Environmental Engineering Reference
In-Depth Information
activated carbons (Anderson, 2000). TCE sorption on the wet zeolites decreased with
increasing surface cation density. Results suggest that TCE be adsorbed in hydrophobic
micropores by displacing loosely bound water, consistent with the theoretical
considerations. This indicates that the process of transferring loosely bound water from
hydrophobic micropores into the bulk phase is energetically favorable (Cheng and
Reinhard, 2006).
Table 11.3 Summary of water treatment by zeolite containing adsorbent.
Type of
Zeolite
Contaminants
Removed
(mg/g)
Issues
Ref.
NH 4 + :4.5
Ni 2+ : 2.3
Zn 2+ : 2.5
Clinoptilolite
Cheap but low adsorption capacity
(Johnson
and Worrall,
2007)
NH 4 + :13.2
Ni 2+ :16.5
Zn 2+ :18
Synthetic
Zeolites-
Vermiculite
Modified zeolite has more adsorption
capacity
NH 4 + :13.64
Natural
Zeolite
Cheap
(Maranon et
al., 2006)
Zn 2+ : 31.58
Synthetic
Zeolite
Powders
Synthetic zeolite in powder form has
more adsorption capacity
(Hui et al.,
2005)
Zeolites with
High SiO 2 /
Al 2 O 3 Ratios
methyl tert-butyl
ether (MTBE),
CHCl 3 & TCE
An equilibrium solution concentration
of 100 g/L, high Si mordenite retained
812 × more MTBE than PACs
(Anderson,
2000)
Y zeolites
from
Hydrophilic
CBV-300 to -
720 & -780
TCE
Sorption of volatile organic compounds
(VOCs) in low organic carbon (< 0.1%)
geosorbents is difficult to predict
because the sorption capacity of the
mineral matrix is poorly understood
(Cheng and
Reinhard,
2006)
Solid Na-Y
Zeolite
Pb and Cd
Pb and Cd removal from solution by
batch ion exchange with a solid Na---Y
zeolite has been studied
(Ahmed et
al., 1998)
Natural
Zeolite
Fe, Pb, Cd, and
Zn from synthetic
mine waters
Pb was removed efficiently from neutral
as well as from acidic solutions, whereas
the uptake of Zn and Cd decreased with
low pH and high iron concentrations
(Wingenfeld
er et al.,
2005)
Co 2+ , Cr 3+ , Cu 2+ ,
Zn 2+ & Ni 2+
Zeolite 4A
The removal performance and the
selectivity sequence of the mixed metal
ions were investigated by adsorption on
pure and chamfered-edge zeolite 4A
prepared from coal fly ash (CFA),
commercial grade zeolite 4A and the
residual products recycled from CFA
(Hui et al.,
2005)
 
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