氮掺杂Bi2O3光催化剂可见光催化降解2,4-二氯酚

采用自制的Bi2O3及氮掺杂Bi2O3(N-Bi2O3)光催化剂,以卤钨灯为光源,在可见光下对2,4-二氯酚进行光催化降解.结果表明,N-Bi2O3较Bi2O3具有更高的可见光催化活性.当N-Bi2O3光催化剂投加量为2.0 g/L、2,4-二氯酚初始浓度为20 mg/L和pH =7时,光催化反应320 min,2,4-二氯酚的降解率最高可达到91.5％.2,4-二氯酚的光催化反应初活性与其浓度之间的关系符合Langmuir-Hinshelwood动力学速率模型.对降解过程中总有机碳及Cl-测试结果表明,N-Bi2O3光催化剂能较好地完成对2,4-二氯酚的深度矿化及脱氯.     

庚醛改性壳聚糖的制备及其对酚类化合物的吸附性能

在相转移催化剂存在下由庚醛与壳聚糖反应生成Schiff's碱,再用NaBH4 还原制备了N-烷基化壳聚糖衍生物,改性壳聚糖(CTS)产物的结构用FTIR和XRD进行了表征,研究了它对2,4-二氯酚的吸附性能. 考察了吸附时间、溶液pH值、2,4-二氯酚浓度和改性剂用量等因素对吸附的影响. 结果表明,改性CTS具有较好的抗酸碱性能;溶液的pH值对吸附的影响较大,在pH=6.0,吸附2 h时对2,4-二氯酚的吸附量最大,酚浓度对吸附的影响符合Freundlich吸附等温方程;改性壳聚糖对2,4-二氯酚的吸附性能明显优于未改性的CTS,对质量浓度为0.6 g/L的2,4-二氯酚溶液的吸附量分别为70.0和7.7 mg/g.     

可见光催化剂La/S-TiO_2/SBA-15的表征及其对2,4-二氯酚的降解

采用溶胶凝胶法制备La-S-TiO2/SBA-15催化剂,并采用XRD、BET、UV-Vis和XPS对材料进行表征,在可见光下对2,4-二氯酚进行光催化降解。催化剂投加量为0.3g·L-1,光照时间为2h时,对50 mg·L-1的2,4-二氯酚的样品表现出最高的光催化活性,降解率达到50.09%,为P25的7.9倍。通过高效液相色谱,气相色谱-质谱法分析了2,4-二氯酚光催化降解的中间产物,并对其降解途径进行了简单分析。     

纳米Fe0降解2,4-二氯酚的影响因素及其机理

采用化学还原法制备了纳米Fe⁰, 并研究了不同条件下纳米Fe⁰对2,4-二氯酚(2,4-DCP)的降解情况, 探讨了纳米Fe⁰降解2,4-二氯酚的反应途径. 结果表明, 纳米Fe⁰对2,4-二氯酚的去除作用包括吸附、脱氯、开环三种机制. 其中脱氯作用是一种界面反应, 发生在氯酚分子被吸附到Fe原子表面之后. 2,4-二氯酚可以脱去一个氯原子生成2-氯酚或4-氯酚, 也可以脱去两个氯原子生成苯酚. 随着氯酚初始浓度的增大, 其相对去除率略有降低, 但绝对降解量有较大提高. 温度不仅影响脱氯速率, 而且影响氯酚的去除途径. 温度较高时脱氯作用占主导地位, 先脱氯后开环, 温度较低时吸附作用占主导地位, 较易发生先开环后脱氯的情况.     

硼掺杂金刚石薄膜电极上二氯酚的电化学阻抗谱研究

以2,4-二氯酚(2,4-DCP)和2,6-二氯酚(2,6-DCP)为模型污染物,采用循环伏安法和电化学阻抗谱研究了硼掺杂金刚石(BDD)电极上2种氯酚的电催化氧化过程.结果表明,2,4-DCP和2,6-DCP的氧化电位分别为1.55和1.62 V.等效电路拟合结果表明,当极化电位由开路电位提高至1.5 V时,2种氯酚的电荷转移电阻均有明显下降,反应控制步骤为扩散控制步骤.与2,6-DCP相比,2,4-DCP在BDD电极上更容易发生直接电化学氧化.     

液下单液滴微萃取-高效液相色谱法测定二氯酚

采用液下单液滴微萃取样品处理方法富集水中的2,4-二氯酚和2,6-二氯酚,高效液相色谱法测定.考察了不同萃取剂、萃取条件及测定条件对检测结果的影响.2,4-二氯酚和2,6-二氯酚的线性范围分别在0.001～20 mg/L和0.003～20 mg/L之间,检出限分别为0.001和0.003 mg/L.     

2,4-二氯苯酚的电化学氧化降解反应研究

采用循环伏安法和原位红外光谱技术研究了2,4-二氯苯酚在Pt电极上的电化学氧化降解反应,结合Fukui函数值预测了2,4-二氯苯酚在电化学氧化过程中的反应位点. 结果表明,Pt电极对2,4-二氯苯酚有良好的电催化活性,2,4-二氯苯酚在电极表面反应主要有3个途径：直接通过电化学反应脱去氯离子,生成苯酚;在·OH的进攻下,C—Cl键断裂,4位Cl较2位Cl先脱去,生成苯二酚,并可进一步氧化生成苯醌以及不饱和羧酸;在·OH的进攻下发生苯环开环反应,生成含氯不饱和羧酸. 在1700 mV左右,2,4-二氯苯酚可经电化学氧化生成CO₂.     

纳米级Pd/Fe双金属体系对水中2,4-二氯苯酚脱氯的催化作用

 利用化学沉淀法制备了纳米级Fe和纳米级Pd/Fe双金属催化剂,研究了它们对2,4-二氯苯酚(2,4-DCP)还原脱氯的催化性能. 结果表明,纳米级颗粒具有较高的比表面积和表面反应活性,其BET比表面积可达12.4 m2/g,当Pd/Fe用量为6 g/L时,2,4-DCP脱氯率达到90%以上. 脱氯效率与pH值、温度、钯含量和Pd/Fe投加量等因素有关. 2,4-DCP在脱氯过程中先生成2-氯苯酚和4-氯苯酚,最终生成苯酚,而少量的2,4-DCP可直接降解成苯酚.     

[Bmim]BF4-NaH2PO4双水相萃取-高效液相色谱法测定水中痕量氯酚类内分泌干扰物

利用离子液体双水相萃取-高效液相色谱(HPLC)法测定了水中痕量氯酚类内分泌干扰物.以2,4-二氯酚(2,4-DCP)、2,6-二氯酚(2,6-DCP)和对氯苯酚(4-CP)为目标分析物,考察了影响离子液体双水相萃取率的主要因素,如分相盐的浓度、水相pH值、萃取时间及离子液体加人量.当NaH2PO4的浓度为0.5 g/...     

类Fenton试剂-罗丹明B-HCl体系动力学荧光法测定环境水样中 2,4-二氯酚

在酸性介质中,痕量2,4-二氯酚对类Fenton试剂与罗丹明B的反应具有明显阻抑作用,且其阻抑作用大小与2,4-二氯酚的浓度有关。据此建立了一种动力学荧光法测定痕量2,4-二氯酚的新方法。考察了各种因素对测定方法灵敏度的影响。在最佳条件下,方法的线性范围为0.04~0.8μg/mL,检出限为0.012μg/mL。将该方法用于7种环境水样和6种合成样品中2,4-二氯酚的测定,加标回收率为93.5%~108.0%,相对误差为-5.45%~4.60%。     

Efficient oxidative degradation of 2-chlorophenol and 4-chlorophenol over supported CuO-based catalysts

A series of metal oxide catalysts for catalytic oxidative degradation of 2-chlorophenol (2-CP) and 4-chlorophenol (4-CP) were prepared, and the supported CuO catalysts were studied particularly. The supported CuO catalysts were characterized by XRD and NH3-TPD techniques, in which CuO/γ-Al2O3 exhibited high degradation activity. The addition of Na2O or K2O into CuO/γ-Al2O3 improved the oxidative degradation of CPs remarkably, in which Na2O was more efficient than K2O. Over CuO/γ-Al2O3-Na2O, CPs were completely converted and the liberation of the inorganic chloride from 2-CP or 4-CP reached 97% or 100% respectively at 30 ?C for 2 h. The supported CuO catalysts with good dispersion of CuO particles and less acid sites were favorable for the efficient oxidative degradation of CPs. In addition, the initial pH of the reaction solution was found to be an important factor which influenced the catalytic oxidative degradation of CPs and the initial pH of 11.2 and 9.8 was preferred for the oxidative degradation of 2-CP and 4-CP respectively over CuO/γ-Al2O3 catalyst.     

氧化铈稳定的CuO簇在CO,C3H6和NO消除中的催化性能（英文）

研究了CuO与γ-Al2O3和CeO2的相互作用,并由此制备出能有效脱除CO,C3H6和NO的催化剂,考察了不同载体表面CuO簇的分散稳定性和耐老化性能.结果发现,随CuO负载量的增加,CuO簇因与CeO2载体的强相互作用而稳定存在;而在γ-Al2O3表面,CuO簇易聚集成较大的颗粒.另一方面,由于CeO2本身较差的热稳定性,表面分散的CuO在950oC高温处理后烧结.因此,基于γ-Al2O3载体优越的耐老化性能,在γ-Al2O3载体分散CeO2,然后再担载CuO,从而得到了稳定的CuO簇,所得催化剂比CuO/γ-A12O3和CuO/CeO2具有更好的催化性能和抗热老化性能.     

The remarkable enhancement of CO-pretreated CuO-Mn2O3/γ-Al2O3 supported catalyst for the reduction of NO with CO: the formation of surface synergetic oxygen vacancy

NO reduction by CO was investigated over CuO/γ-Al2O3, Mn2O3/γ-Al2O3, and CuOMn2O3/γ-Al2O3 model catalysts before and after CO pretreatment at 300 °C. The CO-pretreated CuO-Mn2O3/γ-Al2O3 catalyst exhibited higher catalytic activity than did the other catalysts. Based on X-ray diffraction (XRD), X-ray photoelectron spectroscopy (XPS), UV/Vis diffuse reflectance spectroscopy (DRS), Raman, and H2-temperature-programmed reduction (TPR) results, as well as our previous studies, the possible interaction model between dispersed copper and manganese oxide species as well as γ-Al2O3 surface has been proposed. In this model, Cu and Mn ions occupied the octahedral vacant sites of γ-Al2O3, with the capping oxygen on top of the metal ions to keep the charge conservation. For the fresh CuO/γ-Al2O3 and Mn2O3/γ-Al2O3 catalysts, the -Cu-O-Cu- and -Mn-O-Mn- species were formed on the surface of γ-Al2O3, respectively; but for the fresh CuO-Mn2O3/γ-Al2O3 catalyst, -Cu-O-Mn- species existed on the surface of -Al2O3. After CO pretreatment, -Cu-□-Cu- and -Mn-□-Mn- (□ represents surface oxygen vacancy (SOV)) species would be formed in CO-pretreated CuO/γ-Al2O3 and CO-pretreated Mn2O3/γ-Al2O3 catalysts, respectively; whereas -Cu-□-Mn- species existed in CO-pretreated CuO-Mn2O3/γ-Al2O3. Herein, a new concept, surface synergetic oxygen vacancy (SSOV), which describes the oxygen vacancy formed between the individual Mn and Cu ions, is proposed for CO-pretreated CuO-Mn2O3/γ-Al2O3 catalyst. In addition, the role of SSOV has also been approached by NO temperature-programmed desorption (TPD) and in situ FTIR experiments. The FTIR results of competitive adsorption between NO and CO on all the CO-pretreated CuO/γ-Al2O3, Mn2O3/γ-Al2O3, and CuO-Mn2O3/γ-Al2O3 samples demonstrated that NO molecules mainly were adsorbed on Mn2+ and CO mainly on Cu+ sites. The current study suggests that the properties of the SSOVs in CO-pretreated CuO-Mn2O3/γ-Al2O3 catalyst were significantly different to SOVs formed in CO-pretreated CuO/γ-Al2O3 and Mn2O3/γ-Al2O3 catalysts, and the SSOVs played an important role in NO reduction by CO.     

PREPARATION OF CUO/γ-Al2O3 CATALYSTS FOR CATALYTIC COMBUSTION VOCS VIA PLASMA

CuO/γ-Al2O3 catalysts were prepared by plasma treatment and conventional impregnation methods. The catalytic combustion of two kinds of volatile organic compounds (VOCs), toluene and benzene, were carried out over these CuO/γ-Al2O3 catalysts. The surface properties of these catalysts were characterized by X-ray Diffraction (XRD) and Scanning Electron Microscopy (SEM). The experimental results showed that in catalytic combustion the activity of the CuO/γ-Al2O3 catalyst prepared via plasma was much higher than that of the CuO/γ-Al2O3 catalyst prepared by conventional impregnation method. XRD results showed that an enhanced dispersion had been achieved with the plasma treatment. SEM results indicated that the size became much smaller and the surface became more uniform with the plasma treatment.     

焙烧温度对CuO/γ-Al2O3和CeO2-CuO/γ-Al2O3催化剂NO还原活性的影响

用浸渍法制备了CuO/γ-Al2O3催化剂和CeO2改性的CeO2-CuO/γ-Al2O3催化剂,考察了焙烧温度对CuO/γ-Al2O3和CeO2-CuO/γ-Al2O3催化剂C3H6还原NO反应活性的影响,以及CeO2的添加量对CeO2-CuO/γ-Al2O3催化剂C3H6还原NO反应活性的影响。结果表明,在200 ℃～500 ℃的焙烧温度范围内,焙烧温度对CuO/γ-Al2O3催化剂的活性影响很小；在500 ℃～800 ℃的焙烧温度范围内,随着焙烧温度的升高CuO/γ-Al2O3催化剂的活性急剧下降,由XRD物相测定结果可知,归因于对反应表现惰性的尖晶石CuAl2O4相的生成。当焙烧温度为500 ℃时,CeO2的添加对CuO/γ-Al2O3催化剂的活性影响很小；当焙烧温度为800 ℃时,CeO2的添加对CuO/γ-Al2O3催化剂有明显的助催化作用,当Ce和Cu的摩尔比为1∶10时,NO转化率较为理想。     

CuO/γ-Al2O3脱除烟气中SO2的研究

将CuO/γ-Al2O3用于烟气脱硫研究。考查了脱硫剂制备参数及反应条件对CuO/γ-Al2O3脱硫活性的影响。并对不同载铜量的脱硫剂进行了XRD表征。结果表明，载铜量的质量分数为8%～10%时，脱硫剂具有较高的脱硫活性，高于10%的载铜量致使活性组分CuO在Al2O3表面发生多层覆盖，活性位的利用率下降；在350 ℃～500 ℃的烟气温度及 3 000 L/kg·h～56 000 L/kg·h的操作空速范围内，CuO/γ-Al2O3具有较高的脱硫活性，烟气中的O2对于CuO/γ-Al2O3的脱硫活性是必需的，水的影响不大。     

Study of CO2 Hydrogenation to Methanol over Cu-V/γ-Al2O3 Catalyst

The effect of vanadium addition to Cu/γ-Al2O3 catalyst used in the hydrogenation of CO2 to produce methanol was studied. It was found that the catalytic performance of the Cu-based catalyst improved after V addition. The influence of reaction temperature, space velocity and the molar ratio of H2 to CO2 on the performance of 12%Cu-6%V/γ-Al2Oa catalyst were also studied. The results indicated that the best conditions for reaction were as follows: 240 ℃, 3600 h-1 and a molar ratio of H2 to CO2 the dispersion of the supported CuO species, which resulted in the enhanced catalytic performance of Cu-V/γ-Al2O3 binary catalyst.     

不同助剂掺杂的铬基催化剂的制备及其对乙烷氧化脱氢的催化性能

以硝酸盐作为前驱体,Al₂O₃为载体,采用等体积浸渍法制备了系列不同助剂（Mn, Co, Ce）及不同助剂含量（1%, 3%, 5%, 7%, 10%）掺杂的铬基催化剂,其结构经X-射线粉末衍射(XRD)、 H₂程序升温还原(H₂-TPR)和CO₂程序升温脱附（CO₂-TPD）表征。并考察了催化剂对乙烷氧化脱氢反应的催化性能。结果表明：添加Co助剂有利于活性组分铬的分散,10Cr₃Co/γ-Al₂O₃催化剂表现出最佳催化性能,在反应温度为650 ℃, V(CO₂) ：V(C₂H₆)=3 ：1,空速(GHSV)为3 600 mL·（g·h）^-1条件下,在该催化剂上乙烯产率为36.5%。     

CuO/γ-Al2O3单分散催化剂的XAFS研究

采用XAFS方法研究浸渍法制备并于低温焙烧的CuO/γ-Al2O3催化剂的局域结构.对于CuO负载量小于单层分散阈值的CuO/γ-Al2O3(0.4 mmol/100 m2),结果表明,CuO物种是以层状分散的孤立原子簇存在于γ-Al2O3载体表面,其第一近邻Cu－O配位环境的结构与晶态CuO的相似,键长和配位数分别为0.195 nm和4.对于CuO负载量等于单层分散阈值的CuO/γ-Al2O3(0.8 mmol/100 m2),已有少量的CuO纳米颗粒生成.对于CuO负载量大于单层分散阈值的CuO/γ-Al2O3(1.2 mmol/100 m2),其结构与多晶CuO的相近.基于CuO在γ-Al2O3载体上的三种不同分散状态的结构特点,我们提出了CuO/γ-Al2O3催化剂的结构模型.     

并流淤浆混合法制备铜基甲醇合成催化剂及助剂Al2O3的作用研究

采用并流淤浆混合法制备了一系列具有不同铜锌铝比的铜基甲醇合成催化剂CuO/ZnO/Al2O3,测试了其催化性能(甲醇收率和CO转化率)及物相结构,并对该制备方法进行评价。Cu∶Zn∶Al摩尔比为4∶5∶1 的铜基催化剂显示了最好的催化活性。通过对催化剂前驱物煅烧过程进行DTA分析及对前驱物进行XRD分析表明, 催化剂前驱物的物相与Al2O3的量有关。当Al2O3的量较低时,前驱物的物相以(Cu0.3 Zn0.7)5(CO3)2(OH)6为主;当Al2O3的量较高时,前驱物中物相(Cu0.3Zn0.7)5(CO3)2(OH)6的量下降,而物相Cu2CO3(OH)2的量增加。物相(Cu0.3 Zn0.7)5(CO3)2(OH)6对终态催化剂的活性是十分有利的 。