Pectin cellulose grafted with glycidyltrimethylammoniochloride (GTMAC) was successfully obtained following the processes of depectinfibrillation and cellulose cationization using ordinary Shatian pomelo peel produced in Yongzhou, Hunan, as the raw material. This is the first report on a new type of functionalized sodium alginate-immobilized material prepared from the fibers of pomelo peel. The material was prepared by combining modified pomelo peel cellulose and sodium alginate following the processes of physical and chemical double cross-linking. The prepared material was used to embed the target bacteria to achieve the biodegradation of p-aniline. The concentration of CaCl2 was adjusted when the alginate gelled, and the alginate to yuzu peel cellulose ratio was tuned. The immobilized material-embedded bacteria help achieve the best degradation effect. Bacteria are embedded during the process of the degradation of aniline wastewater, and the functionalization of the cellulose/sodium alginate-immobilized material results in unique surface structure performance. The performance of the prepared system is better than that of the single sodium alginate-based material characterized by a large surface area and good mechanical properties. The degradation efficiency of the system is improved significantly for the cellulose materials, and the prepared materials can potentially find applications in the field of bacteria-fixed technology.

  • Pomelo peel fiber was extracted for the first time and used in the preparation of immobilized material.

  • By combining with sodium alginate, the specific surface area of the fixed material can be increased by the pomelo peel fiber with a spiral tube shape and rough surface.

  • The cationic-modified pomelo peel fiber can improve the mechanical properties and stability of the immobilized material by ionic bonding.

Aniline, one of the most important aromatic amine compounds, has been used extensively in the dye, pesticide, and pharmaceutical industries (Ashouri et al. 2021). However, if not stored and used properly, aniline leaks into the environment, causing a series of environmental problems. This can be attributed to the high toxicity of the compound (Tekle-Roettering et al. 2016). This chemical causes significant health hazards as it readily combines with hemoglobin molecules in animals. The bound hemoglobin will lose the ability to transport oxygen (Zhang et al. 2021), which in turn damages the liver and kidneys. Therefore, in 2017, aniline was officially listed as a serious hazardous compound by the International Health Organization.

Therefore, active research is being carried out to develop methods for proper aniline disposal. Many conventional methods for aniline degradation, such as membrane separation, adsorption, and chemical oxidation, have significant drawbacks. These traditional methods are cost-inefficient (Wang et al. 2021), less efficient, and cause secondary pollution (Zhao et al. 2019). Alternatively, biodegradation is considered a promising method for the removal of aniline as the method is cost-effective and environmentally friendly (Chen et al. 2021). Results obtained using the HPLC technique reveal that the biodegradation of aniline involves the degradation of aniline into catechol by bacteria, and the produced catechol is then converted to cis,cis-muconic acid (Cui et al. 2017). Over the past decades, many bacteria, such as Pseudomonas (Tanaka et al. 2009), Acinetobacter (Hou et al. 2018), and Pigmentiphaga daeguensis (Huang et al. 2018), that can degrade aniline have been identified. However, the efficiency of the process of bacterial biodegradation often depends on the survival of microorganisms as the microorganisms often die due to the toxicity of the contaminants (Pinheiro et al. 2022). The process of free bacterial biodegradation is disadvantageous for recycling products in industries, as the separation process is difficult to execute. Therefore, to solve these problems, it is important to develop bacterial immobilization technology (Mehrotra et al. 2021).

As a promising method, the bacterial immobilization technology has attracted the attention of many scholars as it boasts high bacterial density, stability, and good separation characteristics (Beltrán-Flores et al. 2022; Xue et al. 2022). It has been previously reported (Ngah & Fatinathan 2008) that the materials and procedures used for immobilization are crucial for the application of the immobilized cell system (Elisangela et al. 2009; Sharma et al. 2011). Many natural polymer materials, such as chitosan (Denkbaş & Odabaşi 2000), agar, and alginate, have been used for immobilization as they exhibit good biocompatibility. Moreover, these are cheap materials that can be easily processed (Tanaka et al. 2009). Under conditions of immobilization, bacteria are confined to the substrate for better protection and proliferation. Alginate, a linear polysaccharide composed of a-L-mannuronic acid (M unit) and b-D-guluronic acid (G unit), is widely present in a variety of seaweeds, is considered an excellent carrier for bacterial immobilization, as it is non-toxic, can be easily prepared, and obtained from convenient sources. The presence of numerous carboxyl groups on the walls of alginate promotes the reaction of the molecule with other functional groups (Guo et al. 2020). Although alginate is considered the most promising material for cell immobilization, rapid bacterial reproduction, weak transport properties at high bacterial density (Cui et al. 2017), and mechanical fragility of the substrate limit the application of the material. Hence, it is essential to improve the properties of the substrate to achieve high porosity and mechanical strength. Pomelo cellulose (PC) has a unique pipe-like network structure. It is characterized by good biocompatibility, a large specific surface area, and stable chemical properties (Tang et al. 2020). A combination of PC and alginate can be used to integrate the advantages of the two materials. Therefore, alginate can be blended with PC to overcome the drawbacks of alginate and combine the good characteristics of both polymers. When alginate is mixed with cellulose, a strong ionic interaction is generated between the amino groups in cellulose and the carboxyl groups in alginate. This results in the formation of a polyelectrolyte complex (PEC), which imparts good mechanical properties to the support (Shu & Zhu 2002).

This is the first report that describes the method of the formation of a composite fiber ball from the fibers present in the inner layer of grapes. The material was formed following the electrostatic double cross-linking method (Hrenovic et al. 2009). The fibers were cross-linked with sodium alginate, and the characteristics of the obtained material were compared with the characteristics of ordinary sodium alginate gel beads and pomelo fiber/alginate complexes. The rubber pellets exhibit better permeability than the other systems, and the specific surface area of these pellets is larger than the specific surface area of the other systems. This, in turn, imparts protection and growth-promoting properties during bacterial immobilization to the composite fiber-based spheres. The rate of the growth and degradation of bacteria under these conditions far exceeds those recorded in the presence of sodium alginate gel beads. The results reported herein provide a platform for the realization of the application of biomass materials in the field of bacterial immobilization technology.

Materials

Commercially available analytical grade chemicals were used. Glyceryltrimethylammonium chloride (GTMAC), dimethyl sulfoxide (DMSO), sodium alginate, NaOH, anhydrous sodium metasilicate, ammonium sulfamate, sodium polyphosphate, sodium bicarbonate, Naf-ethylamine hydrochloride, NH4Cl, NaCl, MgSO4·7H2O, anhydrous sodium acetate, CaCl2, K2HPO4, yeast extract, H2O2, H2SO4, and ethyl alcohol were purchased from the market.

Deionized water, obtained from self-made RO/EDI equipment, was used for the experiments.

Preparation of PC

Grapefruit skin fiber is first peeled off of ordinary Shatian pomelo obtained from Yongzhou, Hunan Province (He et al. 2019). The outer layer of the peel containing a large amount of pectin is removed, and the inner layer of the grapefruit peel is placed at a temperature of 45 °C. The oven was dried for 48 h, the inner layer of the peeled water was powdered using a stirrer, and the sample was sieved and dried for 2 h. The obtained product was alkalized to remove impurities. The cellulose to deionized water mass ratio was maintained at 1:25 for 1 h at 25 °C, and the peel fibers were pre-soaked uniformly in sulfuric acid. Following this, it was treated with a solution containing NaOH (7 g/L), Na2SiO3 (2%), and sodium polyphosphate (0.25%). The cellulose to sodium hydroxide mass ratio was 1:15, and the high-temperature cooking method was followed at 100 °C for 2 h in a water bath (Liu et al. 2017). The secondary alkali treatment process increases the concentration of the alkalizing agent. The NaOH concentration increases to 11 g/L, and the Na2SiO3 content increases to 3% under these conditions. Other experimental conditions were kept the same as the primary alkali treatment condition. Finally, it was bleached with H2O2 and then rinsed 5–6 times with deionized water.

Cationization of PC

The prepared fibers were cationized. During this process, 1,000 mg of water-dispersed dry, pre-treated PC and 50 mg of sodium hydroxide powder were thoroughly mixed using a mortar and pestle at room temperature for 5 min. The solid mixture was then transferred to a polyethylene bag, and this was followed by the addition of solvent (water in various volume ratios or water/DMSO mixtures). A cationizing agent (GTMAC) was added to the previous mixture dropwise, and the sample was kneaded evenly by hand. Subsequently, the reaction mixture was kept in a thermostatic ultrasonic water bath at 65 °C for 4 h. All other conditions were similar to the conditions of the wet process. After 4 h, the product was precipitated using 95% ethanol. It was purified and concentrated following the protocols used in the wet method.

Cultivation of photosynthetic bacteria

Rhodopseudomonas palustris culture was purchased from Weifang Zhongtian Technology Feed Co., Ltd. It was directly inoculated into the special nutrient solution of photosynthetic bacteria (PSB) through long-term tests. This process was followed as their origin was different (Sun et al. 2012). The liquid culture medium used in this experiment was self-prepared. One liter of the nutrient solution contained 0.1 g of NH4Cl, 0.5 g of NaCl, 3 g of sodium acetate, 0.1 g of MgSO4·7H2O, 0.1 g of CaCl2, 0.2 g of K2HPO4, and 0.5 g of yeast extract. PSB may have community differences in proliferation habits, so the growth factors are regulated. The pH of the nutrient salts proliferating the PSB, growth temperature, light intensity, bacterial inoculum, presence or absence of light, and carbon sources were regulated.

Domestication of PSB

Industrialized PSB may have some intolerance to aniline that is a highly toxic organic compound. Therefore, it is necessary to carry out a domestication process. According to the principle of domestication of PSB (Li et al. 2019), for a certain amount of inoculum, a concentration of approximately 20% of the target degradation concentration is added to the sample at the same time as the nutrient solution. Aniline is sampled every day under suitable conditions to observe the growth of the PSB. When the PSB gradually adapt to the concentration of the aniline nutrient solution, the domesticated bacteria in the nutrient salt are collected and inoculated under conditions of the target degradation concentration (approximately 40%). The method is repeated until it reaches the target concentration (Sheldon 2007). At this time, the bacterial liquid is the domesticated bacterial stock solution, which is used in a subsequent aniline degradation test.

Sodium alginate/PC composite gel bead

A biological grade sodium alginate is mixed with deionized water in a certain proportion. Following this, it is heated until it dissolves. The mixing process is conducted according to the controlled proportion and the secondary alkalized pomelo fiber. Subsequently, the sample is heated and stirred at 40 °C for 12 h. It is covered with plastic to prevent moisture loss. At the end of the heating process, the heat is turned off, and the temperature of the solution is allowed to come down to room temperature. A certain amount of the bacterial stock is added quickly, and the sample is stirred at high speed for 10 min to distribute the bacteria evenly. Subsequently, the mixed solution is injected into the CaCl2 solution at a constant rate using a syringe (Shankar & Rhim 2018). After calcification, the sample is washed directly and placed in an oven at 60 °C to obtain the sodium alginate/PC composite gel beads, as shown in Figure 1.

Aniline degradation test

The experiments using PSB were carried out on a shaker containing a triangular bottle of volume 250 mL. In the condition optimization experiment, the bacterial reserve solution (inoculated at 30%) was added to the triangular vial (250 mL), and the solution of aniline at an initial concentration of 500 mg/L was added to it. The samples were placed in a shaker at 150 r/min, and bacterial growth rates, stem cell weight, and aniline concentration were measured to assess the influence of pH, temperature, and other factors on the process of aniline degradation.

The gel beads of sodium alginate/grapefruit cellulose composite were put in 100 mL simulated aniline wastewater (1,000 mg/L), and orthogonal experiments were carried out to determine the optimum content of cellulose, sodium alginate, and CaCl2. The effects of dissolved oxygen (DO) and light intensity on the aniline degradation process were then assessed under the optimal ratio, and the repeatability of cellulose pellets was also established.

As aniline participates in diazotization reactions with nitrite under acidic conditions (pH 1.5–2.0), it is coupled with N-(1-naphthyl)ethylenediamine hydrochloride to form a purple dye. The colorimetric method is used for analysis. The sample (0.5–30 μg of aniline) is taken into a 25 mL stoppered test tube and diluted to 10 mL with distilled water. KHSO4 is added to the system to adjust the pH in the range of 1.5–2.0. Following this, a drop of the configured nitrous acid is added. A solution of sodium was added, and the mixture was shaken well. The reaction was allowed to proceed for 2–3 min, following which 0.5 mL of ammonium sulfamate solution was added to the mixture. Subsequently, the mixture was shaken well, and it was allowed to stand for 3 min. N-(1-naphthyl)ethylenediamine hydrochloride (1 mL) was added to the mixture, and the sample was diluted to 25 mL with distilled water. It was reacted at a constant temperature for 30 min. The absorbance was measured at 545 nm, and the change in concentration was calculated by analyzing the absorbance/concentration standard curve.
(1)

Here, Ct (mg/L) and C0 (mg/L) represent the residual concentrations of aniline at time t (h) and in the initial, respectively.

Characterization

The morphology and structure of the pomelo fiber post-treatment and the alginate-cellulose beads were analyzed using a SU8010 scanning electron microscope (SEM) (Hitachi, Japan) at 15 kV. The structural changes of the common sodium alginate gel sphere and the pomeloid fiber sodium alginate composite gel sphere are shown in the image recorded using the Tecnai G2 F30S-Twin transmission electron microscope (TEM) system (Philips-FEI, The Netherlands). The changes in the composition and functional groups of different pomelo fibers following alkalization treatment and NH3·H2O grafting were determined using a Nicolet 6700 Fourier transform infrared (FTIR) (Thermo Nicolet, America) spectrometer. The data were recorded in the wavenumber range of 450–4,000 cm−1 (Zhang et al. 2018). The compositional structure of the gel pellets and the composite fiber spheres were changed. The chemical structure of the sample was further verified using the X-ray photoelectron spectroscopy (XPS) technique (PHI-5000C, USA). The surface area and the pore size distribution were analyzed using the Brunauer–Emmet–Teller method (Quantachrome, Autosorb-Iq-MP).

SEM analysis

The morphological changes of the pomelo fibers under conditions of alkali treatments were studied. It can be seen from Figure 2(a) and 2(d) that when the pomelo fiber is not treated with alkali, the surface of the fiber remains covered (Figure 2) with a large amount of pectin and gelatin. Although it presents porous structures, the surface appears relatively smooth. Following alkalization, the surface of the pomelo fiber began to become rough and wrinkled (Figure 2(b) and 2(c)). Partial removal occurs, and uneven wrinkles appear on the fiber surface under alkaline treatment conditions. In addition, the fiber may be partially distorted during the alkali treatment process (Shao et al. 2018). After two cycles of high-concentration alkali treatment, pectin, wax, and lignin present on the surface of the peel are removed (Figure 2(d)). Bare tubular fibers can be seen under these conditions. It promotes the attachment of bacteria and the transfer of substances.
Figure 1

Schematic diagram of the sodium alginate/PC composite gel bead formation process.

Figure 1

Schematic diagram of the sodium alginate/PC composite gel bead formation process.

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Figure 2

(a) SEM image recorded for PC. (b) SEM image recorded for primary alkalization pomelo cellulose (PAPC). (c) SEM image recorded for secondary alkalization and primary alkalization (SAPC). (d) SEM image recorded for ammoniated secondary alkalization primary alkalization.

Figure 2

(a) SEM image recorded for PC. (b) SEM image recorded for primary alkalization pomelo cellulose (PAPC). (c) SEM image recorded for secondary alkalization and primary alkalization (SAPC). (d) SEM image recorded for ammoniated secondary alkalization primary alkalization.

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As can be seen from Figure 3(a) and 3(b), when sodium alginate is double cross-linked with cellulose obtained from the peels of cationized naringelo presenting a hollow spiral tubular structure, numerous spiral channels are formed on the surface of the prepared composite material. The number of spinal channels in the composite material is higher than the number of channels in the system obtained from pure sodium alginate. Analysis of the SEM images revealed that the surface of the fibers of spherical sodium alginate/pomelo peel composite (Figure 3(d)) was coarser and more porous than the surface of the pure sodium alginate material (Figure 3(c)). The former is more conducive to bacterial attachment and substrate transfer than the latter.
Figure 3

(a) SEM image of the surface of the alginate beads. (b) SEM image of the surface of the alginate/pomelo cellulose beads. (c) SEM image of the inner surface of the alginate beads. (d) SEM image of the inner surface of the alginate/pomelo cellulose beads.

Figure 3

(a) SEM image of the surface of the alginate beads. (b) SEM image of the surface of the alginate/pomelo cellulose beads. (c) SEM image of the inner surface of the alginate beads. (d) SEM image of the inner surface of the alginate/pomelo cellulose beads.

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FTIR results

The cross-linking between the main components of the pomelo fiber layer is revealed by the FTIR profiles of the pomelo fibers subjected to various degrees of alkali treatment (Debnath et al. 2018). The broad absorption band around 3,375 cm−1 can be attributed to the –OH stretching vibration in pectin and cellulose (Figure 4). The wide absorption band at approximately 2,900 cm−1 can be attributed to the CH stretching vibration of the fibers, and the broad absorption band at approximately 1,700 cm−1 can be primarily attributed to the stretching vibration of the C = C unit on the aromatic ring present in cellulose and pectin substrates. The wide absorption band at 1,100 cm−1 corresponds to the stretching vibration of the CO unit in cellulose. In addition, the presence of the broad absorption band at 1,750 cm−1, which appeared only in the non-treated pomelo fiber, indicates that ester-rich pectin and wax systems were removed post-alkali treatment. The –OH group on cellulose facilitates the formation of hydrogen and covalent bonds.
Figure 4

FTIR profiles recorded for PC before and after alkalization and ammonia treatment.

Figure 4

FTIR profiles recorded for PC before and after alkalization and ammonia treatment.

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As can be seen in Figure 5, the intensity of the absorption peak of the composite at 1,750 cm−1 was different from the intensity of the corresponding peak attributable to sodium alginate alone. This change can be attributed to the reaction of the carboxyl and the amino groups present in the pomelo peel fiber and the cationized sodium alginate system.
Figure 5

FTIR profiles recorded for citron after cationization and double cross-linking.

Figure 5

FTIR profiles recorded for citron after cationization and double cross-linking.

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Brunauer-Emmett-Teller (BET) analysis

The specific surface area increased from 5.28 to 12.45 m2/g when sodium alginate was incorporated into cationic pomelo peel cellulose. Analysis of the pore size distribution (Figure 6) revealed the mesoporous structure of the system. The SEM images revealed that the number of holes is larger than that of channels. The surfaces were rough, and the surface area was large. The large surface area facilitates a high rate of material transport at high density, resulting in the generation of a large gap in the degradation levels of two anilines in the later stages. The degradation effect exerted in this case is significantly better than that recorded for ordinary alginate.
Figure 6

BET and pore size distribution of (a) the alginate beads and (b) the alginate/PC beads.

Figure 6

BET and pore size distribution of (a) the alginate beads and (b) the alginate/PC beads.

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XPS analysis

We used the XPS technique to analyze the surface of grapefruit fibers that were modified using the cationizing reagent GTMAC. The characteristic peak of the ammonium cation appeared at 400 eV (Figure 7), indicating that GTMAC reacted with PC and 2,3-epoxy-propyl trimethylammonium chloride was cross-linked to the surface of grapefruit fiber. It was also revealed that the modified PC fiber contained a large number of channels, and it was characterized by a rough surface, a loose structure, and a certain network structure (Figures 6 and 7).
Figure 7

XPS profile recorded for the PC and the cationized PC systems.

Figure 7

XPS profile recorded for the PC and the cationized PC systems.

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Optimization of the aniline degradation parameters

PSB was used for aniline degradation experiments, and it was designed according to the univariate principle. The pH and temperature were changed to obtain the best degradation conditions of aniline.

Effect of pH on the process of aniline degradation

The growth, proliferation, and reproduction of bacteria and the degradation of aniline are significantly affected by pH conditions. It also affects the binding between bacteria and the active sites of organic compounds (Figure 8(a)). The concentrations of the aniline-degrading enzymes in bacteria remain at a certain value (Li et al. 2017). It can be seen from the experimental data that when the pH is equal to 6.5, the degradation effect of aniline is relatively poor, and it can be potentially attributed to the fact that acid inhibits the growth and metabolic activity of bacteria (Sharma et al. 2017). At pH 7.5, the maximum degradation of aniline by bacteria is recorded. It can be attributed to the fact that photosynthetic bacteria grow rapidly at this pH.
Figure 8

Rate of aniline degradation and the dry cell weight at different conditions. (a) temperature, (b) pH, and (c) time.

Figure 8

Rate of aniline degradation and the dry cell weight at different conditions. (a) temperature, (b) pH, and (c) time.

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Effect of temperature on the process of aniline degradation

Under normal circumstances, the degradation efficiency of aniline and the growth of photosynthetic bacteria are one-to-one. The aniline cannot be efficiently degraded as bacteria do not grow efficiently under these conditions. It has been reported that the optimal temperature for the growth of photosynthetic bacteria is approximately 30 °C. Four sets of temperatures (25, 30, 35, and 40 °C) were selected as parameters to study the effect of temperature on the process of degradation of aniline. The experimental results (Figure 8(b)) are consistent with the results reported in the literature. The maximum extent of aniline degradation is achieved at 30 °C, and at 40 °C, the degradation effect decreases slightly. Thus, it can be inferred that temperature affects the activity of the aniline-degrading enzyme.

Effect of time on the process of aniline degradation

As shown in Figure 8(c), PSB growth presents a lag period of 0–24 h. This is followed by a logarithmic period of 24–48 h, in which the dry weight of the cell increases significantly. The cells grow rapidly at approximately 48 h. When the degradation time reaches 3 days, the degradation rate of aniline reaches 67.2%. Following this, the degradation rate becomes stable.

Preparation of composite pellets

The concentrations of ionized pomelo fiber, alginate, and CaCl2 have a great influence on the density, mass transfer performance, and metabolism of pomelo fiber/alginate composite fiber spheres. The three components interact with each other. If good-performance composite microspheres are to be prepared, the optimal composition ratio should be determined by comprehensively testing several factors. The orthogonal test of three factors and four levels was conducted according to Table 1, and the experimental results are shown in Figure 2. The higher the R-value, the better the effect of the microspheres prepared by changing the ratio. The order of influence was A > B > C. This indicated that the cellulose content was the most important factor that affected the degradation process. The optimal concentrations for the microspheres that could be used to achieve high degradation rates are presented in Figure 9 (cellulose 3%, sodium alginate 2%, and calcium chloride 2.5%).
Figure 9

Analysis diagram of aniline degradation factor effect curve. (a) Modified PC, (b) sodium alginate, and (c) CaCl2.

Figure 9

Analysis diagram of aniline degradation factor effect curve. (a) Modified PC, (b) sodium alginate, and (c) CaCl2.

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The addition of sodium alginate and polyethylene glycol (PEG) increased the viscosity of the liquid and the compactness of the microspheres. This affects the mass transfer of substrates and products and reduces the activity of PSB, eventually reducing the degradation rate. The lower the content of sodium alginate and PEG, the looser the microspheres. The decomposition and destruction of the microspheres are promoted under these conditions.

Pomelo fiber, a kind of biomass fiber produced after two alkalization treatment cycles and cation modification, has a great influence on the bioactivity of alginate gel spheres and the extent of the adsorption of bacteria. In particular, the embedded photosynthetic bacteria transformed into composite gel microspheres, which exerted a strong synergistic effect on mass transfer performance. The gradual increase in the pomelo fiber dosage resulted in an increase in the aniline degradation efficiency (Table 2). The cellulose content was increased from 2 to 3% (Figure 9(a)), and the maximum extent of aniline degradation was recorded under these conditions. Following this, the efficiency gradually decreased. The presence of cellulose can increase the load of bacteria, protect bacteria, and increase the running time of bacteria in simulated wastewater. High cellulose content will reduce the mechanical properties of the pellets, reduce the degradation effect, and is not conducive to the growth of embedded bacteria. When the dosage of sodium alginate was gradually increased, the degradation efficiency first increased (Figure 9(b)). It reached the maximum value when the sodium alginate content was 2%. This can be potentially attributed to the low content of sodium alginate, which results in a weakening of the adhesion strength of the composite fiber microspheres. Eventually, the mechanical properties of the composite fiber ball deteriorate. A large number of internal channels is formed when the concentrations of sodium alginate and calcium ions are increased at this point (Figure 9(c)). A loose structure characterizes the material, and the mass transfer and protection performance of the composite microsphere ball is the best at this point. The best aniline degradation effect is recorded under these conditions. If the pomelo fiber content is too large and the sodium alginate content is too low, the mechanical properties of the microspheres will continue to deteriorate. This will result in the cracking and crushing of the pellets. This will eventually result in the reduction of the degradation effect. However, if the concentration of sodium alginate and CaCl2 is too high, the density of the fiber microspheres will increase, affecting the process of the exchange of bacterial substances. This will also affect the activity of the aniline degradation enzyme, resulting in a rapid decrease in the aniline degradation rate. In this experiment, there was some correlation between the number of sodium alginate/PC composite gel beads and modified PC content, as shown in Table 3.

Table 1

Factors and levels of the orthogonal test for L16 (4,3)

LevelFactor
ABC
Modified PC content (%)Sodium alginate content (%)CaCl2 content (%)
1.5 1.5 
2.5 2.5 
LevelFactor
ABC
Modified PC content (%)Sodium alginate content (%)CaCl2 content (%)
1.5 1.5 
2.5 2.5 
Table 2

Results of orthogonal experiments for L16 (4,3)

ABCDegradation rate (%)
Modified PC content (%)Sodium alginate content (%)CaCl2 content (%)
1.5 1.5 39.1 ± 0.22 
66.7 ± 0.33 
2.5 2.5 53.4 ± 0.23 
57.6 ± 0.29 
1.5 72.7 ± 0.45 
1.5 84.7 ± 0.52 
2.5 80.7 ± 0.51 
2.5 77. ± 0.48 
1.5 2.5 67.4 ± 0.39 
10 71.0 ± 0.37 
11 2.5 1.5 74.3 ± 0.35 
12 68.9 ± 0.40 
13 1.5 42.7 ± 0.21 
14 2.5 77.5 ± 0.46 
15 2.5 56.4 ± 0.23 
16 1.5 47.5 ± 0.25 
K1 216.8 ± 0.27 221.9 ± 0.32 245.6 ± 0.34  
K2 315.5 ± 0.49 299.9 ± 0.42 264.7 ± 0.35  
K3 281.6 ± 0.38 264.8 ± 0.33 275.7 ± 0.39  
K4 224.1 ± 0.29 251.4 ± 0.36 252 ± 0.35  
R 91.4 78.0 30.1  
ABCDegradation rate (%)
Modified PC content (%)Sodium alginate content (%)CaCl2 content (%)
1.5 1.5 39.1 ± 0.22 
66.7 ± 0.33 
2.5 2.5 53.4 ± 0.23 
57.6 ± 0.29 
1.5 72.7 ± 0.45 
1.5 84.7 ± 0.52 
2.5 80.7 ± 0.51 
2.5 77. ± 0.48 
1.5 2.5 67.4 ± 0.39 
10 71.0 ± 0.37 
11 2.5 1.5 74.3 ± 0.35 
12 68.9 ± 0.40 
13 1.5 42.7 ± 0.21 
14 2.5 77.5 ± 0.46 
15 2.5 56.4 ± 0.23 
16 1.5 47.5 ± 0.25 
K1 216.8 ± 0.27 221.9 ± 0.32 245.6 ± 0.34  
K2 315.5 ± 0.49 299.9 ± 0.42 264.7 ± 0.35  
K3 281.6 ± 0.38 264.8 ± 0.33 275.7 ± 0.39  
K4 224.1 ± 0.29 251.4 ± 0.36 252 ± 0.35  
R 91.4 78.0 30.1  
Table 3

Relationship between the number of sodium alginate/PC composite gel beads and modified PC content

Number of sodium alginate/PC composite gel beadsModified PC content (%)
35–40 2.0 
50–60 3.0 
70–80 4.0 
90–100 5.0 
Number of sodium alginate/PC composite gel beadsModified PC content (%)
35–40 2.0 
50–60 3.0 
70–80 4.0 
90–100 5.0 

Effect of degradation conditions on the degradation rate

Effect of DO

It can be seen from Figure 10 that the degradation rate of microspheres embedded in photosynthetic bacteria is significantly affected by light intensity. DO is controlled by aeration volume, and the removal rate of aniline increases with an increase of DO in the solution. This can be attributed to the fact that the metabolism of PSB requires a large amount of oxygen, and an increase in DO can improve the removal rate of aniline. Many holes and fixed channels are present in the microspheres, and these promote the process. An increase in the number of microbubbles results in an increase in the gas–liquid contact area. The production of aniline and the movement of bacterial metabolites into and out of these channels were promoted under these conditions. The experimental results are shown in Figure 10. When the DO was 2.0 mg/L, the microsphere degradation rate reached the maximum value of 91.7%. An increase in the number of microbubbles can result in an increase in the gas–liquid contact area. The uniform suspension movement of microspheres in wastewater is promoted under these conditions. This facilitates the absorption of nutrients and the dispersal of metabolites. If the value of DO exceeds the threshold, the degradation rate decreases. This can be potentially attributed to the process of oxygen suppression.
Figure 10

Effect of DO concentration on the degradation rate of aniline.

Figure 10

Effect of DO concentration on the degradation rate of aniline.

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Effect of illumination intensity

Since the embedded photosynthetic bacteria are sensitive to light in the free state, different intensities of light were used to conduct the tests to observe the degradation of cellulose microspheres made of photosynthetic bacteria. The process of aniline degradation was carried out under conditions of varying aeration and light intensity (Figure 11). The experiment showed that the degradation rate of the microspheres was improved to a certain extent when the light intensity was increased. An increase in light intensity resulted in an increase in the degradation rate. The aeration volume was selected to be 2 mg/L. The maximum degree of degradation (96.3%) was recorded when the light intensity was 4,000 Lx. In the experiment, it was found that the optimal light intensity was different with different aeration volumes. When the aeration volume was 1 mg/L, the degradation rate at 3,000 Lx was 76.7%. When the aeration rate was 3 mg/L, the degradation rate at a light intensity of 4,000 Lx was 91.1%. Thus, the degree of aeration exerts a greater impact on the degradation rate than the light intensity.
Figure 11

Effect of illumination intensity on the degradation rate of aniline.

Figure 11

Effect of illumination intensity on the degradation rate of aniline.

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Figure 12

Reusability of alginate/modified PC microspheres.

Figure 12

Reusability of alginate/modified PC microspheres.

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Reusability of alginate/modified PC microspheres

As the photosynthesizing bacteria embedded in cellulose microspheres dynamically decompose aniline, cellulose microspheres cannot be used for prolonged periods. We tested the reusability of the prepared fiber microspheres. The optimized preparation conditions of microspheres are presented (DO: 2 mg/L; light intensity: 400 Lx; degradation rate of aniline: 200.0 mg/L). The experiments were conducted with cellulose (3.0%), sodium alginate (2%), and calcium chloride (2.5%), as shown in Figure 12. After continuous use, the degradation rate gradually increased, and the degradation rate was 96.1% after five cycles. The rate decreased to 86.3% after eight cycles. Thus, the material exhibits good stability.

We extracted grapefruit skin fiber and used it to develop the bio-immobilization technology (Jiang et al. 2018). The aniline degradation efficiency of the sodium alginate/PC composite gel beads was higher than that of the simple sodium alginate gel pellet. SEM, FTIR, XPS, and BET techniques were used to reveal the successful extraction of the material and the unique surface structure properties of pomelo peel fibers. Unique biomass transfer characteristics in sodium alginate/PC composite gel beads were also observed. The maximum extent of aniline degradation by bacteria was achieved at 30 °C at pH of 7.5 in the presence of light (4,000 Lx, DO 2.0 mg/L). The sodium alginate content was 2%, the CaCl2 content was 2%, and the modified PC content was 3%. The mass ratio was 5:1. The results reported herein reveal that plant fibers can be used for bacterial immobilization. Immobilization of natural polymer and organic synthetic polymer can be achieved.

The authors thank the National Science Foundation of China (Grant No. 21736009), the Zhejiang Public Welfare Research Project (Grant No. LGF19B070005), the Basic Public Welfare Research Program of Zhejiang Province (Grant No. 2021C03169), and the Scientific Research Foundation of Zhejiang University of Technology (201910337011) for financial assistance.

All relevant data are included in the paper or its Supplementary Information.

The authors declare there is no conflict.

Ashouri
R.
,
Rasekh
B.
,
Kasaeian
A.
,
Sheikhpour
M.
,
Yazdian
F.
&
Dehghani Mobarakeh
M.
2021
Effect of ZnO-based nanophotocatalyst on degradation of aniline
.
Journal of Molecular Modeling
27
(
3
),
1
14
.
Beltrán-Flores
E.
,
Pla-Ferriol
M.
,
Martínez-Alonso
M.
,
Gaju
N.
,
Blánquez
P.
&
Sarrà
M.
2022
Fungal bioremediation of agricultural wastewater in a long-term treatment: biomass stabilization by immobilization strategy
.
Journal of Hazardous Materials
439
,
129614
.
Chen
H.
,
Sun
C.
,
Liu
R.
,
Yuan
M.
,
Mao
Z.
,
Wang
Q.
,
Zhou
H.
,
Cheng
H.
,
Zhan
W.
&
Wang
Y.
2021
Enrichment and domestication of a microbial consortium for degrading aniline
.
Journal of Water Process Engineering
42
,
102108
.
Cui
D.
,
Shen
D.
,
Wu
C.
,
Li
C.
,
Leng
D.
&
Zhao
M.
2017
Biodegradation of aniline by a novel bacterial mixed culture AC
.
International Biodeterioration & Biodegradation
125
,
86
96
.
Denkbaş
E. B.
&
Odabaşi
M.
2000
Chitosan microspheres and sponges: preparation and characterization
.
Journal of Applied Polymer Science
76
(
11
),
1637
1643
.
Elisangela
F.
,
Andrea
Z.
,
Fabio
D. G.
,
de Menezes Cristiano
R.
,
Regina
D. L.
&
Artur
C.-P.
2009
Biodegradation of textile azo dyes by a facultative Staphylococcus arlettae strain VN-11 using a sequential microaerophilic/aerobic process
.
International Biodeterioration & Biodegradation
63
(
3
),
280
288
.
Guo
X.
,
Wang
Y.
,
Qin
Y.
,
Shen
P.
&
Peng
Q.
2020
Structures, properties and application of alginic acid: a review
.
International Journal of Biological Macromolecules
162
,
618
628
.
He
J.
,
Zhang
W.
,
Ren
X.
,
Xing
L.
,
Chen
S.
&
Wang
C.
2019
Preparation of different activated sludge immobilized carriers and their organic wastewater treatment performance by microbial community
.
Environmental Engineering Science
36
(
5
),
604
613
.
Hrenovic
J.
,
Ivankovic
T.
&
Tibljas
D.
2009
The effect of mineral carrier composition on phosphate-accumulating bacteria immobilization
.
Journal of Hazardous Materials
166
(
2–3
),
1377
1382
.
Huang
J.
,
Ling
J.
,
Kuang
C.
,
Chen
J.
,
Xu
Y.
&
Li
Y.
2018
Microbial biodegradation of aniline at low concentrations by Pigmentiphaga daeguensis isolated from textile dyeing sludge
.
International Biodeterioration & Biodegradation
129
,
117
122
.
Li
J.
,
Li
C.
,
Li
X.
,
Wang
N.
,
Ji
S.
&
An
Q.-F.
2019
3D re-crosslinking of an acid-resistant layer on NaA tubular membrane for application in acidic feed
.
Journal of Membrane Science
589
,
117259
.
Liu
S.
,
Bastola
A. K.
&
Li
L.
2017
A 3D printable and mechanically robust hydrogel based on alginate and graphene oxide
.
ACS Applied Materials & Interfaces
9
(
47
),
41473
41481
.
Mehrotra
T.
,
Dev
S.
,
Banerjee
A.
,
Chatterjee
A.
,
Singh
R.
&
Aggarwal
S.
2021
Use of immobilized bacteria for environmental bioremediation: a review
.
Journal of Environmental Chemical Engineering
9
(
5
),
105920
.
Ngah
W. S. W.
&
Fatinathan
S.
2008
Adsorption of Cu (II) ions in aqueous solution using chitosan beads, chitosan–GLA beads and chitosan–alginate beads
.
Chemical Engineering Journal
143
(
1–3
),
62
72
.
Pinheiro
L. R. S.
,
Gradíssimo
D. G.
,
Xavier
L. P.
&
Santos
A. V.
2022
Degradation of Azo dyes: bacterial potential for bioremediation
.
Sustainability
14
(
3
),
1510
.
Shao
Z.
,
Rong
Q.
,
Chen
F.
&
Qiao
X.
2018
High-spatial-resolution ultrasonic sensor using a micro suspended-core fiber
.
Optics Express
26
(
8
),
10820
10832
.
Sharma
S.
,
Munjal
A.
&
Gupta
S.
2011
Comparative studies on decolorization of textile Azo dyes by different bacterial consortia and pure bacterial isolate
.
Journal of Pharmacy Research
4
(
9
),
3180
3183
.
Sheldon
R. A.
2007
Enzyme immobilization: the quest for optimum performance
.
Advanced Synthesis & Catalysis
349
(
8–9
),
1289
1307
.
Sun
J.-Y.
,
Zhao
X.
,
Illeperuma
W. R. K.
,
Chaudhuri
O.
,
Oh
K. H.
,
Mooney
D. J.
,
Vlassak
J. J.
&
Suo
Z.
2012
Highly stretchable and tough hydrogels
.
Nature
489
(
7414
),
133
136
.
Tanaka
T.
,
Hachiyanagi
H.
,
Yamamoto
N.
,
Iijima
T.
,
Kido
Y.
,
Uyeda
M.
&
Takahama
K.
2009
Biodegradation of endocrine-disrupting chemical aniline by microorganisms
.
Journal of Health Science
55
(
4
),
625
630
.
Tekle-Roettering
A.
,
von Sonntag
C.
,
Reisz
E.
,
Vom Eyser
C.
,
Lutze
H. V.
,
Tuerk
J.
,
Naumov
S.
,
Schmidt
W.
&
Schmidt
T. C.
2016
Ozonation of anilines: kinetics, stoichiometry, product identification and elucidation of pathways
.
Water Research
98
,
147
159
.
Wang
G.
,
Zhang
H.
,
Wang
W.
,
Zhang
X.
,
Zuo
Y.
,
Tang
Y.
&
Zhao
X.
2021
Fabrication of Fe–TiO2–NTs/SnO2–Sb–Ce electrode for electrochemical degradation of aniline
.
Separation and Purification Technology
268
,
118591
.
Xue
J.
,
Liu
Y.
,
Shi
K.
,
Qiao
Y.
,
Cheng
D.
,
Bai
Y.
,
Shen
C.
&
Jiang
Q.
2022
Responses of seawater bacteria in the bioremediation process of petroleum contamination by immobilized bacteria
.
Journal of Environmental Chemical Engineering
10
(
2
),
107133
.
Zhang
P.
,
Yang
H.
,
Lim
K.-S.
,
Ahmad
H.
,
Rong
Q.
,
Tian
Q.
&
Ding
X.
2018
Temperature-independent hygrometry using micromachined photonic crystal fiber
.
Applied Optics
57
(
15
),
4237
4244
.
Zhang
C.
,
Chen
H.
,
Xue
G.
,
Liu
Y.
,
Chen
S.
&
Jia
C.
2021
A critical review of the aniline transformation fate in azo dye wastewater treatment
.
Journal of Cleaner Production
321
,
128971
.
Zhao
Z.
,
An
H.
,
Lin
J.
,
Feng
M.
,
Murugadoss
V.
,
Ding
T.
,
Liu
H.
,
Shao
Q.
,
Mai
X.
&
Wang
N.
2019
Progress on the photocatalytic reduction removal of chromium contamination
.
The Chemical Record
19
(
5
),
873
882
.
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