生化降解工业废水过程中CODcr的变化规律

基于ＣＯＤＢ与废水底物浓度成正比的假设，推导了ＣＯＤｃｒ在生化降解过程中的变化规律。研究了变化规律之特点，并以实验证实了规律的正确性。论证了以ＣＯＤＢ／ＣＯＤｃｒ为指标的废水可生化性评价方法的可行性。     

生化需氧量测定图解法及与标准法的比较

介绍了ＢＯＤ５图解法的原理和实验的条件与方法，并采用图解法和标准法同时对一些实际水样进行ＢＯＤ５测定，将结果进行配对ｔ检验法检验，结果不显著，证明了图解法的合理性、可信性和实用性。     

接种稀释水的空白对BOD5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０．０１－０．１０ｍｇ／Ｌ为宜。     

底泥对河流的二次污染浅析

根据底冲中污染物质累积和释放过程和底泥对河流二次污染的机理,运用适用的模式和苏州河的实测资料,可得到二次污染ＢＯＤ和ＣＯＤ的年释放量,以及增加上覆河上的ＢＯＤ和ＣＯＤ浓度。由此认为,对于底泥污染严重的河流,疏浚是必不可少的,其目的在于清除或隔绝黑富集层上覆河上的二次污染。     

SBR法处理印染废水的研究

应用ＳＢＲ法、ＰＡＣ－ＳＢＲ法，微电解－ＳＢＲ法对印染废水进行了对比处理试验研究。试验结果表明：微电解－ＳＢＲ法处理效果优于其它两种方法，当进水ＣＯＤ＝１０００～１６００ｍｇ／Ｌ，色度＝２００～８００倍，ＢＯＤ５＝２５０～４００ｍｇ／Ｌ时．ＣＯＤ去除率在８５％左右，ＢＯＤ５去除率和脱色率均在９０％以上，出水达到排放标准。     

新型污水生化参数测试仪的研制和应用

介绍了ＤＯ、ＢＯＤｓ、Ｒｓ、ＫＬａ及α、β、θ等污水处理工程常用生化参数的测试原理和仪器应用。用ＢＯＤｓ替代ＢＯＤ５使测试时间从５天缩短到２０分钟，参数值一致。上述参数的测试仪器已鉴定投产。     

加压生物接触氧化法处理增塑剂生产废水试验研究

主要介绍了采用加压生物接触氧化法处理增塑剂废水。在停留时间为２２ｈ，压力为０．４ＭＰａ，水中溶解氧保持５ｍｇ／Ｌ左右时，进水ＣＯＤＣＲ为１１７００ｍｇ／Ｌ，ＢＯＤ５为６８７３ｍｇ／Ｌ，出水ＣＯＤＣｒ去除率为８９％，ＢＯＤ５去除率为９６％。为增塑剂废水治理工程设计提供了重要参数。     

半导体复合系光催化降解水溶性染料研究

研究了半导体复合体系ＺｎＯ－ＣｕＯ－Ｈ２Ｏ２－ａｉｒ对水溶性染料活性艳红Ｘ－３Ｂ等六种有机物质的光催化降解处理，得到了较高的脱色效果和ＣＯＤ去除率。讨论了不同染料光解难易的原因以及脱色率和ＣＯＤ去除率的差异。     

SBR法处理医药有机废水工艺研究

医药有机废水中ＣＯＤｃＲ２０００－３０００ＭＧ／ｌ，ｂｏｄ５３００－５００ＭＧ／ｌ，ｐＨ为４－５左右，采用ＳＢＲ法处理后，ＣＯＤｃｒ去除率大于８５％，ＢＯＤ５去除率大于９０％，ｐＨ６－９。为废水后续处理达标奠定了良好的基础。     

SBR工艺处理制革废水的初探

ＳＢＲ工艺具有许多优点。现有活性污泥处理工艺经适当调整，采用ＳＢＲ工艺对制革废水的处理进行了试验，实践表明，ＳＢＲ曝气池ＣＯＤＣＲ的去除率可达到７０％以上。并探讨了如何进一步提高ＣＯＤＣＲ的去除率。     

废水可生物降解COD组分2种表征方法的比较

利用自行开发的混合呼吸速率测量仪在接种污泥的条件下对重庆某城市污水处理厂污水进行了呼吸速率测试（短期BOD测试,以呼吸速率测量重新进入内源呼吸阶段为结束）;同时应用美国产BI-2000电解质呼吸仪在不接种污泥的条件下对该污水进行了BOD测试（长期BOD测试,理论上以污水中所有有机物矿化为结束）。对2种测试方法及其结果进行了比较,结果表明,2种方法得到的BCOD存在很大差异,短期BOD测试方法得到的结果仅为长期BOD测试方法得到的结果的40％～60％。通过批式呼吸测量方法测定了原废水中的活性异养微生物浓度XH(0),结果表明,XH(0)与BCOD_st之和与BCOD_lt比较接近,两者之比在0.88～1.02之间,平均值为0.94。     

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。     

Semi-specific Microbacterium phyllosphaerae-based microbial sensor for biochemical oxygen demand measurements in dairy wastewater

Although the long incubation time of biochemical oxygen demand (BOD₇) measurements has been addressed by the use of microbial biosensors, the resulting sensor-BOD values gained from the measurements with specific industrial wastewaters still underestimates the BOD value of such samples. This research aims to provide fast and more accurate BOD measurements in the dairy wastewater samples. Unlike municipal wastewater, wastewater from the dairy industry contains many substrates that are not easily accessible to a majority of microorganisms. Therefore, a bacterial culture, Microbacterium phyllosphaerae, isolated from dairy wastewater was used to construct a semi-specific microbial biosensor. A universal microbial biosensor based on Pseudomonas fluorescens, which has a wide substrate spectrum but is nonspecific to dairy wastewater, was used as a comparison. BOD biosensors were calibrated with OECD synthetic wastewater, and experiments with different synthetic and actual wastewater samples were carried out. Results show that the semi-specific M. phyllosphaerae-based microbial biosensor is more sensitive towards wastewaters that contain milk derivates and butter whey than the P. fluorescens-based biosensor. Although the M. phyllosphaerae biosensor underestimates the BOD₇ value of actual dairy wastewaters by 25–32 %, this bacterial culture is more suitable for BOD monitoring in dairy wastewater than P. fluorescens, which underestimated the same samples by 46–61 %.     

新型BOD微生物传感流动注射检测仪的研制

研制采用微生物传感技术和流动分析技术来快速测定BOD的仪器。主要技术性能:测量周期为15min;误差率<5%;偏差<5%。通过对国家标准样品和不同水质污水的测试表明,其具有自动化程度高,测量周期短的优点;准确度、稳定性均达到国家标准;且具有良好的适应性。     

微生物膜法快速测定水中的BOD

利用微生物膜法快速测定水中的BOD,用质控样和标液进行方法准确度和精密度的考察,标准偏差在0.9%～5.2%之间,相对误差≤4.0%,加标回收率为95.5%～103%.与接种稀释法进行对比实验,相对误差在1.5%～10.3%范围内,两种方法测定结果基本一致.     

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。     

黄姜废水的铁炭微电解-混凝预处理研究

研究了高浓度黄姜废水的铁炭微电解-混凝工艺,结果表明,在进水pH 4.0、停留时间为40 min且有曝气条件下,COD去除率达到64.70%,色度去除率为72.22%,废水的BOD/COD值可由0.29提高到0.56,有利于废水的后续生化处理.     

一体化生物膜技术处理滨海农村污水

对厌氧-3级好氧/缺氧生物膜工艺进行技术改进,并对改进后的"一体化生物膜技术"处理低碳氮比农村生活污水进行了实际应用。新工艺增设了回流泵(回流比2∶1),且厌氧段悬浮填料装填率由原来的15%提高到30%,3级好氧/缺氧段YDT型弹性立体填料装填率依次由原来的50%、40%、25%提高到70%、60%和40%。装置连续稳定运行12个月,平均进水量为18 m3/d,HRT为3.7 d,监测结果表明:对COD、BOD、NH3-N、TN、TP和SS平均去除率分别为75.6%、85.9%、86.7%、63.9%、69.3%和85.5%;出水COD、BOD、NH3-N、TN、TP和SS的平均浓度分别在34.9、8.9、3.4、9.9、0.9和6.9 mg/L以下。改进后出水BOD和TN的去除能力有较大提高,除TP外其他各项指标均达到了设计要求。     

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.