2021
DOI: 10.1007/s11814-020-0706-z
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Adsorption performance and mechanism investigation of Mn2+ by facile synthesized ceramsites from lime mud and coal fly ash

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Cited by 12 publications
(7 citation statements)
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“…At the same time, the solution pH increased persistently, indicating that the tobermorite could release OH − independently to regulate the pH. The pseudofirst-order (PFO) and pseudosecond-order (PSO) kinetic models, as described in Equations (4) and (5), were used to fit the kinetic data [ 37 ]. The linear plots and obtained parameters are presented in Figure 6 and Table 1 , respectively.…”
Section: Resultsmentioning
confidence: 99%
See 1 more Smart Citation
“…At the same time, the solution pH increased persistently, indicating that the tobermorite could release OH − independently to regulate the pH. The pseudofirst-order (PFO) and pseudosecond-order (PSO) kinetic models, as described in Equations (4) and (5), were used to fit the kinetic data [ 37 ]. The linear plots and obtained parameters are presented in Figure 6 and Table 1 , respectively.…”
Section: Resultsmentioning
confidence: 99%
“…It can be inferred that the release of OH - from tobermorite might be inhibited in solutions with high Cd 2+ concentrations. Isotherm data obtained in this study were analyzed using the Langmuir and Freundlich isotherm models, which are described in Equations (6) and (7), respectively [ 37 ]: C e /Q e = 1/(Q m K L ) + C e /Q m lnQ e = lnK F + nlnC e where C e (mg/L) is the equilibrium concentration; Q e (mg/g) and Q m (mg/g) are the equilibrium and maximum adsorption capacities; K L (L/mg) and K F ((mg/g)/(mg/L) 1/n ) are the adsorption constants of the Langmuir and Freundlich models, respectively; and n is the empirical constant related to adsorption strength.…”
Section: Resultsmentioning
confidence: 99%
“…To investigate the CIP removal mechanism in detail, the kinetic data of CIP removal by the ceramsite at 25 °C was fitted using the pseudo-first-order and pseudo-second-order kinetic models [ 22 ]. The mathematical equations of the two models are presented in Equations (3) and (4): ln(Q e − Q t ) = lnQ e − k 1 t t/Q t = 1/(k 2 Q e 2 ) + t/Q e where t (h) is the contact time, Q e (mg/g) is the adsorption capacity at equilibrium, k 1 (1/h) is the rate constant of the pseudo-first-order model, and k 2 [g/(mg·h)] is the rate constant of the pseudo-second-order model.…”
Section: Methodsmentioning
confidence: 99%
“…Numerous techniques, such as biodegradation [ 16 ], photodegradation [ 4 , 10 , 11 ], advanced oxidation [ 17 , 18 ], adsorption [ 3 , 19 ], membrane separation [ 20 ], and flocculation [ 19 , 21 ], have been adopted to remove CIP. Among these, adsorption has attracted growing attention due to its flexibility, high efficiency, and low operational cost [ 22 ]. The effectiveness of adsorbents and adsorption conditions are key for removal efficiency and adsorption mechanism.…”
Section: Introductionmentioning
confidence: 99%
“…Moreover, the raw material weight ratio and sintering conditions, including sintering temperature, sintering time, preheating temperature, and preheating time were investigated. Ou, C. et al [ 11 ] used two kinds of ceramsites with pH self-adjustment ability synthesized from lime mud and coal fly ash to efficiently control manganese pollution. The influence of different parameters like contact time, concentration of Mn 2+ , and pH on adsorption performance was examined.…”
Section: Introductionmentioning
confidence: 99%