液膜法提取水溶液中的苯胺

本文研究了用煤油－磷酸三丁酯－Ｓｐａｎ８０－脂肪酸酯－ＨＣｌ溶液制成的液膜体系从水中溶液中提取苯胺的过程。并对溶剂和表面活性剂的选择及用量,搅拌速度,Ｒｉｅ,Ｒｅｗ,外相ｐＨ的选择进行了和系列的研究。结果表明,该法既适用于高浓度又适于低浓度的苯胺水溶液的处理。     

硝酸盐氮,亚硝酸盐氮总量紫外吸收快速测定

水体中尤其是海水中硝酸盐氮的测定较繁琐,干扰物质多,分析时间长,重现性差,准确性不高。文章通过实验介绍一种省时、省力、简便可行不消耗化学试剂且抗氯化物干扰、精度和准确度较高的硝酸盐氮、亚硝酸盐氮总量测定方法。     

铬、镉、铅胁迫对青菜叶片几种生理生化指标的影响

研究了溶液培养条件下铬、镉、铅胁迫对青菜叶片细胞膜透性、叶绿素含量和游离脯氨酸含量等的影响,结果表明：随着Ｃｒ＾６＋,Ｃｄ＾２＋,Ｐｂ＾２＋处理时间的延长和处理浓度的增加,青菜叶片细胞膜透性显著增大,叶绿素ａ／ｂ值逐渐降低,游离脯氨酸含量明显增加,其中游离脯氨酸含量增加的时间比细胞膜透性增大明显超前,而叶绿素ａ／ｂ植降低的时间在这３种重金属中未见明显的规律性。     

Di（2-ethylhexyl）phosphoric acid-coconut oil supported liquid membrane for the separation of copper ions from copper plating wastewater

Permeation of Cu(II) from its aqueous solution through a supported liquid membrane (SLM) containing di(2-ethylhexyl)phosphoric acid (D2EHPA) carrier dissolved in coconut oil has been studied. The effects of Cu(II), pH (in feed), H2SO4 (stripping) and D2EHPA (in membrane) concentrations have been investigated. The stability of the D2EHPA-coconutoil has also been evaluated. High Cu(II) concentration in the feed leads to an increase in flux from 4.1 × 10-9 to 8.9 × 10-9 mol/(m2·s) within the Cu(II) concentration range 7.8×10-4-78.6×10-4 mol/L at pH of 4.0 in the feed and 12.4 × 10-4 mol/L D2EHPA in the membrane phase. Increase in H2SO4 concentration in strip solution leads to an increase in copper ions flux up to 0.25 mol/L H2SO4, providing a maximum flux of 7.4 × 10-9 mol/(m2·s). The optimum conditions for Cu(II) transport are, pH of feed 4.0, 0.25 mol/L H2SO4 in strip phase and 12.4 × 10-4 mol/L D2EHPA (membrane) in 0.5 (m pore size polytetrafluoroethylene (PTFE) membrane. It has been observed that Cu(II) flux across the membrane tends to increase with the concentration of copper ions. Application of the method developed to copper plating bath rinse solutions has been found to be successful in the recovery of Cu(II). rane. It     

富氧助燃技术减少NOx排放

富氧助燃技术是最新节能环保技术,可以用于各种燃料和多种窑炉.不但显著节能、增产,而且能延长炉龄,环保达标,通常几个月就能收回全部投资.富氧燃烧能有效地降低NOx的排放量,在环境问题得到日益重视的今天富氧助燃技术具有显著的经济意义和社会意义.先介绍其节能和环保的机理,然后再介绍有关典型工艺流程、技改要点和典型应用实例.并对热力型NOx的生成进行了探讨.     

高效选择性除铯的PVDF复合膜制备及优化

为实现对放射性核素铯(Cs)的高效去除,本研究基于表面接枝技术利用均苯三甲酰氯(TMC)在羟基化的PVDF微滤/超滤膜表面接枝了一层氨基化SiO2,并通过SiO2表面的氨基基团与Fe3+结合实现亚铁氰化铁(Ferrocyanide,FeCN)的负载,从而制备了FeCN/SiO2/PVDF复合膜.基于膜表面的SEM与XP...     

污水中磷酸盐的离子交换分离初探

在日化工业磷酸盐解析方法的基础上,针对污水中各磷酸盐含量特征,对树脂床高度、淋洗液流速和用量等因素作了选择研究,确定了分离污水中各种磷酸盐及测定其含量的条件和步骤。     

Impact factors of the degradation of bisphenol A by nitrocellulose membrane under illumination

Nitrocellulose membrane (NCM) can produce hydroxyl radicals under illumination, which promotes the oxidative degradation of organic pollutants. In this paper, NCM was used to oxidize bisphenol A (BPA) under simulated sunlight. The effects of pH, temperature, light intensity, anion and cation on the degradation of BPA were analyzed. The photodegradation process of BPA was discussed. The optimal photolysis rate was 0.031 min^?1 when the temperature was 30°C, the light intensity was 2.67 × 10⁴ Lux, and the pH value was 9.0. The alkaline environment, temperature and light intensity can promote the photodegradation of BPA. Except for nitrate ions, anions and cations can inhibit the photodegradation of BPA. Compared with cations, anions have a greater inhibitory effect on BPA degradation. The degradation products of BPA by NCM were analyzed by gas chromatographic/mass. This study may provide useful information for the BPA degradation by NCM in complex water samples.     

壳聚糖聚乙二醇活性炭共混超滤膜制备及性能研究

研究了壳聚糖制备超滤膜,以及致孔剂聚乙二醇(PEG400)、活性炭含量对膜的水通量和截流率的影响。发现PEG的加入大大提高了壳聚糖超滤膜的纯水透过率和对牛白蛋白溶液的截流率。加入活性炭也同样可以提高膜的纯水通量和截流率。结果表明,选择投加5μL(每100mL铸膜液添加5μLPEG)的水溶性PEG400为致孔剂所制得的膜的水通量和截留率最理想。将此膜应用到洗浴废水上,COD去除率达到75%。     

印染废水处理的磁混凝-高梯度磁分离协同作用

混凝过程作为工业废水的预处理技术普遍受到重视,在混凝过程中降低污泥产生量并提高污泥分离速度是该技术发展的方向,基于上述目标,通过将磁粉引入絮体使之磁化并在自行研制的高梯度磁分离装置中实现磁混凝与磁分离的协同作用.以高浊度的印染废水作为试验废水,以色度、COD及SS作为考核指标,重点考察了磁混凝反应及磁分离的影响因素.当印染废水的色度约为900倍、COD约为595 mg/L、SS约为500 mg/L时,在pH=8.5、FeSO4500 mg/L、PAM3.5 mg/L、磁粉400 mg/L的适宜磁混凝反应条件下,相应指标去除率比传统混凝法分别高出17.3%、21.7%及24.2%,此时絮团沉降速度增大了64.3%,污泥体积减少了61%,污泥压缩比为0.39.在电流强度8 A、流速2.5 L/min和介质填充率1%的操作条件下,该磁性絮体流经高梯度磁分离装置时的水力表面负荷达到61.0 m3/m2·h,处理出水达到国家二级排放标准.