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《环境科学导刊》2021,(3)
以香精香料生产废水为实验对象,其COD浓度为58421mg/L,采用混凝沉淀-微电解-Fenton组合工艺对该废水进行预处理,研究废水pH、药剂投加量、反应时间等因素对废水COD去除的影响。结果表明:以5%FeCl_3为混凝剂,在p H=7,FeCl_3投加量为10mL/50mL,0.06%PAM投加量为0.25mL/50mL时,废水COD的去除率为20.1%;铁碳微电解-铁碳材料与废水比例为2∶1(w/v),pH为3~4,曝气反应时间150min时,COD的去除率为14.6%; p H为4~5,双氧水投加量0.4mL/100mL,Fenton反应5h时,去除率为36.6%。经过该组合工艺的处理,香精香料废水总COD去除率可达60%。 相似文献
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采用混凝-Fenton氧化联合处理玉米淀粉废水,确定最佳的混凝和氧化条件。试验结果表明:混凝一阶段中,确定PAC为最优混凝剂,最佳投加量为10 mL/L,PAC和助凝剂PAM投加量配比为2∶2,pH=7,温度为35℃时COD去除率最高;Fenton氧化阶段中,Fe2+/H2O2为2∶5时,COD去除率最高;在混凝二阶段中,PAC和PAM投加量均为70 mL/L时,COD去除效果最好。该处理方法有良好的处理效果,有效降低废水的COD、SS和色度,出水达到排放标准,最后产生的SS可以作为淀粉蛋白回收,为后续产品生产所利用,提高经济效益并具有设备简单、占地面积小、去除率高、操作方便、不产生二次污染物等优点。 相似文献
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为研究含盐有机废水的处理工艺和效率,文章以蔬菜腌制废水为处理对象,用沙滤过滤并富集废水中的悬浮物,用混凝法处理滤后富集液,采用正交实验设计,研究了混凝剂种类、混凝剂投加量、混凝条件对混凝处理效果的影响。研究发现沙滤预处理对其浊度去除率达到25%,对总磷的去除率达到29.25%;正交混凝实验发现,浊度和总磷的去除率最高达94.49%、95.76%,对于电导率的去除率最高只有18.91%,对硝氮的去除率最高只有11.49%,对COD有一定的去除效果,最高为19.56%。综上分析:混凝处理对不溶性成分处理效果较好,而对离子、可溶性物质等相关的指标处理效果较差;直观分析和方差分析发现不同因素对不同指标实验结果的主次影响和交互作用多样、多变,且交互作用对实验影响较大;优方案分析得出,当p H为10,投加24 mL浓度为10μg/L PAM处理此废水时,处理效果最佳。 相似文献
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本文详细介绍了在实验室条件下,采用混凝以及过氧化氢光催化法处理制药废水,研究分析了硫酸铁混凝体系以及过氧化氢光催化体系的最佳工艺参数.结果表明:在硫酸铁混凝降解制药废水的实验中,pH是影响混凝的主要因素,混凝剂的加入具有脱稳作用.PAM具有助凝作用.在混凝实验中降解废水的最佳工艺条件为pH值为7,10mg/L的硫酸铁投加量为0.6mL,1mg/L的PAM投加量为2mL,废水COD去除率可达到70%,SS去除率可达到90%.而经过氧化氢光催化处理混凝后的制药废水,最佳工艺条件为:光催化方式选定为曝气,反应温度控制在20℃~30℃间,1%的过氧化氢投加量为9mL,pH值为4,反应时间为3h,废水COD去除率可达到96%. 相似文献
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本文介绍了用碱式聚合氯化铝处理高浓度有机淀粉废水的效果。用实验室配制的CODw浓度为10000-15000mg/L的淀粉废水以不同用量的碱式聚合氯化铝为絮凝剂处理后,CODw去除率达到28%-47%,再经吸附柱吸附后,CODw去除率可达到65%。 相似文献
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Membrane bioreactor (MBR) used in water and waste water treatment is a developing technique for water pollution control and water reuse. This paper describes a membrane-bioreactor for treatment of waste water in a petrochemical complex. The experimental MBR was a lab scale one composed of an activated sludge bioreactor unit and an ultrafiltration membrane unit. The relationship of COD removal with MLSS and HRT in this MBR was studied. The effects of crossflow velocity, backwash interval and volume of flush liquid on the flux were discussed. The results showed that average removal of COD, oil, SS and turbidity in petrochemical waste water by the MBR was 91%, 86%, 92% and 99% respectively. The average removal of NH3-N and total phosphorous was 85% and 82%. A coefficient of COD removal, k, was 0.017-0.080 L/(mg.d). The membrane flux maintained higher than 60 L/hm2 bar for 34 days without chemical cleaning when the velocity of crossflow was 3.5-3.9 m/s and the backwash interval was 30 minutes and backwash duration at 20 seconds. The results indicated that it is feasible for MBR technology to be used in petrochemical waste water treatment. The treated water could be considered as a source used to make up water for industrial cooling system or to be reused for other purposes. 相似文献
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Membrane bioreactor (MBR) used in water and waste water treatment is a developing technique for water pollution control and water reuse. This paper describes a membrane-bioreactor for treatment of waste water in a petrochemical complex. The experimental MBR was a lab scale one composed of an activated sludge bioreactor unit and an ultrafiltration membrane unit. The relationship of COD removal with MLSS and HRT in this MBR was studied. The effects of crossflow velocity, backwash interval and volume of flush liquid on the flux were discussed. The results showed that average removal of COD, oil, SS and turbidity in petrochemical waste water by the MBR was 91%, 86%, 92% and 99% respectively. The average removal of NH3-N and total phosphorous was 85% and 82%. A coefficient of COD removal, k, was 0.017-0.080 L/(mg.d). The membrane flux maintained higher than 60 L/hm2 bar for 34 days without chemical cleaning when the velocity of crossflow was 3.5-3.9 m/s and the backwash interval was 30 minutes and backwash duration at 20 seconds. The results indicated that it is feasible for MBR technology to be used in petrochemical waste water treatment. The treated water could be considered as a source used to make up water for industrial cooling system or to be reused for other purposes. 相似文献
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以贵阳纺纱厂牛仔布生产车间废水处理工程为实例,介绍了“絮凝床-迷宫沉淀”技术对含靛兰染料、淀粉和PVC浆料的染整废水处理情况。经半年的工程实际运转表明,在进水污染物平均浓度:色度、SS、COD、BOD、NH3-N分别为400(稀释倍数)、97.0mg/L、821mg/L、189.51mg/L、1.8mg/L情况下,处理效果良好,其去除率分别为97.5%、97.4%、94.0%、90.0%、58.3%,出水达到了《纺织染整工业水污染物排放标准》(GB-4287-93)一级,符合环保要求,且可以回用于绿化、冲地坪等。该技术投资和运行费用合理,操作管理方便,适合中小型纺织印染厂废水处理。 相似文献
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采用混凝、氧化的方法对精研精抛清洗废液进行处理,对絮凝过程中所用的6种混凝剂的投加量pH值和氧化过程中的氧化试剂H2O2的投加量分别进行了筛选,同时简单地分析了反应机理.经混凝氧化处理后,COD值由1200mg/mL降至500mg/mL左右,COD去除率达95%;最后进行活性炭吸附,COD值达到国家排放标准. 相似文献
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本文提出了两个治理印染废水的综合物化流程:(1)SE—J型絮凝剂絮凝→气浮→次氯酸钙氧化→炉渣吸附;(2)SE—型絮凝剂絮凝→气浮→活性炭吸附,并对每个处理过程进行了条件实验。实验结果表明:废水经流程(1)处理后,COD去除率达82—87%,色度去除率达88—92%,废水经流程(2)处理后,COD去除率达89—92%,色度去除率达97—98%。经两个流程处理后的出水水质分别接近或达到国家排放标准。 相似文献
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以壳聚糖(CTS)为母体,3-氯-2-羟丙基三甲基氯化铵(CTA)为改性剂,合成了壳聚糖季铵盐阳离子型高分子絮凝剂2-羟丙基三甲基氯化铵壳聚糖(HTCC),以其对高岭土悬浊液的浊度去除率为指标优化合成条件,以HTCC分别与PAC及PAM复配,絮凝处理丁苯橡胶废水.结果表明,最佳合成条件为:质量比MCTS: MCTA: MNaOH =1:2:1.2、反应温度60℃、反应时间3h,在此条件下合成的HTCC对高岭土悬浊液的浊度去除率达96.46%;HTCC+PAC复配在pH6.0~8.0对丁苯橡胶废水的絮凝效果较好,出水余浊<2NTU,色度去除率达92.98%,COD去除率达32.0%;HTCC+PAM复配在pH5.0~8.9对丁苯橡胶废水的絮凝效果最好,余浊<3NTU,COD去除率46.0 %,且投药量小, pH适宜范围宽,优势比较明显.以HTCC与PAC、PAM分别复配处理丁苯橡胶废水可减轻后续生化处理的负荷,降低PAC、PAM的投加量,从而减小出水中残余铝和残余丙烯酰胺单体的含量. 相似文献