锌—镉多相还原法测定硝酸盐氮

水中硝酸盐氮的测定,常用比色法和物理化学法.比色法中,酚二磺酸法精密准确,但试剂制备和实验操作麻烦,且受氯离子(>10mg/L)和亚硝酸盐氮(>0.2mg/L)的严重干扰,对这两种离子含量较高的水样去除干扰步骤繁;物理化学法中的紫外分光光度法,简单快速,但灵敏度低;离子选择电极法受氯离子和碳酸氢根(HCO_3~-/NO_3~->5)干扰;锌—镉还原柱法,灵敏度高,但还原速度慢,且因流速不同使得试样和还原剂接触     

土壤全氮的快速测定

本方法是过硫酸盐氧化消化样品的基础上测定土壤中全氮的光度法.采用碱性过硫酸钾溶液(0.37mol/L K_2S_2O_3,0.375N NaOH)消化土壤样品,然后用百里酚光度法进行测定,具有准确、灵敏、快速、简便等优点,适用于常规和大量样品的分析.     

白泥湖污水处理厂的设计特点

本文主要介绍广东省环境保护工程研究设计室与丹麦克鲁格公司合作设计的白泥湖污水处理厂的特点，重点在引进项目的消化、吸收。     

硝化反应及其控制因素

对硝化菌和亚硝化菌的特性进行了分析，并就碳源不足的废水实行短程硝化—反硝化脱氮的途径进行探讨。     

UNITANK工艺在中、小型污水处理站的应用

介绍了UNITANK工艺的基本构造、运行方式和技术特点及在新疆盐湖制盐有限公司生活污水处理站的应用实例，经过两年的实际运行表明，该工艺应用于中、小型生活污水处理站技术、经济合理，易于管理操作，具有良好的应用前景。     

专家系统在废水生物处理操作和控制中的应用

本文介绍了国外近二十年来专家系统在废水生物处理工艺控制领域的应用及开发的典型系统，分析了废水生物处理工艺难于控制的原因，各类系统的结构和特点及目前废水处理专家系统系统的不足，探讨了废水生物处理专家系统今后深入研究的问题及方向。     

不锈钢壳体的冷挤压工艺及模具设计

壳体是机械中广泛使用的重要零件之一.采用冷挤压工艺可提高质量、降低成本.对不锈钢壳体成形工艺及模具设计作了详细讨论.     

NBIAS中污泥龄对脱氮除磷效果的影响

探讨无回流间歇曝气系统 (简称 NBIAS) ,处理城市污水的污泥龄 ( SRT)对脱氮除磷及有机物去除效果的影响。通过原污水流程试验和人工合成污水静态模拟实验 ,试验结果表明 :在水温为 2 0℃～ 30℃ ,污泥负荷为 0 .2 5～0 .45kg CODcr/ kg MLSS· d,SRT为 1 8～ 2 2 d,HRT为 8～ 1 0 h时 ,利用原污水作为碳源 ,NBIAS在保持较高的 CODcr去除率的同时 ,总氮和总磷的去除率均在 80 %以上。     

Removal of high concentrated ammonia nitrogen from landfill leachate by landfilled waste layer

The landfill of municipal solid waste(MSW) could be regarded as denitrification reactor and involved in ammonia nitrogen biological removal process. In this research, the process was applied to municipal solid waste collected in Shanghai, China, which was characterized by high food waste content. The NH4^ removal efficiency in the system of SBR nitrifying reactor followed by fresh and matured landfilled waste layer in series was studied. In the nitrifying reactor, above 90% of NH4^ in leachate was oxidized to NO2^- and NO3^- . Then high concentrated NO2^- and NO3^- were removed in the way of denitrification process in fresh landfilled waste layer. At the same time, degradation of fresh landfilled waste was accelerated. Up to the day 120, 136.5 gC/(kg dry waste) and 17.9 gN/(kg dry waste) were converted from waste layer. It accounted for 50.15 % and 86.89 % of the total carbon and nitrogen content of preliminary fresh waste, which was 4.42 times and 5.17 times higher than that of reference column respectively. After filtering through matured landfilled waste, BOD5 concentration in leachate dropped to below 100 mg/L, which would not affect following nitrification adversely. Because the matured landfilled waste acted as a well methanogenic reactor, 23% of carbon produced accumulatively from fresh landfilled waste degradation was converted into CH4.