Prospects for a self-sustainable sewage treatment system: a case study on full-scale UASB system in India's Yamuna River Basin

The government of India decided to launch a project to implement 16 full-scale Upflow Anaerobic Sludge Blanket (UASB) reactors (with a total capacity of 598,000 m(3)/d) in the Yamuna River basin under its Yamuna Action Plan (YAP). A polishing pond called the Final Polishing Unit (FPU) was utilized for post-treatment. This paper evaluates the sewage treatment efficiency of the combined system of full-scale UASB reactors and polishing ponds under Indian climatic conditions. Results have shown that the effluent from the sewage treatment plants (STPs) investigated failed to comply with applicable discharge standards in terms of BOD, SS, and fecal coliform removal. Therefore, it is proposed that such proper operation and maintenance as removing excess sludge and scum be conducted in order to increase treatment efficiency. Moreover, trained and experienced workers are also required to operate and maintain the systems, along with a scientific approach.     

序批式生物膜法处理油田采油废水

采用序批式生物膜(SBBR)法处理油田采油废水。研究并开发了特殊活性污泥的培养和驯化方法。在被处理的污水中加入微生物促生剂FYS-5,可迅速培养出处理采油废水的微生物,用此种方法培养出的活性污泥的活性高,去除有毒有害物质的能力强,能够提高处理效率,保持良好的微生物生长状况。在SBBR装置进水COD容积负荷为0.5kg/(m3·d)及进水COD为500mg/L左右的条件下,经过近两个月的连续运转,COD平均去除率超过80%,出水中COD低于100mg/L,符合GB8978-1996《污水综合排放标准》的要求,经过处理的污水可以直接排放。     

Economic evaluation of sewage treatment processes in India

This paper evaluates the total annual cost including capital and operation and maintenance (O&M) costs for the up-flow anaerobic sludge blanket (UASB) and waste stabilization pond (WSP) systems operated in India. It also compares UASB and WSP systems with the activated sludge process (ASP) and biological aerated filter (BAF) systems in terms of total annual cost and chemical oxygen demand (COD) removal cost by assuming various annual interest rates and land prices. It was found that the relationship between capital and O&M costs per unit size of a UASB or WSP system and its treatment capacity can be established by a first-order equation. The relation between the cost of organic removal and capital or O&M cost for various sewage treatment systems at various annual interest rates revealed that, for the Indian context, UASB could be the most suitable option in terms of expenses and treatment efficiency.     

四川沱牌集团污水综合治理工程联动运行及工艺调试

本文介绍了四川沱牌集团污水综合治理工程所采用的预处理-厌氧-好氧处理工艺的联动运行及工艺调试情况,探讨了pH调整、UASB的启动、好氧池丝状菌的控制方法,阐述了UASB的快速启动经验,验证了UASB CASS工艺处理高浓度酿酒废水是可行的。     

Nitrogen recovery in an integrated system for wastewater treatment and tilapia production

An integrated system, consisting of Up-flow Anaerobic Sludge Blanket (UASB)-duckweed-tilapia ponds was used for recovery of sewage nutrients and water recycling. A UASB reactor with 40 liter working volume was used as pre-treatment unit followed by a series of three duckweed ponds for nitrogen recovery. The treated effluent and duckweed biomass was used to feed fishponds stocked with Nile tilapia (Oreochromis niloticus). The UASB reactor was fed with raw, domestic sewage at 6 h hydraulic retention time. The three duckweed ponds were stocked with Lemna gibba and fed with UASB effluent at 15 days hydraulic retention time. Nitrogen recovery from UASB effluent via duckweed biomass represented 81% of total nitrogen removal and 46.5% from the total nitrogen input to the system. In subsequent fishponds the nitrogen recovery from duckweed as fish feed was in the range of 13.4–20%. This nitrogen in fish biomass represented 10.6–11.5 g N from the total nitrogen in the raw sewage fed to the UASB reactor. The growth performance of tilapia (Oreochromis niloticus) showed specific growth rates (SGR) in the range of 0.53–0.97. The range of feed conversion ratio (FCR) and protein efficiency ratio (PER) were 1.2–2.2 and 2.1–2.28, respectively. The results of the experiments showed total fish yield and net fish yield in the range of 17–22.8 ton/ha/y and 11.8–15.7 ton/ha/y respectively. In conclusion UASB-duckweed-tilapia ponds provide marketable by-products in the form of duckweed and fish protein, which represent a cost recovery for sewage treatment.     

Cost analysis of alternative methods for wastewater handling in small communities

Wastewater collection and treatment is quite important for sustainable management. It would be uneconomical and impractical to provide sewer systems and separate wastewater treatment plants (WWTP) for small communities. The decision process in wastewater planning is rather important in terms of comparing the alternatives considered. The two important points in the management of wastewater at rural areas not connected to a sewer system are to develop an optimized operation strategy and to make sure that the complete system is environmentally and economically sustainable. In some regions, package treatment could be an alternative solution. However, in cases where there is an existing large WWTP, a cluster system, where sewage generated by small communities could be transported via conveyors to a centralized WWTP, could be employed. In this study, the wastewater treatment and disposal problems in small communities were addressed and an alternative wastewater handling scenario was proposed. Additionally, three wastewater handling scenarios were compared. As a case study, Gebze villages were selected.     

二段生化+物化法处理污水及中水回用的研究与设计

本文采用二段生物处理和物化处理相结合的处理方法处理某大学校区生活污水,实现处理效率高、占地面积小、工程投资低等特点,处理后各项指标均达到《生活杂用水水质标准》（CJ25．189）,处理费用为0．690元／m^3。     

微生物管式膜污水处理工艺试验与应用

某油田污水处理站设计处理规模1500 m³/d,实际处理量630 m³/d,处理工艺为“微生物接触氧化+加药絮凝沉淀+二级过滤”,在运行过程中投加的混凝剂等药剂成本高,且二级过滤器使用年限过长,其处理后出水无法达到Q/SYTH 0082—2020《油田注水水质规定》中油小于5 mg/L、悬浮物含量小于3 mg/L、粒径中值小于2μm的注水水质要求。该油田污水处理站开展了“特种微生物+低能耗管式膜”污水处理技术研究,并完成现场中试试验,处理后膜出水的悬浮物含量基本稳定在1 mg/L,出水水质达标,表明此工艺处理油田污水是可行和可靠的,为该油田污水处理工艺优化提供了可靠依据。     

污水处理厂化学除磷精确控制系统研究——以山东某污水处理厂为例

我国总磷排放标准日趋严格,污水处理厂为保证出水总磷达标,过量投加化学除磷剂,造成资源浪费。为在出水水质达标的基础上节省化学除磷剂添加量,以山东某污水处理厂为例设计了化学除磷精确控制系统。在充分考虑仪器故障潜在风险的前提下,根据进水磷酸盐负荷实时调整药剂投加量,采用“前馈+反馈”控制的模式,实现加药过程的自动化及智能化。此外,该系统还可以显著节省化学药剂用量,如在山东某污水处理厂试验表明,该系统可节省除磷药剂约12.9%。不仅解决了污水厂除磷剂粗投放的问题,而且还可以增加出水稳定性,减轻运营工作的压力,使污水厂管理向精细化方向迈进。     

Performance of an overland flow system for advanced treatment of wastewater plant effluent

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.     

Treatment of sewage using an aged-refuse-based bioreactor

The refuse in landfills becomes stabilized or aged after years of placement, and the resultant partly or fully stabilized refuse thus obtained is referred to as "aged refuse" in this work. The aged refuse contains a wide spectrum and large quantity of microorganisms, which have been proved to have a strong decomposition capability for both biodegradable and refractory organic matter present in some wastewaters. In this study, the aged refuse excavated from a 10-year old closed landfill compartment at Shanghai Refuse Landfill was used as the substrate in a bioreactor for the biofiltration of sewage taken from the sewage pipeline systems in Shanghai downtown areas. Typically, 120kg of screened aged refuse with a diameter less than 15mm was used as biofiltration material in a round shaped bioreactor with an inner diameter of 80cm and a height of 150cm. Influent sewage with initial COD, BOD, and NH(3)-N concentrations of 400-500, 240-300, and 45-50mg/L, respectively, was introduced into the bioreactor. The corresponding concentrations in the effluent were reduced to below 80-100, 10-20, and 10-15mg/L, respectively, at a hydraulic load of 1000-1200L/m(3) refuse/day, and the treatment efficiencies decreased with increased hydraulic load. The treatment mechanism was also studied. It was found that the pollutant removal efficiencies dramatically decreased when the aged refuse in the bioreactor was preliminarily disinfected using NaClO solutions, indicating that the pollutants in the sewage were biologically removed. The treatment process developed in this work is cost-effective.     

Anaerobic/aerobic treatment of meat processing wastewater

The meat processing industry is believed to produce highly polluted wastewater. Analysis of such wastewater indicated that the waste was highly contaminated with organic compounds as indicated by COD (1544mgO2l–1), BOD (646mgO2l–1), and TSS (1155 mgl–1). Moreover, oil and grease concentrations reached 144mgl–1 treatment of raw wastewater using Upflow Anaerobic Sludge Blanket (UASB) followed by Rotating Biological Contactors (RBC) was studied. Efficiency of the UASB for the removal of CODtotal, BODtotal, TSS, and oil and grease was 56%, 56%, 85%, and 58%, respectively. The quality of the UASB effluent barely complies with the regulatory standards for discharging wastewater into the sewerage network. UASB effluent was subjected for further treatment using a RBC unit to improve the quality of the treated effluent for reuse in irrigation purposes. Residual COD, BOD, TSS, and oil and grease, following RBC, was 132mgO2l–1, 40mgO2l–1, 44mgl–1, and 10mgl–1 respectively. The overall efficiency of the treatment units provided good quality effluent. The overall percentage removal of COD, BOD, TSS, and oil and grease was 91.5%, 94%, 96%, and 91%, respectively. Based on the quality of the treated effluent and guidelines recommended for wastewater reuse, it may be concluded that a slight to moderate restricted irrigation is applicable to reuse the treated effluent in the green belt around the factory. Disinfection should be applied to ensure the safety of such a process.     

NPR工艺在城镇污水处理中的应用

介绍了将NPR工艺应用于某城镇污水处理厂的工程概况,工艺流程,各主要处理构筑物的设计参数以及运行情况,运行实践表明,该工艺对污染物浓度较低的城镇污水有很好的处理效果,各项指标均可达到现行的排放标准。     

Preliminary evaluation of the electrochemical and chemical coagulation processes in the post-treatment of effluent from an upflow anaerobic sludge blanket (UASB) reactor

The main objective of this paper was to perform a preliminary comparative study between chemical and electrochemical coagulation processes, both followed by flocculation and sedimentation of an effluent from an upflow anaerobic sludge blanket (UASB) reactor treating simulated wastewater from an unbleached Kraft pulp mill. The electrochemical treatment removed up to 67% (with aluminum electrodes) and 82% (with stainless-steel electrodes) of the remaining chemical oxygen demand (COD) and 84% (stainless steel) and 98% (aluminum) of the color in the wastewater. These efficiencies were achieved with an energy consumption ranging from 14 to 20 Wh l(-1). The coagulation-flocculation treatment with ferric chloride and aluminum sulfate removed up to 87% and 90% of COD and 94% and 98% of color, respectively. The addition of a high molecular weight cationic polymer enhanced both COD and color removal efficiencies. The two post-treatment processes proved to be technically feasible; however the economical feasibility could not be assessed since the experiments were performed with small reactors that could distort scale factors.     

柠檬酸废水处理改造工程实例

采用多级内循环厌氧反应器MIC/上升式厌氧反应器UASB串联工艺处理柠檬酸生产排放的高浓度有机废水,其中厌氧处理段的COD去除率＞94％,整体COD去除率可达98.3％左右.最终排放口出水COD平均值为190 mg/L,pH值为6～9,达到柠檬酸行业废水排放标准.     

REGIONAL SEWERING AND GROUNDWATER QUALITY IN THE SOUTHERN SAN JOAQUIN VALLEY1

ABSTRACT: Sewage effluent is commonly disposed of on land in arid regions, and the majority usually recharges the groundwater. Few evaluations have been made of the effect of effluent disposal on groundwater quality in the west. Groundwater hydrologists are rarely involved with treatment plant design and operation or effluent disposal in the San Joaquin Valley, California. The author's purpose is to evaluate the effect of regional sewering programs on groundwater quality in this valley. Research was conducted on past studies of sewage effluent disposal. An extensive water sampling program was undertaken near the Fresno Sewage Treatment Plant. Chloride contents were used to trace recharged effluent. The extent of recharged effluent was delineated and traced for about ten miles. Sampling between the plant and the urban Fresno area indicated a high probability of large-scale leakage of raw sewage into the groundwater.     

工业复杂污水综合处理技术研究与应用

普光天然气净化厂在运行中排出的大量污泥、检修中产生的大量成分复杂污水,是困扰下游污水处理的重大难题。文章进行了复杂污水存储技术研究,污水预处理技术研究,污水回收利用技术研究,泥水分离技术研究。文章优化污水存储方案,提升存储空间,解决了净化厂检修污水排放集中、排放量大的难题;组合PAC药剂加注+连续曝气污水预处理工艺技术,最大程度上降低了SBR池处理负担;使外排水满足循环冷却水补水水质要求,实现了外排水的有效回收利用;实现了泥水高效分离,极大降低了污泥处置和运输费用。     

Piggery waste treatment by anaerobic digestion and nutrient removal by ionic exchange

Piggery wastes must be treated before their disposal. The high solids content and high chemical oxygen demand of piggery wastes indicated that anaerobic biological treatment could be successfully applied as primary treatment. For that reason, a comparison between upflow anaerobic sludge bed reactor (UASB) and anaerobic fixed bed reactor (AFBR) at a similar organic volumetric loading rate of 5 kg DQO/m³ day was carried out. 60% of the piggery waste COD was removed with the AFBR compared to 40% with the UASB, thus showing a better performance of the AFBR. After 1-h sedimentation secondary process, both anaerobic effluents were treated by ionic exchange with natural zeolite due to their high values of ammoniacal nitrogen (NH⁺₄ plus free NH₃). The high removal of nutrients reported (90%) shows zeolite to be a good choice as tertiary treatment.     

太湖流域农村生活污水处理技术探讨

2010年江苏省太湖流域主要污染物排放情况显示,太湖流域内的农村生活污水、农田径流和养殖污水是导致太湖水体富营养化的主要污染源。目前,在中国针对农村生活污水的处理技术已有一定研究。根据太湖流域农村生活污水的特点,人工湿地处理技术和稳定塘系统等新型污水处理技术具有良好的应用前景。     

化学合成类制药废水处理工程的工艺设计

根据化学合成类制药废水高盐分、难降解、高浓度的特点,提出了"废水分质分流,物化+生化"的处理思路。高浓度工艺废水经二级氧化处理后再与低浓度废水混合,进入生化处理工艺流程。物化采用"多维电催化+高效微电解"的二级高级氧化处理,生化段采用"UASB厌氧+水解+好氧"的处理工艺。这种联合处理工艺具有处理效果稳定、占地面积小、运行成本较低的特点,废水处理后达到工业园区污水厂接管标准后接入污水管网。