Mg/Al水滑石对水中痕量邻苯二甲酸酯的吸附动力学和热力学

研究了Mg／A1水滑石对水中痕量邻苯二甲酸二甲酯（DMP）、邻苯二甲酸二（2一乙基己基）酯（DEHP）和邻苯二甲酸二辛酯（DnOP）的吸附动力学和热力学特性。结果表明,在所研究的浓度范围内,3种邻苯二甲酸酯的吸附动力学曲线均符合准二级速率方程,DMP、DEHP和DnOP分别在600、200和200min基本达到吸附平衡;3种邻苯二甲酸酯的吸附等温线基本符合Langmuir和Freundlich吸附等温方程;在283～308K范围,pH=6．36,3种邻苯二甲酸酯初始浓度均为50μg／L时,吸附过程△H为负值且绝对值为5～12kJ／mol,表明吸附为放热过程,以表面物理吸附为主,邻苯二甲酸酯在Mg／Al水滑石上的吸附是色散力、诱导力、取向力和氢键力等多种作用力协同作用的结果。     

臭氧-生物活性炭工艺对饮用水中邻苯二甲酸酯类的去除中试研究

以嘉陵江源水的自来水厂滤后水为研究对象,在中试规模上研究了臭氧-生物活性炭工艺对饮用水中微量邻苯二甲酸酯（又称为酞酸酯,phthalate esters,PAEs）的去除效果。选择邻苯二甲酸二甲酯（DMP）、邻苯二甲酸二丁酯（DBP）、邻苯二甲酸二（2-乙基己基）酯（DEHP）、邻苯二甲酸二辛酯（DOP）为目标物质。研...     

氢氧化钠改性沸石对水中Cu~(2+)的吸附特性研究

利用氢氧化钠对天然沸石进行改性,将天然沸石和改性沸石用于吸附去除水中的Cu~(2+),分析了p H、温度、Cu~(2+)初始浓度、吸附时间对Cu~(2+)吸附性能的影响,并对吸附过程的吸附等温模型及吸附动力学进行研究。结果表明,改性沸石对Cu~(2+)的吸附性能明显优于天然沸石,当沸石投加量为10 g/L,Cu~(2+)为200 mg/L,p H为6.67,温度为50℃时,天然沸石和改性沸石对Cu~(2+)的吸附量分别为2.02、2.69 mg/g。Langmuir和Freundlich吸附等温模型均能较好地描述两种沸石对Cu~(2+)的吸附过程。天然沸石对Cu~(2+)的吸附行为更符合准一级动力学方程,而准二级动力学方程对改性沸石的吸附行为拟合度更好。两种沸石对Cu~(2+)的吸附均为非均相吸附,且内扩散过程不是唯一的速控步骤。     

NaCl改性沸石对氨氮吸附性能的研究

采用NaCl溶液对天然沸石进行改性,考察了NaCl浓度、温度及沸石用量对改性效果的影响。通过表面特征分析、吸附机制分析、吸附等温试验和吸附动力学试验,进一步比较了天然沸石和改性沸石对氨氮的吸附性能。结果表明,在NaCl溶液为6%(质量分数)、温度为303 K、天然沸石用量为15 g(以100 mL的NaCl溶液计)的优化条件下,改性沸石对氨氮的吸附效果最佳。扫描电子显微镜(SEM)和比表面积(BET)分析可知,沸石经改性后表面变粗糙,平均吸附孔径变小,比表面积变大。2种沸石对氨氮的吸附过程均可用Langmuir、Freundlich吸附等温方程较好地拟合,在温度为303 K时,改性沸石比天然沸石单分子层饱和吸附量增幅为34%以上。颗粒内扩散是沸石吸附氨氮的限制性因素,其吸附动力学较符合准二级反应动力学方程,拟合结果表明改性沸石具有更好的动力学性能,其吸附速率常数略大于天然沸石。     

十六烷基三甲基溴化铵改性沸石对腐殖酸的吸附性能研究

以十六烷基三甲基溴化铵(CTAB)为改性剂,制备了CTAB改性沸石,并用于对腐殖酸的吸附性能研究。考察了pH、吸附时间及腐殖酸初始浓度对CTAB改性沸石吸附腐殖酸的影响,采用吸附等温方程和反应动力学方程进行拟合分析,并利用扫描电子显微镜(SEM)、X射线光电子能谱仪(XPS)、傅立叶转换红外光谱分析仪(FTIR)对沸石改性前后进行结构表征。结果表明,在温度为25℃、转速为200r/min的条件下,选择pH为7.0、腐殖酸初始质量浓度为10mg/L、吸附时间为180min,此时CTAB改性沸石对腐殖酸的平衡吸附容量为0.16mg/g。相比Freundlich吸附等温方程(R2=0.967),CTAB改性沸石对腐殖酸的吸附更符合Langmuir吸附等温方程(R2=0.998),吸附机制为单分子层吸附。准一级反应动力学方程和准二级反应动力学方程均可以描述CTAB改性沸石对腐殖酸的吸附(R2=0.978)。吸附实验后的CTAB改性沸石上出现了甲基、亚甲基、羟基与羰基伸缩振动吸收峰,说明沸石已负载了CTAB,且腐殖酸已被CTAB改性沸石吸附。     

焙烧态锂铝水滑石对水中氟离子吸附性能研究

采用尿素水热法合成了不同摩尔比的锂铝水滑石(Li/Al LDHs),经480℃煅烧后制备出焙烧态锂铝水滑石(Li/AlLDOs)。研究了Li/Al LDOs对水中氟离子的吸附性能,分别考察了吸附时间、吸附温度和pH等因素对吸附效果的影响,并对吸附机制进行了探讨。结果表明,Li/Al LDOs吸附水中氟离子的行为符合准二级动力学方程,吸附等温数据符合Freundlich吸附等温方程,pH对吸附效果影响较大。X射线衍射分析表明,水滑石样品经历了物相转变及重构过程,Li/Al LDOs可有效去除水体中的氟离子。     

天津市大气PM_(10)与降尘中邻苯二甲酸酯的污染特征及相关性分析

采集天津市4个采样点的大气 PM_(10)与降尘样品,利用CH_2Cl_2和超声对样品中的邻苯二甲酸二甲酯(DMP)、邻苯二甲酸二乙酯(DEP)、邻苯二甲酸二丁酯(DBP)、邻苯二甲酸丁基苄基酯(BBP)、邻苯二甲酸(2-乙基己基)酯(DEHP)和邻苯二甲酸二辛酯(DOP)等6种邻苯二甲酸酯(PAEs)进行提取分离,采用气相色谱/质谱联用仪(GC/MS)定量分析。结果表明,4个采样点大气 PM_(10)样品中6种PAEs总质量浓度为2.371~24.201ng/m3,降尘样品中6种PAEs总质量浓度为222.310~1 184.503ng/g。对于6种PAEs,夏季浓度均高于冬季浓度,且DBP与DEHP是大气 PM_(10)与降尘样品中的主要污染物。6种PAEs总浓度、DBP浓度、DEHP浓度在大气 PM_(10)与降尘样品中存在相关关系,斯皮尔曼相关系数分别为0.929、0.881、0.905(双尾检验,在显著性水平0.01下)。回归分析表明,大气 PM_(10)与降尘样品中6种PAEs总浓度、DBP浓度、DEHP浓度具有一定的共变趋势。     

东莞地下水邻苯二甲酸酯分布特征及来源探讨

在广东东莞地区采集了59组地下水水样和9组地表水水样,采用气相色谱-质谱联用技术进行测定,结果表明,地下水中邻苯二甲酸酯(PAEs)的检出率为39.0％,6种PAEs的质量浓度在未检出～6.70 μg/L.其中,邻苯二甲酸双(2-乙基己基)酯(DEHP)检出率最高,为22.O％,最大值为6.20 μg/L;邻苯二甲酸二...     

生物炭对邻苯二甲酸二甲酯在土壤中自然降解和吸附行为的影响

为了解生物炭应用于邻苯二甲酸酯污染土壤修复的可行性,选择邻苯二甲酸二甲酯作为目标污染物,以花生壳为原料制备生物炭,通过室内模拟试验研究生物炭对邻苯二甲酸二甲酯在土壤中自然降解和吸附行为的影响。结果表明,未添加与添加生物炭土壤中邻苯二甲酸二甲酯的自然降解过程均遵循一级动力学方程,生物炭含量0.5%和1.0%的土壤中邻苯二甲酸二甲酯的半衰期分别延长2.185 d和4.151 d,表明添加生物炭会不同程度地延缓土壤中邻苯二甲酸二甲酯的自然降解;在不同的生物炭含量水平下,土壤对邻苯二甲酸二甲酯的吸附均能很好地符合Freundlich方程所描述的规律,生物炭含量0.1%、0.5%和1.0%土壤的吸附常数Kf分别为35.647、45.830和57.649,显著高于对照土壤(7.793),表明土壤对邻苯二甲酸二甲酯的吸附作用随生物炭含量增加而显著增强。     

天然及CaCl2改性沸石对四环素的吸附

通过静态吸附实验研究了水中四环素在天然和CaCl2改性沸石上的吸附行为及机制。实验表明,天然沸石对四环素具有吸附能力,CaCl2改性可以提高沸石对四环素的吸附能力。天然和改性沸石对四环素的吸附符合拟二级动力学模型,颗粒内扩散不是吸附过程的主要控制步骤。Freundlich和Dubinin-Radushkevich(D-R)等温吸附模型可以较好地描述实验所用2种沸石对四环素的吸附行为,D-R等温方程拟合结果显示吸附过程包含离子交换作用。通过对天然和改性沸石吸附四环素前后溶液中主要阳离子浓度变化分析证实了该吸附过程包含离子交换作用。实验研究了pH值变化对沸石吸附四环素的影响,当pH=3～5时,天然和改性沸石对四环素的吸附量均随pH值的增加而急剧下降,而pH=5～10时,天然和改性沸石对四环素的吸附量变化均不明显,推测可能是离子交换作用和化学沉淀吸附作用所致。另外,实验还初步探索了溶液离子强度对沸石吸附四环素的影响情况,随着溶液中Na+和Ca2+离子强度的增加,吸附量先急剧降低随后趋向平稳,进一步说明了沸石对四环素的吸附过程不是由单一机制控制的。     

Monitoring the sonochemical degradation of phthalate esters in water using solid-phase microextraction

The sonochemical degradation of aqueous solutions containing low concentrations of six phthalate esters at an ultrasonic frequency of 80 kHz has been investigated. Ultrasonic treatment was found capable of removing the four higher molecular mass phthalates (di-n-butyl phthalate, butylbenzyl phthalate, di-(2-ethylhexyl) phthalate and di-n-octyl phthalate) within 30-60 min of irradiation. The rest (dimethyl phthalate and diethyl phthalate) were more recalcitrant and nearly complete removal could be achieved only after prolonged irradiation times. The relative reactivity of phthalates was explained in terms of their hydrophobicity. Experiments were carried out at an overall initial phthalate concentration of 240 microg l(-1), values of electric power of 75 and 150 W, temperatures of 21 and 50 degrees C and in the presence of NaCl to study the effect of various operating conditions on degradation. Solid-phase microextraction (SPME) coupled with GC-MS proved to be a powerful analytical tool to monitor the sonochemical degradation of phthalate esters at low microg l(-1) concentration levels, minimising the risk of secondary contamination during sample preparation, a major parameter to consider during phthalates analysis. The advantages as well as disadvantages of using SPME are also highlighted.     

Hydrotalcites and organo‐hydrotalcites as sorbents for removing pesticides from water

Abstract

This paper reports on the adsorption of different organic pesticides by hydrotalcite, hydrotalcite heated to 500°C and organo‐hydrotalcite in aqueous medium by employing adsorption isotherms, and using X‐ray diffraction and infrared spectroscopy techniques. The results suggest that the adsorption capacity of the different materials depends on their nature as well as on the structure, polarity and hydrophobic or anionic nature of the pesticides. The results also show that hydrotalcite, both natural and after calcination at 500°C, is not a good sorbent of hydrophobic pesticides. The data demonstrated that both types of hydrotalcite, however, are very good sorbents of glyphosphate. Furthermore, the organo‐hydrotalcites may be as good sorbents as organo‐montmorillonites for hydrophobic pesticides.     

CTMAB／SDS改性沸石对水中痕量邻苯二甲酸酯吸附机制

以季铵盐阳离子表面活性剂CTMAB及阴离子表面活性剂SDS对粉末状天然沸石进行复合改性,制备得到了CTMAB／SDS改性沸石。对改性沸石及天然沸石进行红外吸收光谱及XRD衍射表征,并研究了PAEs在天然沸石和CT-MAB／SDS改性沸石上的吸附机制。结果表明,阴阳离子表面活性剂没有对层状结构的键型造成较大的影响;PAEs在天然沸石和CTMAB／SDS改性沸石上的吸附更符合表面吸附一分配作用复合模型;PAEs的表面吸附和分配作用对吸附作用的贡献主要受吸附剂中有机质含量及吸附物质大小、极性及溶解度的影响。     

污泥活性炭对次甲基蓝废水的吸附

立足于污泥的资源化,利用化学活化法制得的污泥基活性炭,处理次甲基蓝染料废水.考察了污泥活性炭的粒径以及染料废水的pH值对染料脱色效果以及活性炭的吸附量的影响,并对吸附过程进行等温吸附线和吸附动力学分析.结果表明,在本研究的范围内,污泥活性炭的粒径越小、染料废水的pH值越高,则污泥活性炭对染料废水的吸附效果越好.当粒径在200目以上时,去除率及吸附量分别为88.2％和136.7 mg/g;当pH值为11时,去除率和吸附量分别为90.4％和91.9 mg/g.污泥活性炭对次甲基蓝染料的吸附脱除符合Langmuir吸附等温线和Lagergren准二级动力学方程.     

溴化十六烷基吡啶改性沸石对水中甲基橙的吸附

采用溴化十六烷基吡啶(CPB)对天然沸石进行改性制备得到了CPB改性沸石,通过批量吸附实验考察了CPB改性沸石对水中阴离子染料甲基橙的去除作用。结果表明,天然沸石对水中甲基橙的吸附能力很差,而CPB改性沸石则可以有效吸附去除水中的甲基橙。CPB改性沸石对水中甲基橙的吸附能力随CPB负载量的增加而增加,CPB负载量最大的改性沸石对水中甲基橙的吸附能力最强。双分子层CPB改性沸石对水中甲基橙的去除率随吸附剂投加量的增加而增加,而CPB改性沸石对水中甲基橙的单位吸附量则随吸附剂投加量的增加而降低。双分子层CPB改性沸石对水中甲基橙的吸附平衡数据可以采用Langmuir等温吸附模型加以描述。根据Langmuir模型计算得到的CPB负载量为341 mmol/(kg沸石)的双分子层CPB改性沸石对水中甲基橙的最大吸附容量为63.7 mg/g(303 K和pH 7)。准二级动力学模型适合用于描述双分子层CPB改性沸石对水中甲基橙的吸附动力学过程。pH和反应温度对双分子层CPB改性沸石吸附水中甲基橙的影响较小。以上结果说明,双分子层CPB改性沸石适合作为一种吸附剂用于去除废水中的甲基橙。     

Attempt to adsorb N-nitrosamines in solution by use of zeolites

The strong adsorption of zeolite for N-nitrosamines in solution was first revealed by use of adsorption, and temperature programmed surface reaction (TPSR) techniques. N-nitrosodimethylamine (NDMA) and N-nitrosopyrrolidine (NPYR) as well as N-nitrosohexamethyleneimine (NHMI) can be adsorbed on zeolite Y, ZSM-5 and A in the solution of methylene chloride or water, which will be helpful for removal of the N-nitrosamines pollution in environmental protection. The equilibrium data were fitted to Freundlich-type isotherms, but the adsorption capacity of zeolites mainly depended on their pore size, surface area and acid-basic properties. Molecular size of adsorbate and solute-solvent interaction also strongly affected the adsorption of N-nitrosamines on zeolite in solution. The extraordinary adsorption properties of NaA zeolite for N-nitrosamines in aqueous solution is first reported and discussed.     

Removal of perfluorinated surfactants by sorption onto granular activated carbon, zeolite and sludge

Perfluorinated surfactants are emerging pollutants of increasing public health and environmental concern due to recent reports of their world-wide distribution, environmental persistence and bioaccumulation potential. Treatment methods for the removal of anionic perfluorochemical (PFC) surfactants from industrial effluents are needed to minimize the environmental release of these pollutants. Removal of PFC surfactants from aqueous solutions by sorption onto various types of granular activated carbon was investigated. Three anionic PFC surfactants, i.e., perfluorooctane sulfonate (PFOS), perfluorooctanoic acid (PFOA) and perfluorobutane sulfonate (PFBS), were evaluated for the ability to adsorb onto activated carbon. Additionally, the sorptive capacity of zeolites and sludge for PFOS was compared to that of granular activated carbon. Adsorption isotherms were determined at constant ionic strength in a pH 7.2 phosphate buffer at 30 degrees C. Sorption of PFOS onto activated carbon was stronger than PFOA and PFBS, suggesting that the length of the fluorocarbon chain and the nature of the functional group influenced sorption of the anionic surfactants. Among all adsorbents evaluated in this study, activated carbon (Freundlich K(F) values=36.7-60.9) showed the highest affinity for PFOS at low aqueous equilibrium concentrations, followed by the hydrophobic, high-silica zeolite NaY (Si/Al 80, K(F)=31.8), and anaerobic sludge (K(F)=0.95-1.85). Activated carbon also displayed a superior sorptive capacity at high soluble concentrations of the surfactant (up to 80 mg l(-1)). These findings indicate that activated carbon adsorption is a promising treatment technique for the removal of PFOS from dilute aqueous streams.     

Atmospheric distribution of particulate- and gas-phase phthalic esters (PAEs) in a Metropolitan City, Nanjing, East China

Phthalic acid esters (PAEs) are used in many branches of industry and are produced in huge amounts throughout the world. An investigation on particulate- and gas-phase distribution of PAEs has been conducted in Nanjing (China). The 12-h daily sampling program (from 8:00 am to 8:00 pm) for ten consecutive days was conducted in April, July and October 2005, and in January 2006 at about 1.5m above the ground level. For comparative purposes, sampling events were simultaneously conducted at two stations, one at the urban center and the other about 12 km from city center for suburban background monitoring. It was observed that the most abundant members of the PAE group were dimethyl phthalate (DMP) (10.1 ng m(-3), average), diethyl phthalate (DEP) (3.4 ng m(-3)), dibutyl phthalate (DBP) (58.8 ng m(-3)), butylbenzyl phthalate (BBP) (3.2 ng m(-3)), di-2-ethylhexyl phthalate (DEHP) (20.3 ng m(-3)) and di-n-octyl phthalate (DOP) (1.2 ng m(-3)). The average contribution of PAEs in the gas phase to the total PAE concentration (Sigma(6)PAE, sum of six PAE congeners) ranged from 75.0% to 89.2%. Both particulate- and gas-phase Sigma(6)PAE concentrations decreased with increasing temperature. Experimentally determined gas-particle partitioning (K(p)) of PAEs is well-correlated with their vapor pressure. The Sigma(6)PAE levels in the urban area are approximately 3.5 times as high as the levels found at the suburban station. The vertical profiles from 1.5 to 30.0m above the ground display slight height dependence.