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Average loading of adsorbent (mg/g).
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For OYE2 and CrS, a 40-fold loading capacity of adsorbent gave best results by scavenging >90% of phenol, going in hand with considerably enhanced conversions and a near-quantitative value for CrS (c 97%) (Table 2).
Results show that by decreasing the operating temperatures in the adsorber to 42 °C, the dynamic CO2 loading of the adsorbent could be increased to 7.4 wt%.
Increasing the CO2 concentrations of the adsorber feed-gas leads to an increase of the CO2 capture rate and dynamic CO2 loading of the adsorbent.
The change of operating pressure does not have a significant effect on the shape of the breakthrough curve or sulfur loading of the adsorbent.
However, large gas bubbles observed at adsorber feed-gas velocities exceeding 0.69 make1 make insufficient gas-solids contact likely, which in turn explains a reduction of the dynamic CO2 loading of the adsorbent at these conditions.
However, batch adsorption studies shows that 85% MG adsorption was achieved for 40 mg of adsorbent loading.
Figure 7a, b shows the influence of dosage of adsorbent loading on UV absorption and percentage adsorption of MG respectively, it is clear from both the graphs that as the amount of the adsorbent increases adsorption capacity also increases.
The effect of adsorbent loading is done by varying the amount of the nanoadsorbent from 5 to 50 mg and stirring it with 100 mL of dye solution under dark for 30 min.
Experiments were carried out as a function of adsorbent loading, pH, contact time, initial dye concentration and temperature using Reactive Red 4 anionic dye (RR4) as a model pollutant.
Alveolar macrophages were treated with carbon blacks and adsorbates in order to evaluate the biologic effect of adsorbate, adsorbent and adsorbate-adsorbent complexes.
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