三维电极对水中染料降解脱色处理

研究了在传统二维电解槽的铁板电极之间填充锰砂并鼓气搅拌，得到三相三维电极流化床反应器，对比两种反应器对酸性大红3R染色模拟废水降解脱色作用，考察了槽电压、支持电解质质量浓度、反应时间等因素对两种反应器处理染料脱色率的影响。实验表明，这些因素对酸性大红3R的降解脱色均有不同程度的影响，在相同条件下，三相三维电极流化床反应器比二维电极电解槽的处理脱色速度快和处理效率高，在不同处理时间内，脱色率可提高30％～50％。紫外-可见光吸收光谱分析表明，该方法不仅能对酸性大红3R的生色基团进行降解脱色，且对萘环不饱和共轭体系也具有破坏降解作用。     

中性条件下超声波/零价铁协同降解活性艳红X-3B

考察了中性条件下超声波降解、零价铁还原及超声波-零价铁联用对活性艳红X-3B模拟废水的降解效果,通过对比降解过程中UV-Vis光谱的变化,探讨了超声波-零价铁协同处理活性艳红X-3B的可行性.结果表明,在中性条件下超声波对活性艳红X-3B降解缓慢,经过25min辐射后,活性艳红X-3B的分解率不足7.5%;零价铁直接还原速率较慢,反应25min后,活性艳红X-3B的分解率仅为48.82%;"超声波/零价铁"对降解活性艳红X-3B有明显的协同效应,25min后分解率达99.42%(600W),反应符合准一级动力学过程.与零价铁直接还原相比,在200W,400W和600W超声波的协同作用下,X-3B降解的表观反应速率常数分别提高了2.12,2.76和4.00倍,半衰期相应缩短.另外,添加H2O2会抑制协同效应.     

层状氢氧化镁铝对染料酸性橙Ⅱ的脱色性能

分别用层状氢氧化镁铝(LDHs)和焙烧层状氢氧化镁铝(CLDH)作为吸附剂,吸附脱除水溶液中染料酸性橙Ⅱ,考察了Mg/Al物质的量之比、吸附剂的投加量、脱色时间、初始pH值等因素对脱色率的影响.结果表明,以Mg/Al物质的量之比为3制得的层状氢氧化镁铝对酸性橙Ⅱ溶液的脱色效果最好;室温下,3.0 g·L-1LDHs和1...     

UV-vis/草酸铁/Fenton体系降解蒽醌染料

以活性艳蓝KN—R作为研究对象,考察了处理活性艳蓝KN-R的主要影响因素。在固定染料浓度为100 mg/L时,得到氧化体系的最佳用量比值为ρ(Fe2+):ρ(H2O2):ρ(H2C2O4)为1:15:1.5。在最佳条件下,脱色率达到95%以上,COD和TOC去除率分别达到87.7%和66.8%。活性艳蓝KN-R脱色的动力学模型为拟一级反应模型。     

酵母菌Y48对活性黑KN-B的脱色研究

从土壤中分离获得了一株对偶氮染料具有明显脱色效果的酵母菌Pseudozyma rugulosa Y48,其对初始浓度为100 mg·L-1的活性黑KN-B的最大脱色率可达99%.采用酵母菌Y48对偶氮染料脱色的优化控制条件是:接种量应不低于3%(体积分数);最适pH值在6-_9之间;氮源(NH4)2SO4的浓度不低于0...     

粒状纳米零价铁/炭的制备及对孔雀绿的降解机理

以活性炭粉末(PAC)为载体,在负载纳米零价铁(nZVI)后,利用高岭土作为黏合剂,制备了1cm大小的粒状纳米零价铁/炭颗粒(nZVI/PAC),对制备条件进行了优化,并采用X射线衍射(XRD)、透射电子显微镜(TEM)、氮吸附/脱附、热重法(TG)对合成对材料进行了表征,模拟了其对典型染料孔雀石绿(MG)的去除研究....     

真菌对染料的脱色研究进展

染料废水的任意排放不仅会造成自然水体的污染、水生动植物的死亡、生态系统的失衡,还会直接对人体产生危害.真菌对染料脱色的研究最早始于上世纪80年代,是目前生物法处理染料废水研究中的热点.本文主要从真菌染料脱色的多样性、真菌染料脱色机理以及真菌染料脱色的应用条件等3方面对真菌染料的脱色研究进展进行综述,探讨了不同种类真菌包括白腐真菌、霉菌、酵母菌等对染料的脱色作用,阐明了真菌吸附脱色、降解脱色的机理,介绍了真菌在染料脱色应用中的优势,并对未来真菌染料脱色研究的方向提出了展望.图1参42     

制备钙钛矿催化剂LaNiO3用于染料废水的降解脱色

为改善普通石墨电极的电催化性能,将以溶胶-凝胶法合成的钙钛矿氧化物LaNiO3混合其它原料做成气体扩散电极,用于电化学降解活性艳红X-3B,以脱色率来考核催化剂的氧还原活性.采用星点设计-效应面曲线法对催化剂制备工艺进行了优化,得出最佳工艺参数为:柠檬酸含量为金属离子物质的量的1.54倍,pH值为9.94,焙烧温度为824.39℃.采用X射线衍射(XRD)、动电位扫描等检测分析方法对所制备的催化剂进行表征和分析.结果表明,制备的催化剂晶相纯净、晶型完整、衍射峰强度较高,是较完整的钙钛矿结构;相比于普通石墨电极,掺杂催化剂的气体扩散电极极化阻力高,氧还原性能良好,有利于有机物的降解.     

零价铁活化过硫酸钠对偶氮染料4BS的脱色机理

以直接耐酸大红4BS为研究对象,利用零价铁(ZVI)活化过硫酸钠(PDS)对其进行脱色研究,考察了PDS浓度、ZVI浓度、pH、温度等对脱色的影响.结果表明,一定浓度的ZVI与PDS联合使用能促进大红4BS的脱色,在20 min时脱色率达98.79%,远高于使用单一药剂的效率,且反应符合准一级反应动力学方程.低pH有利于反应的进行,随着pH值降低,反应速率逐渐加快,在pH=10.42时,反应90 min仅脱色9.41%,而在pH=3.03时脱色率达95.57%.温度的升高虽然能加快大红4BS的脱色,但是会使PDS的利用率降低,当温度由20℃增大到60℃时,PDS的利用率降低12%,且温度对大红4BS降解速率的影响符合阿伦尼乌斯模型(R2=0.988),计算的活化能为14.44 k J·mol-1.分别以叔丁醇与异丙醇为分子探针的自由基清除实验显示:ZVI活化PDS降解大红4BS是以SO-4·为主导的自由基反应过程.     

球磨零价镁/石墨(ZVMg/C)降解水中三氯乙烯

利用机械球磨法制备了零价镁/石墨(ZVMg/C)材料,并将其用于水溶液中三氯乙烯(TCE)的降解.研究通过SEM、BET和XRD等分析手段解析了ZVMg/C的表面形态结构和成分组成;采用正交实验方法优化了ZVMg/C的制备参数,比较了石墨含量对材料性能的影响;并考察了ZVMg/C投加量、溶液初始pH和地下水中常见阴(C...     

Enhanced degradation of Orange II using a novel UV/persulfate/sulfite system

Environmental Chemistry Letters - UV-activated persulfate (PS) systems have been widely employed to remove organic contaminants. However, the heavy use of persulfate may lead to secondary...     

Enhanced reductive degradation of carbon tetrachloride by carbon dioxide radical anion-based sodium percarbonate/Fe(II)/formic acid system in aqueous solution

Complete CT degradation was achieved by SPC/Fe(II)/FA system.Formic acid established the reductive circumstance by producing CO₂·^–.CO₂·^– was the dominant active species responsible for CT degradation.CT degradation was favorable in the pH range from 3.0 to 9.0.SPC/Fe(II)/FA system may be suitable for CT remediation in contaminated groundwater.The performance of sodium percarbonate (SPC) activated with ferrous ion (Fe(II)) with the addition of formic acid (FA) to stimulate the degradation of carbon tetrachloride (CT) was investigated. Results showed that CT could be entirely reduced within 15 min in the system at a variety of SPC/Fe(II)/FA/CT molar ratios in experimental level. Scavenging tests indicated that carbon dioxide radical anion (CO2·^–) was the dominant reactive oxygen species responsible for CT degradation. CT degradation rate, to a large extent, increased with increasing dosages of chemical agents and the optimal molar ratio of SPC/Fe(II)/FA/CT was set as 60/60/60/1. The initial concentration of CT can hardly affect the CT removal, while CT degradation was favorable in the pH range of 3.0–9.0, but apparently inhibited at pH 12. Cl^– and HCO₃^– of high concentration showed negative impact on CT removal. Cl^– released from CT was detected and the results confirmed nearly complete mineralization of CT. CT degradation was proposed by reductive C-Cl bond splitting. This study demonstrated that SPC activated with Fe(II) with the addition of FA may be promising technique for CT remediation in contaminated groundwater.     

Enhanced carbon tetrachloride degradation by hydroxylamine in ferrous ion activated calcium peroxide in the presence of formic acid

• Complete CT degradation was achieved by employing HA to CP/Fe(II)/FA process. • Quantitative detection of Fe(II) regeneration and HO• production was investigated. • Benzoic acid outcompeted FA for the reaction with HO•. • CO₂•⁻ was the dominant reductive radical for CT removal. • Effects of solution matrix on CT removal were conducted. Hydroxyl radicals (HO•) show low reactivity with perchlorinated hydrocarbons, such as carbon tetrachloride (CT), in conventional Fenton reactions, therefore, the generation of reductive radicals has attracted increasing attention. This study investigated the enhancement of CT degradation by the synergistic effects of hydroxylamine (HA) and formic acid (FA) (initial [CT] = 0.13 mmol/L) in a Fe(II) activated calcium peroxide (CP) Fenton process. CT degradation increased from 56.6% to 99.9% with the addition of 0.78 mmol/L HA to the CP/Fe(II)/FA/CT process in a molar ratio of 12/6/12/1. The results also showed that the presence of HA enhanced the regeneration of Fe(II) from Fe(III), and the production of HO• increased one-fold when employing benzoic acid as the HO• probe. Additionally, FA slightly improves the production of HO•. A study of the mechanism confirmed that the carbon dioxide radical (CO₂•⁻), a strong reductant generated by the reaction between FA and HO•, was the dominant radical responsible for CT degradation. Almost complete CT dechlorination was achieved in the process. The presence of humic acid and chloride ion slightly decreased CT removal, while high doses of bicarbonate and high pH inhibited CT degradation. This study helps us to better understand the synergistic roles of FA and HA for HO• and CO₂•⁻ generation and the removal of perchlorinated hydrocarbons in modified Fenton systems.     

Enhanced degradation of trichloroethene by calcium peroxide activated with Fe(III) in the presence of citric acid

Trichloroethene (TCE) degradation by Fe(III)-activated calcium peroxide (CP) in the presence of citric acid (CA) in aqueous solution was investigated. The results demonstrated that the presence of CA enhanced TCE degradation significantly by increasing the concentration of soluble Fe(III) and promoting H₂O₂ generation. The generation of HO? and O₂^-? in both the CP/Fe(III) and CP/Fe(III)/CA systems was confirmed with chemical probes. The results of radical scavenging tests showed that TCE degradation was due predominantly to direct oxidation by HO?, while O₂^-? strengthened the generation of HO? by promoting Fe(III) transformation in the CP/Fe(III)/CA system. Acidic pH conditions were favorable for TCE degradation, and the TCE degradation rate decreased with increasing pH. The presence of Cl^-, HCO₃^-, and humic acid (HA) inhibited TCE degradation to different extents for the CP/Fe(III)/CA system. Analysis of Cl^- production suggested that TCE degradation in the CP/Fe(III)/CA system occurred through a dechlorination process. In summary, this study provided detailed information for the application of CA-enhanced Fe(III)-activated calcium peroxide for treating TCE contaminated groundwater.     

Enhanced degradation of the antibiotic tetracycline by heterogeneous electro-Fenton with pyrite catalysis

There is actually increasing concern about the accumulation of antibiotics, such as tetracycline, in soil and water bodies. There is therefore a need for efficient methods to degrade antibiotics and thus clean waters. Here we tested the degradation of tetracycline using the heterogeneous electro-Fenton-pyrite method and compared the results with the conventional electro-Fenton method. The reaction was performed with a boron-doped diamond or Pt anode and carbon-felt cathode allowing electrogeneration of H₂O₂ from O₂ reduction. Results show an increasing tetracycline mineralization using the following methods: anodic oxidation with electrogenerated H₂O₂, electro-Fenton and then electro-Fenton-pyrite using boron-doped diamond. Ion-exclusion HPLC revealed the complete removal of malic malonic, succinic, acetic, oxalic and oxamic acids. Nitrogen present in tetracycline was mainly mineralized in NH₄ ⁺. The higher efficiency of electro-Fenton-pyrite is explained by self-regulation of soluble Fe²⁺ and pH to 3.0 from pyrite catalyst favoring larger ^·OH generation from Fenton’s reaction.     

Enhanced degradation of trichloroethylene using bentonite-supported nanoscale Fe/Ni and humic acids

Nanoscale zero-valent iron, named nano-Fe⁰, is a reagent used to degrade trichloroethylene in groundwater. However, the efficiency of nano-Fe⁰ is moderate due to issues of dispersion and reactivity. As an alternative we synthesized bentonite-supported nanoscale Fe/Ni bimetals, named bentonite-Fe/Ni, to test the degradation of trichloroethylene in the presence of Suwannee River humic acids, as a representative of natural organic matter. 0.1 mmol/L trichloroethylene was reacted with 0.5 g/L of nano-Fe⁰, bentonite-Fe, Fe/Ni, and bentonite-Fe/Ni nanoparticles. Results show first that without humic acids the reaction rate constants k _obs were 0.0036/h for nano-Fe⁰, 0.0101/h for bentonite-Fe, 0.0984/h for Fe/Ni, and 0.181/h for bentonite-Fe/Ni. These findings show that bentonite-Fe/Ni is the most efficient reagent. Second, the addition of humic acids increased the rate constant from 0.178/h for 10 mg/L humic acids to 0.652/h for 40 mg/L humic acids, using the bentonite-Fe/Ni catalyst. This finding is explained by accelerated dechlorination by faster electron transfer induced by humic quinone moieties. Indeed, the use of 9, 10-anthraquinone-2, 6-disulfonate as a humic analogue gave similar results.     

Enhanced activation of peroxymonosulfate by CNT-TiO2 under UV-light assistance for efficient degradation of organic pollutants

CNT-TiO₂ composite is used to activate PMS under UV-light assistance. Superior performance is due to the enhanced electron-transfer ability of CNT. SO₄•⁻, •OH and ¹O₂ play key roles in the degradation of organic pollutants. In this work, a UV-light assisted peroxymonosulfate (PMS) activation system was constructed with the composite catalyst of multi-walled carbon nanotubes (CNT) - titanium dioxide (TiO₂). Under the UV light irradiation, the photoinduced electrons generated from TiO₂ could be continuously transferred to CNT for the activation of PMS to improve the catalytic performance of organic pollutant degradation. Meanwhile, the separation of photoinduced electron-hole pairs could enhance the photocatalysis efficiency. The electron spin resonance spectroscopy (EPR) and quenching experiments confirmed the generation of sulfate radical (SO₄•⁻), hydroxyl radical (•OH) and singlet oxygen (¹O₂) in the UV/PMS/20%CNT-TiO₂ system. Almost 100% phenol degradation was observed within 20 min UV-light irradiation. The kinetic reaction rate constant of the UV/PMS/20%CNT-TiO₂ system (0.18 min⁻¹) was 23.7 times higher than that of the PMS/Co₃O₄ system (0.0076 min⁻¹). This higher catalytic performance was ascribed to the introduction of photoinduced electrons, which could enhance the activation of PMS by the transfer of electrons in the UV/PMS/CNT-TiO₂ system.     

Sulfate-enhanced degradation of Rhodamine B in the hydrogen peroxide/hydroxylamine system

Environmental Chemistry Letters - Hydroxyl radicals are commonly produced either by metal activation or by using external energy. However, the application of these methods is limited by low working...     

Al~0-O_2体系降解活性黄3RS溶液

酸性条件下,采用Al0-O2体系对活性黄3RS染料溶液进行降解,考察了活性黄3RS的初始浓度,p H、Al0的浓度、温度、Fe2+浓度等因素对其降解率的影响.结果表明,在p H=2和Al0浓度为1 g·L-1时,对50 mg·L-1活性黄3RS的降解率最高,反应150 min时最高可获得92%的降解率;降解后其COD值由126.35 mg·L-1降至49.44 mg·L-1;温度升高,活性黄3RS的降解率提高,其表观反应活化能为108.262 k J·mol-1;动力学分析表明该过程为一级反应,反应速率常数kobs=1.2×10-2s-1;当向体系中加入Fe2+时,其降解速率加快.     

Enhanced triallyl isocyanurate (TAIC) degradation through application of an O3/UV process: Performance optimization and degradation pathways

• UV/O₃ process had higher TAIC mineralization rate than O₃ process. • Four possible degradation pathways were proposed during TAIC degradation. • pH impacted oxidation processes with pH of 9 achieving maximum efficiency. • CO₃^2– negatively impacted TAIC degradation while HCO₃^– not. • Cl^– can be radicals scavenger only at high concentration (over 500 mg/L Cl^–). Triallyl isocyanurate (TAIC, C₁₂H₁₅N₃O₃) has featured in wastewater treatment as a refractory organic compound due to the significant production capability and negative environmental impact. TAIC degradation was enhanced when an ozone(O₃)/ultraviolet(UV) process was applied compared with the application of an independent O₃ process. Although 99% of TAIC could be degraded in 5 min during both processes, the O₃/UV process had a 70%mineralization rate that was much higher than that of the independent O₃ process (9%) in 30 min. Four possible degradation pathways were proposed based on the organic compounds of intermediate products identified during TAIC degradation through the application of independent O₃ and O₃/UV processes. pH impacted both the direct and indirect oxidation processes. Acidic and alkaline conditions preferred direct and indirect reactions respectively, with a pH of 9 achieving maximum Total Organic Carbon (TOC) removal. Both CO₃^2– and HCO₃^– decreased TOC removal, however only CO₃^2– negatively impacted TAIC degradation. Effects of Cl^– as a radical scavenger became more marked only at high concentrations (over 500 mg/L Cl^–). Particulate and suspended matter could hinder the transmission of ultraviolet light and reduce the production of HO· accordingly.