生物法制备聚合硫酸铁及其应用研究_英文_

Biological preparation and application of poly-ferric sulfate flocculant

WANG Hui-min, MIN Xiao-bo, CHAI Li-yuan, SHU Yu-de

School of Metallurgical Science and Engineering, Central South University, Changsha 410083, China

Received 23 September 2010; accepted 5 January 2011

Abstract: A novel inorganic polymer flocculant, poly-ferric sulfate (BPFS) was prepared by oxidation of ferrous sulfate using domestic Thiobacillus ferrooxidans (T·f) under acid condition. The optimal conditions for the preparation were pH value of 1.5, (NH4)2SO4 dosage of 0.5 g/L, initial Fe2+ concentration of 45g/L, inoculum 10%, rotating speed of 120 r/min, reaction time of 5 6 d and reaction temperature of 30 °C. Under the optimal conditions, the BPFS product with pH value of 1.5 2.2, basicity of 17.5% 22.7% and total iron content of 43.87 45.24 g/L was obtained. The application of the BPFS to three wastewaters was carried out, and the removal efficiencies of COD, decolorization and Zn2+ by BPFS can be reached 70%, 90% and 99%, respectively. The result suggests that the BPFS is an excellent flocculant for water treatment. Key words: ferrite; poly-ferric sulfate; flocculant

1 Introduction

Flocculation sedimentation is one of the most widely used and lowest cost techniques for water treatment [1 2], and flocculant is the key in application of flocculation sedimentation technique. Recently, a novel inorganic polymer flocculant, poly-ferric sulfate(PFS) has received much attention because it has many advantages in comparison with conventional flocculant, such as low sample consumption, high efficiency, wide pH application range, low residual iron concentration, hydrolysate with high efficiently dehydration, non-toxicity, low-priced and fast settling rate [3 6].

At present, PFS is mostly prepared by direct oxidation of ferrous sulfate using strong oxidant such as H2O2, KClO3, NaClO, HNO3 or by catalytic oxidation of ferrous sulfate using NaNO2 or NaI as a catalyst in acid media. However, the methods mentioned above have many limitations such as extremely slow reaction, unstable product, low yield, large consumption of catalyst, high cost and emissions of nitrogen oxides causing environmental pollution, so it is difficult to be applied to the industrial production [7 10].

The objective of this study is to develop a new

preparation technique for PFS using the microbes and organic waste, and to gain the BPFS product with low cost, low energy consumption, high-quality and high stability [11 14]; the influencing factors in the preparation process of BPFS and its application in water treatment were also investigated.

2 Experimental

2.1 Microbial adaptation

9K culture medium containing 9 g/L Fe2+ was added into conical flask，then 10% (volume fraction) inoculum was innoculated and cultivated on a thermostatic waterbath at 30 °C with agitation of 120 r/min. The conversion rate of Fe2+ was determined at selected time until it reached 85%. After the reaction, the reaction mixture was used to initiate the next one, and the above-mentioned steps were replicated until the reaction time basically remained stable. With the repeated inoculation and cultivation, T·f bacteria gradually adapted to the new environment, and the reaction time gradually became stable. The T·f bacteria adaptation results are listed in Table 1.

As the T·f bacteria were in a new environment, their growth and oxidability were influenced to a certain extent. The reaction time to meet the oxidation rate

Foundation item: Project (2009ZX07212-001-01) supported by the Major Science and Technology Program for Water Pollution Control and Treatment,

China; Project (50925417) supported by the National Natural Science Foundation for Distinguished Young Scholars of China; Projects (50830301, 51074191) supported by the National Natural Science Foundation of China

Corresponding author: MIN Xiao-bo; Tel: +86-731-88830875; E-mail: mxb@ DOI: 10.1016/S1003-6326(11)61048-0

WANG Hui-min, et al/Trans. Nonferrous Met. Soc. China 21(2011) 2542 2547 2543

2.4 Analytical methods

COD was measured by fast digestion- Reaction times Reaction time required/h

spectrophotometric method and the content of dyes 1 72

expressed as visible light absorbance at 665 nm was 2 65

measured by a visible spectrophotometer; the Zn 3 55

concentration in solution was measured by flame atomic

4 50

absorption spectrophotometry. Fourier transform infrared

5 48

spectroscopy (FTIR) was carried out on Nicolet Magna

550 to obtain the structural information of the BPFS above 85% was 72 h. However, the more reaction times composite. conducted, the less time was required. After 4 times

repeated cultivation, the reaction time requried for 3 Results and discussion oxidation rate above 85% was stabilized to be about 50 h, as listed in Table 1. 3.1 Preparation influence factors 3.1.1 Effect of temperature 2.2 Preparation of BPFS Temperature is very important for microbial growth

Based on breeding selection and domestication, and activity of microbial enzymes. To investigate the eosinophilic aerobic autotrophic bacteria T·f were effect of temperature on BPFS preparation, experiments selected as biocatalyst to prepare BPFS with were conducted at four different temperatures (20, 30, 35 FeSO4·7H2O as raw materials. Ferrous sulfate solution and 40 °C) with 10% inoculum at pH 2.0. The results are was prepared by dissolving a certain amount of shown in Fig. 1.

FeSO4·7H2O in deionized water, the pH value of the solution was adjusted with sulfuric acid. After the addition of essential nutrients, strains were introduced and cultivated in thermostatic waterbath at 30 °C. Under the catalysis of microbes, reddish-brown BPFS was synthesized through a series of oxidation, hydrolysis and polymerization reactions.

2.3 Flocculation experiments

To evaluate the flocculation effect of the prepared BPFS, flocculation experiments were carried out in a jar test apparatus. A lake water with high chemical oxygen demand (COD), a dye wastewater and a zinc containing

wastewater were tested. Selected properties of the tested

2+

Fig. 1 Impact of reaction temperature on conversion of Fesolutions were summarized in Table 2. The experimental

procedurzes were as follows: 5 mL BPFS was added to

It is shown that the conversion of Fe2+ at 30 and the jar and then filled with 400 mL tested solution.

35 °C is much stronger than that at 20 and 40 °C, Afterwards, the suspension was agitated at speed of

illustrating that too high or low temperature is likely to 40 60 r/min for 10 min, then it was left undisturbed for

result in significant decrease of Fe2+ oxidation rate, over 30 min, and the supernatant sample (200 300 mL)

moreover, high temperature increases the amount of was collected for further analysis.

sediment. Thus, the optimum temperature is 30 °C for

the preparation of BPFS. Table 2 Selected properties for tested solutions

3.1.2 Effect of pH Absorbance 2+

COD/ ρ(Zn)/pH is critical to the preparation process, as pH Solution pH (methylene 1 12+(mg·L) (mg·L)increases, the oxidation of Fe gets weak and more blue)

precipitation is generated, lowering the basicity of the

Lake water 6.72 7.02 330 product. However, too low pH is also unfavorable for the

oxidation of Fe2+ due to the inhibition of bacteria growth, Dye

8.0 0.143

and it tends to make the prepared product has strong wastewater

corrosivity, therefore, the pH value of the reaction

Zinc

solution should be well-controlled.

5 6 200 containing

The effect of pH is studied at various pH (2.0, 1.8

wastewater

and 1.5) with other experimental conditions constant.

Table 1 Adaptation results of T·f bacteria

2544 WANG Hui-min, et al/Trans. Nonferrous Met. Soc. China 21(2011) 2542 2547

Figure 2 shows the conversion of Fe2+ versus time at pH value of 2.0, 1.8 and 1.5. The conversion of Fe2+ is stronger at pH 2.0 than that at pH 1.8 and pH=1.5 in the initial stages; however, it is not different at the end of the experiment (after 100 h) with conversion of about 90% at pH=2.0, 1.8 and 1.5. It is found that the precipitation of jarosite [MFe3(SO)(OH)6] can be easily generated at initial pH value of about 2.0, especially with high iron concentration, resulting in inhibition occurring in the oxidation of Fe2+. Therefore, initial pH value of 1.5 is considered to be appropriate for the preparation of BPFS.

impact on the conversion of Fe2+. Thus, 10% inoculum for the preparation of BPFS is chosen. 3.1.4 Effect of initial iron concentration

The effect of the initial Fe2+ concentration on the BPFS preparation was studied by changing the Fe2+ concentration from 35 to 45 g/L. As shown in Fig. 4, with the increase of Fe2+ concentration, the average oxidation rate of Fe2+ decreases, and the color of BPFS gets darker because the growth of bacteria requires proper amount of Fe2+. Low Fe2+ concentration cannot provide sufficient energy to the growth of bacteria and causes the prepared BPFS to be low in iron content and less useful in application. However, too much Fe2+ can inhibit the growth of bacteria. Based on the comparison of the growth of bacteria under different Fe2+ concentration conditions, it is concluded that with the initial Fe2+ concentration of 40 g/L, Fe2+ oxidation rate is more stable and BPFS with good performance can be obtained.

Fig. 2 Impact of initial pH on conversion of Fe

2+

3.1.3 Effect of inoculation amount

To investigate the effect of inoculation amount on the BPFS preparation, experiments were conducted with 5%, 10%, 15% and 20% inoculum. The results are shown in Fig. 3.

Fig. 4 Impact of different initial Fe concentration on conversion of Fe2+

2+

Fig. 3 Impact of inoculum on conversion of Fe2+

Clearly, the conversion of Fe2+ is much lower with 5% inoculum, and the conversion of Fe2+ is only 55% after 56 h. However, with the addition of 10% to 20% inoculum, the conversions of Fe2+ are not significantly different and the conversion of about 98% is obtained after 56 h. It is illustrated that with 10% or more inoculum, the amount of inoculum does not have much

3.1.5 Effect of reaction solution composition on

preparation of BPFS

A certain amount of precipitation can be generated during the preparation of BPFS by microbes. Based on the analysis of X-ray diffraction (XRD), the precipitation is identified as pyrite vanadium with formula MFe3(SO4)(OH). However, the precipitate produced during the preparation of BPFS is undesirable because it can cause the scale in bioreactor and affect the transmit between substrate and metabolites, resulting in deficiencies of the nutrients such as O2, CO2 and substrate Fe2+ and a decrease in the reaction rate. Thus, it is very important to obtain a suitable culture medium with good oxidative activity of bacteria as well as less precipitation [15 18].

As the chemical formula for jarosite precipitation is MFe3(SO4)(OH), where M may be K+, Na+, NH4+ or H3O+, so the precipitation generation is related to the medium pH, cation species and concentration. Usually,

WANG Hui-min, et al/Trans. Nonferrous Met. Soc. China 21(2011) 2542 2547 2545

NH4+ makes great contribution to jarosite precipitation and its concentration has a large influence on the amount of precipitation. Ammonium sulfate [(NH4)2SO4] concentration can be set at 0.5 and 3.0 g/L respectively in medium with pH=1.5 while other ingredients remain constant. The amounts of precipitation that change over time are acquired. The result is shown in Fig. 5.

Fig. 6 FTIR spectrum of BPFS

Fig. 5 Effect of (NH4) 2SO4 concentration on precipitation

As the concentration of (NH4)2SO4 decreases from 3.0 to 0.5 g/L, the amount of precipitation is significantly reduced while the oxidation rate of Fe2+ is not changed. In addition, considering reagent usages and production costs, (NH4)2SO4 concentration of 0.5 g/L is more favorable for the preparation of BPFS.

3.2 Characterization of prepared BPFS

The BPFS prepared under the optimum condition is characterized. pH of the BPFS ranges from 1.5 to 2.2, which is higher than that of the PFS prepared by conventional methods and can reduce corrosion for the reactor. The total iron content of the BPFS is 43.87 45.24 g/L and the basicity is 17.5% 22.7% which is higher than that of the most PFS previously reported, resulting in better flocculability.

Moreover, it is suggested that the BPFS coagulants consist of species containing both Fe and —OH by the analysis of FT-IR spectroscopy (Fig. 6). In particular, peak at 821 cm 1 corresponds to Fe—OH—Fe symmetrical stretching vibrations, peaks at 1 020 and 639 cm 1 are associated with a Fe—O—H bond, peaks at 3 460 and 1 640 cm 1 are related to H—O—H stretching vibrations and peak at around 1 100 cm 1 is the characteristic absorption peak of SO42 [19 23].

3.3 Application of BPFS

The removal efficiencies of COD, decolorization and Zn2+ by the BPFS were investigated at different pH, the results are shown in Fig. 7.

Generally, the treatment effect of the PFS on contaminated water varies with pH. As the BPFS is

Fig. 7 Removal efficiencies of COD (a), decolorization (b) and Zn2+ (c) by BPFS at different pH

2546 WANG Hui-min, et al/Trans. Nonferrous Met. Soc. China 21(2011) 2542 2547

applied to treat the lake water, significant COD removal efficiency (above 70%) is found in the pH range of 6.0 10.0 as shown in Fig. 7(a).

For the treatment of the dye wastewater, the decolorization efficiency increases with increasing pH value. At pH above 8, the decolorization efficiency could be up to 90% (see Fig. 7(b)). Considering PFS is a metal ion containing polymer, it contains various high valence polynuclear complex ions and hydroxyl group —OH. Polymers can be generated by the bridging of —OH which interacts with negative charged materials. By controlling pH, the number hydroxyl complexes, distribution, electrical charge and molecular mass can be adjusted to achieve satisfactory results.

The results of the zinc removal efficiency at different pH using the BPFS are shown in Fig. 7(c). As pH increases, the zinc removal efficiency is enhanced. At pH above 8.0, the zinc removal efficiency reaches over 99%.

At the same time, the flocculating effect of BPFS and PFS is compared. The results are shown in Fig. 8.

content of 43.87 45.24 g/L, which can provides high flocculability and weak corrosivity to the reactor.

2) The BPFS is an effective flocculant for water treatment and the removal efficiencies of COD, decolorization and Zn2+ by the BPFS reach above 70%, 90% and 99%, respectively.

References

[1]

WANG Wan-lin. Recent researches and applications on complex inorganic polymer flocculating agents in China [J]. Industrial Water Treatment, 2008, 28(4): 1 5. (in Chinese)

ZHANG Ya-wen, HU Dong-sheng, PENG Bing-qian. Progress in research of flocculantes for wastewater treatment [J]. Petrochemical Technology & Application, 2009, 27(5): 470 477. (in Chinese)

LI Zhan-shuang, AN Hong-bo, DONG De-gui. Synthesis methods of ferrite series Polymer Flocculants [J]. Applied Science and Technology, 2002, 29(3): 51 53. (in Chinese)

PAN Lu-ting, WU Jin-feng. Research and progress of the preparation technologies of polyferric sulphate [J]. Industrial Water Treatment, 2009, 29(9): 1 5. (in Chinese)

YAN Rui. Water treatment aagent applications [M]. Beijing: Chemical Industry Press, 2000: 105 108. (in Chinese)

YAN Rui. Water-soluble polymers [M]. Beijing: Chemical Industry Press, 1998. (in Chinese)

CHEN Fu-jun, LI Feng-ting, DU Xi-rong. The research on synthesis of polymerization[J]. China Water & Wastewater, 1995, 11(1): 42 44. (in Chinese)

ZHENG Huai-li, LONG Teng-rui, YUAN Zong-xuan. Study on the preparation synthetic methods of polyferric sulphate and its advancement [J]. Chinese Journal of Environmental Engineering, 2000, 1(5): 21 25. (in Chinese)

LI Feng-ting, JI Gen-ding, XUE Gi. The preparation of inorganic coagulant polyferric sulphate [J]. Tech and Biotech, 1997, 123(9): 859 864.

HE Ren-xing, ZHENG Ya-jie, GONG Zhu-qing. Preparation and application of polyferric sulfate flocculants [J]. Environmental Science and Technology, 2004, 27(S): s146 s149. (in Chinese)

FU Ying, YU Shui-li. Characterization and coagulation performance of solid poly silicic ferric (PSF) coagulant [J]. Journal of Non-Crystalline Solids, 2007, 353(22 23): 2206 2213.

LIU Hai-ning, GUAN Xiao-hui. Comprehensive utilization of ferrous sulfate during production of titan white [J]. Environmental Engineering, 2003, 21(5): 74 76. (in Chinese)

ZHAO Yi-heng, WANG Shu-ying, LIU Hai-ning, CAI Guang-yu, GUAN Xiao-hui, YIN Rong. Preparation of biological polymeric ferric sulfate and it's properties of turbidity removal in water [J]. Journal of Northeast China Institute of Electric Power Engineering, 2000, 20(1): 45 48. (in Chinese)

GUAN Xia-hui, LIU Hai-ning, MA Zhi-yi, ZHAO Yi-heng. Preparation of biological polyferric sulfate as a new high efficiency flocculant and its properties [J]. Techniques and Equipment for Environmental Pollution Control, 2005, 5(1): 69 71. (in Chinese) DI Jin-shen, ZHAO Xin-qiao, GENG Bing. Study on removal of Sulfide from acid gas in Industry by Biotechnology [J]. Acta Petrolei Sinica: Petroleum Processing Section, 2003, 19(5): 53 57. (in Chinese)

ANDERS B J, COLIN W. Ferrous sulphate oxidation using T.f review [J]. Process Biochemistry, 1995, 30(3): 225 236.

SONDI I, SNI S, MATIJEVIC E. Precipitation of monodispersed basic iron (III) sulfate (sodium jarosite) particles [J]. Colloid Polym Sci, 2001, 279: 161 165.

[2]

[3]

[4]

[5] [6] [7]

[8]

[9]

[10]

Fig. 8 Comparison of flocculation between PFS and BPFS

[11]

It is shown that compared with the PFS prepared by conventional methods, the BPFS prepared in this study is superior with respect to the turbidity removal and the subsidence effect. This is because BPFS not only has a high degree of polymerization, but also contains microorganisms，which can catalyze the oxidation of organic matter as a condensation nucleus during the flocculating-deposition process. Thus, it is sticky and can improve the coagulation efficiency, resulting in the adsorption of big molecular organic matter.

[12]

[13]

[14]

[15]

4 Conclusions

1) A new preparation method of PFS using T·f bacteria as biocatalyst is developed. The BPFS prepared under the optimum conditions has many advantages over the PFS prepared by conventional methods with high pH of 1.5 2.2, high basicity of 17.5% 22.7% and total iron

[16] [17]

WANG Hui-min, et al/Trans. Nonferrous Met. Soc. China 21(2011) 2542 2547

[18] LONG Zhong-er, HUANG Yun-hong, CAI Zhao-ling, CONG Wei,

OU Yang-fan. Adaption of thiobacillus ferrooxidans tolerating low pH and biooxidation of ferrous sulphate [J]. The Chinese Journal of Process Engineering, 2002, 2(5): 415 420. (in Chinese)

[19] HOSTE S, VWEPONCK L, VANDER K C P. IR study on the solid

state reaction between iron hydroxide and KCN [J]. Bull Soc Chim Belg, 1982, 91(7): 597 604.

[20] JEZOWSKA B T, HANUZA J. The IR spectra and structure of new

binuclear iron (Ⅲ) oxy-complexes with nitrogen-donor ligands [J].

2547

Physical Chemistry, 1975, 23(7): 609 622.

[21] TOWE K M, BRADLEY W F. Mineralogical constitution of

colloidal “Hydrous Ferric Oxides” [J]. Colloidal and Interface Science, 1967, 24(3): 384 392.

[22] GADSDE J A. Infrared spectra of mineral and related inorganic

compounds [M]. London: Butterworths Press, 1975: 154 158.

[23] TANG H X, STUMM W. The coagulating behaviours of Fe(Ⅲ)

polymeric species [J]. Water Res, 1987, 21: 115 121.

生物法制备聚合硫酸铁及其应用研究

王慧敏，闵小波，柴立元，舒余德

中南大学 冶金科学与工程学院，长沙 410083

摘 要：研究生物法制备铁系絮凝剂及其影响因素。以FeSO4·7H2O为原料，利用驯化后的氧化亚铁硫杆菌(T.f)在酸性条件下的催化氧化作用制备生物聚合硫酸铁(PFS)，并确定最佳制备条件。实验表明：在反应液初始pH值1.5、硫酸铵用量0.5 g/L、初始Fe2+浓度45 g/L、接种量10%、温度30 °C时，在转速为120 r/min的恒温水浴摇床中连续培养5~6 d、可以制出pH 1.5~2.2、盐基度17.5%~22.7%、全铁含量43.87~45.24 g/L的产品。实验通过处理3种废水来考察其絮凝性能，结果表明：当PFS投加量一定时，COD去除率可达70%以上，脱色率达90%，Zn2+去除率达99%，说明PFS是一种絮凝效果优异的水处理剂。 关键词：铁系；生物聚合铁；絮凝剂

(Edited by FANG Jing-hua)

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