污泥的分形维数与粒度随统计样本的变化特征

研究了厌氧折流板反应器(ABR)中成熟颗粒污泥和某污水处理厂回流、厌氧、曝气、消化4个单元中絮状污泥的一维、二维分形维数(D₁、D₂、D′₂)及平均粒径在不同统计样本数下的变化规律。结果表明，当统计样本数达到200以上时，ABR中成熟颗粒污泥的D₁、D₂、D′₂值趋于稳定；当样本数达到300以上时，某污水处理厂4个单元中絮状污泥的D₁、D₂、D′₂值也分别趋于稳定。此外，1^#ABR中的颗粒污泥在统计样本数达到350以上时其中位直径趋于稳定，而2^#ABR和某污水处理厂4个处理单元中的污泥，在试验样本数下并未达到稳定。基于研究的结果和相关文献的结论，研究认为，如果需要得到稳定的平均粒径结果，可能需要大量的统计样本数，该样本数至少要大于600。     

双室微生物燃料电池型BOD传感器性能

构建了双室微生物燃料电池(MFC),并应用于污水BOD的检测。优化了MFC型BOD传感器的检测条件,分析了传感器进行污水BOD检测的特征。结果表明,以A2/O污水处理工艺中厌氧段污泥进行接种,双室MFC型BOD传感器2周内完成启动,所产电流达到稳定。传感器的最佳检测条件为外接电阻500Ω,添加缓冲溶液并维持待测水样pH为7.0,添加35 mg/L的L-半胱氨酸作为吸氧剂维持阳极室厌氧环境,阴极室富氧水流量为20 mL/min。利用MFC产生的电流峰值准确检测污水水样BOD浓度,传感器检测范围为10~50 mg/L,检测时间小于3 h;利用MFC产生的电荷量准确检测污水水样BOD浓度,检测范围为10~100 mg/L,检测时间小于10 h。利用MFC电流峰值和电荷量检测污水水样BOD浓度,偏差均小于15%,传感器运行稳定,寿命较长。     

降低负荷以提高反硝化颗粒污泥的稳定性

在上流式污泥床反应器（USB）内，接种好氧活性污泥，以甲醇为碳源，NO-3为电子受体，经过40多d培养，得到良好的反硝化颗粒污泥，粒径2～3 mm，MLSS为36 g/L，氮去除速率和COD去除速率分别在0.15 g NO₃-N/(g VSS·d)和0.8 g COD/(g VSS·d)。当负荷提高至6.44 g NO₃-N/(L·d)继续运行1周后，观察到反应器内颗粒污泥出现上浮，浓度降低，颗粒粒径多数在3～5 mm，外观呈乳白色。为恢复反应器稳定运行，当负荷降至3.86 g NO₃-N/(L·d)时，上浮现象减轻，当负荷降至2.57 g NO₃-N/(L·d)时，上浮现象消失，颗粒污泥密度由不稳定时的1.0018 g/cm³提高到1.0126 g/cm³，颗粒粘连现象基本消失，污泥氮去除速率在0.19 g NO₃-N/(g VSS·d)，连续运行30 d，系统保持稳定。分析认为，颗粒污泥表面微生物生长速度过快是导致不稳定的主要因素，较长的泥龄有利于系统稳定。     

蒽降解菌T2的最佳培养条件及其对蒽的生物降解动力学研究

从长期被石油污染的土壤中筛选得到一株以蒽为惟一碳源的混合菌T₂，在接种量为1%，pH为7，温度为30 ℃，摇床转速为120 r/min，蒽的初始浓度为100 mg/L的条件下培养5 d后，其对蒽的降解率可以达到56.6%。通过单因素实验和正交实验对菌种T₂的培养条件进行研究，得到菌种T₂的最佳培养条件为：接种量为5%，pH为6，温度为35 ℃，蒽的初始浓度为40 mg/L时，最适合菌种生长。另外，菌种T₂对蒽的降解动力     

污泥渗水砖的制备研究

结合压制成型和传统的烧结砖工艺，实验以城市生活污泥、黄河淤泥、煤矸石及砂为原料，制备渗水铺地砖。通过正交试验得到最优工艺参数为w_{(黄河淤泥)}∶ww_(煤矸石)∶w_(污泥)∶w_(砂)＝33％∶22％∶15％∶30％、成型压力为20 MPa、烧结温度为1 100℃、保温时间为1.5 h，骨料砂的粒径为1～2 mm。制备的成品抗压强度为21.8 MPa，渗水系数为1.03×10^－2 cm/s。并对成型压力及烧结温度对渗水砖抗压强度及渗水系数的影响进行了讨论。     

微曝气Fenton氧化法处理模拟双酚A废水的效果及其生物验证

研究了微曝气Fenton氧化法关键工艺参数对模拟双酚A（BPA）废水处理效果的影响，并从活性污泥性质和污染物去除率两方面，采用膜生物反应器(membrane bioreactor, MBR)对微曝气Fenton氧化法的处理效果进行了实验验证，为实现BPA废水的生物处理奠定基础。结果表明，初始pH值、反应时间、H₂O₂/COD(质量浓度比)、H₂O₂/Fe²⁺ (摩尔浓度比)、反应温度及曝气量均对预处理效果有较大影响，在最佳条件下，COD去除率可达70%，BOD/COD值则由原废水的0.02提高到0.50以上。MBR处理上述出水的结果表明，经微曝气Fenton氧化处理BPA的废水，可较好地适应后续的生化处理。     

亚硝酸盐反硝化颗粒污泥的二次启动试验研究

接种0～4℃贮存2个月亚硝酸盐反硝化颗粒污泥，以甲醇为电子供体、亚硝酸盐为电子受体在USB(上流式污泥床)反应器内进行二次启动。结果显示，在逐步提高进水负荷下，约46 d完成了反应器二次启动，污泥床负荷达到3.43 g N/（L·d），NO₂-N去除率为99%；在稳定运行阶段，当进水NO₂-N浓度为50 mg/L、负荷从1.7 g N/（L·d）逐步提高至5.1 g N/（L·d）时，NO₂-N去除率均大于98%；当表观流速为2.68 m/h、进水负荷逐步提高至8.0 g N/（L·d）时，脱氮率下降至63%，过程中污泥床最大去除速率约为5.7 g N/（L·d）。研究认为，亚硝酸盐颗粒污泥床具有稳定和去除效率高等特点。     

剩余污泥制备活性炭及其应用研究

以城市污水处理厂二沉池排出的剩余污泥为原料，采用不同活化方法制备活性炭，同时对比活化效果，研究了制备工艺条件对污泥活性炭吸附性能及产率的影响。结合比表面积、孔径分布和扫描电镜表征分析，对制备的污泥活性炭的性能进行评价，并探讨了污泥活性炭作为水处理吸附剂的去除效果。结果表明，以ZnCl₂为活化剂制备的活性炭性能较好，其最佳制备条件为：活化温度550℃，活化时间45 min，ZnCl₂浓度40％，固液比1∶2。制得的污泥活性炭的碘吸附值为496 mg/g，产率为51.8％，比表面积为301.4 m²/g,孔体积为0.37 mL/g，微孔体积为0.08 mL/g，平均孔径为5.78 nm。将该产品用于处理城市污水，投加量为0.8％，吸附平衡时间约为60 min时，对COD的去除率为81％，吸附容量为42.53 mg/g。     

呼吸测量法测定废水中活性异养菌COD组分

废水中的活性异养菌(XH)会影响废水生物处理过程动力学,过程模拟需要对其定量表征.通过2种方法对城市污水中XH进行呼吸测量,分别结合XH最大比呼吸速率参数(P方法)和细胞生长过程模型拟合(F方法)测定其中的XH-COD组分.结果表明,F方法的测量结果是P方法的0.6～0.9倍,两者存在一定的丰廿关性;对于含高XH、低易生物降解基质(RBCOD)的废水,呼吸测量得不到明显的呼吸速率指数上升段,影响F方法的测定结果,水样稀释和外加RBCOD是可行的改进办法.使用P方法得到某城市污水厂进水的XH-COD占总COD的23%～46%(平均31%),高于多数文献报道结果.     

Fenton氧化破解污水处理厂污泥

研究了Fenton氧化反应的影响因素pH值、H₂O₂/Fe²⁺投加比、反应温度和反应时间对污泥破解效果的影响，并以污泥上清液中蛋白质、糖类、SCOD及污泥TSS、VSS的变化来表征污泥破解的程度。结果表明，最佳破解条件为：pH=5，最佳H₂O₂/Fe²⁺投加比为24：1，反应温度为70℃，反应时间为90 min，在该条件下，SCOD、溶解性蛋白质和多糖分别由88.76、19.70和14.95 mg/L增加到3 714.64、2 039.90和289.70 mg/L；TSS及VSS分别由34.60 g/L、19.76 g/L降为26.60 g/L、14.22 g/L，去除率分别为23.12%和 28.14%。Fenton氧化破解污泥，能够有效促进污泥絮体分解，有利于进行后续的厌氧消化处理。     

Monitoring the toxicity of phenolic chemicals to activated sludge using a novel optical scanning respirometer.

This paper reports the development of optical scanning respirometer for determining the toxicity of chemicals to activated sludge. The respirometer is used to measure the dissolved oxygen concentration by monitoring the luminescence intensity of ruthenium dye immobilized in a polymer film in contact with the wastewater sample. The intensity is related to the extent of oxygen quenching of luminescence. The toxicity of chemicals can be evaluated by measuring the inhibition on respiration rate of microorganism using the scanning respirometer. The IC50 values (concentration of a chemical that exhibits 50% respiration inhibition) of various phenolic chemicals in activated sludge were determined. The performance of this method is compared with other toxicity methods. The experimental results indicate that the reproducibility and sensitivity of this respirometer are reasonably good.     

城市污水厂污水污泥的热值测定分析方法研究

建立热力学指标是污水生物处理过程热力学分析的基础工作，目前仍缺乏污水污泥化学能测试的标准方法。采用IKA C5000型自动热量计对某城市二级污水处理厂进水、出水、初沉污泥、剩余污泥、混合污泥和脱水污泥进行了热值测定，样品前处理采用103～105℃烘干获得干燥基，用苯甲酸进行加标回收。参照煤的发热量测定方法得到样品的高位热值。试验结果显示：出水干燥基的热值为05 kJ/g，进水干燥基的热值为4 kJ/g以上，各工艺段的污泥干燥基热值较高，基本都在12 kJ/g以上，接近右江褐煤水平。测定结果的标准偏差≤±0.452%，相对标准偏差≤±0.136%。通过同一批样品的元素分析及Dulong公式理论推算，发现2种方法可得到相似的结果。     

BOD微生物传感检测仪中高效微生物膜的研究

为了制备高效微生物膜，从污水中筛选菌种（QT2061），经BIOLOG鉴定为枯草芽孢杆菌。并以聚乙烯醇为包埋剂制作BOD生物传感器微生物膜，通过对国家标准样品及几种典型水样的检测，结果表明，该微生物传感器的响应时间为8 min，可连续稳定测试10 d以上；对国家标准溶液的测试结果准确度较高，相对误差≤5%；对实验中几种水样均有响应，测试结果与5日法的测试结果有良好的相关性（相对偏差≤5%）。     

接种稀释水的空白对BOD_5测定的影响

从接种液种类、空白 BOD5大小、接种液最佳添加范围等方面对 BOD5测定进行探讨 ,提出以接纳工业废水的河水作为最佳接种液 ,雨季时以土壤浸取液更适合。探讨了接种液空白值对 BOD5标液和工业废水的影响。结果表明 ,河水空白应控制在 0 .1～0 .8mg/ L,土壤浸取液空白控制在 0 .0 1～ 0 .1 0 mg/ L为宜。     

Preparation of biofilm electrode with Xanthomonas sp. and carbon nanotubes and the application to rapid biochemical oxygen demand analysis in high-salt condition

A Xanthomonas sp. was isolated from the sludge on the drain outlet of a pharmaceutical factory. Then, the bacterium and carbon nanotubes (CNTs) were co-attached to an oxygen electrode for rapid analysis of biochemical oxygen demand (BOD). The response current was linear with BOD values in the range 10 to 300 mg/L for standard BOD solution with a response time of 35 seconds (R = 0.9994) and 20 to 580 mg/L for pharmaceutical wastewater with a response time < or =200 seconds (R = 0.9985), which means that this modified electrode might be used for online BOD analysis of pharmaceutical wastewater. Further studies revealed that the modified electrode can be used for BOD measurement in a high-salt condition. Also, the bacterium/CNTs biofilm can maintain its activity and good performance, even after being sealed and stored at 4 degrees C for 50 days.     

Effects of nano-copper(II) oxide and nanomagnesium oxide particles on activated sludge

Effects of nano-copper(II) oxide (nano-CuO) and nanomagnesium oxide (nano-MgO) particles on activated sludge endogenous respiration (aerobic digestion), biochemical oxygen demand (BOD) biodegradation, and nitrification were investigated through respiration rate measurement. For comparison, the effects of Cu(II) and Mg(II) ions on activated sludge were also studied. Results indicated that soluble Cu(II) has half maximum inhibitory concentration (IC50) values of 19, 5.5, 53, and 117 mg Cu/L for endogenous respiration, BOD biodegradation, ammonium oxidation, and nitrite oxidation, respectively. However, nano-CuO only inhibited BOD biodegradation at 240 mg Cu/L or more, and its associated toxicity was primarily caused by soluble Cu(II). In contrast, soluble Mg(II) was not toxic to activated sludge in the experimental concentration range, but nano-MgO inhibited BOD biodegradation and nitrification with IC50 values of 70 and 143 mg Mg/L, respectively. Further study indicated that the toxicity of nano-MgO resulted primarily from increased pH following MgO hydrolysis.     

Online biochemical oxygen demand monitoring for wastewater process control--full-scale studies at Los Angeles Glendale wastewater plant, California.

The main objective of this investigation is to determine whether or not it would be feasible to use the measured values of biochemical oxygen demand (BOD) of wastewater obtained by an online instrument at the Los Angeles/Glendale Water Reclamation Plant (California) for controlling its activated sludge process. This investigation is part of a project to develop online BOD monitoring for process control in the City of Los Angeles wastewater treatment plants. Tests studied the Siepmann und Teutscher GmbH (ISCO-STIP Inc., Lincoln, Nebraska) BIOX-1010, which uses a bioreactor containing a culture of microbes from the wastewater to measure soluble BOD in 2 minutes. This rapid approximation to the operation of secondary treatment allows anticipation of system response. Calibration measurements allow the operators to find a conversion factor for the instrument's microprocessor to compute values of BOD that agree well with the standard 5-day BOD (BOD5) measurement, despite the differences in the details of the two testing methods. This instrument has recently been used at other wastewater treatment plants, at a number of airports in Europe and the United States to monitor runway runoff, and is also being used on waste streams at an increasing number of food processing plants. A comparison was made between the plant influent BOD values obtained by the BIOX-1010 online monitor from the end of August, 2000, to late January, 2001, and the individual and average values obtained for the same period using the standard BOD5, 20 degrees C test, to determine the effectiveness of the Biox-1010 to identify shock loads and their duration. Individual BOD estimates and averages over periods of overly high biological loads (shock loads) were compared, and the instrument readings were evaluated for their effectiveness in detecting shock loads. The results were highly satisfactory, so the instrument was used to trigger a shock-load warning alarm since late September, 2000. This allowed flow diversion and temporary storage to prevent process upsets.     

BOD5测定中的影响因素

BOD5的测定方法众多，文中从实验用水的质量、接种稀释液的要求、COD5值的确定、计算结果的取舍等方面予以分析．提出经验性的建议和办法。     

Nitrification/denitrification in an intermittent aeration process for swine wastewater

Abstract

Nitrogen removal by a methane fermentation plus activated sludge process with the intermittent aeration was presented based upon a full‐scale pig farm experiment. Swine wastewater had a T‐N/BOD ratio from 0.2–0.29. The BOD concentration input to the process ranged from 1050–1608 mg l^‐1 and the T‐N concentration from 273–350 mg l^‐1. More than 90% of organic carbon was removed in each experimental run. Only small concentrations of NO₃‐N were found in the effluent and higher than 60% of the T‐N and 73% of NH₄‐N which were loaded to the intermittent aeration tank was removed. The nitrogen balance of each run was calculated. Denitrification was estimated to be accountable for 45–90% of the T‐N removed in the intermittent aeration tank. Denitrification rate increased as the BOD concentration increased (> 1300 mg l^‐1). The T‐N removal percentage was a function of the T‐N/BOD ratio of the influent. Although higher DO concentration (> 3 mg l^‐1) did not enhance the denitrification rate, nitrification did maintain at relative higher rates at a lower DO concentration (ave. 1.5 mg l^‐1). An operational condition of intermittent interval of aeration/nonaeration at 1:1 hr is better than that of the condition at 3:1 hr. As a result, T‐N and NH4‐N were removed up to 30% and 40% respectively, and the denitrification rate reached 79% in the intermittent aeration tank. An experimental run in a pilot plant on treating anaerobically pretreated swine wastewater was observed to verify simultaneous nitrification/denitrification. The results of the full‐scale plant experimentation seem to be confirmed by those obtained from the pilot plant runs.     

重金属对活性污泥微生物毒性的比较研究

采用发光细菌毒性、活性污泥脱氢酶毒性、硝化抑制毒性3种方法测定Hg、Cd、Zn、Pb 4种重金属对活性污泥微生物的毒性,并对测定结果进行了比较.结果表明,发光细菌毒性测定方法的灵敏度最高,测得的重金属半数有效浓度(ECSO)最低,4种重金属对发光细菌发光强度的抑制程度由大到小顺序依次为Hg>Cd>Zn>Pb;活性污泥脱氢酶毒性和硝化抑制毒性的测定结果与发光细菌毒性测定结果相比,灵敏度相对较低,测得的重金属ECSO相对较高,测得的活性污泥脱氢酶活性的抑制程度由大到小顺序依次为Cd>Hg>Zn>Pb,与测得的活性污泥硝化速率抑制程度大小顺序一致.但2者测得的EC50有所差别.为了更准确的判定重金属对活性污泥微生物的毒性影响.至少应取不同的重金属毒性终点指示指标做一组毒性实验,而不能以发光细菌毒性测定结果作为唯一的判定依据,这可能会过分夸大重金属对污水处理工艺的冲击能力,导致污水处理成本无谓增加.