Isolation and Characterization of Heterotrophic Nitrifying Strain W1

ENERGY, RESOURCES AND ENVIRONMENTAL TECHNOLOGY Chinese Journal of Chemical Engineering, 20(5) 995ü1002 (2012)

Isolation and Characterization of Heterotrophic Nitrifying Strain W1* LÜ Yongkang (েစࢢ)1,**, WANG Xun (ฆᎅ)1, LIU Bokai (ঞϐ࢚)2, LIU Yuxiang (ঞံະ)3 and YANG Xiaohua (ཷ໋‫)ܟ‬1 1 2 3

Key Laboratory of Coal Science and Technology, Taiyuan University of Technology, Taiyuan 030024, China Engineering & the Built Environment (EBE), University of Cape Town, Cape Town7701, South Africa College of Environmental Science and Engineering, Taiyuan University of Technology, Taiyuan 030024, China

Abstract In a high concentration substrate medium, a heterotrophic bacterium with high removal efficiency of ammonium, named W1, was isolated from activated sludge of coking wastewater treatment facility. The bacterium was Gram-negative, rod-shaped, and identified preliminarily as Alcaligenes sp. according to its morphological and physiological properties and its 16S rRNA gene sequence analysis. In the high concentration ammonium medium (400 mg·L1 NH 4 -N), the effects of C source, N source, C/N ratio and initial pH of medium on ammonium removal were investigated in order to determine the optimal condition for strain W1. The maximum ammonium removal was around 95% in 4 days in an improved medium. The production of N2 gas was examined in a closed system that was full of pure oxygen at the beginning. N2 gas was detected in the system after 4 days of cultivation, which further testified that strain W1 has heterotrophic nitrification and aerobic denitrification abilities simultaneously. Keywords heterotrophic nitrification, aerobic de-nitrification, high concentration ammonium, Alcaligenes sp.

1

INTRODUCTION

Ammonium treatment is essential for preventing water eutrophication in aquatic environments. Wastewater, such as untreated coking wastewater, contains not only high concentration of nitrogen compounds but also high concentration of carbon materials. In untreated coking wastewater, ammonium may reach a concentration of 10003000 mg·L1. It is not applicable to use conventional nitrification with autotrophic bacteria to treat such wastewater because of the following reasons. Firstly, the nitrification rate is extremely slow. To treat high concentration ammonium, large-scale device and long hydraulic retention time (HRT) are required [16]. Secondly, the autotrophs are vulnerable to high loads of ammonium and organic matter [7, 8]. Thus, conventional nitrification can be implemented only after the wastewater is pretreated to reduce C/N ratio [9] or diluted [1, 10]. Thirdly, the system with aerobic/anaerobic conditions requires one aerobic tank and one anaerobic tank, demanding large space [9]. Compared with traditional autotrophic nitrification, heterotrophic nitrification presents larger growth rate, higher production of cells and higher adaptability to heterotrophic nitrifiers [11]. Recently, heterotrophic nitrifier has been intensively studied as potential microorganisms that may be used to overcome problems inherent in the conventional method. However, most of study has focused on low concentration ammonium discharged from domestic wastewater, with less attention on the treatment of high concentration ammonium in coking wastewater. The objectives of this study are to isolate heterotrophic nitrifying bacteria from activated sludge of coking wastewater and examine the ability of the bacterium

to remove ammonium from the medium containing high concentration ammonium. 2 2.1

MATERIALS AND METHOD Isolation of bacterium

2.1.1 Medium Enrichment medium: beef extract-peptone medium [12]. Basic medium: (NH4)2SO4 2.0 g, K2HPO4 0.75 g, NaH2PO4 0.25 g, MgSO4 0.03 g, MnSO4 0.01 g, sodium citrate 5.0 g, H2O 1000 ml, pH 7.2 (According to Stephenson medium [13], calcium carbonate was replaced by sodium citrate in same mass in order to screen one strain of heterotrophic bacterium). Improved medium: (NH4)2SO4 2.0 g, K2HPO4 0.75 g, NaH2PO4 0.25 g, MgSO4 0.03 g, MnSO4 0.01 g, sodium citrate 17.8054 g, H2O 1000 ml, pH 7.0. 2.1.2 Enrichment The beef extract-peptone medium was autoclaved at 121 °C for 30 min. Sterile medium (120 ml) in 250 ml conical flasks (n 3) was inoculated with 2 ml of fresh activated sludge from the coking wastewater, and incubated at 30 °C on a rotary shaker at 120 r·min1. Every 3 days, 0.1 ml of medium was spot-tested for the consumption of ammonium using Nessler’s reagent [13]. 2.1.3 Isolation of ammonium oxidizing bacteria When the Nessler’s reagent tests were proved positive, 1 ml of the enrichment cultures was transferred to basic medium. Some ammonium oxidizing bacteria were isolated by limited dilution method [14]. Purified isolate was obtained by repeated streaking on fresh washed-agar plates (liquid selective medium and 2% washed agar).

Received 2011-06-20, accepted 2011-12-12. * Supported by the National Natural Science Foundation of China (51078252), the International Cooperation Projects of Shanxi Province (2010081018), and the Natural Science Foundation of Shanxi Province (2010011016-1). ** To whom correspondence should be addressed. E-mail: [email protected]

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2.1.4 Preliminary identification of strain performance The isolated strain was tested for its ability to remove nitrogen. The strain was inoculated into 250 ml conical flasks (n 3) containing 120 ml of selected liquid medium and then cultured at 30 qC on a rotary shaker at 120 r·min1. Every day, the medium samples were taken and analyzed for ammonia, nitrite, total nitrogen, mass growth and change in pH. This operation was repeated once every day for 7 days. 2.2

Identification of the isolated strain

Physiological and biochemical characteristics of the isolated bacterium were examined according to the standard methods described previously [15]. The 16S rRNA sequence of the isolate was tested by TaKaRa Biotechnology (Dalian) Co., Ltd. The isolated strain was compared with other microorganisms using the Basic Local Alignment Search Tool program, to decide its species. 2.3

2.3.4 Initial pH of selective medium With the optimal carbon source, nitrogen source and C/N ratio, the effects of initial pH in basic media on ammonium removal by strain W1 were studied. Initial pH of medium was adjusted to 4, 5, 6, 7, 8, 9 and 10 separately by adding 0.1 mol·L1 NaOH or 0.1 mol·L1 HCl solution. The culture conditions were as same as mentioned above. The comparisons of the ammonium removal in different media (different initial pH) gave the optimum initial pH of medium for the bacterium. 2.4 Comparative study on nitrification and growth of strain W1 in basic and improved media One milliliter of cell in logarithmic phase was inoculated in 100 ml of optimum medium and selected medium separately. The bacterium was cultivated for 4 days. The culture conditions were as above. The culture media in the improved medium and basic medium were sampled for chemical analyses.

Optimization of basic medium

2.3.1 Carbon sources The isolated strain was cultured in the basic medium with the substitution of sodium citrate by different carbon sources at the same moles of carbon. The medium containing glucose was autoclaved at 110 qC for 15 min, and all other media at 121 qC for 20 min. The amount of (NH4)2SO4 (N source) was fixed, providing 423.0424.0 mg·L1 NH4-N. The bacterium was incubated at 30qC under aerobic condition on a rotary shaker at 120 r·min1 for 4 days. Then a basic medium with the highest nitrogen removal efficiency was obtained. The carbon source contained in the selected medium was regarded as the optimal carbon source. 2.3.2 Nitrogen sources With the optimal carbon source, isolated strain was cultured in the basic media with the replacement (equivalent moles of nitrogen) of ammonium sulfate by different nitrogen sources. All media were autoclaved at 121 °C for 20 min. The culture conditions were as above. After incubation for 4 days, a basic medium with the highest nitrogen removal efficiency was obtained. The nitrogen source contained in the selected medium was regarded as the optimal nitrogen source. 2.3.3 C/N ratio With the optimal organic carbon and nitrogen source, the influence of C/N ratio in the selected medium on ammonium removal by isolated strain was investigated. The C/N ratio was adjusted to 2, 4, 6, 8, 10, 12, 14, 16, 20 and 30 separately by fixing the amount of (NH4)2SO4 (optimal nitrogen source) and adding sodium citrate (optimal carbon source). The culture conditions were as same as mentioned above. After incubation for 4 days, a basic medium with the highest nitrogen removal efficiency was obtained. This C/N ratio of the medium was regarded as the optimal C/N ratio.

2.5 The influence of initial ammonium concentration With the optimal medium, the influence of ammonium concentration on the nitrifying capability of strain W1 was measured. Initial NH4-N concentration was separately adjusted to 50, 100, 200, 400, 600, 800, 1000, 1200, 1500, 2000 and 3000 mg·L1 using ammonium sulfate and sodium citrate by fixing C/N ratio and initial pH. The culture conditions were as same as mentioned above. 2.6 Identification of aerobic denitrification in pure oxygen system In order to identify whether isolated strain has heterotrophic nitrification and aerobic denitrification abilities simultaneously, the production of N2 gas by isolated strain incubated for 96 h in the improved medium under pure oxygen system was examined. The culture conditions were as above. In the test, 2 ml of the bacterium was inoculated in a 1 L flask containing 200 ml improved medium. Then the sealed flask was filled with pure oxygen in clean environment. To ensure that the system was not infected by other bacteria, air bacterial filter was used during the infusing oxygen process. The equipment was shown in Fig. 1. At the beginning and end of the test, the gas samples in the medium were analyzed using gas chromatography [16]. 2.7

Analytical methods

Growth of the bacterium was monitored by measuring the optical density (OD600) using a spectrophotometer. The concentrations of ammonium ( NH 4 -N) and nitrite ( NO 2 -N) were analyzed using Nessler’s

Chin. J. Chem. Eng., Vol. 20, No. 5, October 2012

Figure 1 Chart of 1L airproof-flask with two oraes 1übiforate rubber stopper; 2ügas sampling point; 3üvalve; 4üair inlet port (rubber tube with clamp was connected with glass tube); 5üair outlet port (rubber tube with clamp was connected with glass tube)

reagent photometry and N-(1-naphthalene)- diaminoethane photometry, respectively. Concentrations of nitrate ( NO3 -N), total nitrogen (TN) and total carbon (TC) were measured by ion chromatography and TOC-TN analyzer. N2 and O2 were assayed by gas chromatography. 3 3.1

RESULTS AND DISCUSSION Identification of strain W1

One heterotrophic bacterium with high-strength ammonium removal ratio and total nitrogen removal ratio was isolated, and named as W1. Strain W1 is a nonmotile, Gram-negative, short rod bacterium, having no endospore. It grows as yellow, opaque, round colonies on plate of solid basic medium. In a series of physiological and biochemical tests, strain W1 is positive for catalase reaction, gelatin liquefaction, starch hydrolysis and oxidase reaction, and negative for V-P test, M-R test, sugar fermentation and indole test. With 16S rRNA obtained by PCR amplification, we observe 99% sequence similarity with that of Alcaligenes sp. F78 (GenBank accession number EU443097.1). On the basis of the above results, strain W1 is confirmed primarily as Alcaligenes sp., named as Alcaligenes sp. W1. 3.2

Preliminary investigation of strain performance

Figure 2 shows the growth in 50 h and ammonium and nitrite concentrations in 7 days when strain W1 was cultivated in basic medium under aerobic condition. The lag phase of strain W1 was only 6 h, indicating that strain W1 has excellent adaptability to the medium containing high concentration ammonium. After 6 h, OD600 value increased rapidly. The strain reproduced rapidly. The maximum growth rate was between 16 h and 36 h, with a maximum growth rate of 0.5526 h1. However, strain W1 accessed to decline phase after 36 h incubation without stationary phase, implying that no adequate nutrition was provided for growth in the basic medium after 36 h incubation,

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Figure 2 Growth and ammonium removal efficiency of strain W1 in selective medium

possibly lacking of carbon source. In the prime of culture, NH 4 -N, the sole N-source, decreased dramatically. The maximum removal rate of NH 4 -N was 121.10 mg·L1·d1. NH 4 -N decreased from 434.47 mg·L1 to 64.75 mg·L1 in 4 days. These data indicates that strain W1 has higher heterotrophic nitrogen removal ability in high concentration ammonium medium, compared with Brevibacillus sp. LY (NH4-Nconcentration decreased from 45.30 mg·L1 to 9.89 mg·L1 in 24 days) [14, 17]. After 4 days, the residual content of NH4-N altered little. Thus, the cultural time was set to 4 days in the following experiments. The comparison of growth curve and ammonium removal curve indicates that the maximum ammonium removal rate appears in decline phase of growth, due to the nitrification, which is consistent with previous reports [18, 19]. 3.3

Optimization of basic medium

3.3.1 Optimization of carbon source Related reports have shown that the ammonium removal ability of heterotrophic bacterium is strongly influenced by carbon sources. Table 1 showed the growth and nitrification ability of strain W1 in the media containing different carbon sources. The OD600 values show that strain W1 grows better in the medium with citrate sodium, ethanamide, peptone and acetate sodium used as sole carbon source. Strain W1 utilizes organic carbon as well as inorganic carbon, indicating that strain W1 has broad adaptability to different organic matters. The comparison of initial and final NH 4 -N contents shows different ammonium removal ability of strain W1 in different carbon sources, probably due to different metabolic pathways. Strain W1 has the best ammonium removal ability in the medium containing citrate sodium. Thus, citrate sodium was used as the optional carbon source for strain W1 in the following experiments. 3.3.2 Optimization of nitrogen source As shown in Table 2, strain W1 is adaptable to different nitrogen sources. It utilizes not only inorganic nitrogen sources, but also organic nitrogen sources. It means the ability of the strain to degrade

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Table 1

The ammonium removal ability of strain W1 with different carbon sources

Carbon source

Initial NH 4 -N/mg˜L1

OD600

Final NH 4 -N/mg˜L1

citrate sodium

1.174(±0.006)

416.79(±2.41)

117.21(±10.17)

ethanamide

1.509(±0.019)

436.99(±3.87)

724.94(±20.56)

peptone

0.553(±0.014)

488.78(±5.32)

471.10(±12.14)

acetate sodium

0.319(±0.017)

443.31(±5.78)

351.12(±6.25)

acetone

0.050(±0.010)

430.68(±7.42)

426.89(±10.42)

methanol

0.034(±0.011)

438.26(±4.21)

391.53(±6.78)

phenol

0.029(±0.006)

438.26(±4.10)

386.48(±7.21)

starch

0.097(±0.006)

471.10(±4.30)

375.11(±6.12)

ethylether

0.040(±0.008)

452.15(±7.30)

419.32(±5.41)

glucose

0.103(±0.011)

516.56(±6.42)

402.90(±8.21)

calcium carbonate

0.153(±0.015)

471.10(±6.89)

333.44(±6.30)

Table 2

The ammonium removal ability of strain W1 with different nitrogen sources Initial NH 4 -N/mg˜L1 Final NH 4 -N/mg˜L1

Nitrogen source

OD600

Intracel-N/mg˜L1

Initial TN/mg˜L1

Final TN/mg˜L1

ammonium chloride

1.310 (±0.012)

79.37 (±1.67)

427.50 (±4.89)

189.25 (±6.12)

410.12 (±7.21)

110.83 (±6.83)

ammonium sulfate

1.162 (±0.007)

69.84 (±1.97)

425.25 (±3.87)

186.50 (±5.48)

407.32 (±3.78)

103.25 (±5.39)

ammonium nitrate

1.072 (±0.009)

61.56 (±0.78)

437.45 (±5.21)

272.71 (±3.23)

220.50 (±4.27)

23.98 (±1.89)

sodium nitrite

0.084 (±0.012)

2.69 (±0.01)

419.50 (±3.42)

406.25 (±6.54)

2.75 (±0.21)

1.36 (±0.23)

sodium nitrate

0.078 (±0.007)

2.61 (±0.01)

434.25 (±3.89)

426.50 (±2.78)

2.53 (±0.23)

1.44 (±0.27)

ethanamide

1.504 (±0.005)

106.07 (±1.10)

427.00 (±3.37)

208.75 (±4.25)

158.25 (±2.57)

124.52 (±1.25)

urea

0.223 (±0.014)

6.26 (±0.02)

418.25 (±2.72)

307.75 (±4.31)

35.67 (±1.89)

13.27 (±0.41)

different forms of nitrogen. It can be seen that strain W1 uses diverse inorganic nitrogen in varying degree, such as NH 4 -N, NO 2 -N, and NO3 -N, probably due to different metabolic pathways. With NO 2 -N and NO3 -N as sole nitrogen sources, strain W1 has not only heterotrophic nitrification ability, but also possibly certain aerobic denitrification ability. It is known that the removed NH 4 -N in medium is converted partially into intracellular nitrogen, partially into nitrification products (NH2OH, NO 2 -N, NO3 -N) and partially into denitrified products. The remained NH 4 -N and nitrification products in medium constitute the remained TN. Thus, the amount of denitrified products (nitrogen removed from media) is calculated by subtracting the amount of intracellular nitrogen from the amount of removed total nitrogen. The calculation shows that when (NH4)2SO4 is the sole nitrogen source, the amount of removed TN and NH 4 -N and the amount of denitrified products have the maximum values, indicating that (NH4)2SO4 is the optimum nitrogen source. 3.3.3 C/N ratio C/N ratio is one of the main important factors for heterotrophic nitrification bacteria. In this study, the ammonium removal of strain W1 in high-strength ammonium medium was investigated by changing C/N ratio (Fig. 3). OD600 value increased almost linearly

Figure 3 Nitrification characteristic and growth of strain W1 at different C/N ratios 1üfinal NH 4 -N; 2üfinal TN; 3üinitial NH 4 -N; 4üinitial TN; 5üfinal NO 2 -N; 6üOD600

with the C/N ratio up to 8, but further increment of C/N ratio did not affect the growth of strain W1. It indicates that the growth of bacterium is affected by C/N ratio when the carbon source is insufficient, but strain W1 presents excellent adaptability to high concentration organic matter. Owing to its good adaptability to different C/N ratios, strain W1 would have a bright foreground of application in coking wastewater treatment. As shown in Fig. 3, the final NH 4 -N concentration first decreases and then increases with the

Chin. J. Chem. Eng., Vol. 20, No. 5, October 2012

increase of C/N ratio, as does the final TN value. The final concentration of NH 4 -N is the maximum at C/N 0.5 (377.64 mg·L1) and the minimum at C/N 12 (28.24 mg·L1), indicating that the ammonium removal ability of strain W1 is influenced significantly by C/N ratio. At C/N 12, the removal efficiency of NH 4 -N is higher. Thus, the optimum C/N ratio is 12. Furthermore, the ammonium removal ability and the growth of strain W1 at high (C/N 20), intermediate (C/N 12) and low (C/N 5) C/N ratios were investigated. Figs. 4 and 5 present the nitrification process and growth of bacterium at different C/N ratios, respectively. In Fig. 4, at C/N 12 and C/N 20, the final concentration of NH 4 -N is about 25 mg·L1, which meets the national discharge standard of class II, while at C/N 5, it is above 100 mg·L1, mainly because the exhaustion of carbon source affects the removal ability and growth of bacterium. After cultivation of 84 h, the concentrations of NH 4 -N and TN are lower at C/N 12, indicating that C/N 12 is the best C/N ratio for strain W1. The NH 4 -N and TN removal ratio were up to 98.32% and 78.38%, respectively, at C/N 12 after 84 h cultivation (data not shown). In Fig. 5, logarithmic growth phase of strain W1 has no remarkable difference at C/N of 5, 12 and 20, suggesting that C/N ratio has little influence on reproduction

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rate of strain. It is inferred that, in industrial applications, the C/N ratio should be strictly controlled in ammonium removal phase, but it is not needed in the cultivation phase. Figure 6 gives the NH 4 -N and TC concentrations in selected medium at C/N 12. The two concentrations decrease with time in parallel, indicating that the carbon and nitrogen sources are utilized at a well-balanced ratio. This testifies that C/N 12 is the best condition for strain W1. In 84 h, ammonium concentration decreases to 28.04 mg·L1, and TC concentration is 3242.50 mg·L1. The remained TC could be further used as carbon source for denitrification. Thus, strain W1 exhibits remarkable nitrification performance at C/N 12. Other characteristics of strain W1 were investigated at C/N ratio of 12.

Figure 6 NH 4 -N and TC concentrations vs. time 1üTC; 2ü NH 4 -N

Figure 4 The nitrification of strain W1 1üTN(C/N 5); 2üTN(C/N 12); 3üTN(C/N 20); 4ü NH 4 - N(C/N 5); 5ü NH 4 -N(C/N 12); 6ü NH 4 -N(C/N 20); 7ü NO 2 -N(C/N 5); 8ü NO 2 -N(C/N 12); 9ü NO 2 -N(C/N 20)

3.3.4 Initial pH In order to examine the adaptability of strain W1 to environment, the ammonium removal of strain W1 at different initial pH (410) after 4 days cultivation was investigated. Fig. 7 shows the ammonium removal and the growth of strain W1 at different initial pH in the basic medium with C/N ratio of 12. The curves can be divided into three stages: pH 45, pH 69, and pH 10.

Figure 7 Ammonium removal and growth of strain W1 at different initial pH 1üinitial NH 4 -N; 2üfinal TN; 3üfinal NH 4 -N; 4üOD600 Figure 5 The growth of strainW1 1üOD600(C/N 5); 2üOD600(C/N 12); 3üOD600(C/N 20)

At the initial pH values of 45, strain W1 does not grow in the basic medium, and therefore does not

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remove ammonium, because the bacterium is dead under strong acid condition. At the initial pH values of 69, strain W1 grows well (OD600ı2.0), indicating that strain W1 has good adaptability to the environment. Meanwhile strain W1 presents favorable ammonium removal ability (final NH 4 -N<100 mg·L1). Thus strain W1 may be further used in industrial applications, especially for coking wastewater treatment. At pH 7, the NH4-N concentration is the lowest and the OD600 value is the largest for pH 69. The ammonium removal is up to 97.09%. Thus pH 7 is the best pH value for strain W1, close to the optimum range for nitrifying bacteria [20]. At the initial pH value of 10, strain W1 does not grow in the basic medium, but part of ammonium in the medium is removed. This is possibly because the removed ammonium leaves the system, which is strong alkaline environment, in the form of ammonia. 3.4 Comparative study on nitrification of strain W1 in basic and improved media Figure 8 shows the nitrification ability of strain W1 in the basic and improved media after 4 days cultivation. The final NH 4 -N and TN concentrations are lower in the improved medium. The removal ratio of NH 4 -N and TN are improved remarkably, from 78.49% and 55.92% to 91.98% and 79.02%, respectively. Therefore, strain W1 exhibits better nitrification ability in the improved medium. Optimization of medium is a highly effective method for enhancing the removal efficiency of ammonium. NO 2 -N accumulation is also lower in the improved medium, which is consistent with the report by Glass et al. that the accumulation of the nitrite intermediate was associated with the inhibition of denitrification [21].

Figure 8 Comparison of nitrification ability in basic medium and improved media improved; basic; blank control

3.5

Influence of ammonium concentration

In industrial productions, substrate concentration is not constant. It is necessary to examine the adaptability of bacterium to different substrate concentrations. Fig. 9 shows the influence of ammonium concentration on the growth and ammonium removal of

Figure 9 The growth and nitrification of strain W1 in media with different substrate concentrations 1üremoval of NH 4 -N; 2üremoval of TN; 3üOD600

strain W1 in the improved medium. The optical density value first increases and then decreases with the increase of initial ammonium concentration (IAC) in the media. At the IAC below 2000 mg·L1, strain W1 presents excellent growing state in the media, though at the IAC of 3000 mg·L1, strain W1 grows poorly. Thus strain W1 exhibits excellent substrate tolerance in the media containing high substrate concentrations. However, the ammonium removal ability of strain W1 presents somewhat different trend. At the IAC below 1200 mg·L1, strain W1 shows good removal rate of NH 4 -N and TN, especially at 200 mg·L1, NH 4 -N and TN removal reaches their maximum values, 92.34% and 81.41%, respectively. When IAC ranges from 1200 to 2000 mg·L1, strain W1 presents good growth but bad ammonium removal ability, mainly due to the prolonged adaptable phase with the increase of substrate concentration. In coking wastewater treatment, if the hydraulic retention time (HRT) of biological treatment is prolonged appropriately, it is possible to omit the pretreatment of coking wastewater and access directly to biological treatment. If so, the cost of wastewater treatment will be reduced substantially. Compared with strain A1[22], which was not able to efficiently transform the substrate at concentrations higher than (536.21±3.15) mg·L1, strain W1 presents excellent adaptability and good nitrification ability in the media containing high ammonium concentrations. To further explain the trend about the growth and ammonium removal of strain W1 at different substrate concentrations, the growth of strain in the medium containing low (100 mg·L1), intermediate (400 mg·L1) and high (1200 mg·L1) NH 4 -N concentrations was investigated. As shown in Fig. 10, the adaptable growth phase of strain W1 prolongs as INC increases, but at different INC, the growth rates of strain in logarithmic growth phase are of similar size. This indicates that the increment of INC has no influence on the activity of strain W1. Meanwhile, the ammonium removal rates increase with the increment of INC. They are 3.81, 7.05 and 12.95 mg·L1·h1 in the media containing 100, 400 and 1200 mg·L1 ammonium, respectively. These data show that nitrification

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Table 3 The changes of gas phase compositions in closed system (%, by volume) Initial O2

Initial N2

Final O2

Final N2

Other gases

100.00 (±1.00)

0.00 (±1.00)

52.51 (±1.79)

35.54 (±2.74)

11.95 (±0.05)

nitrification and aerobic denitrification simultaneously. The aerobic denitrification of strain W1 will be further studied. 4

Figure 10 Growth and ammonium removal in three media containing different initial ammonium concentration 1üfinal NH 4 -N, with initial NH 4 -N of 1200 mg˜L1; 2ü final NH 4 -N, with initial NH 4 -N of 400 mg·L1; 3üfinal NH 4 -N, with initial NH 4 -N of 100 mg˜L1; 4üOD600, with initial NH 4 -N of 100 mg˜L1; 5üOD600, with initial NH 4 -N of 400 mg·L1; 6üOD600, with initial NH 4 -N of 1200 mg˜L1

ability of strain W1 is not affected by the high substrate concentrations (INCİ2000 mg·L1). Figs. 9 and 10 indicate the reason why the removal efficiency of ammonium is inversely proportional to INC. As the INC increases, the adaptation phase extends, so that the time used for nitrification is shorter, lowering the removal efficiency of ammonium. If the time is enough for nitrification for high concentration ammonium, strain W1 will have the same removal efficiency as in low-strength ammonium. Thus, strain W1 exhibits high activity and excellent adaptability to environment containing high COD and ammonium, which is suitable for potential industrial applications. 3.6 Preliminary identification of aerobic denitrification

CONCLUSIONS

Using limited dilution method, one nitrifying bacterial strain was isolated and named as W1. By a series of physiological and biochemical methods and 16S rRNA, strain W1 was identified as Alcaligenes sp. The strain grew well and presented high ammonium removal ability in the medium containing high ammonium concentration (400 mg·L1), and had excellent tolerance to high substrate concentration (INCİ2000 mg·L1), with its activity affected little. In the optimized medium, the growth and ammonium removal ability of strain W1 were obviously improved in 4-day cultivation, in which C/N ratio was the most important factor for strain W1 to improve the process. TN removal ratio reached around 80%. The removed nitrogen far exceeded the quantity of nitrogen used in synthesizing cell. The production of N2 gas in pure oxygen system was examined. The result suggests that strain W1 performs heterotrophic nitrification and aerobic denitrification simultaneously. REFERENCES 1

2

3

4

It is known that the amount of intracellular nitrogen does not generally exceed 30% of total nitrogen. However, the TN removal in this study was up to 79.02% (Fig. 8). For the amount of intracellular nitrogen equal to 30% of total nitrogen, according to the nitrogen balance, 49.02% of TN was missing during the nitrogen removal. Hence, it is inferred that strain W1 performs aerobic denitrification besides heterotrophic nitrification. In order to identify the aerobic denitrification, the production of N2 gas in a closed system was examined. The results shown in Table 3 testify that strain W1 has the ability of aerobic denitrification. At the same time, the removal efficiency of ammonium was 92.43% (data not shown). Thus, it can be concluded that strain W1 performs heterotrophic

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