大气-气溶胶在线装置和离子色谱联用技术对西安市灰霾天气的监测研究

本文使用美国URG公司生产的大气气溶胶(PM2.5)水溶性组分/大气(气态污染物)在线监测分析系统,对西安市2013年1月持续近一月的灰霾天气空气质量污染的全过程,进行了连续不间断监测、分析研究,结果表明:结合西安市气候状况和地形等因素,汽车尾气、集中采暖等人类活动才是造成这次西安市冬季灰霾天气的主要因素.     

还原蒸馏法分析硝基苯类化合物的探讨

由于还原偶氮比色法中锌渣、滤纸吸附对分析硝基苯类化合物有较大影响,文章采用还原后蒸馏的方法分析硝基苯类化合物,该法比滤纸过滤分析结果准确,精密性好,操作简单.     

隔油池在常减压装置的应用

介绍隔油池的结构及原理，论述了它在胜利炼油厂南常减压装置的应用，指出其问题及改进措施．     

米菲司酮废水处理的试验探索

对米菲司酮生产中产生的高浓度有机废水（ＣＯＤｃｒ８．８×１０＾４ｍｇ／Ｌ），采用常压蒸馏－活性炭吸附方法进行试验性处理，ＣＯＤｃｒ的去除率可达９５％以上，ＣＮ－去除率达９９．９％，并可回收乙醇等低沸点有机溶剂。     

关于提高挥发酚测定质量的探讨

探讨了在水样采集及分析测定过程中，如何保证分析结果的可靠性和准确性。     

固定污染源排气中氟化物监测方法研究

采用直接蒸镏法对固定污染源中固态氟化物样品进行处理，使用离子色谱或离子选择电极对样品进行测定，结果表明：其测定范围、精密度、准确度，均能满足环境监测的要求。     

杀虫双生产废水的预处理研究

研究杀虫双生产废水的预处理工艺，对碱性废水采用减压蒸馏法脱盐，馏出比1／3，真空度40kPa,10次循环蒸馏，脱盐率达77％，馏出液的可生化性好，可直接生物处理，酸性废水，尾气吸收废水经混合调碱处理后，CODcr去除率达75％，BODs/CODcr由原水的0．08提高至0．36，各股废水预处理后混合，经7d间歇生化处理的CODcr去除率达68％。     

中文智能型pH线监控仪及其工程应用

介绍了以微计算机为核心的中文智能型pH在线监控仪的软硬件结构、系统配置模式,及多个废水处理工程中pH监控系统的设计思路和小试的工艺流程。     

热泵蒸馏应用于橡胶助剂废水预处理的研究

橡胶助剂废水属于难处理的工业废水，尤其是CBS（N－环己基－2－苯并噻唑次磺酰胺，英文名N－cyclohexy1-2-benzoth-iazole sulfonamide，简称Accelerator CBS)生产废水的COD达40000mg/L，并且含有杂环类有害化合物，难降解，难生化。经过絮凝沉淀、化学氧化、电化学法、吸附法等实验方法，处理效果都不是十分理想。采用热泵蒸馏技术对橡胶促进剂CBS的废水进行预处理实验，可使CBS废水的COD从40000mg/L降至1600mg/L，结果表明，该技术设备简单，投资少，操作方便，运行成本低，并能达到较理想的预处理效果。     

Enhanced solar still productivity using transparent walls with an integral trough and organic porous absorber material

This experimental work has been conducted to compare the performance of the modified stills with that of the conventional still. Three modified stills (S1, S2, and S3) and conventional still (S4) were fabricated, each with 0.5 m² of the basin area. S1 and S3 had transparent double glass walls with air in between acting as insulation, whereas S2 has a single transparent wall. S4 has insulated plywood walls painted black from inside. A mixture of coco peat and charcoal was used in S1, S2, and S3, whereas there was no basin material for S4. Experiments were conducted by changing the water quantity in the solar still ranging from 5 to 10 kg. Maximum distillate output of 5.46 l/m²-d was obtained for S2, whereas it was 3.80 l/m²-d for S4 for an average solar radiation intensity of 675 W/m² (24.3 MJ/m²-d). Use of transparent walls with troughs to collect condensate increased the condenser area by 78.4%. The distillate water cost per liter was estimated as Rs. 0.86 (0.013 US$) and Rs. 1.61 (0.025 US$) for S2 and S4, respectively. Energy payback time for S2 was estimated as 4 months. Theoretical and experimental values showed that there is a significant loss of incoming solar radiation due to wall shadow.