开心果加工废水处理技术研究

研究采用混凝-CASS法处理开心果加工废水。试验结果表明,混凝处理中混凝剂PAC的处理效果优于PFS,其最佳pH范围为7～10,最佳投药量为175mg/L。以PAC为混凝剂处理后的废水采用CASS法进行生化处理,在曝气12h的条件下,CODCr和BOD5去除率分别为94．4%和96．1％,最终出水达到污水综合排放标准的一级标准。     

环境敏感地区纺织染整工业锑污染物排放限值探究

在对纺织染整企业集聚、环境位置敏感的两个典型区域调研的基础上,通过类似重金属标准和毒性类比、排污治理情况及水体底泥中锑含量的分析、水环境承载力和允许排放浓度计算等技术论证,提出环境敏感地区纺织染整工业锑的排放限值按不同排放情形可分别设定为0.1 mg/L和0.05 mg/L。工程实例表明,采用基于聚合硫酸铁混凝沉淀法的高低浓度废水分质处理技术可满足排放限值要求,且经济成本可接受。     

含硫废水预处理方案的经济技术性研究

从技术经济角度对空气催化氧化法和铁盐沉淀法处理含硫废水进行了研究，建立了总投资费用的NPV与废水流量及硫化物浓度的关系．结果表明；不回收FeS沉淀时，空气催化氧化法费用较低；回收FeS沉淀时，铁盐沉淀法费用较低，且存在一个盈亏平衡点，该点浓度约为700mg／L，高于此浓度时，铁盐沉淀法为盈利工艺。     

制药废水净化处理探讨

对甘肃兰药药业集团有限责任公司制药废水经高效混凝气浮处理、一氧池、二氧池、生物处理等工序处理后，废水达到或优于国家规定排放标准，对制药企业废水处理具有指导作用。     

焦化废水生化处理过程中溶解性有机物及毒性变化规律

焦化废水中的溶解性有机物(DOM)作为废水污染物和毒性的主要来源受到广泛关注。厌氧-缺氧-好氧(A-A-O)生物法联合混凝沉淀工艺在焦化废水处理中被广泛应用。于2018年4,7和11月分别采集4座焦化废水处理厂废水,采用光谱学分析手段和水生生物急性毒性试验对A-A-O联合混凝沉淀处理过程中焦化废水的DOM和毒性变化进行分析。结果表明,焦化废水中含有大量不饱和芳香性物质,其中类色氨酸、络氨酸物质占主导,其次为类溶解性微生物代谢产物、类富里酸物质和类腐殖酸类物质;未经处理的焦化废水对藻类和大型溞的急性毒性等级为中毒至高毒。A-A-O联合混凝沉淀处理可去除90%以上的类色氨酸、络氨酸和类富里酸物质,但对类腐殖酸类物质去除率相对较低,仅为约80%,关键去除段为缺氧段和好氧段;该工艺对焦化废水急性毒性削减率为80.51%~94.30%,关键削减段为厌氧段。Pearson相关性分析结果显示,焦化废水溶解性总有机碳(TOC)、类腐殖酸类物质荧光组分C1和类富里酸类物质荧光组分C4与废水急性毒性存在显著正相关关系,可利用其作为水样急性毒性初筛的指示性指标。可为焦化废水生化处理的效能优化和废水毒性控制及安全评估提供科学支撑。     

混凝法深度处理焦化废水的实验研究

文章以经A2/O生化法处理后的焦化废水为研究对象,采用混凝-Fenton法对其进行深度处理。确定了聚合硫酸铁等铁盐处理焦化废水的最佳投药量和pH值,讨论了影响其混凝效果的主要因素。处理后出水的COD去除率达40%以上。混凝剂处理焦化生化外排水中的难降解有机物,COD去除率只有40%左右,经过Fenton试剂氧化后,去除率可以达到70%左右,外排水能够达到国家排放标准。     

混凝脱色-CASS技术处理绒线印染废水工程应用

用混凝脱色-CASS技术处理绒线印染废水，有效地解决了废水的脱色和COD的去除问题，处理后的水质达到了纺织染整工业污水排放标准，该技术的应用，取得了较好的环境、社会和经济效益。     

水解酸化+CASS工艺处理半夏泡制废水工程应用

采用水解酸化+CASS工艺处理半夏泡制废水,工程运行结果表明,在进水COD、NH3-N、SS的质量浓度分别为1800～2200mg/L、60～80mg/L、500～800mg/L时,经该工艺处理后,废水中的COD、NH3-N和SS总去除率可分别达到97.7%、96.3%和95%以上,出水达到《污水综合排放标准》(GB8978-1996)表4一级标准限值。该工艺运行稳定、处理效果好,运行费用低。     

流动注射二乙氨基二硫代甲酸钠光度法测定废水中铜

采用流动注射二乙氨基二硫代甲酸钠分光光度法测定废水中的铜，优化了试验条件，讨论了干扰离子的影响。方法在0mg／L-10.0mg／L范围内线性良好，检出限为0.07mg／L，水样测定的RSD≤0.8％，加标回收率为98.5％-101％，标准样品的测定结果符合要求。     

氰化钾标准中间液保存时间试验

在《水和废水监测分析方法》（第四版）异烟酸-吡唑啉酮光度法测定总氰化物中，需将10mg／L氰化钾标准中间液在临用前再稀释10倍，配成1．0mg／L标准使用液。该方法没有对氰化钾标准中间液保存时间作明确要求，为保证分析结果的准确性，也为提高工作效率，对氰化钾标准中间液在2℃-4℃时的保存时间作试验，测定结果见表1。     

投菌水解（酸化）—生物接触氧化—混凝法处理酵母生产废水

研究了采用投菌水解（酸化）－生物接触氧化－浊凝化处理酵母生产废水。试验结果表明，进水浓度控制在ＣＯＤＣｒ值５０００ｍｇ／Ｌ左右，生化系统可取得较高的处理效率；生经处理出水再以碱式 化铝为混凝剂，聚丙烯酰胺为助凝剂进行混凝处理，其出水ＣＯＤＣｒ值可控制在２００ｍｇ／Ｌ以下，并且可部分回流使用。     

微电解-SBR组合工艺处理医药化工废水研究

医药化工废水作为一种高浓度、难降解有机废水,其预处理效果直接影响到最终出水水质.以硝基苯类废水为处理对象,采用先进微电解-SBR组合工艺技术进行处理试验.结果表明,经微电解处理医药废水硝基苯类、COD的去除率分别为93%和45%左右.废水的可生化性由约0.24提高到0.55.每吨废水处理成本为2.52元.     

Wastewater quality of natural gas fertilizer factory, Fenchuganj and water quality of Kushiara River at the down stream

The physical, chemical and biological characteristics of the wastewater of Natural Gas Fertilizer Factory Ltd. Fenchuganj, Sylhet were determined through extensive laboratory tests in the months of March, July, October and December of the year 2005. Concentration of Suspended Solids was within the range of 445 to 950 mg/L. Bangladesh Industrial Effluent Standards for Suspended Solids is 100 mg/L. Suspended Solids were found above the limit in all the samples. Concentration of Dissolved Solids was found to vary from 576 to 1,456 mg/L. Bangladesh Industrial Effluent Standards, for Dissolved Solids is 2,100 mg/L. Dissolved Solids were found within the limit. Concentration of BOD(5) was found to vary from 4.5 to 8.4 mg/L. Bangladesh Industrial Effluent Standards for BOD(5) is 50 mg/L. For the year 2005, the BOD(5) was found below the limit in all the samples. Dissolved Oxygen of the wastewater was found to be between 2.0 to 3.0 mg/L, which do not satisfy the standard (4.5-8 mg/L). Oil and grease concentration were found in the range of 28 to 68 mg/L, whereas the standard is 10 mg/L for discharge into the inland surface water. In 2005, concentration of Cr(+ 6) was found to vary from 0.01 to 0.156 mg/L in the wastewater. Bangladesh Industrial Effluent Standards, for Cr(+6) is 0.1 mg/L. The concentration of chromium was found above the limit in three samples. Concentration of NO(3) was found to vary from 4.5 to 15.2 mg/L in the wastewater. Bangladesh Industrial Effluent Standards for nitrate is 10 mg/L. The nitrate was found above the limit in three samples. Maximum concentration of ammonia in lagoon 1 was found 1,710 mg/L in month of December. Bangladesh Industrial Effluent Standards for ammonia nitrogen is 100 mg/L. For the year 2005, the ammonia nitrogen was found above the limit in all samples.     

Evaluation of Water Quality Management Alternatives to Control Dissolved Oxygen and Un-ionized Ammonia for Ravi River in Pakistan

Different water quality management alternatives, including conventional wastewater treatment, transportation of wastewater, flow augmentation, low-cost treatment with reuse, and wetlands, are evaluated by using a verified dissolved oxygen (DO) model for the Ravi River. Biokinetic rate coefficients of the Ravi River for both the carbonaceous and nitrogenous oxygen-demanding wastes are adjusted, keeping in view the type and level of wastewater treatment. The conventional activated sludge process with nitrification comes out to be the most expansive alternative to meet the DO standard of 4 mg/L. Additional treatment cost is required to maintain un-ionized ammonia levels <0.02 mg/L, which corresponds to achieving treatment levels of 5 mg/L of DO in the river. Under critical low-flow conditions (i.e., minimum average seven consecutive days) of 9.2 m³/s, a flow augmentation of 10 m³/s can reduce 30 % of the cost with conventional wastewater treatment. Transportation of wastewater from the city of Lahore is a cost-effective alternative with 2.5 times less cost than the conventional process. Waste stabilization ponds (WSP) technology is a low-cost solution with 3.5 times less cost as compared to the conventional process. Further reduction in pollution loads to the Ravi River can be achieved by reusing WSP effluents for irrigation in the near proximity of Lahore along the Ravi River. The study results show that, for highly polluted rivers with such extreme flow variations as in case of the Ravi River, meeting un-ionized ammonia standards can reduce the efforts required to develop carbonaceous biochemical oxygen demand-based waste load allocations.     

生物生态耦合技术处理农村生活污水的应用研究

在对“厌氧池+跌水充氧接触氧化池+水耕蔬菜型人工湿地”生物生态耦合技术应用于农村生活污水处理进行实证研究的基础上，进一步探讨了生物与生态处理单元各自的主要去除对象和效率，为生物生态技术的合理耦合提供了依据。结果表明：在进水COD、TN、TP质量浓度波动范围为51.20~211.12，28.29~122.12，1.26~5.97mg/L时，出水平均质量浓度为15.80，5.51，0.34mg/L，出水水质达到《城镇污水处理厂污染物排放标准（GB 18918—2002）》一级A标准。污水中COD、TN、TP的78%，85%，50%的去除是在生物处理单元完成的，而TP的达标排放还必需生态处理单元的参与。整个处理技术处理效果良好，运行费用低，适合在条件允许的农村地区推广使用。     

假丝酵母菌对高浓度苯酚的降解效果及SDS对其生长影响

从含酚废水处理池污泥中驯化得到苯酚降解菌——假丝酵母菌FD-1,通过试验考察FD-1对高浓度苯酚废水的降解效果,以及十二烷基磺酸钠(SDS)对高浓度苯酚废水中FD-1菌株生长的影响。试验表明,假丝酵母菌FD-1对苯酚的最大降解质量浓度为1 500 mg/L,降解时间为30 h。当苯酚质量浓度不超过1 000 mg/L时,添加适量的SDS可以显著提高苯酚降解速率,进而缩短苯酚降解时间,SDS的最佳投加量为100 mg/L,超过150 mg/L时FD-1生长受到抑制。     

液相色谱-串联质谱法同时测定污水中10种精神活性物质

建立了采用液相色谱-串联质谱法(LC-MS/MS)同时测定污水中10种精神活性物质的分析方法。污水样品经甲酸与甲酸铵调节pH后,加入氘代内标混匀,离心并过滤膜后可直接上样分析。研究表明,在1~250 ng/L的线性范围内,10种精神活性物质的线性相关系数均大于0.992,定量限均低于0.5 ng/L。在3个加标水平下,10种精神活性物质的加标回收率为87.2%~114%,相对标准偏差为0.53%~3.60%(n=3)。将该方法应用于某区域10份生活污水样品的检测,在3份水样中检出吗啡、甲基苯丙胺、氯胺酮等精神活性物质,对应的质量浓度范围分别为3.41~9.55、0.90~1.63、1.06~1.78 ng/L。与经固相萃取前处理后的分析方法相比,该方法可在10 min内完成分离和检测的全过程,具有简单、快速、节约的优点,可用于污水样品中10种痕量水平精神活性物质的定量分析。     

变色酸比色法测定甲胺生产废水中甲醇

建立了变色酸比色测定甲胺生产废水中甲醇的方法，确定了最大吸收波长，优化了试验条件。方法在0mg／L-7．00mg／L范围内线性良好，检出限为0．07mg／L，标准溶液测定的RSD≤0．9％，废水样品的加标回收率为98．8％-101％。     

气相分子吸收光谱法测定印染废水中氨氮的影响因素

采用气相分子吸收法光谱测定印染废水中的氨氮,并对相关影响因素进行探讨。结果证实,硫化物和尿素会对氨氮的测定产生负干扰,硫化物干扰可用乙酸锌-乙酸钠固定液沉淀法去除,尿素干扰可以用稀释法去除,但仅适用于氨氮质量浓度0.10 mg/L且稀释后尿素质量浓度≤100 mg/L的水样;苯胺、浊度和色度对测定无干扰,可直接检测。     

Assessment of current status of zinc in wastewater treatment plants to set effluent standards for protecting aquatic organisms in Japan

New environmental standards for protecting aquatic organisms for zinc (e.g., 0.03 mg/L) in surface waters were set in Japan in 2003. Although wastewater effluent might be one of the major pathways of zinc to public water bodies in Japan, current status of concentration of zinc in wastewater effluent was not clear due to higher detection limits (e.g., 0.5 mg/L) than the level required by the new regulations. This study aims at assessing current status of zinc in wastewater effluent in Japan to revise wastewater effluent standards for protecting aquatic organisms. Survey of zinc in wastewater treatment plants (WWTPs) was carried out in Japan in 2005, setting the detection limits at least 0.01 mg/L. The results of the survey suggested the difficulty to remove zinc (especially dissolved zinc) with conventional activated sludge treatment if concentration of zinc in influent was relatively low. And it was suggested that high concentration of dissolved zinc might be derived from some industries discharging high concentration of zinc. The concentration of zinc in wastewater influent without industrial discharges was about 0.1 mg/L which might be lower than that in wastewater from industries discharging high concentration of zinc. Finally, effluent standards for point sources including WWTPs to public water bodies were set at 2 mg/L in 2006. Based on the results of the survey that it was difficult to remove dissolved zinc discharged from industries at WWTPs, the effluent standards from industries to sewerage were set at the same value of the effluent standards from WWTPs to public water bodies.