高浓度洗毛废水生物降解的研究

根据高浓度洗毛废水的水质特性,选择、驯化出高效污泥和菌株,并对生物降解该废水时的工艺、污泥量、时间三要素进行了深入的研究．结果表明,对于物化处理彻底的废水, Ｈ／ Ｏ 工艺（ 水解／ 好氧工艺） 与好氧工艺处理差异不大;７０ ％ 左右物化效果时, Ｈ／ Ｏ 工艺处理时, Ｃ Ｏ Ｄｃｒ 去除率增加;废水在处理过程中成分变化大,后段水可用筛选优势菌的方法处理．实验室流动模型运行结果为：在原水ρ（ Ｃ Ｏ Ｄｃｒ） １８５４４ ｍｇ／ Ｌ 和设定ｔ Ｈ Ｒ（ 延滞期） 下,混凝后出水ρ（ Ｃ Ｏ Ｄｃｒ） ５３２２ ｍｇ／ Ｌ,水解池出水ρ（ Ｃ Ｏ Ｄｃｒ） ４７６３ ｍｇ／ Ｌ,好氧池出水 Ｃ Ｏ Ｄｃｒ１９９ ．９ ｍｇ／ Ｌ,总 Ｃ Ｏ Ｄｃｒ去除率为９８ ．９ ％     

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％。     

含酚废水高温生物处理效果的研究

本试验模拟焦化废水部分水质,进水酚约１０００ｍｇ／Ｌ,ＣＯＤｃｒ约２０００ｍｇ／Ｌ,水温维持在６０℃￣６８℃,从焦化废水生物处理厂的活性污泥中分离得到的１２株高温菌用于高温处理试验,结果酚的去除率在１２％￣１００％,ＣＯＤｃｒ的去除率在１３％￣９８％,两者的去除率变化如此之大,在于高温菌大多数为芽孢杆菌,是由于它们生活史中的营养细胞和芽胞不断交替演变所致。     

固定化微生物厌氧移动床——好氧法处理偶氮染料废水

在分离获得的三株高效脱色菌组成的混合脱色菌种基础上，利用固定化微生物 氧移动床与好氧生物氧化法结合的工艺处理人工配制的偶氮染料废水，在１５－１８℃的条件下，当原水ＣＯＤ浓度为１５００ｍｇ／Ｌ＝１５８０ｍｇ／Ｌ，色度４００倍，厌氧水为停留时间８ｈ，好氧容积负荷率４．０ｋｇＣＯＤ／ｍ＾３（填料），ｄ时，色度及ＣＯＤ的去除率分别为９６．９％及９３．４％。     

反渗透法处理土霉素结晶母液的研究

土霉素结晶母液经调节ｐＨ值后的水经预滤后进行反渗透处理,可使污染物去除率达９９％以上,排放水ＣＯＤｃｒ１５３ｍｇ／Ｌ、ＢＯＤ１０７ｍｇ／Ｌ水可以回用或达标排放。     

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     

硅营养缓解水稻幼苗Cd、Cr毒害的生理研究

两系法杂交稻“培杂山青”和常规稻“双桂３６”幼苗经较高浓度的Ｃｄ２＋（ｃ＝９．６～３８．４μｍｏｌ／Ｌ）或Ｃｒ３＋（ｃ＝７．５～２５．０μｍｏｌ／Ｌ）处理可使其叶片光合速率、叶绿素（ａ＋ｂ）含量、叶绿素ａ／ｂ比值、叶片可溶性糖、淀粉及可溶性蛋白质含量降低，而叶片的ＰＯＤ活性提高；低浓度Ｃｄ２＋（ｃ＝４．８μｍｏｌ／Ｌ）和Ｃｒ３＋（ｃ＝２．５μｍｏｌ／Ｌ）处理幼苗对上述生理指标有提高作用，但ＰＯＤ活性稍降低．加Ｓｉ（Ｎａ２ＳｉＯ３）［ｃ（ＳｉＯ２）＝１．３３１ｍｍｏｌ／Ｌ］的Ｃｄ、Ｃｒ处理比不加Ｓｉ的Ｃｄ、Ｃｒ处理的幼苗叶片上述生理指标明显提高，且明显降低其ＰＯＤ活性．说明Ｓｉ在不同程度上起到缓解Ｃｄ、Ｃｒ对水稻幼苗的毒害作用．而ｃ（Ｃｒ３＋）＝２５．０μｍｏｌ／Ｌ是“双桂３６”幼苗的致死浓度     

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．     

二段生物接触氧化法处理含硫废水的中试研究

用二段生物接触氧化法探索炼油过程中所产生的含硫废水的处理新方法． 结果表明：经此工艺处理后的出水 Ｃ Ｏ Ｄ、氨氮、硫化物和酚的质量浓度ρ分别为２６６ ．９ ｍｇ／ Ｌ、８２ ．８５ ｍｇ／ Ｌ、１ ．１８ ｍｇ／ Ｌ 和１ ．４３ ｍｇ／ Ｌ,相应的去除率分别为８６ ．３ ％ 、４０ ％ 、９２ ．７ ％ 和９９ ．３ ％ ,出水水质达到国家三级排放标准． 进出水水质的变化曲线表明,生物接触氧化法处理含硫废水对进水水质变化的适应能力比较强,出水水质比较稳定,显示了二段接触氧化法处理含硫废水的可行性     

硝基苯废水的厌氧-好氧基本实验与工艺理论分析

根据含硝基苯（ Ｎ Ｂ） 废水的水质特性,利用自然驯化和诱变驯化得到的两株厌氧菌 Ｂａｃｔｅｒｏｉｄｅｓ ｄｉｓｔａｓｏｎｉｓ（ 吉氏拟杆菌） 和 Ｂａｃｔｅｒｏｉｄｅｓ ｍｅｒｄａｅ（ 屎拟杆菌） ,采用厌氧填充床－ 好氧污泥床相结合的 Ａ／ Ｏ 工艺使 Ｎ Ｂ 得到彻底降解．研究表明：利用吸附能力强的活性炭作为厌氧填充床的载体,可以在短期内使高效菌挂膜;在影响填充床厌氧处理效果中,ｔ Ｈ Ｒ和进水ｐ Ｈ 值是主要影响因素,而 Ｎ Ｂ 质量浓度ρ（ Ｎ Ｂ） 和θ／ ℃次之．实验结果表明：进水ρ（ Ｎ Ｂ） 为３００ ～８００ ｍｇ／ Ｌ, Ｃ Ｏ Ｄ Ｃｒ 值为１ ５００ ～３ ５００ ｍｇ／ Ｌ,色度为１００ ～２５０ 倍,经过厌氧填充床控制ｔ Ｈ Ｒ＝ ２４ ｈ ,硝基苯转化率大于９０ ％ , Ｃ Ｏ Ｄ 去除率为２０ ％ ～３０ ％ ;在好氧污泥床中继续曝气１２ ｈ ,则总 Ｃ Ｏ Ｄ 去除率为６０ ％ ～７０ ％ ,色度去除率大于７０ ％ ．连续９０ ｄ 用氯霉素制药厂实际废水处理运行结果亦显示本工艺的可行性．     

二氧化氯催化氧化处理直接大红染料

研究了ClO2化学氧化体系和ClO2催化氧化体系。实验结果表明:单用ClO2化学氧化处理COD为3 400mg/L的直接大红染料配制废水时,最佳反应pH值为1,氧化剂ClO2经济用量为400 mg/L废水,反应时间为10 min,COD去除率可达85.9%,氧化指数(COD削减量∶ClO2投加量)=7。当ClO2与自制催化剂所组成的催化氧化体系用于对直接大红染料配制废水的处理时,最佳反应pH值为2左右,氧化剂ClO2经济用量为600 mg/L废水,反应时间为6 min,COD去除率可达96.6%,氧化指数=6。结果表明,ClO2催化氧化法是一种新型高效的处理难降解废水的技术,有着广阔的应用前景。     

采用絮凝—接触氧化法处理酿酒行业废水

采用絮凝-接触氧化法处理酿酒行业废水,原废水CODcr浓度为1627-2334mg/L,SS浓度为2095-2301mg/L,BOD5浓度为981-1005mg/L,色度为80-110倍,用絮凝-接触氧化法处理后,CODer浓度为280-295mg/L,SS浓度为178-199mg/L,CODcr浓度为145-150mg/L,色度为20-25倍,CODcr平均去除率为85%。悬浮物平均去除率为91%,BOD5平均去除率为85%,色度平均去除率为77%,各项指标符合国家排废标准。     

复合高效微生物处理高含盐石油开采废水

石油开采废水中高含盐量对微生物处理有强抑制作用。有针对性地筛选驯化了耐盐复合高效处理菌群对大港油田石油开采废水进行有机物降解，在废水的氯离子含量为20000～36000mg／L，COD浓度l600～4000mg／L范围内，高含盐量对耐盐复合高效微生物无明显抑制作用，结合物化处理方法COD去除率稳定在90％左右，处理后水达到二级排放标准。     

加压生物接触氧化法处理染料废水

本试验用一种新方法——加压生物接触氧化法处理染料生产废水.试验规模为1m~3/h.废水先经调节预处理,进水水质平均COD为619mg/L,BOD_5为336mg/L时,经6.5h处理后,出水COD去除率可达70%,BOD_5去除率在98%以上.与常规法相比,它具有处理时间短,主要设备占地面积小,设备投资省及操作总能耗低的特点.     

缺氧—SBR工艺处理焦化废水

对焦化废水进行曝气吹脱,10h氨氮去除率达73．7％,用缺氧－SBR工艺处理焦化废水,进水浓度为COD1474mg/L,NH3-N826.8mg/L时,缺氧SRT10h,SBR曝气10h,沉降2h,出水COD186mg/L,NH3-N290.5mg/L,去除率分别达到87．83％,64．9％。     

Sludge reduction during brewery wastewater treatment by hydrolyzation-food chain reactor system

During brewery wastewater treatment by a hydrolyzation-food chain reactor (FCR) system, sludge was recycled to the anaerobic segment. With the function of hydrolyzation acidification in the anaerobic segment and the processes of aerobic oxidation and antagonism, predation, interaction and symbiosis among microbes in multilevel oxidation segment, residual sludge could be reduced effectively. The 6-month dynamic experiments show that the average chemical oxygen demand (COD) removal ratio was 92.6% and average sludge production of the aerobic segment was 8.14%, with the COD of the influent at 960–1720 mg/L and hydraulic retention time (HRT) of 12 h. Since the produced sludge could be recycled and hydrolyzed in the anaerobic segment, no excess sludge was produced during the steady running for this system.     

Partial anammox achieved in full scale biofilm process for typical domestic wastewater treatment

• A full scale biofilm process was developed for typical domestic wastewater treatment. • The HRT was 8 h and secondary sedimentation tank was omitted. • Candidatus Brocadia were enriched in the HBR with an abundance of 2.89%. • Anammox enabled a stable ammonium removal of ~15% in the anoxic zone. The slow initiation of anammox for treating typical domestic wastewater and the relatively high footprint of wastewater treatment infrastructures are major concerns for practical wastewater treatment systems. Herein, a 300 m³/d hybrid biofilm reactor (HBR) process was developed and operated with a short hydraulic retention time (HRT) of 8 h. The analysis of the bacterial community demonstrated that anammox were enriched in the anoxic zone of the HBR process. The percentage abundance of Candidatus Brocadia in the total bacterial community of the anoxic zone increased from 0 at Day 1 to 0.33% at Day 130 and then to 2.89% at Day 213. Based upon the activity of anammox bacteria, the removal of ammonia nitrogen (NH₄⁺-N) in the anoxic zone was approximately 15%. This showed that the nitrogen transformation pathway was enhanced in the HBR system through partial anammox process in the anoxic zone. The final effluent contained 12 mg/L chemical oxygen demand (COD), 0.662 mg/L NH₄⁺-N, 7.2 mg/L total nitrogen (TN), and 6 mg/L SS, indicating the effectiveness of the HBR process for treating real domestic wastewater.     

Development of combined coagulation-hydrolysis acidification-dynamic membrane bioreactor system for treatment of oilfield polymer-flooding wastewater

• We created a combined system for treating oilfield polymer-flooding wastewater. • The system was composed of coagulation, hydrolysis acidification and DMBR. • Coagulant integrated with demulsifier dominated the removal of crude oil. • The DMBR proceed efficiently without serious membrane fouling. A combined system composed of coagulation, hydrolysis acidification and dynamic membrane bioreactor (DMBR) was developed for treating the wastewater produced from polymer flooding. Performance and mechanism of the combined system as well as its respective units were also evaluated. The combined system has shown high-capacity to remove all contaminants in the influent. In this work, the coagulant, polyacrylamide-dimethyldiallyammonium chloride-butylacrylate terpolymer (P(DMDAAC-AM-BA)), integrated with demulsifier (SD-46) could remove 91.8% of crude oil and 70.8% of COD. Hydrolysis acidification unit improved the biodegradability of the influent and the experimental results showed that the highest acidification efficiency in hydrolysis acidification reactor was 20.36% under hydraulic retention time of 7 h. The DMBR proceeded efficiently without serious blockage process of membrane fouling, and the concentration of ammonia nitrogen (NH₃-N), oil, chemical oxygen demand and biological oxygen demand in effluent were determined to be 3.4±2.1, 0.3±0.6, 89.7±21.3 and 13±4.7 mg/L.     

物化预处理-水解酸化-接触氧化法处理选矿废水

对某浮选厂浮选废水进行混凝沉淀+活性碳吸附预处理,然后进入生化系统,厌氧池、好氧池停留时间为10h.结果证明:进水COD为400～700mg/L,出水74～145 mg/L,去除率达75.8%以上,首次成功地将生物法应用到铅锌选矿废水的处理,若对该工艺进行适当调整,完全可以使出水达到排放或回用标准.