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Frontiers of Environmental Science & Engineering

ISSN 2095-2201

ISSN 2095-221X(Online)

CN 10-1013/X

Postal Subscription Code 80-973

2018 Impact Factor: 3.883

Front. Environ. Sci. Eng.    2018, Vol. 12 Issue (6) : 12    https://doi.org/10.1007/s11783-018-1055-6
RESEARCH ARTICLE
Reduction of wastewater toxicity and change of microbial community in a hydrolysis acidification reactor pre-treating trimethylolpropane wastewater
Xin Xing1,2, Yin Yu2, Hongbo Xi2(), Guangqing Song2, Yajiao Wang1, Jiane Zuo1, Yuexi Zhou2
1. State Key Joint Laboratory of Environment Simulation and Pollution Control, School of Environment, Tsinghua University, Beijing 100084, China
2. Research Center of Water Pollution Control Technology, Chinese Research Academy of Environmental Sciences, Beijing 100012, China
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Abstract

HAP was verified to reduce the toxicity of TMP wastewater effectively.

Actual TMP wastewater was fed in HAP with different dilution ratios for 240 days.

Formaldehyde, 2-ethylacrolein, TMP and 2-ethylhexanol were all greatly removed.

Firmicutes became the dominant phylum (the abundance increased to 57.08%).

Trimethylolpropane (TMP) wastewater is one of the most toxic petrochemical wastewater. Toxicants with high concentrations in TMP wastewater often inhibit the activity of microorganisms associated with biological treatment processes. The hydrolysis acidification process (HAP) is widely used to pre-treat petrochemical wastewater. However, the effects of HAP on the reduction of wastewater toxicity and the relevant underlying mechanisms have rarely been reported. In this study, an HAP reactor was operated for 240 days, fed with actual TMP wastewater diluted by tap water in varying ratios. The toxicity of TMP wastewater was assessed with the inhibition ratio of oxygen uptake rate. When the organic loading rates were lower than 7.5 kg COD/m3/d, the toxicity of TMP wastewater was completely eliminated. When the actual TMP wastewater was directly fed into the reactor, the toxicity of TMP wastewater decreased from 100% to 34.9%. According to the results of gas chromatography-mass spectrometry analysis, four main toxicants contained in TMP wastewater, namely, formaldehyde, 2-ethylacrolein, TMP and 2-ethylhexanol, were all significantly removed, with removal efficiencies of 93.42%, 95.42%, 72.85% and 98.94%, respectively. Compared with the removal efficiency of CODCr, the reduction rate of toxicity is markedly higher by HAP. In addition, the change of microbial community in the HAP reactor, along the operation period, was studied. The results revealed that, compared with the seed sludge, Firmicutes became the dominant phylum (abundance increased from 0.51% to 57.08%), followed by Proteobacteria and Bacteroidetes (abundance increased from 59.75% to 25.99% and from 4.70% to 8.39%, respectively).

Keywords Trimethylolpropane wastewater      Hydrolysis acidification process      Toxicity      Oxygen uptake rate      16S rDNA     
Corresponding Author(s): Hongbo Xi,Yuexi Zhou   
Issue Date: 19 August 2018
 Cite this article:   
Xin Xing,Yin Yu,Hongbo Xi, et al. Reduction of wastewater toxicity and change of microbial community in a hydrolysis acidification reactor pre-treating trimethylolpropane wastewater[J]. Front. Environ. Sci. Eng., 2018, 12(6): 12.
 URL:  
https://academic.hep.com.cn/fese/EN/10.1007/s11783-018-1055-6
https://academic.hep.com.cn/fese/EN/Y2018/V12/I6/12
Fig.1  Schematic diagram of the HAP reactor
Item Value
CODCr 9000 mg/L
pH 3.8
TOC 2560 mg/L
TN 1.468 mg/L
Cl- 9.8467 mg/L
Fe 0.3927 mg/L
Mn 0.0016 mg/L
Cu Not detected
Zn Not detected
Suspend solid 19 mg/L
Tab.1  The characteristics of raw TMP wastewater
Fig.2  CODCr and TOC organic loading rates in influent and effluent and their removal efficiencies. (a) COD (The OLR was 0.5 kg COD/m3/d for stage I, 1 kg COD/m3/d for stage II, 1.8 kg COD/m3/d for stage III, 2.7 kg COD/m3/d for stage IV, 3.5 kg COD/m3/d for stage V, 5 kg COD/m3/d for stage VI, 7.5 kg COD/m3/d for stage VII and 9 kg COD/m3/d for stage VIII); (b) TOC (The OLR was 0.3 kg TOC/m3/d for stage I, 0.6 kg TOC/m3/d for stage II, 1 kg TOC/m3/d for stage III, 1.5 kg TOC/m3/d for stage IV, 2.1 kg TOC/m3/d for stage V, 2.8 kg TOC/m3/d for stage VI, 3.5 kg TOC/m3/d for stage VII and 3.8 kg TOC/m3/d for stage VIII)
Fig.3  Changes of the organic substances in the influent and effluent. (a) Formaldehyde; (b) TMP; (c) Butanoic acid; (d) 2-Ethylacrolein; (e) 2-Ethylhexanol; (f) 2-Ethylhexanoic acid
Operation stage Toxicities (%)
Influent Effluent
Stage I not observed Not observed
Stage II not observed Not observed
Stage III not observed Not observed
Stage IV 33.8±1.7 Not observed
Stage V 42.3±1.1 Not observed
Stage VI 68.4±0.1 Not observed
Stage VII 97.3±0.5 Not observed
Stage VIII 100±0.0 34.9±2.2
Tab.2  Toxicities of the influent and effluent of the hydrolysis acidification process reactor pre-treating TMP wastewater for each stage
Fig.4  Scanning electron micrographs of sludge in HAP reactor on day 0 ((a) and (b)), day 56 ((c) and (d)), and day 212 ((e) and (f))
Type of microorganisms Sample OTUsa) Coverage Species Chao1 Shannon
Eubacteria E0 690 0.9916 600 687.24 6.9606
E7 783 0.9863 661 879.48 6.5656
E14 904 0.9870 743 912.58 7.1888
E28 817 0.9872 675 848.91 7.0794
E42 605 0.9892 442 635.80 4.0923
E56 696 0.9870 495 784.60 5.2093
E70 732 0.9911 468 570.59 5.2922
E100 615 0.9915 331 477.23 3.5828
E212 283 0.9945 270 351.03 4.1672
E240 314 0.9949 263 355.50 4.1458
Archaea A#1 415 0.9936 387 475.67 3.0412
A#4 802 0.9827 707 1103.77 3.4801
A#6 796 0.9847 661 977.38 3.3352
A#8 820 0.9847 820 1061.22 4.8007
Tab.3  Characteristics of community diversity in sludge samples
Fig.5  Microbial community structure and diversity of eubacteria at the phylum level (a) and generic level (b). The abundance is presented as the percentage of the total effective eubacterial sequences in each sample
Fig.6  Microbial community structure and diversity of Archaea at the genus level
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