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These results recommend that the initial sorption technique of copper sulphate powder will also be modelled as a gentle-state sorption process. CaCl2/CNTs composite; and (c) composite material after twentieth cycle of sorption/desorption process. The results indicate that the measured sorption fee (1.7 g/100 g/h) remained constant in the first 1.5 h of the initial sorption process. When the η was increased to 80%, their sorption rates elevated to 56.1, 44.9 and 42.Four g/(m2s), respectively.
The testing results are proven in Fig. 5. It can be observed from Fig. 5a that when the η was 50%, the respective sorption charges of CaCl2/NaCl, CaCl2/sugar and saturated solution of CaCl2 have been 16.6, 12.Zero and 5.6 g/(m2s), respectively. To review whether the regular-state sorption equation could be utilized to powder sorbents, the sorption curve of copper sulphate powder was measured, as proven in Fig.
7. The dashed line is the tangent of the sorption curve on the origin; the worth of its slope, , is the preliminary sorption rate of copper sulphate crystal. Thus, the NaCl strong electrolyte improved the sorption performance, whereas the sucrose non-electrolyte decreased the sorption efficiency. To verify that this method is efficient for powder material, the CaCl2, activated carbon and NaCl with certain ratios have been homogeneously mixed to prepare a composite sorbent.
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