Pursuant to 37 C.F.R. 1.71(e), applicants note that a portion of this disclosure contains material that is subject to copyright protection (such as, but not limited to, diagrams, device photographs, or any other aspects of this submission for which copyright protection is or may be available in any jurisdiction). The copyright owner has no objection to the facsimile reproduction by anyone of the patent document or patent disclosure, as it appears in the Patent and Trademark Office patent file or records, but otherwise reserves all copyright rights whatsoever.
The invention in specific embodiments relates generally to molecular and cellular sample preparation and/or culturing and/or analysis and more particularly to micro structures useful therewith. In further specific embodiments, the invention involves methods, systems, and/or devices for culturing and/or assaying cells and/or other biologically or chemically active materials using a novel culture structure, array, method or chamber. In other embodiments, the present invention relates to methods and/or system and/or apparatus enabling the culturing of cells in a configuration allowing for simulating living tissues and/or organs and/or solid tumors, such as systems for an artificial liver, kidney, pancreas, thyroid, etc. In specific embodiments, the invention involves methods and/or system and/or apparatus involving various structures for manipulating objects, such as cells or beads, in a fluidic medium and optionally performing certain analysis or observations thereof or deriving materials produced from biologic cultures.
The discussion of any work, publications, sales, or activity anywhere in this submission, including in any documents submitted with this application, shall not be taken as an admission that any such work constitutes prior art. The discussion of any activity, work, or publication herein is not an admission that such activity, work, or publication existed or was known in any particular jurisdiction.
High quality molecular and cellular sample preparations are the foundation for effective technology validation as well as for meaningful biological and clinical research and for various clinical and other applications. In vitro samples that closely represent their in vivo characteristics could potentially benefit a wide range of molecular and cellular applications. Handling, characterization, culturing, and visualization of cells or other biologically or chemically active materials (such as beads coated with various biological molecules) has become increasingly valued in the fields of drug discovery, disease diagnoses and analysis, and a variety of other therapeutic and experimental work.
Mammalian cell culture is an essential aspect of medical and biological research and development and ultimately treatment. However, most current practices are labor/resource intensive, not amenable to process control, cannot address cellular length scales, and prevent long-term continuous real-time monitoring or observation. Furthermore, current cell culture practices have not provided fully satisfactory solutions to the challenges of maintaining effective solid aggregates of cells in culture.
Advances have been made by combining microfabrication and microfluidic technologies with cell culture during the past decade; nevertheless, there is not yet a compact device effectively providing the same functionality as traditional cell culture.
Some recent publications and/or patent documents that discuss various strategies related to cell culture using microfluidic systems and related activities include the following U.S. patent applications and non-patent literature, which, along with all citations therein, are incorporated herein by reference to provide background. A listing of these references here does not indicate the references constitute prior art.
Cytoplex, Inc. U.S. Pat. No. 6,653,124 “Array-based microenvironment for cell culturing, cell monitoring and drug-target validation.”
Cellomics, Inc. U.S. Pat. No. 6,548,263 “Miniaturized cell array methods and apparatus for cell-based screening.”
Fluidigm, Inc. Published Application 20040229349 (Nov. 18, 2004) “Microfluidic particle-analysis systems.”
The present invention involves methods and systems related to microfluidic structures for sample preparation, culture, and/or for performing assays or other clinical applications. Exemplary structures provided herein may be scaled to support cell cultures, cell-based assays, molecular and cellular monitoring, monitoring, culturing and assaying using nano-beads or similar structures, and drug screening processes. While a typical application of structures and methods described herein is in maintaining and/or growing cells in culture, the invention can also be adapted to handle other objects on a cellular scale, such as coated and chemically or biologically active beads, etc.
In specific embodiments, the invention involves methods and systems related to continuous cell-culture microfluidic systems. According to specific embodiments of the invention, cells are cultured with continuous fluidic mass transport of medium and optionally with humidity and temperature control.
In further specific embodiments, the invention involves a high fluidic resistance ratio microfluidic device for culturing cells inside an arrangement (or array) of microchambers, providing a tool for cost-effective and automated cell or other culture.
In certain embodiments, materials used to fabricate cell culture components are optically transparent, allowing one or more of various microscopy techniques (e.g., phase contrast, fluorescence, confocal) without disturbing the culture environment. These properties enable the realization of a portable microfluidic cell culture array that can be used in sterile or non-sterile environments for research and commercial applications.
In one example embodiment, a microchamber or a single unit of an array of culture areas consists of a roughly circular microfluidic chamber of about 40 to 50 μm in height with a high fluidic resistance fluidic passage structure, such as passages of about 1 to 4 μm in height, the fluidic passage structure providing a fluidic connection to a medium and/or reagent channel or area.
In another embodiment, the high fluidic resistance fluidic passage structure comprises one or more of an (1) undercut connection of about 1 to 4 μm, connecting to a medium channel, (2) a plurality of high fluidic resistance channels connecting between a culture area and a medium area; (3) a grid of high fluidic passages.
In another example embodiment, a microchamber or a single unit of the array consists of a microfluidic chamber of about 40 to 50 μm with a flow-around medium/reagent channel connection to diffusion micro conduits and with a single opening for receiving cells.
In further example embodiments, one or more micro culture areas are connected to a medium or reagent channel via a grid of fluidic passages (or diffusion inlets or conduits), wherein the grid comprises a plurality of intersection micro high fluidic resistance passages. In one example, passages in the grid are about 1 to 4 μm in height, 25 to 50 μm in length and 5 to 10 μm in width, the grid allowing for more even diffusion between medium or reagent channels and the culture area and allowing for easier manufacturing and more even diffusion.
According to specific embodiments of the invention, the high fluidic resistance ratio between the microchamber and the perfusion/diffusion passages or grid (e.g., ratios in the range of about 10:1, 20:1 to 30:1) offers many advantages for cell culture such as: (1) size exclusion of cells; (2) localization of cells inside a microchamber, (3) promoting a uniform fluidic environment for cell growth; (4) ability to configure arrays of microchambers or culture areas; (4) ease of fabrication, and (5) manipulation of reagents without an extensive valve network. The ability to control the cell culture environment on the microscale produces many opportunities for improving biomedical and biotechnological research.
In specific implementations, large turnover of the medium (e.g., about ˜1/min) permits high cell density (e.g., >107 cells/ml) and optionally the use of CO2 independent buffering of pH.
In specific embodiments, device fabrication is based on micromolding of one or more elastomers (such as, polydimethylsiloxane (PDMS)), allowing for inexpensive mass production of disposable multi-chamber or culture area arrays. Other embodiments can be constructed from bonded silicon/polysilicon surfaces or injection molded polymers.
In order to enhance control over the culture environment, the present invention in specific embodiments uses a two-level lithography process. This solves the issue of non-uniform mass transfer in microfluidic channels caused by the parabolic laminar flow profile when directly culturing cells inside the microfluidic channels. In other embodiments, a single-level lithography process is used, with the desired high fluidic resistance ratio achieved by construction diffusion passages or a diffusion grid with a small cross section, even if the passages have the same height as the culture area.
The present invention, in further embodiments, involves an integrated device or system comprising cellular handling components, one or more cell culture arrays, fluidic connections and devices, and detection and or imaging devices. In specific example systems, the intersectional design of cell culture chambers in an array provides independent cell or chamber addressing and/or allows varying of concentrations of substances in culture medium, for example to provide for a large number of different cellular environments in a very compact cell culture chamber array.
According to specific embodiments of the invention, aspects of the invention can be incorporated into one or more integrated systems that provide simple yet elegant means for advanced cell culturing in a compact space providing an ideal mechanism for high throughput screening, cells analysis, drug discovery, etc. In further specific embodiments, the novel methods and devices according to specific embodiments of the invention can be used in various systems. Applications include point of care diagnosis, tissue engineering, cell-based assays, etc.
While example systems according to specific embodiments of the present invention are described herein as used primarily for performing testing or characterizations of biological cells, it will be understood to those of skill in the art that a culture system according to specific embodiments of the present invention can be used in a variety of applications for manipulating and culturing devices at a roughly cellular size (4 μm-15 μm). These applications include, but are not limited to: cellular systems, chemical systems, viral systems, protein culturing, DNA culturing. In some such applications, known techniques for affixing substances of interest to micron or nano beads can be used to facilitate such culturing.
In further embodiments, the invention can be integrated with a complete miniaturized cell culture system for high throughput cell-based assays or other cell-based or bead based applications. A microfluidic cell culture array according to the invention offers an affordable platform for a wide range of applications in high throughput cell-based screening, bioinformatics, synthetic biology, quantitative cell biology, and systems biology.
According to further specific embodiments of the invention, a portable cell culture array can be deployed in the field or clinic for point-of-care diagnostics of infectious agents or use in personal medicine. For example, clinical cell culture is used for the detection and identification of viruses, such as the causative agent of severe acute respiratory syndrome (SARS). Doctors can also derive important information about individual patients from cultured biopsies, such as for optimization of chemotherapy regimens.
The ability to perform inexpensive high throughput experiments using methods and devices of the invention also has applications in biological research, where thorough characterizations of experimental conditions are currently limited. For example, configuration of a culture array according to specific embodiments of the invention allows the invention to be loaded and handled using systems designed for conventional 96- or 384-well microtiter plate and enables providing a different culture condition in each chamber of an array according to specific embodiments of the invention. In this example a cell culture device according to specific embodiments of the invention can assay 96 or 384 different conditions on a single chip.
In further embodiments, an array of the invention can be embodied in a fully miniaturized system in a portable assay device, for example through the integration of electro-osmotic pumps, optical sensors, and microphysiometers. A microfluidic cell culture array according to specific embodiments of the invention can be involved with a wide range of applications in high throughput cell-based screening, bioinformatics, synthetic biology, quantitative cell biology, and systems biology.
Other Features & Benefits
The invention and various specific aspects and embodiments will be better understood with reference to drawings and detailed descriptions provided in this submission. For purposes of clarity, this discussion refers to devices, methods, and concepts in terms of specific examples. However, the invention and aspects thereof may have applications to a variety of types of devices and systems. It is therefore intended that the invention not be limited except as provided in the attached claims and equivalents.
Furthermore, it is well known in the art that systems and methods such as described herein can include a variety of different components and different functions in a modular fashion. Different embodiments of the invention can include different mixtures of elements and functions and may group various functions as parts of various elements. For purposes of clarity, the invention is described in terms of systems that include many different innovative components and innovative combinations of innovative components and known components. No inference should be taken to limit the invention to combinations containing all of the innovative components listed in any illustrative embodiment in this specification.
In some of the drawings and detailed descriptions below, the present invention is described in terms of the important independent embodiment of a biologic array system and components thereof. This should not be taken to limit the invention, which, using the teachings provided herein, can be applied to a number of other situations. In some of the drawings and detailed descriptions below, the present invention is described in terms of a number of specific example embodiments including specific parameters related to dimensions of structures, pressures or volumes of liquids, or electrical values. Except where so provided in the attached claims, these parameters are provided as examples and do not limit the invention to other devices or systems with different dimensions. All references, publications, patents, and patent applications cited in this submission are hereby incorporated by reference in their entirety for all purposes.
The present invention in specific embodiments is directed to producing a miniaturized, inexpensive platform for “cell-culture-on-a-chip” to make high throughput cell experiments accessible in laboratory, clinical, and field settings. Microfabrication and microfluidic technologies are adapted and extended according to specific embodiments of the invention. Microfabricated devices according to specific embodiments of the invention can more precisely control cell culture environment than can macroscopic systems.
In one example, microfluidic structures are implemented inside a microfluidic device to provide large differences of fluidic resistances of different microchannels. The device can therefore provide uniform and controllable microenvironment for continuous medium exchange cell culture. In another example, the microstructures are controlled by pressurized microchannels for flow regulation and for cellular sample preparation. In yet another example, the high fluidic resistance (which in some embodiments may be a result of a high aspect ratio fabrication) microstructures are positioned inside or adjacent to a microchamber or micro culture area as a passive barrier for cellular and molecular sample immobilization. The device can further be integrated with electrodes for functions such as metabolism monitoring, electro-chemical product generation, electroporation, and a variety of other applications.
The design of a microscale cell culture device presents a number of unique challenges, many of which have been recently discussed. Previous demonstrations of cell culture on microfabricated devices include growth of hepatocytes, lung cells, and insect cells in both silicon and PDMS substrates. These works validated the biocompatibility, nutrient supply, and growth characteristics of cells within microfabricated devices, but have yet to realize a high throughput array that can replicate the main functionalities of traditional cell culture.
Primary cells (those removed from living humans and other animals) represent an important avenue of medical research due to their increased relevance to disease and healthy states. However, the limited availability of tissue donors and the technical difficulties of maintaining these cells in vitro have severely limited their application in biomedical research. Microfluidic systems according to various embodiments of the invention can address these technical challenges by providing an environment with microscale geometry/fluidic control that has particular advantages for maintaining cell growth and/or cell viability and also in more closely creating the environment that certain types of cells would experience in their in vivo state, in particular the densely packed or close proximity environment of living tissues and/or solid tumors or other aggregations of cells. The invention furthermore enables such systems with low sample consumption, and automated operation.
The present invention, according to various specific embodiments as described herein, provides methods, systems, and devices that address the development of a novel high fluidic resistance and/or high aspect ratio microfluidic cell culture array capable of providing a stable and uniform microenvironment for cell growth.
In specific embodiments, further elements such as heterogeneous integration of a temperature control unit such as an ITO heater, allow the invention to provide an automated cost-effective cell culture platform without the large robotic systems adapted by current practices. In specific embodiments, a microfluidic device of the invention replicates the major processes in traditional cell culture, making it adaptable to a large number of applications. As one example and for discussion purposes, 1×5 arrays are discussed for device characterization to decrease the complexity of data processing and time of optical monitoring. Other examples that are discussed herein and/or have been fabricated include a 10×10 array, a 6×6 array, an 8×8 array, and an 8×1 array.
Example Experimental Chamber
In specific embodiments, the microchambers are designed to have the same cell growth area as a typical well in a 1,536 well microtiter plate. The left and right ports are designed to provide continuous perfusion of the medium to the chamber for sustaining cell growth. The top and bottom ports are used to load cells and reagents for cell-based assays.
In a more specific example implementation, each perfusion channel is about 2 μm high and about 2 μm wide compared to the main culture chamber, which is about 1 mm in diameter and about 40 to 50 μm in height. This high aspect ratio between the chamber and the perfusion pathway into it provides numerous advantages as discussed herein.
It will be understood that numerous dimensional variations are possible, including chambers that are not circular, perfusion/diffusion channels that vary somewhat in dimensions between one and another, or other dimensional parameters.
Arrays
In further embodiments, the invention can involve an array of culture regions, such as the examples described above.
A further example nanoliter scale fluidically addressable microfluidic platform according to specific embodiments of the invention is described below. In a specific example, an addressable 6×6 array of eight nanoliter chambers is effective for long term continuous culture of the HeLa human cancer cell line with a functional assay of 36 different cellular microenvironments. In one optional construction, high aspect ratio soft lithography is used to create the high fluidic flow channels, though further study has shown that the same high fluidic resistance can be achieved using a diffusion structures with diffusion passages that have the same height as the main chamber and medium channels. In this example, a “C” shaped ring with a narrow gap along the base is used to further separate individual culture units from flow channels to effectively decouple cell growth regions from pressure-driven transport without the use of active valves. This design avoids problems encountered in some multiplexing nanoliter culture environments by enabling uniform cell loading, maintaining long term cell localization, eliminating shear and pressure stresses on cultured cells, providing stable control of fluidic addressing, and permitting on-chip optical monitoring. The device uses a novel microstructure consisting of a high fluidic resistance roughly “C” shaped cell localization ring, and a low resistance outer flow ring. The central growth area and flow ring in one example were fabricated to be 50 μm in height, allowing cell transport through the device. The “C” shaped cell localization ring defining the 8 nl cell growth area consisted of a barrier with a 2 μm opening along the base with an inner diameter of 450 μm. This space allowed fluid flow through the cell growth area, but was narrow enough to retain cells in the central ring. An example single unit of this structure is illustrated in the SEM photograph shown in
In these embodiments, the individual array unit consisted of a high fluidic resistance inner chamber for cell growth and a low fluidic resistance outer channel for fluid flow. The 103-fold difference in resistance between the two compartments allows uniform loading of the array, controlling cell concentration, and maintaining long-term pattern integrity by selective removal of cells outside the growth area.
In an example device, these capabilities are integrated with aspects of the microfluidic cell culture array described above to produce a 6×6 addressable cell microarray for long-term functional studies. A single mold process with no required surface treatment used for fabrication allows the array to be easily scaled to a much higher size and density. In one example, a 6×6 cell analysis array with four fluidic paths to each chamber was achieved by fabricating an 8×8 matrix and sacrificing the outer row and column of culture units due to slight flow non-uniformities near the edges.
According to specific embodiments of the invention, the inlet and and/or exit of each column or row can comprise different microfluidic interface designs, for example: (1) a multiplexer (a single connection for multiple rows), (2) a concentration gradient generator, or (3) individually addressable connections. The gradient generator was a modified version of published work, and served to create multiple reagent concentrations from two fluidic inlets.
In alternative embodiments, the perfusion ring can be replaced to a high resistance passage into the outer ring, as illustrated in
Example Operation
The 6×6 prototype is capable of culture and assay of 36 different cellular microenvironment conditions. In proof of concept experiments, human cancer cells (HeLa) were loaded into the array and cultured for 7 days to approximately 5*107 cells/ml with a viability of over 97%. Row and column addressing was demonstrated by integrating a microfluidic concentration gradient generator to both dimensions, providing a different assay condition for each array unit using only 4 inlet reagents. Alternatively, individually addressing of each row can be used to allow many different reagents, drug exposure times, or time points to be assayed in this dimension.
After suspended HeLa cells were loaded into the array until the desired concentration was obtained, fresh culture medium was introduced to flush residual cells from the microfluidic channels. After loading, cells were cultured to obtain a high cell density (˜300 cells/chamber). Selective maintenance was conducted every 24 hours to ensure pattern integrity. Array capabilities were demonstrated.
A finite element model was created to predict the fluid velocity profile through this structure. This analysis indicated a 103-fold difference in fluid resistance between flow through the inner chamber and outer channel, agreeing with the analytical approximation based on Hagen-Poiseuille flow. This prediction was verified by tracking the flow of 2 μm beads through the microfluidic device.
Cell Loading
In this example, cell loading rate was controlled using a programmable syringe pump. For observation of cell flow through the microfluidic array, a flow rate of 40 nl/min/column was used, resulting in a flow through of approximately 0.7 cells/sec/unit. In a 100 second period, 218 cells were observed to flow through 3 separate loading columns, verifying the predicted flow rate. Cell flow velocity data within the device was obtained from analysis of time lapse digital recordings from 131 cells for the outer channel and 53 cells for the inner growth area. Uniformity of cell loading was quantified by counting cell numbers in each unit of the 6×6 array after a 2 minute loading period at 500 nl/min/column. The control condition was loaded in a 6×6 array without cell localization structures. Loading uniformity was calculated as the mean±SD (standard deviation) of the final number of cells in each row of the array, with row 1 being the closest to the inlet channel.
With a cell loading rate of 40 nl/min through each chamber, cell velocities were observed at 440±80 μm/s in the flow channel and 0.8±0.3 μm/s in the culture chamber, giving a velocity ratio of 550. This indicated that the flow rate through the central area was in the range of 50 pl/min. Under these conditions, the time scale of small molecule diffusion through the growth area (1.7 minutes) was over 4-fold faster than convective transport. The diffusion dominated mass transfer eliminated shear stresses caused by traditional continuous flow techniques while maintaining a microenvironment amenable for tissue growth. The continuous diffusion of chemicals into the culture environment may also provide a more physiologically accurate model for in vivo reaction kinetics. Additionally, the slow time scale for cellular exposure to reagents can dampen out fluctuations in assay conditions for long term studies.
The uniformity of cell loading in the 6×6 array (19% standard deviation with a minimum of 47 cells) was significantly improved compared to a microfluidic array without the loading structures under the same conditions (150% deviation with 47% of chambers empty). Initial analysis indicated that roughly 1-5% of cells entered the growth chamber. This was significantly larger than the predicted 0.2% of total flow, due largely to the tendency of cell clusters to preferentially enter the localization ring. The 2 μm opening under the cell localization ring also served as a cell concentrator by preventing trapped cells from leaving the chamber. By varying the loading flow rate and time, it was possible to completely fill the culture chambers with cells (˜5*107 cells/nil). Once the cells were localized in the central growth area, they became essentially decoupled from pressure fluctuations in the attached tubing, ensuring that the cells will attach and grow in the desired regions.
Cell Culture
All microfabricated components were sterilized with UV light prior to use. Fluidic connections were sterilized with 70% ethanol and thoroughly rinsed with filtered deionized water prior to use. The device was capable of maintaining a sterile environment while being continuously handled in a non-sterile manner because all fluidic connections were sealed with epoxy, isolating the microfluidic device from the outer environment.
Cells were cultured with continuous perfusion of CO2 Independent Medium (Gibco, Inc.) supplemented with 10% fetal bovine serum, 4 mM L-glutamine, and 1% penicillin/streptomycin. During perfusion, the device was placed inside a 37° C. incubator. Perfusion was controlled with a programmable syringe pump (Cole Parmer 74900), typically set at 0.4 μl/min flow through the arrayed device. Cells were cultured for over two weeks within the microfluidic array with no loss of viability.
Pattern Maintenance
As the cells began to divide within the array, it was possible to maintain the localization pattern by selectively removing cells from outside the growth area. The protease trypsin was introduced to the array to release the adherent cells from the substrate. The large flow velocity in the outer channels caused these cells to be removed from the system while cells in the growth rings were retained. Replacing culture medium to the chambers caused these cells to reattach to the substrate and resume growth. By periodically repeating this process, the cell microarray pattern could be maintained for long periods. In this experiment, the cells were purposefully allowed to overgrow the chambers to demonstrate the limits of pattern maintenance. Even when the cells had completely overgrown the outer channel, selective removal was capable of restoring the pattern such that less than 3% of cells remained outside the central ring. Scheduling treatment every 24 hours ensured over 99% of all cells remained within the central ring. More stringent control of reaction conditions and scheduling can largely eliminate residual cell debris in the outer channel. The ability to maintain cellular localization is crucial for microscale array development by preventing flow non-uniformities resulting from cell growth into the fluidic channels.
Real-time analysis of cellular activity was readily achieved using optical interrogation. The transparency of the microfabricated device at biologically relevant wavelengths permitted seamless adaptation to fluorescent microscopy techniques used in cell biology. Single cell analysis using Raman spectroscopy on bio-functionalized nanoparticles within the cell culture microarray can also be used to monitor activity. The culture units could also be linked to downstream microfluidic analysis modules, such as one developed for single cell nucleic acid isolation and detection.
In a further embodiment, a culture chamber has a single opening for cell introduction and a diffusion culture medium or reagents channel that flows around the culture chamber and is connected thereto by micro inlets or micro perfusion channels.
While this example embodiment has a number of applications, one of particular interest is use in facilitating an artificial liver or artificial liver sinusoid. In an example implementation, high density primary rat hepatocytes received nutrient transport via a biomimetic membrand (or vasculature or virtual membrane) according to specific embodiments of the invention. This configuration demonstrated enhanced viability and cytochrome P450 metabolic activity compared to cultures lacking this multicellular architecture.
The ability to maintain liver specific function of hepatocytes in vitro is an important area of medical and pharmaceutical research due to their central role in drug metabolism. As with most tissues, hepatocytes rapidly lose organ specific function once they are removed from the in vivo environment. While extracellular matrix coatings such as collagen I are traditionally used to maintain primary hepatocytes in culture, this is also known to down-regulate liver specific activityBy utilizing engineering capabilities with micron-scale resolution, the present invention makes it possible to recreate portions of a natural liver architecture.
In one example, a microfluidic artificial sinusoid was fabricated using soft lithography methods as described herein, and consisted of structures molded in silicone elastomer bonded to a glass culture surface. An example basic culture unit contained a 50×30×500 μm hepatic plate, a 50×30 μm cross section vessel, and a biomimetic “endothelial barrier” (or virtual membrane) separating the hepatocyte culture region from the nutrient transport vessel, wherein this biomimetic barrier or virtual membrane is constructed from one or more high fluidic resistance passages using fabrication as described herein.
The microfluidic culture unit mimics properties of liver vasculature in living tissue. Hepatocytes are prepared as a nearly solid mass of cells in “plates” about 50 μm in width. On either side of the hepatocytes are nutrient transport “sinusoids.” Small cross section channels connecting the two compartments localize cells in the growth areas while allowing diffusion of medium. The flow rate (˜5 nl/min), fluid velocity (˜0.5-1.5 mm/sec), and cell number (˜250-500) approximate values found in the liver. The high fluidic resistance ratio design between the cell seeding columns and the medium channels allow diffusion-dominant mass transfer for tissue culture. The small medium channels also prevent hepatocytes from growing into the nutrient supply channels. Thus, in particular embodiments, the present invention functionally recreates the micro-environment found in the normal human liver. In a normal liver, a “hepatocyte plate” is what physiologists typically call the aggregation of hepatocytes located between sinusoid spaces (empty regions allowing for blood flow). This configuration maximizes the number of functional cells without restricting nutrient transport. In many organs, endothelium-lined sinusoids (or spaces) provide the micro-environment for the cells that make up the tissues of an organ and tissues from these organs, as well as other tissues, are particularly suited to culturing as described herein.
Returning to the example embodiment shown in
In order to compare the function of the artificial sinusoids according to specific embodiments of the invention to other liver cell culture techniques, isolated rat hepatocytes (Cambrex) were maintained in the suggested medium on 384-well glass bottom plates and microfluidic sinusoids at two initial cell densities. In the absence of collagen coating, hepatocytes in the microtiter plate and those lacking dense cell-cell contacts lost viability within 4 days. Plating hepatocytes at an equivalent density (2×105 cells/cm2) in the microtiter plate did not improve viability. An assay of liver specific P450 activity verified the increased functionality of the hepatocytes cultured in the microfluidic sinusoid (
These findings indicate that the close physical contact of hepatocytes in the microfluidic sinusoid influences differentiated function. This conclusion agrees with findings on hepatocyte aggregate behavior and may be due to the importance of functional gap junctions in the intact liver (e.g., in S. A. Stoehr, H. C. Isom, Hepatology 38, 1125 (November 2003). Microfluidic engineering enables the control of key aspects of multicellular architecture while at the same time solving the problem of providing adequate mass transfer into tissue density cultures. The application of engineering principles described here can prove useful for the future investigation of organ function.
An alternative embodiment to any of the devices discussed herein involves a grid-like diffusion or perfusion barrier between the medium/reagent channel and the culture area. This barrier can be constructed in a similar way to the micro inlets or passages as described above, except instead of individual inlets, a grid or other arrangement of intersecting micro inlets is used to allow perfusion fluid transport.
Multicellular Tumor Spheroid Model
Another application of the invention is to culture solid tumors that can perform a similar function as multicellular tumor spheroid models for cancer drug screening. Multicellular tumor spheroids (MTS) are densely packed cancer cells grown generally in suspension in culture that mimic properties of tumors inside a living organism. While MTS's are known to provide a better model for cancer drug efficacy than plate cultured tumor cells, they are limited in practice due to the difficulty of spheroid handling and difficulty in observing suspended spheriods. Using the microfluidic method described here, a much improved method to produce high density tumor-like cultures in defined structures is achieved.
Thus, according to specific embodiments of the invention, after prolonged culture of cancer cells in a microfluidic culture chamber, the cells undergo a transition in morphology and assume behavior like that found in MTS. In this condition, extensive cell-cell contacts are made that limit drug penetration into the cell mass, an extracellular matrix is produced, and individual cell boundaries become obscured.
Primary Cell Applications
In addition to the described experiments, a chamber array according to the invention is suited for use with all currently utilized primary cell samples. Primary cells are those harvested from living animal tissue, and are particularly useful for tests where physiological responses are important (e.g. drug screening). Companies such as Cambrex and AllCells are specialized in preparing and selling primary cell samples. Due to the limited supply of primary cell samples, they are not easily integrated into large scale screens. The advantage of a controlled microfluidic format is that with the same number of cells, the throughput of experiments can be increased by 100×. Additionally, since it is important to maintain primary cell function in culture, a microfluidic system enables better control of culture conditions.
A special category of primary cells are stem cells. These cells are capable of differentiation into various cell phenotypes under different conditions. For example, the human embryonic stem cell is known to be able to differentiate into every cell type found in the adult human body. Stem cell culture currently is practiced by maintaining high density colonies of stem cells in well controlled environments. Therefore, the invention described here is ideally suited for applications in stem cell culture, maintenance, and controlled differentiation.
System Example
In one example embodiment, operation of the artificial liver microfluidic device is accomplished using an interface platform with each example chip containing 8 independent cell culture experiments, with a separate inlet and outlet reservoir.
Thus, this embodiment provides independent addressable medium/reagent channels that are not connected. For example, in one configuration as shown in
In an example operation, cell loading is performed on all eight chambers simultaneously, allowing significant cell savings. The poly-dimethyl-siloxane (PDMS) based microfluidic device is interfaced with a standardized “well plate” format (acrylic), allowing direct pipeting of culture medium and reagents. The fabrication of the chip enables visualization of all fluidic flows using standard microscopy or high content screening methods. For cell loading and initial priming, a custom built air pressure control manifold is used. Due to the low flow rates necessary for medium perfusion (˜5 nl/min), a simple gravity driven flow method by tilting the plate to make inlet wells higher than the outlet wells in conjunction with fluidic resistance patterning method can be used to achieve reliable operation in some embodiments, though other pumping mechanisms can also be used.
The microscale nature of the culture device enables research to be performed with significant cell/reagent savings. In current operation, it takes only 5,000 cells (5 μl at 106 cells/ml) to completely fill the 8 unit device. Currently, cell loading is accomplished in under 5 minutes with over 90% of the cells localized to the growth regions. Further optimization is expected to increase the loading efficiency to nearly 100% (all cells placed in the well end up in the microfluidic growth region) by standardizing the cell loading conditions (cell density, loading medium, flow rate) to minimize cell loss in the upstream fluidics. In preliminary observations, a medium flow rate of 5 nl/min (˜8 μl/day) was sufficient to maintain HepG2 cells. Therefore, the standard 384 microtiter well size inlet and outlet reservoirs (containing 100 μl) are sufficient to maintain long term culture (with occasional replenishment). Flow rate through the device during culture is maintained using gravity driven hydrostatic pressure. This is achieved by placing the chip on a fixed incline. By carefully designing the fluidic resistance in the microfluidic channels and the incline angle, initial observations show that a 7.4±1.1 nl/min can be sustained over long periods. The tolerance of this flow (15%) is expected to be much better (<2%) by improving the quality and uniformity of fabrication.
Cell culture within the array was verified using the HepG2 human hepatoma cell line. These observations indicate that there is no nutrient limitation even for very high density cultures after 7 days of gravity driven flow. Furthermore, the viability remained nearly 100% in all 8 units on the chip, and across 3 independent chips, indicating that there are no fundamental flaws in the design or operation.
Preliminary observations of primary rat hepatocyte (Cambrex Bioscience) culture in the device indicated a similar altered morphology that is not observed in plastic dish culture (
Systems and devices as described herein can be fabricated using any techniques or methods familiar from the field of photolithography, nano-fabrication, or micro-fluidic fabrication. For completeness of this disclosure and to discuss additional and independent novel aspects according to specific embodiments of the invention, specifics of example fabrication methods are provided below.
In some embodiments, the microdevices are fabricated using a single mold process, allowing direct array scale-up as well as the capability of integration with additional microfluidic layers. The development of a microfluidic high throughput automated cell-based assay platform allows rapidly determining or observing multiple cellular parameters for applications in quantitative cell biology and systems biology.
In alternative specific embodiments, a high density, scalable microfluidic cell array is implemented using a novel design to mechanically decouple cellular compartments from fluid flow. This is accomplished again using a method of high aspect ratio soft lithography technology, which consists of patterning two different channel heights and/or two different channel widths on a single mold such that fluidic resistance can be finely controlled over up to five orders of magnitude. By localizing cell growth to predefined areas, fluid transport through the array is carefully controlled and isolated from cellular activity.
The device dies were then cut by a razor blade and the fluidic connection ports were punched using an 18 gauge flat tip needle. The device was then irreversibly bonded to a coverglass (Fisher Scientific) after oxygen plasma treatment (PlasmaTherm Etcher, 50 W, 2 Torr, 40 s) on both the bottom of the device and the glass slide. 20 gauge stainless steel connectors (Instech Laboratories) and soft tubings (Cole Parmer Corporation) were used to provide fluidic connections to a syringe pump (Cole Parmer 74900).
In alternative embodiments, (e.g., for the artificial tissue microfluidic device) a different fabrication method was used. An example 8-unit microfluidic bioreactor chip was manufactured by heterogeneously integrating PMMA reservoirs with PDMS microfluidic devices. The previous described method demonstrate the use of PDMS and soft lithography technology for a syringe pump driven cell culture array. For higher throughput cell-based experimentation, an alternative fabrication method was used to “sandwich” PDMS between a PMMA sheet and a glass slide to facilitate integration with plastic-based materials. In this particular example, the PDMS is 0.5 mm thick, the PMMA sheet is 1.5 mm thick and the glass slide is lmm thick. The composite PMMA/PDMS microfluidic chip was then bonded to another piece of PMMA plate containing reagent reservoirs and fluidic connections.
Operation of the microfluidic bioreactor chip was accomplished using an interface platform developed at CellASIC. Each bioreactor chip currently provides 8 independent culture experiments, each with a separate inlet and outlet reservoir, and according to specific embodiments of the invention cell loading can be performed on all eight chambers simultaneously, significantly saving the biomasses. The standard PMMA well plate format allowed direct pipetting of cells, culture medium and reagents. The fabrication of the chip also enables visualization of all fluidic flows using standard microscopy or high content screening methods. For cell loading and initial priming, a custom built air pressure control manifold is used. Due to the low flow rates necessary for medium perfusion (˜5 nl/min), a simple gravity driven flow method proves to be reliable. In addition, each bioreactor chip can be primed and loaded with cells separately, and then put into an incubator for gravity-driven perfusion on inclined racks.
Example all Plastic Fabrication
In further embodiments, a culture device can also be fabricated with all plastics.
To fabricate the microfluidic bioreactor plate, a 6 mm thick PMMA sheet (McMaster-Carr) is laser cut (25 W CO2 laser, VersaLASER) or injection molded to create a top piece containing all cell inlets, drug inlets and perfusate outlet wells. A hard polymer master template (or silicon master template or electroform master template) such as those that can be fabricated in Berkeley Microfabrication Laboratory, is then hot embossed (Tetrahedron Associates, SPF-8) into a 1.5 mm thick PMMA sheet (McMaster-Carr) to create a bottom piece with microfluidic structures. Other than hot embossing, injection molding can also be an option. The top and bottom pieces are then thermally bonded together (Tetrahedron Associates, SPF-8) to complete the microfluidic plate. It is also possible to have the microfluidic structures, inlet and outlet wells on a same single piece.
Various groups have successfully demonstrated hot embossing of nano- to micro-sized features using different master templates, as well as thermal bonding between two PMMA sheets; however, CellASIC is the first one to apply these processes for high throughput cell-based experimentations. The key parameters to address are temperature, pressure and time. The major challenge is the deformation of PMMA during the bonding process. Because the minimum features in various designs according to specific embodiments of the invention, are at micron-scale, the control of temperature in some example fabrication methods is critical. An alternative approach is to use adhesive bonding by spin coating an adhesive layer at a thickness thinner than any microfluidic device features on the plate to prevent blockage of microfluidic channels.
As described above, following identification and validation of a assay for a particular cellular process, in specific embodiments devices and/or systems as described herein are used in clinical or research settings, such as to screen possible active compounds, predicatively categorize subjects into disease-relevant classes, text toxicity of substances, etc. Devices according to the methods the invention can be utilized for a variety of purposes by researchers, physicians, healthcare workers, hospitals, laboratories, patients, companies and other institutions. For example, the devices can be applied to: diagnose disease; assess severity of disease; predict future occurrence of disease; predict future complications of disease; determine disease prognosis; evaluate the patient's risk; assess response to current drug therapy; assess response to current non-pharmacologic therapy; determine the most appropriate medication or treatment for the patient; and determine most appropriate additional diagnostic testing for the patient, among other clinically and epidemiologically relevant applications. Essentially any disease, condition, or status for which a biologic culture is useful can be evaluated.
Web Site Embodiment
The methods of this invention can be implemented in a localized or distributed data environment. For example, in one embodiment featuring a localized computing environment, a microchamber culture device according to specific embodiments of the present invention is configured linked to a computational device equipped with user input and output features. In a distributed environment, the methods can be implemented on a single computer, a computer with multiple processes or, alternatively, on multiple computers.
Kits
A device according to specific embodiments of the present invention is optionally provided to a user as a kit. Typically, a kit of the invention contains one or more microchamber culture array devices constructed according to the methods described herein. Most often, the kit contains a diagnostic sensor packaged in a suitable container. The kit typically further comprises, one or more additional reagents, e.g., substrates, tubes and/or other accessories, reagents for collecting blood samples, buffers, e.g., erythrocyte lysis buffer, leukocyte lysis buffer, hybridization chambers, cover slips, etc., as well as a software package, e.g., including the statistical methods of the invention, e.g., as described above, and a password and/or account number for accessing the compiled database. The kit optionally further comprises an instruction set or user manual detailing preferred methods of using the kit components for sensing a substance of interest.
When used according to the instructions, the kit enables the user to identify disease specific cellular processes. The kit can also allow the user to access a central database server that receives and provides expression information to the user. Such information facilitates the discovery of additional diagnostic characteristics by the user. Additionally, or alternatively, the kit allows the user, e.g., a health care practitioner, clinical laboratory, or researcher, to determine the probability that an individual belongs to a clinically relevant class of subjects (diagnostic or otherwise). In HTS, a kit according to specific embodiments of the invention can allow a drug developer or clinician to determine cellular responses to one or more treatments or reagents, for diagnostic or therapeutic purposes.
Embodiment in a Programmed Information Appliance
The invention may be embodied in whole or in part as a logic or other description for construction of the devices according to specific embodiments of the invention, In such a case, the invention may be embodied in a computer understandable descriptor language, which may be used to create fabricated devices that operate as herein described.
Integrated Systems
Integrated systems for the collection and analysis of cellular and other data as well as for the compilation, storage and access of the databases of the invention, typically include a digital computer with software including an instruction set for sequence searching and/or analysis, and, optionally, one or more of high-throughput sample control software, image analysis software, collected data interpretation software, a robotic control armature for transferring solutions from a source to a destination (such as a detection device) operably linked to the digital computer, an input device (e.g., a computer keyboard) for entering subject data to the digital computer, or to control analysis operations or high throughput sample transfer by the robotic control armature. Optionally, the integrated system further comprises valves, concentration gradients, fluidic multiplexors and/or other microfluidic structures for interfacing to a microchamber as described.
Readily available computational hardware resources using standard operating systems can be employed and modified according to the teachings provided herein, e.g., a PC (Intel x86 or Pentium chip-compatible DOS,™ OS2,™ WINIDOWS,™ WINDOWS NT,™ WINDOWS95,™ WINDOWS98,™ LINUX, or even Macintosh, Sun or PCs will suffice) for use in the integrated systems of the invention. Current art in software technology is adequate to allow implementation of the methods taught herein on a computer system. Thus, in specific embodiments, the present invention can comprise a set of logic instructions (either software, or hardware encoded instructions) for performing one or more of the methods as taught herein. For example, software for providing the data and/or statistical analysis can be constructed by one of skill using a standard programming language such as Visual Basic, Fortran, Basic, Java, or the like. Such software can also be constructed utilizing a variety of statistical programming languages, toolkits, or libraries.
Various programming methods and algorithms, including genetic algorithms and neural networks, can be used to perform aspects of the data collection, correlation, and storage functions, as well as other desirable functions, as described herein. In addition, digital or analog systems such as digital or analog computer systems can control a variety of other functions such as the display and/or control of input and output files. Software for performing the electrical analysis methods of the invention are also included in the computer systems of the invention.
Optionally, the integrated systems of the invention include an automated workstation. For example, such a workstation can prepare and analyze samples by performing a sequence of events including: preparing samples from a tissue or blood sample; placing the samples into a microchamber array of the invention; and detecting cell or other reactions by optical, electrical or chemical measurements. The reaction data is digitized and recorded in the appropriate database.
Automated and/or semi-automated methods for solid and liquid phase high-throughput sample preparation and evaluation are available, and supported by commercially available devices. For example, robotic devices for preparation of cells. Alternatively, or in addition, robotic systems for liquid handling are available from a variety of sources, e.g., automated workstations like the automated synthesis apparatus developed by Takeda Chemical Industries, LTD. (Osaka, Japan) and many robotic systems utilizing robotic arms (Zymate II, Zymark Corporation, Hopkinton, Mass.; Orca, Beckman Coulter, Inc. (Fullerton, Calif.)) which mimic the manual operations performed by a scientist. Any of the above devices are suitable for use with the present invention, e.g., for high-throughput analysis of library components or subject samples. The nature and implementation of modifications to these devices (if any) so that they can operate as discussed herein will be apparent to persons skilled in the relevant art.
Although the present invention has been described in terms of various specific embodiments, it is not intended that the invention be limited to these embodiments. Modification within the spirit of the invention will be apparent to those skilled in the art.
It is understood that the examples and embodiments described herein are for illustrative purposes and that various modifications or changes in light thereof will be suggested by the teachings herein to persons skilled in the art and are to be included within the spirit and purview of this application and scope of the claims.
All publications, patents, and patent applications cited herein or filed with this submission, including any references filed as part of an Information Disclosure Statement, are incorporated by reference in their entirety.
This application is a continuation of U.S. patent application Ser. No. 14,855,584 filed on Sep. 16, 2015, incorporated herein by reference in its entirety, which is a division of U.S. patent application Ser. No. 11/994,997 filed on Aug. 11, 2008, now U.S. Pat. No. 9,260,688 issued on Feb. 16, 2016, incorporated herein by reference in its entirety, which is a 35 U.S.C. § 371 national stage completion of, and claims priority to, PCT international application number PCT/US2006/026364 filed on Jul. 6, 2006, incorporated herein by reference in its entirety, which claims priority to, and the benefit of, U.S. provisional patent application Ser. No. 60/773,467 filed on Feb. 14, 2006, incorporated herein by reference in its entirety, and which also claims priority to, and the benefit of, U.S. provisional patent application Ser. No. 60/697,449 filed on Jul. 7, 2005, incorporated herein by reference in its entirety. Priority is claimed to each of the foregoing applications.
This invention was made with Government support under N00014-03-1-0808, awarded by the Office of Naval Research, and under BES-0239333, awarded by the National Science Foundation. The Government has certain rights in the invention.
Number | Name | Date | Kind |
---|---|---|---|
4055613 | Kapral | Oct 1977 | A |
4661455 | Hubbard | Apr 1987 | A |
4734373 | Bartal | Mar 1988 | A |
4748124 | Volger | May 1988 | A |
5079168 | Amiot | Jan 1992 | A |
5153131 | Wolf et al. | Oct 1992 | A |
5310676 | Johansson et al. | May 1994 | A |
5330908 | Spaulding et al. | Jul 1994 | A |
5376252 | Ekstrom et al. | Dec 1994 | A |
5416022 | Amiot | May 1995 | A |
5424209 | Keamey | Jun 1995 | A |
5437998 | Schwarz et al. | Aug 1995 | A |
5451524 | Coble et al. | Sep 1995 | A |
5462874 | Wold et al. | Oct 1995 | A |
5565353 | Klebe et al. | Oct 1996 | A |
5589112 | Spaulding | Dec 1996 | A |
5593814 | Matsuda et al. | Jan 1997 | A |
5602028 | Minchinton | Jan 1997 | A |
5627070 | Gruenberg | May 1997 | A |
5637469 | Wilding et al. | Jun 1997 | A |
5641644 | Klebe | Jun 1997 | A |
5658797 | Bader | Aug 1997 | A |
5686301 | Falkenberg et al. | Nov 1997 | A |
5686304 | Codner | Nov 1997 | A |
5693537 | Wilson et al. | Dec 1997 | A |
5702941 | Schwarz | Dec 1997 | A |
5714384 | Wilson et al. | Feb 1998 | A |
5763261 | Gruenberg | Jun 1998 | A |
5763275 | Nagels et al. | Jun 1998 | A |
5763279 | Schwarz et al. | Jun 1998 | A |
5786215 | Brown et al. | Jul 1998 | A |
5793440 | Nakasaka et al. | Aug 1998 | A |
5801054 | Kiel et al. | Sep 1998 | A |
5866345 | Wilding et al. | Feb 1999 | A |
5882918 | Goffe | Mar 1999 | A |
5900361 | Klebe | May 1999 | A |
5912177 | Turner et al. | Jun 1999 | A |
5924583 | Stevens et al. | Jul 1999 | A |
5932315 | Lum et al. | Aug 1999 | A |
5942443 | Parce et al. | Aug 1999 | A |
6039897 | Lochhead et al. | Mar 2000 | A |
6048498 | Kennedy | Apr 2000 | A |
6096532 | Armstrong et al. | Aug 2000 | A |
6107085 | Coughlin et al. | Aug 2000 | A |
6153073 | Dubro et al. | Nov 2000 | A |
6190913 | Singh | Feb 2001 | B1 |
6197575 | Griffith et al. | Mar 2001 | B1 |
6228635 | Armstrong et al. | May 2001 | B1 |
6238908 | Armstrong et al. | May 2001 | B1 |
6251343 | Dubrow et al. | Jun 2001 | B1 |
6274337 | Parce et al. | Aug 2001 | B1 |
6277642 | Mentzen et al. | Aug 2001 | B1 |
6297046 | Smith et al. | Oct 2001 | B1 |
6323022 | Chang et al. | Nov 2001 | B1 |
6326211 | Anderson et al. | Dec 2001 | B1 |
6403369 | Wood | Jun 2002 | B1 |
6410309 | Barbera-Guillem et al. | Jun 2002 | B1 |
6455310 | Barbera-Guillem | Sep 2002 | B1 |
6465243 | Okada et al. | Oct 2002 | B2 |
6468792 | Bader | Oct 2002 | B1 |
6481648 | Zimmermann | Nov 2002 | B1 |
6495104 | Unno et al. | Dec 2002 | B1 |
6518035 | Ashby et al. | Feb 2003 | B1 |
6534013 | Kennedy | Mar 2003 | B1 |
6548263 | Kapur et al. | Apr 2003 | B1 |
6551841 | Wilding et al. | Apr 2003 | B1 |
6555365 | Barbera-Guillem et al. | Apr 2003 | B2 |
6562616 | Toner et al. | May 2003 | B1 |
6569675 | Wall et al. | May 2003 | B2 |
6576458 | Sarem et al. | Jun 2003 | B1 |
6585939 | Dapprich | Jul 2003 | B1 |
6593136 | Geiss | Jul 2003 | B1 |
6637463 | Lei | Oct 2003 | B1 |
6648015 | Chow | Nov 2003 | B1 |
6653124 | Freeman | Nov 2003 | B1 |
6673595 | Barbera-Guillem | Jan 2004 | B2 |
6756019 | Dubrow et al. | Jun 2004 | B1 |
6759245 | Toner et al. | Jul 2004 | B1 |
6794184 | Mohr et al. | Sep 2004 | B1 |
6811752 | Barbera-Guillem | Nov 2004 | B2 |
6821772 | Barbera-Guillem et al. | Nov 2004 | B2 |
6846668 | Garman et al. | Jan 2005 | B1 |
6857449 | Chow | Feb 2005 | B1 |
6908767 | Bader | Jun 2005 | B2 |
6915679 | Chien et al. | Jul 2005 | B2 |
6969166 | Clark et al. | Nov 2005 | B2 |
7005292 | Wilding et al. | Feb 2006 | B2 |
7018830 | Wilding et al. | Mar 2006 | B2 |
7022518 | Feye | Apr 2006 | B1 |
7067263 | Parce et al. | Jun 2006 | B2 |
7141386 | Dunfield et al. | Nov 2006 | B2 |
7155344 | Parce et al. | Dec 2006 | B1 |
7160687 | Kapur et al. | Jan 2007 | B1 |
7171983 | Chien et al. | Feb 2007 | B2 |
7192769 | Pykett et al. | Mar 2007 | B2 |
7223371 | Hayenga et al. | May 2007 | B2 |
7343248 | Parce et al. | Mar 2008 | B2 |
7745209 | Martin et al. | Jun 2010 | B2 |
7919319 | Jervis | Apr 2011 | B2 |
9260688 | Hung et al. | Feb 2016 | B2 |
20020039785 | Schroeder et al. | Apr 2002 | A1 |
20020053399 | Soane | May 2002 | A1 |
20020108660 | Staats | Aug 2002 | A1 |
20020110905 | Barbera-Guillem et al. | Aug 2002 | A1 |
20020177221 | Nishiguchi et al. | Nov 2002 | A1 |
20030008388 | Barbera-Guillem et al. | Jan 2003 | A1 |
20030008389 | Carll | Jan 2003 | A1 |
20030030184 | Kim | Feb 2003 | A1 |
20030040104 | Barbera-Guillem | Feb 2003 | A1 |
20030124623 | Yager et al. | Jul 2003 | A1 |
20030143727 | Chang | Jul 2003 | A1 |
20030156992 | Anderson et al. | Aug 2003 | A1 |
20030211012 | Bergstrom et al. | Nov 2003 | A1 |
20040029266 | Barbera-Guillem | Feb 2004 | A1 |
20040043481 | Wilson | Mar 2004 | A1 |
20040072278 | Chou | Apr 2004 | A1 |
20040096960 | Mehta et al. | May 2004 | A1 |
20040132175 | Vetillard et al. | Jul 2004 | A1 |
20040202579 | Larsson et al. | Oct 2004 | A1 |
20040229349 | Daridon | Nov 2004 | A1 |
20040238484 | Le Pioufle | Dec 2004 | A1 |
20050009179 | Gemmiti et al. | Jan 2005 | A1 |
20050019213 | Kechagia et al. | Jan 2005 | A1 |
20050032208 | Oh et al. | Feb 2005 | A1 |
20050072946 | Studer et al. | Apr 2005 | A1 |
20050101009 | Wilson et al. | May 2005 | A1 |
20050106717 | Wilson et al. | May 2005 | A1 |
20050169962 | Bhatia et al. | Aug 2005 | A1 |
20050214173 | Facer et al. | Sep 2005 | A1 |
20050221373 | Enzelberger | Oct 2005 | A1 |
20050260745 | Domansky et al. | Nov 2005 | A1 |
20050266582 | Modlin | Dec 2005 | A1 |
20060003436 | DiMilla et al. | Jan 2006 | A1 |
20060031955 | West et al. | Feb 2006 | A1 |
20060112438 | West et al. | May 2006 | A1 |
20060121606 | Ito et al. | Jun 2006 | A1 |
20060136182 | Vacanti et al. | Jun 2006 | A1 |
20060141617 | Desai et al. | Jun 2006 | A1 |
20060154361 | Wikswo et al. | Jul 2006 | A1 |
20060166354 | Wikswo | Jul 2006 | A1 |
20060199260 | Zhang et al. | Sep 2006 | A1 |
20070026516 | Martin et al. | Feb 2007 | A1 |
20070084706 | Takayama et al. | Apr 2007 | A1 |
20070090166 | Takayama et al. | Apr 2007 | A1 |
20070122314 | Strand | May 2007 | A1 |
20070264705 | Dodgson | Nov 2007 | A1 |
20070275455 | Hung et al. | Nov 2007 | A1 |
20080085556 | Graefing et al. | Apr 2008 | A1 |
20080176318 | Wilson et al. | Jul 2008 | A1 |
20080227176 | Wilson et al. | Sep 2008 | A1 |
20080233607 | Yu et al. | Sep 2008 | A1 |
20090023608 | Hung et al. | Jan 2009 | A1 |
20090203126 | Hung et al. | Aug 2009 | A1 |
Number | Date | Country |
---|---|---|
19948087 | May 2001 | DE |
0155237 | Sep 1995 | EP |
0725134 | Aug 1996 | EP |
0890636 | Jan 1999 | EP |
1539263 | Jan 1979 | GB |
1991015570 | Oct 1991 | WO |
2000056870 | Sep 2000 | WO |
2000060352 | Oct 2000 | WO |
2000078932 | Oct 2000 | WO |
2001092462 | Dec 2001 | WO |
2003085080 | Oct 2003 | WO |
2004059299 | Jul 2004 | WO |
2004106484 | Dec 2004 | WO |
2005023124 | Mar 2005 | WO |
2005035728 | Apr 2005 | WO |
2007008609 | Jan 2007 | WO |
2009089189 | Jul 2009 | WO |
2003098218 | Nov 2013 | WO |
Entry |
---|
P.J. Hung et al., A Novel High Aspect Ratio Microfluidic Design to Provide a Stable and Uniform Microenvirnment for Cell Growth in a High Throuput Mammalian Cell Culture Array, Lap Chip, 2005, 5, 44-48, published online on Nov. 2, 2004. (Year: 2004). |
Ong et al., “A gel-free 3D microfluidic cell culture system”, Biomaterials, vol. 29, No. 22, 2008, pp. 3237-3244, published online May 2, 2008. |
European Patent Office (EPO), “The extended European search report”, dated Apr. 3, 2012, related EP Patent Application No. 06786499.1, pp. 1-7. |
Chang et al., “Fabrication of polymer microlens arrays using capillary forming with a soft mold of microholes array and UV-curable polymer”, Optical Society of America, Optics Express, vol. 14, No. 13, Jun. 26, 2006, pp. 6253-6258. |
Chao et al., “Rapid frabrication of microchannels using microscale plasma activated templating (PLAT) generating water molds”, The Royal Society of Chemistry, Lab on a Chip, vol. 7, 2007, pp. 641-643, published online Apr. 5, 2007. |
Degenaar et al., “A Method of Micrometer Resolution Patterning of Primary Culture Neurons for SPM Analysis”, The Japanese Biochemical Society, J. Biochem., vol. 130, 2001, pp. 367-376. |
Lim et al., “Fabrication of Microfluidic Mixers and Artifical Vasculatures Using a High-Brightness Diode-Pumped Nd: YAG Laser Direct Write Method”, The Royal Society of Chemistry, Lab on a Chip, vol. 3, 2003, pp. 318-323, published online Oct. 13, 2003. |
Runyon et al., “Minimal Functional Model of Hemistasis in a Biomimetic Microfluidic System”, Amgew. Chem. Intl. Ed. 2004, 43: 1531-1536. |
Tan et al., “Microfludic Patterning of Cellular Biopolymer Matrices for Biomimetic 3-D structures”, Kluwer Academic Publishers, Biomedical Microdevices 5:3, 235-244, 2003. |
Hung et al., “Declaration under 37 CFR 1.132 as to the inventionship of the disclosed and claimed subject invention in relation to the co-authors of a reference publication”, Jun. 18, 2014, related U.S. Appl. No. 11/994,997, 10 pages. |
European Patent Office (EPO), “The extended European search report”, dated Apr. 13, 2016, pp. 1-6, with claims searched, pp. 7-10. |
Hung et al., “A novel high aspect ratio microfluidic design to provide a stable and uniform microenvironment for cell growth in a high throughput mammalian cell culture array”, Lab on a Chip, Vo. 5, 2005, pp. 44-48, published online Nov. 2, 2004. |
European Patent Office (EPO), Office Action dated Jul. 10, 2015, related EP application No. 06786499.1 (pp. 1-4), with claims examined (pp. 5-7). |
ISA/US, International Search Report and Written Opinion, dated Apr. 9, 2008, related PCT International Patent Application No. PCT/US2006/026364, (pp. 1-9), claims searched (pp. 10-16). |
CellASIC Corporation, “ONIX Application Note: Microincubator for Long Term Live Cell Microscopy”, Feb. 3, 2012, pp. 1-4. |
Hung et al., “Continuous Perfusion Microfludic Cell Culture Array for High-Throughput Cell-Based Assays”, Biotechnology and Bioengineering, vol. 89, No. 1, Jan. 5, 2005, pp. 1-8, published online Dec. 3, 2004. |
Lee et al., “Dynamic cell culture: a microfluidic function generator for live cell microscopy”, The Royal Society of Chemistry, Lab on a Chip, vol. 9, No. 1, 2009, published online Oct. 20, 2008, pp. 164-166. |
Lee et al., “Microfluidic System for Automated Cell-Based Assays”, Journal of Laboratory Automation, 12(6): 363-367, Dec. 2007. |
Brinkhof Bas, et al., “Meet the Stem Cells, Production of Cultured Wheat from a Stem Cell Biology Perspective”, Engineering Aspects of Food Biotechnology, Ch5, 2004, pp. 111-142. |
Chung, Bong Geun, et al. “Human neural stem cell growth and differentiation in a gradient-generating microfluidic device”, Lab Chip, 2005, vol. 5 No. 4, published online Mar. 9, 2005, pp. 401-406. |
European Patent Office (EPO), Communication pursuant to Article 94(3) EPC dated Dec. 4, 2017, related European application No. EP 16 150 645.6, pp. 1-4, with claims examined, pp. 5-8. |
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20190106664 A1 | Apr 2019 | US |
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