吗啉废水的生化处理工艺

以含有吗啉、甲基吗啉的高浓度有机废水为研究对象,提出了曝气吹脱-吸附-生物处理的联合工艺,并在室内进行了小试实验。结果表明：原废水经过2次曝气吹脱后,ρ(NH₃-N)从62 500 mg/L降为431 mg/L,ρ(COD)从50 840 mg/L降为26 051 mg/L。通过吸附实验,ρ(COD)从26 051 mg/L降为2 769 mg/L,ρ(NH₃-N)从412 mg/L降为134 mg/L。在生物处理室内小试实验中,采用了活性污泥反应器与曝气生物滤池相结合的处理工艺。在活性污泥反应系统中,当废水pH为7.5、ρ(DO)为4.3 mg/L、水力停留时间为30 h时,COD的去除率最高,可以达到83.1%。在曝气生物滤池中,当ρ(DO)为3.3 mg/L时,COD去除率最高,达到55.8%。在生物处理的最佳参数条件下进行连续监测,当进水ρ(COD)为2 769 mg/L、出水ρ(COD)平均值为387 mg/L时,COD去除率可达到85.9%。吗啉废水经过此联合工艺的处理,ρ(COD)从50 840 mg/L降为387 mg/L。     

钨矿选矿废水处理新技术

采用混凝沉淀技术处理钨矿选矿废水,通过试验确定HNJY新型高效复合絮凝剂作为混凝剂最为合适,投加量为120mg/L,经处理后废水出水水质符合国家污水排放标准并能回用,废水SS约11500mg/L,处理后的出水要求为SS<10mg/L。技术经济分析,投资总费用为67.5万元,处理成本为0.60元/m3,设计工艺可靠且经济合理。本工程既防止了废水对环境的潜在污染,又解决了枯水期选矿用水不足的问题。     

柱层累托石材料对有机废水的处理及效果评价

就使用柱层累托石材料对有机废水处理的实验研究进行讨论。采用累托石材料，在用量为15kg/t时，加入用量为4kg/t的还原剂FE，废水中COD去除率达70%；如果再用累托石进行二次吸附，其COD去除率达92%；处理水COD值降为96mg/L，达到GB8978-1996一级排放标准，同时实验了累托石的再生利用效果。     

Improvement on the treatment of thick oil sewage by using integrated biochemical treatment technology

Sewage treatment station in oilfield needs a new process to meet the desired requirements. A new process was proposed to meet the discharge standards, which consisted of the following sub-processes: electrochemical treatment → coagulation treatment → integrated biochemical treatment of moving bed biofilm reactor and membrane bio-reactor → combined treatment process of macroporous adsorption resin. Electrochemical treatment included 5 electrolytic cells, total volume of which was 10 L. The PFS was chosen as the coagulants in the coagulation treatment, and the removal rate of COD could reach 66% when the dosage of PFS was 500 mg/L. The biochemical treatment consisted of anoxic tank, aerobic tank and membrane zone, and the removal rate of COD was about 55–70% when HRT was 12 h. SD300 resin was chosen as the best adsorbent in the treatment using macroporous adsorption resin. In addition, the effluent COD after coagulation treatment process becomes about 180 mg/L, the effluent COD after biological treatment becomes about 50 mg/L, and the last effluent COD with the macroporous adsorption resin becomes about 20 mg/L. The three-dimensional fluorescence spectrum was used to analyze the differences in types of organic matters in water samples between the raw water and the treated one. The results demonstrated that the new process meets the needs of wastewater treatment.     

利用黄钾铁矾类矿物形成过程预处理高浓度含硫废水

利用黄钾铁矾类矿物形成过程对某高浓度工业含硫废水进行预处理,除去一定量的SO42-,使溶液中低价态的硫继续转化成SO42-,再进行氧化处理。采取二次沉淀除去溶液中更多的SO42-,大大降低了该水样的COD值。通过实验得出沉淀的最佳工艺条件为pH值为2.50～3.20,氯化铁晶体(FeCl3.6H2O)最佳投入量为50g/L。经过两次黄钾铁矾类矿物沉淀过程,该废水COD的去除率达到85.29%,结合H2O2的氧化处理,COD去除率可达96%。为高浓度含硫废水进入生化处理前的预处理提供了实验依据。     

Impact of discharge wastewater effluents on the physico-chemical qualities of a receiving watershed in a typical rural community

The qualities of the treated final effluents of a wastewater treatment plant located in a rural community of the Eastern Cape Province of South Africa were assessed over the duration of 12 months. Parameters measured include pH, temperature, electrical conductivity, salinity, turbidity, total dissolved solid, dissolved oxygen, chemical oxygen demand, nitrate, nitrite and orthophosphate levels and these were simultaneously monitored in the treated final effluents and the receiving watersheds using standard methods. Unacceptably, high levels of the assayed parameters were observed in many cases for chemical oxygen demand (7.5–248.5 mg/L), nitrate (1.82–13.14 mg/L), nitrite (0.09–1.3 mg/L), orthophosphate (0.07–4.81 mg/L), dissolved oxygen (4.15–11.22 mg/L) and turbidity (3.68–159.06 NTU) during the study period and are severally outside the compliance levels of the South African Guidelines and World Health Organization tolerance limits for effluents intended for discharge through public sewers into receiving watersheds. The study has revealed that there was an adverse impact on the physico-chemical characteristics of the receiving watershed as a result of the discharge of inadequately treated effluents from the wastewater treatment facility. This poses a health risk to several rural communities which rely on the receiving water bodies primarily as their sources of domestic water. There is need for the intervention of appropriate regulatory agencies to ensure production of high quality treated final effluents by wastewater treatment facilities in rural communities of South Africa.     

The removal of color and COD from wastewater containing water base color by coagulation process

In this study acrylic water base color was removed from synthetic wastewater using coagulation process. Experiments were conducted on the sample containing 100 mg/L and 400 mg/L of acrylic water base color. Destruction of color by means of coagulation/flocculation techniques using ferrous sulfate, alum, lime and polyelectrolyte (cationic, anionic and non ionic). The study was performed in a systematic approach searching optimum values of alum and FeSO₄ concentration, pH and temperature. All the experiments were run in a laboratory scale.The obtained results show that treatment with alum and ferrous sulfate alone proved to be very effective in removing the color (> 99 %) and part of COD (60–70 %) from aqueous solution. Lime alone did not significant change on COD and color removal.     

预处理／复合水解酸化／复合好氧氧化工艺处理综合制药废水

针对传统水解酸化和好氧氧化处理工艺存在的问题,对水解酸化工艺及好氧氧化处理工艺进行了改进;并针对东北制药集团制药废水水质特征,设计开发了预处理 复合水解酸化 复合好氧氧化的生物处理技术。工程设计规模为30000 m3/d,两年的运行结果表明,此工艺运行稳定,耐冲击负荷能力强。当平均进水浓度COD为3600 mg/L、BOD5为1000 mg/L、SS为450 mg/L时,平均出水浓度COD≤300mg/L、BOD5≤100 mg/L、SS≤50 mg/L,达到了国家城市排水三级标准医药企业污水排放标准(COD300mg/L)。     

Removal of bisphenol A (BPA) from biologically treated wastewater by microfiltration and nanofiltration

Bisphenol A (BPA) is an endocrine disruptor that is difficult to completely remove from wastewater by conventional biological methods. Increased post-treatment BPA removal with ceramic membranes is worth investigating because of these membranes’ mechanical and chemical stability and lifespan. To determine the effectiveness of ceramic membranes for post-treatment of biologically treated BPA-contaminated wastewater, microfiltration (MF) and nanofiltration (NF) were conducted. Both processes removed BPA completely at an initial BPA concentration of 0.3 ± 0.14 mg/L. Increased concentration of 0.7 ± 0.29 mg/L decreased BPA removal. MF removed at least 24 % of BPA, presumably because BPA was adsorbed on particulate matter, which was retained by the membrane, or adsorbed on its surface. NF removed up to thrice more BPA. MF and NF completely removed suspended solids and 40–60 % COD. Filtration capacity decreased with time due to fouling but did not depend on initial BPA concentration. BPA concentrations in municipal wastewater are typically lower than the lowest concentration tested, where MF completely removed BPA. Hence, MF ceramic membranes appear a promising solution for post-treatment of BPA-containing wastewater. MF can be used at a much lower transmembrane pressure than NF, requiring less energy to pump wastewater through the membrane, thus reducing costs.     

混凝-催化氧化处理含油污水实验研究

采用复合化学混凝及催化氧化联合工艺对油田生产废水进行了实验研究.结果表明:含油废水经混凝处理后,剩余ρ(CODcr )可以达到300 mg/L左右,剩余悬浮物质量浓度小于10mg/L;再经活性炭载Cu、Pd催化剂的深度处理,含油污水中的ρ(CODcr )值由315 mg/L降至50 mg/L以下,达到了国家的相关排放标准.催化剂可以再生重复使用.     

连续流态下好氧颗粒污泥的培养及处理制药废水的性能

在上流式好氧颗粒污泥床反应器中, 以厌氧颗粒污泥和好氧絮状活性污泥为接种泥, 采用人工配制的模拟废水, 成功培养出性能优异的好氧颗粒污泥.反应器内污泥浓度稳定在5g/L左右, 颗粒污泥粒径为0.5~2.0mm, 当进水COD为2000mg/L, 容积负荷为4.8kg/(m3·d)时, 系统对COD的去除率稳定在96%以上.通过扫描电镜观察, 好氧颗粒污泥是层状结构, 表面有大量丝状菌缠绕, 内部有短杆菌和空穴存在.逐步提高制药废水在进水中的比例, 经过47d的培养, 生物制药废水完全取代模拟废水, 系统对COD、NH₃-N、TP的去除率分别稳定在90%、90%和70%以上.      

High rate anaerobic treatment of Sago wastewater using HUASB with PUF as carrier

Sago industry is one of the major small-scale sectors in India and over 800 units are located in the southern State of Tamilnadu. Processing of sago generates enormous quantities of high strength wastewater requiring systematic treatment prior to disposal. The present study is an attempt to treat the sago wastewater using Hybrid Upflow Anaerobic Sludge Blanket (HUASB) reactor, which offers the advantages of both fixed film and up flow anaerobic sludge blanket treatment. HUASB reactor with a volume of 5.6 L was operated at Organic Loading Rates varying from 10.7 to 24.7 kg COD/m³.day. After 130 days of startup, the reactor produced appreciable decrease in COD of wastewater and removed solids efficiently. The COD removal varied from 91–87%. While the removal of Total Solids was in the range of 61–57%, that of volatile solids varied from 70–67%. The ideal OLR for the reactor was 23.5 kg COD/m³.day. The findings of the study open up newer possibilities of design low cost and compact onsite treatment systems with very short retention periods.     

流动注射合并带停留光度法快速测定环境水样中化学需氧量

研究了KMnO4体系流动注射合并带停留分光光度法对环境水样中化学需氧量(COD)测定的试验条件,包括反应试剂KMnO4的浓度、载流H2SO4的酸度、采样泵泵速及停留时间、反应温度、试剂体积和采样环体积。在不加HgSO4的条件下,Cl-的质量浓度达10000 mg/L对测定无干扰。方法的线性范围为3~150 mg/L,检出限为1 mg/L,精密度(RSD,n=7)为1.2%。方法具有仪器简单,操作方便、快速,干扰少,灵敏度高等优点,用于河水、池塘水和地表水等实际样品的分析,测定值与经典重铬酸钾标准方法结果基本一致。     

Comparative performance evaluation of physicochemical treatment processes for simulated dairy wastewater

In the present study, the effectiveness of physicochemical treatment processes (coagulation and Fenton’s oxidation) was investigated for simulated dairy wastewater (pH = 7.3, chemical oxygen demand (COD) = 3600 mg/l, 5-day biochemical oxygen demand (BOD₅) = 1950 mg/l, total Kjeldahl nitrogen (TKN) = 87 mg/l, and total phosphorous (TP) = 14 mg/l). Plain and ballasted coagulation runs were carried out in a jar apparatus, while Fenton’s oxidation was performed in a three-neck glass reactor. Ballasted coagulation caused an enhancement in the settling rate of sludge though no significant enhancement in the removal of organics was observed. Individually, coagulation and Fenton’s oxidation processes resulted in ~67 and 80 % COD removals, respectively, from the wastewater. The sequential treatment exploring coagulation followed by Fenton’s oxidation showed overall COD, BOD₅, TKN, and TP reductions of ~93, 97, 84, and 70 %, respectively, from the wastewater. However, a biological post-treatment would be required to achieve the effluent discharge standards. The removal of proteins, fats, and amino acids from wastewater was confirmed from Fourier transform infrared analysis of the settled sludge (obtained after coagulation process). Preliminary cost analysis suggested coagulation and the sequential treatment (i.e. coagulation followed by Fenton’s oxidation) as the preferred options.     

河南省永城市浅层地下水化学特征及形成机制

地下水是河南省永城市重要的供水水源,浅层地下水水质污染严重制约了该市经济发展和居民生活质量的提高.在实地调查采样分析的基础上,运用水化学图解法、数理统计法、地球化学模拟法等方法综合分析了永城市浅层地下水的水化学特征和形成机制,探讨了该市浅层地下水污染来源和主要影响因素.结果表明:随含水介质和人类活动影响强度的变化,浅层地下水中K+、Ca2+、NO₃-、Cl-、SO₄2-的浓度和COD（chemical oxygen demand）随深度增加而减少,而Na+、F-、Mg2+、HCO₃-的浓度和TDS（total dissolved solids）随深度增加而上升.在煤矿区及煤化工区浅层地下水中SO₄2-浓度大于250 mg/L,远远高于其他区域的SO₄2-浓度,而在农业区浅层地下水中NO₃-浓度大于30 mg/L,远远高于其他区域的NO₃-浓度.综合分析表明:煤矿及其化工业废水和生活污水排放、过量使用化肥农药是永城市浅层地下水污染的主要因素.      

Activated sludge properties in a submerged membrane bioreactor: effect of COD/TKN ratio of wastewater

The properties of activated sludge are very important in a membrane bioreactor (MBR) in terms of membrane fouling. The most important parameters affecting the membrane fouling can be listed as mixed liquor suspended solid (MLSS) concentration, soluble microbial products (SMPs), extracellular polymeric substances (EPSs), floc size, aeration and viscosity of both supernatant and activated sludge. The COD/TKN ratio also affects the physical properties of sludge in MBR system. This study aimed to investigate the effect of chemical oxygen demand-to-total Kjeldahl nitrogen (COD/TKN) ratio of feed wastewater treated in an MBR on biological components of activated sludge. The activated sludge characteristics were determined by quantitative analyses such as MLSS, EPS, SMP, floc size distribution, zeta potential, relative hydrophobicity and capillary suction time in a submerged MBR treating simulated wastewater having different COD/TKN ratios (16, 56 and 107). The COD and TKN removal efficiencies were found to be almost equal in the sMBRs having different COD/TKN ratios. However, it was seen that the EPS content and SMP concentration in the supernatant increased with increasing COD/TKN ratio. The results indicated that the COD/TKN ratio of feed should be considered as an effective parameter on activated sludge properties in sMBR systems.     

药剂与粉煤灰联合处理再生造纸废水的实验研究

通过混凝实验探讨了用PAC处理再生造纸废水的最佳混凝条件.在此基础上,选用PAM为助凝剂,通过正交实验,获得了较佳的水平条件:先加PAM,质量浓度为3 mg/L,后加PAC,质量浓度为0.2 g/L,反应9 min;处理后的出水经粉煤灰过滤,ρ(COD)可降至37.383 mg/L,ρ(BOD)为20.7 mg/L,浊度为0,pH为11.12,在空气中放置24 h后pH变为8.02.     

Color removal from industrial wastewater with a novel coagulant flocculant formulation

Chemically enhanced wastewater treatment is attracting substantial interest among the currently employed chemical unit processes in wastewater treatment. Coagulation-flocculation has received considerable attention for yielding high pollutant removal, especially color removal. This investigation presents a novel formulation of coagulation-flocculation for color removal from industrial wastewater and illustrates its efficiency, with aid of measurement of solid sludge content, suspended solid content, percentage of solid recovery, UV absorption in wastewater effluent from two automotive factories. The results show that the novel formulation can remove color content from wastewater efficiently. The treated wastewater had UV absorption close to distillated water and color was removed up to 96% by flocculation / coagulation treatment.     

Kinetic modeling of carbon and nutrients removal in an integrated rotating biological contactor-activated sludge system

In this study, kinetics of biological carbon, nitrogen, and phosphorous removal from a synthetic wastewater in an integrated rotating biological contactor-activated sludge system was investigated. The experimental data obtained from varying four significant independent factors viz., hydraulic retention time, chemical oxygen demand for nitrogen to phosphorus ratio, internal recirculation from aerobic to anoxic zone and disks rotating speed were used for the process kinetic modeling. In order to obtain the bioprocess kinetic coefficients, Monod, first-order and Stover?CKincannon models were employed. As a result, Monod and Stover?CKincannon models were found to be the appropriate models to describe the bioprocess in the rotating biological contactor-activated sludge system as the determination coefficient for the first-order model obtained less than 0.79. According to the Monod model, growth yield, microbial decay rate, maximum specific biomass growth rate, and half-velocity constant coefficients were found to be 0.712?g VSS/g COD, 0.008/d, 5.54/d and 55?mg COD/L, respectively. From Stover?CKincannon model, the maximum total substrate removal rate constant and half-velocity constant were determined as 15.2, 10.98, 12.05?g/L?d and 14.78, 7.11, 6.97?mg/L for chemical oxygen demand, nitrogen and phosphorus removal, respectively. The kinetic parameters determined in this study can be used to improve the design and operation of the biological contactor-activated sludge system in full scale.     

污灌区地下水硝酸盐污染来源的氮同位素示踪

为了识别石家庄市南部污灌区地下水硝酸盐污染来源, 采集5种潜在污染源和19组地下水样用于化学和氮同位素分析.灌溉污水NH₄+的δ15N值较低(4.0‰), 施化肥土壤和粪堆下土壤NO₃-的δ15N值分别为1.4‰和12.4‰; 仅施厩肥的蔬菜种植区下伏近30 m厚包气带沉积物NO₃-的δ15N分布显示, 来自动物粪便的NO₃-已运移到11.5 m以下包气带, 均值10.9‰; 污水灌溉农田下伏厚层包气带沉积物样品分析结果指示, 土壤层下伏包气带沉积物δ15N值变幅较小, 均值5.7‰.污灌区内除一深井外, 其他水井地下水硝酸盐浓度变化在52.6~124.5 mg/L之间, 均值79.72 mg/L, δ15N值变化在5.3‰~8.3‰之间, 均值7.0‰.污灌区地下水的δ15N值较污灌区土壤层下伏包气带沉积物的δ15N值高, 表明地下水NO₃-除了来自灌溉的污水外, 还有δ15N值更高的其他来源, 这些来源主要是人和动物粪便.利用线性混合模型计算, 污灌区地下水NO₃-来自灌溉的污水, 约占76%, 而来自人和动物粪便的NO₃-约占24%.为控制污灌区地下水NO₃-浓度进一步增长, 不仅要加强污水灌溉管理, 还要加强人和动物粪便的管理.