农药废水中的有机硫,磷污染物湿式空气氧化反应的研究

以ｏ，ｏ－二甲氧基或ｏ，ｏ－二乙氧基硫代磷酰氯废水为典型废水，在１８０－２３０℃，氧气压力为０．７－１．５ＭＰａ的反应条件下，在２Ｌ的不锈钢的高压釜中，研究了农药废中有机硫磷化合物在温式空气氧化过程中的降解机制。实验结果表明，有机硫磷化合物分子中的有机硫通过氧化反应降解为硫，有机磷通过水解反应降解为磷酸。有机硫氧化生成的硫酸是废水湿式空气氧化程中酸度增加的主要来源。酸性条件比碱性条件更利于有机硫磷     

洗涤废水化学法除磷试验研究

对Ａｌ２（ＳＯ４）３，Ｃａ（ＯＨ）２不同反应条件下去除洗涤废水中总磷的情况作了对比试验，结果表明，按Ｃａ（ＯＨ）２：ＴＰ＝３．７：１．０（重量比）投加试剂，回用生成的磷灰石沉淀助凝，ＴＰ（总磷）去除率可达９５％，ＣＯＤｃｒ有少量去除。     

NP型复合纳滤膜对豆腐废水处理的应用

本文对ＮＰ型复合纳滤膜的分离性能进行了初步实验并在此基础上采用纳滤膜平板过滤装置对豆腐加工过程中产生的废水进行处理，以降低废水中的ＣＯＤ含量，实验结果表明，ＮＰ型复合纳滤膜对０．２％ＭｇＳＯ４溶液的截留率（Ｒ）高于９０％，相应秀量约为２０Ｌｍ＾－２．ｈ＾－１（０．４ＭＰａ），豆腐废水ＣＯＤ的去除率大于９０％     

链霉菌碱性脂肪酶的研究

从杭州土壤中获得的一支链霉菌,通过ＵＶ、ＤＥＳ和Ｃｏ６０ － γ射线的５ 代诱变,选育成功了高产的Ｚ９４－ ２ 菌株,经过对Ｚ９４ －２ 的发酵研究,产碱性脂肪酶活力达５９６ ｕｍＬ,其最适培养基（λｕ Ｌ－１） 为：糊精１０、黄豆饼粉３０、尿素１０ 、Ｋ２ＨＰＯ４０ ．５、ＭｇＳＯ４·７Ｈ２Ｏ０ ．５、ＮａＣｌ１ 和ＡＥＯ９ ０．５ ,产酶的最适条件为：初始ｐＨ９．０～１０．０ ,２６℃培养４８ ｈ．对Ｚ９４－ ２ 与其他菌株的碱性脂肪酶的特性作了比较     

啤酒废水的生物净化与利用研究

以啤酒废水为主的城市污水,通过多级模拟生物净化系统,污水中的有机污染物得到明显转换和去除． Ｂ Ｏ Ｄ５ 、 Ｃ Ｏ Ｄｃｒ、 Ｎ、 Ｐ等污染指标去除率在７９ ．４５ ％ ～９９ ．７０ ％ 之间．随水质的改变,藻类的种类、数量、生物量、叶绿素含量及多样性指数不断上升,清洁种类逐渐增多．在净化后的污水中,鱼虾优质饵料生物—大型蚤数量ｎ达２３４ Ｌ－ １ ,即平均有２ ．６７ ｍｇ Ｌ－ １ 的 Ｃ、０ ．６２ ｍｇ Ｌ－ １ 的 Ｎ、０ ．０９ ｍｇ Ｌ－ １ 的 Ｐ转移到蚤体中．相关分析表明,大型蚤食量与加入藻的量呈正相关关系,与剩余藻的量呈负相关关系．     

进水PCP和CODCr质量浓度对厌氧反应器运行效能的影响

应用以氯酚驯化污泥接上流式厌氧消化反应器（ＵＡＤ）连续处理含五氯酚（ＰＣＰ）废水的试验结果表明，在一定的水力负荷下，试验反应器可稳定地处理ρ（ＣＯＤＣｒ）１２５０－１０００ｍｇ．Ｌ＾－１和ρ（ＰＣＲ）≤１８０ｍｇ．Ｌ＾－１的有毒有机废水，ＣＯＤＣｒ去除率大于９０％，ＰＣＰ去除率大于９９．５％，出水ρ（ＰＣＰ）小于０．５ｍｇ．Ｌ＾－１，维持试验反应器正常运行所必需的最低进水ρ（ＰＣＰ）有关，且进水ρ     

升流式厌氧污泥床工艺处理酵母废液的研究

本文根据酵母废液的水质特点，采用了常温升流式厌氧污泥床处理工艺，即温度在２６．８－２８．０℃，进水ＣＯＤ为７１２９－９８２３ｍｇ·ｌ＾－１时，达到ＣＤＯ去除率６６．０－７１．０％，同时，沼气产率为２．４－３．０Ｌ·ｌ＾－１·ｄ＾－１，沼气中烷含量为６１．５－６９．１％。该法耗能小，沼气可回收，经济效果明显。     

毛发载体生物膜法处理味精离交废水

利用经特定脱脂处理的毛发作载体，经定向培菌挂膜后，对高浓度ＣＯＤ和高硫酸根含量的味精度交废水进行小试和中试研究，表明，在一定供气量和温度条件下，废水ＣＯＤ总去除率可稳定在９６％以上，在供氧不足的兼性条件下或温度较低时，仍有较高去除效果，其对ＳＯ４＾２－的总去除率可达９８％以上，２ｍ＾３／ｈ的中试经历了三个月实际运行，运行结果表明该工艺已具有生产建立生产性装置的技术条件。     

PCDDs在氯仿溶液中的紫外光解

使用ＮＤＣ－３型化学反应仪、３００Ｗ汞灯和１５ｍｌ反应管，于４３℃进行了２，３，７，８－ＴＣＤＤ，１，２，３，７，８－Ｐ５ＣＤＤ，１，２，３，４，７，８－ＨｘＣＤＤ，１，２，３，４，６，７，８－ＨｐＣＤＤ和ＯＣＤＤ在氯仿溶中的紫外光解，其一级反应速率常数测得值依次为０．５４，０．２９，０．１５，０．１５和０．１９ｍｉｎ＾－１，反应半衰期ｔ１／２均在５ｍｉｎ以内，还原脱氯是主要的光解途径，并有大量低     

生物滤池对气相与液相中污染物质的净化

通过实验室研究探讨了生物滤池同时处理废水和废气的可行性。试验结果表明：在２５℃－３７℃条件下，甲苯废气的流量为９０Ｌ／ｈ，甲苯浓度为５００ｍｇ／ｍ＾３；废水的流量为０．４Ｌ／ｈ，ＣＯＤｃｒ浓度为４００－７５０ｍｇ／Ｌ，甲苯与ＣＯＤｃｒ的去除率分别是７０％－７２％和８６％－８９％。     

Pesticide wastewater treatment using the combination of the microbial electrolysis desalination and chemical-production cell and Fenton process

• MEDCC combined with Fenton process was developed to treat real pesticide wastewater. • Pesticide removal was attributable to desalination in the MEDCC. • High COD removal was attributable to organic distributions in different chambers. The combination of the microbial electrolysis desalination and chemical-production cell (MEDCC) and Fenton process for the pesticide wastewater treatment was investigate in this study. Real wastewater with several toxic pesticides, 1633 mg/L COD, and 200 in chromaticity was used for the investigation. Results showed that desalination in the desalination chamber of MEDCC reached 78%. Organics with low molecular weights in the desalination chamber could be removed from the desalination chamber, resulting in 28% and 23% of the total COD in the acid-production and cathode chambers, respectively. The desalination in the desalination chamber and organic transfer contributed to removal of pesticides (e.g., triadimefon), which could not be removed with other methods, and of the organics with low molecular weights. The COD in the effluent of the MEDCC combined the Fenton process was much lower than that in the perixo-coagulaiton process (<150 vs. 555 mg/L). The combined method consumed much less energy and acid for the pH adjustment than that the Fenton.     

微生物菌剂对不同废水的适配试验

采用15种不同的微生物菌剂,以葡萄糖配水、中药提取废水、啤酒废水、氨氮配水等为基质,分别测定了微生物菌剂的耗氧速率和厌氧比产甲烷速率,以单位菌剂对不同基质的耗氧速率和厌氧比产甲烷活性为指标,比较了各菌剂对废水的适配性.根据测定结果选择活性高的菌剂,在试验室进行了菌剂对废水的连续处理试验.结果表明,不同菌剂对同一种废水的好氧或厌氧活性不同,同种菌剂对不同废水的好氧和厌氧活性不同.废水的连续处理试验取得良好的处理效果.No.8菌剂处理葡萄糖配水,系统有机负荷最高可达(COD)10.8 g L-1d-1,COD去除率可达90%以上;采用No.10菌剂处理氨氮配水,好氧氨氮负荷可达(NH4-N )1.42 g L-1d-1,厌氧氨氮负荷可达(NH4-N )0.3 gL-1d-1,系统NH4-N 去除率可达90%以上.图2表3参8     

固氮菌J-25利用味精废水产生絮凝剂的研究

考察了微生物絮凝剂产生菌Azotobacter J-25在味精废水中发酵产生絮凝剂的絮凝特性。实验表明，味精废水经预处理后，加入有机碳源对絮凝剂产生菌Azotobaaer J-25进行培养，菌体在生长过程中产生絮凝剂，并将其分泌到细胞外，培养液的絮凝活性最高达98％以上。该絮凝剂在偏碱性的条件下，对高岭土悬浊液的絮凝效果最好．实际废水的净化实验表明，该微生物絮凝剂对多种废水具有良好的净化效果，尤其对石化废水处理效果最好，CODCr，SS，色度的去除率分别为66．7％，98．3％，93．7％。     

Degradation of refractory organics in concentrated leachate by the Fenton process: Central composite design for process optimization

• 90% total COD, 95.3% inert COD and 97.2% UV₂₅₄ were removed. • High R² values (over 95%) for all responses were obtained with CCD. • Operational cost was calculated to be 0.238 €/g COD_removed for total COD removal. • Fenton oxidation was highly-efficient method for inert COD removal. • BOD₅/COD ratio of leachate concentrate raised from 0.04 to 0.4. The primary aim of this study is inert COD removal from leachate nanofiltration concentrate because of its high concentration of resistant organic pollutants. Within this framework, this study focuses on the treatability of leachate nanofiltration concentrate through Fenton oxidation and optimization of process parameters to reach the maximum pollutant removal by using response surface methodology (RSM). Initial pH, Fe²⁺ concentration, H₂O₂/Fe²⁺ molar ratio and oxidation time are selected as the independent variables, whereas total COD, color, inert COD and UV₂₅₄ removal are selected as the responses. According to the ANOVA results, the R² values of all responses are found to be over 95%. Under the optimum conditions determined by the model (pH: 3.99, Fe²⁺: 150 mmol/L, H₂O₂/Fe²⁺: 3.27 and oxidation time: 84.8 min), the maximum COD removal efficiency is determined as 91.4% by the model. The color, inert COD and UV₂₅₄ removal efficiencies are determined to be 99.9%, 97.2% and 99.5%, respectively, by the model, whereas the total COD, color, inert COD and UV₂₅₄ removal efficiencies are found respectively to be 90%, 96.5%, 95.3% and 97.2%, experimentally under the optimum operating conditions. The Fenton process improves the biodegradability of the leachate NF concentrate, increasing the BOD₅/COD ratio from the value of 0.04 to the value of 0.4. The operational cost of the process is calculated to be 0.238 €/g COD_removed. The results indicate that the Fenton oxidation process is an efficient and economical technology in improvement of the biological degradability of leachate nanofiltration concentrate and in removal of resistant organic pollutants.     

Coupled aerobic and anoxic biodegradation for quinoline and nitrogen removals

Quinoline (C₉H₇N) commonly occurs in wastewaters from the chemical, pharmaceutical, and dyeing industries. As quinoline is biodegraded, nitrogen is released as ammonium. Total-N removal requires that the ammonium-N be nitrified and then denitrified. The objective of this study was to couple quinoline biodegradation with total-N removal. In a proof-of-concept step, activated sludge was sequenced from aerobic to anoxic stages. The ammonium nitrogen released from quinoline biodegradation in the aerobic stage was nitrified to nitrate in parallel. Anoxic biodegradation of the aerobic effluent then brought about nitrogen and COD removals through denitrification. Then, simultaneous quinoline biodegradation and total-N removal were demonstrated in a novel airlift internal loop biofilm reactor (AILBR) having aerobic and anoxic zones. Experimental results showed that the AILBR could achieve complete removal of quinoline, 91% COD removal, and 85% total-N removal when glucose added as a supplemental electron donor once nitrate was formed.     

活性污泥吸附预处理重油裂化制气废水

利用剩余活性污泥对含有高浓度芳香族化合物的重油裂化制气废水进行预处理的研究并提出了合适的吸附条件。结果表明，活性污泥吸附预处理对COD和悬浮物有明显的去除效果，而且可以提高废水BOD5／COD的比值，另外还有降解芳香族化合物的作用，使进入生物处理系统的废水的可生物降解性有明显的改善。这一方法为利用普通废水生物处理系统中产生的剩余活性污泥来预处理难降解的工业废水提供了一条有效的途径。     

Treatment of dye‐containing wastewater by sequencing batch reactor with powdered activated carbon addition

The process involving the combination of powdered activated carbon (PAC) and biomass in the aeration basin of conventional continuous‐flow activated sludge system, known as the PACT process, has proven to be effective for treating toxic pollutants present in industrial wastewaters. In view of the many advantages of sequencing batch reactors (SBR) operationally, the objective of this study is to evaluate the PACT process under SBR operation to treat wastewater containing Acid Blue 25 (AR) and Basic Yellow 2 dyes (BR). The SBR systems were operated with FILL, REACT, SETTLE and DRAW periods in the ratio of 0.25:3.75: 1.0:1.0 for a cycle time of 6 h. The average COD and AR removal efficiencies were 89% and 93%, respectively with PAC addition compared to 76% and 7%, respectively, without PAC addition. In the case of BR, the average removal efficiencies of COD and dye increased from 52% and 9% to 90% and 93%, respectively, with PAC addition. Kinetic study conducted for the REACT period showed that both dyes exhibited a very pronounced inhibitory effect on the activities of the microorganisms. The addition of PAC was capable of reducing the inhibitory effect of only BR but not AR on the microorganisms.     

多通道网状电极电化学预处理垃圾渗滤液反渗透浓缩液

反渗透(Reverse Osmosis,RO)因出水水质好、运行成本低等优势常用于垃圾渗滤液的处理,但产生的RO浓缩液具有COD高、色度高、盐分高、难降解等特点,其处理存在效果差、能耗和成本均较高等问题.本工作采用氧化钌/氧化铱涂层电极(RuO2/IrO2-Ti)的钛网为阳极,以304不锈钢电极为阴极,设计制作了6通道的电化学反应器,通过电化学氧化处理RO浓缩液,研究考查了电流密度、循环流速、比电极面积等参数对COD去除效果的影响,分析了电化学氧化去除难降解有机物并同时脱盐的过程机理与能耗.结果表明,在电流密度32.89 mA·cm^-2,循环流速0.46 cm·s^-1,比电极面积65.10 m²·m^-3的条件下,电化学氧化处理RO浓缩液3 h,COD去除率可达68.0%,TOC去除率可达40.6%,脱盐率可达72.1%,去除单位质量COD能耗仅为常规的板状电极电化学反应器的25.5%.本工作可为垃圾渗滤液RO浓缩液的预处理提供新思路.     

Combined treatment of phenolic wastewater by wet air oxidation and activated sludge

Wet air oxidation (WAO) is employed in this work for treating high concentration chemical wastewater containing phenol and/or phenolic compounds. Experimental results indicate that over 90% removal of phenol or phenolic compounds can be efficiently achieved in the WAO process. Despite of the high treatment efficiency of the WAO process, the treated wastewater, however, still retains relatively high chemical oxygen demand (COD) concentration and does not meet the safe discharge standard. Hence further treatment of the WAO treated wastewater by an aerobic biological treatment using acclimatized activated sludge is necessary. It is found in the present studies that the combined process, if appropriately operated, is capable of drastically reducing the COD concentration of the high concentration chemical wastewater to meet the safe discharge requirement. The operating conditions of the combined process are investigated to determine their respective effects on the overall treatment efficiency. The experimental data also indicate that the oxidation reaction can be represented by a first order kinetics in terms of the component or COD concentration. For both single component and multicomponent wastewaters, the WAO process was found to have different activation energy for oxidation below and above 200°C, suggesting possibly different reaction mechanisms between these temperature ranges. The experimental results provided in the present work can provide significant and practical information for optimizing the combined treatment method.     

垃圾渗滤液的Fenton氧化预处理研究

采用Fenton氧化法对垃圾渗滤液进行预处理,考察了渗滤液初始pH值、H2O2和FeSO4.7H2O投加量、H2O2/Fe2＋投加的物质的量比及氧化反应时间等对Fenton氧化处理效果的影响,获得Fenton氧化处理垃圾渗滤液的最佳工艺条件：初始pH=3.0,H2O2投加量为5.0 mL.L-1,FeSO4.7H2O投加量为3.48 g.L-1,H2O2/Fe2＋物质的量比为4-1,反应时间为1.5 h。最佳条件下处理后垃圾渗滤液COD为5 220 mg.L-1,COD去除率达57.8%。凝胶渗透色谱和三维荧光光谱分析结果表明,垃圾渗滤液中主要含有腐殖酸类大分子物质,经Fenton氧化后降解变成小分子化合物。