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In general, higher desulfurization activity correlates with higher sorbent surface area.
The entire width of the sorbent layer area can be used to develop separations or elute samples.
The effects of reaction temperature, H2S concentration, and sorbent surface area on the extent of sulfur capture and conversion of sorbent are determined.
The results obtained showed significant decrease of sorbent surface area after pretreatment and the presence of smooth CaO grains was typical of the sorbent particle surface morphology.
In the second step, a neural network was used to model the relationship between the three hydration variables and the sorbent surface area.
In the first step of the approach, the main and interactive effects of three hydration variables on sorbent surface area were evaluated using a full factorial design.
The sorbent surface area (271 and 943 m2/g) and the sorption capacity (Qm = 1.03 and 3.59 mmol/g) were estimated for the CS PAA copolymer/MB systems in aqueous solution.
According to this integrated modeling and optimization approach, an optimum sorbent surface area of 62.2 m2 g−1 could be obtained by mixing 13.1 g of coal fly ash and 5.5 g of calcium sulfate in a hydration process containing 100 ml of water and 5 g of calcium oxide for a fixed hydration time of 10 h.
Therefore, sorbent surface area of 218 cm2 was selected.
Open image in new window Fig. 6 Effect of sorbent surface area and time of removal in presence and absence of light for lead ion.
Here we report a simple method, termed the BoNT Assay with a Large Immuno-sorbent Surface Area (ALISSA), that uses common laboratory equipment and commercially available reagents.
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