靛兰染料工业的生产废水治理工艺

靛兰染料(indigo)是一个插烯系的二羰基化合物,同时和苯环共轭而成深色染料,是一个复杂的有机化合物。靛兰染料废水中的金属盐含量、COD、色度均很高。废水经预处理可去除大量金属盐悬浮颗粒,COD去除率达50～55%;生化处理COD去除率达60%,苯胺去除率达99%;通过对物化后几种常用处理方法的比较,论述了吸附是比较理想的方法。经"预处理、生化、物化吸附"二级处理后的靛兰染料废水,出水各项指标均能达到国家排放标准。     

有机污水生物脱氮除磷的生化机理、影响因素及工艺

重点介绍有机污水用生物法脱氮除磷的生化机理，同时叙述了该法的影响因素及工艺，指出该法因工艺简单、灵活和处理能力强，已成为近年来污水处理的重要方法并得到广泛应用。     

关于烧碱厂废氯气回收工艺的探讨

介绍了甘肃省盐锅峡化工总厂近年来在烧碱生产中由过去废氯气直接排入环境改为回收废氯气用于生产三氯乙醛、液氯和次氯酸钠。此法不仅有效地减少了氯气排放和环境污染，而且创造了明显的经济效益。     

腈纶废弃物制备高分子絮凝剂新工艺

作者叙述了以腈纶废弃物为原料，进行催化还原、羧甲基化反应，制备了高分子絮凝剂。研究了反应条件对产物的影响，通过对一系列污水进行处理比较，证明该种工艺与其他工艺相比具有较好的效果。     

城市生活垃圾厌氧消化技术

随着我国经济的发展。城市生活垃圾污染越来越严重。本文阐述了城市生活垃圾生物处理技术以及其特点。着重分析说明了厌氧消化的原理以及处理生活垃圾的影响因素，最后介绍了几种国外常用的厌氧处理工艺。     

甘肃火电机组二氧化硫控制措施探讨

针对甘肃火电机组燃煤煤质特点，比较系统地分析了国内几种常用脱硫工艺在甘肃地区应用的可行性，并就选择二氧化硫控制措施时应注意的几个因素进行了分析和探讨。     

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.     

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.