污泥灰对模拟染料废水的吸附研究

以南京市江心洲污水处理厂污泥为原料热解制得污泥灰,并将其用于吸附直接耐酸大红4BS和活性艳红K-2BP模拟染料废水.考察了吸附剂投加量、吸附时间、温度和pH值对吸附效果的影响,并对其吸附动力学特征进行了探讨.结果表明,反应温度、吸附时间和吸附剂投加量对吸附效果有影响,而废水pH变化则不会引起脱色率的较大改变.室温下,4BS和K-2BP的最佳污泥投加量分别为3g·L-1、10g·L-1.4BS在最佳反应条件（反应时间为25min,反应温度为40℃）下,脱色率可达93%;K-2BP在最佳反应条件（反应时间为150min,反应温度为40℃）下,脱色率约为73%.     

镧掺杂氧化锌光催化降解染料废水研究

以醋酸锌和硝酸镧为原料,丙烯酰胺为单体,N,N’-亚甲基双丙烯酰胺为网络剂,过硫酸铵为引发剂,采用高分子网络凝胶法制备得到掺镧的Zn O纳米粉体。用制备的粉体对甲基橙进行光催化降解实验,考察了掺镧量对其光催化性能的影响。用X射线衍射仪、高分辨率透射电镜、X射线能谱仪、比表面积与孔隙率分析仪等对其进行表征。结果表明,镧的掺入提高了Zn O的光催化活性,镧锌摩尔质量比为0.2%时光催化性能最好,高压汞灯下反应1 h,甲基橙的脱色率为96.5%,相比于未掺杂的Zn O提高了11.5%。     

Efficient treatment of azo dye containing wastewater in a hybrid acidogenic bioreactor stimulated by biocatalyzed electrolysis

In this study, a novel scaled-up hybrid acidogenic bioreactor(HAB) was designed and adopted to evaluate the performance of azo dye(acid red G, ARG) containing wastewater treatment. Principally, HAB is an acidogenic bioreactor coupled with a biocatalyzed electrolysis module. The effects of hydraulic retention time(HRT) and ARG loading rate on the performance of HAB were investigated. In addition, the influent was switched from synthetic wastewater to domestic wastewater to examine the key parameters for the application of HAB. The results showed that the introduction of the biocatalyzed electrolysis module could enhance anoxic decolorization and COD(chemical oxygen demand) removal. The combined process of HAB-CASS presented superior performance compared to a control system without biocatalyzed electrolysis(AB-CASS). When the influent was switched to domestic wastewater, with an environment having more balanced nutrients and diverse organic matters, the ARG, COD and nitrogen removal efficiencies of HAB-CASS were further improved, reaching 73.3% ± 2.5%, 86.2% ± 3.8% and 93.5% ± 1.6% at HRT of 6 hr, respectively, which were much higher than those of AB-CASS(61.1% ± 4.7%,75.4% ± 5.0% and 82.1% ± 2.1%, respectively). Moreover, larger TCV/TV(total cathode volume/total volume) for HAB led to higher current and ARG removal. The ARG removal efficiency and current at TCV/TV of 0.15 were 39.2% ± 3.7% and 28.30 ± 1.48 m A,respectively. They were significantly increased to 62.1% ± 2.0% and 34.55 ± 0.83 m A at TCV/TV of 0.25. These results show that HAB system could be used to effectively treat real wastewater.     

活性黄染料废水脱色动力研究

本文采用草酸铁法（UV/Fe（C2O4）33-/H2 O2）氧化活性黄染料废水,其动力学模型为拟一级动力学反应,反应速率常数分别为0.01084 s-1,通过动力学研究方法获得染料废水脱色反应的半衰期为68s;考察了pH值和反应温度的变化对氧化反应动力学的影响,初始pH值在3.0～4.0之间,对于草酸铁法羟自由基氧化脱...     

石棉摩擦材料废弃物制吸附剂对染料的吸附研究

以石棉摩擦材料加工废弃物为材料制得的吸附剂,在色度５０００倍溶液中对阳离子黄Ｘ－５ＧＬ的静态吸附量为１５９．６８ｍｇ／ｇ,在色度５００倍的溶液中对阳离子艳蓝ＲＬ的静态吸附量为７９．６８ｍｇ／ｇ;对毛纺厂腈纶染缸废水的处理量可达２８０ｍｌ／ｇ,对活性染料亦有较好的吸附效果,吸附饱和吸附剂可通过后处理实现资源化。     

Fe2+-H2O2法处理DSD酸生产氧化母液的研究

为改善DSD酸氧化母液的可生化降解性,将废液先用有机絮凝剂TS-1(一种季胺盐)处理,TS-1的投加量为3g/L,其后用Fe²⁺-H₂O₂法氧化,Fe²⁺和H₂O₂的量分别为150mg/L,7g/L,废液COD和色度的去除率分别可达64%和62%。经处理后的废水,其BOD₅/COD≈0.3,可以认为已达到生化处理的要求。当H₂O₂的投量为2g/L,经Fe²⁺-H₂O₂氧化处理后的废液,再用FeCl₃进行两级混凝处理(FeCl₃的投加量分别为5g/L和2g/L),则COD和色度的去除率可达90%和95%。     

电解法处理活性染料废水的研究

某化工厂活性染料生产废水高CODCr值、高浓度、高色度、高盐分、成分复杂、有毒有害物质多、可生化性差。实验确定了废水经AS剂絮凝和电解预处理的研究方案。主要考察了电极极板材料、电解pH值、电解电压大小、电解时间和电极极板间距对CODCr去除效果的影响 ,从而确定了最佳电解条件 :采用石墨板电极 ,pH =3,电解电压 6 5V ,电解时间 5 0min ,电极极板间距 5cm。最佳条件下经放大实验 ,发现CODCr去除率高达 70 %以上。     

电化学法处理含盐染料废水

研究了电化学法处理含盐染料废水的可行性及其处理效果．结果表明,电化学法对废水的色度和COD具有良好的去除效果,电解过程中余氯的产生对色度和COD的去除有决定性作用．实验确定的高浓度含盐废水电化学处理条件为：电流密度0．017A/cm²,电压10．3V,平均电导率12．35ms/cm,电解60min,色度和COD的去除率分别为85％和99．8％．电解过程无难以继续反应的中间产物生成．     

用聚(丙烯酸/丙烯酰胺)水凝胶吸附单价阳离子染料的研究

研究了用聚 (丙烯酸 丙烯酰胺 ) [P(AAc AAm) ]水凝胶对较高较大浓度范围 (10 -6— 10 -2 mol L)的阳离子染料碱性藏花红 (SafranineT)溶液的吸附过程和水凝胶经解吸后的再吸附性质 .实验结果表明 :增大P(AAc AAm)水凝胶的交联度和电荷比值有利于吸附过程的进行 ,并强化了引发过程 (initiationprocess)而抑制了协同过程 (cooperativeprocess) .水凝胶经解吸后 ,其吸附能力大大地增强 ,复合度 (β)超过 1,约为 1 5 ,此时 ,协同性和染料分子间的疏水相互作用起了主要作用     

Treatment of anthraquinone dye wastewater by hydrolytic acidification-aerobic process

Experiment on microbial degradation with two kinds of biological process, hydrolytic acidification-aerobic process and aerobic process was conducted to treat the anthraquinone dye wastewater with CODc, concentration of 400 mg/L and chroma 800. The experimental result demonstrated that the hydrolytic-aerobic process could raise the biodegradability of anthraquinone dye wastewater effectively. The effluent CODc, can reach 120-170 mg/L and chroma 150 which is superior to that from simple aerobic process.