the bioreactor 100 may be set at -90% to 180%) for 1 second pause at the ends of the range of motion or optionally could be fixed.

9) The stop condition for the process may be based on time such as up to 60 minutes; IC volume as defined in the Bone Marrow Washout which may range from is from 0 to 4000 mL range; or the number of IC exchanges or number of times the IC source fluid is circulated. The number of IC exchanges may be 2.5 from a range of 0.5 to 5.0

Summary of the protocol is below.

Protocol 4 Aggressive Washout

Purpose of protocol: Removes non-adherent cells from the bioreactor. This protocol imposes a small ultrafiltration into the fiber across the entire fiber length.

Step 1 : Aggressive Washout

[Output: Remaining time of step |Countdown in minutes as defined by Stop Condition

Protocol 5: IC or EC Washout Example

In an embodiment, this protocol is to replace media while growing adherent cells. The protocol washes out cellular debris and non-adherent cells. The replacement volume is the number of IC and EC exchanges to be performed or IC or EC volume exchanged.

VICE (IC exchange volume) equals IC loop volume plus volume from media, reagent or wash bags to IC loop. ECE (EC exchange volume) equals EC loop volume plus volume from media, reagent or wash bags to EC loop.

The protocol includes the following.

1) The IC source is IC media introduced through valve 250 by pump 254. Reagent, EC media, or wash solution may optionally be used. The IC media may be media with protein. In this example the volume may be at least 550 mL.

2) The EC source is EC media introduced through valve 276 by pump 278. Reagent, IC media, or wash solution may optionally be used. The EC media may be media without protein. In this example the volume may be at least 810 mL.

3) The IC inlet rate is QEC_A (number of IC Exc * VICE) / (number of EC Exc * V_ECE)

QEC_A ⁼ EC inlet pump rate

VICE ⁼ IC exchange volume which in this example is 218.4 mL.

VECE ⁼ EC exchange volume which in this example is 324.1 mL.

4) IC circulation rate is -AB%*QICA

AB% = VAB (volume from point A to Bin Fig. 2) * 100 / V_ICL- V_KL is IC loop volume.

QicA ⁼ IC inlet pump 254 rate

5) The EC inlet rate is the lesser of Qioo or QMAX where

Qioo = 100 (number of EC Exc * V_ECE) / (number of IC Exc * VICE) and

6) The EC circulation rate is -CD% * QECA- CD% = V_CD (or volume from point C to D, in this example 3.8 mL) * 100/V_ECE-

7) The outlet for the media or washout fluid is either the IC, EC, or both waste 286.

8) The rocker control for the bioreactor 100 is -90° to 180° with 1 second pause at the end of the range of motion. Or alternatively, there is no rocker control motion. 9) The stop condition to end the process includes the number of IC exchanges (Exc.) which may be 2.5 or optionally within a range from 0.5 to 5. The stop condition also includes the number of EC exchanges which may be 2.5 or optionally within a range from 0.5 to 5. A summary of this protocol is as follows.

Protocol 5 IC or EC Washout

Purpose of protocol: Meant for use when growing adherent cells to replace the media in both the IC loop and EC loop. This protocol provides some washout of cellular debris and non-adherent cells. The replacement volume is specified as the number of IC and EC exchanges to be performed.

Calculations:

• One IC exchange volume (V_ICE) is equal to the IC Loop Volume plus the volume from bags to IC loop.

• One EC exchange (V_ECE) is equal to the EC Loop Volume plus the volume from bags to EC Loop.

Step 1: Washout

Protocol 6: Washout through the Membrane Example

In an embodiment, this protocol is to move small molecular components on the IC side to the EC side of the membrane 116. These molecules pass through the membrane by diffusion or ultrafiltration. These could include bi-products of the cell growth. IC components retained by the membrane are not removed from the IC loop. The small molecular weight elements are washed out of the EC side by replacement fluid. The replacement volume is specified by the number of IC volumes - EC volumes exchanged. The protocol includes:

1) The introduction of IC media or optionally other media to the IC side. This may be media with protein.

2) The introduction of EC media or optionally other media te the EC side. This may be media without protein.

3) The IC inlet rate as described for IC/EC washout.

QECA (number of IC Exc * VI_CE) / (number of EC Exc * V_ECE)

4) The IC circulation rate is defined by -VABO% * QICA- VABO% = VABO * 10 / VABI + VABO

VABO is from point A to bioreactor outlet F on Fig. 2 and in this example is 42.1 mL.

VABI is from point A to bioreactor inlet E on Fig. 2 and in this example is 9 mL.

5) The EC inlet rate is the lesser of Q₆₅ or QM_AX where Q₆₅ is defined the same as Qioo for IC/EC washout above.

6) The EC circulation rate is -CD% * Q_ECA as described above for IC/EC washout.

7) The outlet is EC waste.

8) The rocker control is the same for IC/EC washout.

9) The stop condition is the number of IC and EC exchanges which may be 1 or within the range of 0.5 to 5.

The brief summary is as follows.

Protocol 6 IC EC Washout through Membrane

Purpose of protocol: Replaces small molecule components on IC side, which pass through the membrane by either diffusion or by ultra filtration. IC components retained by the membrane are not removed from the IC loop. Components on EC side are washed out by fluid replacement. The replacement volume is specified as the number of IC and EC exchanges to be performed. Calculations:

Step 1 : Washout Through Membrane

Protocol 7: Continuous Add of IC with Ultrafiltration Example

In an embodiment, this protocol adds generally IC fluid at a low flow rate and keeps large molecules on the IC side of the fiber. A similar protocol could be used to add fluid at low flow rate to the EC side. Excess IC fluid will be removed through ultrafiltration if the IC inlet pump 254 is used.

This protocol includes:

1) The IC media is introduced through valve 250 by pump 254 with other media being optional alternatives.

2) EC media may optionally be added but in the IC example the EC inlet flow rate is 0.

3) The IC inlet flow rate is 0.1 mL/min from a range of 0 to 10 mL/min.

4) The IC circulation rate through IC loop 202 is at a maximum of Q_ICCM, 10 X Q_ICA- QICCM is the IC circulation pump rate to keep IC loop 202 well mixed without preventing air from entering filter 116. The inlet pump 254 rate Q_ICA plus the circulation pump 212 rate equals the QI_CCM which in this example is 20 mL/min.

5) The EC circulation rate is QECCM or the pump 228 rate to keep the EC loop 204 well mixed, for example 30 mL/min.

6) The outlet for the excess IC fluid is EC waste as the fluid enters the EC loop 204 through ultrafiltration through the membrane.

7) The rocker control for bioreactor 100 is fixed.

8) The stop condition is a manual stop by the operator although alternatively the stop could be based on selected time or selected IC or EC volume.

Below is a summary of the Continuous Add with Ultrafiltration protocol.

Protocol 7 Continuous Add with Ultra Filtration

Purpose of protocol: Continuously adds fluid at a low flow rate to the IC loop and/or the EC loop. Large molecules may be concentrated in the IC loop if you use the IC Inlet pump for this task. This protocol uses ultrafiltration to remove excess IC fluid if you use the IC Inlet pump.

Step 1 : Feed

Outlet EC Waste

On (-90°, 180°, 1 sec) Range: full range (deg, tune)

Rocker Control

Fixed (0°) (Def) Range: full range (deg)

Output: IC volume Volume or rate as defined by Stop Condition

Output: EC volume Volume or rate as defined by Stop Condition

Protocol 8: Continuous Add with Active Removal Example

In an embodiment, this protocol uses a relatively low flow rate to continuously add to the IC and/or EC loops. Excess IC fluid is removed using EC waste through the membrane 116.

The protocol includes:

1) IC media is added through valve 250 and pump 254 to the IC circuit. Alternatively, other media could be provided continuously such as cell inlet, reagent, wash solution or EC media. If the addition of media or fluid is only for the EC side, there may be no input of fluid through the IC side.

2) Optionally or alternatively media may be added from an EC source to the EC side if only EC addition is desired. The addition may be EC media through valve 276 and pump 278. Alternatively there may be no EC input as the addition is only to the EC side. Reagent, IC media, or wash solution could also be added to the EC side.

3) On the IC side the IC inlet rate of pump 254 is 0.1 mL/min for low flow rate addition. This is selected from a range of 0 to 10 mL/min.

4) For IC addition the IC circulation rate is the maximum of QICCM or 10 X QICA with QICCM being the rate of the IC circulation pump 212to keep the IC loop well mixed and Q_ICA being the rate of the inlet pump 254 in mL/min selected from a range from -100 to 100 mL/min. For example it may be 20 mL/min.

5) If the low flow addition is to the EC side the EC inlet rate may be selected to be 0.1 mL/min from a range of 0 to 20 mL/min.

6) For the EC addition the EC circulation rate is selected to be QECCM which is the rate of the circulation pump 228 in mL/min selected from a potential range of 0 to 100 mL/min, for example 30 mL/min.

7) The outlet in this example is EC waste.

8) The rocker control for the bioreactor 100 is off with no rotation.

9) The stop condition for the protocol is manually though it alternatively may be based on the time (for example 0.1 to 1440 minutes) or IC or EC volumes (for example IC or EC volumes may be from 1 to 4000 mL).

The brief summary of this protocol is set forth below. Protocol 8 Continuous Add with Active Removal

Purpose of protocol: Continually adds a low flow rate to the IC and/or EC loops. A pump is used to remove excess IC fluid.

Step 1 :

Protocol 9: Reagent Add Example

In an embodiment, this protocol loads reagent from reagent bag 244 through valve 248 by pump 254 into the IC side until the bag is empty. The IC waste valve 290 is closed for circulation through circulation loop 202. The cell inlet bag 262 includes at V_FTO of air which is defined as (1 + LP% / 100) * V_KBL + 5 mL, for example 38 ml. LP% is about a 20% pump V_KBL is the volume from bag 244 to IC loop. The cell inlet bag has at least 10 mL of fluid.

The protocol includes:

1) Introduction of reagent through valve 248 by pump 254 to the IC loop 202.

2) Introduction of air, as pump 254 continues, from cell inlet bag 262.

3) Nothing is introduced on the EC side.

4) The IC inlet rate from pump 254 is 10 mL/min selected from a range of 0 to 100 mL/min.

5) The IC circulation rate from pump 212 is the maximum of the IC circulation pump rate 212 to keep the IC loop 202 well mixed or a value selected from the minimum of 300 or 10 x Q_KA (IC inlet pump 254 rate), for example, 100 mL/min.

6) There is no EC inlet but the circulation rate is the rate of the circulation pump 228 to keep the EC loop well mixed, for example 30 mL/min.

7) The outlet is EC waste through valve 292. IC waste through valve 290 is an option.

8) The rocker control for the bioreactor 100 is fixed or stationary. Alternatively, the rocker control range of motion is from -90° to 180° with 1 second pauses at the end of the motion range.

9) The stop for the reagent load is when air reaches the lower sensor 1264 of the air removal chamber or ARC.

10) After air detection the ARC is filled to the upper sensor 1268 from the IC media or a bag such as wash solution or EC media bag that did not contain reagent. Valve 260 and vent are open to purge

ARC air.

11) Media such as IC media through valve 250 and moved by pump 254 continues to chase any reagent from the ARC to the IC loop 202.

12) The stop condition for the chase of reagent is the IC volume (V_ARCA + V_ARCBS) * 2.

V_ARCA is the volume from the bottom sensor of the ARC to point A on Fig. 2.

V_ARCBS is the volume of the ARC between top and bottom sensors. For example, the IC volume may be 22 mL. The range for this volume is between 0 to 100 mL.

The brief summary of this protocol is set forth below.

Protocol 9 Reagent Add

Purpose of protocol: Loads reagent from the reagent bag into the IC loop until the bag is empty. The IC waste valve is closed during this protocol.

Step 1 : Load Reagent

Purpose of Step: Loads reagent into the system.

Precondition: Need at least V_FTo of air in cell inlet bag.

Step 2: ARC Chase

Purpose of Step: Chases reagent from the ARC into the IC Loop.

Protocol 10: Bolus Add Example Γη an embodiment, this protocol adds a selected volume of reagent into the IC loop. A bolus into the EC loop can also optionally be added. If the IC waste (valve 290) is closed ultrafiltration through the membrane 116 to the EC side will occur. The protocol includes:

1) Reagent as the IC source is introduced through the pump 254. Alternatively other sources of media or wash could be used for a bolus amount.

2) No EC source. However, if bolus amount is to EC side only there would be no IC source and bolus amount would be introduced by pump 278.

3) For IC bolus, inlet would be 10 mL/min selected from a range up to the rate of the inlet pump.

4) The IC circulation rate is the maximum of QICCM as compared to the minimum of 300 or 10 x Q_ICA as described above with respect to the Reagent Add protocol. This is selected from the range of -300 to 300 mL/min. In this example it may be 100 mL/min.

5) If the bolus is to the EC side there is no IC inlet or source.

6) The EC circulation is QECCM or the rate of the circulation pump 228 to keep the EC loop 204 well mixed. In this example it may be 30 mL/min.

7) The outlet is EC waste through valve 292. Alternatively it could be to harvest through valve 298 or to IC waste through valve 290.

8) The rocker control is off or alternatively could be set for rotation as described previously.

9) The stop condition can be selected to be based on time up to 20 minutes or an IC volume selected to be 10 mL in a range up to 200 mL.

The Bolus Add protocol is summarized below. Protocol 10 Bolus Add

Purpose of protocol: Quickly adds a selected volume of reagent into the IC loop; you can add an EC bolus at the same time. During the default condition the IC waste valve closed, which forces ultrafiltration.

Step 1: Bolus Add

Reagent

IC Media

EC Source Wash

EC Media

None (Default)

Time (1 min) Range: 0.1 to 20 min

Stop Condition IC volume: 10 (Default) Range: 1 to 200 mL

EC volume: (15 mL) Range: 1 to 300 mL

Default: 10

IC Inlet Rate (ml/min)

Range: 0 to Q_ARC mL/min

IC Circulation Rate (ml/min) Default: Maximum of (2_[CcM,min(300,10xQicA))

Range: -300 to 300 mL/min

Default: 0

EC Inlet Rate (ml/min)

Range: 0 to 300 mL/min

Default: Q_ECC

EC Circulation Rate (ml/min)

Range: 0 to 300 mL/min

EC Waste (default)

Outlet IC Waste

Harvest

On (-90°, 180^°, 1 sec) Range: full range (deg, time)

Rocker

Fixed (0°) (Default) Range: full range (deg)

Output: IC volume Volume as defined by Stop Condition

Output: EC volume Volume as defined by Stop Condition

Protocol 11 : Harvest Cells Example

In an embodiment, this protocol relates to transferring cells once they are in suspension from the IC loop. Additional protocols described below relate to releasing the cells from the membrane 116 in the bioreactor to place them in suspension prior to harvest.

The protocol includes as follows:

1) Media is inputted from an IC source such as IC media through valve 250 and pump 254.

Alternatively reagent, wash solution or EC media could be the IC source. The media may be harvest media. As the cells are non-adherent and have been reloaded from the membrane, no tryspin is recirculated after release from the membrane.

2) Similarly EC media is provided through valve 276 and pump 278. Wash solution, reagent or IC media could also be introduced.

3) The IC inlet rate is 400 mL/min selected from a range from 100 to 500 mL.

4) The IC circulation rate is -AB% * Q_KA with AB% is V_AB * 100 / Via,. V_AB is the volume from point A to point B on Fig. 2 and ia, is the volume of the IC loop 202. Q_JCA is the pump rate of the inlet pump 254. In this example it is 69 mL/min. 5) The EC inlet rate is UFR₄₀₀ or the negative ultrafiltration rate required to have zero transmembrane pressure at the bioreactor outlet in co-current flow and IC inlet rate = 400 mL/min and EC waste valve 292 is closed. The upper range is 100 mL/min and in this example it is 60 mL/min.

6) The EC circulation rate is QECCM as described previously in a range up to 300 mL/min, for example 30 mL/min.

7) The outlet for the suspended cells is the harvest bag which receives the IC outlet.

8) The rocker control for bioreactor rotation is from -90° to 180° with 1 second pauses at the end position.

9) The stop condition for the protocol is IC volume 2 x VI_CL, for example 378 mL. The brief summary of the Harvest Cell protocol is as follows.

Protocol 1 1 Harvest Cells

Purpose of protocol: Transfers cells in suspension from the IC loop, including cells in the bioreactor, to the harvest bag.

Step 1 : Harvest Cells

Purpose of Step: Same as above

Protocol 12: Release Adherent Cells Example

In an embodiment, this protocol may be executed and followed prior to the Harvest Cell protocol. The first part of the protocol may include a change of IC/EC media. For example, a media such as PBS may be used to remove protein, calcium or magnesium form the suspension.

The second part of the protocol relates to the addition of a reagent such as trypsin to release the cells from the membrane 116. This is followed by a chase to the IC loop as well as mixing the reagent in the IC loop.

The protocol includes as follows:

1) Addition of wash solution through valve 270, 212 and pump 254 to IC side. Reagent solution, EC media or IC media are optional alternatives if they contain a solution such as PBS. In this example, 1370 mL of PBS was used.

2) If the cells are on the EC side the alternative would be for EC introduction of PBS.

3) The IC inlet rate is

QECA (number of IC Exc * VICE / (number of EC Exc * V_ECE)- ICE is the IC exchange volume VI_CL + icBL- ECE is the EC exchange volume V_ECL + V_ECBL-

4) The IC circulation rate is -AB% * QICA as described in the definitions which in this example is - 17mL/min.

5) The EC inlet rate is the lesser of Qioo or QMAX where oo = 100 (number of EC Exc * V_ECE) / (number of IC Exc. * VICE) and QM_A = 300. In this example the EC inlet rate is 148 mL/min.

6) The EC circulation rate is -CD% * QECA as defined in the definitions.

7) The outlet can be IC waste or EC waste or both through valves 290 or 292.

8) The rocker control for bioreactor 100 is -90°, 180° with 1 second pause at the end of the range of motion, or alternatively fixed.

9) The stop condition for the wash is the number of IC and EC exchanges, in this example 2.5 each.

10) The wash is followed by the reagent introduction such as tryspin to release the cells. This is from the reagent bag 244 through valve 248 and pump 254. At least a volume V_FTO i needed in the bag. 11) The IC inlet is 50 mL/min.

12) The IC circulation is 300 mL/min.

13) There is no EC inlet but circulation is QECCM or rate to keep EC loop mixed.

14) The rocker control is on as described above with chase.

15) The stop condition is the ARC stop or when the lower sensor 1264 detects air.

16) After air detection the ARC is filled with wash or alternatively IC or EC media to upper sensor 1268.

17) Mixing of the reagent continues in the IC loop for 4 minutes. The protocol summary is as set forth below.

Protocol Release Adherent Cells

Purpose of protocol: Releases cells from the membrane, leaving the cells in the IC Loop.

Step 1:

Purpose of Step: Performs Protocol IC/EC Washout in preparation for adding reagent. For example, the system replaces IC/EC media with PBS to remove protein, Ca^1"1", and Mg^ in preparation for adding trypsin.

Parameters to be tested:

• Check for any updates from Protocol IC/EC Washout. Step 2: Load Reagent

Purpose of Step: Loads reagent into the system until the bag is empty. Precondition: Need at least V_FTo of air in bag containing the reagent.

Step 4: Mix

Purpose of Step: Mixes the reagent within the IC Loop.

Protocol 13 : Condition Media

In an embodiment, this protocol oxygenates the EC media before the addition of cells to the IC side of the bioreactor 100. The initial steps of the protocol include:

1) The EC source is generally EC media without protein introduced through valve 276 by pump 278.

2) IC circulation is enough to prevent air introduction through the hollow fibers or QICCM- In this example, it is 20 mL/min.

3) The EC inlet rate is 0.1 mL/min.

4) The EC circulation rate is QECCE or the pump rate to equilibrate the EC loop. In this example it is 25 mL/min.

5) The outlet is EC waste through valve 292.

6) The rocker control is fixed with no rotation.

7) The stop for the high circulation rate conditioning is based on time from a range of 6 to 15 minutes.

8) A maintenance protocol is part of the condition media protocol.

9) The conditions for maintenance are the same as that outlined above, except that the EC circulation is reduced to QECCM which is the rate of the circulation pump to keep the EC loop mixed, for example

30 mL/min. Also, the stop for maintenance is a manual operator controlled stop. The maintenance is maintained until the operator desires cell load.

The summary of the protocol is as follows. Protocol Condition Media

Purpose of protocol: Oxygenates the media to proper concentrations before loading the cells. Step 1:

Purpose of Step: Accelerates the conditioning of the media using a high EC circulation rate.

Protocol 14: Coating Bioreactor Example Γη an embodiment, this protocol is directed to coating the IC side of the bioreactor with a reagent such as fibrenectin for cell attachment. Other reagents can be used. The protocol loads the reagent until the reagent bag is emptied, chases the reagent from the ARC, and circulates the reagent. In the protocol, the cell inlet bag contains VFTO or (1 + LP% / 100 * VICBL + 5 mL) as described in the definitions, according to embodiments. In this example, it is 40.2 mL.

The protocol includes:

1) Providing reagent from reagent bag through valve 248 and pump 254 to the IC side.

2) Cell inlet bag also may be open for fluid flow through valve 264.

3) There is no EC source or inlet rate.

4) The IC inlet rate is 10 mL/min.

5) The IC circulation rate is the maximum of (20, (min (300, 10 x QICA)) with Q_ICA being the inlet pump 254 rate. In this example, it is 100 mL/min.

6) EC circulation rate is QECCM as described previously as the circulation rate to keep to EC loop mixed. In this example, it is 30 mL/min.

7) The outlet is EC waste through valve 292.

8) The rocker control is off. Alternatively it could rotate from -90° to 180° with 1 second pauses at the end of the range of motion.

9) The stop condition for the reagent load is detection of air by lower sensor 1264 of the ARC. 10) After reagent load stop the ARC is loaded to upper sensor 1268 and gas evacuates through outlet 1224 and valve 260.

1 1) The chase can be IC media, wash or EC media provided through valve 270 if wash solution and pump 254 to the IC side.

12) The stop condition for the chase portion of the protocol is IC volume (VARCA + VARCBS) * 2. V_ARCA is the volume from the bottom of the ARC to point A on Fig. 2. VARCBS is the volume of the

ARC between sensors.

13) For circulation of the reagent, a low flow EC media is provided on the EC side. This may be media through valve 276 or from the reagent, IC media or wash bags through pump 278.

14) The EC inlet rate during circulation is 0.1 mL/min.

15) The IC inlet rate is QICCM which is the circulation pump 212 rate to keep the IC loop well mixed.

16) The EC circulation rate is QECCM which is the EC circulation pump 228 to keep the EC loop well mixed, in this example 30 mL/min.

17) The stop condition for circulation is either time selected or a manual stop. The protocol is summarized below.

Protocol Coat Bioreactor Purpose of Task: Coats the bioreactor membrane with a rea Step 1 : Load Reagent

Purpose of Step: Loads reagent into the system.

Precondition: Need at least Vp_To of air in the cell inlet bag.

Step 3 : Circulate

Purpose of Step: Circulates reagent in the IC Loop.

Protocol 15: Cell Attachment Example

In an embodiment, the purpose of this protocol is to enable adherent cells to adhere to the IC side of the membrane while allowing flow on the EC side. The cells are already in the IC side. The protocol includes as follows:

1) Only an EC source and EC circulation is used. There is no IC source, IC inlet rate or IC circulation rate.

2) The EC inlet is EC media with options for reagent, IC media, or wash. The media flows though valve 276 as EC media, and through pump 278.

3) The EC inlet rate is low 0.1 mL/min flow.

4) The EC circulation rate QECCM as described above which in this example is 30 mL/min.

5) The outlet is the EC waste through valve 290.

6) The rocker control is fixed or stationary.

7) The stop condition is a manual stop. Alternatively the stop could be based on time or EC volume.

The brief summary of the protocol is as shown below. Protocol Cell Attachment Purpose of protocol: Enables adherent cells to attach to the membrane while allowing flow on the EC loop. The pump flow rate to the IC loop flow is set to zero.

Step 1: Cell Attachment

Protocol 16: User-Defined Task Example

In an embodiment, this protocol allows the user to define the task. The setting options are as follows:

The disclosure further relates to the following embodiments for use with the cell expansion system.

Entering Pump Rates

According to embodiments, there are four task settings that require one to enter a pump rate: the IC Inlet Rate, the IC Circulation Rate, the EC Inlet Rate, and the EC Circulation Rate. Each setting corresponds to a button that appears on the Setup screen.

The following example describes how to enter a pump rate.

According to an embodiment, from the Setup screen:

1. Touch the button for the pump rate for which it is desired to change, such as IC Inlet Rate.

A data entry pad appears, and the button that was touched, IC Inlet Rate in this example, changes to black.

2. Enter the desired rate using the data entry pad.

The data entry pad displays the rate entered.

3. Touch Enter on the data entry pad.

The button now displays the rate entered, and it changes from black to its designated color. In this example, IC Inlet Rate displays the rate that was entered and changes from black to yellow.

Automatically Calculated Pump Rates

In accordance with embodiments of the present disclosure, a task can include a pump rate, such as the IC Circulation Rate, that the system automatically calculates based on another pump rate for that task, such as the IC Inlet Rate. To denote an automatically calculated pump rate, a note is included underneath the affected pump rate in the table of settings for the affected step, in embodiments.

According to embodiments, one can override an automatically calculated pump rate by entering the desired rate, as long as it is within the available options for that setting. However, one cannot override an automatically calculated rate if there are no other available options for that setting. The highlighted row in Table A is an example of how an automatically calculated pump rate that one can override appears in a table of settings, in embodiments. Table A: An example of an automatically calculated pump rate (override available)

The highlighted row in Table B is an example of how an automatically calculated pump rate that cannot override appears in a table of settings, according to embodiments.

Table B: An example of an automatically calculated pump rate (override not available)

Connect Sampling Coil

In accordance with embodiments of the present disclosure, the following instructions describe how to attach a sampling coil accessory set to the cell expansion set once the existing sample coil on the cell expansion set has been used.

1. Use a sterile tubing welder to attach the media source to the appropriate line on the cell expansion set.

2. Touch Task.

3. Touch Set Management.

4. Touch Connect Sampling Coil.

The Setup: Connect Sampling Coil screen appears, as shown below, which prompts one to select the IC Inlet Source and enter the chase volume.

The Setup: Connect Sampling Coil screen

5. Touch in the IC Inlet Source field.

A menu of IC inlet source options appears, and the IC Inlet Source field changes to black. The available IC inlet source options for this task include IC Media, Reagent, EC Media, and Wash.

6. Select the desired IC Inlet Source from the menu.

The IC Inlet Source field displays the option selected and changes to gray.

7. Touch in the Chase Volume field.

A data entry pad appears.

8. Enter the desired chase volume using the data entry pad.

The data entry pad displays the chase volume entered.

9. Touch Start.

The Connect Sampling Coil status screen appears, which includes a progress bar.

10. When the screen prompts one to connect the sampling coil, open the incubator door and uncoil the existing sample coil from the rocker assembly.

11. Remove the sample coil strain relief from the line.

12. Use a sterile tubing welder to attach one end of the sampling coil accessory set to one end of the existing sample coil.

13. Use a sterile tubing welder to attach the remaining end of the sampling coil accessory set to the remaining end of the existing sample coil.

14. Open the sterile welds.

15. Reconnect the sample coil strain relief to the sample coil line.

16. Re-coil the sample coil around the rocker assembly. 17. Connect the sample coil strain relief to the rocker assembly.

18. Close the incubator door.

19. Touch Next.

The system continues the task, and the system updates the Connect Sampling Coil status screen and the status message at each step throughout the task. When the system completes the task the home screen appears, the system changes to an idle state, and the status line displays Idle.

Load Cells Without Circulation

Purpose: loads the cells into the bioreactor from the cell inlet bag until the bag is empty. This task does not use IC circulation to distribute the cells, according to embodiments. This task includes two separate steps in embodiments:

• Step 1 : loads the cells from the cell inlet bag into the bioreactor.

• Step 2: chases the cells from the ARC to the bioreactor. Larger chase volumes spread the cells and move them towards the IC outlet.

Table C describes the bags of solution needed to attach to each line when performing Load Cells Without Circulation, according to embodiments of the present disclosure. These solutions and corresponding volumes are based on the factory default settings for this task.

Before starting this task, one must satisfy the following preconditions, in embodiments:

• Include a minimum of approximately 40 mL of air in the cell inlet bag.

• Follow instructions related to, "Using the In-line Filter 200 Micron Accessory Set" , to add the inline filter to the cell inlet line of the cell expansion set, if desired.

Table C: Solutions for Load Cells Without Circulation

Load Cells Without Circulation pathway: Task>Load and Attach>Load Cells Without Circulation

1. Confirm the settings for step 1 shown in Table D.

Table D: Step 1 Settings for Load Cells Without Circulation

Setting Factory Default Setting Options

2. Confirm the settings 3 for step 2 shown in Table E,

Table E: Step 2 Settings for Load Cells Without Circulation

Setting Factory Default Setting Options

IC Inlet IC Media Reagent, IC Media, Wash, EC Media

IC Inlet Rate 50 mL/min Same as Step 1

IC Circulation Rate 0 mL/min Same as Step 1

EC Inlet None N/A

EC Inlet Rate 0 mL/min N/A

EC Circulation Rate 30 mL/min Same as Step 1

Outlet EC Waste N/A

Rocker Control In Motion (-90°, 180°, Same as Step 1

1 sec)

Stop Condition IC Volume (47 mL) IC Volume (1 to 200 mL)

3. Touch Start.

4. Check the status line to confirm that the task started.

5. Verify that there are no contents left in the bag.

When the system completes the task the home screen appears, the system changes to an idle state, and the status line displays Idle.

IC EC Washout Through Membrane

Purpose: replaces small molecule components on the IC side, which pass through the membrane either by diffusion or by ultrafiltration, according to embodiments. IC components retained by the membrane are not removed from the IC circulation loop. Components on the EC side are washed out by fluid replacement. The replacement volume is specified by the number of IC Volumes and EC Volumes exchanged, in embodiments. Table F describes the bags of solution needed to attach to each line when performing IC EC

Washout Through Membrane, in embodiments. These solutions and corresponding volumes are based on the factory default settings for this task.

Table F: Solutions for IC EC Washout Through Membrane

IC EC Washout Through Membrane pathway: Task>Washout>IC EC Washout Through

Membrane

1. Confirm the settings for IC EC Washout Through Membrane shown in Table G.

Table G: Settings for IC EC Washout Through Membrane

Setting Factory Default Setting Options

Stop Condition Exchange Exchange (0.5 to 5.0 IC Volumes) (0.5 to 5.0 EC

(1 IC Volumes) Volumes)

(1 EC Volumes)

2. Touch Start.

3. Check the status line to confirm that the task started.

Feed Cells

Purpose: continuously adds a low flow rate to the IC circulation loop and/or the EC circulation loop, according to embodiments. There are several outlet settings that one can use to remove the fluid added to the system during this task.

Table H describes the bags of solution needed to attach to each line when performing Feed Cells, in embodiments. These solutions and corresponding volumes are based on the factory default settings for this task.

Table H: Solutions for Feed Cells

2. Touch Start.

3. Check the status line to confirm that the task started.

4. Touch Finish when ready to complete the task.

5. Touch Yes.

The home screen appears, the system changes to an idle state, and the status line displays Idle.

Feed Cells With Ultrafiltration

Purpose: continuously adds fluid at a low flow rate to the IC circulation loop and/or the EC circulation loop, according to embodiments. If one uses the factory default settings for this task and the solution volumes based on those defaults, large molecules could become concentrated in the IC circulation loop, and then the task would use ultrafiltration to remove excess fluid on the IC side of the bioreactor.

Table J describes the bags of solution needed to attach to each line when performing Feed Cells With Ultrafiltration, in embodiments. These solutions and corresponding volumes are based on the factory default settings for this task.

Table J: Solutions for Feed Cells With Ultrafiltration

Feed Cells With Ultrafiltration pathway: Task>Feed and Add>Feed Cells With Ultrafiltration

1. Confirm the settings for Feed Cells With Ultrafiltration shown in Table K.

Table K: Settings for Feed Cells With Ultrafiltration

2. Touch Start.

3. Check the status line to confirm that the task started.

4. Touch Finish when ready to complete the task.

5. Touch Yes.

The home screen appears, the system changes to an idle state, and the status line displays Idle. Add Fluid Continuously

Table L describes the bags of solution needed to attach to each line when performing Add Fluid Continuously. These solutions and corresponding volumes are based on the factory default settings for this task.

Table L: Solutions for Add Fluid Continuously

Add Fluid Continuously pathway: Task>Add>Add Fluid Continuously

1. Confirm the values for each setting for Add Fluid Continuously shown in Table M.

Table M: Settings for Add Fluid Continuously

2. Touch Start.

3. Check the status line to confirm that the task started.

4. Touch Finish when ready to complete the task.

5. Touch Yes.

Add Fluid Continuously With Ultrafiltration

Purpose: continuously adds fluid at a low flow rate to the IC circulation loop and/or the EC circulation loop, in accordance with embodiments of the present disclosure. If one uses the factory default settings for this task and the solution volumes based on those defaults, large molecules could become concentrated in the IC circulation loop, and then the task would use ultrafiltration to remove excess fluid on the IC side of the bioreactor.

Table N describes the bags of solution needed to attach to each line when performing Add Fluid Continuously With Ultrafiltration, in embodiments. These solutions and corresponding volumes are based on the factory default settings for this task.

Table N: Solutions for Add Fluid Continuously With Ultrafiltration

Add Fluid Continuously With Ultrafiltration pathway: Task>Add>Add Fluid Continuously With Ultrafiltration

1. Confirm the settings for Add Fluid Continuously With Ultrafiltration shown in Table O.

Table O: Settings for Add Fluid Continuously With Ultrafiltration

4000 mL), EC Volume (1 to 4000 mL)

2. Touch Start.

3. Check the status line to confirm that the task started.

4. Touch Finish when ready to complete the task.

5. Touch Yes.

The home screen appears, the system changes to an idle state, and the status line displays Idle. Custom Tasks

According to embodiments of the present disclosure, the system includes five Custom tasks: Custom 1, Custom 2, Custom 3, Custom 4, and Custom 5. A Custom task allows one to enter all of the settings for a task manually. In embodiments, the system does not save the settings manually entered for a Custom task, so one must enter the settings each time the task is performed; however, one can configure the settings for each Custom task. For information about configuring the default settings for a Custom task, see "Configuring Default Settings for Tasks.". Table P shows the factory default settings and all the possible setting options for all of the Custom tasks, in accordance with

embodiments.

Table P: The factory defaults and setting options for all of the Custom tasks

The following example explains how to select, setup, and start a Custom task.

1. Touch Task.

2. Touch Custom.

3. Touch Custom 1.

The Setup Confirmation screen appears for Custom 1.

4. Touch Modify to select the settings for the task. Table P shows all the possible setting options for all of the Custom tasks, according to embodiments of the present disclosure.

5. Touch Start.

6. Check the status line to confirm that the task stalled.

Configuring Display Settings

According to embodiments of the present disclosure, one can configure certain display settings for the system from the Configuration: Display screen. The following instructions describe how to access the Configuration: Display screen.

1. Touch Configuration.

The Configuration Selection screen appears, as shown below:

The Configuration Selection screen 2. Touch Configure Display Settings. The Configuration: Display screen appears, as shown below:

The Configuration: Display screen

In embodiments, one can perform the following actions from the Configuration: Display screen:

• Change the format of the date display.

• Set the current date.

• Change the format of the time display.

· Set the current time.

• Change the type of decimal separator that the system uses.

• Change the language in which the system displays information.

Changing the Date Format

In embodiments, the default date format is MM-DD-YYYY. The date format can be changed to either DD-MM-YYYY or YYYY-MM-DD, according to embodiments.

From the Configuration: Display screen:

1. Touch the button that shows the desired date format.

The button selected changes to black.

2. Touch Save.

The system saves and applies the changes, and the Configuration: Display screen closes.

Setting the Current Date

In embodiments, from the Configuration: Display screen: 1. Touch in the Month field.

A data entry pad appears.

2. Use the data entry pad to enter the month.

3. Touch Enter.

The Month field displays the value entered.

4. Touch in the Day field.

A data entry pad appears.

5. Use the data entry pad to enter the day.

6. Touch Enter.

The Day field displays the value entered.

7. Touch in the Year field.

A data entry pad appears.

8. Use the data entry pad to enter the year in the four-digit format (YYYY).

9. Touch Enter.

The Year field displays the value entered.

10. Touch Save.

The system saves the changes, and the Configuration: Display screen closes. Changing the Time Format

In embodiments, the default time format is the 24-hour clock. One can change the time format to the 12-hour clock.

From the Configuration: Display screen:

1. Touch the button that shows the desired time format.

The button selected changes to black.

2. Touch Save.

The system saves and applies the changes, and the Configuration: Display screen closes. Setting the Current Time

In embodiments, from the Configuration: Display screen:

1. Touch in the Hour field.

A data entry pad appears.

2. Use the data entry pad to enter the hour.

3. Touch Enter.

The Hour field displays the value entered.

4. Touch in the Minute field.

A data entry pad appears.

5. Use the data entry pad to enter the minutes. 6. Touch Enter.

The Minute field displays the value entered.

7. Touch in the Second field.

A data entry pad appears.

8. Use the data entry pad to enter the seconds.

9. Touch Enter.

The Second field displays the value entered.

10. Touch Save.

Changing the Decimal Separator

In embodiments, the default decimal separator is the period (.). One can change the decimal separator to a comma (,).

From the Configuration: Display screen:

1. Touch the button that shows the desired decimal separator.

The button selected changes to black.

2. Touch Save.

The system saves and applies the changes, and the Configuration: Display screen closes. Changing the Language Used to Display Information

In embodiments, the default language used to display information is English.

From the Configuration: Display screen:

1. Touch in the Language field.

The language selection window appears.

2. Touch the desired language.

The Language field displays the selected language.

3. Touch Save.

The system saves the changes, and the Configuration: Display screen closes. In embodiments, the system is restarted to display information in the new language.

Configuring System Settings

According to embodiments of the present disclosure, one can configure certain system settings from the Configuration: System screen. The following instructions describe how to access the

Configuration: System screen.

1. Touch Configuration.

The Configuration Selection screen appears. 2. Touch Configure System Settings.

The Configuration: System screen appears, as shown below:

Configuration: System

The Configuration: System screen

In embodiments, one can perform the following actions from the Configuration: System screen:

• Turn the incubator on or off.

• Change the temperature set point for the system.

· Configure the low-temperature alarm.

• Turn the alarm sound on or off.

Turning the Incubator On or Off

According to an embodiment, from the Configuration: System screen:

1. Under Incubator, touch On or Off.

The button selected changes to black.

2. Touch Save.

The system saves and applies the changes, and the Configuration: System screen closes. Changing the Temperature Set Point

In embodiments, the default temperature set point is 37 °C. The range for the temperature set point is 34 to 40 °C.

From the Configuration: System screen:

1. Touch in the Temperature Set Point field. A data entry pad appears.

2. Use the data entry pad to enter the desired temperature.

3. Touch Enter.

The Temperature Set Point field displays the value entered.

4. Touch Save.

The system saves and applies the changes, and the Configuration: System screen closes. Configuring the Low-Temperature Alarm

In embodiments, the low-temperature alarm allows one to specify a certain number of degrees, and when the system reaches that many degrees below the set point it triggers an alarm. One can also turn off the low-temperature alarm. The following instructions explain how to turn on and configure the low-temperature alarm.

From the Configuration: System screen:

1. Under Low-Temperature Alarm, touch On.

On changes to black.

2. Touch in the Difference From Set Point field.

A data entry pad appears.

3. Use the data entry pad to enter the desired number of degrees (within a 1 to 5 °C range).

4. Touch Enter.

The Difference From Set Point field displays the value entered.

5. Touch Save.

The system saves and applies the changes, and the Configuration: System screen closes.

Turning the Alarm Sound On or Off

In embodiments, from the Configuration: System screen:

1. Under Alarm Sound, touch On or Off.

The button selected changes to black.

2. Touch Save.

The system saves and applies the changes, and the Configuration: System screen closes. Configuring Default Settings for Tasks

According to embodiments of the present disclosure, the system allows one to configure the default settings for each task. When one configures the default settings for a task, the system replaces the factory default settings with the configured settings, so each time the task is selected, it automatically populates with the configured default settings. The system also allows one to reset a task, which restores all of the settings for a selected task back to its factory default settings. When configuring a task, one can only configure settings that are available for that task, in embodiments. If a certain setting cannot be configured, the button for that setting is not enabled. In embodiments, one can use the task setting tables listed for each step of a task as guidance for the available settings when configuring a task. The following example describes how to configure the default settings for Release Adherent Cells With Harvest.

1. Touch Configuration.

The Configuration Selection screen appears.

2. Touch Configure Default Settings for Tasks.

The Task Defaults Selection screen appears.

3. Touch Release and Harvest.

4. Touch Release Adherent Cells With Harvest.

The Configure Confirmation screen appears, as shown

The Configure Confirmation

5. Touch Configure above the step for which it is desired to configure settings. The Configure Defaults screen appears for that step, as shown below:

The Configure Defaults screen

6. Touch the button for the setting to configure, and change that setting, as desired.

7. Repeat step 6 for any other settings to configure for that step of the task.

8. Touch Next Step to configure the settings for the following step, or touch Confirm to return to the Configure Confirmation screen.

9. From the Configure Confirmation screen, touch Save.

The system saves and applies the changes, and the home screen appears.

Adding a Step to a Custom Task

In embodiments, the factory default for a Custom task is a single step, but one can configure a Custom task to have multiple steps. There are six steps that one can add to a Custom task: · Wash Out Lines

• Wash Out Lines Through Membrane

• Wash Rapidly

• Harvest Cells

• Add Bolus

· Custom

Each step includes factory default settings, which one can configure using the Configure button. For more information on configuring default settings see "Configuring Default Settings for Tasks." Tables Q, R, S, T, U, and V below show the factory default settings and all the possible setting options for each available step, according to embodiments of the present disclosure.

Table Q: Wash Out Lines

Table S: Wash Rapidly

Table T: Harvest Cells

Table U: Add Bolus

Setting Factory Default Setting Options

IC Inlet Reagent Reagent, IC Media, Wash, EC Media, None

IC Inlet Rate 10 mL/min 0 to 200 mL/min

Table V: Custom

The following example explains how to add a step to a Custom task during configuration, according to an embodiment.

1. Touch Configuration.

2. Touch Configure Default Settings for Tasks.

The Task Defaults Selection screen appears.

3. Touch Custom.

4. Touch the Custom task to configure, such as Custom 1.

The Configure Confirmation screen appears for the selected task.

5. Touch Add Step.

The step selection window appears, as shown below:

The step selection window

6. Touch the desired step, such as Wash Out Lines.

The factory default settings for the step selected now appear on the Configure Confirmation screen. Note: To remove the step added, touch the remove button located above that step.

7. Touch Save.

The system saves and applies the changes, and the home screen appears.

It will be apparent to those skilled in the art that various modifications can be made to the apparatus, systems, and methods described herein. Thus, it should be understood that the embodiments are not limited to the subject matter discussed in the Specification. Rather, the present disclosure is intended to cover modifications, variations, and/or equivalents. The acts, features, structures, and/or media are disclosed as illustrative embodiments for implementation of the claims. The invention is defined by the appended claims.

Claims

What is claimed is:

1. A method of controlling a process in a cell expansion system, the method comprising: providing a fluid conveyance assembly, wherein the fluid conveyance assembly comprises a bioreactor; engaging the fluid conveyance assembly; providing an air removal chamber, wherein the air removal chamber is mounted on the fluid conveyance assembly, and wherein the air removal chamber comprises a fluid containment chamber, the fluid containment chamber comprising: a fluid entrance aperture; a fluid exit aperture, wherein the fluid exit aperture is coupled to a fluid exit tube; and a vent aperture, wherein the vent aperture is located above the fluid entrance aperture and the fluid exit aperture; providing a pump to pump a fluid through the fluid entrance aperture and into the fluid containment chamber of the air removal chamber; initiating the process, comprising: operating the pump to pump the fluid through the fluid entrance aperture and into the fluid containment chamber, wherein the fluid reaches a fluid level in the fluid containment chamber; allowing the fluid to pass through the fluid exit aperture to enter the fluid exit tube; providing a sensor to detect the fluid level in the fluid containment chamber; detecting the fluid level using the sensor; providing a stop condition, comprising: meeting the stop condition when the fluid level in the fluid containment chamber reaches a predetermined level as detected by the sensor; and when the fluid level in the fluid containment chamber is at the predetermined level, stopping the process based on meeting the stop condition.

2. The method as defined in claim 1, wherein providing the stop condition comprises meeting the stop condition when the sensor detects air.

3. The method as defined in claim 2, wherein providing the sensor comprises providing an ultrasonic sensor.

4. The method as defined in claim 2, wherein providing the sensor comprises providing an optical sensor.

5. The method as defined in claim 1, wherein the process comprises chasing the fluid from the air removal chamber.

6. The method as defined in claim 1, further comprising: when the fluid level in the fluid containment chamber is higher than the predetermined level, continuing to pump the fluid through the fluid entrance aperture and into the fluid containment chamber.

7. The method as defined in claim 1, wherein the process comprises loading media from a media bag into the bioreactor until the media bag is empty, wherein the media is the fluid.

8. The method as defined in claim 7, wherein the process comprises loading cells, and wherein the media bag is a cell inlet bag.

9. The method as defined in claim 7, wherein the process comprises loading a reagent, and wherein the media bag is a reagent bag.

10. The method as defined in claim 1, wherein the process comprises a step from a protocol, and wherein the protocol comprises one of: loading cells into the bioreactor, comprising: using a high flux cell load, loading cells into the bioreactor, comprising: using a load with circulation, adding reagent, releasing adherent cells, or coating the bioreactor.

11. The method as defined in claim 1, further comprising: a second sensor to detect a top level of the fluid level in the fluid containment chamber.

12. A method of operating a cell expansion system with a stop condition, the method comprising: selecting a protocol to load media into a bioreactor of the cell expansion system, wherein the protocol comprises a first process; determining whether a condition for the first process is set; when the condition for the first process is not set, setting the condition; selecting the stop condition for the first process, wherein the stop condition comprises a detection of a gas/fluid interface in an air removal chamber; and selecting to execute the protocol.

13. The method as defined in claim 12, wherein the protocol further comprises a second process, the first process comprising loading the media from a media bag into the cell expansion system until the media bag is empty, and the second process comprising chasing the media from the air removal chamber into a circulation loop of the cell expansion system.

14. The method as defined in claim 13, wherein the circulation loop comprises an intracapillary loop.

15. The method as defined in claim 12, wherein selecting a protocol to load media into the bioreactor comprises: selecting the media, the media comprising one of: cells from a cell inlet bag, or reagent from a reagent bag.

16. The method as defined in claim 12, wherein one or more sensors detect the gas/fluid interface at a predetermined measuring position within the air removal chamber.

17. The method as defined in claim 16, wherein the one or more sensors comprise an ultrasonic sensor.

18. The method as defined in claim 12, wherein the protocol comprises one of: loading cells into the bioreactor, comprising: using a high flux cell load, loading cells into the bioreactor, comprising: using a load with circulation, adding reagent, releasing adherent cells, or coating the bioreactor.

19. A cell expansion system comprising a capability to stop a process, wherein the stopping of the process is automated, the system comprising: a fluid conveyance assembly, wherein the fluid conveyance assembly comprises a bioreactor; an air removal chamber, the air removal chamber comprising a fluid containment chamber, wherein the fluid containment chamber comprises: a fluid entrance aperture; a fluid exit aperture; and a vent aperture, wherein the vent aperture is located above the fluid entrance aperture and the fluid exit aperture; at least one sensor for detecting a fluid in the fluid containment chamber; and a controller, in communication with the at least one sensor, wherein the controller is operable to: signal to start the process, comprising: signal to start the one or more pumps for pumping the fluid through the fluid entrance aperture and into the fluid containment chamber of the air removal chamber; receive an indication from the at least one sensor when a lack of the fluid is detected by the at least one sensor; and in response to receiving the indication from the at least one sensor, altering the one or more pumps.

20. The cell expansion system as defined in claim 19, wherein the altering the one or more pumps comprises: stopping the one or more pumps to stop the process.

21. The cell expansion system as defined in claim 19, wherein the process comprises loading, by the one or more pumps, media from a media bag through the air removal chamber and into an intracapillary side of the bioreactor until the media bag is empty, and wherein the media is the fluid.

22. The cell expansion system as defined in claim 19, wherein the process comprises a step from a protocol, and wherein the protocol comprises one of: loading cells into the bioreactor, comprising: using a high flux cell load, loading cells into the bioreactor, comprising: using a load with circulation, adding reagent, releasing adherent cells, or coating the bioreactor.

23. The cell expansion system as defined in claim 19, wherein the at least one sensor is an ultrasonic sensor, and wherein the at least one sensor detects the lack of fluid by sensing air.