水溶液中氯代烷烃的催化还原脱氯研究

研究了氯代甲烷系列和氯代乙烷系列的各种氯代烷烃在铁、铜二相金属体系中的还原脱氯反应,分析了氯代有机物结构性质对还原脱氯反应的影响和规律性,探讨了氯代烷烃在金属还原作用下的还原脱氯机理．     

聚氯乙烯(PVC)水解脱氯的研究

采用高压反应釜，在过热水条件下对PVC脱氯过程进行研究，结果表明，水解工艺可以有效地脱除PVC中的氯，并就工艺条件对脱氯效果的影响进行讨论，适宜的工艺条件为：反应温度220℃，反应时间2h，初始压力3.0MPa，碱浓度4%。     

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.     

水介质中催化剂Raney Ni催化2-氯酚加氢脱氯

选择水作为反应介质,以氢气为氢源,研究了Raney Ni催化下、水溶液中2-氯酚的加氢脱氯,调查了溶剂、碱助剂和碱金属或碱土金属氯化物对加氢脱氯反应的影响.发现在水体系中,2-氯酚更容易被加氢脱氯,水作为反应介质时显著改善了加氢脱氯的反应环境,消除了无机氯化物在催化剂表面的吸附和累积,使催化剂保持了高活性.     

多氯联苯微生物厌氧脱氯研究进展

多氯联苯是一种典型的持久性有机污染物,其在环境中的转化归趋备受关注.在厌氧条件下,多氯联苯可以通过微生物脱氯进行降解,该降解方式虽然广泛存在于自然界中,但是受生物地球化学因素的影响较大,调控较为复杂.本文对多氯联苯的厌氧微生物脱氯降解进行综述,讨论了脱氯路径和自然界中8种主要脱氯历程;脱氯微生物及相关的微生物还原脱卤酶;影响脱氯速率、程度和历程的主要物理和地球化学因素(温度、pH和氧化还原水平、碳源、电子受体、电子供体及抑制物).最后分析了多氯联苯厌氧脱氯研究中存在的问题并对其前景进行展望.     

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。     

厌氧颗粒污泥对五氯苯酚脱氯过程中的影响因素

在间歇培养血清瓶中,研究了厌氧颗粒污泥对五氯酚脱氯过程中的影响因素.结果表明,葡萄糖、酵母膏和蛋白胨显著提高了PCP的脱氯速率.添加甲酸、乙酸、乙醇对PCP脱氯速率有一定提高,丙酸和丁酸对脱氯速率没有影响.20%氢气的加入对PCP脱氯速率的影响显著.废水中硝酸盐和硫酸盐等电子受体的存在降低了PCP的脱氯速率.微生物抑制剂氯仿、青霉素降低了PCP脱氯速率,表明厌氧微生物尤其是甲烷菌对还原脱氯有重要影响.PCP最佳还原脱氯温度为38℃,最佳pH为7,低的氧化还原电位(<-200mV)有利于脱氯的进行.图5参13     

PVC的热解脱氯动力学分析

采用动态热重法对PVC热解脱氯反应动力学进行了研究，对不同升温速率下TG曲线采用下同方法分析，计算出反应速率常数、反应级数、活化能等脱氯反应动力学参数，并推断出反应机制，分析结果表明，PVC热解存在两个阶段，氯原子主要在250℃-300℃之间以HCl的形式释放，且反应为一级反应。     

土壤还原过程对氯代有机污染物还原脱氯的影响与机制

自然环境中,大多数氯代有机污染物厌氧还原脱氯反应是与土壤环境中一些生源要素的生物化学还原过程相伴生。有机污染物的种类、生物有效性以及毒性能够显著影响这些生源要素的转化,反过来,土壤中活跃的氧化还原反应也可以显著影响有机污染物的动力学转化过程。本文从氧化还原顺序上综述了反硝化过程、铁还原过程、硫酸盐还原过程和产甲烷过程对氯代有机污染物厌氧还原脱氯过程的影响与作用机制,旨在为氯代有机污染物在厌氧环境中还原脱氯的过程与机理的进一步研究、以及还原脱氯与微生物介导的生源要素氧化还原过程的耦合作用机制的揭示提供参考。     

醇胺类物质促进飞灰中氯代芳烃加氢脱氯的研究

分别以三乙醇胺(TEA)和一乙醇胺(MEA)作为氢源,六氯苯(HCB)作为模型化合物,研究了在密闭体系下飞灰中氯代芳烃的加氢脱氯作用.考察了TEA或MEA添加量、热处理温度和时间对脱氯效率的影响,证实有明显的脱氯反应发生.当MEA或TEA添加量为8%时,经过250℃,2 h热处理,脱氯效率分别可达94.7%和78.6%...     

Pd/MCM-41催化水溶液中碘苯Ullmann反应的研究

以水溶剂中Ullmann反应为目标反应,设计具有纳米介孔结构的Pd/MCM-41作为其高效催化剂.与传统SiO2载体负载的Pd催化剂比较,该催化剂在以水为介质的碘苯偶合（Ullmann反应）中显示出优良的催化活性和对联苯的选择性.     

Al_2O_3负载Pd-Cu催化剂催化1,2-二氯乙烷加氢脱氯性能

采用共浸渍法制备了一系列Al2O3负载金属Pd、Cu催化剂.通过元素分析（ICP）、氮气吸脱附（BET）、X射线粉末衍射（XRD）、透射电镜（TEM）等技术对催化剂进行了表征,并以1,2-二氯乙烷气相加氢脱氯为探针反应,考察了Pd-Cu/Al2O3催化剂的钯铜比、反应温度、反应时间等因素对催化活性以及反应产物乙烯选择性的影响.结果发现,提高Cu负载量可在催化剂中形成Pd-Cu合金,并促进催化剂对乙烯的选择性.此外,当温度为250℃,Pd、Cu负载量分别为0.78%和1.9%时的Pd-Cu/Al2O3催化剂对1,2-二氯乙烷的催化加氢脱氯效果最佳,最终产物乙烯的选择性可达到80%以上.     

Catalytic reduction of water pollutants: knowledge gaps,lessons learned,and new opportunities

● Advances, challenges, and opportunities for catalytic water pollutant reduction. ● Cases of Pd-based catalysts for nitrate, chlorate, and perchlorate reduction. ● New functionalities developed by screening and design of catalytic metal sites. ● Facile catalyst preparation approaches for convenient catalyst optimization. ● Rational design and non-decorative effort are essential for future work. In this paper, we discuss the previous advances, current challenges, and future opportunities for the research of catalytic reduction of water pollutants. We present five case studies on the development of palladium-based catalysts for nitrate, chlorate, and perchlorate reduction with hydrogen gas under ambient conditions. We emphasize the realization of new functionalities through the screening and design of catalytic metal sites, including (i) platinum group metal (PGM) nanoparticles, (ii) the secondary metals for improving the reaction rate and product selectivity of nitrate reduction, (iii) oxygen-atom-transfer metal oxides for chlorate and perchlorate reduction, and (iv) ligand-enhanced coordination complexes for substantial activity enhancement. We also highlight the facile catalyst preparation approach that brought significant convenience to catalyst optimization. Based on our own studies, we then discuss directions of the catalyst research effort that are not immediately necessary or desirable, including (1) systematic study on the downstream aspects of under-developed catalysts, (2) random integration with hot concepts without a clear rationale, and (3) excessive and decorative experiments. We further address some general concerns regarding using H₂ and PGMs in the catalytic system. Finally, we recommend future catalyst development in both “fundamental” and “applied” aspects. The purpose of this perspective is to remove major misconceptions about reductive catalysis research and bring back significant innovations for both scientific advancements and engineering applications to benefit environmental protection.     

Catalytic decomposition of polychlorinated biphenyls (PCBs)

In this study, polychlorinated biphenyls (PCBs) were decomposed by low‐temperature heat treatment with metallic catalyst, and with metallic catalyst and a hydrogen source. Of the catalysts used, iron (Fe) was the most active catalyst for the decomposition of PCBs, and the decomposition was due to dechlorination. The addition of hydrogen sources accelerated the decomposition of PCBs in the presence of catalyst. Surface analysis of the catalyst using X‐ray photoelectron spectroscopy (XPS) suggested that the emitted chlorine was presumed to form metal chloride. The reactions of each homolog can be expressed by a successive first‐order reaction model. This means that a substituted chlorine is successively detached during this reaction. The overall decomposition rate in this reaction system was controlled by that of the lower chlorinated homologs. The decomposition rates with Fe and NaBH₄ for the lower chlorinated homologs were about 10 times as fast as the rates with only Fe.     

Effect of Cu-ZSM-5 catalysts with different CuO particle size on selective catalytic oxidation of N,N-Dimethylformamide

● A series of Cu-ZSM-5 catalysts were tested for DMF selective catalytic oxidation. ● Cu-6 nm samples showed the best catalytic activity and N₂ selectivity. ● Redox properties and chemisorbed oxygen impact on DMF catalytic oxidation. ● Isolated Cu²⁺ species and weak acidity have effects on the generation of N₂. N, N-Dimethylformamide (DMF), a nitrogen-containing volatile organic compound (NVOC) with high emissions from the spray industry, has attracted increasing attention. In this study, Cu-ZSM-5 catalysts with different CuO particle sizes of 3, 6, 9 and 12 nm were synthesized and tested for DMF selective catalytic oxidation. The crystal structure and physicochemical properties of the catalyst were studied by various characterization methods. The catalytic activity increases with increasing CuO particle size, and complete conversion can be achieved at 300–350 °C. The Cu-12 nm catalyst has the highest catalytic activity and can achieve complete conversion at 300 °C. The Cu-6 nm sample has the highest N₂ selectivity at lower temperatures, reaching 95% at 300 °C. The activity of the catalysts is determined by the surface CuO cluster species, the bulk CuO species and the chemisorbed surface oxygen species. The high N₂ selectivity of the catalyst is attributed to the ratio of isolated Cu²⁺ and bulk CuO species, and weak acidity is beneficial to the formation of N₂. The results in this work will provide a new design of NVOC catalytic oxidation catalysts.     

载体特性对Pd-Cu/TiO2催化剂催化脱氮性能的影响

以Pd-Cu／TiO2为催化剂，采用催化加氢技术进行脱氮研究．结果表明：TiO2载体的特性对催化活性及N2选择性有显著影响，与773K和973K温度下焙烧得到的载体相比，以573K温度下焙烧得到的TiO2为载体制备的Pd（5wt％）-Cu（1．25wt％）／TiO2催化剂可显著提高催化效率及N2选择性．     

Formic acid fractionation towards highly efficient cellulose-derived PdAg bimetallic catalyst for H2 evolution

The present work, in which cellulose isolated from formic acid fractionation (FAC) is decorated with polyetherimide (PEI) to attain highly efficient cellulose-derived PdAgbimetallic catalyst (PdAg-PEI-FAC), has been investigated, and the catalyst properties are characterized by XRD, XPS, BET, ICP-AES and HAADF-STEM. The as-obtained Pd3.75Ag3.75-PEI-FAC exhibits excellent catalytic performance for H2 evo-lution from a sodium formate-free formic acid (FA) aqueous medium at ambient temperature and the turnover frequency (TOF) reaches a high value of 2875 h-1, which is superior to most of the previously reported Pd-based heterogeneous catalysts supported on a carbon matrix in the literature. The remarkable catalytic activities of PdAg-PEI-FAC result from high dispersion Pd and synergistic effects between the PdAg bimetallic system. Furthermore, the amide (-NH) group in PEI coated on cellulose acting as a proton scavenger efficiently improves the catalytic property of catalyst. In addition, the critical factors affecting H2 release, such as FA concentration, reaction temperature, PdAg compositions and support matrix type, are also evaluated. Based on the experimental results, the probable three-step mechanism of H2 evolution from FA over Pd3.75Ag3.75-PEI-FAC is proposed. In the end, the activation energy (Ea) of Pd3.75Ag3.75-PEI-FAC catalyst is calculated to 53.97 kJ mol-1, and this catalyst shows unique robustness and satisfactory re-usability with no loss of catalytic activity after five recycles. The findings in this work provide a novel routine from lignocellulose fractionation towards cellulose-derived catalyst for H2 evolution.     

High dechlorination of PCBs catalysed by carbon under mild conditions

This article reports high dechlorination of toxic polychlorinated biphenyls (PCBs) under mild conditions. PCBs are priority pollutants acting as endocrine disruptors, human carcinogens and environmental estrogens. Previous remediation methods involving high temperature and pressure have drawbacks such as high cost, de novo dioxins synthesis and difficult recovery of vaporized PCBs. On the other hand, dechlorination methods using mild conditions show the problem of catalyst deactivation. Here, activated carbon was used for the first time as catalyst to dechlorinate 2,4,5 trichlorobiphenyl. High dechlorination, of 87%, was achieved under mild conditions. 2,4,5 trichlorobiphenyl was treated at 40–150°C with calcium hydroxide, sodium hydroxide and sulfur in mixed water and organic solvents. Dechlorination products were biphenyl, orthohydroxy biphenyls, 2,4 dihydroxy biphenyls and biphenyl-2-thiol. Dichlorobiphenyl and orthochlorobiphenyls were found in trace quantities. We found that carbon particles catalysed dechlorination by substitution reactions and suppressed further chlorination. Dechlorination at biphenyl ortho position was preceded by substitution reaction by hydroxyl and thiol ions. Moreover, in the absence of carbon, dechlorination was lower and substituted products were not observed. These findings may be applied at industrial scale to remediate PCB-contaminated waste.