有机磷阻燃剂生产废水预处理工艺研究

采用液膜萃取—酸析沉降—络合萃取组合工艺对有机磷阻燃剂生产废水进行预处理.最佳工艺条件为:液膜萃取时,液膜油相(表面活性剂与煤油的混合液)与内水相(H2SO4溶液)的体积比2∶1、乳化液膜与废水的体积比1∶8、废水pH 13.0,硫酸体积分数10％、煤油中表面活性剂质量浓度30 g/L、液膜萃取时间 15 min;酸析沉降时,废水pH l.0,酸析沉降时间30 min;络合萃取时,络合萃取剂(烷基叔胺N235与煤油的混合液)中烷基叔胺N235体积分数30％,络合萃取剂与废水的体积比1∶4,废水pH l.0,络合萃取时间30 min.在此最佳处理条件下,废水COD总去除率可达93％,吡啶去除率达99.9％以上,总磷去除率可达97％,BOD5/COD提高至0.32,有利于后续生化处理.     

Changes of organic acid exudation and rhizosphere pH in rice plants under chromium stress.

The effect of chromium (Cr) stress on the changes of rhizosphere pH, organic acid exudation, and Cr accumulation in plants was studied using two rice genotypes differing in grain Cr accumulation. The results showed that rhizosphere pH increased with increasing level of Cr in the culture solution and with an extended time of Cr exposure. Among the six organic acids examined in this experiment, oxalic and malic acid contents were relatively higher, and had a significant positive correlation with the rhizosphere pH, indicating that they play an important role in changing rhizosphere pH. The Cr content in roots was significantly higher than that in stems and leaves. Cr accumulation in plants was significantly and positively correlated with rhizosphere pH, and the exudation of oxalic, malic and citric acids, suggesting that an increase in rhizosphere pH, and exudation of oxalic, malic and citric acid enhances Cr accumulation in rice plants.     

德兴铜矿不同年份废石产酸规律研究

矿山选矿废石、尾矿在长期堆积过程中氧化产生的酸性废水会对环境造成严重危害.实验选取德兴铜矿1、5、10和20年废石进行产酸规律研究,静态评价结果显示,4种废石均有产酸潜势,且除1年废石以外均已产酸.为期9个月的动态评价结果表明,4个年份的废石pH均与电导率呈显著负相关,检出离子主要为氟化物、Cu2+、Zn2+、SO2-4、Fe3+.1年废石在整个实验进行中并未产酸,5、10年废石产酸稳定,20年废石产酸缓慢,可推断废石的产酸过程为:不产酸-高速产酸-稳定产酸-产酸速率下降.     

BI废水制取己二酸过程中分解反应催化剂的研究

以环己烷空气氧化装置产生的酸性洗涤废水(BI有机废水)为原料,通过分析不同条件下分解氧化产物组成,考察了分解反应催化剂种类、用量及分解反应时间对产物二元酸的分布及己二酸表观收率的影响。试验结果表明,在钴盐存在下使BI有机废水浓缩液回流反应120min以上,再经硝酸氧化可使由BI有机废水制取己二酸的表观收率达到BI有机废水总质量的10%～12%。     

安徽铜陵铜尾矿硫形态及硫同位素分布特征

分析讨论了安徽铜陵水木冲S和SP剖面尾矿砂的理化指标、硫形态变化和硫酸根硫同位素组成与分布特征.结果显示：S和SP剖面整体呈酸性,pH值为2.59~6.12和3.50~6.27,由下而上有明显的降低趋势;Eh随剖面由下至上明显升高,范围为66~457和-37~307mV;酸可挥发性硫（AVS）含量为0~62.36和0~3.44mg/g,黄铁矿硫（CRS）含量为0.70~32.30mg/g和0.17~5.39mg/g;AVS与CRS的变化趋势基本一致,随剖面自下而上减少,且AVS先于CRS被氧化.2个剖面元素硫（ES）含量为0~8.83和0~3.62mg/g,随深度变化无明显规律.硫酸根硫（SO₄^2--S）含量为8.44~66.34和8.48~29.87mg/g,自下而上呈降低趋势,且分别在剖面的氢氧化物薄膜层（11.5~16.5cm和18~54cm）出现高值区.2个剖面总硫（TS）含量为9.18~109.69和12.38~37.72mg/g,表层由于淋滤含量较低,底层变化则不大.位于斜坡上的SP剖面TS及各形态硫含量均低于S剖面,表明淋滤对硫含量影响更明显.硫酸根硫同位素δ³⁴S为-3.32‰~13.43‰和-3.08‰~1.80‰,S-9硫酸根δ³⁴S为13.43‰,指示其来自于伴生硬石膏,其余层位δ³⁴S偏负且变幅较小,指示其硫酸根主要来源于硫化物的氧化.     

软骨藻酸胶体金免疫层析检测试纸条的研制

制备软骨藻酸（DA）胶体金免疫层析快速检测试纸条,建立一种快速检测贝类食品中软骨藻酸含量的检测方法.采用柠檬酸三钠还原氯金酸法制备颗粒直径20 nm的胶体金;电镜鉴定后,确定胶体金标记软骨藻酸单克隆抗体的最佳条件并制备金标抗体;金标抗体喷涂在玻璃纤维垫上制成胶体金结合垫;软骨藻酸与牛血清蛋白（BSA）的偶联物构成的包被...     

生化黄腐酸对污染水体生物修复的强化作用

研究了生化黄腐酸（BFA）对污染水体生物修复的强化作用。生化黄腐酸能提高水体中微生物活性,加快微生物对目标污染物的降解。在污染水体生物修复强化作用的试验中,投加生化黄腐酸,CODCr、NH3-N、TP和浊度的去除率分别增加了29．47％、20．61％、35％和19．86％,同时有利于水体DO的提升。     

水环境中腐殖酸与镉离子结合作用的影响因素

通过测定不同化学条件下腐殖酸与镉离子作用后的游离态镉离子浓度及其结合率,研究各因素对腐殖酸与镉离子作用的影响。研究结果表明,pH值、离子强度、投加镉离子总浓度、腐殖酸浓度和反应温度均影响腐殖酸与镉离子的结合。pH值在4.5~6.5范围内,随pH值升高,腐殖酸与Cd²⁺的结合率增大,游离态Cd²⁺浓度减少。溶液的离子强度增大对结合反应有抑制作用。投加Cd²⁺总浓度的增大会导致结合态Cd²⁺浓度和游离态Cd²⁺浓度逐渐增加,而其结合率逐渐减小。腐殖酸浓度逐渐增大,使Cd²⁺和腐殖酸的结合率逐渐增大。在20℃~50℃范围内时,随反应温度升高,游离态Cd²⁺浓度逐渐减小,其结合率逐渐增加。     

Humic acid and free radical in environment of Kaschin-Beck disease areas

The humic acid contents in drinking water and soil in Kaschin-Beck disease areas were found more than that of non-disease areas in this research. Changes of free radical concentration in drinking water were agreed with that of humic acid contents in drinking water of Kaschin-Beck disease areas. A positive correlation of free radical concentration and humic acid content in drinking water has been shown (r=0.913) . The structure of I. R. spectra of humic acid under ultraviolet light has been changed. Thus it indicated that free radical was resulted from benzoqiunonyl groups of humic acid in environment.     

Degradation of acid fuchsine by a modified electro-Fenton system with magnetic stirring as oxygen supplying

The current modified electro-Fenton system was designed to develop a more convenient and e cient undivided system for practical wastewater treatment. The system adopted a cathode portion that employed magnetic stirring instead of common oxygen gas di usion or gas sparging to supply oxygen gas for the electrolyte solution. Key factors influencing the cathode fabrication and activity were investigated. The degradation of acid fuchsine with a self-made graphite-polytetrafluorethylene cathode was studied using a spectrophotometer. It was found that the cathode generated hydrogen peroxide with high current e ciency and the hydrogen peroxide yield of the cathode did not decay after 10 times reuse. With the Pt anode at a ferrous ion concentration of 0.5 mmol/L, a pH of 3, and using magnetic stirring, dye decolorization could be rapidly accomplished but the destruction of benzene rings and intermediates was fairly di cult. With a Fe anode, dye degradation was more complete.