复合功能树脂吸附处理2-氨基吡啶生产废水的研究

采用中和法对2-氨基吡啶生产废水进行预处理,然后采用NDA-88复合功能吸附树脂固定床工艺对预处理过的废水进行动态吸附和脱附.实验结果表明,NDA-88树脂对2-氨基吡啶的吸附量为150.1 mg/g.每个周期处理废水30 BV(床体积),前12 BV出水COD由2 800mg/L降至100mg/L以下,后18BV出水...     

新试剂NBTDAPNP的合成及与镉的显色反应

阐述了新试剂 6 -硝基 -苯并噻唑 -重氮氨基 - 4-硝基苯的合成方法、结构鉴定、分析性能及在光度分析中的应用。该试剂对镉有很高的显色灵敏度 ,ε4 55可达 2 43× 10 5L/mol·cm ,用分光光度法可直接测定水样中镉 ,与原子吸收光谱法结果一致。     

2,6-二氨基蒽醌/石墨烯复合电极强化电吸附Pb2+

电吸附高效去除水中重金属离子的关键在于开发性能优异的电极材料.采用2,6-二氨基蒽醌(DA)修饰还原氧化石墨烯(r GO),通过溶剂热法成功制备了DA@rGO复合电极,考察了复合电极的电化学性质及电吸附Pb~(2+)性能.循环伏安测试表明,复合电极电化学性质优异,比电容在电流密度为1 A·g-1时达到304. 4 F·g-1,DA修饰显著提高了复合电极的赝电容.电吸附Pb~(2+)测试表明,施加电压为-1. 2 V时电吸附效果最优,反应60 min后Pb~(2+)去除率达94. 8%.电吸附过程符合一级动力学方程,Langmuir模型拟合得到Pb~(2+)的饱和吸附量为356. 66 mg·g-1,明显高于r GO电极(319. 40 mg·g-1),DA修饰引起的电容增加是复合电极Pb~(2+)吸附量提高的重要原因.使用0. 5 mol·L-1硝酸处理可使电极吸附的Pb~(2+)在5 min内脱附完全,实现吸附剂再生.经过10次电极吸附-脱附循环后,DA@rGO复合电极对Pb~(2+)的吸附去除率保持在88%左右,电极循环性能稳定.     

Performance of dithiocarbamate-type flocculant in treating simulated polymer flooding produced water

Produced water from polymer flooding is di cult to treat due to its high polymer concentration, high viscosity, and emulsified characteristics. The dithiocarbamate flocculant, DTC (T403), was prepared by the amine-terminated polyoxypropane-ether compound known as Je amine-T403. The product was characterized by IR spectra and elemental analysis. The DTC agent chelating with Fe2+ produced a network polymer matrix, which captured and removed oil droplets e ciently. Oil removal by the flocculent on simulated produced water with 0, 200, 500, 900 mg/L of partially hydrolyzed polyacrylamide (HPAM) was investigated for aspects of e ectiveness of DTC (T403) dosage and concentrations of HPAM and Fe2+ ions in the wastewater. Results showed that HPAM had a negative influence on oil removal e ciency when DTC (T403) dosage was lower than 20 mg/L. However, residual oil concentrations in tested samples with di erent concentrations of HPAM all decreased below 10 mg/L when DTC (T403) dosage reached 30 mg/L. The concentration of Fe2+ in the initial wastewater had a slight e ect on oil removal at the range of 2–12 mg/L. Results showed that Fe3+ could not be used in place of Fe2+ as Fe3+ could not react with DTC under flocculated conditions. The e ects of mineral salts ions were also investigated.