用次氯酸钠法处理选矿废水

采用次氯酸钠法处理铅锌硫化矿选矿废水，考察了废水初始pH、NaClO加入量及反应时间对选矿废水COD去除率的影响。在废水pH为4、NaClO加入量为100g/L、反应时间为30min的条件下，选矿废水的COD去除率可达到98．3％；当pH为11、反应时间为10min、NaClO加入量为1g/L时，选矿废水的COD去除率为39．4％。     

顶空气相色谱法测定食品中甜蜜素含量

采用顶空气相色谱法测定食品中甜蜜素含量,探讨了气液相平衡条件及色谱条件的选择,实验结果表明甜蜜素的标准溶液在0.1-0.4μg/l范围内具有良好的线性关系,回收率为87.5%-101.8%,相对标准偏差为2.6%.     

水杨酸法检测水质氨氮的改进方法

该氨氮检测方法是对水杨酸分光光度法的改进,通过将50 g/L的水杨酸改为150 g/L的水杨酸钠,将有效氯为3. 5 g/L的次氯酸钠溶液改为5 g/L的二氯异氰尿酸钠溶液,增加了检测试剂的稳定性和贮存时间,同时将氨氮测定上限从1 mg/L提高至2. 5 mg/L,并将显色时间从60 min优化为30 min,使得此方法更为便捷。该方法的氨氮标准曲线线性关系良好,相关系数为0. 999 6,准确性和精密度高,加标回收率良好,适用于不同类型水质中氨氮的检测。     

水杨酸钠-次氯酸钠法海水氨氮快速检测方法研究

对水杨酸钠-次氯酸钠法测量海水氨氮化学分析条件进行了研究。通过正交实验对水杨酸钠-次氯酸钠法试剂配比进行优化,并确定了最佳试剂配比。同时,用水杨酸钠-次氯酸钠法和靛酚蓝法测量24个海水水样,测量结果无显著差异。在反应温度为35℃,反应时间为10 min时,用改进后的方法分别测量60、120μg/L的氨氮标准溶液,相对标准偏差分别为4.0%、2.8%,回收率分别为99.8%、100.8%。该方法试剂无毒、环保,操作简单、快速,可满足营养盐自动分析仪现场快速测量的要求,提高仪器的环境友好性。     

污水处理厂消毒技术对抗生素抗性菌的强化去除

基于消毒技术对污水处理厂出水中总异养菌(total heterotrophic bacteria,HPC)及5种抗生素抗性菌(antibiotic resistant bacteria,ARB):氨苄霉素抗性菌(AMP)、红霉素抗性菌(ERY)、四环素抗性菌(TET)、卡那霉素抗性菌(KAN)、环丙沙星抗性菌(CIP)的去除情况研究,分析消毒技术对ARB的强化去除效果.结果表明,实际污水处理厂的紫外消毒对ARB去除率仅为18.2%~40.9%,且AMP含量最高;另外,消毒技术对ERY有选择性去除效果,对其他4种ARB无明显选择性去除效果(P0.05);最后结合次氯酸钠、臭氧、紫外消毒处理对COD、NH_4~+-N的去除效果,确定强化去除ARB的消毒方式中臭氧,次氯酸钠和紫外的最佳浓度和剂量依次为5.0 mg·L~(-1)、25.0 mg·L~(-1)和45.0 m J·cm~(-2),ARB去除率依次为45.5%~74.5%、66.1%~85.5%、68.6%~85.5%,另外次氯酸钠耦合紫外消毒强化去除ARB的效果更佳.     

过硫酸钠原位修复三氯乙烯污染土壤的模拟研究

以过硫酸钠(Na₂S₂O₈)为氧化剂,柠檬酸(CA)螯合Fe(Ⅱ)溶液作为活化剂,建立箱体模型模拟场地三氯乙烯(TCE)污染土壤的原位化学氧化修复.结果表明,经CA螯合Fe(Ⅱ)活化的Na₂S₂O₈能较好的修复TCE污染土壤,持续氧化27 d后TCE浓度降到10 mg·kg^-1以下;采用抽出氧化、循环再用的方式,地下水TCE浓度到45 d时降到21.4 μg·L^-1.同时,氧化过程中过硫酸钠会产生SO₄^2-,使土壤和地下水的pH降低;土壤有机质含量下降约10.1%.     

改良型固定化Pseudomonas oleovorans DT4降解四氢呋喃的研究

成功构建出了新型的海藻酸钠-活性炭纤维复合固定化Pseudomonas oleovorans DT4来去除四氢呋喃,并优化了该复合固定化载体组分的含量,发现在海藻酸钠含量为3%,活性炭纤维含量为1.5%条件下,制备成细胞浓度为6×109g-1的协同固定化细胞在初始THF浓度为360 mg·L-1时的降解速率达到最大为24.0 mg·(L.h)-1,同时其机械强度也得到了显著的提升.此外与游离菌体相比,该固定化细胞在不同温度和pH条件下的降解速率表现得更加稳定,且去除效果均能稳定在80%以上.在改进的反应体系中,协同固定化小球高效降解THF的重复利用次数达到80批以上,显示出该载体良好的可行性.     

Supercritical water oxidation of polyvinyl alcohol and desizing wastewater：Influence of NaOH on the organic decomposition

Polyvinyl alcohol is a refractory compound widely used in industry. Here we report supercritical water oxidation of polyvinyl alcohol solution and desizing wastewater with and without sodium hydroxide addition. However, it is difficult to implement complete degradation of organics even though polyvinyl alcohol can readily crack under supercritical water treatment. Sodium hydroxide had a significant catalytic effect during the supercritical water oxidation of polyvinyl alcohol. It appears that the OH ion participated in the C-C bond cleavage of polyvinyl alcohol molecules, the CO2-capture reaction and the neutralization of intermediate organic acids, promoting the overall reactions moving in the forward direction. Acetaldehyde was a typical intermediate product during reaction. For supercritical water oxidation of desizing wastewater, a high destruction rate (98.25%) based on total organic carbon was achieved. In addition, cases where initial wastewater was alkaline were favorable for supercritical water oxidation treatment, but salt precipitation and blockage issues arising during the process need to be taken into account seriously.     

Oxidation inhibition of sulfite in dual alkali FGD system

A laboratory-scale well-mixed thermostatic reactor with continuously blasting air was used to investigate the oxidation inhibition of sulfite in dual alkali flue gas desulfurization （FGD） system. The effects of operating parameters such as pH value and catalyst concentration on the oxidation were studied. Sodium thiosulfate was used in the system, and was found that it significantly inhabited the sulfite oxidation. In the absence of catalyst, sodium thiosulfate at 12.67 mmol/L had an inhibition efficiency of approximately 98%. While in the presence of catalyst, sodium thiosulfate at 26.72 mmol/L had an inhibition efficiency less than 85.0%. The oxidation reaction order of sulfite in the sodium thiosulfate was determined to be -1.90 and 4）.55 in the absence and presence of the catalyst, respectively. Apparent activation energy of oxidation inhibition was calculated to be 53.9 kJ/mol. Pilot tests showed that the consumption rate of thiosulfate agreed well with the laboratory-scale experimental results.     

膨润土对复合污染中表面活性剂的吸附及机理

选取阳离子表面活性剂氯化十六烷基吡啶(CPC)、阴离子表面活性剂十二烷基苯磺酸钠(SDBS)及非离子表面活性剂Triton X-100(TX-100)为代表,研究了其在膨润土上的吸附行为,探讨了膨润土阳离子交换容量(CEC)、温度、盐度对CPC吸附的影响.结果表明,Na基膨润土对CPC的吸附性能最好,对SDBS基本无吸附,对TX-100的吸附介于两者之间.Na基膨润土对CPC的吸附是阳离子交换和疏水键缔合共同作用的结果,对TX-100的吸附主要是通过其与膨润土硅氧表面间的氢键作用,同时通过疏水键作用形成吸附双分子层;SDBS在Ca基膨润土上的吸附损失量先增大后减小,在1.5倍临界胶束浓度 (CMC)时达到极大值,主要机理是SDBS与膨润土中的Ca²⁺产生沉淀作用,而胶束具有再溶解沉淀的作用.膨润土对CPC的吸附量随着温度升高而降低,随着CEC的增大而增大,一定浓度NaCl的加入有利于其在膨润土上的吸附.