phosphorus removal from wastewater by mineral apatite
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Phosphorus removal from wastewater by mineral apatite
Nathalie Belliera, Florent Chazarenca,b,�, Yves Comeaua
aDepartment of Civil, Geological and Mining Engineering, Ecole Polytechnique, 2900 Edouard-Montpetit, Montreal, Que., Canada H3T 1J4bInstitut de recherche en biologie vegetale, Universite de Montreal, 4101 rue Sherbrooke Est, Montreal, Que., Canada H1X 2B2
a r t i c l e i n f o
Article history:
Received 4 April 2006
Received in revised form
12 May 2006
Accepted 18 May 2006
Available online 10 July 2006
Keywords:
Apatite
Hydroxyapatite crystallization
Phosphorus removal
Wastewater treatment
nt matter & 2006 Elsevie.2006.05.016
thor. Institut de recherchl.: +1 514 872 3942; fax: +
Florent.Chazarenc@umon
A B S T R A C T
Natural apatite has emerged as potentially effective for phosphorus (P) removal from
wastewater. The retention capacity of apatite is attributed to a lower activation energy
barrier required to form hydroxyapatite (HAP) by crystallization. The aim of our study was
to test the P removal potential of four apatites found in North America. Minerals were
collected from two geologically different formations: sedimentary apatites from Florida
and igneous apatites from Quebec. A granular size ranging from 2.5 to 10 mm to prevent
clogging in wastewater applications was used. Isotherms (24 and 96 h) were drawn after
batch tests using the Langmuir model which indicated that sedimentary apatites presented
a higher P-affinity (KL ¼ 0.009 L/g) than igneous apatites (KLE0.004 L/g). The higher density
of igneous material probably explained this difference. P-retention capacities were
determined to be around 0.3 mg P/g apatite (24 h). A 30 mg P/L synthetic effluent was fed
during 39 days to four lab-scale columns. A mixture of sedimentary material (apatite and
limestone 50–50%, w/w) showed a complete P-retention during 15 days which then
declined to 65% until the end of the 39 days lab scale test period. A limitation in calcium
may have limited nucleation processes. The same mixture used in a field scale test showed
60% P-retention from a secondary effluent (30 mg COD/L, 10 mg Pt/L) during 65 days without
clogging.
& 2006 Elsevier Ltd. All rights reserved.
1. Introduction
Adverse effects of eutrophication due to the presence of
anthropogenic phosphorus (P) in surface waters are well-
established. Conventional technologies for P-removal from
wastewater are physical processes (settling, filtration), che-
mical precipitation (with aluminium, iron and calcium salts),
and biological processes that rely on biomass growth
(bacteria, algae, plants) or intracellular bacterial polypho-
sphates accumulation (De-Bashan and Bashan, 2004). Low
cost, low maintenance extensive treatment processes based
on P-retention in filters containing reactive media have been
developed and showed promising results (De-Bashan and
Bashan, 2004). The aim of this project was to favour P-
r Ltd. All rights reserved.
e en biologie vegetale, U1 514 872 9406.treal.ca (F. Chazarenc).
crystallization in a filter located at the downstream end of the
sludge treatment line to reduce clogging by suspended solids.
Natural apatite, a mineral found in igneous, sedimentary and
metamorphic rocks (Nriagu and Moore, 1984), and in teeths
and bones, was shown to favour P-removal from wastewater
(Joko, 1984; Jang and Kang, 2002; Molle et al., 2005). The scope
of this paper was to test and evaluate the P-removal potential
of several apatites found in North America.
The driving mechanisms in the process of P-crystallization
consist essentially in nucleation (precipitation of hydroxya-
patite (HAP): Ca10(PO4)6OH2), followed by crystal growth.
Nucleation is believed to be initiated by the formation of a
metastable precursor, characterised by an amorphous phase
consisting in the combination of calcium phosphates at
niversite de Montreal, 4101 rue Sherbrooke Est, Montreal, Que.,
ARTICLE IN PRESS
WAT E R R E S E A R C H 4 0 ( 2 0 0 6 ) 2 9 6 5 – 2 9 7 12966
a Ca/P molar ratio of between 1 and 1.5 (Zoltek, 1974). The
presence of a crystal acts like a catalyst which lowers the
activation energy barrier between the crystal and HAP. Seeded
precipitation of calcium phosphate is favoured by a high pH,
an increased contact time and a high Ca/P molar ratio. Several
media favouring the seeded precipitation of phosphate from
wastewater were tested, such as magnetite minerals
(Karapinar et al., 2004), steel slags (Shilton et al., 2005; Kostura
et al., 2005; Kim et al., 2006; Korkusuz et al., 2005; Naylor et al.,
2003), calcite limestone and concrete (Song et al., 2006;
Comeau et al., 2001; Molle et al., 2003). P-retention capacity
of mineral apatites for wastewater treatment varied between
2.7 and 4.8 mg P/g apatite in batch experiments which were
followed by successful column tests (Joko, 1984; Molle et al.,
2005).
For P-removal using natural apatites, adsorption mechan-
isms are also believed to play a role and the distinction
between adsorption and crystallization is not clear (Molle
et al., 2005). Considering that their concomitant action is
expected to occur, adsorption is believed to enhance nuclea-
tion/crystallization (Stumm and Morgan, 1996).
In this paper, the P-retention potential of three igneous
apatites from Quebec, one sedimentary apatite from Florida
and one sedimentary limestone was studied. Batch tests were
first performed which enabled to draw isotherms and rank
the samples according to their P-removal potential. Then,
flow-through lab and field scale column tests were conducted
which showed the better potential of sedimentary apatites
mixed with limestone over igneous apatites.
2. Material and methods
2.1. Media tested and sample preparation
Four apatite-containing materials and a limestone, identified
by their suppliers, were tested (Table 1). Samples were
prepared as follows: crushing, rinsing, air-drying and sieving.
During extraction, the associated gangue of the Cargill apatite
was separated by the supplier. This may have reduced the
amount of calcium and hydroxide available in the sample.
Table 1 – Apatite-containing media tested
Media supplier Location Geographiccoordinatesa
M
Cargill (USA) Florida 2714104900N Ph
8115004300W
Soquem (Quebec) Sept-Iles 5011502800N
6612904400W
Arianne (Quebec) Lac St-Jean 4915400500N
7014503000W
Niobec (Quebec) St-H de
Chicoutimi
4813200800N
7110902800W
Graymont
(Quebec)
Joliette 4610004100N
7312702600W
a Geographic Reference System: WGS 84.b Niobec is exploiting niobium oxide (Nb2O5).
In view of full-scale filters where clogging should be
avoided, a granular size of 2.5–10 mm for batch and column
experiments was used.
Particle-size distribution was determined (ASTM D 421-422)
to estimate the specific surface area of the 2.5–10 mm
material assuming a spherical shape. The density of each
material was determined according to ASTM standard test
methods (ASTM C 127-01 for 5–10 mm fraction, and ASTM D
854-02 for 2.5–5 mm fraction).
2.2. Batch tests
Batch tests were conducted with synthetic solutions (KH2PO4
in distiled water) with a gyratory shaker (160 rpm) at 2272 1C.
A mass of 35 g of material was placed in a 1 L glass flask filled
with 700 mL of solution. The pH (8.070.1) and conductivity
(10007100mS/cm) were adjusted using NaOH and NaCl to be
similar to a secondary treated effluent. Isotherm experiments
were conducted at P solutions ranging from 5 to 150 mg P/L
and lasting 24 and 96 h. All samples were analysed for pH,
conductivity, turbidity, suspended solids and orthopho-
sphates (o-PO4).
P adsorption capacity was modelled using Langmuir
isotherms, linearized as
Ce
qe
¼1KLþ
aL
KLCe, (1)
where Ce is the equilibrium concentration of P in solution
(mg P/L) and qe is the amount of P adsorbed (mg P/g material).
The Langmuir constants are graphically defined by KL and aL.
KL describes the affinity between P and the material, and is
represented by the initial slope. The constant KL/aL deter-
mines the P adsorption maximum.
2.3. Column tests
Lab scale column tests were carried out using four 100 mm
diameter columns filled with 2.5 L of material (Niobec, Cargill,
Graymont and Cargill/Graymont mixture 50–50%w/w). A
synthetic P solution (P–PO4 30 mg/L, tap water, pH 7.570.1)
was continuously pumped into the bottom of each column at
ine or prospectdeposit
Identification Geologicalformation
osphate rock mine Francolite-
hydroxyapatite
Sedimentary
Prospect apatite/
magnetite
Fluoroapatite Igneous
Prospect apatite/
ilmenite
Apatite Igneous
Niobium mineb Fluoroapatite Igneous
Limestone quarry Limestone Sedimentary
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Table 2 – Chemical and physical characteristics of the five tested media
Material Chemical composition (%w/w) Density (g/cm3) Specif. area (m2/kg) Particle sizeb
Si Al Ca Mg Fe P d10 (mm) d60 (mm)
Cargill 5.5 0.8 31.4 0.7 1.1 11.3 2.85 0.72 2.8 4.5
Soquem 10.3 4.0 8.6 4.0 22.0 2.4 3.51 0.48 3.0 6.0
Arianne 15.0 4.7 7.0 4.7 19.0 2.0 3.37 0.53 3.0 6.0
Niobec 2.7 0.7 25.7 6.3 3.6 5.2 3.00 0.58 3.0 6.0
Graymont n.a.a n.a. n.a. n.a. n.a. n.a. 2.72 0.57 3.5 7.0
a n.a: not available.b d10, d60: grain size of 10% and 60% material by weight.
Table 3 – Influent and effluent characteristics of lab scalecolumns test
Conductivity(mS/cm)
pH Ca2+
(mg/L)
Synthetic
influent
531726 7.970.1 31.870.7
Niobec effluent 575763 7.670.3 31.170.9
Cargill effluent 491739 7.170.4 2.872.5
Graymont
effluent
571749 7.970.2 32.372.6
Cargill/
Graymont
effluent
560751 7.670.3 29.171.7
WAT E R R E S E A R C H 40 (2006) 2965– 2971 2967
a flow rate of 0.7 L/d for 39 days (hydraulic retention time of
1.5 d considering void space [HRTv]). Samples were taken at
the inlet and outlet of the columns, every day during the first
15 days and every three days until day 39.
Field scale tests were carried out using a 6.5 L total volume
column filled with a mix of Cargill apatite and Graymont
limestone (50–50%w/w). The columns were installed at a fish
farm plant and were fed with a constructed wetland effluent
(30 mg COD/L, 10 mg Pt/L) such that the HRTv was initially set
at 0.33 d and operated during 65 days.
The concentration was fixed at of 30 mg P/L in lab scale
tests, based on annual average concentrations measured in a
wetland effluent from a fish farm plant. Since the field scale
tests were conducted during summer, P retention was more
important in the constructed wetland resulting in a lower P
concentration of the wetland effluent (10 mg P/L).
2.4. Analytical methods
Orthophosphates were measured using the Quickchem flow
injection analysis method # 10-115-01-1-Q derived from the
automated ascorbic acid reduction method (Standard Meth-
ods, 1998). Ionic measurements conducted on samples
collected from column tests, as well as chemical composition
of tested minerals, were analysed by the atomic absorption
spectroscopy method (Standard Methods, 1998).
3. Results and discussion
3.1. Chemical and physical media characteristics
The Ca and P content of the Cargill apatite (Table 2) was in the
same range as those tested by Molle et al. (2005) which
containing 37.3% Ca and 16.8% P, and materials tested by Joko
(1984) containing 37.6% Ca and 15.2% P. The Ca/P molar ratio
of 2.78 of the Cargill apatite, compared to the ratio of 1.67 of
pure hydroxyapatite, suggests that some P was substituted by
CO32� which is generally the case in carbonate-substituted
(low-grade) phosphate rock like francolite (Nriagu and Moore,
1984). The presence of calcite or dolomite in the gangue
associated to the apatite may also have contributed to
increase this ratio (Slansky, 1986). The occurrence of iso-
morphic substitutions in apatite from Morocco (Molle et al.,
2005), giving a lower density of 2.48 g/cm3 compared to that
from Cargill (Table 2), resulted in an increase of the internal
porosity (Zapata and Roy, 2004) and in a larger surface of
reaction (Table 3).
Igneous rocks are characterized by a higher density (Table
2), suggesting a lower internal porosity due to their mode of
crystallization in magma (Zapata and Roy, 2004). Apatites
from Soquem, Arianne and Niobec showed concentrations
varying between 2% and 5% P (Table 2) which is in the range of
natural igneous apatite (Nriagu and Moore, 1984). Aluminium,
magnesium and iron were also present in a relatively high
proportion, notably in the Soquem and Arianne apatites
(Nriagu and Moore, 1984; Al 0.05%).
3.2. Batch tests
A solubilization batch test (in distiled water) showed no
electrical conductivity and pH variation with apatite samples,
while dissolution of limestone from Graymont led to an
increase in pH (from 8.0 to 9.5) and in conductivity. Langmuir
isotherms determined after 24 h, showed a limited affinity
between apatites and P, as indicated by the smooth initial
slopes (Fig. 1). Graymont limestone 24 h isotherms showed a
constant affinity with P either because adsorption took place
regardless of the material, or due to the increase of adsorbate
which proportionally augmented adsorbing sites (Sposito,
1989).
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0.0
0.1
0.2
0.3
0 20 40 60 80 100 120 140
Ce (mgP/L)
qe
(mg
P/g
mat
eria
l)
Cargill Langmuir Cargill
Graymont Langmuir Graymont
Cargill Langmuir Cargill
Graymont Langmuir Graymont
0.0
0.1
0.2
0.3
0 20 40 60 80 100 120 140
Ce (mgP/L)
qe
(mg
P/g
mat
eria
l)
Soquem Langmuir SoquemArianne Langmuir ArianneNiobec Langmuir Niobec
Soquem Langmuir SoquemArianne Langmuir ArianneNiobec Langmuir Niobec
0.0
0.2
0.4
0.6
0.8
1.0
0 20 40 60 80 100 120 140
Ce (mg P/L)
qe
(mg
P/g
mat
eria
l)
0.0
0.2
0.4
0.6
0.8
1.0
0 20 40 60 80 100 120 140
Ce (mg P/L)
qe
(mg
P/g
mat
eria
l)
(A) (B)
(D)(C)
Fig. 1 – Equilibrium isotherms of phosphate (22 1C) (Cargill apatite and Graymont limestone: (A) 24 h, (C) 96 h; Soquem,
Arianne and Niobec apatites: (B) 24 h, (D) 96 h).
WAT E R R E S E A R C H 4 0 ( 2 0 0 6 ) 2 9 6 5 – 2 9 7 12968
P-retention capacities calculated from the 24 h Langmuir
isotherms (in mg P/g material: Graymont: 1.09; Arianne: 0.41;
Soquem: 0.37; Cargill: 0.31; Niobec: 0.28) were low compared
to those found in the literature (2.7–4.8 mg P/g apatite; Molle
et al., 2005; Joko, 1984). According to 96 h isotherms (Fig. 1), a
greater affinity was found between P and sedimentary
materials. Igneous apatites were found to be less reactive
with P, possibly due to their lower internal porosity. Con-
sidering the importance of calcium in P-retention mechan-
isms, the limited dissolution observed for the Cargill apatite
and the absence of calcium in the synthetic P-solution
possibly led to a limitation in available Ca.
The low specific surface area of the material used in this
study, due to the relatively coarse material, influenced the
P-removal efficiency. Furthermore, apatite crystal sizes were
relatively small (0.1–0.5 mm in Niobec apatite), compared to
the granular size selected (2.5–10 mm), reducing the rates of P
adsorption. Using 24 h Langmuir isotherms, the tested
materials ordered by decreasing affinity based on KL coeffi-
cients were as follows: Cargill4Arianne4Niobec4Soquem4-
Graymont. Some indications in batch experiments suggest
that adsorption occurred almost instantaneously and was
rapidly followed by precipitation. Adsorption being a surface
phenomenon, it is considered that the high densities
associated with igneous materials was not favourable to
these types of apatites as adsorbents, in which poor internal
porosities were expected. Since the Cargill apatite presented a
lower density compared to igneous apatites, this could
explain the high affinity found for the sedimentary
apatite. No improvement for the igneous apatite was appar-
ent after 96 h.
Fluoroapatite presents a pH zero point of charge (pHZPC)
varying between 4 and 6, a lower value than for hydroxyapa-
tite (7.6–8.6), which may discredit compounds rich in fluor-
apatite (Arianne, and Soquem) as favourable substrates for
phosphate adsorption. Apatites are, however, largely asso-
ciated with other minerals in their natural state, and
adsorption may occur in non-apatitic mineral support
(especially in Arianne and Soquem media).
Another linearization of Langmuir isotherm (Kd ¼ qe/
Ce ¼ f(qe)) allowed the identification of two potential
P-retention mechanisms for Cargill apatite (results not
shown). This was illustrated in others studies (Søvik and
Kløve, 2005; Molle et al., 2005) and could correspond to an
adsorption mechanism at low P content followed by pre-
cipitation mechanism at great P content. But the maximum
initial P concentration in our batch experiment (150 mg P/L)
was too low to clearly identify these two potential P-retention
mechanisms and to go further in the discussion.
3.3. Lab scale column experiments
Considering batch test results, only one of the igneous apatite
(Niobec) was tested in lab scale column experiments. For
increased availability of calcium the Cargill apatite was mixed
with Graymont limestone.
P-retention by the Niobec apatite was poor and the column
seemed to become saturated after 15 days (Fig. 2), confirming
the relatively poor efficiency of this type of material. During
the first 15 days the retention by Cargill and Cargill/Graymont
mixture was comparable and close to 100%. Then a slight
decrease appears for Cargill’s. The removal of the associated
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0
100
200
300
400
500
600
0 100 200 300 400 500 600 700 800 900
Padded (mgP cumulated)
P r
emo
ved
(m
gP
cu
mu
late
d)
NiobecCargillGraymontCargill/Graymont
100% retention
50% retention
Fig. 2 – P-removal as a function of P added (lab scale experiment).
Table 4 – Influent and effluent characteristics of field scale column
Sampling point pH Cond (mS/cm) COD (mg/L) Total P (mg P/L)
Inlet 7.170.3 241768 32711 7.672.3
Outlet 7.870.4 286738 2877 1.971.1
WAT E R R E S E A R C H 40 (2006) 2965– 2971 2969
gangue of the Cargill apatite may have reduced the amount of
calcium and hydroxide availability of the sample thus
reducing its nucleation performance. In column tests using
untreated natural apatites, Molle et al. (2005) showed a
significant dissolution of calcium carbonate (5 mg/L Ca)
leading to a pH increase from 7.0 to 8.0.
Graymont limestone showed a relatively stable retention
over time that remained near 50%. Effluent analysis at the
outlet of each column showed for Cargill’s a significant
consumption of Ca2+ over time and a decrease in pH
(Table 4) which suggested HAP formation and crystallization.
Results showed that Graymont limestone favoured P
precipitation as it represented a source of Ca2+ and OH�.
The P retention curve for the Cargill/Graymont mixture
appeared to be the addition of the curves for the two distinct
materials, avoiding the initial poor removal observed with
Graymont’s alone. This suggested that Cargill’s probably
provided a better seed precipitant than Graymont’s. At the
outlet of the Cargill/Graymont mixture, the pH and Ca
concentration were higher than in Cargill’s and appeared to
favour P-retention (which equals about 200 g of P retained per
m3 of column after 39 days), but they were probably not high
enough to obtain more than 60% P-retention.
In case of P levels of about 15–20 mg/L, the minimum inlet
Ca level recommended for Ca–P precipitation, according to
Jang and Kang (2002), should be 40–60 mg/L. For the field scale
column test, it was chosen to use a single column of a
limestone/apatite mixture as it represented the most promis-
ing media tested. The Cargill/Graymont mixture seemed to be
the best compromise to increase the pH, dissolve some Ca
and favour HAP precipitation.
3.4. Field scale column experiments
The column was installed downstream of a constructed
wetland of a fresh water fish farm wastewater treatment
plant. Despite the variable composition of the influent
(Table 4), the column worked with a total P retention
efficiency of 60% without showing signs of either clogging or
salting out (Fig. 3).
During the field scale test, there was a conflicting effect of
pH. On one hand a higher pH at the column inlet favore Ca
dissolution, but on the other hand it led to a reduction of HAP
formation by reducing the available OH� in solution. Having a
too great pH variability at the inlet could become a problem to
ensure a long term P retention, the best pH being around
neutrality for HAP.
The field scale column efficiency was enough to reduce
P-level to reach 2 mg P/L but the long-term stability of the
process remains to be established. The next step would be to
test mesocosm columns under a prolonged period (e.g. 1 year)
under varying influent and operational conditions such as Ca
availability, retention time and pH.
4. Conclusion
Phosphorus affinity was found to be higher with Cargill
sedimentary apatite as substrate, compared to igneous
apatites in batch experiments. Sedimentary apatites are
believed to favour crystallization of HAP due to intrinsic
characteristics, notably their internal porosity. The presence
of secondary minerals associated to the gangue would be
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Inlet ≈ 15.5 mg P/d
Retention ≈ 9.5 mg P/d
0
200
400
600
800
1000
1200
0 10 20 30 40 50 60 70
Elapsed time (d)
Rem
ove
d P
(m
gP
cu
mu
late
d)
Inlet cumulated PRetained cumulated P
Fig. 3 – P-retention efficiency during the field scale experiment.
WAT E R R E S E A R C H 4 0 ( 2 0 0 6 ) 2 9 6 5 – 2 9 7 12970
beneficial by contributing to a source of Ca, which is essential
for Ca–P precipitation. Relatively low P-retention capacities
were obtained, probably because the available Ca from
dissolution rapidly became depleted. Testing pure Cargill
material including the gangue would be of interest.
With igneous apatites, neither HAP crystallization nor Ca–P
precipitation were believed to have occurred considering the
higher affinity of P with other metals like Fe, Mg, Al as pointed
out in other studies. Crystallography tests could confirm this
interpretation.
Best pH conditions are conflicting as a low pH would favour
Ca dissolution and a high pH would favour HAP crystal-
lization. In small scale wastewater treatment plants, pH
fluctuations may be important thus reducing P-retention
availability. A source of calcium and hydroxide should be
provided to avoid such conflicting operation conditions.
Sedimentary and igneous North American apatites showed
low and poor retention capacity for P-removal, respectively.
Nevertheless, the potential of apatites for crystallization and
P-recycling merits attention. Further studies should be
conducted with regards to the critical conditions associated
to pH, calcium, and orthophosphates concentrations.
Acknowledgements
The authors thank Denis Bouchard for technical support and
Dwight Houweling for reviewing an earlier draft of the
manuscript. This research was financed by the Natural
Sciences and Engineering Research Council of Canada.
R E F E R E N C E S
Comeau, Y., Brisson, J., Reville, J.-P., Forget, C., Drizo, A., 2001.
Phosphorus removal from trout farm effluents by constructed
wetlands. Water Sci. Technol. 44 (11–12), 55–60.
De-Bashan, L.E., Bashan, Y., 2004. Recent advances in removingphosphorus from wastewater and its future use as fertilizer(1997–2003). Water Res. 38 (19), 4222–4246.
Jang, H., Kang, S.H., 2002. Phosphorus removal using cow bone inhydroxyapatite crystallization. Water Res. 36 (5), 1324–1330.
Joko, I., 1984. Phosphorus removal from wastewater by thecrystallization method. Water Sci. Technol. 17, 121–132.
Karapinar, N., Hoffmann, E., Hahn, H.H., 2004. Magnetite seededprecipitation of phosphate. Water Res. 38 (13), 3059–3066.
Kim, E.-H., Lee, D.-W., Hwang, H.-K., Yim, S., 2006. Recovery ofphosphates from wastewater using converter slag: Kineticsanalysis of a completely mixed phosphorus crystallizationprocess. Chemosphere 63 (2), 192–201.
Korkusuz, E.A., Beklioglu, M., Demirer, G.N., 2005. Comparison ofthe treatment performances of blast furnace slag-based andgravel-based vertical flow wetlands operated identically fordomestic wastewater treatment in Turkey. Ecol. Eng. 24 (3),185–198.
Kostura, B., Kulveitova, H., Lesko, J., 2005. Blast furnace slags assorbents of phosphate from water solutions. Water Res. 39 (9),1795–1802.
Molle, P., Lienard, A., Grasmick, A., Iwema, A., 2003. Phosphorusretention in subsurface constructed wetlands: Investigationsfocused on calcareous materials and their chemical reactions.Water Sci. Technol. 48 (5), 75–83.
Molle, P., Lienard, A., Grasmick, A., Iwema, A., Kabbabi, A., 2005.Apatite as an interesting seed to remove phosphorus fromwastewater in constructed wetlands. Water Sci. Technol. 51(9), 193–203.
Naylor, S., Brisson, J., Labelle, M.-A., Drizo, A., Comeau, Y., 2003.Treatment of freshwater fish farm effluent using constructedwetlands: The role of plants and substrate. Water Sci. Technol.48 (5), 215–222.
Nriagu, J.O., Moore, P.B., 1984. Phosphate Minerals. Springer-Verlag, Heidelberg.
Shilton, A., Pratt, S., Drizo, A., Mahmood, B., Banker, S., Billings, L.,Glenny, S., Luo, D., 2005. ‘Active’ filters for upgrading phos-phorus removal from pond systems. Water Sci. Technol. 51(12), 111–116.
Slansky, M., 1986. Geology of Sedimentary Phosphates. NorthOxford Academic Publishers Ltd.
Song, Y., Weidler, P.G., Berg, U., Nuesch, R., Donnert, D., 2006.Calcite-seeded crystallization of calcium phosphate for phos-phorus recovery. Chemosphere 63 (2), 236–243.
ARTICLE IN PRESS
WAT E R R E S E A R C H 40 (2006) 2965– 2971 2971
Sposito, G., 1989. The Chemistry of Soils. Oxford University Press,
New-York.
Standard Methods (Standard Methods for the Examination of
Water and Wastewater), 1998. 20th ed., American Public
Health Association/American Water Works Association/Water
Environment Federation, Washington, DC, USA.
Søvik, A.K., Kløve, B., 2005. Phosphorus retention processes in
shell sand filter systems treating municipal wastewater. Ecol.
Eng. 25 (2), 168–182.
Stumm, W., Morgan, J.J., 1996. Aquatic Chemistry—ChemicalEquilibria and Rates in Natural Waters, third ed. Wiley-Interscience Publishers, Iowa.
Zapata, F., Roy, N.R., 2004. Use of phosphate rocks for sustainableagriculture, Report ISBN 92-5-105030-9, Food and AgricultureOrganization of the United Nations-FAO Land and WaterDevelopment Division and International Atomic EnergyAgency, Rome, Italy.
Zoltek Jr., J., 1974. Phosphorus removal by orthophosphatenucleation. J. Water Pollut. Control Fed. 46, 2498–2520.