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The treatment of aniline in aqueous solutions by gamma irradiation

  • Li Jia-Tong , Ling Yong-Sheng , Shan Qing , Hei Da-Qian , Zhao Dan und Jia Wen-Bao EMAIL logo
Veröffentlicht/Copyright: 20. Januar 2017
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Abstract

A laboratory investigation of the radiation-induced degradation of aniline by gamma irradiation is the subject of this paper. During the inquiry, several aqueous samples with aniline concentrations of 25, 50, 75, 100 and 200 mg/L were irradiated for 5, 10, 15, 20, 25 and 30 h, respectively, by a 60Co source with an absorbed dose rate of 0.78 kGy/h at the core channel. After the testing, the project authors scrutinized the aqueous samples to determine the effects of their irradiation by analyzing the pH, the hydroxyl radical and the H2O2 of the individual initial concentrations. The findings showed that gamma irradiation is effective in removing aniline from aqueous solutions and, in the process, tends to remove the chemical oxygen demand (COD). Among other findings, the tests revealed that at a 25 mg/L aniline concentration, up to 100 % removal is possible after only 5 h of exposure. The authors explained that kinetic studies have shown that the degradation of aniline follows a pseudo first-order reaction. They have also shown that pH plays a significant role in aniline-removal efficiency. The tests in this study revealed that with a dose of 7.8 kGy, the removal efficiency of COD in an alkaline environment is higher than that of an acidic environment. With the absorbed dose increases, the authors learned that an acidic environment is helpful for the removal efficiency of COD. They also found that by adding 50 g/L of sodium bicarbonate as the hydroxyl radical scavenger, there was an 8 % decrease in the removal efficiency of COD at the absorbed dose of 23.4 kGy. This indicates the importance of using a hydroxyl radical in the gamma irradiation process. Also, a 1 g/L H2O2 addition increases the COD removal rate from 31 % to 55 %. This percentage-point jump shows a synergistic effect in the use of gamma irradiation. The authors also identified several major decomposition products by GC/MS which are useful in the radiation-induced degradation of aniline by gamma irradiation process. Finally, they present proposals of possible pathways for successful aniline decomposition.

1 Introduction

Aniline, which has been widely used in the production of dyestuff, rubber, medicine and pesticide, is a poisonous compound [1]. Due to its high toxicity to the environment and to humans, aniline and its compounds have been listed among the priority-control pollutants by The State Environmental Protection Administration (SEPA). Researchers around the world have experimented with many methods of removing aniline and its compounds from the environment.

A current method for successful aniline removal involves a biological treatment that utilizes bacteria which has been acquired through separation methods [24]. Other popular, and successful, chemical methods of pollutant removal involve Advanced Oxidation Processes (AOPs) [57]. Karunakaran et al. [8] has experimented with sunlight and ultraviolet light using CdS as a catalyst. Their tests revealed that sunlight is more effective than ultraviolet light in the photocatalytic oxidation of aniline. Other research projects have combined methods for degradating aniline with such processes as ozone/UV oxidation [9], electro-Fenton [10, 11], photocatalytic processes [12, 13] and γ/enzymatic hydrolysis [14].

Irradiation technology has become a promising and powerful tool in the treatment of pollutants. When aqueous solution is irradiated by a high-energy beam, water molecules become excited and ionized, and produce large amounts of active particles like hydroxyl radicals, hydrated electrons, and hydrogen atoms, all of which play an important role in the degradation of organic pollutants [15, 16]. Christensen, H [17] made a study of the reactions between different radicals and aniline by pulse radiolysis. Qin et al. [18] investigated the oxidation of aniline by using different radicals, and discussed the end products in their findings. Solar et al. [19] made inquiries into the individual formation and decay kinetics of aniline by pulse radiolysis. All of these studies focused on kinetics and the end products of aniline.

In the present work, aniline was chosen as the target. The project involved testing the effect of the initial concentration of aniline, the absorbed dose, the initial pH, and the free-radical scavenger on the degradation of selected aniline samples. The project also included an inquiry into the enhancement of gamma irradiation degradation with H2O2 as well as a survey of the field of degradation kinetics.

2 Experiments and methods

2.1 Materials

The aniline, the hydrochloric acid naphthalene ethylenediamine (C12H14N2·2HCl, molecular weight of 259.20 g/mol), and the sulfamic acid ammonium (H6N2O3S,molecular weight of 114.12 g/mol) were purchased from Aladdin Industrial Inc.(China). The hydrogen peroxide, the sodium hydroxide, the ammonia, the carbon tetrachloride and the sulfuric acid were obtained from Nanjing Chemical Reagent Co. Ltd. All of the chemicals were of analytical grade or the higher purity available from the supplier. The water used in all of the experiments was ultrapure water.

2.2 Radiolysis experiments

Aniline solutions were irradiated in a 10 ml centrifuge tube with the designated initial concentration at room temperature. Each group of samples was irradiated for different time periods. The reference samples were non-irradiated samples. In addition, three groups of parallel samples were set up for guaranteeing the statistics of data. Some of the results are listed in Table 1.

Data of the parallel samples were used to calculate the standard deviation. Table 1 indicates that the standard deviation was small enough so that the measuring method and all of the instruments were thought to be available. In order to conduct the experiments efficiently, three groups of parallel samples were set up in the tests as are described in parts 3.2, 3.4 and 3.5 of this article.

All irradiation experiments were performed at a gamma irradiator which was located at the Center of Irradiation Research, Nanjing University of Aeronautics and Astronautics (NUAA). The experiments used a 60Co-γ source with an activity level of about 1.48 × 1016 Bq for irradiation. A silver dichromate dosimeter was used for detecting absorbed doses with an absorbed dose rate of 0.78 kGy/h. The initial pH was adjusted by using 1 mol/L H2SO4 or NaOH solutions.

2.3 The analytical instruments and methods

2.3.1 The Uv-vis spectrophotometer analysis

The measurement of aniline concentrations was carried out by using a UV-Vis spectrophotometer (UV-2550, Shimadzu, Japan). A 10 mm quartz colorimetric cuvette was used as the solution container in the experiments. The scan band ranged from 200 nm to 900 nm. During the experiment, the method of measurement was the hydrochloric acid naphthalene ethylenediamine method [20], and the absorption peak of aniline was 545 nm.

The degradation rate of aniline was determined as follows (eq. 1)):

(1)Thedegradationrateofaniline%=C0CC0×100%

where C0 represents the initial concentration of aniline before irradiation and C represents the concentration of aniline after irradiation, respectively.

2.3.2 The analysis of the chemical oxygen demand (COD)

In this study the chemical oxygen demand (COD) was used as a parameter to evaluate the efficiency of the degradation. A COD rapid tester (5B-3C, Shanghai Lian Hua Industrial Co. Ltd. China) was used for measuring the chemical oxygen demand (COD).

2.3.3 The gas chromatography and the mass spectrometer (GC/MS) analysis

A gas chromatograph-mass spectrometer (TRACE DSQ, Thermo Electron Corp, USA) was employed. An AC-5, 30 m × 0.22 mm i.d. quartz capillary column with a 0.25 μm film was used, with helium as the carrier gas monitored at a constant flow of 1 mL/min. The temperature of the injection port was 250 °C, and the quantity of the sample injection was 1.5 μL volume. The condition of the sample analysis is listed as follows: the initial temperature 40 °C, hold 3 min, 10 °C/min ramp to 280 °C, hold 5 min, the total analysis time 32 min.

2.3.4 The ammonia nitrogen rapid tester analysis

In the present study, ammonia nitrogen was measured to verify the conversion of organic nitrogen, and an ammonia-nitrogen rapid tester (5B-6D, Shanghai Lian Hua Industrial Co. Ltd. China) was employed to measure the concentration of ammonia nitrogen.

2.3.5 The ion chromatograph (IC) analysis

An ion chromatograph (ICS900, Dionex Corp, USA) was employed to verify the existence of nitrate and nitrite. An AS23, 2 × 250 mm analytical column and an AG23, 2 × 50 mm protect column were used, with an eluent constant flow of 1 mL/min. The eluent was composed of 0.8 mM sodium bicarbonate and 4.5 mM carbonic acid. A conductivity detector was equipped on the ion chromatograph.

3 The results and discussion

3.1 The determination of the standard curve

To measure the aniline concentration by the UV-Vis spectrophotometer, the hydrochloric acid naphthalene ethylenediamine method [20] was referred, and the absorbances of samples with different known concentrations of aniline (5, 10, 20, 50, 100 and 200 mg/L) were measured by UV-vis spectrophotometer. The relation between the absorbance at 545 nm and the known concentration of aniline is shown in Figure 1.

Table 1:

The results of the experiments.

Initial concentration (mg/L)Irradiation dose (kGy)Concentration of sample 1 (mg/L)Concentration of sample 2 (mg/L)Concentration of sample 3 (mg/L)Standard deviation (%)
507.86.5076.5006.4900.854
10015.622.86022.95722.9034.860
Table 2:

The degradation kinetics of aniline at different initial concentrations.

Concentration (mg/L)Kinetics equationsDose constant d(kGy–1)R2
50-ln(C/C0)=1.27897D+0.066151.280.89
75-ln(C/C0)=0.96181D+0.039120.960.91
100-ln(C/C0)=0.40325D+0.059490.400.88
200-ln(C/C0)=0.35643D+0.040260.360.90
Table 3:

The analyzed compounds identified by the GC/MS.

SymbolRT (min)Molecular WeightCompoundsStructural formula
A6.1893Aniline
B13.9594Phenol
C4.18106Ethylbenzene
Table 4:

The change of nitrite in aqueous solution.

Absorbed dose (kGy)Retention time (min)Peak area (•S*min)
09.9000
7.89.8930.0100
15.69.9000.0070
23.49.9230.0057
Table 5:

The change of nitrate in aqueous solution.

Absorbed dose (kGy)Retention time (min)Peak area (•S*min)
014.7000
7.814.6830.0097
15.614.7170.0054
23.414.6870.0070
Figure 1: The relation between the absorbance and the concentration of aniline.
Figure 1:

The relation between the absorbance and the concentration of aniline.

The absorbance was measured after diluting each sample 10 times. The result after the linear fitting is shown in eq. 2):

(2)Y=0.77317+0.08867XR2=0.99969

Where Y stands for the absorbance; X stands for the concentration of aniline; R2 stands for linear correlation coefficient. Good linearity as shown in eq. 2 indicates that eq. 2 can be used to determine the aniline concentration for the following irradiated samples.

3.2 The degradation kinetics of aniline solution by gamma irradiation

By using eq. 2 the concentration of aniline in each irradiated sample was calculated. The relationships between the degradation efficiency of aniline and its corresponding absorbed dose are shown in Figure 2.

Figure 2: The degradation efficiency along with the absorbed doses (Initial concentrations of aniline were 25, 50, 75, 100 and 200 mg/L).
Figure 2:

The degradation efficiency along with the absorbed doses (Initial concentrations of aniline were 25, 50, 75, 100 and 200 mg/L).

The results indicate that the initial concentration of aniline and the absorbed dose influences its degradation efficiency. For the samples with the same initial concentration of aniline, the degradation efficiency of aniline increases rapidly with the increase of the absorbed dose. However, the degradation efficiency decreases with the increasing initial concentration of aniline, because the number of the intermediate products increases with the increase of the initial concentration of aniline, and the intermediate products also take part in the degradation reaction. Thus, the intermediate products act as competitors with aniline. The degradation efficiencies for initial aniline concentrations of 25, 50, 75, 100 and 200 mg/L are 100 %, 94 %, 85 %, 82 % and 70 %, respectively.

The reaction velocity is defined as the concentration change per unit dose in a selected dose interval. The radiation-induced degradation of many pollutants is known to observe pseudo first-order behavior [2124]. The kinetics models were listed in the eq. 3 [24]:

(3)lnCC0=dD

where C0 stands for the initial concentration of aniline (mg/L); C stands for the concentration of aniline at a dose of D (mg/L). D is the absorbed dose during the irradiation (kGy), and d stands for the pseudo first-order kinetic constant used to describe the degradation rate (kGy–1).

C, C0, and D are known to calculate the d (dose constant, kGy–1). Table 2 lists the d value at different initial concentrations. The results show that the d value decreases with the increase of the initial concentration. This suggests that the aniline degradation rate is lower at a high initial concentration than that at a low initial concentration. In addition, the correlation coefficients suggest that the degradation of aniline follows pseudo first-order kinetics [24].

Some degradation rate constants of other degradation methods are shown in various professional journals. Jin Anotai et al [25]. indicated that when the experimental condition (0.01 M aniline, 1.07×10−3 M Fe2+, 74 g SiO2/L, current 4 A, pH 3.2) was set up, the reaction rate of aniline reached 0.053 M/min by the Electro-Fenton process and 0.029 M/min by the Fluidized-bed Fenton process. Ming-Chun Lu et al. [26] indicated the rate constant of aniline by photo-degradation at different initial concentrations. When the initial concentration of aniline ranged from 0.047 mM to 0.80 mM, the rate constant decreased from 0.1950 to 0.0017 (mM min)–1.

3.3 The effect of the initial pH of the aniline solution

1 mol/L of sulfuric acid and sodium hydroxide solution were used for adjusting the pH of the aniline solution ranged from 2 to 11. The relationship between the removal efficiency of COD and the initial pH are shown in Figure 3.

Figure 3: The removal efficiency of COD along with the change of pH. (a) The initial concentration of aniline was 25 mg/L. (b) The initial concentration of aniline was 50 mg/L. (c) The initial concentration of aniline was 100 mg/L.
Figure 3:

The removal efficiency of COD along with the change of pH. (a) The initial concentration of aniline was 25 mg/L. (b) The initial concentration of aniline was 50 mg/L. (c) The initial concentration of aniline was 100 mg/L.

The removal efficiency of COD was calculated following eq. (4):

(4)Theremovalefficiency%=COD0CODCOD0×100%

Where COD0 stands for the initial COD value of the aniline solution, and COD stands for the COD value after irradiation.

Figure 3 shows a similar trend which indicates that the removal efficiency of COD is higher in an alkaline environment than in an acidic environment at a low absorbed dose of 7.8 kGy, which was observed in the initial concentrations of 25, 50 and 100 mg/L. On the contrary, at a high absorbed-dose rate of 15.6 kGy, the removal efficiency of COD was lower in an alkaline environment than in an acidic environment. The main reason for this is that aniline tends to exist in a molecular form instead of an ion form in alkaline solution. This is helpful for the aniline-degradation process. Too, hydroxyl radical is easily produced in an alkaline environment. With the absorbed dose increases, organic carbon is converted into inorganic carbon which exists in the forms of HCO3-, and CO32- in an alkaline solution. These react with hydroxyl radicals, resulting in a decrease in the removal efficiency of COD (eq. 5), eq. 6, 27]. In an acidic solution, however, inorganic carbon escapes in the form of CO2 and has no influence on the concentration of hydroxyl radicals [28].

(5)CO32+OHCO3+OH
(6)HCO3+OHCO3+H2O

When researchers have treated aniline pollution through biological means, optical density (OD) is commonly used to represent the degradation rate of aniline. This procedure performs the same function as COD in the irradiation–degradation process. Junmin Li et al. [3] found that when the pH of aniline solution ranged from 3 to 13, the suitable pH for strain HSA6 was wide (from 5 to 11) and the optimal pH was 6 whose OD value reached 2.6 in 40 h.

3.4 The role of an hydroxyl radical

When ultrapure water is irradiated by gamma ray, many kinds of active substances generate in the solution (eq. 7, 29, 30].

(7)H2OOH2.8+eaq2.7+H0.6+H3O+2.7+H2O20.72+H20.45

The hydroxyl radical, hydrogen radical and hydrated electrons have an effect on the degradation of organic pollutants. In the experiments described here, sodium bicarbonate was chosen as the scavenger of the hydroxyl radical to allow for discussion on the influence of hydroxyl radicals on the degradation process. The influence of the sodium bicarbonate addition is shown in Figure 4.

Figure 4: The influence of sodium bicarbonate addition.
Figure 4:

The influence of sodium bicarbonate addition.

One can see in Figure 4 that with the increase of the concentration of the sodium bicarbonate addition, the removal efficiency of COD decreased significantly. The reason for this is that when sodium bicarbonate is added to the solution, the HCO3- competes with the aniline to react to the hydroxyl radical (eq. 6, 27], leading to the decrease of COD removal efficiency. This indicates that hydroxyl radicals play a major role in the degradation of aniline.

3.5 The enhancement of aniline degradation by irradiation with the addition of H2O2

In the present study, the enhancement of the H2O2 addition was investigated by analyzing the change of the COD removal efficiency in the presence of H2O2, whose initial concentrations in the samples were 0, 100, 200, 500 and 1000 mg/L. The results are shown in Figure 5.

Figure 5: The enhancement of the removal efficiency by using hydrogen peroxide. (a) The initial concentration of aniline was 100 mg/L. (b) The initial concentration of aniline was 200 mg/L.
Figure 5:

The enhancement of the removal efficiency by using hydrogen peroxide. (a) The initial concentration of aniline was 100 mg/L. (b) The initial concentration of aniline was 200 mg/L.

Figure 5 shows that the removal efficiency of COD by gamma irradiation improved significantly in the presence of H2O2. This can be explained by the fact that the addition of H2O2 in the solution improves the yield of hydroxyl radicals by eq. 8 and eq. 9 [3032]. The removal of COD is facilitated by the increase of hydroxyl radicals.

(8)H2O2+eaqOH+OH
(9)H2O2+HOH+H2O

In comparison with other methods of treating aniline pollution, Jin Anotai et al [33]. reported on the effectiveness of using the ordinary Fenton route. He said that when the concentration of aniline was 0.01 M, the removal efficiency of COD was steady, around 14 %, with the addition of 0.01 M Fe2+ and 0.3 M H2O2. He also noted that under the same conditions, the removal efficiency of COD was steady, around 40 %, by using the electro-Fenton method.

3.6 The intermediate products formation

To confirm the species of organic intermediates forming in the radiolytic decomposition of aniline, the samples were analyzed by the GC/MS. Since the samples had no water requirements, carbon tetrachloride was used to extract the aniline and its intermediates from the aqueous solutions. The decomposition by products are identified and listed in Table 3.

3.7 The organic nitrogen analysis

In the present study, an ammonia nitrogen rapid tester and an ion chromatograph were used to analyze the concentration change of the ammonium ion and the nitrite and nitrate. The concentration of the aniline was 200 mg/L and the absorbed doses were 7.8, 15.6 and 23.4 kGy. The results are shown in Figure 6, Table 4 and Table 5.

Figure 6: The relation between the concentration of ammonium and absorbed dose.
Figure 6:

The relation between the concentration of ammonium and absorbed dose.

The concentration of the ammonium ion was measured by the ammonia nitrogen rapid tester. Figure 6 shows that with the increase of the absorbed dose, the concentration of the ammonium ion increased significantly. This indicates that with the formation of the hydroxyl radical, and aniline’s subsequent reaction to it, the hydroxyl radical replaces the amidogen and nitrogen appears as the ammonium ion in aqueous solutions [34].

The ion chromatograph was used to verify the existence of nitrate and nitrite. In the result of ion chromatograph analysis, peak area has a positive correlation with the concentration, thus, the peak area was used to represent the concentration of nitrate and nitrite. Table 4 shows the increase of the absorbed dose along with the concentration of nitrite, which at first increased and then slowly decreased. Table 5 illustrates how the nitrate peaked at 14 min. This discovery showed that with the increase of the absorbed dose, nitrate in aqueous solution manifested itself.

The results cited above indicate that when aniline reacts with radicals, nitrogen presents itself as the ammonium ion, and nitrate and nitrite appear and remain in aqueous solutions [35].

3.8 The decomposition pathways

The results analyzed by the GC/MS, ammonia-nitrogen rapid tester and the ion chromatograph have formed this project’s proposed pathways for the decomposition of aniline, as shown in Figure 7. In gamma irradiation, the hydroxyl radical generates in aqueous solution, and it reacts with the aniline, resulting in the formation of phenol (B, 36, 37]. The amidogen is substituted and oxidized, and then exists as an ammonium ion, nitrate and nitrite in aqueous solution [35]. In addition, the gamma ray attacks the bond between the amidogen and the aromatic ring, resulting in the formation of an aromatic ring with a single electron. Ethyl then reacts with the aromatic ring and ethylbenzene (C) forms. Finally, the aromatic ring mineralizes into CO2, H2O, etc.

Figure 7: The proposed pathway for aniline decomposition by gamma irradiation in aqueous solution.
Figure 7:

The proposed pathway for aniline decomposition by gamma irradiation in aqueous solution.

In a previous study, Knight J A [34] investigated the products of aniline by gamma radiolysis, and identified some complicated cross-linked products of aniline. He discovered that the reaction of the amino group was about 14 times greater than that of the phenyl ring. He did not, however, discuss the changes that can take place in organic nitrogen.

4 Conclusions

The degradation of aniline in aqueous solution by gamma irradiation is effective. A list of the experiments which wrought this finding and were performed by the project authors are as follows: (1) With the increase of the absorbed dose and the decrease of the initial concentration, the degradation efficiency of aniline increases significantly. (2) The gamma irradiation degradation of aniline follows pseudo first-order kinetics. (3) The initial pH of aqueous solution has an effect on the removal efficiency of COD. At a dose of 7.8 kGy, the removal efficiency of COD in an alkaline environment is higher than that in an acidic environment. With the increase of the absorbed dose, an acidic environment is helpful for the removal efficiency of COD. (4) Hydroxyl radicals play an important role in degradation of aniline’ (5) H2O2 creates synergies with gamma irradiation for the degradation of aniline in aqueous solutions, since the removal efficiency of COD increases significantly with the increase of H2O2. (6) With irradiation by gamma ray, organic nitrogen converts into an ammonium ion and nitrate and nitrite appears in aqueous solution. (7) Intermediate byproducts have been identified and possible pathways for aniline decomposition by gamma irradiation in aqueous solution are proposed.

Funding statement: This work was supported by the National Natural Science Foundation of China (Grant No. 11405086) and National Key Scientific Instrument and Equipment Development Projects (Grant No. 2013YQ40861). And this work was supported by a Project Funded by the Priority Academic Program Development of Jiangsu Higher Education Institutions (PAPD).

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Received: 2016-5-18
Revised: 2016-8-1
Accepted: 2016-9-16
Published Online: 2017-1-20
Published in Print: 2017-1-1

© 2017 by Walter De Gruyter GmbH

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Heruntergeladen am 26.9.2025 von https://www.degruyterbrill.com/document/doi/10.1515/jaots-2016-0173/html
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