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.     

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.     

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.     

Pd/TiO_2催化剂对三氯生的催化加氢脱氯研究

采用沉淀-沉积法制备不同载体的Pd负载型催化剂,采用透射电镜(TEM)、X-射线衍射(XRD)和电感耦合等离子体发射光谱(ICP-AES)对材料进行表征;并以所得材料为催化剂对三氯生(TCS)的催化加氢脱氯反应进行了研究.结果表明,Pd/TiO_2型催化剂在TCS加氢脱氯反应中具有较好的效果,反应活性随着Pd负载量的提高而增强.当反应物初始浓度为0.016 mmol·L~(-1),pH值为10,催化剂0.36%Pd/TiO_2用量为20mg时,TCS在70 min可以完成脱氯过程.碱性条件下,p H的升高不利于反应的进行.当催化剂用量在15—25 mg时,催化剂质量标化的反应初活性没有明显变化,表明催化反应过程不受传质阻力的影响.当反应物初始浓度在0.009—0.02 mmol·L~(-1)时,反应初活性随浓度的提高显著增加,但进一步增加反应物的浓度时初活性没有明显提高,因此,TCS在Pd/TiO_2催化剂上的脱氯行为符合Langmuir-Hinshelwood模型,表明TCS的加氢脱氯受表面吸附所控制.催化反应的过程中生成多种脱氯中间产物,反应的最终产物为2-羟基二苯醚.     

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.     

Al2O3负载Pd催化剂对溴氯代乙酸的催化加氢脱卤研究

分别以氧化铝、氧化硅和多壁碳纳米管为载体,采用沉淀-沉积法制备负载型Pd催化剂.采用透射电镜(TEM)、X射线衍射(XRD)、电感耦合等离子体发射光谱(ICP-AES)、X射线光电子能谱(XPS)等手段对材料进行表征,并对溴氯代乙酸(BCAA)的液相催化加氢脱卤反应进行了研究.结果表明,由于Pd/Al_2O_3催化剂具有较高的等电点,因此相对于Pd/CNT、Pd/SiO_2在BCAA的加氢脱卤反应中具有更高的活性.以Pd/Al_2O_3为目标催化剂,对BCAA的加氢脱卤展开研究,发现催化活性随Pd的负载量的增加而提高.当反应物的初始浓度为0. 1 mmol·L~(-1),pH值为5.6,Pd(1.39)/Al_2O_3用量为25 mg·L~(-1)时,BCAA在20 min时可以实现完全脱溴并在反应2 h后脱氯达60.5%.另外,pH的升高不利于脱卤反应的进行.当反应物的浓度从0. 05 mmol·L~(-1)提高到0.4 mmol·L~(-1)时,反应初活性从1.55 mmol·L~(-1) min~(-1) gCat~(-1)提高到8.37 mmol·L~(-1) min~(-1) gCat~(-1).进一步通过拟合Langumir-Hinshelwood模型,相关系数达到0.97,说明BCAA的加氢脱卤是吸附控制机制.催化过程中溴氯代乙酸的脱溴和脱氯具有协同作用,反应最终生成乙酸.     

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%...     

改性碳纳米管负载Pd基催化剂对二氯乙酸的催化加氢脱氯

以壳聚糖(chitosan,CS)为单体,采用表面沉积交联法对多壁碳纳米管(CNT)改性得到壳聚糖修饰的碳纳米管(CS-CNT).分别以CS-CNT和CNT为载体,用硼氢化钠还原法制备Pd/CNT和Pd/CS-CNT负载型催化剂.采用元素分析仪、电感耦合等离子体发射光谱仪(ICP)、透射电镜(TEM)、比表面积与孔径分布测定仪(BET)、X射线光电子能谱(XPS)等对材料进行表征,并对二氯乙酸的液相催化加氢脱氯反应进行了研究.结果表明,与Pd/CNT相比,Pd/CS-CNT对二氯乙酸有更高的催化活性.此外,该催化加氢脱氯反应受溶液pH及催化剂表面Pd颗粒的影响.二氯乙酸的催化加氢脱氯反应符合Langmuir-Hinshelwood模型,表明该反应过程由二氯乙酸在催化剂表面的吸附所控制.     

2种水稻土胶体界面五氯酚的还原脱氯转化

研究了紫泥田和浅脚紫泥田2种水稻土胶体界面五氯酚(PCP)的还原转化效果,以及添加Fe2+或草酸对五氯酚还原转化效果的影响.采用表观一级反应动力学描述土壤胶体界面五氯酚的转化过程.结果表明,紫泥田和浅脚紫泥田土壤胶体界面五氯酚的还原转化动力学常数分别为0.0375d-1和0.0430d-1,半衰期分别为18.5d和16.1d;厌氧条件下水稻土胶体中铁氧化物还原溶解产生的吸附态Fe2+对五氯酚具有一定的还原转化能力.添加1.0mmol·L-1Fe2+或1.0mmol·L-1草酸均能显著促进土壤胶体界面五氯酚的还原转化和氯离子的产生,紫泥田土壤胶体界面五氯酚的还原转化半衰期分别减少到9.6d和6.0d,浅脚紫泥田土壤胶体界面五氯酚的转化半衰期分别减少到7.9d和3.0d.草酸促进作用更加显著的原因是铁-草酸配合物的生成.土壤胶体界面五氯酚的还原转化、脱氯效率与土壤胶体的比表面积、吸附态亚铁离子浓度有一定的正相关关系.促进土壤中吸附态亚铁离子和草酸等低分子量有机酸的产生能显著促进有机氯的还原转化.     

氯代芳烃催化氢转移脱氯的研究

本文以甲酸钠为氢源,对聚乙烯吡咯烷酮锚定的ＰｄＣｌ２催化氯代芳烃脱氯进行了研究,考察了反应条件对反应的影响,研究了脱氯的选择性。结果表明;该方法具有卓越的脱氯选择性,催化剂用量少,反应条件温和,操作简便。本文并对其脱氯反应机理进行了初步探讨。     

碱金属氧化物对V2O5-WO3/TiO2催化剂脱硝性能的影响

在V2O5-WO3/TiO2催化剂上负载碱金属氧化物（K2O,Na2O）,通过BET,XRD和SEM等方法对微观结构进行表征,研究不同含量碱金属氧化物对催化剂脱硝活性、N2O生成率和SO2氧化率的影响.结果发现,较大含量的碱金属对催化剂微观结构有一定影响.碱金属氧化物与催化剂表面V物种的结合生成部分碱金属盐（如KVO3）,改变了催化剂的表面结构,使催化剂中有效活性位的数量大大降低,从而导致催化剂活性降低.两种碱金属氧化物对催化剂的毒性顺序为K2O〉Na2O.     

树脂负载α-FeOOH异相光Fenton降解水中己烷雌酚

以Amberlite200树脂为载体,在Fe(NO3)3-HNO3体系中恒温水解制备了负载型催化剂α-FeOOH/Resin,以己烷雌酚(HEX)为目标化合物,研究了α-FeOOH/Resin的异相Fenton催化性能.结果表明,α-FeOOH/Resin异相Fenton反应能够有效降解水中的HEX,紫外光和H2O2的协同作用很大程度地提高了降解效率;pH值的降低或初始H2O2浓度的提高,均能增加HEX的降解速率;在中性条件下,HEX的光Fenton降解过程中,溶出的铁元素对降解贡献不大,异相Fenton反应起主导作用;催化剂重复使用后仍具有较好的催化活性和机械强度,说明铁在其表面负载牢固,催化剂具有一定的实用性.     

Rapid degradation of carbon tetrachloride by commercial micro-scale zinc powder assisted by citric acid

We developed an effective method for degradation of carbon tetrachloride (CT) in contaminated water. Zinc metal as a reducing agent for CT in aqueous solutions has been previously studied in some detail, but the rapid corrosion of zinc surface usually reduces its efficiency in removing CT. We assumed that citric acid could enhance the degradation of CT by zinc powder due to the elimination of a passivation layer of Zn(II) (hydr)oxides on the surface of zinc powder through chelating of organic ligands with Zn(II) produced from the reaction and keeping the exposure of active sites to targets. Here the influence of citric acid on the decomposing of CT by commercial micro-scale zinc powder was investigated in a pH range of 3.5–7.5 at 25°C in batch experiments. Reaction mixtures were analysed by gas chromatography/headspace analysis, and Cl⁻ concentration was determined by turbidimetry. The results demonstrate that the degradation of CT by zinc metal alone is very weak, but the addition of citric acid can assist zinc powder to decompose CT more completely and rapidly at all pHs. Degradation of CT took place mainly in the first 10 min of reaction, coupled with 75–95% of CT removal. Maximum dechlorination percentage (82.4%) of CT was obtained at pH 5.5. In that case, chloroform and dichloromethane, as main intermediates, were found at low levels during the whole reaction, suggesting that CT may be sequentially and multiply degraded so quickly that methane is yielded before the intermediates can be desorbed and released to aqueous solution. When compared with the current methods of nano-scale zinc and bimetallic systems, the application of commercial micro-scale zinc particles assisted by organic ligands is of environmental significance since it allows decontamination of aqueous chlorinated organic compounds at low cost and with high efficiency.     

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.     

Photocatalytic oxidation of humic substances with TiO<Subscript>2</Subscript>-coated glass micro-spheres

The photocatalytic oxidation of humic substances in aqueous solutions and natural waters with TiO₂ attached to buoyant, hollow glass micro-spheres was studied. A maximum oxidation efficiency of 3.6 mg W^–1 h^–1 was achieved in neutral or alkaline media at a plane surface concentration of the catalyst attached to the micro-spheres of 25 g m^–2. Proceeding by different mechanisms in acidic and alkaline media, the photocatalytic oxidation efficiency did not benefit from an excessive presence of hydroxyl radical promoters, hydrogen peroxide and alkali.     

过渡金属催化剂上CO还原NO反应性能的研究

在一系列负载型过渡金属催化剂上考察了ＣＯ－ＮＯ和ＣＯ－Ｏ２的反应性能。结果表明，催化剂的ＣＯ－Ｏ２反应活性高于ＣＯ－ＮＯ反应，催化剂表面ＮＯ解离是ＣＯ－ＮＯ反应的速率控制步骤。低温反庆有利于Ｎ２Ｏ的生成，高温有利于Ｎ２的生成。     

Effect of preparation parameters on catalytic properties of Pt/graphite

Catalytic ozonation of aqueous solutions of oxalic acid was examined in the presence of graphite-supported platinum catalysts. The catalytic activity of graphite was significantly enhanced by loading platinum. The removal efficiency of oxalic acid was 3.0%, 47.6% and 99.3% for ozonation alone, graphite catalytic ozonation and Pt/graphite catalytic ozonation in 30 min under the experimental condition, respectively. The influence of support pretreatment, solvent, impregnation time, platinum loading amount and reduction temperature on the activity of Pt/graphite catalyst was investigated. The pretreatment of graphite support had no effect on activity improvement of Pt/graphite catalyst. Solvent and impregnation time also no great effect on the activity. Platinum loading amount and reduction temperature influenced the catalyst activity significantly. The optimal catalytic performance of Pt/graphite was obtained when 1.0% platinum loading and 623 K of reduction temperature was adopted. The Pt/graphite catalyst was used for five times with no significant decrease in its activity and more than 90% oxalic acid removal was obtained.     

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.     

V2O5/AC催化剂对氨还原NO的研究

考察了V2O5/AC催化剂对NH3选择催化还原NO的影响，结果表明，以浓硝酸预氧化处理的活性焦为载体对催化剂活性有很大提高，这是由于浓硝酸预氧化后，活性焦表面产生了较多的含氧官能团可能吸附更多的NH3,并且提高了活性组分V2O5的含量，反应气氛中加入SO2后，二都活性都增加，但差异消失，这是由于SO2存在时，反应生成的SO4^2-离子的酸性强于浓硝酸预氧化产生的含氧官能团的酸性，催化剂在使用前经过煅烧和氧化对催化剂活性有很大改善。SO2存在时，V2O5含量为1wt%的催化剂活性提高。