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The design of catalytic distillation (CD) columns is a challenging task because of the superposition of chemical reaction and distillation in one apparatus.
The feasibility of internally finned monoliths (IFMs) as a packing for multifunctional reactors, such as catalytic distillation (CD) columns, is investigated by evaluating the most important design parameters.
CD columns that align to gaps inserted into the query are ignored.
Therefore, we weight aligned CD columns not as a function of their match score, but rather proportionately to their effective number of independent observations.
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The (c) columns report the result of the logistic MESE model.
In Fig. 6b, c columns I, II amd III, the corresponding Bode and phase diagrams of these samples are given.
Similarly, for both men and women, β ̂ 2 is reasonably similar in columns (a) and (b), but appears biased upward in the (c) columns.
Matrices with samples in r rows and environmental variables in c columns were generated for water (31 × 13) and sediment (13 × 12) data.
Samples were separated in two 30 cm PLGel Mixed C columns (Agilent) at 30°C with distilled chloroform as the mobile phase.
Open image in new window Fig. 6 The load deflection curves of glulam columns considered in the analysis a columns with length of 600 mm; b columns with length of 850 mm; c columns with length of 1100 mm.
This consisted in the construction of a two-way contingency table CT with r rows and c columns, meaning that method A produces r row clusters and method B produces c columns clusters.
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