Source: https://patents.google.com/patent/JP2008501365A/en
Timestamp: 2019-11-14 09:45:37
Document Index: 717270114

Matched Legal Cases: ['Application No. 60', 'Application No. 60', 'Application No. 60', 'Application No. 10', 'Application No. 1', 'Application No. 6', 'art 24', 'art 24']

JP2008501365A - Generation of shear force in the reactor - Google Patents
Generation of shear force in the reactor Download PDF
JP2008501365A
JP2008501365A JP2007527675A JP2007527675A JP2008501365A JP 2008501365 A JP2008501365 A JP 2008501365A JP 2007527675 A JP2007527675 A JP 2007527675A JP 2007527675 A JP2007527675 A JP 2007527675A JP 2008501365 A JP2008501365 A JP 2008501365A
JP2007527675A
アンドレイ ジェイ． ザルア，
ブライアン オー． ベノア，
ジョージ ジェイ． ベラ，
セス ティー． ロジャース，
2004-06-07 Priority to US57797704P priority
2005-06-07 Application filed by バイオプロセッサーズ コーポレイション filed Critical バイオプロセッサーズ コーポレイション
2008-01-24 Publication of JP2008501365A publication Critical patent/JP2008501365A/en
In certain embodiments, a biological or biochemical that has the ability to apply shear stress to a liquid sample component and has a volume of less than about 2 mL and includes a liquid sample and a shear stress generating element. An apparatus for performing a biological or biochemical reaction including a reactor is disclosed. The shear stress generating element is included in the device, and the entire shear stress generating element is rotationally moved along a selected motion path that intersects a first location in the device and a second location in the device. Constructed and arranged to move with or without rotational movement. Also, moving a liquid or gas shear stress generating element along a selected operating path in the device to generate a reproducible and controllable level of shear stress at selected locations within the liquid sample. A method of applying shear stress to a component of a liquid sample is also disclosed.
This application is based on US Patent Act 119 (e) 35, US Provisional Application No. 60 / 577,977 entitled “Gas Control in a Reactor” filed on June 7, 2004, June 6, 2004. US Provisional Application No. 60 / 577,986 entitled “Reactor Mixing” filed on May 7, US Provisional Application No. 60/57 entitled “Creation of Shear in a Reactor” filed on December 14, 2004 It claims priority to 636,420. Each of these is hereby incorporated by reference in its entirety.
This specification discloses the generation of shear forces in a reaction system, and in certain embodiments, the generation of shear forces that affect the behavior of living cells.
Cells are cultured for a variety of reasons. Cell culture aimed at proteins or other beneficial substances produced by cells is increasing. Typically, the cells need to be maintained in a unique state with respect to viable and / or optimal growth and / or production capacity, and for many cell cultures, the maintenance of conditions such as the use of a controlled environment May be necessary or effective. The presence of other factors such as nutrients, metabolic gases such as oxygen and / or carbon dioxide, proper levels of humidity and temperature, can affect cell growth and / or cell behavior. Cells need time to proliferate during which favorable conditions should be maintained. In some cases, as in the case of special bacterial cells, cell culture may be successful with a run time as short as 24 hours. In other cases, such as when handling special mammalian cells, it may take about 30 days or more for successful culture.
Typically, cell culture is performed in a medium containing the necessary nutrients that is suitable for cell growth. Cells are generally cultured in locations such as incubators where environmental conditions can be controlled. Incubator sizes have traditionally been carefully maintained from several cultures and / or small incubators for small culture volumes (eg, about 1 cubic foot or less) to maintain the desired environmental conditions. It can extend to an entire room or multiple rooms.
More generally, a wide range of reaction systems for producing chemical reactions, biochemical reactions and / or products of biological systems are known. Chemical plants including catalysis, biochemical fermenters, pharmaceutical plants and other system hosts are well known. Biochemical treatment may involve the use of living microorganisms (eg, cells) to produce certain substances.
As described in US patent application Ser. No. 09 / 707,852, filed Nov. 7, 2000, entitled “Microreactor,” which is incorporated herein by reference, cells are microscale. In particular, many cultures may be performed in parallel because they may be cultured in (ie, a culture volume of about a few milliliters or less).
While significant and valuable advances have been made in the field of cell culture and other areas, improvements are believed to be beneficial.
The following co-owned application relating to methods and devices and / or materials relating to the related subject matter and / or useful or potentially useful for the practice of the present invention, namely by Rodgers et al. 2003 US patent application Ser. No. 10 / 457,017 entitled “System and Method for Process Automation” filed Jun. 5, 2003; filed Jun. 5, 2003 by Rodgers et al. US patent application Ser. No. 10 / 457,049 entitled “Materials and Reactor Systems having Humidity and Gas Control” published as / 0058437, Miller et al., June 5, 2003 US patent application Ser. No. 10 / 457,015 entitled “Reactor Systems Having a Light-Interacting Component” filed on March 25, 2004 and published as 2004/0058407 on June 25, 2004, by Zarur et al. US Patent Application No. 10 / 456,929, entitled “Apparatus and Methods for Manufacturing Substrates”, filed on September 16, 2003 and published on July 8, 2004 as 2004/0132166. US Patent Application No. 1 entitled “Determination and / or Control of Reactor Environmental Conditions” No. 0 / 664,046, entitled “Systems and Methods for Control of pH and Other Reactor Environmental Conditions,” filed September 16, 2003 and published as 2005/0026134 on Miller et al. US patent application Ser. No. 10 / 664,068, US patent application Ser. No. 10 / 664,067 entitled “Microreactor Architecture and Methods” filed September 16, 2003 by Rodgers et al. And Rodgers et al. US Patent Application No. 6 entitled "Control of Reactor Environmental Conditions" filed on the same day / No. 577,985 are each hereby incorporated by reference.
This specification discloses related systems such as chemical, biological and / or biochemical reactor chips and / or reactors and microreactor systems. In some cases, the subject matter of the present invention encompasses interrelated products, alternative solutions to a particular challenge, and / or multiple different uses of one or more systems and / or articles.
According to one embodiment of the present invention, an apparatus capable of applying shear stress to a liquid sample component for performing a biological or biochemical reaction includes a vessel having a volume of less than about 2 mL. Equipped with a chemical or biochemical reactor, the container contains a liquid sample. The apparatus also includes a shear stress generating element that does not include a vessel or conduit surface that contacts the liquid, the shear stress generating element being included in the apparatus, and the entire shear stress generating element being a first in the apparatus. And is constructed and arranged to move with or without rotational movement along a selected movement path that intersects a second location in the apparatus.
In accordance with another embodiment of the present invention, an apparatus capable of applying shear stress to a liquid sample component for performing a biological or biochemical reaction includes a biological sample containing a liquid sample. Or a biochemical reactor is provided. The apparatus also includes a shear stress generating element that does not include a surface of a container or conduit that contacts the liquid, the shear stress generating element is included in the container, and the entire shear stress generating element is the first in the container. And is constructed and arranged to move along a selected motion path that intersects a second location in the container and a second location in the container. In this embodiment, the change in operation of the shear stress generating element in the vessel that causes a change in the level or pattern of shear stress in the liquid sample does not significantly affect gas exchange between the liquid sample and the exterior of the reactor.
According to yet another embodiment of the present invention, an apparatus capable of applying shear stress to a liquid sample component for performing a biological or biochemical reaction comprises a biological or biochemical container. And a vessel containing a liquid sample. The device also generates shear stress generating elements within the device that are movable within the device when the device is flipped and the generation of reproducible and controllable levels of shear stress at selected locations within the liquid sample. And a control system configured to control the operation of the shear stress generating element to facilitate.
According to another embodiment of the present invention, a method of applying shear stress to a biological or biochemical component of a liquid sample contained in a container operates a shear stress generating element in the container containing the liquid sample and And / or controlling its operation, wherein the operation of the shear stress generating element occurs upon inversion of the container, the operation being performed at a selected location within the liquid sample at a biological or biochemical component Apply reproducible and controllable levels of shear stress.
In another embodiment of the present invention, an apparatus capable of applying a shear stress to a liquid sample component for performing a biological or biochemical reaction includes a container configured to contain a liquid sample. A biological or biochemical reactor is provided, and the surface of the container includes a membrane having an oxygen transmission rate of 0.061 O 2 mol / (day · m 2 · atm) or more. The apparatus is further included in the container, and when the container contains a liquid sample, the entire shear stress generating element intersects a first location in the container and a second location in the container during operation. A shear stress generating element constructed and arranged to move along the selected motion path.
In yet another embodiment of the invention, the method of applying a shear stress to a biological or biochemical component of a liquid sample is reproducible to the biological or biochemical component at a selected location within the liquid sample and To apply a controllable level of shear stress, the entire shear stress generating element is moved within the device along a selected operating path that intersects a first location within the device and a second location within the device. Including free movement in a suspended manner, the shear stress generating element is either a gas or a liquid.
According to a further embodiment of the invention, an apparatus capable of applying shear stress to a liquid sample component for performing a biological or biochemical reaction has a volume of less than about 2 mL and a liquid sample A biological or biochemical reactor comprising a container containing The apparatus also includes a shear stress generating element that does not include the surface of the container or conduit that contacts the liquid, the shear stress generating element being included in the container and constructed and arranged to pivot within the container. And the pivoting motion produces a reproducible and controllable level of shear stress at selected locations within the liquid sample.
The present specification discloses reaction systems, such as chemical, biological and / or biochemical reactor chips and / or microreactor systems, and systems and methods for using such devices. In certain embodiments of the present invention, a chip, reactor or reaction system containing a liquid sample may be used as a reaction site container (hereinafter simply referred to as a “container”), such as a cell culture chamber, for example, to apply a specific shear stress to the cells. For the purpose of reproducibly controlling and / or generating shear stress. Shear stress can have a dramatic effect on the behavior of many types of living cells, for example by changing one or more of protein production, gene expression, cell morphology or likelihood of cell death. it can. Shear stress is determined using shear stress generating elements such as bubbles, solid beads (eg, glass or plastic balls), magnetic activation elements (eg, magnetic beads) and / or liquid masses that are immiscible with the liquid sample. May be generated.
Certain chemical and pharmaceutical bioreactors, including large-scale bioreactors, can hydrobiologically shear biological cells via mixing impellers and / or gas distribution and / or various other pumping and / or mixing means. To be exposed to. Due to the various effects of shear stress on living cells in these bioreactors, the success of bioreactor operation may depend on the generation of an adequate amount of hydrodynamic shear stress. Data obtained from the microreactor system described herein can be used to design, operate or modify larger scale bioreactors, particularly in connection with shear stress generation. In certain embodiments, data obtained from or known about the shear stress exposure pattern of cells in a larger reactor is more extensive under conditions of more realistic shear stress exposure. It may be simulated in a microreactor system provided by the present invention to test and / or optimize the effects of other changes in the operation and / or design of the reaction system. In addition, the ability to bring selected hydrodynamic shear stress exposure to cells and / or control hydrodynamic shear stress exposure for larger reaction system designs, both in its entirety, is hereby incorporated by reference. US patent application entitled “Methods of Providing Biochemical Analyzes”, filed on the same date as this application, and filed on the same date as this application, and attorney docket number B1102 filed on the same date as this application. 70044US00, which is described in a US patent application entitled “Microreactor Simulation of Macroreactor”. Furthermore, the ability to bring selected hydrodynamic shear stress exposure to cells and / or control cellular hydrodynamic shear stress exposure becomes increasingly important in technologies involving human tissue engineering and extracorporeal organ assist devices. It's getting on.
For example, in typical conventional small cell culture systems such as well plates and multiple shake flasks, it is difficult to control the generation of similar levels of shear stress at specific locations within multiple containers. For example, placing the well plate on a conventional mixing / shaking device places the well in a different position and / or orientation relative to the shaker mechanism. The liquid in one well of a well plate may tend to move in a very different manner than in another well, thus making it difficult to generate similar shear forces in multiple wells Become.
In certain embodiments of the invention, multiple sample vessels are similarly positioned and oriented on the same rotating device. With such a configuration, the effect of changing certain parameters at a controlled shear stress level may be tested in parallel.
In addition, certain cell culture systems, such as systems that include multiple well plates or shake flasks, capable of performing parallel processing and / or high throughput (eg, by changing migration or shaking speed). Changing the parameter affecting the shear stress operates to substantially change the amount of surface area at the interface between the liquid sample and the gas, thereby affecting the gas exchange rate.
In certain embodiments of the invention, the shear stress may be controlled substantially independently of the rate of gas exchange with the liquid sample, and thus the level and / or pattern of shear stress within the liquid sample. Is not significantly affected by the amount of surface area at the interface between the liquid sample and the gas, and therefore typically has a substantial effect on the gas exchange rate between the liquid sample and the outside of the reactor containing the liquid sample. Does not affect the top.
Such an embodiment is functionally associated with a shear stress generating element in the reactor and the reactor, and for example gravity, centrifugal force, mechanical force, air pressure, liquid pressure, magnetic force and / or electrical force. A control system, such as a computer-implemented process control system, configured to move the shear stress generating element and / or control the operation of the shear stress generating element through the application of an external force such as .
In typical conventional systems, such as perfusion systems and rotating drum systems that can allow for some control of shear forces, a relatively large volume of liquid sample, for example, exceeding 5 milliliters, may be required for operation. . In addition, many such systems require a separate force / flow generating component for each liquid sample. For example, in a perfusion system, each container to be perfused often requires a separate pump and / or controller, and in a rotating drum system, each rotating drum assembly or small group of rotating drum assemblies is a separate motor. And / or a controller is often required.
Certain embodiments of the present invention often include methods and systems that allow for the controllable generation of shear stress in a container without the use of a pump external to the container. In some such embodiments, immiscible materials such as bubbles, immiscible liquids or solids are used as shear stress generating elements in the container so that the movement of the immiscible material generates shear stress in the container. The In some embodiments, a bubble (or other immiscible substance) is placed in a container such as a reaction site container and is moved relative to the liquid sample present in the reaction site container by reorienting the reaction site container. Is done. The density difference between the immiscible material and the liquid sample results in the operation of the immiscible material via gravity and / or centrifugal force.
Containers used in accordance with the present invention may have a small volume and / or multiple containers on a single chip so that multiple containers can be efficiently reoriented and / or controlled. It may be supplied. In some cases, shear stress is regenerated in multiple containers using a single mechanism that applies force and, in certain embodiments, in multiple containers, to produce motion of the shear stress generating element. It may be generated into a possible expression. For example, in certain embodiments, a plurality of chips including a plurality of containers each including a shear stress generating element are attached to a single device configured to rotate a plurality of chips (eg, FIG. 4). reference). Facilitating parallel testing of multiple liquid samples can efficiently achieve the effect of shear stress on many different cells under many different shear stress exposure conditions.
In typical conventional cell culture reaction systems, such as shake flasks and well plates, shear stress may be applied to cells contained in the liquid sample using a rotating stir bar inside the reactor and / or Alternatively, the shear stress is a cell culture that includes sufficient gas phase in contact with the liquid to allow sufficient liquid action to produce the desired level of mixing / stirring / shear stress depending on the physical agitation / action of the vessel. It may be produced by physically stirring / operating the container containing the object. In such conventional systems, the ability to generate strain rates and shear patterns at predetermined locations within the container may be difficult and / or limited.
In certain embodiments of the invention, movement of a shear stress generating element along an operating path in a container containing a liquid sample applies shear stress to components such as cells in the liquid sample. The movement of the shear stress generating element along the operating path intersecting the first location in the vessel and the second location in the vessel is not purely rotational and does not have a predetermined implementation, unlike a rotating stir bar. The form prescribes an operation that is not primarily rotational. As described below in connection with the motion path in certain embodiments, the first and second locations in the container may be the same location, so that the shear stress generating element is in the motion path beginning and ending at the same location. Move along. The motion path may be curved or straight.
In certain embodiments of the invention described herein, a shear stress generating element may be used that does not include the surface of the container or conduit that contacts the liquid. Some conventional perfusion systems use an injector / plunger device or other piston-type device to generate a liquid flow in the perfusion container. In other conventional perfusion systems, fluid flow may be generated using a container having a flexible and / or squeezable surface. Certain embodiments of the present invention use free suspended shear stress generating elements and / or shear stress generating elements attached to the surface of the container.
In the case of shake flasks, well plates or other non-closed reactors, the gas-liquid contact interface area is the main parameter that determines gas exchange. Shaking or other changes in the magnitude of the operation can significantly change the interfacial area, so shear stress generation and gas exchange rates are not substantially independent.
In the container of certain embodiments of the present invention, a gas permeable / liquid impermeable membrane is used in the surface area of the container. The permeability of this membrane can substantially control the overall gas exchange rate between the contained liquid sample and the environment outside the vessel, typically the incubator environment. In a closed container that includes a gas permeable membrane and is filled with a liquid, such as that found in certain embodiments of the invention, changing the level of shear stress generation, for example, by changing the operating speed of the shear stress generation element, Typically, the gas exchange rate between the sample and the outside of the container may not be substantially changed. In such embodiments, the generation of shear stress is substantially independent of the gas exchange rate.
In certain embodiments involving bubbles as a shear stress generating element, changing the level of shear stress that occurs may typically result in a relatively modest change in the interfacial area between the liquid sample and the bubbles present. Many membranes that may not be used to control the rate of gas exchange with the outside of the vessel may have sufficiently low gas permeability, for example with respect to oxygen and / or carbon dioxide, and thus during operation Any change to the interface area between the liquid sample and the bubble will not substantially change the overall gas exchange rate or the gas concentration in the liquid sample.
As an example, if the shear stress generating element is deformable (such as bubbles or immiscible liquids), there may be a slight difference in the oxygen exchange rate, and changes in the rotational speed will contact the shear stress generating element Changing the membrane area will slightly change the membrane area available for oxygen exchange between the liquid sample and the environment outside the container. However, when using typical oxygen-permeable or semi-permeable membranes, even those with high oxygen permeability similar to 4-methyl-1-pentene (described below) and other similar membranes The change in the overall oxygen exchange rate seems to be weak enough to be insubstantial.
Referring now to FIG. 1, a portion of a chip that may be used in certain embodiments of the present invention is schematically illustrated. The portion shown in this figure is a layer 2 that contains a series of voids therein, and when the layer 2 is positioned between two adjacent layers (not shown), the series of voids is a series of sealed channels and reactions. Define the site. A sealed container may be a predetermined substance (eg, a predetermined gas) between and / or between the container and / or including inlet and outlet ports / channels under predetermined operating conditions. ) Is considered sealed as long as it can contain a liquid sample inside without leakage.
FIG. 1 shows one embodiment of a chip that includes six reaction sites 4 defined by a reaction site container 20. Reaction site 4 defines a series of generally aligned elongated voids in a relatively thin, generally flat piece of material that defines layer 2. The reaction site 4 may be addressed by a series of channels including a channel 8 for delivering chemical species to the reaction site 4. In FIG. 1, each reaction site 4 defines a reactor 14 with associated fluid connections (eg, channels 6 and 8 and port 9), as indicated by the dotted lines. In FIG. 1, layer 2 includes six such reactors, each reactor having substantially the same configuration. In other embodiments, the reactor may include more than one reaction site and / or additional channels, ports, etc. The chip may include any number of reactors, some or all of which may be the same, or some of them may be different (eg, different sized containers, different shaped containers , Different access channel sets, etc.). In some embodiments, there may be a container that does not include a reaction site as part of the reactor. For example, the reactor may include a vessel that does not include reaction sites but allows for optical detection, mixing, and / or generation of shear stress.
The chip or reaction system used in accordance with certain embodiments of the invention may be minimal, for example, less than about 5 milliliters, less than about 1 milliliter or less, and in some embodiments as small as 0.01 milliliters. A reaction site vessel having In some embodiments, the reaction site includes a compartment or container that includes a surface formed of a membrane.
In some embodiments of the present invention, the reactors, vessels and / or reaction sites in the chip are constructed and arranged to maintain an environment that promotes, for example, the growth of one or more types of living cells simultaneously. Also good. In some cases, the reaction site may be supplied with fluid flow, oxygen, nutrient distribution, etc. that are similar to those found in living tissue, for example, the tissue where the cells originated. Thus, the chip may be capable of providing a state closer to that in vivo than that supplied by the batch culture system. In embodiments where one or more cells are used at the reaction site, the cells are essentially any cell type, such as prokaryotic cells (eg, bacterial cells) or eukaryotic cells (eg, mammalian cells) Also good. The precise environmental conditions required at the reaction site for a particular cell type or types are known to those of ordinary skill in the art using routine experimentation or may be determined by those skilled in the art.
As discussed above, in certain embodiments, an immiscible material that acts as a shear stress generating element may be provided in the reaction site vessel 20. The liquid sample, cells suspended in the liquid and / or cells attached to the walls of the reaction site container, move the immiscible material within the reaction site container 20 to cause movement of the liquid and resulting shear. It may be exposed to stress exposure.
In one set of embodiments, the present invention provides techniques and systems for generating and controlling the level and distribution of shear stress in a liquid sample in a container, such as the previously mentioned chip reaction site container 20. In accordance with certain embodiments of the present invention, computational fluid dynamics may be used to determine the level and distribution of shear stress generated by moving a shear stress generating element within a fluid sample. The hydrodynamic shear stress τ is a function of the fluid viscosity μ and the gradient or strain rate γ (eg, dVx / dy) in the velocity field within the fluid.
τ = μγ (1)
The strain rate has an infinite time unit (typically 1 / s), and as a standard, the viscosity of water at room temperature is approximately 0.001 kg / m −s .
In some embodiments, the immiscible material may have a density that is sufficiently different from the average density of the liquid sample or carrier liquid so that changing the orientation of the container moves the immiscible material relative to the container. Good. This density difference may be, for example, at least 1% difference, at least 2% difference, at least 5%, at least 7% or at least 10% difference from the average density of the liquid sample or carrier liquid. This change in orientation causes the immiscible material of different density to rise or settle in the reaction site vessel 20 depending on whether the immiscible material has a higher or lower density than the liquid sample.
As used herein, “immiscible” defines a relationship between two substances that are nearly immiscible with each other but may be partially miscible. “Immiscible” materials remain largely separated from each other in an observable split state, even though they are somewhat miscible with each other. For example, air and water can contain only water or aqueous solutions and some air, although the air is slightly soluble in water and water vapor may be present in the air. This definition is satisfied in that the phase is largely separated into regions. Other examples of immiscible materials include oils and water, polymer beads and water, and the like, some of which are miscible with each other.
Introduction of an immiscible substance into the liquid sample in the container 20 may include the addition or generation of bubbles. Bubbles may be introduced by partially filling the container with a liquid sample and leaving a portion as an originally present gas (typically air). In other embodiments, bubbles may be formed by vapor deposition, cell respiration, or introduction of gas after filling the container.
In some cases, the container includes a predetermined gas region in fluid communication with the container. In certain embodiments, this predetermined gas region is positioned within the container. The predetermined gas region may be constructed and arranged to include a shear stress generating element when the shear stress generating element is not being used to generate the shear stress.
In some embodiments, the container 20 may include a solid element such as a polymer bead or glass ball that acts as a shear stress generating element. It is also possible to use a liquid that is immiscible with the liquid sample as the shear stress generating element. Of course, any combination of the above immiscible materials may be used in the container. For purposes herein, the liquid sample itself or any portion thereof is not considered a shear stress generating element.
One method according to certain embodiments of the present invention for moving a shear stress generating element includes changing the orientation of the reactor using a rotating device such that the shear stress generating element moves within the reactor. . For example, shear stress generating elements such as bubbles may be included in the liquid sample container, and reversing the container may cause the bubbles to move from one end to the other by buoyancy.
The rotating device described herein may be configured to orient and secure a chip, article or other substrate in any of a variety of suitable orientations. Depending on the structure of the chip, article or other substrate, such a predetermined orientation may be particularly effective to provide a predetermined level and / or pattern of shear stress generation. As will be described in more detail later in the context of FIGS. 2a to 2c, the orientation of the tip fixed relative to the rotating device comprises one or more elongated containers for the purpose of generating and / or controlling shear stresses. It may be related to the operation of the article.
For example, in FIG. 2a, a chip 1 comprising a plurality of elongate containers 20, such as cell culture containers (eg defining a predetermined reaction site), each characterized by a longitudinal direction 19, substantially Are fixed to a rotating device 3 configured to rotate around a horizontal axis 5. The chip 1 is fixed to the apparatus 3 by arranging the longitudinal axis direction 19 of the container 20 with respect to the horizontal axis 5 so that the longitudinal axis direction 19 is substantially parallel to the horizontal axis 5. As the tip 1 rotates around the axis 5 via the rotation of the rotating device 3, the immiscible substance 17 moves up and down with respect to the direction of gravity, resulting in a reaction site vessel as shown in FIG. 3a. Transverse movement occurs within 20 (perpendicular to the longitudinal direction 19). The immiscible material 17 can reach the sidewall of the reaction site vessel 20 depending on the rotational speed, the relative density and / or viscosity of the immiscible material 17 and the liquid sample, and other factors. At high rotational speeds, the immiscible material 17 may not have time to move completely to one side wall before the reaction site vessel 20 is inverted against buoyancy or gravity, while the immiscible material 17 is opposite. Move in the direction. At slower rotational speeds or larger density differences, the immiscible material 17 moves faster and can reach one side wall before the orientation of the reaction site vessel is reversed.
In the arrangement shown in FIG. 2 b, the chip 1 is substantially horizontal in the longitudinal direction 19 of the container 20 so that the longitudinal direction 19 is substantially perpendicular to the substantially horizontal axis 5 and does not intersect the axis 5. It is fixed to the device 3 by being arranged relative to the shaft 5. In this embodiment, as shown in FIG. 3 b, when the tip 1 is rotated about the axis 5, the immiscible substance 17 tends to follow a detour path in the container 20. Such a path may help resuspend attached or established cells or other chemical species along the inner circumference of the container 20. Similar to the embodiment of FIG. 2a, the degree of travel of the immiscible material 17 depends on the rotational speed and the relative density and viscosity of the immiscible material 17 and the liquid sample.
In the configuration shown in FIG. 2 c, the chip 1 is substantially horizontal in the longitudinal direction 19 of the container 20 so that the longitudinal direction 19 is substantially perpendicular to and intersects the substantially horizontal axis 5. It is fixed to the device 3 by being arranged with respect to the shaft 5. In this configuration, the immiscible substance 17 moves in an end-to-end direction 19 during rotation. Similar to the embodiment of FIGS. 2a and 2b, the degree of travel of the immiscible material 17 depends on the rotational speed, the relative density of the immiscible material 17 and the liquid sample, and other factors.
The rotating device 3 may be rotated at any suitable speed. Depending on the embodiment, for example, rotational speeds of 2 rpm, 4 rpm, 8 rpm, 16 rpm, 32 rpm or 65 rpm may be used. In other embodiments, depending on the species present in the liquid sample, the type and density of shear stress generating elements present, the level of shear stress desired, the size of the vessel and rotator and other factors, these A much higher or a much lower rotational speed would be appropriate. In certain embodiments, a discontinuous, eg, pulsed rotational speed may be used. For example, the device 3 may be rotated at a low speed for a length of time and then at a higher speed for a short time. A higher rotational speed can help remove components from the inner surface of the container and / or promote a more uniform distribution of the components throughout the liquid sample. In other embodiments, the rotation of the device 3 may be completely stopped for a while, for example to carry out a measurement of a liquid sample or internal components.
In certain embodiments of the present invention, a single device may be used to move a reaction site vessel containing multiple chips or liquid samples to generate shear stress. The apparatus may be used to manipulate chemical, biological or biochemical samples according to various embodiments of the present invention. Other devices are possible as the above devices, and are included in the present invention. The apparatus includes a solid shaped housing that is generally rectangular. In some embodiments, the housing of the device includes two generally square facing major surfaces joined by four ends of a rectangular shape. The housing may be configured as an incubator, for example. In some cases, the housing may be sufficiently sealed to keep the device clean, dust-free, in a laminar flow field, sterile, etc. depending on the application.
In certain embodiments, a control system is used to operate the apparatus or other devices involved in generating shear stress. The control system may be configured to control one or more parameters associated with the apparatus, shear stress generating element, reaction vessel, tip and / or any other component involved in the overall shear stress generating system. Good. For example, the control system may control the rotational speed (constant or variable) of the components of the device. The control system may be attached to a device other than, for example, a rotating device, and the control system adds gas to or from the reaction vessel to change the size of the bubbles acting as shear stress generating elements. It may be attached to a system capable of extracting gas. In certain embodiments, the control system may include the ability to change the orientation of the chip relative to the rotating device.
The control system may be programmed to receive various data feedback during control operations, allowing for adjustment and / or optimization of various operating parameters during operation. In certain embodiments, the control system uses the feedback data to develop parameter values for future operations and / or to control current operating parameters, for example, FLUENT® (FLUENT USA). : Lebanon, New Hampshire), etc., may be configured to operate with a simulation product that is a computational fluid dynamics software product.
The control system may comprise a computer implemented system. The computer-implemented control system includes a processing unit (ie, processor), a memory system, input / output devices and interfaces (eg, interconnection mechanisms) and transport circuitry (eg, one or more buses), image and audio data input / output. It may include several known components and circuits, including other components such as output (I / O) subsystems, dedicated hardware and other components and circuits as known to those of ordinary skill in the art. Further, the computer system may be a multiprocessor computer system or may include a plurality of computers connected over a computer network.
A device for securing a plurality of individual substrates, such as a chip that may be constructed to contain a sample, is mounted on an axis within the housing that passes through two opposing major surfaces of the housing. . The device is in the form of a rotatable wheel having a plurality of members extending radially outward, the plurality of members having a plurality of chips within which one or more chips can be positioned. Define the slot. When the chip is fixed in the slot, the device is rotated manually or automatically around the axis, so that the chip fixed in the slot is periodically inverted. Of course, in some embodiments, the shaft may pass through only one of the major surfaces of the housing.
In one face of the housing that defines one of the housing ends joining the opposing major surfaces, a chip (or other substrate) can be introduced into and removed from the housing interior. The port exists. The access port can be anywhere in the housing that allows proper access to the device by a chip or other substrate, such as on one side of the housing or on one or more major surfaces of the housing. It may be positioned. In order to insert the chip into the device to lock into the slot of the device, the device is rotated so that the desired slot is aligned with the access port, and then the chip is routed through this access port. Inserted and fixed in the selected area by the slot. The device can be any arbitrary predetermined to align the desired slot and access port so that one or more chips can be positioned within the predetermined slots and their known locations. The tip may be rotated to a radial orientation and thus the chip may be removed from the device such that the particular slot that secures the particular chip is aligned with the access port for removal from the device . The chip (or other substrate) is inserted into and removed from the housing via the access port by essentially any suitable technique, including manual operation by hand, actuator or robotic operation, etc. May be. An access port is an opening in the wall of the housing that optionally includes a flap, door, or other member that allows the access port to be closed when not used to introduce or remove a chip from the housing. Also good.
In certain embodiments, instead of or in addition to operating the container 20 to move the shear stress generating element, eg, by reversal of rotation as discussed above, magnetic, electrical, mechanical, air pressure, Fluid pressure and / or other forces may be used. For example, one or more beads depending on the magnetic and / or electric field may be placed in the container 20. To move such beads within the container 20, a controlled application of magnetic and / or electric fields may be used. A shear stress generating element that is moved by forces other than gravity / buoyancy may be the same density as the liquid that contains it. In some embodiments, a single controlled magnetic or electric field may be used to move the beads within several containers 20. Such an embodiment can reduce the number of operating components of the overall system. Specifically, the ability to reduce or eliminate movement of the container 20 while generating shear stress can allow for better application of measurement techniques such as optical measurement techniques to liquid samples.
Within the container, free suspended shear stress generating elements such as bubbles or beads described above may be used, but depending on the embodiment, it is movably attached directly or indirectly to the surface of the container. A shear stress generating element may be employed. For example, as shown in FIG. 4a, the movable member 17 ′ may be slidably attached to the surface 21 of the container 20 at two points and may be movable along the length of the container depending on the applied force. . The movable member 17 'can be of the methods described herein, such as changing the orientation of the container, applying a magnetic force, and / or applying an electrical, mechanical, air, fluid, or other force. Either may be used to move. For purposes of this specification, the movable member 17 'is movably attached to the surface 21 of the container 20, but is not considered to be the surface of the container 20 itself.
FIG. 4b illustrates one embodiment of a shear stress generating element that pivots within the container 20 to generate shear stress. Member 17 "is mounted at one location on surface 21 so that it can pivot within container 20. Member 17" is liquid when container 20 is moved or reoriented relative to the direction of gravity. It may have a density that allows movement within the sample. In certain embodiments, the member 17 "may be responsive to a magnetic or electric field such that a change in the orientation of the container 20 with respect to the magnetic field or electric field and / or these fields will cause movement of the member 17". A component that reacts in such a field may be included.
According to some embodiments of the present invention, the characteristics of the container, such as its size and / or geometry, may be altered to affect the generation and / or distribution of shear stress. For example, as shown in FIG. 5, which is a perspective view of one embodiment of the container, the thickness of the container 20 is such that the path of travel of bubbles or other shear stress generating elements traverses the thinner portion 24 of the container. Or it may vary along its length to be contained within the portion 24. In other embodiments (not shown), the thickness of the container 20 may vary continuously or discontinuously along its length and / or width. In the thinner part 24, the bubble containing the shear stress generating element deforms and / or operates slower than expected in other parts, so that while moving the thinner part 24, the other parts of the container Different levels and patterns of shear stress are generated from the part. In other embodiments (not shown), the thinner portion 24 may extend along a larger percentage of the length of the container 20. Conversely, in contrast to the illustrated configuration, the portion 24 of the container 20 may be manufactured to be thicker than the peripheral area of the container.
In some embodiments, one or more ports (ie, inlet and outlet ports) of the chip are defined by “self-sealing” ports. A self-sealing port may be addressable by a needle when at least one side of the port is covered with a material layer, and the material layer is generally ported when a needle is inserted and withdrawn through the material. A seal that does not permeate seeds such as fluid introduced into the chip through is formed. In certain instances, the layer of the chip may be formed of a self-sealing material, i.e., the material may be penetrated by a solid object, but after such penetration, it generally has its shape. regain. For example, the top layer of the chip may be pierced by a mechanical device such as a needle, but may be made of an elastomeric material that closes hermetically when the needle or other mechanical device is withdrawn.
FIG. 6 shows the computational fluid dynamics simulation results of the shear stress of a shear stress generating element containing bubbles that move around the container as the container of the inventive system rotates. The shear stress plotted is averaged over the total volume of the container and is shown for various rotation angles. As a reference, at its vertical starting position, the container shall be oriented at zero degrees.
In this particular simulation, FLUENT, Inc., located in Lebanon, New Hampshire. Three-dimensional strain rate simulations were performed using the FLUENT 6.1 computational fluid dynamics software package. The container was modeled as having a shape as shown in FIG. 5, mounted on the rotating device in an orientation similar to that shown in FIG. 2b, and positioned approximately 11.9 centimeters from the rotational axis of the rotating device. The volume of the container is about 555 microliters, the length of the container is 3.75 centimeters, and the depth is 1.9 millimeters. The width along the center of the container is 11 millimeters. The depth of the thin portion 24 is about 1.54 millimeters. The bubble to be simulated moves along a path that is substantially similar to the path shown in FIG. 3b. The modeled rotational speed was 4 rpm and the foam occupancy in the container volume was 20%.
FIG. 7 shows a contour plot of the strain rate taken along the section VII-VII in FIG. 5 during 90 ° rotation based on the simulation results described above. The unit of strain rate is second −1. The higher strain rate region (white region) in the container was located along the liquid / gas interface.
Definitions As used herein, a “chemical, biological, or biochemical reactor chip” (equivalently, simply referred to as “chip”) is an integral type that includes one or more reactors. It is an article. “Integral article” means a single piece of material or an assembly of components connected together. As used herein, when referring to two or more objects and being “connected together,” this does not separate from each other during normal use, eg manually Means an object that cannot be separated, which requires at least the use of tools and / or breaks, peels, etc. (separation of adhesives, tools, components fixed together in one piece) Will damage at least one of the components.
The chip may be connected or inserted into a larger framework that defines the entire reaction system, for example a high throughput system. The system is primarily by other chips, chassis, cartridges, cassettes and / or larger machines or sets containing conduits or channels, reactant sources, cell types and / or nutrients, inlets, outlets, sensors, actuators And / or may be defined by the controller. Typically, the chip may be an article that is generally flat or planar (ie, having one dimension that is small compared to the other dimensions), but in some cases, the chip is a non-planar article. For example, the chip may have a cubic shape, a curved surface, a solid or block shape, or the like.
As used herein, a “reaction site” is constructed and arranged to cause a physical, chemical, biochemical and / or biological reaction during use of a chip or reactor. Is defined as the location within the reactor. In some cases, there may be more than one reaction site in a reactor or chip. The reaction may be, for example, a mixing or separation process, a reaction between two or more chemicals, a photoactive or photosuppressive reaction, a biological process, and the like. In certain embodiments, the reaction site may include one or more cells and / or tissues.
In certain embodiments, the volume of the reaction site can be minimal or any convenient size. Specifically, the reaction site is in various embodiments less than 1 liter, less than about 100 ml, less than about 10 ml, less than about 5 ml, less than about 3 ml, less than about 2 ml, less than about 1 ml, less than about 500 microliters, about It may have a volume of less than 300 microliters, less than about 200 microliters, less than about 100 microliters, less than about 50 microliters, less than about 30 microliters, less than about 20 microliters or less than about 10 microliters. Also, in certain cases, the reaction site may have a volume of less than about 5 microliters or less than about 1 microliter. In another set of embodiments, the reaction sites may have a size that is 2 millimeters deep, 500 microns deep, 200 microns deep, or 100 microns deep.
As used herein, “elongated” when referring to an article chamber or substrate or container or a predetermined reaction site is included within the outer boundary / container by the first line segment. Perpendicular to the first line segment connecting two points on the outer boundary / container other than the same two points to be connected and passing through the geometric center of the chamber or substrate or container or predetermined reaction site The geometry of the chamber or substrate or container or predetermined reaction site that is substantially longer than the second straight segment, connects two points on the outer boundary / container contained within the outer boundary / container Refers to a chamber or substrate or container or predetermined reaction site characterized by the presence of a first straight segment passing through the center, for example having an outer boundary or peripheral shape of the container. For example, the article is characterized in advance by a thickness measured in a direction perpendicular to the plane of the chip and a length and width measured in directions perpendicular to each other and parallel to the surface of the chip. If it is a flat tip with a positive displacement container that defines a defined reaction site (eg, as is the case with thin, rectangular or oval, teardrops, other predetermined reaction sites) If the length is substantially greater than the width, the predetermined reaction site is “elongate”. In the case of an elongated chamber, substrate, container or predetermined reaction site, it is contained within the outer boundary / container, connecting two points on the outer boundary / container and the chamber or substrate or container or predetermined The longest linear segment and collinear direction that passes through the geometric center of the reaction site is referred to herein as the "longitudinal direction" of the chamber or substrate or vessel or predetermined reaction site.
As used herein, a “membrane” typically has a shape such that one of its dimensions is smaller than the other dimension, in an environment where it is or may be exposed. A thin sheet of material that is permeable to at least one substance. In some cases, the membrane may be generally flexible or non-rigid. By way of example, the membrane is a rectangle having a length and width of about a few millimeters, centimeters or more and a thickness of less than 1 millimeter, and sometimes less than 100 microns, less than 10 microns, or less than 1 micron or less. Or a circular material may be sufficient. The membrane may define a reaction site and / or part of the reactor, or the membrane divides the reaction site into two or more parts that may have substantially the same or different volumes or dimensions. May be used for For example, the reaction site may be divided into three parts, four parts or five parts. For example, the reaction site may be divided into a first cell culture portion and a second cell culture portion located on the side of the first reservoir portion and the additional two reservoir portions, the additional reservoir One of the portions is separated from the first cell culture portion by a membrane and the other is separated from the second cell culture portion by a membrane. One or more membranes may also define one or more walls of the reaction site vessel. For example, in certain embodiments, a first membrane (eg, a membrane that is permeable to gas and not permeable to vapor) defines a first wall of the reaction site vessel. In another embodiment, a second membrane (eg, a membrane that is permeable to gas and not permeable to vapor) defines a second wall of the reaction site vessel. Non-limiting examples of materials that the membrane can permeate include water, O 2 , CO 2 or the like. As an example, the membrane for water is less than about 1000 (grams micrometer / m 2 · day), less than 900 (grams micrometer / m 2 · day), and 800 (grams micrometer / m 2 · day). ), Less than 600 (grams micrometer / m 2 · day) or less, and in some cases the actual permeability of water through the membrane is a function of relative humidity Also good. As another example, the membrane may have a permeability of about 0.061 O 2 mol / (day · m 2 · atm) or more to oxygen.
Some membranes are semi-permeable, which is recognized by those of ordinary skill in the art to be membranes that are permeable for at least one species but not immediately permeable for at least one other species There may be. For example, a semi-permeable membrane may allow oxygen to pass through it but may not allow it to pass through water vapor, or allow water vapor to pass through it, but at a rate May be at least an order of magnitude less than oxygen. Alternatively, the semi-permeable membrane may be selected to allow water to permeate it but not certain ions. For example, the membrane may be permeable to cations but substantially impermeable to anions, or permeable to anions but to cations. May be substantially impermeable (eg, cation exchange membranes and anion exchange membranes). As another example, the membrane may be substantially impermeable to molecules having a molecular weight greater than or equal to about 1 kilodalton, 10 kilodaltons, or 100 kilodaltons. In certain embodiments, the membrane is impermeable to cells, but may be chosen to be permeable to a variety of selected materials, for example, the membrane may be nutrients, proteins and cells, It may be permeable to other molecules produced by waste or the like. In other cases, the membrane may be gas impermeable. Some films can transmit specific light (eg, infrared, ultraviolet or visible light, light of a wavelength that interacts with a device that utilizes the film, visible light unless otherwise noted). If the film is substantially transparent, it absorbs no more than 50% of the light, as described in detail herein, or in other embodiments, no more than 25% or 10% of the light. In some cases, the membrane may be both semi-permeable and substantially transparent.
In some cases, the membrane material may include a monomer or polymer or copolymer, a polymer blend, a multilayer structure comprising the polymer in at least one layer, and the like. Non-limiting examples of polymers that may be used in the membrane material include polytetrafluoroethylene (eg, commercially available under the name TEFLON® by DuPont, Wilmington, Del., For example, TEFLON ( (Registered trademark) AF, etc.) or polyfluoro organic materials such as certain amorphous fluoropolymers, silicones such as polystyrene, polypropylene ("PP"), polydimethylsiloxane, polysulfone, polycarbonate, polymethyl acrylate and poly Acrylics such as methyl methacrylate, high density polyethylene (“HDPE”), low density polyethylene (“LDPE”), linear low density polyethylene (“LLDPE”), ultra low density polyethylene (“ULDPE”), and other polyethylenes , PET, poly salt Vinyl ( "PVC") materials, nylon, include thermoplastic elastomers, poly (1-trimethylsilyl-1-propyne) ( "PTMSP") and those similar thereto. Another example is poly (4-methylpentene-1) or poly (4-methyl-1-pentene) or poly (4-methyl-2-pentyne (“PMP”). Examples of PMP include Mitsui Examples include those sold under the name TPX ™ by Plastics (White Plains, NY) As yet another example, membrane materials include poly (4-methylhexene-1), poly (4-methylheptene- 1), poly (4-methyloctene-1), etc. In some cases, these materials may be copolymerized and / or polymer blends related to polymers as described above. It may be in the state.
In some embodiments, two or more components of the chip may be joined using an adhesive. As used herein, “adhesive” is given its general meaning as used in the art, ie an auxiliary that can fix or join two separate materials together. It is a material. For example, an adhesive may be used to bond the film to the substrate layer that defines the reaction site. Non-limiting examples of adhesives suitable for use according to the present invention include silicone adhesives such as pressure sensitive silicone adhesives, neoprene based adhesives and latex based adhesives. The adhesive is applied to one or more components of the chip using any suitable method, for example by applying the adhesive to the chip components as a liquid or as a semi-solid material such as an elastic solid. It may be attached. For example, in certain embodiments, the adhesive is a transfer tape to the component (e.g., a tape with adhesive attached thereto, and when the tape is applied to the component, the adhesive or adhesive At least part of which remains attached to the component. In one set of embodiments, the adhesive may be a pressure sensitive adhesive, i.e., the adhesive is not normally or substantially adhesive, but under the influence of pressure, such as about 6 atm or about 13 atm (about 100 psi or about 100 psi). 200 psi) to become adhesive at higher pressures and / or increase its adhesion. Non-limiting examples of pressure sensitive adhesives include AR Clad 7876 (commercially available from Adhesives Research, Inc., Glenlock, Pa.) And Trans-Sil Silicone PSA NT-1001 (Dielectric, Holyak, Mass.). Commercially available from Polymers).
In some embodiments, the chip has one or more reaction sites fixed together, at least in part, as described above (ie, with or without adhesive) 2. It may be constructed and arranged so that it can be defined by more than one component. In some cases, the reaction site may be free of adhesive that is adjacent to or otherwise in contact with one or more surfaces that define the reaction site, such as the reaction site side if adhesive is present. It can be said that it is effective when leaching into the fluid. Of course, the adhesive may be used elsewhere in the chip, for example at other reaction sites. Similarly, in certain cases, the reaction site uses an adhesive, and at least a portion of the adhesive used to build the reaction site remains in the chip, and thus it defines the reaction site or sites. It may be constructed to remain adjacent to or otherwise in contact with the surface. Of course, as discussed above, other components of the chip may be constructed without the use of adhesives.
While several embodiments of the present invention have been described and illustrated herein, those of ordinary skill in the art will perform the functions described above and / or the results and / or one described herein. Or, various other means and / or configurations for achieving multiple advantages will be readily envisioned. Each such variation and / or modification is intended to be within the scope of the present invention. More generally, those skilled in the art will appreciate that all parameters, dimensions, materials and configurations described herein are intended to be illustrative and that the actual parameters, dimensions, materials and / or configurations are It will be readily appreciated that the teachings of the present invention depend on the particular application used. Those skilled in the art will recognize, or be able to ascertain using no more than routine experimentation, many equivalents to the specific embodiments of the invention described herein. Accordingly, the embodiments described above are provided by way of illustration only, and the present invention is within the scope of the appended claims and their equivalents, except as specifically described and claimed. It should be understood that the method can be implemented. The present invention pertains to each individual feature, system, article, material, kit, and / or method described herein. Further, two or more of such features, systems, articles, materials, kits and / or methods may be inconsistent with each other, even if such features, systems, articles, materials, kits and / or methods are inconsistent with each other. These combinations are included in the scope of the present invention.
All definitions set forth and used herein take precedence over dictionary definitions, definitions set forth in documents incorporated by reference, and / or the general meaning of the defined terms. That should be understood.
The indefinite articles “a” and “an” as used herein and in the claims are to be understood to mean “at least one” unless the contradictory description clearly indicates otherwise. is there.
As used herein in the specification and in the claims, “and / or” is used to refer to elements that are thus connected, ie, elements that are displayed in a connected manner and in others in a disjunctive manner. It should be understood to mean “either or both”. In addition to the elements specifically identified by the clauses using “and / or”, other elements may optionally be present, regardless of whether they are associated with the specifically identified elements. is there. Thus, to give a non-limiting example, when the phrase “A and / or B” is used with an unconstrained language such as “comprising”, this indicates only A in some embodiments (optional Selection includes elements other than B), in another embodiment only B is shown (optionally includes elements other than A), yet another embodiment shows both A and B (optionally) , And other elements).
As used herein in the specification and in the claims, “or” should be understood to have the same meaning as “and / or” as defined above. For example, “or” or “and / or” when separating a plurality of items in a list is inclusive, ie includes at least one of several elements or listed elements, It shall also be construed to include additional items that contain more than one and are not listed as optional. However, only wordings that clearly indicate an objection such as “only” or “exactly one” or “consisting of” when used in the claims are listed in several elements or lists. Refers to containing exactly one of the elements. In general, the phrase “or” as used herein is preceded by an exclusive phrase such as “any”, “one of”, “one” or “exactly one”. This is to be interpreted only as displaying an exclusive alternative (ie, “one or the other, but not both”). “Consisting essentially of” as used in the claims shall have its general meaning as used in the field of patent law.
As used herein and in the claims, the phrase “at least one” referring to a list of one or more elements is selected from any one or more elements in the list of elements. Is intended to mean at least one element, but does not necessarily include at least one of every element specifically listed in the list of elements. It does not exclude any combination of elements. This definition also applies to elements other than those referred to by the phrase “at least one” specifically identified in the list of elements, whether or not they are associated with the specifically identified elements. It is anticipated that an element may exist as an option. Thus, to name a non-limiting example, the phrase “at least one of A and B” (or “at least one of A or B” as the equivalent or “at least one of A and / or B” as the equivalent) In one embodiment, B (and optionally including elements other than B) refers to at least one A that optionally includes two or more, and in another embodiment, A (and optional) (Including elements other than A as a selection) refers to at least one B that optionally includes two or more, and in yet another embodiment, at least one A that optionally includes two or more and Refers to at least one B (and optionally including other elements), etc., optionally including two or more.
In addition, in any method including two or more actions claimed in the present specification, unless the objection is clearly pointed out, the order of the actions in the method does not necessarily describe the actions of the above method. It should also be understood that the order is not limited.
In the claims and in the text of the above specification, “comprising”, “including”, “carrying”, “having”, “including”, “related to”, “holding” and these It should be understood that all transitional phrases, such as those similar to, are meant to be non-restrictive, i. However, the transitional phrases “consisting of” and “consisting essentially of” are each an exclusive or semi-exclusive transitional phrase as defined in US Patent Office Patent Examination Handbook No. 2111,03.
Non-limiting embodiments of the present invention will now be described by way of example with reference to the accompanying drawings. The accompanying drawings are schematic and are not drawn to scale. Throughout the drawings, each identical or nearly identical component that is depicted is typically represented by a single numeral. For the sake of clarity, the numbering of every component in every drawing is omitted for clarity, and the illustration of every component in each embodiment of the present invention is omitted if unnecessary. Abbreviated.
FIG. 1 shows one layer of a chip containing six reactors containing usable reaction site vessels according to one embodiment of the present invention. 2a-2c show various orientations that can position the chip on the rotating device. 3a-3c show the selected direction of movement of the shear stress generating element in the container. FIG. 4a shows an exemplary embodiment of a shear stress generating element that is slidably attached to a container. FIG. 4b shows an exemplary embodiment of a shear stress generating element that is pivotally attached to the container. FIG. 5 is a perspective view showing a container having a thickness that varies along the operating path of the shear stress generating element. FIG. 6 is a graph illustrating shear stress simulated by computational fluid dynamics modeling generated by a shear stress generating element including bubbles moving through the reaction site vessel shown in FIG. FIG. 7 is a plan view at 90 degrees rotation showing a contour plot of the strain rate of a flat section along the line VII-VII shown in FIG.
An apparatus having the ability to apply a shear stress to a liquid sample component to perform a biological or biochemical reaction,
A biological or biochemical reactor comprising a container having a volume of less than about 2 mL, wherein said container contains a liquid sample and does not include the reactor and the surface of the container or conduit in contact with the liquid. An element wherein the shear stress generating element is included in the device and the entire shear stress generating element is selected to intersect a first location in the device and a second location in the device An element constructed and arranged to move along a path with or without rotational movement;
The apparatus of claim 1, wherein the shear stress generating element is contained within a container containing the liquid sample and is movable within the container.
The apparatus of claim 1, wherein the container is constructed and arranged to facilitate cell culture.
The apparatus of claim 3, wherein the container is constructed and arranged to facilitate mammalian cell culture.
The apparatus of claim 1, further comprising a gas permeable, liquid vapor impermeable first membrane defining a first wall of the container.
The apparatus of claim 1, wherein the shear stress generating element has an average density that is at least 1% different from the average density of the liquid sample.
The apparatus of claim 1, wherein the shear stress generating element has an average density that is at least 5% different from the average density of the liquid sample.
The apparatus of claim 1, wherein the container has a volume of less than about 1.3 mL.
The change in operation of the shear stress generating element that causes a change in the level or pattern of shear stress in the liquid sample does not significantly affect gas exchange between the liquid sample and the exterior of the reactor. apparatus.
The apparatus of claim 1, wherein the shear stress generating element is a bubble contained within the apparatus.
The apparatus of claim 1, wherein the shear stress generating element is a bubble contained in a container containing the liquid sample and movable within the container.
The control system further comprising a control system configured to control the operation of the shear stress generating element to facilitate the generation of a reproducible and controllable level of shear stress at selected locations within the liquid sample. The device described.
The apparatus according to claim 1, wherein the gas permeable and liquid vapor impermeable membrane has an oxygen permeability of 0.061 O 2 mol / (day · m 2 · atm) or more.
The apparatus of claim 13, wherein the membrane has an oxygen transmission rate of 0.6 O 2 mol / (day · m 2 · atm) or less.
The apparatus of claim 1, wherein the gas permeable, liquid vapor impermeable second membrane defines a second wall of the container.
The apparatus of claim 2, wherein the thickness of the container varies along a selected operating path of the shear stress generating element.
The apparatus of claim 1, further comprising a plurality of containers each having a volume of less than about 2 mL and each containing a liquid sample.
The multiple containers reside on one chip, and the chip is constructed to enable it to be stably connected in a selected orientation relative to other similar chips in the device The apparatus of claim 17, wherein
The apparatus of claim 1, wherein the shear stress generating element is a solid element.
The apparatus of claim 1, wherein the shear stress generating element is liquid immiscible within the liquid sample.
The apparatus of claim 1, further comprising a rotating device to which the container is attached.
The tip further includes a predetermined gas region in fluid communication with the container, wherein the shear stress generating element is disposed within the gas region when the shear stress generating element is not being used to generate shear stress. The device of claim 1, which can be made.
The apparatus of claim 1, further comprising an inlet port, an outlet port, and a self-sealing elastomeric material that defines portions of the inlet port and the outlet port.
The apparatus of claim 1, wherein the container is defined by a void in the substrate layer.
6. The apparatus of claim 5, wherein the adhesive layer adheres the gas permeable and vapor impermeable membrane to the substrate layer.
A biological or biochemical reactor comprising a container containing a liquid sample;
A shear stress generating element that does not have a container or conduit surface in contact with the liquid, wherein the shear stress generating element is contained within the container, and the entire shear stress generating element is a first location within the container and An element constructed and arranged to move along a selected motion path that intersects a second location in the container;
A change in operation of the shear stress generating element in the vessel that causes a change in the level or pattern of shear stress in the liquid sample does not significantly affect gas exchange between the liquid sample and the exterior of the reactor, .
27. The apparatus of claim 26, further comprising a gas permeable, liquid vapor impermeable first membrane defining a first wall of the container.
28. The apparatus of claim 27, further comprising an inlet port, an outlet port, and at least one microfluidic channel in fluid communication with the vessel.
28. The apparatus of claim 27, wherein the container is constructed and arranged to hold at least one live mammalian cell.
27. The apparatus of claim 26, wherein the shear stress generating element has an average density that is at least 1% different from the average density of the liquid sample.
27. The apparatus of claim 26, wherein the container has a volume of less than about 5 mL.
27. The apparatus of claim 26, wherein the shear stress generating element is a bubble.
27. A control system configured to control operation of the shear stress generating element to facilitate the generation of reproducible and controllable levels of shear stress at selected locations within the liquid sample. The device described.
27. The apparatus of claim 26, wherein the shear stress generating element is a solid element attached to the container.
35. The apparatus of claim 34, wherein the shear stress generating element is slidably attached to the container.
27. The apparatus of claim 26, wherein the shear stress generating element is liquid immiscible within the liquid sample.
A shear stress generating element within the device that is movable within the device upon reversal of the device;
And a control system configured to control operation of the shear stress generating element to facilitate the generation of reproducible and controllable levels of shear stress at selected locations within the liquid sample.
38. The apparatus of claim 37, wherein the container has a volume of less than 5 mL.
38. The apparatus of claim 37, wherein the container has a volume greater than 0.01 mL and less than 3 mL.
38. The apparatus of claim 37, wherein the container has a volume greater than 0.5 mL and less than 3 mL.
38. The apparatus of claim 37, further comprising a gas permeable, liquid vapor impermeable first membrane defining a first wall of the container.
38. The apparatus of claim 37, wherein the shear stress generating element has an average density that is at least 1% different from the average density of the liquid sample.
38. The apparatus of claim 37, wherein the shear stress generating element is a bubble.
38. The apparatus of claim 37, wherein the shear stress generating element is a bubble contained within a container containing the liquid sample and movable within the container.
A method of applying shear stress to a biological or biochemical component of a liquid sample contained in a container, comprising:
Operating and / or controlling the operation of a shear stress generating element in a container containing a liquid sample, the operation of the shear stress generating element occurring upon reversal of the container, the operation being performed by the liquid sample Applying a reproducible and controllable level of shear stress to a biological or biochemical component at a selected location within.
46. The method of claim 45, wherein the container is capable of holding at least one live cell.
46. The method of claim 45, wherein the container is capable of holding at least one live mammalian cell.
46. The method of claim 45, wherein a gas permeable, liquid vapor impermeable membrane defines the first wall of the container.
46. The method of claim 45, wherein the operation applies a preselected level of shear stress at the selected location within the liquid sample.
It further includes an additional and separate action to operate and / or control the shear stress generating element within the container containing the liquid sample, the operation of the shear stress generating element occurring when the container is inverted. 50. The method of claim 49, wherein the additional and separate operations apply different preselected levels of shear stress at selected locations within the liquid sample.
46. The method of claim 45, wherein the shear stress generating element is a bubble.
46. The method of claim 45, wherein the shear stress generating element is liquid immiscible within the liquid sample.
46. The method of claim 45, wherein the container is less than about 5 mL.
46. The method of claim 45, wherein the container is less than about 1 mL.
46. The method of claim 45, wherein the container is less than about 0.01 mL.
46. The method of claim 45, wherein operating and / or controlling the operation of the shear stress generating element comprises rotating the container.
57. The method of claim 56, wherein rotating the container includes rotating the container about an axis external to the container.
57. The method of claim 56, further comprising rotating the container using a discontinuous rotational speed.
A biological or biochemical reactor comprising a container configured to contain a liquid sample, the surface of the container having an oxygen of 0.061 O 2 mol / (day · m 2 · atm) or more A reactor comprising a membrane having a permeability;
A selected action that is contained within the container and that when the container contains the liquid sample, the entire shear stress generating element intersects a first location in the container and a second location in the container during operation. A shear stress generating element constructed and arranged to move along a path.
60. The apparatus of claim 59, wherein the container has a volume of less than 5 mL.
61. The apparatus of claim 60, wherein the container contains the liquid sample and the shear stress generating element is a bubble.
60. The apparatus of claim 59, wherein the shear stress generating element is a solid element.
60. The apparatus of claim 59, wherein the container comprises the liquid sample and the shear stress generating element is liquid immiscible within the liquid sample.
60. The apparatus of claim 59, wherein the membrane has an oxygen transmission rate of 69.7 O 2 mol / (day · m 2 · atm) or less.
60. The apparatus of claim 59, wherein the membrane has an oxygen transmission rate of 140 O 2 mol / (day · m 2 · atm) or less.
The control system further comprising a control system configured to control operation of the shear stress generating element relative to the container to generate a reproducible and controllable level of shear stress at selected locations within the liquid sample. 59. The apparatus according to 59.
A method of applying shear stress to a biological or biochemical component of a liquid sample, comprising:
A first location in the device and a second location in the device to apply a reproducible and controllable level of shear stress to the biological or biochemical component at a selected location in the liquid sample; A method comprising freely moving the entire shear stress generating element in a suspended manner in the apparatus along selected intersecting motion paths, wherein the shear stress generating element is either a gas or a liquid.
68. The method of claim 67, wherein the liquid sample is contained in a reaction site container capable of holding at least one live cell.
69. The method of claim 68, wherein the at least one living cell is a mammalian cell.
68. The method of claim 67, wherein the gas permeable, liquid vapor impermeable membrane comprises defining the first wall of the container.
68. The method of claim 67, wherein operating the shear stress generating element applies a preselected level of shear stress at a selected location within the liquid sample.
68. The method of claim 67, wherein the shear stress generating element is a bubble.
68. The method of claim 67, wherein the shear stress generating element is liquid immiscible within the liquid sample.
68. The method of claim 67, wherein operating the shear stress generating element comprises changing the orientation of the device relative to the direction of gravity.
68. The method of claim 67, wherein operating the shear stress generating element comprises applying a magnetic field to the shear stress generating element.
68. The method of claim 67, wherein operating the shear stress generating element comprises applying an electric field to the shear stress generating element.
68. The method of claim 67, wherein the shear stress generating element is freely suspended in a container having a volume of less than about 2 mL.
Receiving feedback of at least one measurement from the liquid sample;
68. The method of claim 67, further comprising adjusting at least one control parameter of the device in response to the measurement.
68. The method of claim 67, further comprising operating simulation software to determine at least one parameter value that controls the apparatus.
A biological or biochemical reactor comprising a container having a volume of less than about 2 mL and containing a liquid sample;
A shear stress generating element that does not have a container or conduit surface in contact with the liquid, wherein the shear stress generating element is contained within the container and is constructed and arranged to operate pivotally within the container Wherein the pivoting motion produces a reproducible and controllable level of shear stress at selected locations within the liquid sample.
81. The apparatus of claim 80, wherein the shear stress generating element is a membrane having ends that are pivotally attached to the inner surface of the container.
JP2007527675A 2004-06-07 2005-06-07 Generation of shear force in the reactor Granted JP2008501365A (en)
JP2008501365A true JP2008501365A (en) 2008-01-24
JP2007527675A Granted JP2008501365A (en) 2004-06-07 2005-06-07 Generation of shear force in the reactor
JP5466009B2 (en) * 2006-12-06 2014-04-09 アッシュ モリス リミテッド Improved flow reactor
AT121790T (en) * 1988-10-21 1995-05-15 Molecular Devices Corp Method and apparatus for measuring the effects of cell-active agents on living cells.