Pretreatment of hypersaline mustard wastewater with integrated bioreactor

Qiang He , Ting-ting Zhang , Hong-xiang Chai , Shi-wei Yang , Jian Zhou , Guo-jun Du

Journal of Central South University ›› 2012, Vol. 19 ›› Issue (6) : 1673 -1678.

PDF
Journal of Central South University ›› 2012, Vol. 19 ›› Issue (6) : 1673 -1678. DOI: 10.1007/s11771-012-1192-1
Article

Pretreatment of hypersaline mustard wastewater with integrated bioreactor

Author information +
History +
PDF

Abstract

A full-scale experimental study of treating mustard wastewater by the integrated bioreactor with designed scale of 1 000 m3/d is conducted combined with a demonstration project. The systematical researches on the efficiency of combined operation conditions of anaerobic-aerobic and anaerobic-aerobic-flocculation as well as chemical phosphorus removal of hypersaline mustard wastewater are conducted. The optimal operation condition and parameters in pretreatment of mustard wastewater in winter (the water temperature ranges 8–15 °C) are determined: the anaerobic load is 3.0 kg (COD)/(m3·d), the average COD and phosphate concentration of the inflow are respectively 3 883 mg/L and 35.53 mg/L and the dosage of flocculent (PAC) is 400 mg/L. The anaerobic-aerobic-flocculation combined operation condition and postpositive phosphorous removal with ferrous sulfate are employed. After treatment, the COD of the effluent is 470 mg/L and the average phosphate concentration is 5.09 mg/L. The effluent could achieve the third-level of Integrated Wastewater Discharge Standard (GB 8978-1996).

Keywords

mustard wastewater / aerobic treatment / anaerobic treatment / integrated bioreactor / chemical phosphorus removal

Cite this article

Download citation ▾
Qiang He, Ting-ting Zhang, Hong-xiang Chai, Shi-wei Yang, Jian Zhou, Guo-jun Du. Pretreatment of hypersaline mustard wastewater with integrated bioreactor. Journal of Central South University, 2012, 19(6): 1673-1678 DOI:10.1007/s11771-012-1192-1

登录浏览全文

4963

注册一个新账户 忘记密码

References

[1]

LefebvreO., MolettaR.. Treatment of organic pollution in industrial saline wastewater: A literature review [J]. Water Research, 2006, 40(20): 3671-3682

[2]

UygurA., KargiF.. Salt inhibition on biological nutrient removal from saline wastewater in a sequencing batch reactor [J]. Enzyme Microbial Technology, 2004, 34(3/4): 313-318

[3]

FontenotQ., BonvillainC., KilgenM., BoopathyR.. Effects of temperature, salinity, and carbon:nitrogen ratio on sequencing batch reactor treating shrimp aquaculture wastewater [J]. Bioresource Technology, 2007, 8(9): 1700-1703

[4]

WenX.-h., ZhanX.-m., WangJ.-l., QianYi.. Review of the biological treatment of salinity wastewater [J]. Environmental Science, 1999, 20(3): 104-106

[5]

CristinaS. C. C., PaulaV. B. Q., GabrielaS., LuísF. C. C., HansB., SandraC. M., PaulaM. L. C.. Use of constructed wetland systems with Arundo and Sarcocornia for polishing high salinity tannery wastewater [J]. Journal of Environmental Management, 2012, 95(1): 66-71

[6]

KartalB. I., KolevaM., ArsovR., StarW. V. D., JettenM. S. M., ScrousM.. Adaptation of a freshwater anammox population to high salinity wastewater [J]. Journal of Biotechnology, 2006, 126: 546-553

[7]

WindeyK., BoI. D., VerstraeteW.. Oxygen-limited autotrophic nitrification-denitrification (OLAND) in a rotating biological contactor treating high-salinity wastewater [J]. Water Research, 2005, 39(18): 4512-4520

[8]

GuerreroL., OmilF., MendezR., LemaJ. M.. Treatment of saline wastewater from fish meal factories in an anerobic filter under extreme ammonia concentrations [J]. Bioresource Technology, 1997, 61(1): 69-78

[9]

MonhanS. V., BabuV. L., BhaskarY. V.. Influence of recirculation on the performance of anaerobic sequencing batch biofilm reactor (AnSBBR) treating hypersaline composite chemical wastewater [J]. Bioresource Technology, 2007, 98(7): 1373-1379

[10]

ZhouJ., GanC.-j., LongT.-r., ChaiH.-xian.. Research on efficiency of anaerobic sequencing batch biofilm reactor for hypersalt mustard tuber wastewater treatment [J]. China Water & Wastewater, 2006, 22(17): 77-79

[11]

YangL.. Biodegradation of dispersed diesel fuel and high salinity conditions [J]. Water Research, 2000, 34(13): 3303-3314

[12]

YangL., LaiC. T.. Biological treatment of mineral oil in a salty environment [J]. Water Science and Technology, 2005, 42(5): 369-375

[13]

MaQ., XuD.-w., GuX.-xi.. Study on the treatment of mustard tuber wastewater with high salinity by UASB-aerobic-coagulation process [J]. Industrial Water Treatment, 2011, 31(4): 62-65

[14]

WuD.-j., SunW., TanF.-xun.. Experimental study on the treatment of mustard tuber wastewater by the process of hydrolysis-acidgenesis-SBR-coagulation [J]. Technology of Water Treatment, 2009, 35(6): 60-63

[15]

FengX.-h., ZhuM.-x., WenL.-q., DingS.-ming.. Removal of COD from mustard wastewater by Fenton-like reagents oxidation process [J]. Chinese Journal of Environmental Engineering, 2008, 2(11): 1483-1486

[16]

LiZ., ZhouJ., ZengC.-yin.. Nature of the vegetable processing wastewater and its influence on the secondary sedimentation in activated sludge process [J]. Water & Wastewater Engineering, 2005, 31(11): 57-60

[17]

ZhouJ., WuQ.-t., LongT.-r., WangX.-ming.. Establishment of microbiological system for treatment of mustard tuber wastewater with high salinity [J]. China Water & Wastewater, 2007, 23(15): 17-20

[18]

ChenY., ZengC.-y., LongT.-r., LiX.-ping.. Selection of aerobic biological process for treatment of integrated mustard tuber wastewater [J]. China Water & Wastewater, 2009, 25(15): 21-24

AI Summary AI Mindmap
PDF

109

Accesses

0

Citation

Detail

Sections
Recommended

AI思维导图

/