The design and running effect of treatment of wastewater from pharmaceutical intermittent production by iron-carbon(Fe/C)-Fentonhydrolysis acidification-anoxic/aerobic(A/O)process were introduced.The results of co...The design and running effect of treatment of wastewater from pharmaceutical intermittent production by iron-carbon(Fe/C)-Fentonhydrolysis acidification-anoxic/aerobic(A/O)process were introduced.The results of continuous operation showed that when the flow rate of the influent wastewater was 300 m^3/d,after the influent high-concentration wastewater(CODCrand NH4+-N concentration were 35 000 and 1 000 mg/L,respectively)and medium-concentration wastewater(CODCrand NH4+-N concentration were 1 500 and 100 mg/L,respectively)were treated by the process,CODCrand NH4+-N concentration in the effluent decreased to 360-410 and 20-25 mg/L,respectively,and the quality of the effluent could meet the Grade III standard of Integrated Wastewater Discharge Standard(GB 8978-1996).The combined process was proved to be an effective method to treat wastewater from pharmaceutical intermittent production,and its operation was stable.展开更多
How to use water resource effectively is an important problem in developing industry. Three combined processes which are composed of oil separator+de-emulsification flocculation+sand filtration (SDF), oil separato...How to use water resource effectively is an important problem in developing industry. Three combined processes which are composed of oil separator+de-emulsification flocculation+sand filtration (SDF), oil separator q-hydrolytic acidification+SBR (SAS) and oil separator+de emulsification flocculation +SBR (SDS) are conducted in laboratory-scale experiment to treat oil extraction wastewater for an oil field. The experimental results show that the removal rate of COD(chemistry oxygen demand) and oil treated by SDF process are 85 % and 95 % respectively, the residual oil in effluent can meet the discharge standard, but the residual COD can not. The removal rate of COD and BOD (biological oxygen demand) of the SAS effluent are 85% and 90% respectively, the BOD can meet but the COD can not meet discharge standard. So the further treatment is required in the process. The SDS effluent with removal rate of 95% and 90% are obtained for COD and BOD respectively, which can completely meet the national standards of oil wastewater discharge and refilling (China). The experimental result shows that oil extraction wastewater has turned into water resource after being, treated by SDS.展开更多
A combined system consisting of hydrolysis acidification, denitrification and nitrification reactors was used to remove carbon and nitrogen from the nylon - 6 production wastewater, which was characterized by good bio...A combined system consisting of hydrolysis acidification, denitrification and nitrification reactors was used to remove carbon and nitrogen from the nylon - 6 production wastewater, which was characterized by good biodegradability and high nitrogen concentration. The influences of Chemical Oxygen Demand (COD) in the influent, recirculation ratio, Hydraulic Residence Time (HRT) and Dissolved Oxygen (DO) concentration on the system performances were investigated. From results it could be seen that good performances have been achieved during the overall experiments periods, and COD, Total Nitrogen (TN), NH^+ -N and Suspended Solids (SS) in the effluent were 53, 16, 2 and 24 mg· L^-1, respectively, which has satisfied the first standard of wastewater discharge established by Environmental Protection Agency (EPA) of China. Furthermore, results showed that operation factors, viz. COD in the influent, recirculation ratio, HRT and DO concentration, all had important influences on the system performances.展开更多
Carbon source is a critical constraint on nutrient removal in domestic wastewater treatment.However,the functions of particulate organic matter(POM) and some organics with high molecular weight(HMW) are overlooked...Carbon source is a critical constraint on nutrient removal in domestic wastewater treatment.However,the functions of particulate organic matter(POM) and some organics with high molecular weight(HMW) are overlooked in the conventional process,as they cannot be directly assimilated into cells during microbial metabolism.This further aggravates the problem of carbon source shortage and thus affects the effluent quality.Therefore,to better characterize organic matter(OM) based MW distribution,microfiltration/ultrafiltration/nanofiltration(MF/UF/NF) membranes were used in parallel to fractionate OM,which obtained seven fractions.Hydrolysis acidification(HA) was adopted to manipulate the MW distribution of dissolved organic matter(DOM) and further explore the correlation between molecular size and biodegradability.Results showed that HA pretreatment of wastewater not only promoted transformation from POM to DOM,but also boosted biodegradability.After 8 hr of HA,the concentration of dissolved organic carbon(DOC) increased by 65%,from the initial value of20.25 to 33.48 mg/L,and the biodegradability index(BOD5(biochemical oxygen demand)/SCOD(soluble chemical oxygen demand)) increased from 0.52 to 0.74.Using MW distribution analysis and composition optimization,a new understanding on the characteristics of organics in wastewater was obtained,which is of importance to solving low C/N wastewater treatment in engineering practice.展开更多
文摘The design and running effect of treatment of wastewater from pharmaceutical intermittent production by iron-carbon(Fe/C)-Fentonhydrolysis acidification-anoxic/aerobic(A/O)process were introduced.The results of continuous operation showed that when the flow rate of the influent wastewater was 300 m^3/d,after the influent high-concentration wastewater(CODCrand NH4+-N concentration were 35 000 and 1 000 mg/L,respectively)and medium-concentration wastewater(CODCrand NH4+-N concentration were 1 500 and 100 mg/L,respectively)were treated by the process,CODCrand NH4+-N concentration in the effluent decreased to 360-410 and 20-25 mg/L,respectively,and the quality of the effluent could meet the Grade III standard of Integrated Wastewater Discharge Standard(GB 8978-1996).The combined process was proved to be an effective method to treat wastewater from pharmaceutical intermittent production,and its operation was stable.
文摘How to use water resource effectively is an important problem in developing industry. Three combined processes which are composed of oil separator+de-emulsification flocculation+sand filtration (SDF), oil separator q-hydrolytic acidification+SBR (SAS) and oil separator+de emulsification flocculation +SBR (SDS) are conducted in laboratory-scale experiment to treat oil extraction wastewater for an oil field. The experimental results show that the removal rate of COD(chemistry oxygen demand) and oil treated by SDF process are 85 % and 95 % respectively, the residual oil in effluent can meet the discharge standard, but the residual COD can not. The removal rate of COD and BOD (biological oxygen demand) of the SAS effluent are 85% and 90% respectively, the BOD can meet but the COD can not meet discharge standard. So the further treatment is required in the process. The SDS effluent with removal rate of 95% and 90% are obtained for COD and BOD respectively, which can completely meet the national standards of oil wastewater discharge and refilling (China). The experimental result shows that oil extraction wastewater has turned into water resource after being, treated by SDS.
基金Shanghai Science and Technology Committee(No.042312045)Shanghai Post-doctor Fund
文摘A combined system consisting of hydrolysis acidification, denitrification and nitrification reactors was used to remove carbon and nitrogen from the nylon - 6 production wastewater, which was characterized by good biodegradability and high nitrogen concentration. The influences of Chemical Oxygen Demand (COD) in the influent, recirculation ratio, Hydraulic Residence Time (HRT) and Dissolved Oxygen (DO) concentration on the system performances were investigated. From results it could be seen that good performances have been achieved during the overall experiments periods, and COD, Total Nitrogen (TN), NH^+ -N and Suspended Solids (SS) in the effluent were 53, 16, 2 and 24 mg· L^-1, respectively, which has satisfied the first standard of wastewater discharge established by Environmental Protection Agency (EPA) of China. Furthermore, results showed that operation factors, viz. COD in the influent, recirculation ratio, HRT and DO concentration, all had important influences on the system performances.
基金supported by the Jiangsu Water Resources Protection Project(No.2015005)the National High-Tech Research Program(863)of China(No.2012AA063302)the Fundamental Research Funds for Central Universities(No.2013/B14020391)
文摘Carbon source is a critical constraint on nutrient removal in domestic wastewater treatment.However,the functions of particulate organic matter(POM) and some organics with high molecular weight(HMW) are overlooked in the conventional process,as they cannot be directly assimilated into cells during microbial metabolism.This further aggravates the problem of carbon source shortage and thus affects the effluent quality.Therefore,to better characterize organic matter(OM) based MW distribution,microfiltration/ultrafiltration/nanofiltration(MF/UF/NF) membranes were used in parallel to fractionate OM,which obtained seven fractions.Hydrolysis acidification(HA) was adopted to manipulate the MW distribution of dissolved organic matter(DOM) and further explore the correlation between molecular size and biodegradability.Results showed that HA pretreatment of wastewater not only promoted transformation from POM to DOM,but also boosted biodegradability.After 8 hr of HA,the concentration of dissolved organic carbon(DOC) increased by 65%,from the initial value of20.25 to 33.48 mg/L,and the biodegradability index(BOD5(biochemical oxygen demand)/SCOD(soluble chemical oxygen demand)) increased from 0.52 to 0.74.Using MW distribution analysis and composition optimization,a new understanding on the characteristics of organics in wastewater was obtained,which is of importance to solving low C/N wastewater treatment in engineering practice.