Abstract:The equilibria of adsorption of aspartame in an aqueous solution on a commercial resin and three
chemically modified Amberlite XAD-2 resins were measured at different temperatures within the range
(0 to 35) °C. The functional groups, introduced by nucleophilic substitution in the aromatic rings of the
divinylbenzene−styrene matrix, were bromine (−Br), bromoethyl (−CH2CH2Br), and chloromethyl (−CH2Cl). All of the isotherms showed a nonlinear and favorable shape with decreasing adsorption capacity as
the tempera… Show more
“…The experimental equilibrium data as shown in Table 3 were fitted to the Langmuir and Freundlich models. 19,20 The adsorption behavior of NERCB 09 agreed with the Langmuir isotherm model well. Figures 1 and 2, temperature had little effect on the adsorption capacity, but adsorption capacity increased dramatically when the pH value decreased.…”
Section: Adsorption Characteristics Of Nercb 09mentioning
Succinic acid is one of the platform chemicals that can be bioproduced from renewable resources. Separation of succinic acid by adsorption from model solutions and fermentation broth by weak alkaline anion exchange adsorbents was studied. Adsorption capacities and regenerability of several sorts of adsorbents were tested. In a static test, the adsorbent NERCB 09 has the adsorption capacity of 0.11 g succinic acid g -1 at succinic acid concentrations of 5 g L -1 . In packed column test, its capacity was as high as 0.56 g succinic acid g -1 when the feeding concentration was 50 g L -1 . NERCB 09 showed the high selectivity toward succinate over both glucose and amino acid at acidic or neutral conditions. Langmuir/Freundlich isotherm models and pseudofirst/second-order equations were presented to simulate the adsorption behavior. Data showed that the temperature had little effect on the adsorption isotherm. Kinetic parameters suggested that about 1.5 h were sufficient for the adsorption equilibrium. The adsorbent was easily regenerated. The adsorption capacity was steady after 30 cycles and showed 96% average recovery.
“…The experimental equilibrium data as shown in Table 3 were fitted to the Langmuir and Freundlich models. 19,20 The adsorption behavior of NERCB 09 agreed with the Langmuir isotherm model well. Figures 1 and 2, temperature had little effect on the adsorption capacity, but adsorption capacity increased dramatically when the pH value decreased.…”
Section: Adsorption Characteristics Of Nercb 09mentioning
Succinic acid is one of the platform chemicals that can be bioproduced from renewable resources. Separation of succinic acid by adsorption from model solutions and fermentation broth by weak alkaline anion exchange adsorbents was studied. Adsorption capacities and regenerability of several sorts of adsorbents were tested. In a static test, the adsorbent NERCB 09 has the adsorption capacity of 0.11 g succinic acid g -1 at succinic acid concentrations of 5 g L -1 . In packed column test, its capacity was as high as 0.56 g succinic acid g -1 when the feeding concentration was 50 g L -1 . NERCB 09 showed the high selectivity toward succinate over both glucose and amino acid at acidic or neutral conditions. Langmuir/Freundlich isotherm models and pseudofirst/second-order equations were presented to simulate the adsorption behavior. Data showed that the temperature had little effect on the adsorption isotherm. Kinetic parameters suggested that about 1.5 h were sufficient for the adsorption equilibrium. The adsorbent was easily regenerated. The adsorption capacity was steady after 30 cycles and showed 96% average recovery.
“…Table 4 exhibits the pattern that the adsorption capacity of JN-10 for the HA increases when the temperature of the solution rises. The isometric enthalpies of adsorption were calculated according to the derivative Van't Hoff equation [19]: The free energy of adsorption was calculated according to the equation [20]:…”
Section: Isometric Enthalpies For the Ha Adsorbed By Jn-10mentioning
“…The Langmuir-Freundlich (LF) isotherm resembles the format of the Langmuir isotherm model but is modified according to the Freundlich isotherm model to satisfy the Henry's law behavior at the equilibrium adsorption of the adsorbates [35]. The Langmuir-Freundlich isotherm model often takes the following form [2,35,36],…”
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