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介绍了永嘉县电镀废水的产生及排放现状,针对其电镀废水的性质及污染状况,提出了具体的治理措施,并以永嘉县电镀企业现状为参照,从电镀企业污染源控制技术上提出了一些综合电镀污水处理技术方案以及统一规划、统一管理的集中控制建议。 相似文献
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氯化铁处理AB工艺二级出水中的磷 总被引:1,自引:1,他引:0
铁盐混凝剂因其高电荷、安全无毒、易于控制等优点,在城市污水厂除磷方面得到了进一步的发展和应用。为了考察FeCl3除磷的作用特征,探讨除磷效率随pH值、FeCl3投加量等混凝参数的变化规律,以氯化铁(FeCl3)为除磷剂,某城市污水处理厂二级出水为实验水样,进行了实验研究。研究结果表明,水样的硬度对混凝剂除磷性能有较大影响,在最佳工艺条件———不调节水样pH值、FeCl3投加量为75 mg/L时,可将废水中的总磷含量从4.95 mg/L降至0.44 mg/L以下,处理出水可达《城镇污水处理厂污染物排放标准》(GB 18918-2002)中的一级A排放标准(GB18918-2002)(TP<0.50 mg/L)。 相似文献
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Simultaneous removal of ammonium and phosphate by zeolite synthesized
from coal fly ash as influenced by acid treatment 总被引:5,自引:0,他引:5
ZHANG Bao-hu WU De-yi WANG Chong HE Sheng-bing ZHANG Zhen-ji KONG Hai-nan 《环境科学学报(英文版)》2007,19(5):540-545
Zeolite synthesized from fly ash (ZFA) without modification is not efficient for the purification of NH4+ and phosphate at low concentrations that occur in real effluents, despite the high potential removal capacity. To develop an effective technique to enhance the removal efficiency of ammonium and phosphate at low concentrations, ZFA was modified with acid treatment and the simultaneous removal of ammonium and phosphate in a wide range of concentration was investigated. It was seen that when compared with untreated ZFA, only the treatment by 0.01 mol/L of H2SO4 significantly improved the removal efficiency of ammonium at low initial concentrations. The behavior was well explained by the pH effect. Treatment by more concentrated H2SO4 led to the deterioration of the ZFA structure and a decrease in the cation exchange capacity. Treatment by 0.01 mol/L H2SO4 improved the removal efficiency of phosphate by ZFA at all initial P concentrations, while the treatment by concentrated H2SO4 (≥0.9 mol/L) resulted in a limited maximum phosphate immobilization capacity (PIC). It was concluded that through a previous mild acid treatment (e.g. 0.01 mol/L of H2SO4), ZFA can be used in the simultaneous removal of NH4+ and P at low concentrations simulating real effluent. 相似文献
448.
Chinese traditional medicine wastewater, rich in macromolecule and easy to foam in aerobic biodegradation such as Glycosides, was treated by two identical bench-scale aerobic submerged membrane bioreactors (SMBRs) operated in parallel under the same feed, equipped with the same electronic control backwashing device. One was used as the control SMBR (CSMBR) while the other was dosed with powdered activated carbon (PAC) (PAC-amended SMBR, PSMBR). The backwashing interval was 5 min. One suction period was about 90 min by adjusting preestablished backwashing vacuum and pump frequency. The average flux of CSMBR during a steady periodic state of 24 d (576 h) was 5.87 L/h with average hydraulic residence time (HRT) of 5.97 h and that of PSMBR during a steady periodic state of 30 d (720 h) was 5.85 L/h with average HRT of 5.99 h. The average total chemical oxygen demand (COD) removal efficiency of CSMBR was 89.29% with average organic loading rate (OLR) at 4.16 kg COD/(m^3.d) while that of PSMBR was 89.79% with average OLR at 5.50 kg COD/(m^3.d). COD concentration in the effluent of both SMBRs achieved the second level of the general wastewater effluent standard GB8978-1996 for the raw medicine material industry (300 mg/L). Hence, SMBR with electronic control backwashing was a viable process for medium-strength Chinese traditional medicine wastewater treatment. Moreover, the increasing rates of preestablished backwashing vacuum, pump frequency, and vacuum and flux loss caused by mixed liquor in PSMBR all lagged compared to those in CSMBR; thus the actual operating time of the PSMBR system without membrane cleaning was extended by up to 1.25 times in contrast with the CSMBR system, and the average total COD removal efficiency of PSMBR was enhanced with higher average OLR. 相似文献
449.
Overland flow (OF) systems were evaluated and compared for advanced treatment of municipal and industrial effluents, including nutrients and nondegradable chemical oxygen demand (COD) removal. Three pilot plants were constructed at the Shahin Shahr Wastewater Treatment Plant (WWTP), Isfahan, Iran. Each pilot was assigned a specific wastewater and all were simultaneously operated for 8 months. Treatment of primary effluent, activated sludge secondary effluent, and lagoon effluent of textile wastewater was investigated at application rates (ARs) of 0.15, 0.25, and 0.35m(3)m(-1)h(-1). During 5 months of stable operation after a 3-month acclimation period, mean removals of total 5-day biochemical oxygen demand (TBOD(5)), total COD (TCOD), total suspended solids (TSS), total nitrogen (TN), total phosphorus (TP) and turbidity were 74.5%, 54.8%, 66.2%, 39.4%, 35.8%, and 67.7% for primary effluent; 52.9%, 52.9%, 66.5%, 44.4%, 39.8%, and 50.1% for activated sludge effluent; 65.7%, 58.7%, 70.3%, 41.7%, 41.3%, and 54.9% for textile wastewater lagoon effluent, respectively. The model of Smith and Schroeder, 1985. Field studies of the overland flow process for the treatment of raw and primary treated municipal wastewater. Journal of Water Pollution Control Federation 57, 785-794] was satisfactory for TBOD(5). For all treatment parameters a standard first-order removal model was inadequate to represent the data but a modified first-order model provided a satisfactory fit to the data. Based on the results of this study, it can be concluded that an OF system as advanced treatment had the ability to meet effluent discharge permit limits and was an economical replacement for stabilization ponds and mechanical treatment options. 相似文献
450.
This article describes how options for managing dairy effluent on the Lower Murray River in South Australia were evaluated
using multiple criteria analysis (MCA). Multiple criteria analysis is a framework for combining multiple environmental, social,
and economic objectives in policy decisions. At the time of the study, dairy irrigation in the region was based on flood irrigation
which involved returning effluent to the river. The returned water contained nutrients, salts, and microbial contaminants
leading to environmental, human health, and tourism impacts. In this study MCA was used to evaluate 11 options against 6 criteria
for managing dairy effluent problems. Of the 11 options, the MCA model selected partial rehabilitation of dairy paddocks with
the conversion of remaining land to other agriculture. Soon after, the South Australian Government adopted this course of
action and is now providing incentives for dairy farmers in the region to upgrade irrigation infrastructure and/or enter alternative
industries. 相似文献