预处理／复合水解酸化／复合好氧氧化工艺处理综合制药废水

针对传统水解酸化和好氧氧化处理工艺存在的问题,对水解酸化工艺及好氧氧化处理工艺进行了改进;并针对东北制药集团制药废水水质特征,设计开发了预处理 复合水解酸化 复合好氧氧化的生物处理技术。工程设计规模为30000 m3/d,两年的运行结果表明,此工艺运行稳定,耐冲击负荷能力强。当平均进水浓度COD为3600 mg/L、BOD5为1000 mg/L、SS为450 mg/L时,平均出水浓度COD≤300mg/L、BOD5≤100 mg/L、SS≤50 mg/L,达到了国家城市排水三级标准医药企业污水排放标准(COD300mg/L)。     

EPP填料曝气生物滤池处理城市污水厂二级出水的中试研究

对韩国产EPP填料应用于曝气生物滤池（BAF）处理二级出水的效果及影响因素进行了研究,结果表明：利用该填料的BAF系统处理二级出水,CODCr,平均去除率为49．1％,BOD5平均去除率为51．4％,NH4^＋-N平均去除率为76％,SS平均去除率为52．6％。系统稳定运行后,出水水质达到了城市杂用水水质控制指标。改变水力负荷和气水比对CODCr、BOD5、NH3^-N的去除效率都有影响,但对SS去除率影响不大。     

解决污水快速渗滤土地处理系统占地突出的新方法

根据污水快速渗滤土地处理系统的主要特点和局限 ,针对该系统占地突出这一问题 ,提出了通过采用人工填料 ,提高水力负荷 ,加快污水在系统中的渗透速度 ,从而减小系统占地面积的新方法。对随水力负荷的提高使系统可能产生的出水水质变差、介质堵塞以及投资费用增高等问题进行了分析 ,并且对在涿州进行的现场小型工程的试验进行了验证。得出结论认为改进的人工构建快速渗滤系统切实可行。     

中空纤维膜作生物膜载体无泡供氧处理污水研究

采用中空纤维膜作生物膜载体及无泡供氧装置,利用具有死端式和漂浮式特点的浸没式接触氧化工艺进行污水处理试验研究.结果表明:在控制系统工作压力0.03 MPa、污水中ρ(DO)为5～8 mg/L及HRT＝8h的条件下,污水中COD、BOD、SS的去除率分别达70%、90%和75%以上,NH3 -N、P的去除率也在70%以上.系统连续运行3个月,表现了较好的稳定性和抗有机负荷冲击能力.     

人工快速渗滤系统处理农村生活污水实验研究

文章研究了不同渗滤介质组成的人工土柱对生活污水的处理能力,结果表明河砂＋斜发沸石＋方解石滤料对COD、NH3-N都有较高去除率,水力负荷也较高。将该组合用于农村生活污水处理工程,出水水质可以达到《城镇污水处理厂污染物排放标准》（GB18918-2002）一级A标准。     

多层渗滤介质处理微污染水体的中试研究

对传统的渗滤系统进行改进,采用多层渗滤介质系统,以期增大人工土层对颗粒有机物的接触氧化表面积,同时设置曝气装置保证好氧过程的氧气供应,可以大大提高污水地下处理系统的水力负荷。以北京典型的细砂、中砂、粗砂和砾石为填充材料,处理北京市海淀区上庄水库的污染水体,远优于类似的系统。现场试验结果表明,改进后的系统能创造良好的好氧/厌氧环境,对污染物去除效果良好,COD_Cr、TN、NH⁺₄-N和TP去除率分别达到了48.57%~94.87%、18.49%~70.21%、20.51%~87.50%和5692%~80.65%,出水达到了地表水Ⅲ-Ⅳ类水质标准。多层渗滤介质系统通过微生物的硝化、反硝化作用实现生物脱氮是去除氮的主要途径;土壤的吸附与沉淀作用是去除磷的主要途径。      

人工快渗污水处理系统水力负荷周期的设计

人工快渗(CRI系统)源自快速渗滤污水土地处理系统(RI系统),并沿用了其中的干湿交替工作方式,因此, 水力负荷周期同样也成为CRI系统的重要设计参数,也是系统设计的一大难点。目前CRI系统水力负荷周期的设计,不仅需要根据已有的经验,而且还要通过一段调试运行才能确定,设计过程中缺乏理论依据和设计原则。为此,笔者研究了CRI与RI系统两者之间的差异,充分考虑水力负荷周期调整对CRI系统运行的各方面影响,分别从防止NH4 N穿透和保证系统NH4 N充分硝化两个角度,提出了水力负荷周期中淹水时间和落干时间确定新方法,并通过松岗试验实例进行了初步验证,为今后CRI系统水力负荷周期的设计提供了有效的理论依据和设计原则。     

河道污染治理技术-- 生物接触氧化填料研究

选择不同填料对生物接触氧化法处理生活污水进行了进一步的研究与应用,探讨了温度、接触氧化停留时间等因素对其处理效果的影响。实验研究结果表明,在水温为18℃~20℃,水力负荷为70m l/m in时,采用鹅卵石和沸石的复合填料挂膜,进行生物接触氧化法处理生活污水,在降解NH3-N和氨氮等方面取得良好效果,COD、NH3-N去除率都高达80%以上。     

风成沙污染水处理系统去除BOD5的效果评价

利用风成沙净化污染水试验，结果表明，在水力负荷为1.0m/d、湿干周期比为12h:12h或48h:48h条件下，风成沙处理污染水系统对BOD5处理效果较好，出水ρ(BOD5)≤2mg/L，优于《地表水环境质量标准（GHZB1－1999）》Ⅰ类标准。影响处理效果的因素主要有湿干周期化、水力负荷和接种驯化方式等。     

上流式曝气生物滤池深度处理炼油厂外排污水

炼油厂外排污水水质复杂,可生化性已较差,但上流式曝气生物滤池对其有较好的处理效果.研究结果表明曝气生物滤池处理炼油厂外排污水在有机负荷(COD)为 4.39 kg·m-3·d-1、水力负荷为3 m3· m-2·h-1、气水比为31下,COD、NH3-N的去除率达到81.9%、73.2%;曝气生物滤池的主要影响因素依次是水力负荷、气水比、有机负荷;得到的经验速度方程与Monod方程基本吻合.该实验为炼油厂外排污水再生回用提供了一种工艺方法.     

Treatment of domestic wastewater using upflow anaerobic sludge blanket reactor

This paper presents the findings of the study on treatment of domestic wastewater using a laboratory scale Hybrid Upflow Anaerobic Sludge Blanket (HUASB) reactor. The reactor with a working volume of 5.9 L and plastic cut rings as packing media was operated at varying Hydraulic Retention Time (HRT) for a period of 110 days. While the COD removal varied from 75–86%, the BOD removal was in the range of 70–91%. Methane content in the biogas was 62±3%. VFA levels fluctuating between 100 and 186 mg/L (as acetate) did not pose operational problems such as souring of the reactor. During the treatment, nutrient levels exhibited an increasing trend. HUASB system could be designed with very short HRT of 3.3 hours, which will reduce the treatment cost significantly. It appears to be a promising alternative for the treatment of domestic wastewater in developing countries like India     

Modelling of moving bed biofilm reactor (MBBR) efficiency on hospital wastewater (HW) treatment: a comprehensive analysis on BOD and COD removal

Performance of moving bed biofilm reactor system for a real hospital wastewater (HW) was experimented, modelled, and optimized using response surface methodology. Prior to conducting laboratory tests, design of the experiments was evaluated to minimize any prediction error. Statistical analyses demonstrated the models’ validity and adequacy for anticipation of the removal of BOD and COD by the process. The models predictions (with desirability of 0.98) were found to be in very good agreement with confirmative experiments results. The results indicated that under convenient operating conditions of the studied variables (packing rate 70%, HRT 24 h, and MLSS 3000 mg/L), the removal efficiencies for BOD and COD were 97.8 and 95.6%, respectively. Moreover, kinetics of the biological process showed that removal of organic matters for the tested wastewater adheres to modified Stover–Kincannon model with a correlation coefficient of 0.998. Ratio of BOD to COD of 0.6 (optimal range for biological treatment normally is >0.5) suggests acceptable efficiency of the reactor for decomposing organic load. A high overall efficiency of the process and fulfilling the related standards make this system an appropriate option for treating HDW.     

组合生物技术处理制药废水及其生物相

为有效治理化学制药废水和生物制药废水,采用水解酸化-活性污泥[-曝气生物滤池组合工艺对制药废水进行室内模拟生物处理研究。结果表明：该工艺对出水COD、BOD₅的去除率均大于90%,已达到《污水综合排放标准》（GB 8978-1996）二级标准。对生物相的显微镜观察分析表明,污泥絮体和生物膜生长良好,并出现变形虫、轮虫和漫游虫等原生和后生动物。对各构筑物中的细菌进行分离纯化,同时应用BIOLOG细菌鉴定系统进行鉴定,分别得到8株、3株、6株可培养的细菌。     

三维电极法预处理山梨酸废水

用三维电极法对山梨酸废水进行了降解实验,并考察电极材料、反应器电压、电解时间、进水pH值等因素对处理效果的影响。实验结果表明,以不锈钢作阳极,石墨作阴极,柱状活性炭作填料,在槽电压为20 V、主电极极间距为11 cm的条件下,pH值为 4.0±0.2的山梨酸废水在电解20～30 min后,COD去除率达48%以上,而且废水的BOD/COD提高到0.40。     

利用天然矿物处理造纸黑液

实验使用未经处理的天然矿物处理草浆黑液 ,然后用其沉渣烧制陶瓷制品 ,形成一条与其他草浆黑液处理方法不同的思路。处理过程中 ,用硫酸溶液调节黑液的 pH值 ,再用天然矿物进行处理 ,处理效果最好的条件是 :pH =3,凹凸棒石粒度小于 6 0目 ,用量为 1g/ 10mL黑液 ,此时 ,COD值去除率约为 50 %。以处理废液后的天然矿物沉渣为主要原料 ,通过不同配方和不同工艺条件可烧制出合格的建筑陶瓷材料 ,这对小型浆厂具有一定的实用性 ,既处理草浆黑液 ,又利用天然矿物沉渣 ,不会造成二次污染。     

High rate anaerobic treatment of Sago wastewater using HUASB with PUF as carrier

Sago industry is one of the major small-scale sectors in India and over 800 units are located in the southern State of Tamilnadu. Processing of sago generates enormous quantities of high strength wastewater requiring systematic treatment prior to disposal. The present study is an attempt to treat the sago wastewater using Hybrid Upflow Anaerobic Sludge Blanket (HUASB) reactor, which offers the advantages of both fixed film and up flow anaerobic sludge blanket treatment. HUASB reactor with a volume of 5.6 L was operated at Organic Loading Rates varying from 10.7 to 24.7 kg COD/m³.day. After 130 days of startup, the reactor produced appreciable decrease in COD of wastewater and removed solids efficiently. The COD removal varied from 91–87%. While the removal of Total Solids was in the range of 61–57%, that of volatile solids varied from 70–67%. The ideal OLR for the reactor was 23.5 kg COD/m³.day. The findings of the study open up newer possibilities of design low cost and compact onsite treatment systems with very short retention periods.     

固定化生物技术在合成染料废水处理中的应用

在多级折流板反应器生物处理装置中,采用活性炭为载体人工固定化生物处理合成染料废水,出水水质稳定, 出水中的烷烃肽链变短;其对COD_Cr和BOD₅的去除率可达96.46%、99.77% ;对SO^2-₄和钙镁总量的去除效率超过80.37%、78.66%;折流板反应器的容积负荷率N_v可达2.8 kg COD/(d•m³)。活性炭经生物固定化后,不仅不会影响它的处理效果,还会延长活性炭的使用寿命;当冲击性有机负荷发生时,固定化生物活性炭能够承受并能很快恢复。     

Determination of design criteria for UASB reactors as a wastewater pretreatment system in tropical small communities

A pilot scale study was set up to investigate the principle design parameters of up flow anaerobic sludge blanket (UASB) reactors for treating wastewater of small communities in the tropical regions of Iran. A steel pipe with a diameter of 600 mm and a height of 3.6 m was used as the reactor in which a digestion and a 3-phase separator element had a volume of 0.848 and 0.17 m³ respectively. During this study, which lasted for 203 days, two distinct phases were carried out according to the ambient temperature. The temperature of the wastewater entering the reactor was naturally ranged from 22 to 26 °C and no heat exchanger was used. The hydraulic retention times including 2, 4, 6, 8, and 10 hours with various loading rates of 0.95 to 5.70 kg COD/m³/day for colder period and from 1.35 to 6.40 kg COD/m³/day for warmer period were examined. On the basis of the results the optimal hydraulic retention time for warmer period with a 2.20 kg COD/m³/day organic loading rate was 6 hours which BOD5, COD and TSS removal efficiency were 71, 63 and 65 percent respectively. During the colder period the removal ratio of BOD5, COD and TSS with an optimal hydraulic retention time of 8 hours and organic loading rate of 1.22 kg COD/m³/day were 54, 46 and 53 percent respectively.     

吗啉废水的生化处理工艺

以含有吗啉、甲基吗啉的高浓度有机废水为研究对象,提出了曝气吹脱-吸附-生物处理的联合工艺,并在室内进行了小试实验。结果表明：原废水经过2次曝气吹脱后,ρ(NH₃-N)从62 500 mg/L降为431 mg/L,ρ(COD)从50 840 mg/L降为26 051 mg/L。通过吸附实验,ρ(COD)从26 051 mg/L降为2 769 mg/L,ρ(NH₃-N)从412 mg/L降为134 mg/L。在生物处理室内小试实验中,采用了活性污泥反应器与曝气生物滤池相结合的处理工艺。在活性污泥反应系统中,当废水pH为7.5、ρ(DO)为4.3 mg/L、水力停留时间为30 h时,COD的去除率最高,可以达到83.1%。在曝气生物滤池中,当ρ(DO)为3.3 mg/L时,COD去除率最高,达到55.8%。在生物处理的最佳参数条件下进行连续监测,当进水ρ(COD)为2 769 mg/L、出水ρ(COD)平均值为387 mg/L时,COD去除率可达到85.9%。吗啉废水经过此联合工艺的处理,ρ(COD)从50 840 mg/L降为387 mg/L。