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Following this step, we performed model-based analysis using the parallel flow model (sum of exponential terms), and the logistic growth model.
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Using the parallel plate flow chamber, we examined rolling interactions of undifferentiated HL-60 cells for two different incubation concentrations of P-selectin: 0.5 and 1.5 μg/ml.
Using the parallel plate flow chamber, we examined the rolling interactions of HL-60 cells for two different incubation concentrations of P-selectin: 0.5 and 1.5 μg/ml.
when using the parallel version.
Results show, taking into account pumping losses, that using constant stoichiometry the parallel flow field results in a higher system power under low current density operation compared to the interdigitated configuration.
A number of serious disadvantages have been observed for the reference design, where the parallel flow circuit is used, which is inherent in the majority of blanket modules.
The best result was achieved under the parallel flow condition.
The methanol conversion ratio, yield of hydrogen production in the product of the tree-shaped microreactor, are all evaluated and compared with the corresponding microreactor using a parallel flow pattern.
We then determined if lipid emulsions and LPS inhalation changed the adhesive properties of monocytes using a parallel flow chamber.
To determine the NP targeting in the flow condition, NP suspensions were flown over the vWF-coated glass sides at 10 dyn/cm using a parallel flow system.
The results obtained with the gradient chamber were validated by examining 2, 12 and 50 dynes.cm−2 using normal parallel flow chambers.
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