ArticlePDF Available

Nutrient Recovery from Piggy Wastewater by Enhancing Struvite Crystallization Process

Authors:

Abstract and Figures

The problem of nutrient pollution from piggy wastewater has been considered as a serious problem. Enhancing struvite crystallization process is an efficient technology for ammonium recovery. In our study, the optimal reaction conditions of pH, Mg2+: NH4+: PO43- molar ratio, mixing reaction time, and different kinds of chemicals combinations for ammonium recovery were examined. The conclusions were drawn as following. The optimal pH for ammonium recovery was 9.0. The optimal Mg2+: NH4+: PO43- molar ratio for ammonium recovery was 1.3:1:1. The optimal mixing reaction time for ammonium recovery was 10 min. The chemicals combination of MgCl2 + Na2HPO4 was the most efficient for ammonium recovery. Scanning electron microscopy analysis indicated the unshaped struvite crystal was coarse and its size was irregular.
Content may be subject to copyright.
Nutrient recovery from piggy wastewater by enhancing struvite
crystallization process
Tao Zhang
a
, Ci Fang, Ping Li, Rongfeng Jiang
b
Key Laboratory of Plant-Soil Interactions of Ministry of Education, College of Resources and
Environmental Sciences, China Agricultural University, Beijing 100193, PR China
a
taozhang@cau.edu.cn,
b
rfjiang@cau.edu.cn
Keywords: nutrient; struvite crystallization; enhancing; piggy wastewater.
Abstract. The problem of nutrient pollution from piggy wastewater has been considered as a serious
problem. Enhancing struvite crystallization process is an efficient technology for ammonium
recovery. In our study, the optimal reaction conditions of pH, Mg
2+
: NH
4+
: PO
43-
molar ratio, mixing
reaction time, and different kinds of chemicals combinations for ammonium recovery were examined.
The conclusions were drawn as following. The optimal pH for ammonium recovery was 9.0. The
optimal Mg
2+
: NH
4+
: PO
43-
molar ratio for ammonium recovery was 1.3:1:1. The optimal mixing
reaction time for ammonium recovery was 10 min. The chemicals combination of MgCl
2
+ Na
2
HPO
4
was the most efficient for ammonium recovery. Scanning electron microscopy analysis indicated the
unshaped struvite crystal was coarse and its size was irregular.
Introduction
Nowadays, ammonium, a kind of nutrient for plant growth, contained in piggy wastewater has
become one of the main sources of pollution to the water environment. Therefore, the treatment of
ammonium from piggy wastewater is important for water environment. The traditional treatment
processes of ammonium removal are biological process and physico-chemical process. Biological
process is economical for ammonium removal, but it is not effective for pretreatment of ammonium
removal from wastewater. Physico-chemical processes can be applied in pretreatment of ammonium,
such as air stripping, ionic exchange, and struvite (MgNH
4
PO
4
·6H
2
O) precipitation
[1, 2]
.
Struvite crystallization of ammonium by forming magnesium ammonium phosphate has been
studied widely
[3, 4]
. The ammonium recovery from wastewater by enhancing struvite crystallization
process has been regard as a useful technology. Struvite is a white crystalline substance consisting of
magnesium, ammonium and phosphorus in equal molar concentrations. The basic chemical reaction
to form Struvite has been expressed in Eq. (1)
[5]
.
2 3
4 4 2 4 4 2
Mg NH PO 6H O MgNH PO 6H O
+ +
+ + +
(1)
In our study, the objective of this study was to investigate optimal pH, optimal molar ratio, optimal
mixing reaction time, and different kinds of chemicals combinations in laboratory scale experiments
for piggy wastewater.
Materials and Methods
Materials
The raw wastewater used in the experiments was synthetical piggy wastewater. Table 1 shows some
main parameters of the wastewater sample.
Methods
Experiments were performed as follows. Firstly, magnesium salt and phosphate were added to raw
wastewater at experimental condition (1.0:1:1-1.5:1:1). Secondly, the reaction solution pH was
adjusted at experimental condition (7.5-10.5). Thirdly, the reaction solution was agitated by magnetic
Applied Mechanics and Materials Vols. 522-524 (2014) pp 579-583
© (2014) Trans Tech Publications, Switzerland
doi:10.4028/www.scientific.net/AMM.522-524.579
All rights reserved. No part of contents of this paper may be reproduced or transmitted in any form or by any means without the written permission of TTP,
www.ttp.net. (ID: 70.176.193.228-03/02/14,04:18:00)
stirrers at experimental mixing reaction time (5-60 min) and then settled for 10 min. Finally, the
reaction solution was filtered with 0.45µm membrane filter and the supernatant was collected to
measure NH
4+
.
Analysis
The experiments choose ammonium recovery ratio as the indicator for selecting optimal reaction
conditions. The concentration of NH
4+
was measured according to Standard Methods. The collected
precipitate was washed with deionized water for 3 times, and dried in an oven at 40
for 48 hours,
and then analyzed by scanning electron microscopy (SEM, S-3400N, Hitachi, Japan).
Table 1 Characteristics of wastewater
Parameter Unit Concentrations
COD mg/L 600±30
NH
4
+
-N mg/L 200±10
PO
4
3
-
-P mg/L 30±3
Result and Discussion
Optimum pH
Solution pH is the most important factor for enhancing stuvite crystallization process. The experiment
was to study optimal pH of ammonium recovery from piggy wastewater by enhancing struvite
crystallization process. This experiment was tested by adding MgCl
2
and Na
2
HPO
4
into the samples,
and the molar ratio of Mg
2+
: NH
4+
: PO
43-
was 1.3:1:1. The pH range was 7.5-10.5. The mixing
reaction time was 10 min.
Fig.1 showed that the optimal ammonium recovery ratio for piggy wastewater was at pH 9.0. When
pH is lower than the optimal point, hydrogen ions in reaction solution inhibit struvite crystallization.
When pH is higher than the optimal point, Mg
3
(PO
4
)
2
is formed instead of struvite. In the literature,
there are some papers dealing with the optimal pH for ammonium recovery. Stratful et al.
[7]
reported
that ammonium recovery ratio was high than 97% at pH 9, 9.5 and 10. Zhang et al.
[8]
reported the
optimum pH for ammonium recovery from landfill leachate was 9.5.
Optimum Molar Ratio
Mg
2+
: NH
4+
: PO
43-
molar ratio is an important factor for enhancing stuvite crystallization process.
Overdosing either Mg
2+
or PO
43-
can lower the remaining ammonium concentration. In fact, although
overdosing PO
43-
could increase ammonium concentration, there are several problems for overdosing
PO
43-
. First of all, overdosing PO
43-
did not provide significant increasing in ammonium recovery. In
addition, overdosing PO
43-
will lead to the high concentration of PO
43-
in the effluent. As a result, the
experiment was to study the optimal Mg
2+
: NH
4+
: PO
43-
molar ratio of overdosing Mg
2+
for struvite
precipitation in piggy wastewater. This experiment was tested by adding MgCl
2
and Na
2
HPO
4
into the
samples. The pH was 9.0. The mixing reaction time was 10 min.
Fig.2 showed, the optimal Mg
2+
: NH
4+
: PO
43-
molar ratio for ammonium recovery from piggy
wastewater was 1.3:1:1. With an increase in Mg
2+
: NH
4+
: PO
43-
molar ratio from 1.0:1:1 to 1.3:1:1,
the recovery ratio of ammonium increased rapidly. With an increase in Mg
2+
: NH
4+
: PO
43-
molar ratio
from 1.3:1:1 to 1.5:1:1, the recovery ratio of ammonium did not increase significantly. Li et al.
[9]
were deal with NH
4+
recovery from landfill leachate by chemical precipitation and reported
overdosing 10% Mg
2+
could further increase ammonium efficiency.
580 Environmental Protection and Sustainable Development
Optimum Reaction Time
The optimal reaction time for struvite formation was investigated due to it is an important factor for
engineering application. This experiment was tested by adding MgCl
2
and Na
2
HPO
4
into the samples.
The molar ratio of Mg
2+
: NH
4+
: PO
43-
was 1.3: 1: 1. The pH range was 9.0.
Fig.3 showed, the optimal mixing reaction time for ammonium recovery from piggy wastewater
was 10 min. When the mixing reaction time was increasing from 5 min to 10 min, the ammonium
recovery ratio was increased significantly. When the mixing reaction time was increasing from 10
min to 60 min, the ammonium recovery ratio was increased slightly. Celen and Turker
[10]
have do
some research for struvite reaction time in anaerobic digester effluents and indicated the 40 min was
safe time for struvite mixing and constant rest.
Fig 1. NH
4+
recovery ratio at different pH
Fig 2. NH
4+
recovery ratio at different Mg
2+
:
NH
4+
: PO
43-
molar ratio
Optimum Chemicals Combinations
The factor of different chemicals combinations of magnesium and phosphate source is important for
enhancing struvite crystallization. The combinations of chemicals, MgCl
2
+ Na
2
HPO
4
, Mg(OH)
2
+
H
3
PO
4
, MgCO
3
+ H
3
PO
4
,
were employed for the experiments and carried out with Mg
2+
: NH
4+
: PO
43-
molar ratio of 1.3:1:1, pH of 9.0, and mixing reaction time of 10 min.
Fig.4 showed the relationship between chemicals combinations and ammonium recovery ratio. The
chemicals combination of MgCl
2
+ Na
2
HPO
4
was the most efficient for ammonium recovery. The
efficiency of chemicals combinations of Mg(OH)
2
+ H
3
PO
4
and MgCO
3
+ H
3
PO
4
for ammonium
recovery was lower than the chemicals combination of MgCl
2
+ Na
2
HPO
4
. But the chemicals
combination of MgCl
2
+ Na
2
HPO
4
was generated high salt concentration in the effluent. 1 mole of
ammonium recovery will lead to 2 mole of NaCl generated
[8]
. Adding the chemicals combinations of
Mg(OH)
2
+ H
3
PO
4
and MgCO
3
+ H
3
PO
4
as sources of magnesium salt and phosphate could
significantly minimize the salt concentration.
Surface characterization
The struvite precipitates was collected at the reaction condition of Mg
2+
: NH
4+
: PO
43-
molar ratio
1.3:1:1, pH 9.0, mixing reaction time 10 min, and the chemicals combinations of MgCl
2
and
Na
2
HPO
4.
SEM analysis (Fig.5) showed that the surface of the crystal was coarse, unshaped. The size
of struvite precipitates was irregular (20-200 um).
Applied Mechanics and Materials Vols. 522-524 581
Fig 3. NH
4+
recovery ratio at different
reaction time
Fig 4. NH
4+
recovery ratio at different
chemicals combinations
Fig 5. SEM analysis of struvite precipitates
Conclusions
As a method for ammonium recovery from piggy wastewater, the following conclusions could be
obtained for struvite precipitation.
(1) The optimal ammonium recovery ratio for piggy wastewater was at pH 9.0.
(2) The optimal Mg
2+
: NH
4+
: PO
43-
molar ratio for ammonium recovery from piggy wastewater was
1.3:1:1.
(3) The optimal mixing reaction time for ammonium recovery from piggy wastewater was 10 min.
(4) The chemicals combination of MgCl
2
+ Na
2
HPO
4
was the most efficient for ammonium
recovery.
(5) SEM analysis indicated the unshaped struvite crystal was coarse and its size was irregular.
Acknowledgements
The work was supported by a grant from the Specialized Research Fund for the Doctoral Program of
Higher Education (20120008120013), the Chinese Universities Scientific Fund of China Agricultural
University (2011JS169), and the TOTO Water Environment Fund of China Environmental Protection
Foundation. Thanks to the Analytical Instrumentation Center of Peking University.
582 Environmental Protection and Sustainable Development
References
[1] S. Uludag-Demirer, M. Othman: Bioresource Technol. Vol. 100 (2009), p.3236-3244.
[2] T. Zhang, Q. Li, L. Ding, H. Ren, K. Xu, Y. Wu, D. Sheng: J. Environ. Sci. Vol.23(6) (2011),
p.881-890.
[3] J. D. Doyle, S. A. Parsons: Water Res. Vol.36 (2002), p.3925-3940.
[4] T. Zhang, L. Ding, H. Ren, X. Xiong: Water Res. Vol.43 (20) (2009), p.5209-5215.
[5] K. S. Le Corre, E. Valsami-Jones, P. Hobbs, S. A. Parsons: Crit. Rev. Environ. Sci. Tech. Vol.39
(2009), p.433-477.
[6] I. Stratful, M. D. Scrimshaw, J. N. Lester: Water Res., Vol.35 (2001), p.4191-4199.
[7] T. Zhang, L. Ding, H. Ren: J. Hazard. Mater., Vol.166 (2009), p.911-915.
[8] X. Z. Li, Q. L. Zhao, X. D. Hao: Waste Manage., Vol.19 (1999), p.409-415.
[9] I. Celen, M. Turker: Environ. Technol., Vol.22 (2001), p.1263-1272.
Applied Mechanics and Materials Vols. 522-524 583
Article
Ideonella sp. TH17, an autotrophic hydrogen-oxidizing bacterium (HOB), was successfully enriched and isolated from activated sludge in a domestic wastewater treatment plant (WWTP). Batch experiments were conducted to identify the cell growth and ammonium (NH4⁺-N) removal, and to verify the pathways of nitrogen utilization under different conditions. At a representative NH4⁺-N concentration of 100 mg/L in domestic wastewater, it was the first time that a HOB achieved a nearly 100% ammonium removal. More than 90% of NH4⁺-N was assimilated to biomass nitrogen by strain TH17. Only a little of N2 (<10% of initial NH4⁺-N) was detected without N2O emission in aerobic denitrification process. Autotrophic NH4⁺-N assimilation contributed predominantly to biomass nitrogen production, supplemented by assimilatory nitrate (NO3⁻-N) reduction under aerobic conditions. A total of 17 amino acids, accounting for 54.25 ± 1.98% of the dry biomass, were detected in the bacterial biomass harvested at 72 h. These results demonstrated that the newly isolated strain TH17 was capable of removing NH4⁺-N and recovering nutrients from wastewater efficiently. A new solution was thus provided by this HOB for ammonium treatment in sustainable WWTPs of future.
Article
This paper proposes the modified mechanical and mathematical modeling of lead zirconium titanate (PZT) sensor based on the PZT constitutive relation in order to solve the complicated boundary condition and stress situation of PZT sensor due to the effect of adhesive-layer damping. The experimental study on the surface-bonded PZT sensor is chosen to carry out the correctness of the proposed models. The results show that the PZT sensor modeling is simplified to three types. When the amplitude of harmonic force is constant, the greater the excitation frequency, the more sensitive the output voltage is, the easier the signal acquisition is. At a certain frequency, the voltage output is proportional to the force amplitude. The larger the area or thickness of PZT, the greater the output voltage is, the more sensitive the signal output is. The output voltage is in quadratic relation to the bonding thickness. Furthermore, the smaller the output voltage, the greater the damping is. The signal loss is about 25.82%. The signal acquisition effect of the PZT square wafer is better than that of circular wafer under the same area of PZT sensor. The research achievements reveal the sensing mechanisms and validate the efficiency of the developed model and effectively simulate and detect direct piezoelectric rule of PZT sensor.
Article
Full-text available
The effects of environmental conditions on ammonia removal as struvite (Magnesium ammonium phosphate, MAP) were studied in a laboratory scale batch reactor. MAP precipitation was carried out by adding phosphoric acid and magnesium source either as MgCl, or MgO. The effect of temperature, pH, MgN:P ratios were studied. Temperature did not significantly affect ammonia removal between 25-40 degrees C and over 90% removal was obtained. The effect of pH, however,was significant and highest removal was reached at pH 8.5-9.0. The various stoichiometric ratios of ammonium to Mg and P have been tested and slight excess of Mg and P found to be beneficial for higher recovery of ammonia as struvite. However further increase in Mg and P ratios did not result in further ammonia removal which is also costly for the practical application of the process. When MgO was used as M source,the ammonia recovery was 60-70% whereas the useMgCl2 has increased this figure up to 95%. In addition a two step purification process was developed to recover MAP crystals from impurities of the anaerobic digester. Firstly, precipitates were dissolved in acid and impurities were removed by centrifugation. The clarified supernatant was re-precipitated by adjusting its pH with caustic. It was shown that in the two steps process white MAP crystals could be obtained with over 85% recovery to be used for another applications. The economical analysis of the process has shown that ammonia in the digester effluents can be recovered at the cost of $7.5-8.0 kg(-1) NH4+-N. The rate of reaction is very fast and is completed almost in minutes. This simplifies the process design resulting in a smaller reaction vessel.
Article
Ammonium nitrogen removal from wastewater has been of considerable concern for several decades. In the present research, we examined chemical precipitation recycle technology (CPRT) for ammonium nitrogen removal from coking wastewater. The pyrolysate resulting from magnesium ammonium phosphate (MAP) pyrogenation in sodium hydroxide (NaOH) solution was recycled for ammonium nitrogen removal from coking wastewater. The objective of this study was to investigate the conditions for MAP pyrogenation and to characterize of MAP pyrolysate for its feasibility in recycling. Furthermore, MAP pyrolysate was characterized by scanning electron microscope (FESEM), transmission electron microscope (TEM), Fourier transform infrared spectroscopy (FTIR) as well as X-ray diffraction (XRD). The MAP pyrolysate could be produced at the optimal condition of a hydroxyl (OH(-)) to ammonium molar ratio of 2:1, a heating temperature of 110 degrees C, and a heating time of 3h. Surface characterization analysis indicated that the main component of the pyrolysate was amorphous magnesium sodium phosphate (MgNaPO(4)). The pyrolysate could be recycled as a magnesium and phosphate source at an optimum pH of 9.5. When the recycle times were increased, the ammonium nitrogen removal ratio gradually decreased if the pyrolysate was used without supplementation. When the recycle times were increased, the ammonium nitrogen removal efficiency was not decreased if the added pyrolysate was supplemented with MgCl(2).6H(2)O plus Na(2)HPO(4).12H(2)O during treatment. A high ammonium nitrogen removal ratio was obtained by using pre-formed MAP as seeding material.
Article
Chemical precipitation is a useful technology to remove ammonium (NH(4)(+)) from landfill leachate. In this paper, the removal of ammonium from landfill leachate was studied. The objective of this study was to investigate optimum pH, optimum molar ratio, and different kinds of chemicals combinations for magnesium ammonium phosphate (MAP) precipitation. Furthermore, the kinetics of MAP formation and surface characterization were analyzed. The results indicated that ammonium in landfill leachate could be removed with the optimum pH of 9.5. The Mg(2+):NH(4)(+):PO(4)(3-) molar ratio was practically controlled at 1.15:1:1 to remove ammonium effectively and avoid higher concentration of PO(4)(3-) in the effluent. Highest salt concentration was generated by using MgCl(2).6H(2)O plus Na(2)HPO(4).12H(2)O. Compare to MgCl(2).6H(2)O and Na(2)HPO(4).12H(2)O, adding MgO and 85% H(3)PO(4) could significantly minimize the salt concentration, although ammonium removal ratio was 9 percent lower. The lowest ammonium removal ratio was generated by adding Ca(H(2)PO(4))(2).H(2)O and MgSO(4).7H(2)O. Moreover, the kinetics experiment shown that the rate of reaction was closer to the first-order kinetic model. Fourier transform infrared spectroscopy (FTIR) and X-ray diffraction (XRD) analysis indicated that MAP was the main composition of the precipitates. Scanning electron microscopy with energy dispersive X-ray (SEM-EDX) analysis indicated that the unshaped crystal was coarse and its size was irregular, the surface composition of the precipitates contains a great deal of O, P, Mg and trace of C, K, Na, Cl.
Article
Chemical precipitation to form magnesium ammonium phosphate (MAP) is an effective technology for recovering ammonium nitrogen (NH4(+)-N). In the present research, we investigated the thermodynamic modeling of the PHREEQC program for NH4(+)-N recovery to evaluate the effect of reaction factors on MAP precipitation. The case study of NH4(+)-N recovery from coking wastewater was conducted to provide a comparison. Response surface methodology (RSM) was applied to assist in understanding the relative significance of reaction factors and the interactive effects of solution conditions. Thermodynamic modeling indicated that the saturation index (SI) of MAP followed a polynomial function of pH. The SI of MAP increased logarithmically with the Mg2+/NH4+ molar ratio (Mg/N) and the initial NH4(+)-N concentration (CN), respectively, while it decreased with an increase in Ca2+/NH4+ and CO3(2-)/NH4+ molar ratios (Ca/N and CO3(2-)/N), respectively. The trends for NH4(+)-N removal at different pH and Mg/N levels were similar to the thermodynamic modeling predictions. The RSM analysis indicated that the factors including pH, Mg/N, C(N), Ca/N, (Mg/N)x (CO3(2-)/N), (pH)2, (Mg/N)2, and (C(N))2 were significant. Response surface plots were useful for understanding the interaction effects on NH4(+)-N recovery.
Article
The present review provides an understanding of principles of struvite crystallization and examines the techniques and processes experimented to date by researchers at laboratory, pilot, and full-scale to maximize phosphorus removal and reuse as struvite from wastewater effluents. Struvite is mainly known as a scale deposit causing concerns to wastewater companies. Indeed, struvite naturally occurs under the specific condition of pH and mixing energy in specific areas of wastewater treatment plants (e.g., pipes, heat exchangers) when concentrations of magnesium, phosphate, and ammonium approach an equimolar ratio 1:1:1. However, thanks to struvite composition and its fertilizing properties, the control of its precipitation could contribute to the reduction of phosphorus levels in effluents while simultaneously generate a valuable by-product. A number of processes such as stirred tank reactors and air-agitated and -fluidized bed reactors have been investigated as possible configurations for struvite recovery. Fluidized bed reactors emerged as one of the promising solutions for removing and recovering phosphorus as struvite. Phosphorus removal can easily reach 70% or more, although the technique still needs improvement with regard to controlling struvite production quality and quantity to become broadly established as a standard treatment for wastewater companies.
Article
The landfill leachate in Hong Kong usually contains quite high NH4+–N concentration, which is well known to inhibit nitrification in biological treatment processes. A common pre-treatment for reducing high strength of ammonium (NH4+–N) is by an air-stripping process. However, there are some operational problems such as carbonate scaling in the process of stripping. For this reason, some technical alternatives for NH4+–N removal from leachate need to be studied. In this study, a bench-scale experiment was initiated to investigate the feasibility of selectively precipitating NH4+–N in the leachate collected from a local landfill in Hong Kong as magnesium ammonium phosphate (MAP). In the experiment, three combinations of chemicals, MgCl2·6H2O+Na2HPO4·12H2O, MgO+85% H3PO4, and Ca(H2PO4)2·H2O+MgSO4·7H2O, were used with the different stoichiometric ratios to generate the MAP precipitate effectively. The results indicated that NH4+–N contained in the leachate could be quickly reduced from 5618 to 112 mg/l within 15 min, when MgCl2·6H2O and Na2HPO4·12H2O were applied with a Mg2+:NH4+:PO43− mol ratio of 1:1:1. The pH range of the minimum MAP solubility was discovered to be between 8.5 and 9.0. Attention should be given to the high salinity formed in the treated leachate by using MgCl2·6H2O and Na2HPO4·12H2O, which may affect microbial activity in the following biological treatment processes. The other two combinations of chemicals [MgO+85% H3PO4 and Ca(H2PO4)2·H2O+MgSO4·7H2O] could minimise salinity after precipitation, but they were less efficient for NH4+–N removal, compared with MgCl2·6H2O and Na2HPO4·12H2O. COD had no significant reduction during this precipitation. It was found that the sludge of MAP generated was easily settled within 10 min to reach its solids content up to 27%. The other characteristics including capillary suction time (CST) and dry density (DD) of the MAP sludge were also tested. The experimental results indicate that the settled sludge is quite solid and can be directly dumped at a landfill site even without any further dewatering treatment.
Article
The removal of ammonium (NH(4)(+)) and phosphate (PO(4)(3-)) from supernatant of anaerobic digestion by magnesium ammonium phosphate (MAP) formation was studied. To be able to find out the loss of NH(4)(+) by its transformation to NH(3), rates of NH(4)(+) removal by aeration and by MAP formation combined with aeration were compared. NH(4)(+) removal by aeration was found to be insignificant. The kinetics of MAP formation was fast. The removal rate of NH(4)(+) and Mg(2+) was the smallest and the largest, respectively based on rate constants calculated. The removal of NH(4)(+) showed sensitivity to Mg(2+) and PO(4)(3-) concentrations and controlled the purity of MAP precipitate. The removal of PO(4)(3-) was found to be sensitive to mainly Mg(2+) ion. These results also indicated that as the supernatant solution became more saturated in terms of MAP forming ions, the effect of pH increase became insignificant in the removal of ions from the solution.
Article
Struvite precipitation in wastewater treatment works has caused substantial operational problems since the early 1960s. Struvite, magnesium ammonium phosphate hexahydrate (MgNH4PO4 6H2O), is a white inorganic crystalline mineral that precipitates in places with increased turbulence such as pumps, aerators and pipe bends. Batch experiments were conducted to examine the influence of a number of physical and chemical parameters on struvite crystallisation. This was undertaken by dosing a medium of de-ionised water with varying concentrations of Mg2+, NH4+ and PO4(3-) ions. Preliminary experiments found that struvite could be precipitated out of solution at pH 10 and increasing the ion concentration stoichiometrically could increase crystal yield. Increasing the NH4+ concentration increased purity of the precipitate. As reaction time was increased from 1 to 180 min, crystal size was found to increase from 0.1 to 3mm.
Article
Recent legislation on the removal of nutrients from wastewater has led to a number of operation problems with struvite scaling. Struvite is MgNH4PO4 x 6H2O and this paper reviews the formation, control and recovery of struvite from primarily municipal wastewater and other waste streams. Treatment options for control and technologies for recovery are discussed.
  • S Uludag-Demirer
  • M Othman
S. Uludag-Demirer, M. Othman: Bioresource Technol. Vol. 100 (2009), p.3236-3244.