污泥臭氧化减量技术的影响因子

采用臭氧作为剩余污泥的细胞裂解剂,并与生物接触氧化工艺相结合进行污泥减量的实验研究,臭氧化后的污泥上清液回流入曝气池与污水合并处理。结果表明:在臭氧投量为0.05kgO3/kgMLSS,臭氧化污泥量为进水量的5%条件下,生物接触氧化系统对SCOD和NH4-N的平均去除率分别为87.06%和84.80%,出水水质同对比实验相当;同时获得了0.054(gMLSS/去除1gSCOD)的剩余污泥产率,与对比实验相比降低了78.4%。     

碱减量印染废水特征污染物的生物降解特性

利用气相色谱-质谱联用(GC/MS)和液相色谱-质谱联用(LC/MS)对碱减量印染废水特征污染物在不同条件下生物降解产物进行了研究.结果表明,对苯二甲酸(TA)、分散橙4RL、分散蓝2BLN3种特征污染物在好氧环境和厌氧环境中都可以降解,其中TA最容易降解,2BLN次之,4RL的生物降解性能最差.4RL分解过程产生大量对微生物具有很强的抑制作用的苯胺类物质;易降解物质的添加可以增强难降解物质的分解,这种作用在厌氧条件下更加明显.对特征污染物的分解规律进行了分析和推断.     

Power system planning with emission constraints: Effects of CCS retrofitting

Today, the world's energy needs are still supplied mainly from fossil fuel based resources. This is true for electricity generation as well, thus making the power sector responsible for 45% of greenhouse gas emissions. The present climate crisis has made it necessary to minimise emissions in power generation, with low-carbon energy sources taking on greater significance in recent years. However, most low-carbon sources have inherent problems, like intermittency and high capital expenditure. A suitable alternative is carbon capture and storage (CCS) technology which allows continued fossil fuel-based electricity generation at much lower rates of emission. Two approaches are possible in the deployment of CCS technology. The first is to introduce new power plants equipped for carbon dioxide (CO₂) capture, while systematically shutting down existing coal power plants. Another is to retrofit existing power plants for CO₂ capture. These approaches are compared in this work. The study shows that allowing CCS retrofitting of existing power plants can reduce the overall cost requirement significantly. In addition, a sensitivity analysis is also done to study the effect of nuclear energy on the overall energy mix.     

污泥龄对剩余污泥减量化的影响

为了解决污水厂生化系统剩余污泥产量过多的问题,采用延长污泥龄(SRT)的方法,对剩余污泥减量化的影响进行了研究。实验得知:污泥龄由8d增至16d时,污泥表观产率系数下降28.53%,而污泥龄由8d增至24d时,污泥表观产率系数下降51.12%。污泥龄的延长对CODCr的去除能力没有明显的影响,但使出水NH3-N浓度和TP浓度均升高,通过调整碳氮磷源的比例降低出水NH3-N和TP浓度。实验结果表明:SRT的延长,不仅降低活性污泥工艺中的剩余污泥的产量,同时还能降低处理与处置的费用,有发展前景,值得深入研究。     

Waste minimization study in a solvent-based paint manufacturing plant

Solvent-based paint manufacturing plants produce significant quantities of hazardous waste, which must be properly treated before it can be disposed. Since the cost for treating this waste is high, reducing the quantity of waste has become a crucial issue in this industry.Waste minimization options are beneficial for the owner of the plant as well as for the environment. The quantity of hazardous waste can be minimized by changing the plant's technology or by substituting hazardous substances, which are used in the paint manufacturing process, with environmentally friendly ones. Furthermore, separating the various waste streams makes it easier to recover raw materials and enhances the possibility of their reuse within the production process. This will decrease operational costs for the plant.This paper presents a case study of waste minimization in a solvent-based paint manufacturing plant. Source reduction, recovery, and recycling methods are taken into consideration. Its aim is to develop an understanding of the facility's waste generating processes, to suggest ways to reduce the waste production, and finally to select an appropriate waste minimization option to suggest to the plant. Some of the suggested methods are currently being practiced while others are at initial stage of development.     

小型化自动在线大气汞分析仪的开发及移动观测应用

基于金汞齐-冷原子荧光法开发了一套小型气态元素汞(TGM)在线监测仪,该仪器采用真空系统设计,体积小、重量轻,可实现无人值守自动运行,适用于车载移动观测.实验测试表明,仪器在典型时间分辨率4 min条件下的检出限能达到0.2 ng·m~(-3),优于商品化大气汞分析仪;且具有较高的精密度,标气重复实验相对偏差2%,工作曲线拟合优度R~20.999.将该仪器搭载于机动车内,对北京市四、五环路沿线气态元素汞进行了移动监测,测得四环路与五环路TGM平均浓度分别为2.25、2.63 ng·m~(-3).该仪器可提供高时空分辨率的大气汞浓度数据,可为气态元素汞的监测和污染控制提供技术支持.     

A process integration approach to industrial water conservation: a case study for an Indian starch industry

A case study for water using network of a Starch industry in the state of Gujarat, India, is undertaken with an aim to reduce demineralised water and freshwater flow rates and consequently the wastewater flow rate. The problem was identified as a multi contaminant, reuse and recycle problem. The freshwater consumption and demineralised water consumption were 100 t/h and 51 t/h respectively before modification and the network was dealing with three major contaminants such as total organic content, total dissolved solids and total suspended solids. A program was developed in MATLAB for analysis using Water Pinch. The improved water using network designed for the present work consumed less demineralised and freshwater. The reductions are of the tune of 28% and 64.38% for demineralised and fresh water respectively. Due to alteration in piping, there will be a saving of 406 026 INR per year, which will be utilized for development of efficient environment policy for the company. The entire concept had been implemented on plant level on 1st February-2009 and the reductions are of the tune of 25% and 60% for demineralised and fresh water respectively.     

厌氧水解酸化-好氧氧化Ａ1/Ａ2/O工艺剩余污泥减量对系统运行效果的影响

在碱减量印染废水Ａ₁/Ａ₂/O生物处理系统中,利用污泥回流可以实现对剩余污泥的有效减量.剩余污泥回流到Ａ₁段,增加了Ａ₁段中污泥的有机负荷,却提高了系统对COD的去除率.在Ａ₁段COD容积负荷2.54 kg/(m³·d)、水力停留时间为9.45 h和7.56 h条件下,Ａ₁段COD的去除率分别由15.9％提升至23.9％,12.3％提升至22.8％.在进水COD浓度1 000 mg/L、Ａ₁段COD容积负荷2.54 kg/(m³·d)、进水色度450倍、系统温度30℃条件下,Ａ₁段出水色度有污泥回流时较无污泥回流下降30％以上,系统出水的色度比无污泥回流时降低30％左右.回流剩余污泥使Ａ₁段出水pH略低于无污泥回流的情况,但对Ａ₂段和O段pH值影响不大.在有剩余污泥回流的系统中,系统各段出水的SS浓度均比无回流系统大.长期污泥回流会造成系统内难生物降解物质的积累,必须适时地进行排泥、气水冲刷等恢复系统污泥活性的措施.