Fe0体系降解2,4-二氯酚的影响因素及其反应机理

采用铁屑、炉渣及河砂混合介质降解2,4-二氯酚(2,4 - DCP)模拟废水,研究铁屑粒径、铁屑投加量、铁屑与炉渣配比、pH值等因素对2,4- DCP脱氯效果的影响,探讨Feo体系降解2,4- DCP的反应机理.结果表明,铁屑粒径、铁屑投加量、铁屑与炉渣配比、pH对2,4- DCP脱氯效果均有显著影响,在铁屑粒径为2～5mm、不改变废水pH、铁屑与炉渣质量比为31:9条件下,Feo体系对2,4- DCP去除率高达97％.2,4- DCP经脱氯后主要产物为2-氯酚、4-氯酚和苯酚,反应后废水的可生化性明显提高,利于后续的生物处理.     

pH值对＂Fe^0-厌氧微生物＂降解2,4-二氯酚的影响

考察pH值对Fe0与微生物联合降解2,4-二氯酚(2,4-DCP)的效果,结果表明:与微生物单独作用相比,其与Fe0的联合作用可促进污染物降解,且中性或偏碱性环境促进效果较酸性明显;"Fe0 微生物"体系中Fe0腐蚀产生的OH-可有效平衡葡萄糖发酵产酸,增强体系的缓冲能力,较好实现污染物的降解;联合体系对污染物的降解是Fe0的电子催化与微生物协同作用的结果;Fe0腐蚀产物中Fe2 居多,Fe3 较少,Fe2 对微生物降解2,4-DCP有稍微的促进作用.     

Fenton试剂氧化法修复2,4-二氯酚污染土壤的研究

在泥浆体系中采用Fenton试剂氧化法修复2,4-二氯酚(2,4-DCP)污染的土壤.在恒温、避光条件下,研究2,4-DCP在泥浆体系中的解吸作用,并考察过氧化氢、硫酸亚铁、pH值、水土比、磷酸二氢钾、腐殖酸(HA)等因素对2,4-二氯酚去除效率的影响.试验结果显示,2,4-DCP在泥浆体系中有较高的解吸速率;2,4-DCP的解吸效率与水土比有关,水土比越大,解吸效率越高.研究表明:Fenton试剂氧化法能够有效地去除土壤中的2,4-DCP,过氧化氢和铁的最佳质量比为5:1,最佳pH值范围为2-3;水土比越大,2,4-DCP的去除效果越好;在pH=3时,磷酸二氢钾浓度、腐殖酸投加量和催化剂种类对2,4-DCP的去除效率影响很小.     

共价三嗪有机框架材料对水中氯酚类污染物的光催化脱氯降解

利用共价三嗪有机框架材料(CTF-1)对4-氯酚(4-CP)、2,4-二氯酚(2,4-DCP)、2,4,6-三氯酚(2,4,6-TCP)和五氯酚(PCP)等4种不同氯原子取代数目的氯酚类污染物进行光催化降解研究,探讨了底物结构对氯酚脱氯降解效率的影响及机制.结果表明,氯酚脱氯降解过程明显受苯环氯原子取代数目的影响,氯原子数目越多,脱氯降解效率越高,氯原子数目与表观速率常数呈显著正相关,氯酚降解及脱氯速率均为：PCP>2,4,6-TCP>2,4-DCP>4-CP.对CTF-1光催化降解氯酚机制研究表明,活性物种在反应中不起作用,体系反应机制为针对氯酚上取代氯位点进行水解脱氯过程.本研究结果为深入揭示氯酚脱氯降解机制提供了理论依据,也为光催化技术处理卤代酚类废水提供了技术参考.     

不同氯酚催化氧化降解反应动力学

通过共沉淀法制备了Fe-Cu-柱撑黏土(Fe-Cu-PILC)催化剂,并以单氯酚、二氯酚、三氯酚作为模式化合物,研究了氯酚中氯原子取代数目、取代位置对其降解动力学的影响,并探讨了氯离子的存在对反应的影响,也基于费米分布函数对其降解动力学进行非线性拟合.结果显示,这种基于费米函数的半经验模型适用于模拟氯酚氧化降解动力学反应(R20.818).氯酚降解速率如下:3-氯酚(3-CP)3,5-二氯酚(3,5-DCP)2,3-二氯酚(2,3-DCP)3,4-二氯酚(3,4-DCP)2,5-二氯酚(2,5-DCP)4-氯酚(4-CP)2-氯酚(2-CP)2,4-二氯酚(2,4-DCP)2,4,6-三氯酚(2,4,6-TCP)2,6-二氯酚(2,6-DCP).氯酚降解过程明显受到苯环氯原子取代数目、取代位置的影响,且氯原子取代位置具有更重要的影响:氯原子取代数目相同时,间位氯越多,降解越快,邻、对位越多,降解越慢.这主要通过影响表观速率常数k和半衰期t*得以实现.3,5-DCP降解表观速率常数k高达18.17 h~(-1),半衰期为0.2 h,而2,6-DCP表观速率常数仅为0.64 h~(-1),半衰期为5.88 h.氯离子的存在对氯酚降解动力学过程产生不同程度的抑制作用,其中2,6-DCP、2,4,6-TCP的抑制作用最为明显,这主要是由于氯离子的存在延长了其半衰期(分别由5.88 h、4.29 h延长至9.00 h、5.99 h),而对3,4-DCP、3,5-DCP则几乎没有抑制作用.表明氯离子抑制邻位氯代程度高的氯酚降解而不抑制间位氯代程度高的氯酚降解.研究结果为深入揭示氯酚降解机理提供了理论基础,也为提高含酚废水降解速率提供了技术参考.     

Pd-Fe/C催化氯酚还原脱氯-氧化联合降解

以Pd和Fe为活性金属组分通过沉积沉淀法制备了负载型Pd-Fe/C双金属催化剂,针对氯酚类污染物进行催化还原脱氯和催化氧化的连续降解处理.通过ICP-MS、XRD和TEM对催化剂进行表征,证实0.5%Pd-0.5%Fe/C催化剂中活性金属组分Pd和Fe在载体表面分散性最好,催化剂比表面积达到718.8 m~2·g~(-1).在温和条件下,以水作为反应介质,研究了负载型Pd-Fe/C催化剂对4-氯苯酚(4-CP)和2,4-二氯苯酚(2,4-DCP)的连续降解过程和反应条件,以及催化剂的重复使用情况.考察了Pd和Fe的负载量及p H值对催化剂活性的影响,得到了最佳反应条件,以0.5%Pd-0.5%Fe/C为催化剂,20 min内完成4-CP和2,4-DCP的催化还原脱氯,产物都为苯酚;之后加酸调节pH=5,并加入H2O2继续进行催化氧化,苯酚被彻底降解为H_2O和CO_2,而且转化率在60 min内可以达到97.5%以上,从而实现4-CP和2,4-DCP的彻底降解.     

驯化的活性污泥强化降解土壤中氯酚的研究

以接种驯化的活性污泥为生物强化手段,在小型生物泥浆反应器中,研究了受氯酚污染土壤的修复情况.考查了添加驯化活性污泥对土壤中氯酚降解的强化效果,并对土壤中邻氯苯酚(2-CP)、对氯苯酚(4-CP)和2,4-二氯酚(2,4-DCP)在单一污染体系中的降解情况进行了研究.结果表明,在生物泥浆反应器中添加用邻氯苯酚(2-CP)驯化的活性污泥可以明显地促进土壤泥浆中2-CP的降解,是一种有效的强化手段.该方法对土壤中的4-CP和2,4-DCP也有较好的降解效果,对三种氯酚的降解速率由大到小的顺序为2-CP,4-CP,2,4-DCP.反应结束时,泥浆体系中剩余的氯酚基本都残留在土壤中,固液分离后的水相可以直接排放或者在土壤修复过程中循环利用.     

碳纳米管负载Pd基催化剂对水中2,4-二氯酚的催化加氢脱氯

对多壁碳纳米管(MWNTs)进行掺氮得到含氮的多壁碳纳米管N-MWNTs,分别以MWNTs和N-MWNTs为载体,采用浸渍法合成了催化剂Pd/MWNTs和Pd/N-MWNTs.使用透射电镜(TEM)、电感耦合等离子体发射光谱仪(ICP)、X射线衍射仪(XRD)、元素分析仪等对催化剂进行了表征,并对2,4-二氯酚(2,4-DCP)的液相催化加氢脱氯反应进行了研究.结果表明,Pd/N-MWNTs对2,4-DCP具有更高的催化活性;该反应体系的催化反应过程不受传质阻力的影响;2,4-DCP在催化剂上的加氢脱氯行为符合Langmuir-Hinshelwood模型,即2,4-DCP的还原脱氯受表面吸附所控制.     

Pd/Fe和Ni/Fe二元金属去除水体中莠去津的比较

对比Ni/Fe和Pd/Fe二元金属对莠去津的催化降解特性.结果表明,在相同反应条件下(C0=20.0mg·l-1,pH=3.0,金属添加量为1.0g),与Fe0相比,Pd/Fe对莠去津表现出比Ni/Fe更加明显的催化脱氯效果,反应75min,Fe0对莠去津的脱氯效率为7.09%,Ni/Fe达到99.11%,而Pd/Fe反应30min就能够100%还原莠去津.通过SEM,XRS和BET-N2测试,Pd以无定形状态分布在Fe0的表面,有利于比表面积的增大,Ni/Fe和Pd/Fe的比表面积分别为11.671和16.94m2·g-1;而且Pd/Fe对H2有非常强的吸附能力,1cm3的Pd在常温下能够吸附1000ml H2,最高能够达到2800ml.体系pH值对Ni/Fe和Pd/Fe催化莠去津的影响非常大,pH=2.0时, Pd/Fe反应15min能够100%降解莠去津;pH=3.0时,30min达到完全降解;pH=4.0和未调节pH条件下,75min的脱氯效率只有82.55%和46.5%.     

纳米零价铁对溶液中PCB77的降解及其影响因素

设计了以溶液初始pH值、3,3’,4,4’-四氯联苯(PCB77)初始浓度、纳米零价铁(Fe0)投加量、纳米零价硅(Si0)投加量、腐殖酸和环糊精浓度为影响因素的正交试验,研究纳米Fe0降解PCB77时各因素对反应体系中PCB77残留率、氢离子浓度及氧化还原电位变化的影响及其相互关系。结果表明,在溶液初始pH值为4.5,初始ρ(PCB77)为1 mg.L-1,纳米Fe0投加量为10 g.L-1,纳米Si0投加量为0,ρ(腐殖酸)为0.25 g.L-1,ρ(环糊精)为1 g.L-1时,反应2 h后,PCB77残留率最低,为35.2%。溶液初始pH值对反应体系中PCB77的残留率影响最大,纳米Fe0投加量次之;溶液初始pH值对反应体系中氢离子浓度变化影响最大,环糊精投加量次之;PCB77初始浓度对反应体系中氧化还原电位变化影响最大,纳米Fe0投加量次之。     

Degradation of chlorinated phenols by nanoscale zero-valent iron

Chlorophenols (CPs), as important contaminants in groundwater, are toxic and difficult to biodegrade. Recently nanoscale zero-valent iron received a great deal of attention because of its excellent performance in treating recalcitrant compounds. In this study, nanoscale zero-valent iron particles were prepared using chemical reduction, and the reductive transformations of three kinds of chlorinated phenols (2-CP, 3-CP, and 4-CP) by nanoscale zero-valent iron under different conditions were investigated. The transformation process of the CPs was shown to be dechlorination first, then cleavage of the benzene ring. The removal efficiency of the CPs varied as follows: 2-CP > 3-CP > 4-CP. The reactivity of CPs was associated with their energy of lowest unoccupied molecular orbit (E _LUMO). With the increase in initial concentrations of CPs, removal efficiency decreased a little. But the quantities of CPs reduced increased evidently. Temperature had influence on not only the removal efficiency, but also the transformation pathway. At higher temperatures, dechlorination occurred prior to benzene ring cleavage. At lower temperatures, however, the oxidation product was formed more easily.     

零价铁对土壤中4-氯苯酚还原脱氯研究

氯苯酚是常见的环境污染物，它们在土壤中的加速分解可以减少对人类健康的危害。以恒温培养为方法，GC-MS为检测手段，研究了在常温常压下土壤中4-氯苯酚(4-CP)在零价铁作用下的还原脱氯反应。结果表明：4-CP可以被来自零价铁的电子还原，零价铁能够有效促进土壤中的4-CP脱除苯环上的氯原子，从而达到降低毒性、增加可生化性目的。反应条件如初始pH、时间、零价铁用量等均对4-CP还原脱氯效率有重要影响，特别是当初始pH值控制在偏酸时更有利于反应的进行。在零价铁加入量500mg、初始pH=4、反应时间7d的条件下，零价铁对土壤中4-CP还原脱氯效率最高可以达到65％。利用实验数据，对零价铁作用下4-CP还原脱氯的反应机理也进行了初步探讨。     

Enhanced 4-chlorophenol biodegradation by integrating Fe2O3 nanoparticles into an anaerobic reactor: Long-term performance and underlying mechanism

• 4-chlorophenol biodegradation could be enhanced in Fe₂O₃ coupled anaerobic system. • Metabolic activity and electron transport could be improved by Fe₂O₃ nanoparticles. • Functional microbial communities could be enriched in coupled anaerobic system. • Possible synergistic mechanism involved in enhanced dechlorination was proposed. Fe₂O₃ nanoparticles have been reported to enhance the dechlorination performance of anaerobic systems, but the underlying mechanism has not been clarified. This study evaluated the technical feasibility, system stability, microbial biodiversity and the underlying mechanism involved in a Fe₂O₃ nanoparticle-coupled anaerobic system treating 4-chlorophenol (4-CP) wastewater. The results demonstrated that the 4-CP and total organic carbon (TOC) removal efficiencies in the Fe₂O₃-coupled up-flow anaerobic sludge blanket (UASB) were always higher than 97% and 90% during long-term operation, verifying the long-term stability of the Fe₂O₃-coupled UASB. The 4-CP and TOC removal efficiencies in the coupled UASB increased by 42.9±0.4% and 27.5±0.7% compared to the control UASB system. Adding Fe₂O₃ nanoparticles promoted the enrichment of species involved in dechlorination, fermentation, electron transfer and acetoclastic methanogenesis, and significantly enhanced the extracellular electron transfer ability, electron transport activity and conductivity of anaerobic sludge, leading to enhanced 4-CP biodegradation performance. A possible synergistic mechanism involved in enhanced anaerobic 4-CP biodegradation by Fe₂O₃ nanoparticles was proposed.     

Study of Fishes in the Chung-Kung Stream: Species Distribution and Organochlorine Pesticide Residues

Abstract

In this study, we investigated the potential for reductive dechlorination of 2,4-dichlorophenol (2,4-DCP), 2,4,6-trichlorophenol (2,4,6-TCP), and pentachlorophenol (PCP) by municipal sewage sludge adapted to 2,4-DCP at different concentrations. 2,4-DCP was completely dechlorinated within 4 weeks. After 18 weeks' incubation, 2,4,6-TCP was also completely dechlorinated and the residue of PCP was 0, 44.46, 51.96% at 0.5, 5, and 50 μg ml¹ respectively. the 2,4-DCP adapted communities initially removed the ortho-chlorine from PCP of 5.0, 50 μg ml¹, following an ortho < para < meta order of chlorine removal. Intermediate products were 3,4,5-TCP, 3,5-DCP, 3-CP (3-chlorophenol), phenol, benzoate and hexanoic acids, whereas PCP (0.5 μg ml¹) indicated a preference for meta-chlorine removal. the intermediate product of 2,4,6-TCP at three concentrations were 2,4-DCP, phenol, benzoate and hexanoic acid. These products were identified by GC-MASS spectrometry. the effects of supplements, including sodium citrate (0.08 mM), sodium pyruvate (0.18 mM), sodium sulphate (0.14 mM) had a direct stimulatory effect on the dechlorination of 2,4,6-TCP and PCP after treatment for 4 weeks, but dechlorination was inhibited after 8 weeks.     

A pulsed switching peroxi-coagulation process to control hydroxyl radical production and to enhance 2,4-Dichlorophenoxyacetic acid degradation

• A new pulsed switching peroxi-coagulation (PSPC) system was developed. • The EC_T for 2,4-D removal in the PSPC was lower than that in the EF. • The iron consumption for 2,4-D removal in the PSPC was lower than that in the PC. The aim of this study was to develop a new pulsed switching peroxi-coagulation system to control hydroxyl radical (?OH) production and to enhance 2,4-Dichlorophenoxyacetic acid (2,4-D) degradation. The system was constructed with a sacrifice iron anode, a Pt anode, and a gas diffusion cathode. Production of H₂O₂ and Fe²⁺ was controlled separately by time delayers with different pulsed switching frequencies. Under current densities of 5.0 mA/cm² (H₂O₂) and 0.5 mA/cm² (Fe²⁺), the ?OH production was optimized with the pulsed switching frequency of 1.0 s (H₂O₂):0.3 s (Fe²⁺) and the ratio of H₂O₂ to Fe²⁺ molar concentrations of 6.6. Under the optimal condition, 2,4-D with an initial concentration of 500 mg/L was completely removed in the system within 240 min. The energy consumption for the 2,4-D removal in the system was much lower than that in the electro-Fenton process (68±6 vs. 136±10 kWh/kg TOC). The iron consumption in the system was ~20 times as low as that in the peroxi-coagulation process (196±20 vs. 3940±400 mg/L) within 240 min. The system should be a promising peroxi-coagulation method for organic pollutants removal in wastewater.     

不同填料对人工湿地模拟柱中指示菌的去除

为研究不同填料对指示菌的去除效果,选取沸石、无烟煤、页岩、蛭石、陶瓷滤料、砾石、钢渣、生物陶粒8种填料,进行垂直流人工湿地模拟柱净化污水试验。结果表明,8种填料中对3种指示菌(异养细菌、大肠菌群和粪链球菌)去除率较高的为钢渣(99.9%)和无烟煤(95.9%),推测主要是因为其出水分别呈碱性和酸性造成。除钢渣和无烟煤外,去除率较高的为沸石和蛭石,去除率较低的为陶瓷滤料和生物陶粒。相关分析结果表明6种填料(不包括钢渣和无烟煤)对指示菌去除率与填料的渗透系数间存在负相关关系,推测它们主要是通过过滤吸附的机制去除指示菌。     

人工湿地磷吸附饱和基质的化学再生研究

长期处理了生活污水后的人工湿地基质对磷素的吸附会达到饱和,通过化学浸提方法,研究了2种无机酸（盐酸和硫酸）,酸和碱（盐酸和氢氧化钠溶液）对饱和吸附磷基质的释磷效果以及再生后基质吸附磷效果。结果表明：盐酸和硫酸对基质释磷的差异性不大,硫酸的释磷效果略好于盐酸,对3种基质的释磷效果几乎都大于80%;碱对砂和煤渣释磷效果好,对高炉渣释磷效果差,但经碱再生后的高炉渣、砂基质对磷素的吸收率极高,磷素初始浓度在1～50mg·L-1范围内时,吸收率在95.18%～99.04%范围内,对基质的再生能力好,而经碱再生后的煤渣基质对磷素的吸收率却很低,吸收率不超过21.14%。     

Biofilm-electrode process with high efficiency for degradation of 2,4-dichlorophenol

2,4-Dichlorophenol (2,4-DCP) from chemical industry wastewaters has caused serious environmental pollution. Removal of 2,4-DCP using either physico-chemical or biological methods is not very efficient. In this paper, a combination of biological and electrochemical methods gave satisfactory results. By comparisons of the degradation of 2,4-DCP and the removal of chemical oxygen demand (COD) in electrochemical, biological and biofilm-electrode processes, it was found that the biofilm-electrode process possesses the highest degradation efficiency and removal rate; both the pure electrochemical and the pure biological processes were far less efficient. The removal efficiency of 2,4-DCP using the biofilm-electrode process was 100% in 48 h, while that using the pure electrochemical and the pure biological processes were 62 and 42%, respectively. The experiments show that the current of 5 mA for the cathode of 9 cm² and the initial concentration 100 mg/l of 2,4-DCP were the optimal parameters of technology for the biofilm-electrode process. The excellent effects are due to the withdrawing electron action of bacterium, electrochemically anodic oxidation and cathodic dechlorination. It is the first time that the biofilm-electrode method was applied in 2,4-DCP degradation. Here, we demonstrated that biofilm-electrode process is a promising method to remove some aromatic compounds in industrial wastewater.     

红壤胶体铁氧化物界面有机氯的非生物转化研究进展

综述了红壤胶体铁氧化物的结构、形态及其转化;铁氧化物界面有机氯的非生物转化过程及其影响因素;异化铁还原作用下的有机氯转化过程。有机氯的非生物转化主要包括氧化转化与脱氯转化过程。氧化转化包括暗态下的化学氧化与光化学氧化过程;脱氯转化包括脱氢卤化、加氢脱氯、脱双卤、二聚脱氯与亲核置换脱氯等反应过程。有机氯的非生物转化主要受胶体界面pH、Eh、水溶性有机物、金属离子、铁氧化物形态与铁还原细菌等的显著影响。有机氯非生物转化的化学-微生物耦合机制、复合污染条件下重金属对界面有机氯非生物转化过程的影响机制、红壤胶体界面有机氯污染的综合调控技术方法等三个方面值得关注,有助于推动土壤胶体界面环境化学的发展。     

Efficient dechlorination of 2,4-dichlorophenol in an aqueous media with a mild pH using a Pd/TiO2NTs/Ti cathode

In this study, palladium-loaded titania nanotubes was fabricated on a titanium plate (Pd/TiO₂NTs/Ti) for efficient electrodechlorination of 2,4-chlorophenol with a mild pH condition. The nature of Pd/TiO₂NTs/Ti electrodes was characterized by field-emission scanning electron microscope (FESEM), X-ray diffraction (XRD), X-ray photoelectron spectroscopy (XPS), and cyclic voltammetry (CV) techniques. The characterization results indicated the generation of Pd⁰ nanoparticles which were evenly dispersed on titania nanotubes arrays on the Pd/TiO₂NTs/Ti surface. An effective degradation efficiency of up to 91% was achieved within 60 min at cathode potential of −0.7 V (vs. SCE) and initial pH of 5.5. The effects of the applied cathode potential and initial pH on the degradation efficiency were studied. A near neutral condition was more favorable since very low and very high pHs were not conducive to the dechlorination process. Furthermore, the intermediates analysis showed that the Pd/TiO₂NTs/Ti electrode could completely remove chlorine from 2, 4-dichlorophenol since only phenol was detected as the byproduct and the concentration of released chlorine ions indicated near-complete dechlorination. This work presents a good alternative technique for eliminating persistent chlorophenols in polluted wastewater without maintaining strong acidic environment.