大气颗粒物“二重源解析”技术的误差分析

"二重源解析"模型计算结果的误差是采样误差、样品处理误差、化学组分分析误差、数据处理误差以及数学模型误差等所有误差的积累。提出了"二重源解析"解析结果的相对误差和标准偏差表达式,并用之计算了某市利用"二重源解析"模型计算的源贡献值的相对误差和标准偏差,还针对从源排放出来的初始态颗粒物在传输过程中发生的扬尘态变化提出了扬尘转化率的概念和计算方法。     

不同环境条件下偶氮染料酸性大红GR的生物降解性能

为了考察不同环境条件下偶氮染料酸性大红GR生物降解性能,采用已驯化的混合菌群作为接种液进行偶氮染料酸性大红GR脱色试验。结果表明,微氧条件下(静置敞口培养),偶氮染料酸性大红GR脱色效果最佳,染料脱色主要发生在菌体的对数生长期。混合菌群对pH、温度适应范围较广,pH为3.32~9.18,温度在20℃~37℃范围内均可以获得较好脱色效果,脱色率均在80%以上。微氧条件下酸性大红GR降解历程表明,偶氮基整个共轭系统被破坏,生成了一种新的结构,使原有的某些精细结构在二阶导数光谱中得以表现,由此探讨其生物降解机理。     

三步法处理大港油田12井综合废水的实验研究

根据大港油田12井综合废水的污染特征,提出了"混凝-内电解-H2O2氧化"三步处理的方法。实验结果表明:三步法处理后可以使原水的CODcr从4930mg/L降低到128mg/L,去除率达到97%。处理后水质达到国家《污水综合排放标准》(GB8978-1996)二级标准要求。     

汽爆麦草固态发酵木质素酶

木质素是地球上主要的可再生芳香族化合物 ,是地球上仅次于纤维素的第二丰富可再生天然资源 ,然而 ,对它的利用研究却很少 ,是天然高分子中未开发的领城[1] .80年代初发现了木质素过氧化物酶 (ＬｉＰ) [2 ,3] 和锰过氧化物酶 (ＭｎＰ) [4 ] 以后 ,木质素酶和木质素生物降解研究取得了一定进展 .但木质素微生物转化降解研究中仍存在许多问题 .( 1)由于木质素酶解是一种非专一性的、以自由基为基础的链反应过程[5] .因此 ,木质素酶在化学工业、煤化学和环境保护方面具有很大的开发前景 .而现在木质素酶的生产大多用合成培养基 ,必需添加昂贵的…     

Heavy metal contamination in the vicinity of an industrial area near Bucharest

BACKGROUND, AIMS AND SCOPE: Chromium enters into the aquatic environment as a result of effluent discharge from steel works, electroplating, leather tanning industries and chemical industries. As the Cr(VI) is very harmful to living organisms, it should be quickly removed from the environment when it happens to be contaminated. Therefore, the aim of this laboratory research was to develop a rapid, simple and adaptable solvent extraction system to quantitatively remove Cr(VI) from polluted waters. METHODS: Aqueous salt-solutions containing Cr(VI) as CrO4(2-) at ppm level (4-6 ppm) were prepared. Equal volumes (5 ml) of aqueous and organic (2-PrOH) phases were mixed in a 10 ml centrifuge tube for 15 min, centrifuged and separated. Concentrations of Cr(VI), in both the aqueous and organic phases, were determined by atomic absorption spectrometry. The effects of salt and acid concentrations, and phase-contact time on the extraction of Cr(VI) were investigated. In addition, the extraction of Cr(VI) was assessed in the presence of tetramethylammonium chloride (TMAC) in 2-PrOH phase. Effects of some other metals, (Cd(II), Co(II), Cu(II), Ni(II) and Zn(II)), on the extraction of Cr(VI) were also investigated. RESULTS AND DISCUSSION: The Cr(VI) at ppm level was extracted quantitatively by salting-out the homogeneous system of water and 2-propanol(2-PrOH) using chloride salts, namely CaCl2 or NaCl, under acidic chloride media. The extracted chemical species of Cr(VI) was confirmed to be the CrO3Cl-. The ion-pair complex extracted into the organic phase was rationalized as the solvated ion-pair complex of [2-PrOH2+, CrO3Cl-]. The complex was no longer stable. It implied the reaction between extracted species. Studies revealed that salts and acid directly participated in the formation of the above complex. Use of extracting agents (TMAC) didn't show any significant effect on the extraction of Cr(VI) under high salting-out conditions. There is no significant interference effect on the extraction of Cr(VI) by the presence of other metals. The Cr(VI) in the organic phase was back-extracted using an aqueous ammonia solution (1.6 mol dm(-3)) containing 3 mol dm(-3) NaCl. The extraction mechanism of Cr(VI) is also discussed. CONCLUSIONS: Salting-out of homogeneous mixed solvent of 2-propanol can be employed to extract Cr(VI) quantitatively, as an ion-pair of [2-PrOH2+ * CrO3Cl-] solvated by 2-PrOH molecules. Then, the complex becomes 'solvent-like' and is readily separated into the organic phase. The increase of Cl- ion concentration in the aqueous phase favors the extraction. The 2-PrOH, salts and acid play important roles in the extraction process. There is no need to use an extracting agent at a high salting-out condition. RECOMMENDATIONS AND PERSPECTIVES: Chromium(VI) must be quickly removed before it enters into the natural cycle. As the 2-PrOH is water-miscible in any proportion, ion-pairing between 2-PrOH2+ and CrO3Cl- becomes very fast. As a result, Cr(VI) can easily be extracted. Therefore, the method is recommended as a simple, rapid and adaptable method to quickly separate Cr(VI) from aqueous samples.     

基于PANDA平台的飞行器脉动压力激励随机振动响应分析

目的 形成自主再入飞行数值模拟预测技术.方法 采用模态叠加法开展自由结构的多点脉动压力激励随机振动响应分析,基于PANDA高性能力学分析平台进行并行实现研究,构建相应的求解模块.针对飞行器再入过程,基于自主研发的软件模块,分析飞行器自由状态的模态特性及其在实测脉动压力载荷下的振动响应,并与商业软件分析结果 进行比对.结...     

混合型微生物絮凝剂产生菌的最佳培养条件

从活性污泥中筛选出具有较高絮凝活性的混合菌MBFH,研究了各种条件对混合菌产絮凝剂的影响.结果表明,混合菌MBFH产絮凝剂的最佳培养条件为:温度30℃、初始pH8.0、摇床转速为120r/min、培养基含糖量2%、相对接种量15%,其对高岭土悬浊液的絮凝率可达到88%.图5表4参9     

混合菌对石油的降解

从含油污水中分离得到4株能高效降解石油的微生物菌株(X2、X3、X4、X5),经鉴定,4株菌分别属于黄单胞菌属(Xanthomonas sp.)、动胶菌属(Zoogloea sp.)、芽孢杆菌属(Bacillus sp.)和邻单胞菌属(Plesiomonas sp.).通过观察4株菌在原油培养基中的生长变化过程,确定了其中的优势菌;并对4株菌进行复配实验以确定各株菌混合后的石油降解效果;用正交实验法确定达到最佳石油降解效果各菌的投加量;通过对残油的Gc-MS测定分析,确定各菌在降解石油时所起的作用.结果表明,混合菌株中菌X4为优势菌,且有高的降解效果(达68,60％),其它3株降解率不高的菌混合投加也能达到较高的降解效果(达63.17％),菌X4是混合菌株维持高降解率的关键;达到最佳降解效果的各菌投加量分别为0.1％、0.1％、0.5％、2.0％;菌X2和菌X3降解C12-C16直链烃和少量支链烃,菌X4和菌X5对C12-C22直链烃有好的降解效果.图2表4参10     

一体化间歇曝气完全混合活性污泥法

一体化间歇曝气完全混合活性污泥法处理装置采取特殊的沉淀区构造,改变了活性污泥的循环流动方式,通过间歇曝气,反应区交替处于好氧/缺氧状态,达到了有机物高效去除、高效硝化反硝化及控制污泥膨胀的效果.该方法具有出水水质好、运行稳定、能耗低、流程简洁和操作管理方便的特点,是一种很有发展潜力的一体化中小型生活污水、城市污水处理系统.     

混合型污水处理厂原位生物强化脱氮中试及微生物群落结构分析研究

针对混合型污水处理厂进水水质波动大、C/N低、总氮稳定达标困难等共性问题,开发出适宜于低C/N、贫营养等苛刻环境条件的高效脱氮菌剂.现场中试结果表明:经过脱氮菌强化后,生化系统脱氮效率提升8.5百分点,出水平均总氮较强化前下降3 mg/L,出水水质稳定性明显提升,生物强化效果显著.在不补加碳源条件下,深度处理出水总氮完...