利用EXCEL求算水中非离子氨

Excel是办公自动化中非常重要的一款软件，它的数据处理功能在现有的文字处理软件中可以说是独占螯头，通过简单的学习，结合国家标准给出的换算公式，利用EXCEL编制程序，方便快捷地计算水中非离子氨浓度，计算结果表明，当实际测得水温和pH与表中数据吻合时三种计算方法结果无明显差异，当实际测得的水温和pH与表中不对应时，查表法存在明显偏差，而使用EXCEL运算就能与笔算结果一致，准确可靠。     

环境样品监测中总氮低于氨氮的原因

环境样品监测中常出现的氨氮高于总氮现象,主要由从取样到数据处理过程中7个方面的因素造成,人为只能将其控制在一定范围内.得出上述结果,只要达到分析质量控制和质量保证要求,分析数据就应当是准确可靠的.     

低温高铁锰氨氮地下水两级生物净化快速启动

为了实现东北地区低温（5~6℃）高铁、锰、氨氮（TFe：9~15mg/L，Fe²⁺：6~12mg/L，NH₃-N：1.4~2.0mg/L，Mn²⁺：1.4~2.0mg/L）地下水的净化及解决同层净化中运行稳定性差、出水锰超标的问题，在水厂净化车间开展“两级曝气+两级过滤”工艺启动研究，采用差滤速和同滤速2种启动方式分别启动两级生物净化工艺.结果表明，2种启动方式分别在106，59d启动成功.同滤速启动可以有效的缩短两级生物净化的启动时间，铁、锰、氨氮去除负荷可达110.69，18.80，19.54g/（m²·h），沿程分析发现，铁在一级滤柱的60cm处即被去除至痕量；85.08%的氨氮在一级滤柱中去除，沿程各段去除均匀，14.92%的氨氮在二级滤柱中去除；锰的去除率和氧化活性去除区位受滤速及进水氨氮浓度影响较大，33.72%的锰在一级滤柱中去除，66.28%的锰在二级滤柱中去除，锰的去除仍然是滤池成熟的决定性因素.     

焦化厂废水中氨的测定——气敏电极法

研究了用气敏电极测定焦化厂废水中氨的分析方法，对测定的线性范围，响应时间、回收率、干扰物质等作了理论探讨和大量试验。在ｐＨ为１１５～１４０时，线性范围为１００×１０－５～１００×１０－１ｍｏｌ／Ｌ，最低检出限为５０×１０－６ｍｏｌ／Ｌ，ＲＳＤ≤２５％。     

氨法脱硫在热电厂中应用

随着二氧化硫对环境的污染越来越严重，国家环保局对燃煤电厂二氧化硫排放进行严格控制，电厂加装脱硫装置是迟早的事。阐述了氨法脱硫的工艺流程和自动控制．同时结合工程调试中出现的问题进行分析，为今后的脱硫工程提供一些借鉴。     

Field measurements of dissociation of ammonium nitrate at a Beijing site

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三唑磷农药废水厌氧处理可行性研究

采用厌氧流化率工艺处理在唑磷农药废水，必须降低原水中ＮＨ３－Ｎ含量，调整营养比例，当ＣＯＤ：Ｎ：Ｐ＝（１８０～２００）：５：１时，在中温厌氧消化条件下，ＣＯＤ含量可从４１７０ｍｇ／ｌ，去除率约５０％，沼气产率达到０．２５６ｍ＾３／ｍ＾３．ｄ。因此，把厌氧处理作为好氧处理的预处理单元，能确保整个处理系统出水达标。     

沱江和釜溪河的氨治理及氨回收

本文介绍了沱江和釜溪河近年来的氨污染现状及危害，认为氨是应治理的首位污染物；简要分析了生物、化学、物理化学三类除氨方法的优缺点；着重介绍了吹脱法除氨技术，提出用吹脱法治理沱江和釜溪河的无机氨污染，并进行了上述各法的经济效益比较     

Modelling nitrogen fluxes at the landscape scale

The distribution and impacts of different nitrogen pollutants are inextricably linked. To understand the problem fully, the interactions between the different pollutants need to be taken into account. This is particularly important when it comes to abatement techniques, since measures to reduce emissions of one nitrogen pollutant can often lead to an increase in another. This project represents a step towards greater understanding of these issues by linking together new and existing nitrogen flux models into a larger framework. The modelling framework has been constructed and some of the nitrogen flows between fields, farms and the atmosphere have been modelled for a UK study area for typical farm management scenarios.     

Concentrations of disinfection by-products in swimming pool following modifications of the water treatment process: An exploratory study

The formation and concentration of disinfection by-products (DBPs) in pool water and the ambient air vary according to the type of water treatment process used. This exploratory study was aimed at investigating the short-term impact of modifications of the water treatment process on traditional DBP levels (e.g., trihalomethanes (THMs), chloramines) and emerging DBPs (e.g., Halonitromethanes, Haloketones, NDMA) in swimming pool water and/or air. A sampling program was carried to understand the impact of the following changes made successively to the standard water treatment process: activation of ultraviolet (UV) photoreactor, halt of air stripping with continuation of air extraction from the buffer tank, halt of air stripping and suppression of air extraction from the buffer tank, suppression of the polyaluminium silicate sulfate (PASS) coagulant. UV caused a high increase of Halonitromethanes (8.4 fold), Haloketones (2.1 fold), and THMs in the water (1.7 fold) and, of THMs in the air (1.6 fold) and contributed to reducing the level of chloramines in the air (1.6 fold) and NDMA in the water (2.1 fold). The results highlight the positive impact of air stripping in reducing volatile contaminants. The PASS did not change the presence of DBPs, except for the THMs, which decrease slightly with the use of this coagulant. This study shows that modifications affecting the water treatment process can rapidly produce important and variable impacts on DBP levels in water and air and suggests that implementation of any water treatment process to reduce DBP levels should take into account the specific context of each swimming pool.