We have developed an expandable modular body-on-a-chip system that allows for a plug-and-play approach with several in vitro tissues. The design consists of single-organ chips that are combined with each other to yield a multi-organ body-on-a-chip system. Fluidic flow through the organ chips is driven via gravity and controlled passively via hydraulic resistances of the microfluidic channel network. Such pumpless body-on-a-chip devices are inexpensive and easy to use. We tested the device by culturing GI tract tissue and liver tissue within the device. Integrated Ag/AgCl electrodes were used to measure the resistance across the GI tract cell layer. The transepithelial resistance (TEER) reached values between 250 to 650 Ω cm(2) throughout the 14 day co-culture period. These data indicate that the GI tract cells retained their viability and the GI tract layer as a whole retained its barrier function. Throughout the 14 day co-culture period we measured low amounts of aspartate aminotransferase (AST, ∼10-17.5 U L(-1)), indicating low rates of liver cell death. Metabolic rates of hepatocytes were comparable to those of hepatocytes in single-organ fluidic cell culture systems (albumin production ranged between 3-6 μg per day per million hepatocytes and urea production ranged between 150-200 μg per day per million hepatocytes). Induced CYP activities were higher than previously measured with microfluidic liver only systems.
Predicting drug-induced liver injury with in vitro cell culture models more accurately would be of significant value to the pharmaceutical industry. To this end we have developed a low-cost liver cell culture device that creates fluidic flow over a 3D primary liver cell culture that consists of multiple liver cell types, including hepatocytes and non-parenchymal cells (fibroblasts, stellate cells, and Kupffer cells). We tested the performance of the cell culture under fluidic flow for 14 days, finding that hepatocytes produced albumin and urea at elevated levels compared to static cultures. Hepatocytes also responded with induction of P450 (CYP1A1 and CYP3A4) enzyme activity when challenged with P450 inducers, although we did not find significant differences between static and fluidic cultures. Non-parenchymal cells were similarly responsive, producing interleukin 8 (IL-8) when challenged with 10 μM bacterial lipoprotein (LPS). To create the fluidic flow in an inexpensive manner, we used a rocking platform that tilts the cell culture devices at angles between ±12°, resulting in a periodically changing hydrostatic pressure drop and bidirectional fluid flow (average flow rate of 650 μL/min, and a maximum shear stress of 0.64 dyne/cm2). The increase in metabolic activity is consistent with the hypothesis that, similar to unidirectional fluidic flow, primary liver cell cultures derived from human tissues increase their metabolic activity in response to bidirectional fluidic flow. Since bidirectional flow drastically changes the behavior of other cells types that are shear sensitive, the finding that bidirectional flow increases the metabolic activity of primary liver cells also supports the theory that this increase in metabolic activity is likely caused by increased levels of gas and metabolite exchange or by the accumulation of soluble growth factors rather than by shear sensing. Our results indicate that device operation with bi-directional gravity-driven medium flow supports the 14-day culture of a mix of primary human liver cells with the benefits of enhanced metabolic activity. Our mode of device operation allows us to evaluate drugs under fluidic cell culture conditions and at low device manufacturing and operation costs.
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