活性炭纤维净化印刷过程产生的VOCs废气

介绍了应用局部排气的方法,收集印刷过程的挥发性有机化合物（VOCs）废气,应用活性炭纤维（ACF）吸附脱附有机废气回收净化装置,进行印刷厂VOCs废气的回收与治理,详细描述了印刷车间VOCs废气的收集与处理工艺过程及其效果.测试结果表明,应用此工艺和设备可以有效地进行印刷过程大风量的VOCs废气的回收和治理.     

无锡太湖新城污水处理厂改良型A^2／O工艺的调试与运行

介绍了无锡市太湖新城污水处理厂的一期工程设计概况和所采用的改良型A^2/O脱氮除磷工艺，分析、探讨了污水处理厂的调试、培菌、试运行过程中出现的问题，并针对性地采用了一系列的解决措施。由监测数据表明，该工艺运行可靠，出水水质稳定，实现了污水处理厂的正常运行。     

倒置A2/O污水处理工艺的特点及应用实例

传统A²/O工艺在保证脱氮效果的同时除磷效果往往不佳。在充分分析传统A²/O工艺的基础上，提出了将缺氧池置于厌氧池前面，厌氧池后设置好氧池的分点进水倒置A²/O工艺。某污水厂的现场试验表明，在COD去除能力与常规A²/O工艺相当的情况下，倒置A²/O工艺的脱氮除磷功能明显优于常规A²/O工艺。     

河流水质的动态马尔柯夫评价

根据马尔柯夫过程的原理,在水质级别评价结果的基础之上,构造水质变化的概率转移矩阵,并对转移概率赋权计算绝对进步度,然后在此基础上引出相对进步度的概念,用相对进步度来评价河流水质在一段时期内的变化程度.运用该方法计算了中国四大河流2005年的水质相对进步度,并对计算结果进行了分析.     

A/O工艺处理城市生活工业综合污水的耐受性研究

针对目前城市污水处理厂进水水质以生活污水为主转向以难生物处理的工业废水为主的现状,进行了A/O工艺的耐受性试验.结果表明:随着工业废水比例的增加,厌氧、好氧污泥活性都显著下降,厌氧污泥的耐受性较高;随着运行时间的延长,两类污泥的活性逐步得到不同程度的恢复;工业废水比例越高,活性恢复所需时间越长;两类污泥的协同代谢作用保证了出水效果.A/O工艺所能耐受的进水中制药废水、印染废水和生活污水的分配比(体积比)为3∶3∶4.     

城市污水处理厂除臭技术

介绍了城市污水处理厂臭气来源、成分及产量。针对目前国内外除臭技术的研究和发展情况，分析了污水处理厂的各种物理、化学和生物除臭方法的技术原理、优缺点和应用现状。结合日本城市污水处理厂的运行实际，重点介绍了一种不产生臭气的新技术——腐殖活性污泥法的工艺流程、特点及其应用现状。     

磷酸铵镁沉淀法脱氨机理、应用及沉淀剂循环

铵根离子可以和镁盐、磷酸根在适当的条件下生成磷酸铵镁沉淀,利用这一反应可以去除水中的氨氮.本文从磷酸铵镁的性质、反应机理、反应条件及沉淀剂循环利用等方面,对这一方法进行了介绍和总结,并对今后该技术发展提出了建议.     

Isotopic modelling of the significance of bacterial sulphate reduction for phenol attenuation in a contaminated aquifer

A Triassic sandstone aquifer polluted with a mixture of phenolic hydrocarbons has been investigated by means of high-resolution groundwater sampling. Samples taken at depth intervals of 1 m have revealed the presence of a diving pollutant plume with a sharply defined upper margin. Concentrations of pollutant phenols exceed 4 g/l in the plume core, rendering it sterile but towards the diluted upper margin evidence for bacterial sulphate reduction (BSR) has been obtained. Groundwaters have been analysed for both delta34S-SO4 and delta18O-SO4. Two reservoirs have been identified with distinct sulphate oxygen isotope ratios. Groundwater sulphate (delta18O-SO4 = 3-5/1000) outside the plume shows a simple linear mixing trend with an isotopically uniform pollutant sulphate reservoir (delta18O-SO4 = 10-12/1000) across the plume margin. The sulphur isotope ratios do not always obey a simple mixing relation, however, at one multilevel borehole, enrichment in 34SO4 at the plume margin is inversely correlated with sulphate concentration. This and the presence of 34S-depleted dissolved sulphide indicate that enrichment in 34SO4 is the result of bacterial sulphate reduction. Delta34S analysis of trace hydrogen sulphide within the plume yielded an isotope enrichment factor (epsilon) of -9.4/1000 for present-day bacterial sulphate reduction. This value agrees with a long-term estimate (-9.9/1000) obtained from a Rayleigh model of the sulphate reduction process. The model was also used to obtain an estimate of the pre-reduction sulphate concentration profile with depth. The difference between this and the present-day profiles then gave a mass balance for sulphate consumption. The organic carbon mineralisation that would account for this sulphate loss is shown to represent only 0.1/1000 of the phenol concentration in this region of the plume. Hence, the contribution of bacterial sulphate reduction to biodegradation has thus far been small. The highest total phenolic concentration (TPC) at which there is sulphur isotope evidence of bacterial sulphate reduction is 2000 mg/l. We suggest that above this concentration, the bactericidal properties of phenol render sulphate-reducing bacteria inactive. Dissolved sulphate trapped in the concentrated plume core will only be utilised by sulphate reducers when toxic phenols in the plume are diluted by dispersion during migration.     

高速微涡活性污泥法提高氧利用效率的研究

概述了高速微涡活性污泥法的工艺特点，并对该法提高氧的转移及利用效率进行了研究和机理分析。