Journal of Environmental Science and Engineering B 7 (2018) 331-336
doi:10.17265/2162-5263/2018.09.002
D
DAVID
PUBLISHING
Thermodynamic Principles of Dittmarite Precipitation
Asmare Atalay and Brodie Whitehead
Agricultural Research Station, Virginia State University, Petersburg, Virginia 23806, USA
Abstract: Dittmarite is a naturally occurring mineral which is also produced by municipal wastewater treatment processes. It
contains ammonium:magnesium:phosphate in molar ratios of 1:1.25:1, respectively. Dittmarite (MgNH4PO4·H2O) has a very stable
crystalline structure, its solubility constant (Kso) is a product of the activity coefficient (ɣ) and the activity of the individual species
that make up the compound. The conditional solubility product, PS = CT, Mg CT,NH4 CT,PO4 = Kso/αMg αNH4 αPO4 ɣMg ɣNH4 ɣPO4.
A theoretical plot of -log Ps vs. pH gives a pH of 10.7 for maximum dittmarite precipitation, albeit precipitation may begin at lower
pH values. The pKso for dittmarite at 25 °C is determined to be 13.359 from the final equilibrium pH values taking all relevant
magnesium, phosphate and ammonium species into account. The geochemical speciation model, MINTEQA2 was used to verify the
optimum conditions for the precipitation of dittmarite. Such theoretical predictions allow the control of phosphorus and nitrogen
discharges from animal and municipal wastewaters and serve as key factors in preventing surface water eutrophication and
groundwater pollution.
Key words: Dittmarite, precipitation, thermodynamics, MINTEQA2, wastewater.
1. Introduction
Use of phosphorus and nitrogen enriched feeds in
CAFO (Confined Animal Feeding Operations), land
application of animal manure and chemical fertilizer
on agricultural land, and municipal as well as
industrial wastewaters, all contribute a great deal to
the eutrophication of surface waters. Application of
manure slurries to crop land beyond allowable limits
results in high levels of phosphorus and nitrogen in
runoff that negatively impact aquatic animals.
Municipal wastewater treatment plants are setup to
remove these nutrients from domestic and industrial
wastewater through a network of treatment processes.
Thus, controlling the discharge of phosphorus and
nitrogen in wastewater is a key factor in preventing
eutrophication. Authors’ previous research [1] has
developed and enhanced a chemical precipitation
method that removes over 90% of phosphorus and
nearly 20% of nitrogen from both synthetic and
municipal wastewaters as dittmarite. While various
Corresponding author: Asmare Atalay, Ph.D., research
professor, main research fields: soil chemistry and
environmental science. VSU-ARS Publication No. 533.
phosphate forms are present in nature, the most
common is calcium phosphate which is stable at very
high pH. Among other phosphates, one with practical
relevance is dittmarite (MgNH4PO4). Dittmarite
appears naturally in bat guano and as a nuisance
precipitate in conduits at municipal wastewater
treatment plants. Most recently, dittmarite and its
hexahydrate form, struvite, have found relevance as
value-added products in agriculture. Dittmarite has
been postulated to form as intermediate reaction
product before it transforms into the more stable
hexahydrate, struvite [2]. Many interesting data are
available concerning factors involved in precipitation
of dittmarite/struvite in phosphorus recovery
processes in wastewater treatment systems as well as
their occurrence in geologic deposits. Precipitation of
dittmarite/struvite has been studied with regard to
solution composition and pH, and attention has been
given to the kinetics and mechanism of
dittmarite/struvite precipitation in the condition of
constant
supersaturation
[3];
with
special
consideration to the possible difference in the
solubility and dissolution kinetics of different
dittmarite/struvite morphologies [4].
332
Thermodynamic Principles of Dittmarite Precipitation
Precipitation of P in the form calcium phosphate is
not a new idea, it has been known since 1939 [5]. In
fact, such a precipitate had been considered a nuisance
by wastewater engineers since it clogged transfer lines
preventing normal flow of wastewater [6]. However,
precipitation of P as dittmarite, a potentially value
added product, is not widely known. Dittmarite is a
monohydrated magnesium ammonium phosphate
crystal which is drier and finer in particle size than the
amorphous phosphate, and easily managed for
transport and land application purposes. Understanding
dittmarite formation in a solution that contains other
organic and inorganic constituents is a challenge.
However the process can be simplified by initially
dissolving the inorganic and organic species with
mineral acid. Authors’ preliminary work has indicated
that use of a chelating substance was beneficial since
it trapped excess positive ions and brought them into
solution. Additional magnesium source was needed to
overwhelm the system and occupy all active sites. In
the process freed magnesium was able to combine
with free ammonium and phosphate ions to form
dittmarite. The choice of which form of magnesium to
use usually depends on the characteristic of the waste
to be treated. Authors used a magnesium source in the
trial studies that enhanced dittmarite formation.
However, Miles and Ellis [7] encountered difficulty in
precipitating phosphate-bearing minerals from
wastewater when they used a 50% magnesium
hydroxide slurry and a phosphate fertilizer to reduce
ammonia content. Because of the low solubility of
magnesium oxide, the reaction time was longer and
residual magnesium oxide existed after the reaction.
However, magnesium chloride could be a good
precipitant for dittmarite formation since the pH
would be better controlled. It might be slightly acidic
compared to the other forms of magnesium, in which
case precautions might be needed to control the pH.
Authors’ preliminary laboratory studies have indicated
that in order to obtain optimum results for dittmarite
precipitation, the magnesium chloride or magnesium
hydroxide molar ratio to phosphate ratio should be
specific. Kofina and Koutsoukos [8] reported that total
suspended solids above 1,000 mg/L interfered with
the phosphate precipitation process. One way to
overcome it, based on our preliminary studies, would
be to lower the pH and allow the acidification process
to dissolve the solids.
2. Materials and Methods
2.1 Equilibrium Speciation Modeling
The geochemical speciation model, MINTEQA2 [9]
allows full speciation of the dittmarite system to
compute the concentration of each species: H2PO4-,
H3PO4, OH-, NH3 (aq), MgOH+, MgOH-, MgPO4-,
MgH2PO4+, MgHPO4 (aq), HPO42-, Mg2+, PO43- and
NH4+. The equilibrium equations given in Table 1
describe the possible reactions and species that form
during dittmarite formation.
Table 1 Equilibrium constants for the various reactions and potential species used in the MINTEQA2 speciation model to
determine dittmarite precipitation [10].
Equilibrium
H2PO4- + H+ ֖ H3PO4
HPO42- + H+ ֖ H2PO4PO43- + H+ ֖ HPO42HPO42- + Na+ ֖ NaHPO4H2PO4- + Mg2+ ֖ MgH2PO4+
HPO42- + Mg2+ ֖ MgHPO4
PO43- + Mg2+ ֖ MgPO4SO42- + H+ ֖ HSO4SO42- + Mg2+ ֖ MgSO4
NH4+ ֖ NH3 (aq) + H+
H2O ֖ H+ + OH-
LogK at 37 °C
2.21
7.18
12.18
0.85
1.207
2.815
4.92
2.03
1.97
9.25
-13.62
LogK at 25 °C
2.148
7.198
12.375
0.85
1.207
2.428
4.92
1.99
2.23
9.24
-13.997
Thermodynamic Principles of Dittmarite Precipitation
Dittmarite and struvite have very low solubility in
water (approximately 160 mg/L at pH 7 and 25 °C)
with a solubility product (Ksp) between 10-10 and
10-13.3 [4, 6, 11-13]. For dittmarite, MgNH4PO4·H2O,
the equilibrium solubility constant can be expressed as
follows [14]:
Kso = {Mg+2} {NH4+} {PO43-}
= ɣMg+2[Mg+2] ɣNH4+[NH4+] ɣPO43-[PO43-]
= ɣMg2+CT,Mg αMg2+ • ɣNH4+CT,NH4+αNH4+ •
ɣPO43-CT,PO43-αPO43The conditional solubility product, PS, becomes:
PS = CT, Mg CT, NH4 CT,
PO4 = ܵܭO / αMg αNH4 αPO4 ɣMg ɣNH4 ɣPO4
Then, Ps is a function of pH and their relationship
can be plotted as shown in Fig. 1. This minimum
value will occur when the product (ɣMg2+) × (ɣNH4+)
× (ɣPO43-) is a maximum. The conditional solubility
2.3 Dittmarite Precipitation and X-Ray Diffraction
Dittmarite samples from the pilot study [1] were
dried in oven at 105 °C and prepared for further
analysis. The resulting white crystalline powder (Fig.
2) was analyzed for phase identification using a
Rigaku micro XRD (X-Ray Diffraction) system using
a Cu Kα rotating anode, operating at 40 kV/20 mA
and an imaging plate for detection. A small amount of
8
1
Mg2+
6
-1
4
-3
2
NH4+
-5
0
-2
1
3
5
7
9
11
13
-4
-7
-9
-6
MgNH4PO4.H2O
-11
-8
-10
Log (ionization fraction)
2.2 Theoretical Development
product of magnesium ammonium phosphate,
dittmarite, illustrates a situation where more than one
of the dissolving species is affected by solution pH.
These species are the ammonium ion (HN4+) and the
phosphate ion (PO43-). Because an increase in pH will
decrease the ammonium ion concentration and
increase the phosphate ion concentration, it follows
that there should be a pH value where the solubility of
MgNH4PO4 (s) is a minimum (Fig. 1).
The minimum value for Ps occurs when the product
αMgαNH4αPO4 is a maximum. From the above figure,
the minimum solubility (Ps) occurs when pH = 10.7,
which indicates the maximum precipitation of
ammonium as dittmarite [15]. Beyond pH = 10.7,
various species of calcium phosphate such as
hydroxylapatite and amorphous phosphate forms of
aluminum and iron phosphates also precipitate.
Log (Ps)
The applicable mass balance, acid-base and
complex formation equilibria equations for dittmarite
(struvite) chemistry are given by Buchanan [6].
MINTEQA2 modeling was used in conjunction with
laboratory experiments to predict the potential for
dittmarite precipitation as a function of pH and
magnesium, ammonium and phosphate molar ratio.
Each model prediction was run at a temperature of
25 °C and negligible ionic strength. If the ionic
strength is fixed, it becomes independent of the
solution chemistry [9]. This means, there could be
inert ions present in large enough concentrations such
that their impact on ionic strength might be important.
To satisfy this curiosity, a separate run was done that
included all other major ions in the solution. However,
no major difference was seen in the results as
compared to the limited input. The runs were
performed over a series of pH values to determine
how the concentrations of each constituent change
with pH. The pilot-scale study conducted for use in
the MINTEQA2 speciation model is described in a
previous study [1].
333
-13
PO43-
-15
-12
pH
Fig. 1 Theoretical relationship between the conditional
solubility product, PS and pH indicating maximum
precipitation of dittmarite at pH 10.7
334
Thermodynamic Principles of Dittmarite Precipitation
the sample was placed inside a 0.1 mm S-glass
capillary, positioned at the center of four-circle
goniometer and rotated 360° continuously in a plane
parallel to the beam. The sample was irradiated for 15
minutes, and system software was used to integrate
each image to create a 2θ versus intensity plot. The
pattern was checked for matches in our ICDD
(International Center for Diffraction Data) database of
diffraction patterns. Then a small amount of the
powder was placed on a carbon adhesive tab to verify
the
elemental
composition
using
EDS
(Energy-Dispersive X-Ray Spectrometry). The sample
pattern matched the ICDD reference for dittmarite
with minor mixtures of newberyite and mascagnite.
Dittmarite was obtained from both wastewater and
via synthesis using laboratory chemicals. It can be
characterized by its physical and chemical properties.
XRD of the material synthesized in the laboratory was
confirmed to be dittmarite (see Fig. 3). The presence
of dittmarite is indicated by the location of intensity
peaks. Vertical lines on the graph represent where the
Fig. 3
dittmarite peaks should occur. Some of the more
definite non-dittmarite peaks show the presence of
other minerals, newberyite and mascagnite. This
indicates that P precipitates other than dittmarite are
forming in the reaction process. The formed
precipitate is enhanced with P not only from dittmarite
but also from newberyite, mascagnite and other
unidentified P-bearing minerals shown in the XRD
diagram.
A
B
Fig. 2
Dittmarite precipitated from (A) synthetic
chemicals and (B) wastewater.
XRD results of dittmarite showing the specific peak characteristics.
Thermodynamic Principles of Dittmarite Precipitation
3. Results and Discussion
Since magnesium is considered to be the main
ingredient needed for the precipitation of phosphorus
and nitrogen from wastewater, the following are basic
reactions that occur when dittmarite is precipitated in
the presence of various sources of magnesium,
ammonium and phosphate:
(NH4)3PO4 + MgCl2 + H2O MgNH4PO4·H2O (1)
(NH4)2HPO4 MgO + H2O MgNH4PO4·H2O (2)
(NH4)3PO4 + MgCO3 + H2O MgNH4PO4·H2O (3)
(NH4)3PO4 + Mg(OH)2 + H2O MgNH4PO4·H2O (4)
(NH4)3PO4 + MgSO4 + H2O MgNH4PO4·H2O (5)
Other forms of P-bearing minerals have been
known to cause major problems in wastewater. A
historical problem in wastewater treatment plants is
the precipitation of P as calcium phosphate in the
presence of high levels of dissolved calcium followed
by the formation of dittmarite as described by the
following reactions:
3Ca2+ + 2PO43- Ca3(PO4)2
(6)
+
+2
CaPO4 + Mg + NH4 + H2O MgNH4PO4·H2O (7)
However, such problems could be avoided by
slowly adding a strong mineral acid solution to the
wastewater. This would partially digest the organic
matter and dissolve minerals to release all bound
metals into solution. Alternatively one can use EDTA,
which has the advantage of binding calcium ions, may
be added to release the phosphate ions into solution as
described by the Eq. (8):
Ca3(PO4)2 + EDTA EDTA-Ca + PO43(note the free phosphate in solution) (8)
The free phosphate ion would now be available to
combine with ammonium and magnesium ions in
solution to form dittmarite. In the wastewater
treatment scenario, once the wastewater reaches the
treatment plant, the pH would be raised and a high
dose of magnesium added to force the reaction
towards dittmarite formation. It would be prudent to
add more magnesium to enhance the precipitation of
dittmarite. The stability constant for EDTA-Mg
335
complex is 10+8.7 [16-18] which means magnesium
will be bound and unable to precipitate P as dittmarite.
Zhang, et al. have noticed that when the magnesium
concentration was increased by more than twice that
of EDTA, a sharp reduction in P was observed due to
the formation of P-bearing minerals [2]. It is also
interesting to note that in the process of dittmarite
formation, calcium is usually considered an impurity
because the calcium ion can block the active site on
the crystal lattice. Increase in calcium concentration is
expected to inhibit dittmarite growth and lead to the
formation of an amorphous substance rather than the
desired crystalline dittmarite. The same principle
would apply during the process of dittmarite
precipitation from animal and municipal wastewaters.
Since authors’ overall goal is to recover P from
wastewater, the result we obtained in the preliminary
trial [1] is a favorable one. The following chemical
analyses provide values that are pertinent for
evaluating dittmarite as a fertilizer source: Magnesium,
15.65% as Mg or 25.95% as MgO; Phosphorus, 19.94%
P or 45.69% P2O5; Nitrogen 9.02% N or 16.76%
(NH4)2O. These values are about twice the amount
found in ammonium magnesium phosphate
hexahydrate; and they provide over four times the
phosphorus and about two times the nitrogen in a
regular 10-10-10 fertilizer. Therefore precipitating P
as dittmarite has more environmental and agricultural
advantages over other forms of P-bearing minerals. In
the laboratory study, dittmarite was recovered by
gravity settling followed by centrifugation. The result
was a crystalline powder similar to very fine sand (Fig.
2a). We believe the texture can be enhanced by adding
fine sand of similar particle size, a process called
nucleation that can be applied at the final recovery
stage of wastewater treatment. This will permit ease of
handling and transportation of dittmarite.
4. Conclusion
Dittmarite is the monohydrated version of struvite,
which is considered a nuisance in wastewater
Thermodynamic Principles of Dittmarite Precipitation
336
treatment processes. Dittmarite is a naturally
occurring mineral which is also found in bat guano.
The use of MINTEQA2 speciation model along with
theoretical chemical equilibria was able to predict the
optimum pH under which dittmarite is precipitated
from wastewater. X-Ray diffraction and chemical
analysis have revealed that dittmarite in its purest
form is a white crystalline mineral with very low
solubility in water (about 160 mg/L) at 25 °C. The
chemical composition of dittmarite reveals that it
could be commercialized as an alternative fertilizer
supplement.
[8]
[9]
[10]
[11]
[12]
References
[1]
[2]
[3]
[4]
[5]
[6]
[7]
Atalay, A., Whitehead, B. L., Oyewole, O., and Brown, Z.
2017. “Removal of Nitrogen and Phosphorus from animal
and Municipal Wastewaters as Dittmarite.” J. Environ.
Sci. and Engineering B 6: 295-300.
Zhang, T., Bowers, K. E., Harrison, J. H., and Chen, S.
2010. “Releasing Phosphorus from Calcium for Struvite
Fertilizer production from Anaerobically Digested
Dairy Effluent.” Water Environment Research 82 (1):
34-42.
Sarkar,
A.
K.
1991.
“Hydration/Dehydration
Characteristics of Struvite and Dittmarite Pertaining to
Magnesium Ammonium Phosphate Cement System.” J.
Material Sci. 26: 2514-8.
Bhuiyan, M. I. H., Marvinic, D. S., and Beckie, R. D.
2007. “A Solubility and Thermodynamic Study of
Struvite.” Environ. Tech. 28 (9): 1015-26.
Rawn, A. M., Banta, A. P., and Pomeroy, R. 1939.
“Multiple Stage Sewage Digestion.” Trans. Am. Soc.
Civil Eng. 105: 93-132.
Buchanan, J. R., Mote, C. R., and Robinson, R. B. 1994.
“Thermodynamics of Dtruvite Formation.” Transactions
of the ASAE 37 (2): 617-21.
Miles, A., and Ellis, T. G. 1999. “Struvite Precipitation
Potential for Nutrient Recovery from Anaerobically
[13]
[14]
[15]
[16]
[17]
[18]
[19]
Treated Waste.” In Proceedings of the ASCE 1999
National Conference on Environmental Engineering,
June 7-10, 1999. Chicago, Illinois, 161-6.
Kofina, A. N., and koutsoukos, P. G. 2005. “Spontaneous
Precipitation of Struvite from Synthetic Wastewater
Solution.” Crystal Grouth and Design 5: 489-96.
USEPA. 1991. MINTEQA@, U.S. Environmental
Protection
Agency.
www.epa.gov/ceampubl/mmedia/minteq 301/11/2010.
Smith, R. M., and Martell, A. E. 1989. Critical Stability
Constants. Vol. 6, Plenum Press.
Burns, J. R., and Finlayson, B. 1982. “Solubility Product
of Magnesium Ammonium Phosphate Hexahydrate at
Various Temperatures.” J. Urology 128: 426-8.
Taylor, A. W., Frazier, A. W., and Gurney, E. L. 1963.
“Solubility Products of Magnesium Ammonium and
Magnesium Potassium Phosphates.” Transactions
Faraday Society 59: 1580-4.
Web, K. M., and Ho, G. E. 1992. “Struvite
(MgNH4PO4.6H2O) Solubility and Its Application to
Piggery Effluent Problem.” Water Science Technology 26
(9-11): 2229- 32.
Stumm, W., and Morgan, J. J. 1981. Aquatic Chemistry:
An Introduction Emphasizing Chemical Equilibria in
natural Waters. New York: John Wiley & Sons.
Babic-Ivancic, V., Kontrec, J., Kralj, D., and Brecevic, L.
2002. “Precipitation Diagrams of Struvite and Dissolution
Kinetics of Different Struvite Morphologies.” Croatica
Chemica Acta 75 (1): 89-106.
Sawyer, C., McCarty, P., and Parkin, G. 1994. Chemistry
for Environmental Engineering (4th ed.). New York:
McGraw Hill.
Snoyink, V. L., and Jenkins, D. 1980. Water Chemistry.
New York: John Wiley & Sons.
Benefield, L. D., Judkins, J. F., and Weand, B. L. 1982.
Process Chemistry for Water and Watewater Treatment.
Englewood Cliff, NJ: Prentice-Hall Inc..
LeCorree, K. S., Valsami-Jones, E., Hobbs, P., and
Parson, S. A. 2005. “Impact of Calcium on Struvite
Crystal Size, Shape and Purity.” J. Cryst. Gropwth 283:
514-22.