无顺市水污染物总量分配探讨

根据抚顺市地表水系和水域功能区划的分布情况，采用了定额达标分配、治理费用最小，及按现有排污总量进行达标分配的方法对水污染物进行总量分配，从而对减少污染物排放，控制水体污染提供了技术支持。     

陶瓷微滤膜过滤黑液的清洗与再生

对无机陶瓷微滤膜过滤草桨黑液的膜清洗及再生的方法进行了研究。考察了物理和化学方法的再生效果、单种清洗剂的清洗效果、复合方法的清洗效果和效果的可重复性。结果表明物理冲洗、高温灼烧、单一的化学清洗剂清洗均可以提高陶瓷膜的再生通量；但是复合方法对陶瓷微滤膜的再生效果较好，其中按氢氧化钠溶液清洗、硝酸溶液清洗、次氯酸钠溶液清洗的实验步骤，膜的再生渗透通量高．且重复性强，可望在工业生产的在线清洗中应用。     

上海市大气颗粒物高浓度区污染物的源解析

应用受体模式的化学质量平衡法支９个监测点的大气颗粒物进行污染源的源解析，得出这９个监测点的各类污染源平均贡献率为建筑尘占３２．１％，土壤尘占２７．５％，钢铁尘占２４．９％，燃煤尘占１４．８％，汽车尘和燃油尘分别占０．２％和０．４％。     

海水中氰化物测定方法探讨

对应用异烟酸 吡唑啉酮分光光度法测定海水中氰化物的方法进行了补充和改进,提高了海水氰化物测定方法的精密度和准确度。     

烟气脱硫工艺的选择

论述了现今国内外烟气脱硫的现状及烟气脱硫工艺的分类，国内外较为先进的烟气脱硫工艺的机理及特点，且对不同的脱硫技术的优缺点进行了全面的比较，对需要进行脱硫的装置现状了科学地分析，并最终提出选择合理的脱硫工艺的方法及注意的问题。     

抚顺地区大气总悬浮微粒的元素富集特征及污染来源研究

本文采用Ｘ射线荧光法分析了抚顺地区采暖期与非采暖期大气总悬浮微粒中Ａｓ等２０种元素的浓度水平，用富集因子法，因子分析法及多元回归法识别该地区的主要污染源，并估算它们对总悬浮微粒的贡献，其贡献率为：煤炭燃烧２６．９％〈冶金工业２６．８％，风砂土壤２２．０％；汽车燃油６．７％，其它污染源１７．６％。     

包埋法固定化细胞技术及其在水处理中的应用研究

固定化细胞技术(主要为包埋技术),由于方法简单、条件温和、较高的稳定性及细胞容量,在废水处理中应用广泛.本文主要介绍了近年来固定化细胞技术在污水深度处理中的应用研究现状和发展前景,并对固定化细胞技术在污水深度处理过程中的影响因素进行简要论述.     

3,5-二甲基吡唑磷酸盐硝化抑制作用初探

采用室内培养实验的方法,以不加抑制剂的尿素作为对照,对比研究DMPP及它的同分异构体3,5-二甲基吡唑磷酸盐作为硝化抑制剂对尿素氮在土壤中转化的影响.结果表明,3,5-二甲基吡唑磷酸盐具有一定的硝化抑制作用.在培养期间,施加3,5-二甲基吡唑磷酸盐的土壤中硝态氮的含量一周后始终低于对照,铵态氮的含量一用后始终高于对照.但在培养试验中后期(三周以后),3,5-二甲基吡唑磷酸盐的硝化抑制效果劣于DMPP.3,5-二甲基吡唑磷酸盐能否作为新型硝化抑制剂,还要对它的生理、生态效应等进行进一步的研究.     

超声波/Fenton联用对对硝基苯酚的处理

采用超声/Fenton联用技术对水中对硝基苯酚(P-NP)进行处理,探讨了单纯超声(US)、Fenton试剂法、US/Fenton试剂法联用对P-NP的处理效果和影响因素,结果表明,对于浓度为10mg/L的P-NP, 当pH=3、H2O2与Fe2 投加量之比为10:1、H2O2投加量为40mg/L时降解效果最好,通过动力学分析发现US/Fenton试剂法对P-NP的降解具有明显的协同效应.     

Insights into the mechanism of the deterioration of mainstream partial nitritation/anammox under low residual ammonium

Residual ammonium is a critical parameter affecting the stability of mainstream partial nitritation/anammox (PN/A), but the underlying mechanism remains unclear. In this study, mainstream PN/A was established and operated with progressively decreasing residual ammonium. PN/A deteriorated as the residual ammonium decreased to below 5 mg/L, and this was paralleled by a significant loss in anammox activity in situ and an increasing nitrite oxidation rate. Further analysis revealed that the low-ammonium condition directly decreased anammox activity in situ via two distinct mechanisms. First, anammox bacteria were located in the inner layer of the granular sludge, and thus were disadvantageous when competing for ammonium with ammonium-oxidizing bacteria (AOB) in the outer layer. Second, the complete ammonia oxidizer (comammox) was enriched at low residual ammonium concentrations because of its high ammonium affinity. Both AOB and comammox presented kinetic advantages over anammox bacteria. At high residual ammonium concentrations, nitrite-oxidizing bacteria (NOB) were effectively suppressed, even when their maximum activity was high due to competition for nitrite with anammox bacteria. At low residual ammonium concentrations, the decrease in anammox activity in situ led to an increase in nitrite availability for nitrite oxidation, facilitating the activation of NOB despite the dissolved oxygen limitation (0.15–0.35 mg/L) for NOB persisting throughout the operation. Therefore, the deterioration of mainstream PN/A at low residual ammonium was primarily triggered by a decline in anammox activity in situ. This study provides novel insights into the optimized design of mainstream PN/As in engineering applications.