Synthesis of hydrotalcite powder and bead to remove arsenate - Tung Nguyen Thanh
4. CONCLUSIONS
Powder HT was synthesized at low and high super saturation condition. The HT formation
under high super saturation condition with short reaction time had the highest As(V) removal
efficiency. It could remove As(V) from 500 g/L to 6 g/L; met Vietnamese standard for
drinking water of 10 g/L (QCVN01-2009/BYT). The high As(V) removal efficiency of HT
synthesized with short reaction time is a new finding in this study.
Bead HT were fabricated with alginate and PAM binders. PAM binding bead had the
highest As(V) removal efficiency. The As(V) removal of freeze drying alginate/MA was close to
that of MA with PAM binder and much higher than that of heat drying alginate/MA. Freeze
drying alginate/MA also had advantage of higher adsorption rate than PAM binding MA.
Further investigation to improve the capacity of freeze drying alginate/MA is needed.
Acknowledgements. This research is financially supported by GSGES seeds research funding program for
overseas field campuses of Kyoto University (Fiscal year 2015)
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Vietnam Journal of Science and Technology 55 (4C) (2017) 204-209
SYNTHESIS OF HYDROTALCITE POWDER AND BEAD TO
REMOVE ARSENATE
Tung Nguyen Thanh
1
, Thuy Ly Bich
1, *
, Shinya Echigo
2
1
School of Environmental Science and Technology, Hanoi University of Science and
Technology, No.1 Dai Co Viet Street, Ha Noi, Viet Nam
2
National Institute of Public Health, 2-3-6 Minami, Wako 351-0197, Japan
*
Email: thuy.lybich@hust.edu.vn; nguyentung2407@gmail.com; shinyae@gmail.com
Received: 15 July 2017; Accepted for publication: 15 October 2017
ABSTRACT
The affecting factors on the synthesis of hydrotalcite (HT) powder and bead for effective
arsenate removal were investigated. HTs with a ratio of Mg:Al = 2:1 (MA) were synthesized by
the co-precipitation method at 70
o
C with reaction times of 1 and 120 - 300 min. The synthesis
of MA with a reaction time of 1 min was done under high supersaturation condition, the others
under low supersaturation conditions. The characteristics of MA were examined by X-ray
diffraction (XRD), scanning electron microscopy, and nitrogen adsorption/desorption isotherms.
According to the XRD patterns, pure HT was obtained for all tested conditions. With increasing
reaction time from 1 to 300 min, the crystal size of MA increased from 4.9 to 11.3 μm, the
surface area of MA increased from 9.3 to 71.4 m
2
/g. Batch-mode experiments showed that 1-min
reaction time MA had the highest As(V) removal capacity. MA beads were separately
synthesized using alginate and poly acrylamide (PAM) as binding agents. For alginate/MA, heat
drying (110
o
C) and freeze drying were applied to test the effect of these drying methods on the
beads. The results showed that As(V) adsorption capacity of PAM/MA was the highest, closely
followed by freeze drying/alginate/MA, much higher than that of heat drying/alginate/MA bead.
Keywords: hydrotalcite, arsenate, adsorption.
1. INTRODUCTION
HT is a promising adsorbent to treat environmental pollutants [1 - 3]. However, the
common form of HT (powder) limits its application to environment treatment system. Thus, HT
in bead forms had been synthesized to overcome this disadvantage [4, 5].
The problem of arsenic pollution in Viet Nam is serious [6]. The research on As removal by
different materials has been done by several researchers in Vietnam as presented elsewhere [7].
In this study, we synthesized powder HT with the formula of Mg4Al2(OH)12CO3•3H2O
named MA under low and high super saturation conditions with different reaction times. As(V)
removal capacities and other characteristics of the synthesized MAs were compared. Then, MA
Synthesis of hydrotalcite power and bead to remove arsenate
205
beads with either alginate or PAM as binder were fabricated. As(V) removal capacities of the
synthesized MA beads were compared.
2. MATERIALS AND METHODS
2.1. Materials
Mg(NO3)2 Al(NO3)3 Na2CO3 (England-PA) were used for synthesis experiments. Standard
solution of As(V) (H3AsO4 in HNO3) with concentration of 1000 mg/L (MERCK) was used as
stock solution for As(V).
2.2. Synthesis of HT powder and bead
a. HT powder formation under low supersaturation condition: MA was synthesized by
injecting the mixture of 100 mL of 1 M Mg(NO3)2 and 50 mL of 1 M Al(NO3)3 at a rate of
150 mL/h into 260 mL of 1 M Na2CO3 at 70
o
C with mixing (300 rpm). Soaking intervals of 2, 3,
4, 5 hr were applied, and the materials were named MA2, MA3, MA4, MA5, respectively. The
obtained crystals were then filtered and washed with distilled water for three times, in which
once under sonication. The MAs were then dried at 110
o
C for 24 hr and grinded by a ball
grinner (Retsch MM200) and sieved (150 m mesh) to obtain the MA powder. The reaction time
interval was chosen from the fact that the lowest reaction time for HT formation under low
supersaturation condition in literature was 2 hr [8-12].
b. HT powder formation under high supersaturation condition: Our results later on showed
that even at the shortest reaction time (i.e., 2 hr), HT can be formed at 100% efficiency and
As(V) removal capacity was not significantly different. Therefore, we conducted HT formation
experiment under high super saturation condition in which the mixture of 100 mL of 1 M
Mg(NO3)2 and 50 mL of 1 M Al(NO3)3 was quickly added to into 260 mL of 1 M Na2CO3 at 70
o
C and shaking shortly until the solution become completely homogenous (about 1 min). This
material was named MA0.
c. HT bead fabrication: Three grams of the mixture of sodium alginate and MA with an
alginate ratio of 5 % was dispersed in 20 mL of distilled water. The mixture was added dropwise
with a syringe into 10 % CaCl2 solution to produce beads in spherical form with diameter of 2
mm. The alginate/beads were dried by two methods: heating at 105
o
C until completely dried
and freeze drying. The freeze drying was done by completely freezing the bead at -20
o
C before
drying with a Labconco freezer dryer. PAM binder was applied at a ratio of 6 % by a similar
process with the heat dried bead by alginate binder. The ratios of alginate and PAM binder were
chosen from pre-experiment that the minimum binder percentages to keep beads stable after
shaking in water at 150 rpm for 1 hr were used.
2.3. HT powder characteristic analysis
XRD analysis was carried out by D8 Advance-Bruker XRD. SEM image was taken by
Nova nanoSEM 450-FEI. Nitrogen adsorption/desorption isotherms (BET) was measured by
Germini VII 2390.
Thanh Tung Nguyen, Bich Thuy Ly, Shinya Echigo
206
2.4. As(V) removal experiments
Batch mode adsorption tests of powder: The tests were carried out in 50 mL Erlenmeyer
flasks containing 50 ml of 500 g/L As(V) solutions with a solid-to-liquid ratio of 0.2 g/L (pH,
7; temperature, 25
o
C; mixing, 150 rpm; contact time,1 hr). The solution was then filtered and
As(V) in the filtrate was measured by ICP-MS (Perkin Elmer).
Batch mode adsorption test for bead: The absorption tests for MA bead were carried
similarly with the test for MA powder except that they were done in 100 mL solution for time
interval of 1, 3, 6, 16, 24, 48 hr.
3. RESULTS AND DISCUSSION
3.1. Structure of materials
Figure 1. XRD patterns of MA materials, the numbers above peaks are Miller Index.
Figure 2. SEM images of MA materials: a) MA0, b–e) MA(2-5).
XRD patterns of the synthesized MAs were presented in Fig.1. For all the MAs,
crystallized HT-like phase peaks were presented with typical peak at 2θ of 11.5o, 23.5o, 35o and
39.5
o
[13] No other crystalline phase peak was detected.
Synthesis of hydrotalcite power and bead to remove arsenate
207
The average weights of obtained MA(0-5) (n = 2 each) were 11.7 0.1 g. This value was
equal with theoretical mass of MA (calculated from its chemical formula) of 11.7 g, proving that
the formation efficiency of HT was about 100 %. XRD pattern and weights analysis results
indicated that initial reactants reacted completely. More interestingly, the obtained results
showed that HT could be synthesized with short reaction time which, so far, has not been
reported for MA synthesis as far as we know.
3.2. Effect of reaction period on crystal size
The sizes of single crystal were calculated following Debye-Scherrer formula [8] and
summarized in Table 1. The data in Table 1 showed that crystal sizes increased with the
increasing of reaction time. MA0 had the smallest crystal size of 49 Å, clearly lower than crystal
size of other MAs(95-113 Å). Those sizes were smaller than those in other researches, such as
230 Å [8] and 526 – 1653 Å [9]. The differences in those sizes were because the reaction periods
in this study were shorter than those of previous researches (18 h and 200
o
C [8] and at 200
o
C
and 24 h [9]). This increase of crystal sizes with reaction period was well explained because of
the smaller crystals were consumed by larger particle by Ostwald rippening mechanism. SEM
results (Fig. 2) showed that polycrystal sizes increased with reaction times. Hexagonal shape can
be observed in SEM image of MA(2-5) even though they were not so clear. Those crystals were
significantly different from the crystals forming under high supersaturation condition with short
reaction time (MA0), in which the crystal form was hardly observed.
Table.1. Single crystal size of Mas.
Samples Full width at half maximum (angle) Single crystal size(Å)
MA0 1.622 49
MA2 0.840 95
MA3 0.737 108
MA4 0.704 113
MA5 0.736 108
3.3. As(V) treatment efficiency of powder MA
The treatment efficiencies of MA on As(V) were presented in Fig 3. The removal efficiency
of MA0 was the best (99.1 %). MA2, MA3, MA4, MA5 showed no significant difference in
As(V) removal efficiency. This highest adsorption capacity of MA0, however, interestingly in
contrast with BET results indicated that the specific area of MA0 (9.3 m
2
/g) was significantly
lower than those of MA(2-5) of 70.4 - 71.4 m
2
/g. Further research about this phenomenon to
apply MA to environment treatment should be conducted.
3.4. As(V) removal capacity of MA bead
The As(V) removal efficiencies of MA beads are presented in Fig. 4. The data showed that
the fabricated MA with PAM as the binder had highest As(V) removal efficiency. The removal
efficiency reached equilibrium at 72 % after 24 hr.
Thanh Tung Nguyen, Bich Thuy Ly, Shinya Echigo
208
Figure 3. As(V) removal efficiency and crystal size
of MAs in powder form (V = 50 mL, Co = 500 g/l,
solid-to-liquid ratio = 0.2 g/l, pH = 7; temperature 25
o
C, ; mixing = 150 rpm; contact time = 1 hr).
Figure 4. As(V) removal efficiency by MA beads
(V = 100 mL, Co = 500 g/l, solid-to-liquid
ratio = 0.2 g/l, pH = 7; temperature 25
o
C;
mixing = 150 rpm).
The adsorption rates of alginate/MA were high in the first 6 hr and slowed down in the later
phase reached equilibrium after around 16 hr. The alginate MA bead finished by heat drying had
As(V) removal efficiency of 42 % much lower than the ones finished by freezer drying (68 %).
This result can be explained by comparing SEM data of heat drying and freeze drying alginate
bead presented in other research [14, 15]. The heat drying bead had almost no pore whereas the
freezed ones had pores [14, 15]. Further investigation in freeze drying method of HT/alginate
bead may help to increase their As(V) removal efficiency.
4. CONCLUSIONS
Powder HT was synthesized at low and high super saturation condition. The HT formation
under high super saturation condition with short reaction time had the highest As(V) removal
efficiency. It could remove As(V) from 500 g/L to 6 g/L; met Vietnamese standard for
drinking water of 10 g/L (QCVN01-2009/BYT). The high As(V) removal efficiency of HT
synthesized with short reaction time is a new finding in this study.
Bead HT were fabricated with alginate and PAM binders. PAM binding bead had the
highest As(V) removal efficiency. The As(V) removal of freeze drying alginate/MA was close to
that of MA with PAM binder and much higher than that of heat drying alginate/MA. Freeze
drying alginate/MA also had advantage of higher adsorption rate than PAM binding MA.
Further investigation to improve the capacity of freeze drying alginate/MA is needed.
Acknowledgements. This research is financially supported by GSGES seeds research funding program for
overseas field campuses of Kyoto University (Fiscal year 2015).
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