Qiong Wan1, Xuan Li1, Yingchun Ren2, Yixi Cao3, Kai Ju1, Guohong Yang1, Yongqing Sun1, Xinyan Zhang1. 1. School of Architecture and Civil Engineering, Xi'an University of Science and Technology, Xi'an 710054, China. 2. Yihai Kerry (Zhoukou) Biotechnology Co., Ltd., Zhoukou 466000, China. 3. Shaanxi Water Affair Water Ecology Comprehensive Development Group Co., Ltd., 11801, New Century Building, 2 Gaoxin Road, Xi 'an 710075, China.
Abstract
The temperature/pH dual-responsive gel spheres were prepared by orthogonal experiments and response surface methodology, and finally, the optimal synthesis conditions were obtained by a composite score, including swelling, mechanical properties, mass transfer properties, and so forth. The results showed that a sodium alginate concentration of 3% (w/v), CaCl2 concentration of 2% (w/v), gelling time of 40 h, drop height of 14 cm, NaCl concentration of 0.6% (w/v), N-isopropylacrylamide concentration of 0.03% (w/v), and acrylic acid concentration of 4.06% (w/v) were optimal synthesis conditions. The environmental change tolerance experiments showed that the nitrogen removal of the dual-response nitrifying gel spheres was better than the domesticated sludge at low temperatures (4 °C) and in alkaline (pH 9 and 10) conditions. The as-obtained gel spheres can respond intelligently to the changes in ambient temperature and pH. It is hoped that this study will provide technical parameters for the development and application of microbial immobilization carriers.
The temperature/pH dual-responsive gel spheres were prepared by orthogonal experiments and response surface methodology, and finally, the optimal synthesis conditions were obtained by a composite score, including swelling, mechanical properties, mass transfer properties, and so forth. The results showed that a sodium alginate concentration of 3% (w/v), CaCl2 concentration of 2% (w/v), gelling time of 40 h, drop height of 14 cm, NaCl concentration of 0.6% (w/v), N-isopropylacrylamide concentration of 0.03% (w/v), and acrylic acid concentration of 4.06% (w/v) were optimal synthesis conditions. The environmental change tolerance experiments showed that the nitrogen removal of the dual-response nitrifying gel spheres was better than the domesticated sludge at low temperatures (4 °C) and in alkaline (pH 9 and 10) conditions. The as-obtained gel spheres can respond intelligently to the changes in ambient temperature and pH. It is hoped that this study will provide technical parameters for the development and application of microbial immobilization carriers.
Microbial
immobilization is a vital way to enhance the functionality
of microorganisms, where the target microorganisms are confined to
a limited area (carrier material) to maintain high biomass and biological
activity.[1] Compared to free bacteria, immobilized
microorganisms have the advantages of high biodegradation rates, good
environmental tolerance, and easy solid–liquid separation.[2] Simultaneously, the immobilization technology
is suitable for various functional microorganisms, including anaerobic
ammonia-oxidizing bacteria, aerobic denitrifying bacteria, and hydrocarbon-degrading
bacteria.[3−6] Therefore, the technology has gradually shown great potential in
different areas such as bio-hydrogen production, soil remediation,
and wastewater treatment.[7−9]The choice of the carrier
material is crucial to the diffusion
of microbial immobilization techniques. A good carrier material should
have unique features, including good stability, high mass transfer
capacity, cheap and easy raw materials availability, and good biocompatibility.[10,11] Particularly prominent among these is the natural organic carrier
sodium alginate (SA), a linear anionic polysaccharide composed of
β-d-mannuronic acid and α-l-guluronic
acid.[12−14] It is enriched with −OH and −COOH,
can form stable hydrogels with multivalent cations such as Ca2+ (except Mg2+ cations), and is currently one of
the most demanded carrier materials.[15,16] Since the
integrated adsorption—biodegradation—assimilation process
is the only mechanism behind the removal of targeted pollutants by
immobilized microorganisms,[2] changes in
the external environment such as temperature, pH, magnetic field,
ionic strength, and so forth can inhibit the growth and metabolism
of free microorganisms, resulting in lower pollutant removal rates.
Therefore, the development and promotion of gel spheres resistant
to external environmental changes are highly recommended.Poly-N-isopropyl acrylamide (PNIPAAm) and polyacrylic
acid (PAA) are typical sensitive polymers utilized to prepare responsive
gel spheres. PNIPAAm is thermally responsive due to its inherently
lower critical solution temperature (LCST), approximately 32 °C.[17−19] This is demonstrated by the fact that when the ambient temperature
is below LCST, PNIPAAm appears to swell hydrophilically, and conversely,
it shrinks in volume and is hydrophobic.[20] PAA can respond to pH value changes by protonation or deprotonation
due to the abundance of ionizable −COOH moieties in its structure.[21] Numerous papers have shown that gel spheres
modified by PNIPAAm or PAA show a satisfactory response to temperature/pH
changes, thus resisting the inhibition of functional microorganisms’
activity by external environmental changes.[22−25]In this study, the optimum
calcium alginate (CA) gel spheres were
successfully prepared using orthogonal experiments; on this behalf,
the pore structure was optimized by the modification effect of NaCl
solution. The biocompatible CA gel spheres were used as the core substrate
and interacted with NIPAAm, acrylic acid (AA), and N,N-methylenebisacrylamide (MBA) reagents to produce
a temperature/pH responsive layer and result in the formation of optimizing
environmentally dual-responsive gel spheres. It is proposed that this
study will provide a new platform for the development and application
of microbial immobilization carriers.
Results
and Discussion
Preparation and Optimization
of CA Gel Spheres
SA is the prime material required for the
preparation of CA gel
spheres, and its mass concentration affects the sphericity, mechanical
strength, and ease of preparation of gel spheres. Lower concentration
of SA results in poor sphericity and poor strength, while higher concentration
of SA provides higher strength CA spheres due to its high viscosity,
but it still suffers from severe trailing and complicated preparation.
Besides, previous studies have suggested that CaCl2 concentration,
gel time, and drop height also have a dominant effect on CA gel sphere
properties (such as sphericity, mechanical strength, and swelling).[26−28] Therefore, in this study, the above four factors were tested orthogonally
to determine the optimal synthesis conditions for CA gel spheres,
and the results are shown in Table . The relationship between factors and scores was also
plotted using the value of each factor level as the horizontal coordinate
and the mean value of the corresponding composite score for each factor
level as the vertical coordinate (Figure ). As depicted in Figure , the composite score of CA gel spheres tends
to increase first and then decrease with increasing SA concentration,
with a maximum value achieved at a SA concentration of 3% (w/v). Similarly,
the CA gel spheres achieved a maximum composite score at a CaCl2 concentration of 2% (w/v), a gelling time of 40 h, and a
drop height of 14 cm. It was deduced that the optimal synthesis conditions
for CA gel spheres are A4B1C4D5 (A4, B1, C4, and D5 indicate SA concentration of 3% (w/v), CaCl2 concentration
of 2% (w/v), gelling time of 40 h, and drop height of 14 cm, respectively).
Based on the magnitude of the R-value of the extreme
difference derived from the orthogonal experiment and the results
of the ANOVA presented in Table , it could be seen that the ranking of the factors
affecting the composite score was A(20.4) > C(4.8) > B(4) = D(4).
SA concentration significantly affected the composite score.
Table 1
Orthogonal Test Resultsa
factors
sample
A (%)
B (%)
C (h)
D (cm)
composite
score
1
0.5
2
10
6
22
2
0.5
3
20
8
24
3
0.5
4
30
10
15
4
0.5
5
40
12
22
5
0.5
6
50
14
14
6
1
2
20
10
30
7
1
3
30
12
27
8
1
4
40
14
32
9
1
5
50
6
28
10
1
6
10
8
25
11
2
2
30
12
37
12
2
3
40
14
39
13
2
4
50
6
32
14
2
5
10
8
40
15
2
6
20
10
31
16
3
2
40
14
43
17
3
3
50
6
40
18
3
4
10
8
40
19
3
5
20
10
36
20
3
6
30
12
40
21
4
2
50
6
38
22
4
3
10
8
38
23
4
4
20
10
36
24
4
5
30
12
38
25
4
6
40
14
40
Note: A, B, C, and D indicate
SA
concentration, CaCl2 concentration, gelling time, and drop
height, respectively.
Figure 1
Relationship
diagram between factors and score.
Table 2
Analysis of Variance and Significance
Testa
source
sum of squares
of deviations
freedom
mean square
F-value
F0.05 (4,4)
F0.01 (4,4)
significance
A
1413.04
4
353.26
23.93
6.39
15.98
**
B
59.04
4
14.76
1.00
6.39
15.98
C
70.64
4
17.66
1.20
6.39
15.98
D
52.64
4
13.16
0.89
6.39
15.98
error
59.04
4
14.76
sum
1654.4
20
Note: A, B, C,
and D indicate SA
concentration, CaCl2 concentration, gelling time, and drop
height, respectively, ** indicates highly significant correlation.
Relationship
diagram between factors and score.Note: A, B, C, and D indicate
SA
concentration, CaCl2 concentration, gelling time, and drop
height, respectively.Note: A, B, C,
and D indicate SA
concentration, CaCl2 concentration, gelling time, and drop
height, respectively, ** indicates highly significant correlation.
Preparation
and Optimization of NaCl-Modified
Gel Spheres
High concentrations of Ca2+ ions can
cause changes in the structure of the resulting CA gel spheres to
make them too dense, which negatively impacts their mass transfer
properties.[29] It has been shown that immersing
CA gel spheres in a suitable concentration of NaCl solution can effectively
improve this defect, and some of the chelated carboxylate moieties
are replaced by Ca2+ to free state by Na+, making
the internal structure of the gel spheres more loose and porous.[30] In this study, the optimum CA gel spheres produced
in Section were
placed in NaCl solutions of different concentrations (0–0.9%,
w/v) and scored in four aspects: swelling, mechanical strength, oscillatory
breakage rate, and mass transfer performance. As can be seen from
the results presented in Figure , the highest composite score was achieved at 0.6%
(w/v) NaCl-modified gel spheres. Therefore, 0.6% (w/v) NaCl solution
was chosen as the optimal synthesis condition for the NaCl-modified
gel spheres.
Figure 2
Relationship diagram between NaCl concentration and score.
Relationship diagram between NaCl concentration and score.
Preparation and Optimization
of Temperature/pH
Dual-Response Gel Spheres
Response surface methodology (RSM)
is one of the ideal methods to reduce the number of experiments and
is used for modeling, data analysis, and optimization purposes.[31]Table shows the results of the trials of the effect of the independent
variables NIPAAm, MBA1, AA, and MBA2 concentration
on the composite score. Figure shows a response surface plot of the effect of the independent
variables on the composite score. Figure a,c shows that NIPAAm concentration was inversely
proportional to the composite score if MBA1 concentration
was certain. The predicted maximum composite score of 38.13 was achieved
at NIPAAm and MBA1 concentration of 0.03 and 0.02%, respectively.
From Figure b,d, it
could be seen that if the MBA2 concentration was certain,
the composite score tends to increase and then decrease with the increase
of AA concentration. The maximum composite score of 38.13 was achieved
at AA and MBA2 concentration of 4.06 and 0.26%, respectively.
Therefore, the optimal synthesis conditions for the dual-response
gel spheres were selected as 0.03 and 0.02% of NIPAAm and MBA1 in the temperature-modified solution, 4.06, and 0.26% of
AA and MBA2 in the pH-modified solution.
Table 3
Box-Behnken Design
and Effect of Independent
Variables on Composite Score as a Response
runs
NIPAAm (%)
MBA1 (%)
AA (%)
MBA2 (%)
composite
score
1
0.93
0.01
0.1
0.23
28
2
1.83
0.02
5
0.23
36
3
0.93
0.02
2.55
0.23
37
4
0.93
0.03
2.55
0.01
36
5
0.03
0.02
0.1
0.23
29
6
0.93
0.02
2.55
0.23
37
7
0.93
0.01
2.55
0.45
35
8
0.03
0.01
2.55
0.23
37
9
0.93
0.02
0.1
0.01
28
10
0.93
0.02
2.55
0.23
37
11
0.93
0.02
5
0.45
36
12
1.83
0.02
2.55
0.01
34
13
1.83
0.02
2.55
0.45
36
14
0.93
0.03
5
0.23
35
15
0.03
0.02
5
0.23
37
16
1.83
0.01
2.55
0.23
36
17
0.93
0.02
2.55
0.23
37
18
0.93
0.03
2.55
0.45
37
19
0.93
0.02
2.55
0.23
36
20
0.93
0.03
0.1
0.23
29
21
0.03
0.03
2.55
0.23
36
22
0.03
0.02
2.55
0.01
36
23
1.83
0.03
2.55
0.23
35
24
0.93
0.01
2.55
0.01
33
25
0.03
0.02
2.55
0.45
35
26
0.93
0.02
0.1
0.45
31
27
1.83
0.02
0.1
0.23
33
28
0.93
0.02
5
0.01
32
29
0.93
0.01
5
0.23
37
Figure 3
Surface plot for composite
score with respect to the three-dimension
(3D) of NIPAAm and MBA1(a); 3D of AA and MBA2(b); 2D of NIPAAm and MBA1(c); and 2D of AA and MBA2(d).
Surface plot for composite
score with respect to the three-dimension
(3D) of NIPAAm and MBA1(a); 3D of AA and MBA2(b); 2D of NIPAAm and MBA1(c); and 2D of AA and MBA2(d).
Gel Sphere Characterization
SEM Analysis
The optimum CA gel
spheres, NaCl-modified gel spheres, and dual-response gel spheres
were not significantly different, all being spheres of uniform particle
size (approximately 4 mm in diameter) and opalescent and translucent
throughout. After dehydration-liquid nitrogen-freeze dried operations,
all types of gel spheres had exhibited an undulating surface (Figure a–c) and a
complete network structure (Figure d–f). The surface of the optimum CA gel spheres
modified by NaCl and dual response, in turn, showed a trend of greater
fold (Figure a), insignificant
fold (Figure b), greater,
uniform, and lesser fold (Figure c). This phenomenon may be related to the pore distribution
and structure of the various types of gel spheres. From the monitored
profile, it can be stated that the NaCl-modified gel spheres (Figure e) showed evident
delamination from the outside to the inside compared to the optimum
CA gel spheres (Figure d), and this phenomenon may be related to the length of the NaCl
modification time. Meanwhile, the shell–core structure (dense
outside and sparse inside) shown in Figure f confirms the successful development of
optimal dual-response gel spheres, forming a composite gel sphere
with a CA as the core and a temperature/pH responsive layer as the
shell layer. Besides, this structure effectively traps the microorganisms
embedded in the gel spheres, providing sufficient space for them to
grow and multiply. Moreover, it can provide a stable living environment
for the proper growth of microorganisms. When the temperature/pH of
the environment fluctuates, the outer temperature/pH response layer
can achieve a real-time response and maintain a relatively stable
and favorable microenvironment for microorganisms to grow.
Figure 4
SEM surface
image of the optimum CA gel spheres (a), NaCl-modified
gel spheres (b), and dual-response gel spheres (c); SEM interior image
of the optimum CA gel spheres (d), NaCl-modified gel spheres (e),
and dual-response gel spheres (f).
SEM surface
image of the optimum CA gel spheres (a), NaCl-modified
gel spheres (b), and dual-response gel spheres (c); SEM interior image
of the optimum CA gel spheres (d), NaCl-modified gel spheres (e),
and dual-response gel spheres (f).
BET Analysis
From the summary table
of gel sphere properties (Table ), it could be observed that the average particle size
of the three optimum gel spheres was 3.8 mm, and there was no significant
difference found in density (all close to the density of water). Regarding
specific surface area and pore size, the optimum CA gel spheres had
a significant specific surface area value of 1.455 m2/g
with an average pore size of 15.10 nm. The specific surface area of
the optimum NaCl-modified gel spheres decreased abruptly up to 0.052
m2/g, probably due to the full replacement of Ca2+ in the CA gel spheres by Na+, resulting in a lower cross-link
density and increased macropore content (average pore size of 62.10
nm).[30] The optimum dual-response gel spheres
were based on the optimum NaCl-modified gel spheres modified with
polymers PNIPAAm and PAA, whose 3D network structure intertwines with
the CA gel spheres, a 3D grid structure, and formed a temperature/pH
responsive layer on the surface.[32] The
final mesoporous material with a specific surface area of 0.113 m2/g and an average pore size of 26.88 nm was produced.
Table 4
Summary of the Three Types of Gel
Sphere Properties
type
diameter
mm
density g/cm3
BET specific
surface area m2/g
average pore
size nm
the optimum CA gel spheres
3.8
0.98
1.455
15.10
the optimum NaCl-modified
gel spheres
1.00
0.052
62.10
the optimum dual-response gel spheres
0.99
0.113
26.88
FT-IR
Analysis
The optimum CA gel
spheres (Figure S1a) and the optimum NaCl
modified gel spheres (Figure S1 b) showed
the same trend in infrared (IR) spectra, both having −OH stretching
vibration peaks (positioned at 3339 cm–1), −COO– antisymmetric (located at 1592 cm–1), and symmetric (peaked at 1416 cm–1) stretching
vibration peaks.[33,34] However, the latter individual
characteristic peaks emerged with greater intensity and were more
pronounced, indicating that the arrangement of the functional groups
was sparser after modification with NaCl. Compared to Figure S1b, a broad peak detected at 3398 cm–1 was assigned to N–H conjugation, peak monitored
at 1243 cm–1 was referred to C–N bond stretching
vibration, isopropyl C–H bond out-of-plane wobble vibration
at 672 cm–1, and C=O stretching vibration
at 1719 cm–1 (characteristic peaks of carboxyl groups)
in Figure S1c, all endorsed the successful
preparation of the optimum dual-response gel spheres.
Gel Sphere Response Experiment
Figure exhibits the variations
in swelling for three types of optimum gel spheres (made in Sections
2.1–2.3, respectively) for different temperatures 5–50
°C (at pH 7) or different pH 2–12 (at temperature 20 °C).
In Figure a, it could
be seen that the swelling of the three types of optimum gel spheres
tends to increase first and then decrease with the increase in temperature,
and the maximum swelling is achieved at 30 °C. The optimum dual-response
gel spheres swelling increased for the temperature range 5–30
°C, probably due to the increased hydration of the gel sphere
network at higher temperatures.[35] As in
numerous previous studies, the dual-response gel spheres did not achieve
high swelling at high temperatures (40–50 °C).[36] This may be due to the fact that under high
temperature conditions, the intramolecular hydrogen bonds were broken,
the hydrophobicity of the gel spheres was increased, and the water
molecules within the structure were released, reducing the degree
of swelling.[37,38] The optimum NaCl-modified gel
spheres had significantly lower mechanical properties (6–9
N) compared to the optimum CA gel spheres (>20 N), although they
had
a large swelling at all temperatures. The optimum dual-response gel
spheres were temperature-sensitive and had a high mechanical strength
(11–14 N), making them more beneficial for encapsulating microorganisms
for biological treatment of wastewater.
Figure 5
Effect of response on
the swelling of gel spheres: (a) temperature
and (b) pH.
Effect of response on
the swelling of gel spheres: (a) temperature
and (b) pH.Figure b shows
that the swelling of the three types of gel spheres increased with
an increase in the pH value. The change in swelling was relatively
flat for the pH range 2–8 and 10–12 and increased significantly
for the pH range 8–10. At pH 10, the swelling of the optimum
CA gel spheres, the optimum NaCl-modified gel spheres, and the optimum
dual-response gel spheres increased to 51.19, 48.01, and 53.14%, respectively.
Overall, a minimum of 14.67% (at pH 2) and maximum of 53.99% (at pH
12) swelling of the gel spheres occurred on the dual-response gel
spheres, achieving a dual-response gel sphere response characteristic
to pH. This was closely related to the formation of a −COOH–
rich temperature/pH-responsive layer on its surface (consistent with
the results in Figure S1c). Moreover, −COOH
was negatively charged (−COO–) at higher
pH due to deprotonation, with an increase in electrostatic repulsion,
changes in the pore structure of the gel spheres, and a consequent
increase in swelling monitored.[21,39,40]Figure shows
that
the morphology of the optimum dual-response gel spheres at different
temperatures and pH conditions. At the same temperature (T = 5 °C), the higher the pH, the larger the size of the gel
spheres (increasing by about 0.8 mm). Similarly, at the same pH (pH
= 10), the higher the T, the larger the size of the
gel spheres (increasing by about 0.7 mm).
Figure 6
Morphology of dual-response
gel spheres: (a) T = 5 °C, pH = 7; (b) T = 5 °C, pH = 10;
and (c) T = 30 °C, pH = 10.
Morphology of dual-response
gel spheres: (a) T = 5 °C, pH = 7; (b) T = 5 °C, pH = 10;
and (c) T = 30 °C, pH = 10.
Environmental Change Tolerance Experiment
Figure exhibits
denitrification performance of the optimum dual-response nitrifying
bacteria gel spheres for different temperatures 4–50 °C
(at pH 7) or pH 4–10 (at temperature 20 °C). The NH4+–N removal rate by the optimum dual-response
nitrifying bacteria gel spheres increased first and then decreased
with increasing temperature (Figure a). The maximum NH4+–N
removal rate (45.21%) was achieved at 30 °C. The reason may be
that the gel spheres had a temperature/pH responsive layer, when the
temperature was lower than LCST, the gel spheres appear to swell hydrophilically
and the surface micropores open up, allowing the nitrobacteria embedded
in the inner layer of the gel spheres to come into full contact with
the NH4+–N in solution.[37] However, compared to domesticated sludge, it did not show
nitrogen removal advantages at medium temperatures (20 and 30 °C)
due to mass transfer limitations. In contrast, the optimum dual-response
nitrifying bacteria gel spheres showed superior denitrification performance
at low temperatures (4 °C) with 31.07% removal of NH4+–N, 6.87% higher than the domesticated sludge.
The reason may be that the gel slowed down the inhibition of microbial
growth at low temperatures and provided a good living space for microorganisms,
thus offering the possibility of effective degradation of ammonia
nitrogen.[14,41,42]
Figure 7
Tolerance to
environmental changes of the optimum dual-response
nitrifying bacteria gel spheres (A) and acclimated sludge (B): (a)
temperature and (b) pH.
Tolerance to
environmental changes of the optimum dual-response
nitrifying bacteria gel spheres (A) and acclimated sludge (B): (a)
temperature and (b) pH.Overall, the effect of
pH on the domesticated sludge and the optimum
dual-response nitrifying bacteria gel spheres showed similar trends:
NH4+–N removal rate increased and then
decreased with increasing pH (Figure b). Due to the intrinsic characteristics of the nitrifying
bacteria [optimum pH range for AOB and NOB (7.5–8.5),[43] the maximum NH4+–N
removal rate (52.21%) was achieved at pH 8 for the domesticated sludge.
The optimum dual-response nitrifying bacteria gel spheres did not
show nitrogen removal benefits at this pH due to mass transfer limitations.
On the contrary, at pH 9 and 10, there was a high ammonia removal
(45.10 and 31.63%, respectively), which was 2.89 and 3.69% higher
than that of the domesticated sludge, respectively. The reason was
that at high pH, the pore structure of the optimum dual-response nitrifying
bacteria gel spheres changes, with a more porous and sparse surface
and increased removal of ammonia nitrogen.[39]In summary, the optimum dual-response gel spheres had the
ability
to enhance the tolerance of microorganisms to unfavorable external
environments and was expected to provide a reference for developing
and applying microbial immobilization carriers.
Conclusions
In the study, we explored the optimal synthesis
conditions for
the dual-response gel spheres. The main conclusions can be summed
up as followsBy constructing an orthogonal experiment
with the composite score as the evaluation index, it was concluded
that the optimum synthesis conditions for CA gel spheres were SA concentration
of 3% (w/v), CaCl2 concentration of 2% (w/v), gelling time
of 40 h, and drop height of 14 cm. In addition, the factors affecting
the composite score of the gel spheres were ranked as follows: SA
concentration > gelling time > CaCl2 concentration
= drop
height.The swelling
and mass transfer properties
of the CA gel spheres modified with 0.6% (w/v) NaCl were significantly
improved than those of the pristine CA gel spheres.The optimal synthesis conditions for
the dual-response gel spheres were explored using the RSM: NIPAAm,
MBA1, AA, and MBA2 concentrations of 0.03% (w/v),
0.02% (w/v), 4.06% (w/v), and 0.26% (w/v), respectively.The results of the environmental change
tolerance experiment, the response experiment, and various characterization
methods (SEM, BET, and FT-IR) showed that the optimum temperature/pH
dual-response gel spheres were successfully prepared. It is hoped
that it will provide a valuable reference for the development and
application of microbial immobilization carriers, and consideration
can be given to exploring the implementation of LCST and pH control
of the material in the future.
Materials and Methods
Reagents and Instruments
SA(AR),
CaCl2(AR), NaCl(AR), ammonium persulfate (APS) (AR), and
tetramethylethylenediamine (TMEDA) (BR) were purchased from Sinopharm
Chemical Reagent Co. MBA(AR) was purchased from Sas Chemical Technology
(Shanghai) Co. NIPAAm(BR) and AA(BR) were purchased from Tricia (Shanghai)
Chemical Industry Development Co. Sodium bisulfite (SBS) (ACS) was
purchased from Beijing Bailingway Technology Co.A digital push–pull
meter (HP-50, HANDPI, China) was used to measure the mechanical strength
of the gel spheres. The structure and specific surface area of the
gel spheres were observed and analyzed by using scanning electron
microscopy (SEM) (JSM-6460LV, JEOL, Japan) and a specific surface
and porosimetry instrument (ASAP 2020, Micromertics, USA), respectively.
The changes in the gel spheres’ characteristic peaks after
modification were analyzed by Fourier transform IR (FTIR) (Nicolet
6700, Thermo Scientific, USA) to cross-check the changes noticed in
the material structure.
Preparation of Gel Spheres
The overall
process of preparing the gel spheres is presented in Figure . The specific steps are as
follows:
Figure 8
Preparation of gel spheres.
Preparation of gel spheres.
CA Gel Spheres
The SA solution
was first cooled to room temperature after complete dissolution (50–60
°C water bath) and then added drop by drop to the CaCl2 solution at a fixed height using a rubber-tipped dropper. It was
cross-linked at 4 °C for a specific time and rinsed 2–3
times with deionized water. To obtain the optimum CA gel spheres,
a 4-factor [A: SA concentration (%), B: CaCl2 concentration
(%), C: gelling time (h), and D: drop height (h)] 5-level orthogonal
experiment was used in this study. The ultimate use of the gel spheres
is to encapsulate microorganisms for the biological treatment of wastewater.
As there is no unified evaluation standard, in order to evaluate the
gel spheres quantitatively, a preliminary study was conducted by equally
assigning weights to five aspects (sphericity,[33,44,45] swelling,[46−48] mechanical properties,[49−51] oscillatory breakage rate,[44,52,53] and mass transfer properties[42,44,54]) on the basis of previous studies by other scholars (Table ). The orthogonal experimental
design factors and scoring criteria are given in Tables and 7.
Table 5
Summary of Gel Sphere Performance
carrier
performance
remarks
references
PVA–SA
sphericity
scored for
sphericity, size, and shape
(44)
CA
shape characterization
of hydrogels using spherical factors
(33)
CA
SA concentrations
were selected based on whether spherical and uniformly sized CA gel
spheres were produced
(45)
SA/PEI
swelling
characterization using the swelling rate
(46)
semi-IPN superabsorbent
nanocomposite
(47)
PVA/alginate
(48)
PAC–SA
mechanical properties
characterization using
compressive strength
(49)
3D PVA gel
beads
(50)
methyl cellulose/CA beads
(51)
PVA/SA
oscillatory
breakage rate
agitation
of gel beads at 600 rpm and final recording
of the breakage rate
(52)
PVA/PPG hydrogel
agitation
of gel beads at 2000 rpm and final
recording of the breakage rate
(53)
PVA–SA
the pellets
were placed in an isometric shaker for 48 h and the breakage was recorded
(44)
PVA–SA–diatomite
mass transfer properties
characterization using
mass transfer rates
(42)
PAC–SA
(54)
PVA–SA
the
gel spheres
were immersed in ink for 20 min and
characterized by the color shade of the central section and the radius
of immersion
(44)
Table 6
Orthogonal Experimental Table
factorsa
levels
A (%)
B (%)
C (h)
D (cm)
1
0.5
2
10
6
2
1
3
20
8
3
2
4
30
10
4
3
5
40
12
5
4
6
50
14
Note: A, B, C, and D indicate
SA
concentration, CaCl2 concentration, gelling time, and drop
height, respectively.
50–90% uniformly spherical in size (diameter = 4 mm), the rest is ellipsoidal and olive shapes, 0–20% adhesion
5–8
more than 50% non-spherical, heavily (more than 50%) adherent
0–4
swelling
swelling of 15–30
9–10
swelling of 5–15 and 30–40
5–8
swelling of 0–5 or >40
0–4
mechanical properties
mechanical strength of 20–25 N
9–10
mechanical strength of 10–20 N
5–8
mechanical strength of 0–1 N
0–4
oscillatory breakage
rate
breakage rate
of 0–10%
9–10
breakage rate of 10–50%
5–8
breakage rate >50%
0–4
mass transfer properties
actual nitrite nitrogen
concentration/theoretical nitrite nitrogen concentration in gel spheres
of 90–100%
9–10
actual nitrite nitrogen
concentration/theoretical nitrite nitrogen concentration in gel spheres
of 70–90%
5–8
actual nitrite nitrogen
concentration/theoretical nitrite nitrogen concentration in gel spheres
<70%
0–4
Note: A, B, C, and D indicate
SA
concentration, CaCl2 concentration, gelling time, and drop
height, respectively.
NaCl-Modified CA Gel
Spheres
The
optimum CA gel spheres were cast into different concentrations (0–0.9%)
of NaCl solution, left to react for 2 h, and rinsed 2–3 times
with deionized water to obtain the optimum NaCl-modified CA gel spheres.
Temperature/pH Dual-Response Gel Spheres
5 g of drained optimized NaCl-modified CA gel spheres was cast
into the temperature-modified solution [a mixture(15 mL) of NIPAAm,
MBA, APS (6.0 mg), and TMEDA (17.0 μL)], left to react for 2
h, and rinsed 2–3 times with deionized water to produce temperature-responsive
gel spheres. It was continued to be cast into a pH-modified solution
[a mixture (10 mL) of AA, MBA, APS (6.0 mg), and SBS (6.0 mg)], left
to react for 30 min, and rinsed 2–3 times with deionized water
to finally produce a temperature/pH dual-response gel sphere. Design-expert
8.0.5 software with the Box-Behnken RSM was used to determine the
relationship between the variables and the responses. NIPAAm (X1), MBA1 (X2), AA (X3), and
MBA2 (X4) concentrations were used as independent
variables and the composite score (including swelling, mechanical
properties, oscillatory breakage rate, and mass transfer properties)
as the dependent variable to finally obtain the optimum temperature/pH
dual-response gel spheres. The levels and ranges of the experimental
independent variables are given in Table . Here, MBA1 and MBA2 were the cross linker MBA added to the temperature-modified solution
and the pH-modified solution, respectively.
Table 8
Design
Factor Level Table
factor coding level
number
variables
unit
–1
0
1
X1
NIPAAm
(%)
0.03
0.93
1.83
X2
MBA1
0.01
0.02
0.03
X3
AA
0.1
2.55
5
X4
MBA2
0.01
0.23
0.45
Optimum Dual-Response
Nitrification Gel
Spheres
The sludge (from the aeration tank of a university
wastewater plant in Xi’an), which had been domesticated for
23 days, was made into a bacterial suspension (100 g/L) by centrifugation
(2000 rpm, 10 min). The mixture was added to the SA solution in a
certain ratio (VSA/Vbacteria suspension = 4:1) and mixed well. The subsequent
preparation steps were the same as those for the final preferred optimum
dual-response gel spheres.
Performance
Characterization
Swelling
20
dried gel spheres of
uniform particle size were immersed in a 0.9% NaCl solution and left
to swell at 25 °C until equilibrium reached, at which point the
gel sphere mass (We) was constant. The
formula is as followswhere We is the
weight of gel sphere after swelling equilibrium in g; Wd is the weight of gel spheres after vacuum drying in
g.
Mechanical properties
A digital
push–pull gauge was used to measure the maximum pressure borne
by the gel spheres. A uniform size gel sphere was placed on the lower
platen, and the handwheel was shaken to move the upper platen downwards
until the gel sphere was broken, and then the pressure was recorded
at this point. The average of the three measurements was the maximum
pressure to which the gel sphere was subjected.
Oscillatory breakage rate
50 intact
gel spheres were placed in equal amounts of 0.9% NaCl solution (30
mL), then put in a shaking incubator, and shaken at a constant temperature
(25 °C) at an equal frequency (200 rpm for 3 days). The gel spheres
were observed under a light microscope, and the breakage was analyzed.
The formula for oscillatory breakage rate is as follows:where S0 is number
of unbroken gel spheres before oscillation = 50; S1 is number of unbroken gel spheres after oscillation.
Mass Transfer Properties
10 g gel
spheres were added to 20 mL of nitrite solution (10 mg/L), placed
in an incubator, and shaken at constant temperature (25 °C) and
at equal frequency (200 rpm) for 2 h. The concentration of nitrite
in the solution was measured by the formula given belowwhere V1 is initial
nitrite nitrogen solution volume, 20 mL; V2 is total volume of gel spheres dosed, 10 mL; C1 is initial nitrite nitrogen solution concentration, 10 mg/L;
and C2 is nitrite nitrogen solution concentration
after 2 h, mg/L.
SEM analysis
The gel spheres were
dehydrated in a graded ethanol series [10 min in each of 20, 40, 50,
60, 70, 80, 90% (w/v) ethanol and then twice in anhydrous ethanol
to remove the final traces of water]. The dehydrated beads were then
placed in liquid nitrogen (5 min)—freeze dried (24 h) to obtain
dry gel sphere particles. It was then cut in half with a knife, sprayed
with gold, and placed on a conductive gel, and the surface structure
and profile of the gel sphere were observed using SEM with a secondary
electron detector, a scanning voltage of 20 kv, and a working distance
of 7.0 mm.
BET analysis
The gel spheres were
first treated with liquid nitrogen (5 min)—freeze dried (24
h) and then ground and sieved (80 mesh) to obtain the final dried
gel sphere powder. 0.2 g was put into an ASAP-2020 pore structure
surface area analyzer, and the sample was tested by a N2 adsorption–desorption technique. The Brunauer–Emmett–Teller
(BET) equation was used to calculate the specific surface area of
the sample, and the BJH model was used for pore size analysis.
FTIR Analysis
FTIR spectra were
recorded in the wavenumber range of 400–4000 cm using the KBr
pellet method.
Temperature/pH Response
Experiments
Three types of optimum gel spheres (optimum CA
gel spheres, optimum
NaCl modified gel spheres, and optimum dual-response gel spheres)
were investigated for swelling. Thirty vacuum-dried spheres of the
three optimum gel types were put into solutions of different temperatures
(5, 20, 30, 40, and 50 °C) or pH (2, 4, 6, 8, 10, and 12) to
investigate the variation of swelling with temperature and pH, respectively.
The temperature values of the dispersions were adjusted with a refrigerator
and a water bath thermostatic oscillator. The pH values were adjusted
with a 0.1 M HCl solution and a 0.1 M NaOH solution.The optimum
dual-response nitrifying bacteria gel spheres (20%
dosing rate) after three days of activation and the domesticated sludge
with the same amount of bacteria were put into the synthetic wastewater
(Table for specific
components) at different temperatures (4–50 °C) or pH
(4–10). Ammonia removal rate within 5 h was used as a performance
indicator to assess tolerance to external environmental changes.
Authors: M J Chalanqui; S Pentlavalli; C McCrudden; P Chambers; M Ziminska; N Dunne; H O McCarthy Journal: Mater Sci Eng C Mater Biol Appl Date: 2017-09-27 Impact factor: 7.328
Authors: Mitulkumar A Patel; Mohamed H H AbouGhaly; Jacqueline V Schryer-Praga; Keith Chadwick Journal: Carbohydr Polym Date: 2016-08-29 Impact factor: 9.381