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Troubleshooting and Optimization of High-Strength Inhibitory Chemical Wastewater Treatment Process
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作者 严月根 Calvert C.Churn +2 位作者 何光辉 郑巧庚 Philip C.Y.Wong 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2005年第6期800-808,共9页
Wastewaters from the chemical industry are usually of high-strength and may contain minor inhibitory and recalcitrant organics that are at times not readily identifiable. This paper describes the experience of a biolo... Wastewaters from the chemical industry are usually of high-strength and may contain minor inhibitory and recalcitrant organics that are at times not readily identifiable. This paper describes the experience of a biological waste water treatment plant (WWTP) processing a COD concentration of 43000 mg·L^-1 wastewater from an oxochemical manufacturing plant. Stage improvements of the plant process by dilution of the inhibitory influent using other chemical wastewater streams resulting in a synergistic process effect, and removal of inhibitory organics by phase separation via acidification, effectively achieved process optimization producing a high quality effluent. In particular, the COD removal efficiency of granular sludge based anaerobic reactors increased from 56% to 90%. The final effluent COD decreased from 250mg·L^-1 to 50mg·L^-1, consistently meeting the COD concentration of 100 mg·L^-1 regulatory discharge limit. The success of the process enhancements supports the hypothesis that long-chain quaternary carboxylic acids act as substrate inhibitors in the biological process. 展开更多
关键词 operational experience waste water treatment plant (WVCTP) granular sludge chemical wastewater INHIBITORY RECALCITRANT long-chain quaternary carboxylic acids
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A Case Study on the Utilization of Wind Energy Potential on Remote and Isolated Small Wastewater Plants 被引量:1
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作者 Joao Femando Pereira Gomes Pedro Manuel Saraiva Cardoso 《Journal of Energy and Power Engineering》 2012年第4期554-560,共7页
Small WWTP (wastewater treatment plants) are frequently located, by necessity, in remote and isolated sites, which increases the difficulty of its energy supply. This paper describes a case study which is a step by ... Small WWTP (wastewater treatment plants) are frequently located, by necessity, in remote and isolated sites, which increases the difficulty of its energy supply. This paper describes a case study which is a step by step procedure concerning the evaluation of the wind potential of sites that are dependent of in-situ energy generation, as well as, on the utilization of the potential wind energy in Magoito WWTP. The adopted methodology comprised the collection of one year of in-situ wind data and its validation by comparison with historical data of more than 10 years of a nearby anemometric station. The data provided by the two anemometric stations was statistically treated and allowed the analysis of the results from the two stations. These results are promising in terms of wind availability and velocity. Finally, the study comprised the simulation of the local wind conditions for a considerable larger area in order to find the best site for locating a wind turbine. 展开更多
关键词 Wind energy waste water treatment plants wind potential.
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Overview coking plant & Lurgi gasifier plant waste water treatment
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作者 HU Lishun 1 , WANG Sijing 2 , HUANG Yan 2 , XUE Junli 1 ( 1 Fuels and Emissions Lab , GE Global Research Shanghai , Shanghai , China 2 GE Energy-Power & Water , Shanghai , China ) 《化工进展》 EI CAS CSCD 北大核心 2012年第S1期298-301,共4页
The paper described the coking plant and Lurgi gasifier plant waste water types and characteristics , comparing the COD and ammonia-N level in different source of waste water in the plant.The currently maturity coking... The paper described the coking plant and Lurgi gasifier plant waste water types and characteristics , comparing the COD and ammonia-N level in different source of waste water in the plant.The currently maturity coking plant waste water treatment method was statement in the paper and analyzed the pros and cons of each method.The primary cost analysis of each type of waste water treatment was also completed in the paper.According to these analyses , recommendation was prepared for coking plant and Lurgi gasifier plant waste water treatment. 展开更多
关键词 COD Lurgi gasifier plant waste water treatment Overview coking plant SCWO FIGURE
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Occurrence,distribution,and potential influencing factors of sewage sludge components derived from nine full-scale wastewater treatment plants of Beijing,China 被引量:3
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作者 Xu Wang Meiyan Li +1 位作者 Junxin Liu Jiuhui Qu 《Journal of Environmental Sciences》 SCIE EI CAS CSCD 2016年第7期233-239,共7页
Millions of tons of waste activated sludge(WAS) produced from biological wastewater treatment processes cause severe adverse environmental consequences. A better understanding of WAS composition is thus very critica... Millions of tons of waste activated sludge(WAS) produced from biological wastewater treatment processes cause severe adverse environmental consequences. A better understanding of WAS composition is thus very critical for sustainable sludge management. In this work, the occurrence and distribution of several fundamental sludge constituents were explored in WAS samples from nine full-scale wastewater treatment plants(WWTPs) of Beijing, China. Among all the components investigated, active heterotrophic biomass was dominant in the samples(up to 9478 mg/L), followed by endogenous residues(6736 mg/L),extracellular polymeric substances(2088 mg/L), and intracellular storage products(464 mg/L)among others. Moreover, significant differences(p 〈 0.05) were observed in composition profiles of sludge samples among the studied WWTPs. To identify the potential parameters affecting the variable fractions of sludge components, wastewater source as well as design and operational parameters of WWTPs were studied using statistical methods. The findings indicated that the component fraction of sewage sludge depends more on wastewater treatment alternatives than on wastewater characteristics among other parameters. A principal component analysis was conducted, which further indicated that there was a greater proportion of residual inert biomass in the sludge produced by the combined system of the conventional anaerobic/anoxic/oxic process and a membrane bioreactor. Additionally, a much longer solids retention time was also found to influence the sludge composition and induce an increase in both endogenous inert residues and extracellular polymeric substances in the sludge. 展开更多
关键词 wastewater treatment plant waste activated sludge Sludge component Solids retention time Extracellular polymeric substances Principal component analysis
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Characterization of odorous charge and photochemical reactivity of VOC emissions from a full-scale food waste treatment plant in China 被引量:7
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作者 Zhe Ni Jianguo Liu +3 位作者 Mingying Song Xiaowei Wang Lianhai Ren Xin Kong 《Journal of Environmental Sciences》 SCIE EI CAS CSCD 2015年第3期34-44,共11页
Food waste treatment plants (FWTPs) are usually associated with odorous nuisance and health risks, which are partially caused by volatile organic compound (VOC) emissions. This study investigated the VOC emissions... Food waste treatment plants (FWTPs) are usually associated with odorous nuisance and health risks, which are partially caused by volatile organic compound (VOC) emissions. This study investigated the VOC emissions from a selected full-scale FWTP in China. The feedstock used in this plant was mainly collected from local restaurants. For a year, the FWTP was closely monitored on specific days in each season. Four major indoor treatment units of the plant, including the storage room, sorting/crushing room, hydrothermal hydrolysis unit, and aerobic fermentation unit, were chosen as the monitoring locations. The highest mean concentration of total VOC emissions was observed in the aerobic fermentation unit at 21,748.2-31,283.3 μg/m^3, followed by the hydrothermal hydrolysis unit at 10,798.1-23,144.4 μg/m^3. The detected VOC families included biogenic compounds (oxygenated compounds, hydrocarbons, terpenes, and organosulfur compounds) and abiogenic compounds (aromatic hydrocarbons and halocarbons). Oxygenated compounds, particularly alcohols, were the most abundant compounds in all samples. With the use of odor index analysis and principal components analysis, the hydrothermal hydrolysis and aerobic fermentation units were clearly distinguished from the pre-treatment units, as characterized by their higher contributions to odorous nuisance. Methanthiol was the dominant odorant in the hydrothermal hydrolysis unit, whereas aldehyde was the dominant odorant in the aerobic fermentation unit. Terpenes, specifically limonene, had the highest level of propylene equivalent concentration during the monitoring periods. This concentration can contribute to the increase in the atmospheric reactivity and ozone formation potential in the surrounding air. 展开更多
关键词 Food waste treatment plant In-situ monitoring VOC emissions Odorous charge Photochemical reactivity
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Performance of Wuxi WWTP in China 被引量:1
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作者 WANGLin WANGLi JIANGYifeng: 《Journal of Ocean University of Qingdao》 2003年第2期224-229,共6页
In Wuxi Wastewater Treatment Plant, the Anaerobic, anoxic and oxic (A2/O) process was employed to remove the nitrogen and phosphorus, which exhibited the positive results of the high removal efficiency for phosphorus ... In Wuxi Wastewater Treatment Plant, the Anaerobic, anoxic and oxic (A2/O) process was employed to remove the nitrogen and phosphorus, which exhibited the positive results of the high removal efficiency for phosphorus with a range of 67.7% to 89.9% and an average value of 78.0. The effluent of phosphorus met the national discharge standard. The removal of TN was effected by both BOD variation of influent and wastewater temperature. TN removal was in the range of 28.5% to 55.8% with an average value of 39.4%. The energy cost was 0.15 kWh(m3d)-1 or 1.35 kWh(kgBOD@d)-1. The annual average sludge production was 46.3 m3d-1, the annual average dosage for the dewatering was 40 kg d-1 . 展开更多
关键词 waste water treatment plant (WWTP) combined collection system organic load nutrient removal operation and management cost (O&M cost) ANAEROBIC anoxic and oxic (A^2/O)
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