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In two dimensions, flow occurs either in a horizontal plane or cross section (profile).
The design of such reactors requires a prior knowledge of the jet dimensions, flow pattern and heat transfer characteristics.
Good agreement is observed for a range of reactors having various geometric dimensions, flow rates and reactant concentrations.
The aim is to model (in 2 dimensions) flow towards a sampling probe used to extract reservoir fluids from the rock surrounding a newly-drilled well.
A comparison between the condensation and the reaction jets has been presented in terms of plume dimensions, flow and temperature patterns.
The effects of a multi-segment catalyst and cavities on channel walls are examined and discussed in terms of various catalyst layouts, cavity dimensions, flow conditions, and reactor properties.
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In three-dimensions, flow deformation maps, whose eigenvalues determine the FTLE, develop steep gradients over shorter finite times than in two-dimensions.
The critical Reynolds number for the flow regime transformation is smaller than that for the routine dimension flow path.
In general, the DDG and its variants show promising properties and it indicates that these approaches have a great potential for higher dimension flow problems.
To prevent loss of analytes during the online analyses, the first-dimension flow rate did not exceed the 0.2 μL min−1.
Modulation between the first- and second-dimension, which may be achieved by focussing and desalting on trap columns before analyses on the D column [ 36], may allow reducing the D column diameter and, thus, the second-dimension flow rate.
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