厌氧膜生物反应器对乳品废水处理效果的研究

采用厌氧膜生物反应器(AnMBR)对乳品废水进行处理,装置连续运行100d,研究了不同进水COD_(Cr)浓度(3 000、5 000、7 000、9 000 mg/L)对出水水质及反应器内污泥特性的影响,并与常规厌氧生物反应器的处理效果进行对比。结果表明,温度为35℃,HRT为48h时,COD_(Cr)去除率和氨化率随着进水COD_(Cr)浓度的降低而升高,最高可达89%和38%以上。TN去除率随着进水COD_(Cr)浓度的增加先增高后降低,在7 000 mg/L条件下,去除率为55%。装置在运行过程中,MLVSS/MLSS平均值约为0. 7,SVI值在60～80 m L/g的范围内,污泥具有良好的活性与沉降性。AnMBR与常规厌氧生物反应器相比,在处理高浓度乳品废水时运行更加稳定,耐冲击负荷能力更强,出水水质更好。     

柠檬酸废水处理改造工程实例

采用多级内循环厌氧反应器MIC/上升式厌氧反应器UASB串联工艺处理柠檬酸生产排放的高浓度有机废水,其中厌氧处理段的COD去除率＞94％,整体COD去除率可达98.3％左右.最终排放口出水COD平均值为190 mg/L,pH值为6～9,达到柠檬酸行业废水排放标准.     

海上溢油回收技术研究及发展

论述了厌氧-好氧(A/O)工艺的基本原理及工艺参数。该工艺在冀东油田两座废水处理站的应用结果表明,对废水中石油类物质、COD、硫化物去除效果明显。高一联合站及柳一联合站污水经处理后,石油类物质去除率分别为90.6%和96.0%;COD去除率分别为86.0%和91.6%;硫化物去除率分别为94.8%和98.2%,处理后的污水均达到一级排放标准。另外,采用厌氧-好氧工艺的成本相对较低,处理费用低于0.5元/m3。处理后的污水若回注地下,平均费用为4.7元/m3。     

厌氧-好氧工艺在含油废水生化处理中的应用

(中国石油冀东油田分公司安全环保处)论述了厌氧-好氧(A/O)工艺的基本原理及工艺参数。该工艺在冀东油田两座废水处理站的应用结果表明,对废水中石油类物质、COD、硫化物去除效果明显。高一联合站及柳一联合站污水经处理后,石油类物质去除率分别为90.6%和96.0%;COD去除率分别为86.0%和91.6%;硫化物去除率分别为94.8%和98.2%,处理后的污水均达到一级排放标准。另外,采用厌氧-好氧工艺的成本相对较低,处理费用低于0.5元/m3。处理后的污水若回注地下,平均费用为4.7元/m3。     

海上溢油回收技术研究

论述了厌氧-好氧(A/O)工艺的基本原理及工艺参数。该工艺在冀东油田两座废水处理站的应用结果表明,对废水中石油类物质、COD、硫化物去除效果明显。高一联合站及柳一联合站污水经处理后,石油类物质去除率分别为90.6%和96.0%;COD去除率分别为86.0%和91.6%;硫化物去除率分别为94.8%和98.2%,处理后的污水均达到一级排放标准。另外,采用厌氧-好氧工艺的成本相对较低,处理费用低于0.5元/m3。处理后的污水若回注地下,平均费用为4.7元/m3。     

垃圾场渗出污水厌氧处理的可行性研究

采用血清瓶静态试验法研究了垃圾渗出污水的厌氧处理的可行性。试验表明:垃圾渗出污水对厌氧发酵微生物无抑制作用,有良好的厌氧降解性,产气率为0.321/g·COD,污水中的大部份有机物都能被厌氧消化,COD_cr去除率为78.2%,发酵过程中还能获得能源——沼气。具有良好的应用前景。     

无动力厌氧＋人工湿地组合模式处理农村生活污水效果分析

通过对已建污水处理工程无动力厌氧＋人工湿地组合模式的处理效果进行监测,结果表明：正常运行情况下,该处理模式化学需氧量的去除率在28％～90％之间,平均为66％;氨氮的去除率在7％-66％之间,平均34％;总磷的去除率在5％～84％之间,平均42％;90％以上出水水质达到三级排放标准;厌氧池对污染物去除的贡献率基本与后段的人工湿地持平;入水污染物负荷量与去除率呈显著正相关关系。     

使用厌氧混合消化反应器处理石化废水

本文介绍一种采用厌氧混合消化反应器对酸性石化废水进行厌氧处理的方法。该法在HRT(水力停留时间,以下类同)为17小时、有机负荷率为20.04(公斤.化学耗氧量/立方米.天的条件下,可获得挥发性有机酸去除率为91％,化学耗氧量去除率为84％。反应器最终出水含氨氮为44毫克/升、含磷酸盐12.3毫克/升。     

VFA对餐厨垃圾两相厌氧发酵处理效率的影响

为探究两相厌氧系统中挥发性脂肪酸（Volatile Fatty Acid,VFA）与pH、总化学需氧量（Total Chemical Oxygen Demand,TCOD）去除率、总碱度等指标的关系,确定最适宜的VFA浓度范围,以稳定运行一年以上的餐厨垃圾两相中温厌氧发酵处理系统各阶段浆料为主要研究对象,通过使用SPSS进行数据分析,VFA对系统pH变化、COD去除率、TAL变化有显著影响。     

石灰法制浆黑液厌氧发酵技术的研究—厌氧发酵动态模型实验

本文介绍了应用上流式厌氧污泥床反应器处理半化学浆石灰法制浆黑液的研究.所采用的反应器容积为21升,当进水COD负荷荷为1.6克/升·天至7.0克/升·天时,处理后、COD去除率为70—74.5％(BOD去除率为80～88％).其沼气产气率0.4～0.7升/克COD(0.6～0.7升/克BOD),甲烷含量60～65％,滞留期1.5～1.6天.经过较长时间的稳定运行,厌氧活性污泥达到颗粒化程度,结果证明实验是成功的. 本实验为治理同类型制浆黑液的污染提供了一种有效的方法.并且是一种可获取能源的低能耗的实用性技术.     

中温厌氧消化垃圾焚烧发电厂渗滤液的试验研究

采用逐渐提高有机负荷的半连续进料方式,研究中温(35℃左右)条件下,猪粪为接种物,厌氧消化焚烧发电厂垃圾渗滤液的消化规律。试验以5%为单位,由5%体积负荷渗滤液起开始填料,逐步提高至35%的体积负荷。试验进行的7个负荷,消化系统pH值稳定在7.2~7.8之间,碱度、氨氮浓度较高,分别在7803~17948 mg/L、673~1630 mg/L之间,为系统提供了良好的酸碱缓冲环境。低负荷时,VFA值较低,生物气中甲烷含量稳定在60%左右;高负荷时,随着渗滤液的加入,VFA值波动较大,甲烷含量也随VFA值的变化起伏波动(25%负荷时,甲烷含量出现峰值,高达75.5%)。消化系统共进料2800 mL渗滤液(即197.3 gCODCr),累计产气量83086 mL,平均每gCODCr产沼气约421.1 mL(平均gCODcr产甲烷约273.7 mL)。进水渗滤液CODCr浓度为70472 mg/L,实验结束时,消化液CODCr浓度降至3373 mg/L,CODCr去除率高达95.2%。     

IABR-IBAF工艺处理猪场稳定塘废水的实验研究

难降解有机物含量高且碳氮比失调是造成养猪场稳定塘废水难于处理的主要原因。本文采用基于固定化微生物技术的厌氧折流板（IABR）与曝气生物滤池（IBAF）组合工艺处理稳定塘废水,对比了IABR-IABF组合工艺与单一IBAF工艺的处理效果,研究了碱度和碳源对硝化反硝化过程的影响。组合工艺平均进水COD1532．6mg／L,平均出水为332．7mg／L,去除率为78％,NH3-N平均进水538．6mg／L,平均出水为12．3mg／L,去除率97．7％。以新鲜废水做反硝化阶段的碳源时TN去除率93％,可有效解决脱氮过程中的碳源成本问题。     

Biogas production from slaughterhouse wastewaters and use of biofertilizer obtained for biodegradation of aromatic hydrocarbons

The anaerobic digestion of industrial wastes produces a biogas that is an alternative to the use of fossil fuels for energy production. At the end of this process, the stabilized biomass presents high levels of nutrients, which can be used both as biofertilizers in agriculture and for the biodegradation of contaminants in the soil through improvement of the microbiota. Thus, this study aimed to evaluate biogas production by industrial wastes and to use the biofertilizer for the bioremediation of soils previously contaminated with gasoline. The biomass (420 mL) generated approximately 10 liters (L) of methane and 3 L of other gases. Anaerobic incubation reduced total and volatile solids, as well as biochemical oxygen demand, chemical oxygen demand, and the carbon and nitrogen contents of the biomass. The bioremediation experiment showed that 15 days after contamination with gasoline, the addition of the biofertilizer improved the degradation efficiency of monoaromatic hydrocarbons; however, the degradation of polyaromatic hydrocarbons was less time efficient. So, we conclude that the anaerobic incubation of industrial wastes generates a high amount of biogas, and that biofertilizer deposition into contaminated soil does not affect the efficiency of the degradation of aromatic hydrocarbons after 30 days. Novelty or significance : Anaerobic incubation of industrial wastes generates a high calorific value gas, which can be used as an alternative source of energy. And, the resulting biomass, called biofertilizer, can be used to remediate soils contaminated with hydrocarbons.     

高浓度焦化废水低温厌氧初探

本文探讨了温度变化对高浓度焦化废水厌氧分解的影响。当温度较低时(9.2℃～11.2℃),低温耐冷菌驯化污泥较常温污泥COD_(Cr)日降解率(Da)高出2～3倍。因此,当温度下降至低温时,可通过增补耐冷菌来提高系统的降解效率。     

三步法处理大港油田12井综合废水的实验研究

根据大港油田12井综合废水的污染特征,提出了"混凝-内电解-H2O2氧化"三步处理的方法。实验结果表明:三步法处理后可以使原水的CODcr从4930mg/L降低到128mg/L,去除率达到97%。处理后水质达到国家《污水综合排放标准》(GB8978-1996)二级标准要求。     

偶氮染料的厌氧——好氧生物降解过程和影响因素

偶氮染料是总量最大、种类最多的合成染料,其降解处理通常采用厌氧-好氧技术。厌氧过程可实现偶氮染料的还原,好氧过程则完成还原产物芳香胺的去除。厌氧过程受偶氮染料结构和浓度、底物的种类和浓度、其他电子受体、氧化还原介体、温度和DO等环境因素以及水力停留时间的影响。好氧条件下芳香胺的降解过程受其自身的结构、浓度、外加碳源以及降解体系等影响,且自氧化过程影响了芳香胺的生物降解。在实际废水处理中应创造良好的条件提高偶氮染料的厌氧一好氧生物降解效率。     

混凝强化COD_Cr减排方案的研究

通过M—BFA、PAFS和PFS三种混凝剂对出水浊度、CODcr和TP的去除效果的研究,分析了混凝强化降低上海市某污水处理厂出水CODcr的效果,给出了混凝强化CODcr减排方案。实验结果表明,采用M—BFA和PAM组合强化混凝,可控制CODcr浓度在120mg／L以内。     

Microbially mediated aerobic and anaerobic degradation of acrylamide in a western United States irrigation canal

Acrylamide (AMD), a neurotoxin and suspected carcinogen, is present at concentrations of up to 0.05% in linear anionic polyacrylamide, which is under evaluation as a temporary sealant in unlined irrigation canal systems across the United States. We examined the microbially mediated degradation of AMD and diversity of AMD-degrading microbial physiotypes in the Rocky Ford Highline Canal, Colorado to better constrain the potential fate ofAMD in a canal environment. Microorganisms able to use AMD (500 mg L(-1)) as a sole nitrogen source were relatively abundant (2.3 x 10(3) to 9.4 x 10(3) cells mL(-1) in water and 4.2 x 10(3) to 2.3 x 10(5) cells g(-1) in sediment). Only sediment samples contained microorganisms able to use AMD as a sole carbon source. Acrylamide (up to 100 mg L(-1)) was efficiently removed from amended canal water and sediment slurries under aerobic conditions, but no AMD degradation was observed in abiotic controls. Anaerobic degradation of AMD by nitrate-, sulfate-, and iron-reducing microorganisms was also tested, with nitrate reducers affecting the highest amounts of AMD removal (70.3-85%) after 60 d. All representatives (n=15) from a collection of 256 AMD-degrading microbial isolates from Rocky Ford Highline Canal were closely related to well characterized environmental bacteria capable of facultative nitrate respiration. Our results demonstrate that natural microbial populations within this canal are capable of AMD degradation under aerobic and anaerobic conditions and that this degradation is performed by naturally abundant bacteria likely to be present in other freshwater irrigation canals or similar lotic habitats.     

Relationships between anaerobic consortia and removal efficiencies in an UASB reactor degrading 2,4 dichlorophenol (DCP)

To gain more insight into the interactions between anaerobic bacteria and reactor performances (chemical oxygen demand-COD, 2,4 dichlorophenol-2,4 DCP removals, volatile fatty acid-VFA, and methane gas productions) and how they depended on operational conditions the microbial variations in the anaerobic granular sludge from an upflow anaerobic sludge blanket (UASB) reactor treating 2,4 DCP was studied. The study was composed of two parts. In the first part, the numbers of methanogens and acedogens in the anaerobic granular sludge were counted at different COD removal efficiencies. The relationships between the numbers of methanogens, the methane gas production and VFA production were investigated. The COD removal efficiencies increased to 74% from 30% while the number of total acedogens decreased to 10 from 30 cfu ml(-1). The number of total methanogens and acedogens varied between 11 x 10(3) and 10 x 10(9)MPN g(-1) and 10 and 30 cfu ml(-1) as the 2,4 DCP removal efficiencies were obtained between 60% and 99%, respectively. It was seen that, as the number of total acedogens decreased, the COD removal efficiencies increased. However, the number of total methanogens increased as the COD removal efficiencies increased. Correlations between the bacterial number and with the removal efficiencies obtained in different operational conditions were investigated. From the results presented in this paper a high correlation between the number of bacteria, COD removals, methane gas percentage, 2,4 DCP removals and VFA was observed. In the second part, methanogen bacteria in the anaerobic granular sludge were identified. Microbial observations and biochemical tests were applied to identify the anaerobic microorganisms from the anaerobic granular sludge. In the reactor treating 2,4 DCP, Methanobacterium bryantii, Methanobacterium formicicum, Methanobrevibacter smithii, Methanococcus voltae, Methanosarcina mazei, Methanosarcina acetivorans, Methanogenium bourgense and Methanospirillum hungatei were identified.