Coupling mechanism of activated carbon mixed with dust for flue gas desulfurization and denitrification

To clarify the effect of coking dust, sintering dust and fly ash on the activity of activated carbon for various industrial flue gas desulfurization and denitrification, the coupling mechanism of the mixed activated carbon and dust was investigated to provide theoretical reference for the stable operation. The results show that coking dust had 34% desulfurization efficiency and 10% denitrification efficiency; correspondingly, sintering dust and fly ash had no obvious desulfurization and denitrification activities. For the mixture of activated carbon and dust, the coking dust reduced the desulfurization and denitrification efficiencies by blocking the pores of activated carbon, and its inhibiting effect on activated carbon was larger than its own desulfurization and denitrification activity. The sintering dust also reduced the desulfurization efficiency on the activated carbon while enhancing the denitrification efficiency. Fly ash blocked the pores of activated carbon and reduced its reaction activity. The reaction activity of coking dust mainly came from the surface functional groups, similar to that of activated carbon. The reaction activity of sintering dust mainly came from the oxidative property of Fe₂O₃, which oxidized NO to NO₂ and promoted the fast selectively catalytic reduction (SCR) of NO to form N₂. Sintering dust was activated by the joint action of activated carbon, and both had a coupling function. Sintering dust enhanced the adsorption and oxidation of NO, and activated carbon further promoted the reduction of NO_x by NH₃; thus, the denitrification efficiency increased by 5%-7% on the activated carbon.     

ASM1中废水和污泥组分浓度的测定方法研究

对呼吸计量法应用于校准ASM1作了简明的阐述。在呼吸速率与模型组分关系的基础上,介绍了ASM1中废水与污泥各组分浓度的测定方法,并指出模型组分细化的意义。     

活性炭吸附与生物活性炭脱臭效果的比较研究

针对污水收集与处理系统中恶臭气体的组成与特性,比较分析不同情况下活性炭吸附与生物活性炭的脱臭效果。当干活性碳总处理气量达到1.3m~3/g时,出现穿透。将吸附饱和的活性炭填料塔转为生物滴滤反应器后,仍能较快的实现挂膜生长,达到满意的处理效果。直接运行的生物活性炭滴滤器对H_2S的处理效率在95％以上,并具有较强的恢复能力。H_2S平均出口浓度为0.052mg/m~3。循环液pH值与盐度在一定范围内对系统影响不大。     

活性污泥系统动力学模拟方法的综合分析

活性污泥法的应用现状和污水中氮磷排放标准的日益严格，使得传统数学模型已满足不了目前的要求，需要对活性污泥系统复杂的动力学规律进行有效模拟。文章在综合分析活性污泥动态模型国内外研究现状的基础上，介绍了3种占主流地位的模型：活性污泥数学模型、神经网络模型和混合模型。这3种模型在污水处理的设计、运行控制和工艺优化等方面各有其独到之处。     

活性污泥外循环SBR系统循环污泥释磷能力研究

本试验以HAc作为厌氧释磷的碳源有机物，以SBR系统外循环污泥作为研究对象，探索外循环活性污泥的厌氧释磷能力和获取高浓度富磷污水的途径，试验表明：厌氧过程中聚磷菌吸收HAc和释放PO4^3 的分子比为1：1。即吸收2．06mgHAc-COD将诱导1mgP释放，单位时段比污泥的平均释磷速率Vp=6.54.t^0.76，理想的厌氧时间为60－180min，减少循环污泥释磷系统的反应容积可以提高富磷污水磷酸盐的浓度。     

城市污水高效低耗生物脱氮工艺研究

采用活性污泥与生物膜法相结合工艺处理城市生活污水，可以高效去除污水中的有机物和NH4^ -N。研究结果表明：水力停留时间为7．5h、回流比为1．5、无外加碳源时，COD的去除率大于90％，NH4^ -N的去除率大于99％；平均出水COD小于40mg／L，NH4^ -N小于1mg／L，TN的去除率60％左右；反硝化过程的适宜C／N为4～5。     

小诺霉素发酵废水好氧生物处理试验研究

对具有强抑制性污染物的抗生素小诺霉素发酵废水，选择活性污泥、粉末活性炭（ＰＡＣＴ）、纯氧曝气等３种好氧生物处理法进行了比较试验。根据实验结果，小诺霉素发酵废水的生物降解呈抑制动力学，采用Ｍａｒｑｕａｒｔ方法对动力学模式进行参数估计。ＰＡＣＴ能够有效地降低降解过程中微生物受到的抑制作用，从而明显地改善了生物处理过程动力学。     

活性炭厌氧流化床处理毒性有机废水存在的问题与对策

活性炭厌氧流不处理毒性有机废水存在问题，对含有活性炭能吸附而生物难降解成份的废水，通过定期替换少量活性炭、能维持工艺的稳定运行。     

活性硅酸聚合硫酸铁的研究

以硅酸钠，硫酸和聚合硫酸铁为原料制备活性硅酸合硫酸铁，测定了ＡＳＰＦＳ红外光谱，了Ｆｅ／Ｓｉ摩尔比和水样ＰＨ值等因素对产品和除浊效果的影响当Ｆｅ／Ｓｉ摩尔比为１．５时产品稳定性和除浊效果均较好。     

活性污泥数学模型中异养菌产率系数的测定研究

利用活性污泥数学模型预测污水生物处理系统,首先必须确定其参数和水质组分。采用间歇活性污泥法和呼吸计量法对活性污泥数学模型中异养菌产率系数γ_H进行测定研究。结果表明,间歇活性污泥法测定结果重现性较差,试验控制条件比较严格;呼吸计量法测定结果准确性较高,重现性良好,因而,呼吸计量法是比较可行的γ_H测定方法。