2006
DOI: 10.1016/j.jenvman.2005.11.003
|View full text |Cite
|
Sign up to set email alerts
|

Sorption of cadmium and zinc from aqueous solutions by zeolite 4A, zeolite 13X and bentonite

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1
1
1

Citation Types

1
22
0

Year Published

2009
2009
2021
2021

Publication Types

Select...
7
1

Relationship

0
8

Authors

Journals

citations
Cited by 119 publications
(26 citation statements)
references
References 20 publications
1
22
0
Order By: Relevance
“…V is the volume of the solution (cm 3 ) and W is the mass of sorbent (g) used. 49 where q e (mg g –1 ) and C e (mg dm –3 ) are the equilibrium concentrations of As( v ) in the adsorbed and liquid phases, and q m (mg g –1 ) and b (L mg –1 ) are the Langmuir constants and q m is the maximum monolayer capacity. q e = K f C e 1/ n where K f (mg g –1 ) and n (L mg –1 ) are the Freundlich constants, which are related to the sorption capacity and intensity of adsorption, respectively. The sorption equilibrium data of As( v ) onto Fe-GN were analysed by fitting the data to Langmuir and Freundlich isotherm models using Origin Pro 8.6.…”
Section: Methodsmentioning
confidence: 99%
“…V is the volume of the solution (cm 3 ) and W is the mass of sorbent (g) used. 49 where q e (mg g –1 ) and C e (mg dm –3 ) are the equilibrium concentrations of As( v ) in the adsorbed and liquid phases, and q m (mg g –1 ) and b (L mg –1 ) are the Langmuir constants and q m is the maximum monolayer capacity. q e = K f C e 1/ n where K f (mg g –1 ) and n (L mg –1 ) are the Freundlich constants, which are related to the sorption capacity and intensity of adsorption, respectively. The sorption equilibrium data of As( v ) onto Fe-GN were analysed by fitting the data to Langmuir and Freundlich isotherm models using Origin Pro 8.6.…”
Section: Methodsmentioning
confidence: 99%
“…Temperature, pH, zeolite concentration and initial metal concentration are the major parameters that are considered to have an effect on the removal of heavy metals. Several studies report the superior heavy metal sorption capacities for zeolites with low Si:Al ratios [38,[41][42][43]. The prominent role played by Si:Al ratio on the sorption of heavy metals has been demonstrated in the study of Leinonen and Lehto [42].…”
Section: Structure Of Zeolitementioning
confidence: 98%
“…Strong bases can lead to desilication, whereas strong acids can break Al atoms. Zeolite structure can be destroyed at extreme pH values, which in turn can reduce sorption [40,43]. Since zeolite is capable of changing the pH of the solution, there is a possibility for these processes to occur during the treatment of polluted water.…”
Section: Ph Ph Is Used As An Indirect Measurement Of the Concentratiomentioning
confidence: 99%
“…Typical equilibrium times for Zn 2+ -uptake by clays (stevensite 44 and bentonite 45 ) and zeolites (A, 46 4A, 45 13X 45 ) are within 2 h of contact and maximum sorption capacities are generally found to be between 0.3 mmol g −1 and 2.5 mmol g −1 . A number of studies has shown that the pseudosecond-order model is representative of these processes and k 2 values in the range 8.3 × 10 −3 to 15.43 g mmol −1 min −1 are reported.…”
Section: Ag + and Zn 2+ Ion Exchange Kineticsmentioning
confidence: 99%
“…A number of studies has shown that the pseudosecond-order model is representative of these processes and k 2 values in the range 8.3 × 10 −3 to 15.43 g mmol −1 min −1 are reported. [44][45][46] In comparison, the Zn 2+ -exchange rates for Tob-Na1 (k 2 = 8.50 × 10 −4 g mmol −1 min −1 ) and Tob-Na4 (k 2 = 9.87 × 10 −4 g mmol −1 min −1 ) are considerably slower than those documented in the literature; however, the extents of Zn 2+ -uptake by the tobermorite specimens were found to be towards the top end of the reported range for clays and zeolites. [44][45][46] …”
Section: Ag + and Zn 2+ Ion Exchange Kineticsmentioning
confidence: 99%