光催化剂SrTiO3的制备及其性能的研究

论述用化学液相共沉淀法制备SrTiO_3的最佳条件,及在不同的活化条件下对SrTiO_3光催化性能的影响。此外还研究了掺入过渡金属氧化物对SrTiO_3催化性能的改善。     

溴化十六烷基三甲铵膨－润土对印染废水的脱色作用

试验了ＣＴＭＡＢ－膨润上处理印染废水的最佳条件，发现它对印染液的脱色率明显高于原土；并将ＣＴＭＡＢ－膨润土与Ａｌ２（ＳＯ４）３联用处理实际印染废水，脱色率达８７．５％，且能降低其ＣＯＤ值。     

CDs/ZnO/g-C3N4三元组份协同作用促进光催化降解染料

采用浸渍-热聚合法制备CDs/ZnO/g-C3N4复合材料，考察其对罗丹明B的光降解效率。利用 XRD、TEM、XPS、UV-Vis DRS、FI-IR等手段对催化剂进行表征和评价。结果表明：CDs/ZnO/g-C3N4仍保持石墨相g-C3N4的晶型结构，三元组份相互协同作用使CDs/ZnO/g-C3N4表现出优异的光催化性能，其降解罗丹明B的效果优于单体g-C3N4、ZnO及ZnO/g-C3N4，脱色率可达到70%左右。     

脱色树脂在木糖脱色中的应用

介绍了脱色树脂在木糖液中的脱色性能，同时提出了脱色树脂脱色的最佳工艺条件。并且脱色树脂应用于木糖液脱色，既简化了生产工艺，又降低了工人的劳动强度，具有较好的现实意义。     

染色废水的还原脱色及其回用

使用还原型双组分脱色剂对含有不同种类水溶性染料的染色废水进行脱色处理，重点研究了脱色剂用量、反应温度、pH值和时间对脱色反应的影响。并且将脱色后的染色废水回用于织物染色中，在染料的上染速率曲线和颜色特征方面进行了比较。结果表明，随着脱色刑用量的增加，染色废水的脱色率都逐渐升高：中性pH条件和温度的升高均可以促进染色废水的脱色；在60℃～700℃，脱色率可达到90％；在常温下3～5分钟内完成脱色，而直接染料不超过15分钟，脱色废水能够回用于织物染色中，染料的上染曲线几乎没有变化，染色深度和色差变化极小。     

Chlorophyll adsorption on acid-activated clay

An acid-activated clay (Çanakkale montmorillonite from Turkey) was used to adsorb chlorophyll from hexane solutions. The phenomenon seems to be mainly driven by the interaction of chlorophyll with acid sites. The adsorption of chlorophyll on Brönsted acid sites was indicated by a characteristic infrared band for the -OH group at 3671 cm^?1. The variations in the structure of clay mineral and chlorophyll during adsorption have been examined by differential thermal analysis, thermogravimetry and infrared spectroscopy of the activated clay before and after adsorption of chlorophyll. Oxidation of adsorbed chlorophyll was completed at quite a high temperature.     

电化学氧化与还原联合处理偶氮染料废水的效能

以Sb掺杂Ti/SnO2电极为阳极,铝板为阴极,设计了一种电化学氧化与电化学还原联合作用反应器.以浓度为100mg/L甲基橙模拟废水为研究对象,探究了电化学氧化与电化学还原联合作用的处理效能,并运用紫外-可见吸收光谱初步探究了甲基橙的降解机理.结果表明:在电流密度为20 mA/cm2、电解质浓度为0.10mol/L条件下,先电化学还原反应60 min再电化学氧化60 min联合处理甲基橙模拟废水,甲基橙的脱色率为94%,COD去除率为85%,处理能耗为0.21k Wh/g(COD).降解前后的紫外-可见吸收光谱的变化表明,电化学联合作用先使甲基橙的偶氮键断裂,然后破坏其苯环共轭体系,从而使甲基橙降解.     

羧甲基壳聚糖处理印染废水实验研究

目的 研究羧甲基壳聚糖（CM-CHO）处理水溶性染料废水脱色的工艺条件，为实际印染废水的脱色处理提供参考数据．方法 采用羧甲基壳聚糖对活性红染料溶液和毛巾厂的印染废水进行混凝处理，通过研究pH值、投加量、沉降时间和搅拌强度对脱色效果的影响。确定适宜的操作条件；同时对比了羧甲基壳聚糖和壳聚糖对实际废水的处理效果。结果 实验表明，pH、投加量和沉降时间对脱色效果影响很大，而快速和慢速搅拌时间对其影响不明显．结论 羧甲基壳聚糖对水溶性染料废水及实际印染废水具有良好的脱色效果．对水溶性染料废水，在pH=9．0，投加量在50mg／L下有最好的脱色效果。脱色率达90％以上，在相同的工艺条件下，羧甲基壳聚糖处理效果优于壳聚糖，羧甲基壳聚糖对印染废水的混凝处理可作为实际废水处理的前处理。     

Degradation of 1‐amino‐4‐bromoanthraquinone‐2‐sulfonic acid using combined airlift bioreactor and TiO2‐photocatalytic ozonation

BACKGROUND: Traditional treatment systems failed to achieve efficient degradation of anthraquinone dye intermediates at high loading. Thus, an airlift internal loop reactor (AILR) in combination with the TiO₂‐photocatalytic ozonation (TiO₂/UV/O₃) process was investigated for the degradaton of 1‐amino‐ 4‐bromoanthraquinone‐2‐ sulfonic acid (ABAS). RESULTS: The AILR using Sphingomonas xenophaga as inoculum and granular activated carbon (GAC) as biocarrier, could run steadily for 4 months at 1000 mg L^?1 of the influent ABAS. The efficiencies of ABAS decolorization and chemical oxygen demand (COD) removal in AILR reached about 90% and 50% in 12 h, respectively. However, when the influent ABAS concentration was further increased, a yellow intermediate with maximum absorbance at 447 nm appeared in AILR, resulting in the decrease of the decolorization and COD removal efficiencies. Advanced treatment of AILR effluent indicated that TiO₂/UV/O₃ process more significantly improved the mineralization rate of ABAS bio‐decolorization products with over 90% TOC removal efficiency, compared with O₃, TiO₂/UV and UV/O₃ processes. Furthermore, the release efficiencies of Br^? and SO₄^2? could reach 84.5% and 80.2% during TiO₂/UV/O₃ treatment, respectively, when 91.5% TOC removal was achieved in 2 h. CONCLUSION: The combination of AILR and TiO₂/UV/O₃ was an economic and efficient system for the treatment of ABAS wastewater. © 2012 Society of Chemical Industry     

铝炭微电解处理刚果红废水的脱色动力学研究

采用铝炭微电解法处理刚果红废水。动力学研究结果表明,铝炭微电解降解刚果红的脱色过程符合表观二级动力学方程。刚果红脱色反应速率随着溶液初始p H、铝粉投加量、温度、摇床转速的增大而提高,随着铝炭质量比的降低先提高后降低。在温度为15~35℃范围内刚果红脱色反应活化能为17.75 k J/mol。采用铝炭微电解法处理某纺织印染公司实际印染废水,实验表明,在p H为11~12范围内,废水COD去除率不低于50%,反应后出水基本无颜色。