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The real adsorption separation has been investigated by dynamic breakthrough tests at 297 K and 101.325.
Dynamic breakthrough curves were used to investigate the best adsorption conditions in bioethanol liquid phase.
The performance of these HUMs was confirmed by real-time dynamic breakthrough experiments.
Dynamic breakthrough capacities of the analogs were compared to 13X zeolite and BPL activated carbon.
The performance of materials as H2S adsorbents was tested using a home-developed dynamic breakthrough test.
Dynamic breakthrough profiles have been registered and exploited to determine ion exchange equilibria and mass transport resistances.
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A dynamic H2S breakthrough test was used (Fig. 1) and the resulting breakthrough curves for tested adsorbents are shown in Fig. 5.
Experimental methods have included XRD characterization, adsorption isotherms, and dynamic adsorption breakthrough.
A dynamic CO2/N2 breakthrough setup was constructed to separate CO2 from a CO2/N2 mixture (representing a flue gas), Fig. 1.
In addition, extensive dynamic column breakthrough experiments were conducted with the synthesized sample to establish the gas transport mechanism.
The gas separation capabilities of all the samples were examined using a developed dynamic CO2/N2 breakthrough setup, as shown in Fig. 2.
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