Journal of Chemistry
Volume 2016 (2016), Article ID 1797396, 6 pages
http://dx.doi.org/10.1155/2016/1797396

Research Article

Adsorptive Performance of Ni(II) from Aqueous Solutions Using Biochar Made of Phragmites australis by Adding Ammonium Polyphosphate as Flame Retardant

Peng Liu,¹ Min Yue,¹ and Houyong Zhang²

¹School of Environment Science and Engineering, Shandong University, Jinan 250100, China
²Jinan Environmental Monitoring Center, Jinan 250014, China

Received 11 December 2015; Accepted 9 February 2016

Academic Editor: Maria Roca

Copyright © 2016 Peng Liu et al. This is an open access article distributed under the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.

Abstract.

The withered Phragmites australis (PA) surrounding the rivers can cause the secondary pollution of water. In this research, by changing the ratio () of ammonium polyphosphate (APP), used as flame retardant, to PA at different temperatures, a series of BC samples were prepared for further analysis in several perspectives, namely, surface morphologies, surface areas, surface functional groups, and yields. The analysis indicated that, after being charred, the produced BCs obtained enhanced yields and promoted surface acidity. As adsorbent to remove Ni(II) from aqueous solutions, the BCs with APP improved the sorption of Ni(II) dramatically, compared with those purely produced by pyrolysis of PA, and obtained the maximum of adsorption capacity with the of 0.25 at 400°C.

1. Introduction

Biochar (BC), a kind of porous carbon material, is carbonization by biomass in anoxic or anaerobic conditions at low temperature. It has been widely used in carbon emission reduction, water purification, adsorption of heavy metals, and soil improvement [1, 2]. In winter, the withered Phragmites australis (PA) played a negative role in normal operation of the constructed wetland and the secondary pollution of water [3]. Therefore, the withered PA is used to produce biochar, which will be a “turning waste into wealth” method [4]. In order to enhance the yields and properties of BC, the common method is adding flame retardants. Ammonium polyphosphate (APP), a kind of excellent performance flame retardant, contains many advantages such as avirulent, insipidity, no corrosive gas produced, less hygroscopicity, and high thermal stability [5]. APP has been gradually used for the compound fertilizer and liquid fertilizer production and especially has been widely used in the developed countries. It is a good try to use APP as flame retardants for producing BC.

This research is designed to evaluate the feasibility of APP as flame retardants for produced BC; to study the effect of additive amount of APP and charring temperature (300, 400, and 500°C) on the textural and chemical properties of produced BCs; and to evaluate the sorption capacities of produced BCs toward Ni(II) by comparing with the BCs derived from pyrolysis of PA without adding APP.

2. Materials and Methods

2.1. Materials and Chemical Reagents

Phragmites australis (PA), with porous caudex system and large cell gap, can be used as a low-cost and efficient precursor for BC production. The PA grew in wetlands in Shandong, a province located in the eastern part of China. After being reaped in winter, the PA was washed in distilled water for a few times and aired in a 105°C environment for 24 hours and then smashed into pieces of approximately 0.45–1.0 mm [6]. Ammonium polyphosphate (APP) was used as flame retardant. By dissolving a weighted quantity of NiCl₂·5H₂O in distilled water, the Ni(II) solution was obtained. All chemical reagents used were of analytical grade.

2.2. Preparation of Activated Carbons

About 10 g PA were fully mixed with a weighted amount of APP and 10 mL distilled water, and the mixed samples were then aired in a 105°C environment for 12 hours to evaporate the moisture. The ratios (, g APP/g PA) were 0, 0.25, 0.5, and 1.0, respectively. After being dried, the samples were placed in 150 mL ceramic crucibles, and each ceramic crucible was covered with a fitting lid. Then these samples were charred at 300, 400, and 500°C for 1 hour under N₂ flow of 500 mL/min in the muffle furnace (combustion chamber, 300 mm × 200 mm × 120 mm), respectively [7]. In order to assess the impacts of APP on the final BCs, another three BC samples without APP were prepared at the charring temperatures of 300, 400, and 500°C for 1 hour. After being cooled to room temperature, the charred residues were pulverized for subsequent demineralization with 0.1 mol/L HCl. The samples were thoroughly washed in distilled water until pH of the washing liquid attained and kept a constant degree and then aired for 9 hours at a 105°C environment. These BC samples were hereafter referred to as s, in which and represent the final charring temperature and the , respectively.

2.3. Characterization Methods

The thermogravimetric analysis (TGA) and derivative thermogravimetric (DTG) curves of PA and the different impregnations mixture of PA and APP were derived from a thermogravimetric analysis (TGA-50 analyzer). The PA samples were referred to as s, in which and represent the final charring temperature (300, 400, and 500°C) and the (0, 0.25, 0.5, and 1.0), respectively. Each sample was heated up to a designed temperature and kept at this temperature for 1 hour at a heating rate of 10°C/min. The Brunauer-Emmett-Teller (BET) surface areas () of BCs were measured by the adsorption of N₂ at 77 K in a surface area analyzer (Quantachrome Corporation, USA). The was also calculated from the isotherms in the BET equation. The surface textures of the BCs were observed by a scanning electron microscope (SEM Hitachi S4800, Japan). The surface functional groups of BCs were defined by using Boehm’s titration method.

Adsorption experiments were conducted with the initial concentration of Ni(II) in the range of 10–60 mg/L. The adsorption dose was 600 mg/L using 100 mL flask. The initial pH was adjusted with addition of 0.01 M HCl or NaOH to the value of . The flasks were kept in an isothermal water bath and agitated at 180 rpm for 36 hours to ensure that equilibrium was reached. The amount of Ni(II) adsorbed at equilibrium (, mg/g) was calculated by

in which and represent the initial and equilibrium concentration of Ni(II) (mg/L), respectively; is the solution volume (); and is the mass of adsorbent (g).

3. Results and Discussion

Figure 1 shows the thermogravimetric analysis of samples. It can be seen from TGA curves that () samples displayed much lower weight loss than samples, indicating that APP has good flame retardant performance for PA. The yields of BCs, as listed in Table 1, were defined as the ratio of the weight of produced BC to the weight of PA used for charring. Yields of the BCs declined with increasing temperature and increased with increasing the amount of APP added. The yields of () were dramatically much higher than , which also confirmed that APP used as fire retardant played a key role in BCs preparation.

Table 1: Surface area, yields, and surface functional groups of the BC samples.

Samples number
(m²/g)
Yield (%)
Carboxyl (mmol/g)
Lactone (mmol/g)
Phenolic (mmol/g)
Total acidic functional groups (mmol/g)

BC-300-0
4.6
29.5
0.1964
0.3217
0.5741
1.0922

BC-300-0.25
167.9
56.0
0.3011
0.3719
1.1727
1.8457

BC-300-0.5
164.3
58.6
0.3036
0.2936
0.8999
1.4971

BC-300-1.0
151.7
66.8
0.2992
0.3300
0.8419
1.4711

BC-400-0
7.9
25.1
0.1841
0.2709
0.6449
1.0999

BC-400-0.25
177.7
48.0
0.3661
0.3284
1.0713
1.7657

BC-400-0.5
181.2
53.8
0.3663
0.3575
0.9701
1.7121

BC-400-1.0
171.4
57.8
0.3858
0.3359
0.9469
1.6686

BC-500-0
12.1
16.5
0.0790
0.4102
0.4923
0.9815

BC-500-0.25
165.8
43.4
0.6180
0.1099
1.1835
1.9744

BC-500-0.5
149.5
50.4
0.3567
0.3615
1.0829
1.8012

BC-500-1.0
157.2
54.8
0.5329
0.1220
0.9919
1.6469

(a)

(b)

(c)

(d)

(e)

(f)

Figure 1: Thermogravimetric analysis (TGA) and derivative thermogravimetric (DTG) curves of samples. (a) TGA curves of PA-300- samples; (b) DTG curves of PA-300- samples; (c) TGA curves of PA-400- samples; (d) DTG curves of PA-400- samples; (e) TGA curves of PA-500- samples; (f) DTG curves of PA-500- samples.

The weight loss for the samples during thermogravimetric analysis could be divided into three stages. In the first stage, the small amount of weight loss was caused by loss of water and light volatile compounds in PA with the temperature rising from room temperature to 200°C. Then, a significant weight loss occurred with temperature from 200°C to the final temperature (300, 400, or 500°C), which was mainly caused by evolution of volatile compounds generated by decomposition of hemicellulose, cellulose, and lignin in PA. In the last stage, as temperature kept at a constant value of 300, 400, or 500°C, the samples displayed a continuous and slight weight loss. In the chemical reaction of PA with APP, PA is in the reducing atmosphere resulting from the formation of carbonization layer promoted by the presence of APP. Thereby, the char of PA is promoted at the high temperature in the muffle furnace. Besides, with the increase of temperature, APP can decompose into H₃PO₄ and phosphates. The fire retardation and dehydration condensation in reaction of H₃PO₄ with lignocellulose also contribute to the char of PA [8, 9].

SEM micrographs of the BCs are shown in Figure 2. After carbonization without APP, BCs showed a similar structure to PA, while the structure of BC-400-0.5 was obviously corroded. Some particles or flakes on the surfaces of BC-400-0.5 were observed, which could result from the chemical vapor deposition of pyrolysis products. As shown in Table 1, the BET surface area of samples increased with increasing pyrolysis temperature. The production of volatile compounds inside PA particles gradually increased as the final temperature rises, which caused increase of porosity. Obviously, it could be drawn that the of () were higher than that of , indicating that APP as a fire retardant was efficient to pore-forming in BCs preparation. And the results of Boehm’s titrations were also showed in Table 1. The surface acidity of (), carboxyl, in particular, was much more than . This demonstrated that phosphoric acid was released by APP in BCs preparation. The previous researches indicated that the active surface acidic characteristic of carbons could contribute to adsorption of heavy metal [10]. Therefore, the Ni(II) adsorption of BCs would be improved.

(a)

(b)

(c)

(d)

Figure 2: SEM micrographs of (a) PA sample, (b) BC-400-0 sample, and (c and d) BC-400-0.5 sample.

The adsorption isotherms of Ni(II) onto the BCs, as shown in Figure 3, were analyzed at different initial Ni(II) concentrations varying from 10 to 60 mg/L. In order to estimate the maximum adsorption capacity of Ni(II) onto the BCs, both of Langmuir (2) and Freundlich (3) isotherm models were conducted to simulate the sorption:

Here, represents the absorption amount (mg/g); represents the equilibrium concentration (mg/L); represents the maximum sorption capacity (mg/g); represents the Langmuir sorption constant; and and are the Freundlich constants.

(a)

(b)

(c)

Figure 3: Sorption isotherms of Ni(II) on the BCs. (a) BC-300- samples; (b) BC-400- samples; (c) BC-500- samples.

The constants of both models fitting into the adsorption data were presented in Table 2. The correlation coefficient () in Langmuir model were much higher than those obtained from Freundlich model, indicating that the adsorption of Ni(II) on the BCs was simulated better by Langmuir model than Freundlich model. This also is observed from Figure 3 that the Langmuir model fits the data better. The values of the BCs were between 0 and 1, representing a favorable sorption of Ni(II) onto the BCs. As shown in Table 2 and Figure 3, the adsorption capacities of Ni(II) onto the samples obtained its maximum at (BC-300-0.25, BC-400-0.25, and BC-500-0.25) for different charring temperatures and at = 400°C for different . The considerable Ni(II) sorption capacity of BC-400- sample () could be attributed to the roles of the higher surface area and more acid functional groups.

Table 2: Langmuir and Freundlich constants related to the adsorption isotherms of Ni(II) for the BCs samples.

Samples number
Langmuir
Freundlich

(mg/g)
(L/mg)

(g⁻¹)

BC-300-0
9.7466
0.0451
0.8714
0.3942
1.4126
0.8888

BC-300-0.25
15.408
0.3169
0.9872
0.1071
9.4480
0.8983

BC-300-0.5
9.4787
0.3748
0.9975
0.0879
6.3414
0.8093

BC-300-1.0
7.1174
0.5569
0.9998
0.0957
4.7841
0.8950

BC-400-0
9.0090
0.2054
0.9917
0.1390
4.7119
0.9102

BC-400-0.25
19.231
0.4948
0.9979
0.1473
10.770
0.9567

BC-400-0.5
15.898
0.4565
0.9983
0.1216
9.6253
0.9766

BC-400-1.0
14.859
0.1760
0.9658
0.1438
7.4076
0.7877

BC-500-0
10.142
0.3728
0.9978
0.1427
5.6305
0.9224

BC-500-0.25
15.528
0.6002
0.9982
0.1328
9.3008
0.8772

BC-500-0.5
15.244
0.8200
0.9964
0.1098
10.046
0.7865

BC-500-1.0
14.025
0.2094
0.9932
0.1920
6.1398
0.9652

4. Conclusions

This study investigated the preparation of BCs by using APP as flame retardant. The results indicated that, by comparing with the samples, enhanced the porosity and surface acidity of BCs were developed by using APP as flame retardant; using APP as flame retardant for BC production can dramatically enhance the Ni(II) adsorption capacities of the produced BCs.

Conflict of Interests

The authors declare that there is no conflict of interests regarding the publication of this paper.

Acknowledgment

This work was supported by the China Postdoctoral Science Foundation (2013M540551).

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