阅读说明：本技术 用于混合设备的排气系统 (Exhaust system for a mixing apparatus ) 是由 T·R·弗莱彻 W·毛罗 D·尼斯 于 2019-08-30 设计创作，主要内容包括：本发明公开了一种用于混合设备的过滤器单元,包括亲水性过滤器和疏水性排气过滤器。亲水性过滤器配置为接收包括液体和气体的流体。亲水性过滤器还被配置为对液体进行消毒。疏水性排气过滤器配置为接收来自亲水性过滤器的气体。疏水性排气过滤器进一步包括排气口和膜,该膜配置为使过滤器单元的内部与过滤器单元的外部分离,气体通过流过膜并从排气口流出而从过滤器单元排出。在一些实施例中,过滤器单元还包括消泡装置,其被配置为从亲水性过滤器接收气体、由液体包含被捕获的气体构成的泡沫、以及液体中的一些,并且还被配置为从泡沫中释放气体中的至少一些。(A filter unit for a mixing apparatus includes a hydrophilic filter and a hydrophobic vent filter. The hydrophilic filter is configured to receive a fluid comprising a liquid and a gas. The hydrophilic filter is also configured to disinfect the liquid. The hydrophobic vent filter is configured to receive gas from the hydrophilic filter. The hydrophobic exhaust filter further comprises an exhaust port and a membrane configured to separate an interior of the filter unit from an exterior of the filter unit, the gas being exhausted from the filter unit by flowing through the membrane and out the exhaust port. In some embodiments, the filter unit further comprises a bubble removal device configured to receive some of the gas, the foam comprised of liquid including trapped gas, and the liquid from the hydrophilic filter, and further configured to release at least some of the gas from the foam.)

1. A filter unit for a mixing apparatus, comprising:

a hydrophilic filter configured to receive a fluid comprising a liquid and a gas, the hydrophilic filter further configured to disinfect the liquid; and

a hydrophobic exhaust filter configured to receive gas from the hydrophilic filter, the hydrophobic exhaust filter further comprising a vent and a membrane configured to separate an interior of the filter unit from an exterior of the filter unit, the gas being exhausted from the filter unit by flowing through the membrane and out the vent.

2. The filter unit of claim 1, wherein the hydrophobic vent filter is configured to receive some of the liquid from the hydrophilic filter.

3. The filter unit of claim 1, wherein the hydrophobic vent filter is at least partially constructed of at least one of polytetrafluoroethylene or polyvinylidene fluoride.

4. The filter unit according to claim 1, wherein the hydrophilic filter is at least partially composed of polyethersulfone.

5. The filter unit of claim 1, wherein the hydrophobic vent filter further comprises a hollow cylindrical filter element disposed within a cylindrical filter container, the filter container comprising the vent, and the filter element comprising the membrane; and

wherein the filter element is coupled to the filter container such that gas is exhausted from the filter unit by flowing across the membrane into the hollow center of the filter element and out the exhaust port.

6. The filter unit of claim 1, wherein the hydrophilic filter comprises a hollow cylindrical filter element disposed within a cylindrical filter container, the filter container comprising an outlet, and the filter element comprising a second membrane configured to disinfect a liquid; and

wherein the filter element is coupled to the filter container such that liquid is discharged from the filter unit by flowing across the second membrane into the hollow center of the filter element and out the outlet.

7. A filter unit for a mixing apparatus, comprising:

a hydrophilic filter configured to receive a fluid, the fluid comprising a liquid, a gas, and a foam, the foam being comprised of the liquid including the trapped gas, the hydrophilic filter further configured to disinfect the liquid;

a bubble removal device configured to receive some of the gas, foam, and liquid from the hydrophilic filter, the bubble removal device further configured to release at least some of the gas from the foam; and

a hydrophobic exhaust filter configured to receive gas from the bubble removal device, the hydrophobic exhaust filter further comprising an exhaust port and a membrane configured to separate an interior of the filter unit from an exterior of the filter unit, the gas being exhausted from the filter unit by flowing through the membrane and out the exhaust port.

8. The filter unit of claim 7, wherein the hydrophobic vent filter is configured to receive some of the liquid from the bubble removal device.

9. The filter unit of claim 7, wherein the bubble removal device comprises a bubble removal material configured to release at least some of the gas from the foam.

10. The filter unit of claim 9, wherein the defoaming substance comprises stainless steel shavings.

11. The filter unit of claim 7, wherein the hydrophobic vent filter is at least partially constructed of at least one of polytetrafluoroethylene or polyvinylidene fluoride.

12. A filter unit according to claim 7, wherein the hydrophilic filter is at least partly composed of polyethersulfone.

13. The filter unit of claim 7, wherein the hydrophobic vent filter further comprises a hollow cylindrical filter element disposed within a cylindrical filter container, the filter container comprising the vent, and the filter element comprising the membrane; and

wherein the filter element is coupled to the filter container such that gas is exhausted from the filter unit by flowing across the membrane into the hollow center of the filter element and out the exhaust port.

14. The filter unit of claim 7, wherein the hydrophilic filter comprises a hollow cylindrical filter element disposed within a cylindrical filter container, the filter container comprising an outlet, and the filter element comprising a second membrane configured to disinfect a liquid; and

wherein the filter element is coupled to the filter container such that liquid is discharged from the filter unit by flowing across the second membrane into the hollow center of the filter element and out the outlet.

15. A method of filtering a solution comprising:

receiving a fluid comprising a liquid, a gas, and a foam at a filter unit consisting of a hydrophilic filter, a bubble removal device, and a hydrophobic vent filter, the foam consisting of the liquid including trapped gas;

directing the gas and the foam to a bubble removal device, wherein the bubble removal device is configured to release at least some of the gas from the foam;

passing gas across a membrane of a hydrophobic exhaust filter and out of an exhaust port to be exhausted, the membrane being configured to separate an interior of the filter unit from an exterior of the filter unit;

sterilizing the liquid by a hydrophilic filter; and

discharging the sterilized liquid from the filter unit.

16. The method of claim 15, wherein the hydrophobic vent filter is configured to receive some of the liquid.

17. The method of claim 15, wherein the bubble removal device comprises a bubble removal material configured to release at least some of the gas from the foam.

18. The method of claim 15, wherein the hydrophobic vent filter is at least partially constructed of at least one of polytetrafluoroethylene or polyvinylidene fluoride.

19. The method of claim 15, wherein the hydrophobic vent filter further comprises a hollow cylindrical filter element disposed within a cylindrical filter container, the filter container comprising the vent, and the filter element comprising the membrane; and

wherein venting gas comprises venting gas by flowing gas across the membrane into the hollow center of the filter element and out the vent.

20. The method of claim 15, wherein the hydrophilic filter comprises a hollow cylindrical filter element disposed within a cylindrical filter container, the filter container comprising an outlet, and the filter element comprising a second membrane configured to disinfect a liquid;

wherein sterilizing the liquid comprises flowing the liquid across the membrane into the hollow center of the filter element; and

wherein discharging the sterilized liquid includes discharging the liquid from the outlet.

Technical Field

Embodiments of the present technology generally relate to components of automated methods and apparatus for mixing at least one material with at least one fluid. More particularly, embodiments of the present technology relate to sterilization and/or filtration components for automated methods and apparatus that are particularly suited for reconstituting dry components into bioprocess solutions.

Background

Bioprocesses are processes that utilize living cells or components thereof to obtain a desired product. Biological treatment typically requires the use of various solutions. For example, the initial steps of a biological process may involve cell culture, which typically requires the use of cell culture media to successfully culture new cells. Subsequent steps in the bioprocess may then require the use of various buffer solutions as part of the product purification process.

Bioprocess solutions are typically hydrated from dry ingredients immediately prior to use in large stainless steel tanks or disposable mixing devices. The typical process is time consuming, expensive, and has no direct value to the desired product.

Although the basic cell culture process has not changed significantly over the years, the volume of cell cultures continues to increase dramatically, changing the requirements for media preparation. Not only are there more research laboratories, pharmaceutical and biotechnology companies using cell culture methods, but they often do so on a large scale. Biotech companies may consume thousands of liters of liquid media per day and employ large numbers of manufacturing technicians and scientists to produce antibodies, growth factors or reconstituted proteins from cell cultures for commercial use. The present disclosure provides an automated system and method for preparing bioprocess solutions with an in-line mixing device that can help reduce the time, labor, error and contamination risks required in these processes while also improving reliability and consistency.

The use of an in-line mixing device requires venting of gases such as air during, for example, a reconstitution process for the preparation of bioprocess solutions. If not vented, the air may displace the reconstituted solution in the mixing device. Furthermore, the air present in the in-line mixing device may not pass through the filtration membrane (e.g., sterilizing the hydrophilic membrane), resulting in a slowing or even stopping of the flow of the aqueous liquid in the mixing device.

Disclosure of Invention

In general, embodiments described herein relate to components of automated methods and apparatus for preparing dry ingredients into liquid solutions (e.g., preparing powdered bioprocess media into liquid bioprocess media). As discussed further below, dry ingredients tend to require less storage space, have a longer shelf life, are less expensive, and require less shipping and handling time than pre-packaged liquid solutions. Thus, when a liquid solution is desired, it would be advantageous to utilize automated methods and apparatus designed to make the preparation of the liquid solution from dry ingredients simple, straightforward, and repeatable, rather than purchasing prepackaged liquid solutions. Thus, a technique according to some embodiments involves components of an automated method for mixing dry ingredients (e.g., powdered media) into a fluid such as a cell culture medium or buffer. More particularly, some embodiments of the present technology relate to sterilization and/or filtration components for mixing devices that can be used via automated methods, wherein the automated methods and mixing devices are each adapted to reconstitute a dry ingredient into a liquid in a predetermined volume amount.

Various dry ingredients can be reconstituted into liquid solutions using the present techniques. For example, as used herein, dry ingredients may refer to powdered cell culture media, dry powder media, dry buffer powders, granular media, dry salts, dry chemicals, dry components, dry materials, and unhydrated ingredients.

One embodiment relates to a filter unit for a mixing apparatus. The filter unit includes a hydrophilic filter and a hydrophobic exhaust filter. The hydrophilic filter is configured to receive a fluid comprising a liquid and a gas. The hydrophilic filter is also configured to disinfect the liquid. The hydrophobic exhaust filter is configured to receive gas from the hydrophilic filter. The hydrophobic exhaust filter further comprises an exhaust port and a membrane configured to separate an interior of the filter unit from an exterior of the filter unit, the gas being exhausted from the filter unit by flowing through the membrane and out of the exhaust port.

Another embodiment relates to a filter unit for a mixing apparatus. The filter unit includes a hydrophilic filter, a defoaming device, and a hydrophobic exhaust filter. The hydrophilic filter is configured to receive a fluid including a liquid, a gas, and a foam including a trapped gas. The hydrophilic filter is also configured to disinfect a liquid. The bubble removal device is configured to receive some of the gas, foam, and liquid from the hydrophilic filter. The bubble removal apparatus is also configured to release at least some of the gas from the foam. The hydrophobic exhaust filter is configured to receive gas from the bubble removal device. The hydrophobic exhaust filter further comprises an exhaust port and a membrane configured to separate an interior of the filter unit from an exterior of the filter unit, the gas being exhausted from the filter unit by flowing through the membrane and out of the exhaust port.

Another embodiment relates to a method of filtering a solution. The method includes receiving a fluid comprising a liquid, a gas, and a foam of the liquid including the trapped gas at a filter unit comprised of a hydrophilic filter, a bubble removal device, and a hydrophobic vent filter; directing the gas and the foam to a bubble removal device, wherein the bubble removal device is configured to release at least some of the gas from the foam; and causing the gas to cross the membrane and be exhausted from an exhaust port of the hydrophobic exhaust filter, the membrane being configured to separate an interior of the filter unit from an exterior of the filter unit. The method further includes sterilizing the liquid through the hydrophilic filter, and discharging the sterilized liquid from the filter unit.

Drawings

The above-described and other features, aspects, and advantages of the present technology will now be described with reference to the accompanying drawings in conjunction with various embodiments. However, the illustrated embodiments are merely examples and are not intended to limit the present invention.

Fig. 1 is a schematic view of a mixing apparatus including a filter unit for reconstituting a powder (e.g., powdered bioprocess media) according to an exemplary embodiment.

Fig. 2 is a detailed schematic diagram of the filter unit of fig. 1 according to an exemplary embodiment.

Fig. 3 is a perspective view of a filter element of a filter unit according to an exemplary embodiment.

FIG. 4 is a cross-sectional view of the filter element of FIG. 3 according to an exemplary embodiment.

Fig. 5 is a detailed schematic view of the filter unit of fig. 1 depicting the flow of fluid within the filter, according to an exemplary embodiment.

Detailed Description

In the following detailed description, reference is made to the accompanying drawings, which form a part hereof. In the drawings, like numerals generally identify like components, unless context dictates otherwise. The illustrative embodiments described in the detailed description, drawings, and claims are not meant to be limiting. The detailed description is intended as a description of exemplary embodiments and is not intended to represent the only embodiments that may be practiced. As used herein, the term "exemplary" means "serving as an example, instance, or illustration," and should not necessarily be construed as preferred or advantageous over other embodiments. Other embodiments may be utilized, and other changes may be made, without departing from the spirit or scope of the subject matter presented here. It will be readily understood that the aspects of the present disclosure, as generally described herein, and illustrated in the figures, can be arranged, substituted, combined, and designed in a wide variety of different configurations, all of which are explicitly contemplated and form part of this disclosure.

Embodiments described herein generally relate to filtration and/or sterilization components of devices, systems and methods for preparing solutions from dry ingredients, for example, from cell culture media in dry powdered cell culture media or buffer solutions in dry powdered buffers. One or more of the provided embodiments may overcome one or more of the disadvantages, limitations, or shortcomings of the art in reconstituting solutions, particularly in reconstituting cell culture media in dry form, including dry powder media. For example, in some embodiments described herein, the component may facilitate venting of a gas, such as air, from the apparatus for reconstituting the powder, such that reconstitution proceeds more efficiently and produces a solution, e.g., free of unwanted foam or trapped gas, such as air.

The present disclosure refers to the systems and methods described herein in the context of preparing liquid cell culture media from powdered cell culture media. However, it should be understood that the systems and methods described herein may be adapted to prepare other types of solutions. For example, the systems and methods described herein may be used to prepare buffers for chromatography and downstream processing of biopharmaceutical drug substance substances. As another example, the systems and methods described herein may be used to prepare various "bioprocess solutions," or solutions used in processes that use living cells or components thereof to obtain a desired product. Further, it is contemplated that the systems and methods described herein may be adapted for use in many of the broader commercial or industrial applications. For example, many liquid medications are prepared in hospital pharmacies with a certain frequency and quantity. The saline solution, nutritional formulation, imaging agent, dye, sterile solution and anesthetic are reconstituted into a liquid. Additional alternative applications include, but are not limited to, pesticides, the preparation of fertilizers, and any of a variety of beverages (e.g., milk, iced tea, etc.) typically made from powders, all of which may be reconstituted using embodiments of the systems and methods described herein. In this regard, the dry ingredients that may be reconstituted using the present system and method are not limited to powdered cell culture media and may include dry powder media, dry buffer powders, granular media, dry salts, dry chemicals, dry components, dry matter, and anhydrous ingredients.

FIG. 1 is an overall system diagram of one embodiment of a mixing device 10. Preferably, the mixing device 10 is made of a material suitable for the cell culture environment, such as a medical grade plastic or other non-toxic material that is non-toxic, does not contaminate the media. The mixing apparatus 10 includes a first mixing chamber 12, a second mixing chamber 14, and a filter unit 16 connected together by various lengths of tubing 18 (e.g., flexible hose). The conduit also includes various valves 20 disposed therein to selectively permit (e.g., when the valve is in an open position) and stop (e.g., when the valve is in a closed position) fluid flow through the valve. In an exemplary embodiment, the valve is a pinch valve, although in other embodiments the valve may be or include other types of valves, such as a ball valve. In various embodiments, the mixing device 10 is designed to reconstitute a powdered cell culture medium into a liquid culture medium. For example, the mixing device 10 may be a single-use device in which the necessary media components (e.g., powdered cell culture media, sodium bicarbonate, etc.) are prepackaged. However, one skilled in the art will appreciate that the mixing apparatus 10 may also be used to reconstitute other forms of undissolved cell culture media (e.g., granulated cell culture media), to prepare bioprocess buffers from a dry form, or more generally to reconstitute a liquid from a powder.

First, in various embodiments, the first mixing chamber 12 contains a dry powder medium to be reconstituted into a liquid medium. For example, the first mixing chamber 12 may be provided with a predetermined amount of dry powder medium. In some embodiments, the first mixing chamber 12 may be pre-packaged with a predetermined amount of dry powder media already therein. Additionally, in various embodiments, the first mixing chamber 12 is designed to facilitate mixing of the medium with purified water and/or with other powders or liquids, such as dissolved sodium bicarbonate or supplements. For example, the first mixing chamber 12 may include a top and/or bottom cone connected to a top end and/or a bottom end, respectively, of the first mixing chamber 12 to facilitate the generation of a swirling motion as fluid enters the first mixing chamber 12. The swirling motion helps to facilitate mixing of the dry powder medium, purified water, dissolved sodium bicarbonate, supplements, etc. Various configurations and embodiments of the first Mixing Chamber 12 are described in U.S. patent application No.15/087,826 entitled "Media Mixing Chamber" filed on 31/3/2016, which is hereby incorporated by reference in its entirety.

The first mixing chamber 12 also includes various ports, such as a top port, an upper port, and a lower port, through which fluid can flow into and out of the first mixing chamber 12. In an exemplary embodiment, at least some of the ports may be positioned on the first mixing chamber 12 such that the fluid enters the first mixing chamber 12 at an angle that is substantially tangential to an inner wall of the first mixing chamber, which may further facilitate mixing of the various media components in the first mixing chamber. Additionally, the first mixing chamber 12 is connected via at least some ports and conduits 18 to various inlets 22 which in turn may be connected to various sources of fluid for the reconstitution process, such as water, supplements of cell culture medium and compressed air, which will flush the remaining medium from the apparatus 10 once the reconstitution process is complete.

In various embodiments, the second mixing chamber 14 contains additives to the cell culture medium. In an exemplary embodiment, the second mixing chamber 14 contains sodium bicarbonate powder, and the second mixing chamber 14 is designed to promote mixing of sodium bicarbonate with purified water. Additionally, the second mixing chamber 14 may be prepackaged with a predetermined amount of sodium bicarbonate therein. In some embodiments, the second mixing chamber 14 is configured similar to the first mixing chamber 12 (e.g., including a top and/or bottom cone coupled to a top end and/or a bottom end, respectively, of the second mixing chamber 14 to facilitate a swirling motion as fluid enters the second mixing chamber 14). In other embodiments, the second mixing chamber 14 is configured differently than the first mixing chamber 12. Various configurations and embodiments of the second Mixing Chamber 14 are also described in U.S. patent application 15/087,826 entitled "Media Mixing Chamber" filed on 31/3/2016, the entire contents of which are incorporated herein as noted above.

Similar to the first mixing chamber 12, the second mixing chamber 14 includes various ports, such as a top port and a lower port, from which fluid can flow into and out of the second mixing chamber. Additionally, at least some of the ports may also be positioned on the second mixing chamber 14 such that the fluid enters the second mixing chamber 14 at a substantially tangential angle relative to the inner wall of the mixing chamber. The second mixing chamber 14 is also connected to various inlets 22, for example to a water source, via at least some of the ports with the ducts 18. Also, as shown in fig. 1, the first mixing chamber 12 and the second mixing chamber 14 may be connected to each other through their respective ports having the pipe 18.

The apparatus 10 further comprises a filter unit 16 located before the outlet 24 of the apparatus 10. The filter unit 16 is configured to filter the reconstituted solution flowing into the filter unit 16. For example, in the embodiment shown in fig. 1, fluid may flow from first mixing chamber 12 and/or a water source into filter unit 16. The filter unit 16 may be further configured to disinfect the solution flowing into the filter unit 16. Additionally, as described in further detail below, the filter is configured to remove air or other gases from the solution. Once the reconstituted solution has been filtered and/or sterilized by the filter unit 16, the solution exits the device 10 via the outlet 24 and is directed, for example, into a sterile storage container.

Additionally, in various embodiments, the mixing device 10 may include various sensors for making measurements in the mixing device 10. These sensors may include, for example, pressure sensors (e.g., for detecting water pressure within the apparatus 10), conductivity sensors (e.g., for detecting conductivity of the solution within the apparatus 10, and thus the concentration of the solution), cumulative volume sensors, such as a rotary flow meter (e.g., for detecting the volume and flow rate of the fluid consumed during mixing), pH sensors (e.g., for detecting the pH of the solution within the apparatus 10), viscometers (e.g., for measuring the viscosity of the fluid within the apparatus 10), and the like. For example, in the embodiment of FIG. 1, the apparatus 10 includes a sensor 26 positioned as shown in the conduit 18. These sensors 26 may include: a pressurization sensor configured to measure the pressure of the fluid flowing into the filter unit 16 (e.g., to ensure that the backpressure of the filter unit 16 does not become too high); a conductivity sensor configured to measure the conductivity of the solution flowing into the filter unit 16, thereby indirectly measuring the concentration of the solution flowing into the filter unit 16 and ultimately out of the apparatus 10; and a volume sensor configured to measure a volume and a flow rate of water consumed during the mixing process.

In various embodiments, the powdered media is also mixed into the liquid media in the mixing apparatus 10 by an automated process. For example, the computing system may control the opening and closing of valves and fluid sources (e.g., water source, compressed air source, supplemental sources) used during the automated method to control the mixing of the powdered media. The computing system may open and/or close valves and component sources in response to various triggers. For example, the computing system may receive measurements from the mixing device 10 related to the mixing process (e.g., obtained from pressure sensors, conductivity sensors, and volume sensors). The computing system may then open and/or close the valve and/or the fluid source in response to receiving measurements of certain levels, below or above certain levels, within certain ranges, etc. As another example, the computing system may open and/or close the valve and/or the fluid source in response to a certain amount of elapsed time.

The use of the mixing apparatus 10 for preparing a liquid medium from a dry powdered medium by an automated process is an improvement over the current art as it allows for easy and efficient liquid medium preparation. Additionally, having programmed logic (e.g., implemented by processing circuitry executing instructions stored on a non-transitory machine-readable medium as part of a computing system) that controls the automated method enables repeatable and consistent preparation of liquid media from dry powder media. Additional details regarding various configurations and embodiments of the mixing device 10 and Automated methods for use with the mixing device 10 are described in U.S. patent application 16/017,014 entitled "Automated Method and Apparatus for preparation Bioprocess Solutions," filed on 25.6.2018, which is incorporated herein in its entirety.

Hydrating and filtering powders, such as powdered cell culture media, in a closed or substantially closed system (e.g., mixing apparatus 10) requires venting of gases, such as air. Air does not pass through the hydrophilic membrane of a typical disinfecting filter (e.g., filter unit 16) used to disinfect filtered aqueous liquids under normal operating pressures. If air is not removed by the exhaust, the filter flow will decrease and eventually stop because the air drains the aqueous liquid to the upstream side of the filter. Additionally, the dry areas of the hydrophilic membrane will not allow aqueous liquids to pass through.

Thus, in order to allow the liquid to flow efficiently through the mixing device, the filter of the device requires a vent. However, the vent must be selectively permeable to the outside air and not to the internal microorganisms, which may contaminate the solution in the equipment and damage the closed system. Additionally, the vent should prevent the discharge of the aqueous liquid mixed in the mixing apparatus.

In this case, it has been determined that the use of a semi-permeable hydrophobic membrane with sufficiently small pores (e.g., 0.2 μm or less) can selectively allow the egress of air or other gases and prevent the egress of incoming microbial contamination and aqueous liquids, provided that the membrane is substantially dry and free of foam. However, hydration of a powder (e.g., powdered cell culture medium) can produce a mixture of liquid and air that can create very small bubbles and bubbles (e.g., solution liquid containing trapped air), thereby preventing air from escaping through the hydrophobic membrane. Foam and bubbles will wet the membrane, while the wetted area of the hydrophobic membrane will not allow air to pass through. The reduction in the exhaust flow rate causes an accumulation of air in the system, which displaces the aqueous liquid on the upstream side of the hydrophilic filter, as described above, and eventually reduces the flow rate of the aqueous liquid filtrate. In this way, it was further determined that sufficient exhaust gas could be maintained by employing a bubble removal device immediately upstream of the hydrophobic exhaust filter. By helping to break up small bubbles and foam, the device effectively separates aqueous liquids from air and can prevent wetting of hydrophobic vent filters.

Fig. 2 is a detailed view of the filter unit 16 incorporating these advantageous features. In various embodiments, the filter unit 16 includes a hydrophilic filter 100, a bubble removal device 102, and a hydrophobic vent filter 104. The hydrophilic filter 100 is a sterilizing filter and includes a membrane for sterilizing an incoming solution. In some embodiments, hydrophilic filter 100 comprises a hollow cylindrical filter element 100b (not shown in fig. 2). The cross-sectional views of fig. 3 and 4 depict a cylindrical filter element 100b that includes a pleated membrane 100c (e.g., at the outer surface of the filter element). As shown in fig. 5, the hydrophilic filter 100 includes a cylindrical filter element 100b, and the cylindrical filter element 100b is fitted into a cylindrical filter container 100a such that a space exists between the filter element 100b and the filter container 100 a. The cylindrical filter element 100b includes a membrane 100c that sterilizes a solution that enters the hydrophilic filter 100. For example, the aqueous liquid entering the hydrophilic filter 100 passes through the membrane 100c of the cylindrical filter element 100b at a rate of 5-15L/min. Thus, in various embodiments, the solution enters the hydrophilic filter 100 via inlet 106, enters the space between the filter container 100a and the filter element 100b, is sterilized by passing through the membrane 100c of the filter element 100b into the hollow center of the filter element 100b, and is discharged from the hydrophilic filter 100 via outlet 108. In various embodiments, hydrophilic filter element 100b is at least partially constructed of a hydrophilic material, such as polyethersulfone ("PES").

Referring again to fig. 2, the bubble removal device 102 includes a bubble removal substance 110, the bubble removal substance 110 configured to break up small bubbles and foam in the solution to release air trapped therein. For example, in some embodiments, the defoaming substance may be steel wool or stainless steel shavings. Accordingly, the bubble removal device 102 is configured to receive at least some of the solution from the hydrophilic filter 100, including any foam and air mixed with the solution, and break up the bubbles and foam in the solution to release air from the solution. By way of illustration, the defoaming substance 110 may be configured to break up bubbles and foam by a combination of the dynamics of the flowing solution and the structure of the defoaming substance 110.

The hydrophobic vent filter 104 is configured to vent air or other gases from the solution mixed in the device 10. For example, in some embodiments, the hydrophobic exhaust filter 104 may exhaust up to 50L of air during mixing. As shown in fig. 5, in some embodiments, hydrophobic vent filter 104 includes a cylindrical filter element 104b (including a membrane on an outer surface of filter element 104b, similar to filter element 100b and membrane 100c) fitted to cylindrical filter container 104 a. Thus, in various embodiments, air from hydrophilic filter 100 (and any solution that is accidentally pushed or sprayed into hydrophobic vent filter 104) enters hydrophobic vent filter 104, into the space between filter container 104a and filter element 104 b. The air then flows through the membranes of filter element 104b into the hollow center of the interior of filter element 104b, and then out of hydrophobic vent filter 104, and thus apparatus 10, through vent 112 located at the top of hydrophobic vent filter 104 (e.g., incorporated as part of filter container 104 a). Additionally, membrane 104c separates the interior of filter unit 16 from the exterior of filter unit 16 so that, for example, microorganisms and unwanted particles do not enter apparatus 10 and damage the closed system of apparatus 10. In various embodiments, the hydrophobic vent filter element 104b is at least partially constructed of a hydrophobic material such as polytetrafluoroethylene ("PTFE") or polyvinylidene fluoride ("PVDF").

Fig. 5 shows the flow of solution and air through the filter unit 16. In the embodiment of fig. 5, the flow of non-sterile solution is shown by solid arrows 200, the flow of air or other gas is shown by dashed arrows 202, and the flow of sterile solution is shown by dashed arrows 204. Additionally, fig. 5 shows a filter container 100a, 104a and a filter element 100b, 104b for each of the hydrophilic filter 100 and the hydrophobic vent filter 104. As shown, the hydrophilic filter 100 includes a hydrophilic filter container 100a and a hydrophilic filter element 100b, and the hydrophobic vent filter 104 includes a hydrophobic filter container 104a and a hydrophobic filter element 104 b.

As shown in fig. 5, non-sterile solution 200 and air or other gas 202 enter hydrophilic filter 100 through inlet 106. The non-sterile solution 200 fills the space between the hydrophilic filter container 100a and the hydrophilic filter element 100 b. The non-sterile solution 200 passes through the membrane 100c of the hydrophilic filter element 100b (e.g., at a rate of 5-15L/min), is thereby sterilized, and enters the hollow center within the hydrophilic filter element 100 b. The sanitizing solution 204 is then discharged from the filter unit 16 by flowing through the outlet 108 (e.g., an outlet coupled to the hydrophilic filter container 100a through which the sanitizing solution 204 is discharged from the hydrophilic filter 100). The sterilization filtrate 204 may then be collected in a sterilization container and used, for example, as part of a biological process.

Additionally, the non-sterile solution 200 and any air or other gas 202 may flow from the hydrophilic filter 100 into the bubble removal device 102. For example, in effect, air and any bubbles or foam may rise from the unsterilized solution 200 in the hydrophilic filter into the bubble removal device 102. The defoaming substance 110 in the defoaming device 102 breaks up the bubbles and foam in the solution, thereby releasing the air 202 trapped therein and allowing the unsterilized solution to flow back into the hydrophilic filter 100.

The air or other gas 202 then flows into the hydrophobic vent filter 104 (e.g., along with a small amount of non-sterile solution that is also pushed or sprayed into the hydrophobic vent filter 104). As shown in fig. 5, air 202 flows into the space between the hydrophobic filter container 104a and the hydrophobic filter element 104 b. Air flows through the membrane 104c of the hydrophobic filter element 104b into the hollow center of the hydrophobic filter element 104 b. The membrane (e.g., 0.2 μm barrier) of the hydrophobic filter element 104b prevents bacteria and other microorganisms from entering the device 10. The air then flows out of the center of the hydrophobic filter element 104b and through the exhaust port 112, exiting the device 10.

In this way, the filter unit 16 is able to separate and vent air from the mixed solution, as well as sterilize the solution, while maintaining a closed system of the mixing apparatus 10. The filter unit 16, which is comprised of the hydrophilic filter 100, the bubble removal device 102 and the hydrophobic vent filter 104, thus provides the technical advantages discussed above. Additionally, in some embodiments, the above-described configuration of the filter unit 16 represents an unusual approach for solution disinfection and air venting during the mixing process, as many hydrophobic filters may be recommended for performance only in dry conditions. For example, although hydrophobic filters may be tested to measure the minimum "breakthrough pressure" of water, it is recommended that many hydrophobic filters not be wetted, as moisture may affect the performance of the hydrophobic filter. In contrast, in the above-described filter unit 16, although the hydrophobic exhaust filter 104 is not directly configured to receive the flow of the non-sterile solution, the hydrophobic exhaust filter 104 may still contact some of the non-sterile solution from the bubble removal device 102 (e.g., because the momentum of the flow of the non-sterile solution sprays the non-sterile solution into the hydrophobic exhaust filter 104). As such, the above-described configuration of filter unit 16 may be unusual in filtration systems. However, as described above, such a configuration may allow the apparatus 10 to effectively expel air, as well as separate trapped air from the mixed solution, while maintaining the solution inside the apparatus 10 and maintaining a closed system. Thus, this configuration may be advantageous for many applications of the device 10.

Alternatively, in some embodiments, the filter unit 16 may not include the bubble removal device 102. Instead, the hydrophilic filter 100 may be directly connected to the hydrophobic vent filter 104 (not shown). In such embodiments, the non-sterile solution is more likely to spray or flow into the hydrophobic vent filter 104, thus increasing the surprise of using this configuration. However, this arrangement may allow for effective disinfection and venting of the solution, for example, where foaming is less important or problematic.

It should also be understood that in some embodiments, the filter unit 16 may be arranged in other configurations than the filter unit 16 shown in fig. 2 and 3. For example, in some embodiments, there is no need to sterilize the solution mixed in the apparatus 10. As such, the filter unit 16 may include the bubble removal device 102 and the hydrophobic vent filter 104, but not the hydrophilic filter 100. Alternatively, in other embodiments, the filter unit 16 may include different or additional components, such as multiple vents. Alternatively, it should be understood that in other embodiments, the device 10 may be configured differently than the device 10 shown in FIG. 1. For example, in some embodiments, filter units 16 may be located in different sections of apparatus 10.

Further, while the above embodiments have been described with reference to the reconstitution of powdered cell culture media, it should be understood that embodiments of the mixing device 10 and filter unit 16 may be used with automated method embodiments to reconstitute various dry components into liquids, such as various bioprocess powders into bioprocess solutions. It is further contemplated that the liquid solvent used may be water, alcohol or other organic. The solubility characteristics, the solvent to be used, the amount required and the chemical interaction between the solvent and the reconstituted chemical will be used to provide guidance for the construction of the mixing apparatus 10 and/or filter unit 16 and any automated methods for reconstituting a powder using the apparatus 10.

The filter unit 16 may comprise nylon or cellulose acetate. Additionally, for media products, the one or more membranes used in the filter unit 16 may be a 0.2 μm filter, although it is contemplated that other filter sizes may be selected for certain functions. For example, the preparation of running buffers requires a clean solution, but does not necessarily require the use of a disinfectant solution, and a 0.45 μm filter is sufficient. Also, larger pore sizes may be required to prepare more viscous solutions. In short, the membranes used in the filter unit 16 may have any desired size, volume, pore size, etc.

Those skilled in the art will recognize that various modifications and changes may be made without departing from the scope of the described technology. Such modifications and variations are intended to fall within the scope of the embodiments as defined by the appended claims. Those skilled in the art will also appreciate that components included in one embodiment may be interchanged with other embodiments. One or more portions of the depicted embodiments may be included with other depicted embodiments in any combination. For example, any of the various components described herein and/or depicted in the drawings may be combined, interchanged, or excluded from other embodiments.

Embodiments herein have been described with reference to the accompanying drawings. The drawings show certain details of specific embodiments that implement the systems and methods described herein. However, the description of the embodiments with the drawings should not be construed as imposing on the present disclosure any limitations that may be present in the drawings.

With respect to the use of any plural and/or singular terms herein, those having skill in the art can translate from the plural to the singular and/or from the singular to the plural as is appropriate and/or applicable. Various singular/plural permutations may be expressly set forth herein for the sake of clarity.

It will be understood by those within the art that, in general, terms used herein, and especially in the appended claims, are generally intended as "open" terms (e.g., the term "including" should be interpreted as "including but not limited to" the term "including" and "having" should be interpreted as "including at least" and "having at least," respectively, the term "includes" should be interpreted as "includes but is not limited to," etc.). It will be further understood by those within the art that if a specific number of an introduced claim recitation is intended, such an intent will be explicitly recited in the claim, and in the absence of such recitation no such intent is present. For example, as an aid to understanding, the following appended claims may contain usage of the introductory phrases "at least one" and "one or more" to introduce claim recitations. However, the use of such phrases should not be construed to imply that the introduction of a claim recitation by the indefinite articles "a" or "an" limits any particular claim containing such introduced claim recitation to embodiments containing only one such recitation, even when the same claim includes the introductory phrases "one or more" or "at least one" and indefinite articles such as "a" or "an".

Further, configurations are typically used where those conventions are similar to "at least one of A, B, and C, etc." with the intent that one of ordinary skill in the art will understand the convention (e.g., "a system having at least one of A, B, and C" will include but not be limited to having A alone, B alone, C alone, A and B together and A and C together and B and C together and/or A, B, and C, etc.). Such a configuration is typically used where those conventions are similar to "at least one of A, B, or C, etc." with the intent that one skilled in the art will understand the convention (e.g., "a system having at least one of A, B, or C" will include but not be limited to possessing A alone, B alone, C alone, A and B together, A and C together and B and C together and/or A, B, and C, etc.). It will be further understood by those within the art that, in fact, any allosteric word and/or phrase presenting two or more alternative terms, whether in the specification, claims or drawings, should be understood as contemplating possibility of including one of these terms, one of the two terms or both. For example, the phrase "a or B" will be understood to include the possibility of "a" or "B" or "a and B".

For the purposes of this disclosure, the term "coupled" means that two members are directly or indirectly coupled to each other. Such connections may be fixed or movable in nature. Such joining may be achieved with the two members or the two members and any additional intermediate members being integrally formed as a single unitary body with one another or with the two members or the two members and any additional intermediate members being attached to one another. Such a connection may be permanent in nature or may be removable or releasable in nature.

The techniques discussed herein have many applications, and while specific embodiments of the techniques have been described in detail, it will be apparent to those skilled in the art that the disclosed embodiments may be modified in light of the design considerations discussed herein. Accordingly, the foregoing description is to be considered exemplary rather than limiting, and the true scope of the invention is that defined by the following claims.