絮凝- 电气浮法处理乳化油废水

含乳化油废水由于表面活性剂的存在处理难度较大。通过絮凝——电气浮方法处理乳化油废水,确定絮凝及絮凝——电气浮所需的最佳絮凝剂用量;通过正交试验考察了pH值、电流密度、电极间距及气浮时间等操作参数的影响,得到絮凝一电气浮的最优操作条件为电流密度为20．83A／m^2,电极间距为1cm,pH值为7．4。在聚合硫酸铁投加量为50mg／L,电气浮30min时COD去除率可达95．2％。此方法对轴承厂废水的COD去除率可达75％,出水COD可降至91．9mg／L。结果表明用这种方法处理乳化油废水是可行的。     

一种高效复合絮凝剂对多种废水的处理效果

用聚合氯化铝（PAC）和聚丙烯酰胺（PAM）复配成复合絮凝剂（PAC＋PAM）应用于污染河水、生活污水、工业废水和餐饮废水等6种废水的处理，结果表明。PAC、PAM、PAC＋PAM对污染河水的CODc。SS、浊度有显著降低作用，PAC＋PAM的净水效果明显优于PAC和PAM；PAC＋PAM对6种废水中COD的去除率为81．5％～90．4％，平均84．6％。对SS的去除率为81．9％～96．5％，平均88．9％，对浊度的去除率为91．3％-98．0％，平均95．1％；处理后悬浮物基本被絮凝沉降，水体变得较清澈透明，异味或臭味消除。说明本PAC＋PAM复合絮凝剂对各种废水均有良好的净水效果，具有重要的应用价值。     

PAC和PAM复合絮凝剂在洗涤剂废水处理中的应用研究

絮凝性能的实验研究表明,PAC和PAM复合絮凝剂是处理洗涤剂废水的理想絮凝剂,采用该复合絮凝剂处理洗涤剂废水时的最佳操作条件如下：PAC用量为1．5g／L,PAM用量为10mg／L,pH值约为7．0,絮凝搅拌速度60r／min,絮凝搅拌时间30min,沉淀池沉淀时间为30min。该实验结果在中试规模的应用中得到了较好地验证,中试试验研究表明采用PAC和PAM复合絮凝剂处理洗涤剂废水,CODCr和LAS(直链烷基苯璜酸钠)去除率分别可达85％和72％以上,有效地解决了LAS难以生物降解等问题。     

絮凝-酸析-NaClO-Fenton联合处理页岩气产出水研究

以涪陵页岩气田产出水为研究对象，研究絮凝、酸析、Fenton氧化和NaClO氧化相互协同作用下，采出水COD去除率的变化程度及规律。比较了不同组合方式下水样COD去除效果及变化规律，考察了絮凝剂、次氯酸钠和Fenton试剂的加量以及体系pH值对去除率的影响，结果表明：（1）单一絮凝或酸析条件下，最高COD去除率＜25%，在絮凝剂加量80mg/L、酸析pH为4时，絮凝-酸析协同处理COD去除率达到＞40%；（2）原始水样直接进行次氯酸钠氧化，COD最高去除率为75.01%，絮凝-酸析后进行次氯酸钠氧化，最高COD去除率为80.34%，与原始水样相比提高了5.33%，且达到相同的COD去除效果，絮凝-酸析后水样对次氯酸钠的需求量低于原始水样；（3）絮凝-酸析后水样进行Fenton氧化与原始水样直接进行Fenton氧化相比，COD去除率提高了6.07%；（4）絮凝-酸析-NaClO- Fenton协同处理，水样COD去除率达到＞90%，其中最高去除为94.17%，与絮凝-酸析-NaClO和絮凝-酸析-Fenton处理相比分别提高了13.83%和5.27%。水样首先经过絮凝-酸析预处理，达到削减后续次氯酸钠和Fenton氧化负荷、降低药剂用量目的，然后经过Fenton试剂和次氯酸钠对不同类型特征污染物选择性去除的协同作用，可达到较高的COD去除率。     

中药废水处理工程设计研究

某工程采用微电解、上流式厌氧污泥床（UASB）、高效接触反应器（HCR）处理中药废水，处理规模2500m^3／d。运行结果表明：采用该工艺COD去除率达97．9％，BOD去除率达97。4％，色度去除率达98．2％，出水完全达到《污水综合排放标准》（GB8978-96）中的一级排放标准，且工程投资和运行费用较低。     

聚合硅酸硫酸铝对印染废水的预处理实验研究

本文采用硅酸钠、硫酸和硫酸铝为原料，制备出无机高分子絮凝剂聚合硅酸硫酸铝，探讨了聚合硅酸硫酸铝对广东某毛纺企业印染废水的应用性能。结果表明，聚合硅酸硫酸铝对COD和色度的去除率优于硫酸亚铁，COD和色度去除率分别可达31．8％和84％，减轻了后续生化系统的压力。     

纳米二氧化钛光催化氧化降解苯酚废水实验

开展实验室模拟苯酚废水的二氧化钛光催化氧化实验。结果表明：在苯酚废水曝气量为0～3L/min的条件下，随着曝气量的增大，COD去除率先增大后减小；初始浓度不变，光照时间为1h的条件下， 调节pH值在3～11，苯酚废水COD去除率随着pH值的增大而减小，当pH值为11时， COD去除率又开始增 大，酸性条件比碱性条件下COD去除率高；随着二氧化钛投加量的增加，COD去除率增大，当二氧化钛投加量 为10g/L时，COD去除率反而降低，二氧化钛最佳投加量为3g/L；随着苯酚废水初始浓度由75mg/L增加至300mg/L，COD去除率由78.2％降低到58.1％；反应温度的改变对COD和TOC的去除率没有影响。     

SBR法处理炼油废水的研究

研究了SBR（程序间歇式活性污泥）法处理炼油废水的最佳工艺条件和除氮效果，以及投菌SBR法处理炼油废水中污染物的效果。确定了SBR法处理炼油废水最佳反应温度为25℃－40℃，pH值为6.0-8.5，反应时间为8－12h，活性污泥浓度为2000－4000mg/L。当反应期内好氧曝气和缺氧搅拌交替进行3－4次，脱氧率可以达到90％以上。将实验室筛选得到的除油菌投加于BR复合生物反应器中处理炼油厂隔油池出水，废水中各种污染物的去除率分别为：COD93．5％，石油类98．6％，总氮89．8％。     

某公司印染废水处理工程实例

某公司采用“一级混凝沉淀一水解酸化-A／O法-二级混凝沉淀”工艺处理印染废水,工程日常运行结果表明,在废水主要指标CODQ为660～690mg／L、色度为1200倍时,处理后出水COD0为70-90mg／L,色度为28-35倍,CODo的去除率为86％-89％,色度的去除率约为97％。废水处理系统综合电耗0．8kW·h／t污水,废水处理总运行费用2．2元／t污水,具有较好的技术经济指标。     

再生造纸废水絮凝除浊试验研究

本研究采用絮凝法对再生造纸废水中含细小纤维、无机填料的悬浮物进行处理试验，比较了硫酸亚铁与聚丙烯酰胺复合絮凝剂和聚硅酸氯化铁盐两种絮凝剂的絮凝效果，研究了制备聚硅酸氯化铁盐的铁硅比、pH值、碱化度以及投加量与废水除浊率之间的相互关系。实验结果表明：在最佳条件下，絮凝效果优异，除浊率达到98％，上清液无色透明。     

废水中环氧丙烷降解菌株的培育及降解效果研究

本文通过对污泥的驯化筛选得到4株降解环氧丙烷废水的优势茵A、B、C、D，并对降解效果最好的一个菌株A进行研究，得到其最佳降解条件是温度为30℃、pH为5、废水浓度为20％、反应时间为9h，其COD去除率可达到63．24％左右。     

Combined chemical and biological oxidation of penicillin formulation effluent

Antibiotic formulation effluent is well known for its important contribution to environmental pollution due to its fluctuating and recalcitrant nature. In the present study, the chemical treatability of penicillin formulation effluent (average filtered COD(o)=830 mg/l; average soluble COD(o)=615 mg/l; pH(o)=6.9) bearing the active substances penicillin Amoxicillin Trihydrate (C(16)H(19)N(3)O(5)S.3H(2)O) and the beta-lactamase inhibitor Potassium Clavulanate (C(8)H(8)KNO(5)) has been investigated. For this purpose, the penicillin formulation effluent was subjected to ozonation (applied ozone dose=2500 mg/(lxh)) at varying pH (2.5-12.0) and O(3)+H(2)O(2) (perozonation) at different initial H(2)O(2) concentrations (=2-40 mM) and pH 10.5. According to the experimental results, the overall Chemical Oxygen Demand (COD) removal efficiency varied between 10 and 56% for ozonation and 30% (no H(2)O(2)) and 83% (20 mM H(2)O(2)) for the O(3)+H(2)O(2) process. The addition of H(2)O(2) improved the COD removal rates considerably even at the lowest studied H(2)O(2) concentration. An optimum H(2)O(2) concentration of 20 mM existed at which the highest COD removal efficiency and abatement kinetics were obtained. The ozone absorption rate ranged between 53% (ozonation) and 68% (perozonation). An ozone input of 800 mg/l in 20 min was sufficient to achieve the highest BOD(5)/COD (biodegradability) ratio (=0.45) and BOD(5) value (109 mg/l) for the pre-treated penicillin formulation effluent. After the establishment of optimum ozonation and perozonation conditions, mixtures of synthetic domestic wastewater+raw, ozonated and perozonated penicillin formulation effluent were subjected to biological activated sludge treatment at a food-to-microorganisms (F/M) ratio of 0.23 mg COD/(mg MLSSxd), using a consortium of acclimated microorganisms. COD removal efficiencies of the activated sludge process were 71, 81 and 72% for pharmaceutical wastewater containing synthetic domestic wastewater mixed with either raw, ozonated or perozonated formulation effluent, respectively. The ultimate COD value obtained after 24-h biotreatment of the synthetic domestic wastewater+pre-ozonated formulation effluent mixture was around 100 mg/l instead of 180 mg/l which was the final COD obtained for the wastewater mixture containing raw formulation effluent, indicating that pre-ozonation at least partially removed the non-biodegradable COD fraction of the formulation effluent.     

纳米级聚合氯化铝处理石化废水絮凝效果研究

采用自制的纳米级聚合氯化铝絮凝荆处理石大科技股份公司胜华炼油厂隔油池出水，以处理后水样的透光率作为混凝沉降效果的评价指标，并对絮凝剂投加量、搅拌速度、搅拌时间等影响混凝效果的因素进行了研究。试验表明，聚合氯化铝对石化废水的处理达到较为理想的效果，聚合氯化铝混凝处理石化废水的最佳条件为：纳米级聚合氯化铝投加量为15mg／L左右，慢速搅拌的搅拌速度为50～60rpm，快速搅拌的搅拌速度为190—225rpm，快速搅拌时间90s。慢速搅时间10min时效果最佳。使用Al-Ferron逐时络合比色法及XRD对絮凝荆进行了表征，结果证实样品中Alb含量可达到85％左右。     

SBR中好氧颗粒污泥的培养

采用竖式SBR作为反应器，利用城市污水处理厂剩余污泥作为接种污泥，通过不间断运行培养出好氧颗粒污泥。实验结果表明，采用非限量曝气模式好氧颗粒污泥降解模拟污水的效果较好，其COD去除率可达98％以上。曝气量对好氧颗粒污泥的形成和稳定具有重要影响，当气速为26．5m／h时，好氧颗粒污泥的性状和处理有机废水效果最佳。同时好氧颗粒污泥对pH值的变化不明显，当pH为5—8范围内，其COD去除率都可达到85％以上。但是未经驯化的好氧颗粒污泥对对硝基苯酚和对氯苯酚两种芳香类有机物较敏感，而对硝基苯酚对其毒性更大。当对硝基苯酚和。对氯苯酚浓度为10mg／L时，其COD去除率仅为42．5％和52％。     

短暂交替曝气方式在PSB法处理高浓度苯胺废水中的应用

利用酸化—PSB—活性污泥法工艺处理高浓度毒性苯胺废水,在24h的停留时间下,比较PSB阶段不同曝气时间对苯胺废水处理效果的差异。结果表明:不同时间的曝气处理对光合细菌处理苯胺废水的效果存在差异。以曝气时间为2h的反应器处理效果最佳,COD去除率达96.1%,苯胺去除率达97%,同时,相邻周期交替采用1h、2h曝气处理,废水COD去除率提高了20%以上,苯胺去除率提高了10.9%~14.2%。     

Significance of iron compounds in chemical and electro‐oxidation treatment of sugar industry wastewater: Batch reaction

Industrialization plays a major role in a nation's growth. However, with an increase in industrial activities, pollution levels are also increasing. Among all industries, the sugar‐processing industry is one that requires large amounts of water to process the sugar, and, consequently, it discharges large amounts of water as effluent. Highly polluted wastewater brings changes to the physicochemical characteristics of the surrounding environment. Iron compounds have had a significant impact when they are used in wastewater treatment in various applications, including when they are used to minimize the pollution levels in sugar industry wastewater (SIWW). To minimize the pollutant levels from SIWW, iron compounds have been key for uses in treatments involving chemical and electro‐oxidation. Two different methodologies of electrocoagulation and chemical coagulation have been used to treat SIWW. In electrocoagulation, an iron plate is used as an electrode material under specific operating conditions. Ferrous sulfate and ferric chloride have been used as chemical coagulants at various pH and mass loading levels. The use of iron metals shows an 82% reduction in chemical oxygen demand (COD) and an 84% reduction in color at the optimum condition of pH 6, an electrode distance of 20 millimeters, and a current density of 156 square centimeters. As a chemical coagulant, iron salt (ferrous sulfate) provides a reduction of 77% COD and a 91% reduction of color at pH 6 and a 40‐millimole mass loading. Electrochemical treatment using iron was found to be suitable to treat SIWW. The sludge generated after treatment can be burned or composted with the possible recovery of some of the treatment costs.     

Ultrasound and enzyme assisted biodegradation of distillery wastewater

Irradiation with ultrasound (US) and use of an enzyme (E) as pretreatment techniques were carried out to treat a complex effluent (distillery wastewater). These two techniques have been used alone as well as in combination and the efficacy of these techniques was tested by subjecting the effluent to subsequent aerobic biological oxidation (AO). When used alone, US exposure for 30 min and 2 h yielded the best COD reduction during the aerobic oxidation step (US+AO). For the enzyme when used alone, a pH value of 4.8 (corresponding to the optimum pH of the enzyme), a dose of 50 U and a pretreatment time of 24 h yielded better COD removal efficiency as compared to untreated effluent (aerobic oxidation alone). When used in combination, ultrasound followed by enzymatic pretreatment (US+E+AO) yielded the best COD removal efficiencies during aerobic oxidation as compared to the other combinations tested for the treatment of the distillery wastewater. A 4-fold increase in the initial oxidation rate was observed over the untreated batch for the integrated technique (US+E+AO). On the basis of the variation in the values of the biokinetic parameters it can be concluded that the type of pretreatment scheme affects the subsequent rate of the aerobic oxidation significantly.     

用超声气浮—BAF组合工艺处理油田稠油污水

利用超声气浮处理机对稠油油田污水进行的室内试验研究结果表明,超声气浮工艺对污水中COD的去除效果不明显,去除率只有23.0%。但是,经超声气浮处理后,污水的可生化性明显得到改善,BOD5/CODcr值由0.18上升到0.31,这为稠油污水的二级生化处理创造了条件。稠油污水经超声气浮-BAF组合工艺处理后,出水水质可达到国家GB8978-1996一级标准的水质要求。