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1.
改性废报纸纤维对水中Cr(Ⅵ)的吸附研究   总被引:1,自引:0,他引:1  
利用环氧氯丙烷与三甲胺对废报纸纤维进行改性制备阴离子吸附材料(CWNF),通过傅里叶变换红外光谱(FT-IR)、扫描电镜(SEM)、能谱(EDS)、热重分析(TGA)、比表面积(BET)对改性前后废报纸纤维进行表征,并研究其去除水中六价铬离子Cr(VI)的性能.结果表明,改性后废报纸纤维(CWNF)对Cr(VI)的吸附能力显著提高.当CWNF投加量为1g/L,溶液pH为1时,对100mg/L Cr(VI)的最大吸附量为38.66mg/g,平衡时间为60min,比改性前废报纸纤维(WNF)的吸附量(24.18mg/g)提高了59.88%.Langmuir与Freundlich等温吸附方程均能较好地描述CWNF对Cr(VI)的吸附特性,吸附动力学更符合拟二级速率方程.  相似文献   

2.
油菜秸杆外壳对水溶液中六价铬的吸附作用   总被引:3,自引:0,他引:3  
为探讨油菜秸秆外壳去除水溶液中重金属铬的可能性及其影响因素,并研究其吸附性能和吸附机制.采用Box-Behnken Design实验设计研究了水溶液中六价铬[Cr(VI)]初始浓度、pH值范围、油菜秸秆外壳添加量和吸附温度4个因素对油菜秸秆外壳去除溶液中Cr(VI)的影响作用;用吸附等温方程、吸附动力学方程与热力学方程分别探讨了油菜秸秆外壳去除水溶液中Cr(VI)的行为;采用红外光谱技术对油菜秸秆外壳吸附水溶液Cr(VI)前后进行表征,探讨其吸附机制.油菜秸秆外壳去除溶液中Cr(VI)的最佳条件组合为:在吸附时间为1440min时,Cr(VI)初始浓度为99.15mg/L、pH值为1.01、油菜秸秆外壳添加量为2.90g/L和吸附温度35.70℃,Cr(VI)去除率为91.97%;吸附等温线拟合,吸附Cr(VI)行为符合Freundlich方程,为优惠吸附;热力学研究表明:溶液中Cr(VI)吸附属吸热反应,且为自发吸附行为;吸附动力学显示:油菜秸秆外壳去除溶液Cr(VI)符合准二阶动力学方程,吸附过程中存在离子交换;红外光谱提示:吸附过程中,O—H、C—H、NH3+、N—H和C—O基团与Cr(VI) 络合吸附发挥了重要作用.油菜秸秆外壳能够有效吸附水溶液中的Cr(VI),pH值是最为重要的影响因素.  相似文献   

3.
改性沸石和铁粉的复合材料处理水中六价铬的研究   总被引:1,自引:0,他引:1  
利用海藻酸盐的凝胶化将零价铁粉固定于改性沸石表面,制得复合材料,以期在保留改性沸石的吸附性的同时增加铁粉的还原性.复合材料的扫描电镜图片可以看出铁粉分散嵌于海藻酸钙薄层,同时海藻酸钙不会阻碍Cr(VI)与改性沸石的接触.实验考察材料去除水中Cr(VI)性能,结果表明:复合材料,改性沸石,铁粉的除Cr(VI)效率分别为:74.1%,38.4%,9.1%,这得益于改性沸石和铁粉相互的协同作用. 对反应后复合材料进行XPS检测,其表面含有Cr3+,Cr6+表明了材料吸附能力同时还具有还原性.并且对Cr(VI)去除的现象能用伪二级吸附动力学方程描述.平衡吸附量qe和反应速率常数k呈相反的变化趋势.铁粉含量为5.4%的材料性能较好:qe为0.96mg/g, k为0.011g/(mg×h);在Cr(VI)浓度为70mg/L时,上述铁含量的复合材料仍具有较高的处理性能,其qe和k分别为 1.29mg/g, 0.0094g/(mg×h).  相似文献   

4.
以壳聚糖和经酒石酸改性的平菇粉末为材料,通过戊二醛进行交联反应,制得壳聚糖-改性平菇凝胶小球(CMPOD)复合生物吸附剂,用于水溶液中Cr(VI)的吸附去除.结果表明,在实验所测pH值(2~10)范围内,复合吸附剂对Cr(VI)的吸附量随着pH值上升而降低;随着Cr(VI)初始浓度或温度的提高,吸附剂对Cr(VI)的吸附量均相应增加,当Cr(VI)初始浓度为600mg/L,温度为50℃,Cr(VI)吸附量可达190mg/g以上;Cr(VI)的吸附符合准二级动力学方程及Freundlich等温吸附模型;热力学分析表明,吸附剂对Cr(VI)的吸附过程为自发的吸热反应.扫描电镜(SEM)分析显示,吸附剂具有发达的网状结构,吸附Cr(VI)后网状孔隙被填充,且能谱分析(EDS)出现明显的Cr(VI)吸收峰;傅立叶红外光谱分析(FTIR)表明,壳聚糖中的氨基成功引入复合吸附剂中,在Cr(VI)吸附中为主要作用官能团.  相似文献   

5.
制备了巯基纤维素并用其对含Cr(VI)离子的溶液进行了静态吸附实验.研究了pH值、吸附时间、反应温度、吸附剂用量等因素对吸附性能的影响.结果表明:在pH值为2、Cr(VI)浓度为50 mg/L和吸附剂为0.5 g时,常温条件下吸附6h后,Cr(VI)去除率达到99.2%,吸附反应符合Langmuir和Freundlich等温方程.  相似文献   

6.
改性污泥活性炭吸附废水中Cr(Ⅵ)的性能研究   总被引:1,自引:0,他引:1  
以污水处理厂剩余污泥为原料,1.0 mol/L KOH做活化改性剂,制备污泥活性炭,探讨不同条件下其对废水中Cr(VI)的吸附性能.结果表明,污泥活性炭对Cr(VI)吸附的最佳条件为:pH为2,温度为25℃,污泥活性炭投加量为5 g/L,吸附时间为40 min.此条件下,废水中Cr(VI)的去除率可达99%以上.动力学分析表明,污泥活性炭对Cr(VI)废水的吸附符合准二级动力学方程与Langmuir等温式.  相似文献   

7.
小麦秸秆对Cr(Ⅵ)的吸附特性及动力学、热力学分析   总被引:8,自引:3,他引:5  
为实现农业废料资源化,解决含铬废水的污染问题,研究了小麦秸秆对Cr(Ⅵ)的吸附性能.试验考察了pH,小麦秸秆投加量,温度和初始ρ〔Cr(Ⅵ)〕对吸附活性的影响,进而确定了小麦秸秆去除Cr(Ⅵ)的最优条件.结果表明:当pH=1.0,温度为50 ℃,固液比为40 g/L时,小麦秸秆对Cr(Ⅵ)的吸附效果最佳.在pH=1.0,温度为30 ℃,固液比为4 g/L的条件下,初始ρ〔Cr(Ⅵ)〕分别为50,100和150 mg/L时,吸附6 h达到平衡,饱和吸附量分别为6.281,11.942 和13.981 mg/g.吸附动力学反应符合准二级动力学方程.吸附热力学反应符合Langmuir吸附等温方程.结合FTIR谱图和SEM结果,推断小麦秸秆对Cr(Ⅵ)的吸附过程以化学吸附为主.   相似文献   

8.
研制了煤渣-沸石复合多孔介质材料用于去除苇田养殖水体中的氨氮和COD_(Cr)。通过材料中煤渣、沸石不同配比对吸附效果的影响实验,确定了其配比为2:1。进而以吸附实验探讨了该材料对水中氨氮和COD_(Cr)的吸附性能。结果表明,该材料对氨氮和COD_(Cr)的吸附过程可用伪二级动力学方程和Langmuir等温方程描述;在25℃条件下,通过Langmuir吸附等温方程拟合出的最大吸附量分别为0.271 mg/g、0.680 mg/g,而吸附速率主要受到边界层扩散和内扩散的控制。该材料对实际水体的吸附效果显示,在不同COD_(Cr)浓度条件下其对氨氮的去除有着较好的稳定性,对COD_(Cr)的去除效率随着COD_(Cr)初始浓度的增大稍有增加。  相似文献   

9.
采用化学交联法制备了壳聚糖/氧化石墨烯(Cs/GO)复合材料,并用于含Cr(Ⅵ)废水的吸附研究。探讨了吸附剂组成、pH、吸附时间、Cr(Ⅵ)初始浓度对吸附剂去除Cr(Ⅵ)的影响。结果表明:Cs含量为GO质量的10%、溶液p H为2.00、Cr(Ⅵ)初始浓度为100 mg/L时吸附效果最好。吸附平衡时间为150 min。Langmuir吸附等温模型和拟二级吸附动力学方程能较好的拟合该吸附过程;该材料经过4次吸附-解吸循环吸附试验后,仍保持一定的吸附能力。因此,Cs/GO复合材料可用于含Cr(Ⅵ)废水的处理。  相似文献   

10.
以黑曲霉菌丝体作为吸附剂,通过静态吸附实验研究了各种因素对其吸附去除废水中Pb2+的影响。结果表明:当Pb2+初始浓度为50 mg/L,吸附剂用量为1.0 g/L,吸附时间为45 min,pH为5.0时,吸附效果最佳。此时吸附量为44.1 mg/g,去除率为90.86%。使用准二阶动力学方程可较好的拟合黑曲霉对Pb2+的吸附,表明该吸附过程以化学吸附为主。等温吸附过程可用Freundlich方程描述,说明该吸附为多分子层吸附。傅立叶红外光谱分析表明,黑曲霉吸附剂表面的酯羰基(-COO-)、羧基(-COOH )和羟基(-OH )在吸附Pb2+的过程中发挥主要作用。  相似文献   

11.
为了研究改性制备核桃壳对石油烃吸附程度,以化学改性制备核桃壳为吸附剂,考察了溶液p H值、时间和温度对改性核桃壳吸附石油烃效果的影响。结果表明:当温度为298 K,p H为7.0,0.2 g改性核桃壳吸附处理100 m L浓度为60 mg/L的柴油溶液,80 min后吸附量最大,可达到12.57 mg/g。该吸附过程符合准二级动力学方程,其相关系数达到0.9999。在3种温度(298,308,318 K)条件下的吸附等温曲线更符合Freundlich模型。通过热力学计算证实,该吸附过程是吸热的、自发的过程,一定程度上的升温有助于石油烃的吸附。  相似文献   

12.
A novel illite@carbon (I@C) nanocomposite adsorbent has been synthesized via a facile hydrothermal carbonization process (HTC) using glucose as carbonaceous source and illite as the carrier. The morphology, microstructure and surface properties of the prepared nanocomposite adsorbent were analyzed by FESEM, TGA, XRD, FT-IR and Zeta potential measurements. Batch experiments were carried out on the adsorption of Cr(VI) to determine the adsorption properties of the composite. The adsorption of Cr(VI) onto the I@C nanocomposite was well described by the pseudo-second-order kinetic model and Langmuir isotherm. Compared with the illite and carbon material (SC) separately, the prepared I@C nanocomposite adsorbent exhibited enhanced adsorption performance for Cr(VI) with a maximum adsorption capacity of 149.25 mg/g, which was higher than that of most reported adsorbents. In addition, the adsorption process was spontaneous and endothermic based on the adsorption thermodynamics study. The adsorption of Cr(VI) by I@C was highly pH-dependent and the optimum adsorption occurred at pH 2.0. The Zeta potential analysis results indicated that the electrostatic interactions between anionic Cr(VI) and the positively charged surface of the adsorbent might be critical to the adsorption mechanism. This study demonstrated that the I@C nanocomposite should be a promising candidate for a low-cost, environmental friendly and highly efficient adsorbent for the removal of toxic Cr(VI) from wastewater.  相似文献   

13.
采用浸渍法制备负载镧镁活性氧化铝改性除氟剂,用于去除溶液中氟离子。通过正交实验考察镧镁摩尔比、焙烧温度和焙烧时间对改性活性氧化铝吸附性能的影响,得出最佳合成条件为镧、镁物质的量比1∶2,焙烧温度300℃,焙烧时间2.0 h。研究吸附时间、投加量、p H值和共存阴离子对氟离子吸附效果的影响。结果表明:吸附时间为3.0 h、投加量为3.6 mg/L,p H值在6~9,除氟效果最好,氟离子去除率为94.5%;对比不同阴离子对除氟性能的影响,除氟性能受阴离子影响力大小为:CO2-3>SO2-4>Cl->NO-3;吸附剂对氟离子的吸附过程符合伪二级动力学模型,吸附等温线满足Langmuir吸附等温式,其饱和吸附量为7.663 mg/g;不同温度下的热力学结果表明该反应为自发吸热反应。  相似文献   

14.
铁氧化物改性黏土对Cr(Ⅵ)的吸附性能研究   总被引:2,自引:0,他引:2  
利用铁氧化物对黏土进行了包覆改性,采用静态吸附法对该改性黏土吸附Cr(Ⅵ)的特性进行了研究,并考虑了反应时间、pH、浓度、温度对吸附的影响。实验结果表明,整个吸附过程基本在3h内完成;改性黏土对Cr(Ⅵ)的吸附量随溶液初始pH的增大而明显减小;随着溶液初始浓度和温度的增大而增大。同时,在初始pH为3.0的条件下,研究了改性黏土吸附Cr(Ⅵ)的动力学和热力学特性,结果表明,改性黏土对Cr(Ⅵ)吸附能较好地符合准二级动力学方程和Langmuir等温式。由Langmuir等温式得出,在293K、初始pH为3.0条件下的单层饱和吸附量为12.91 mg•g-1。确定了改性黏土吸附Cr(Ⅵ)的热力学参数,表明该吸附过程是一个吸热的自发过程。与原土的对比实验表明,改性黏土对Cr(Ⅵ)的吸附能力大大增强。  相似文献   

15.
Pollutants that exist in anionic species are issues of concern in water treatment. Compared to cationic pollutants, the removal of anionic pollutants by adsorption is more difficult because most adsorbents carry predominantly negative charges in neutral and alkaline environments. In this study, a cross-linked chitosan derivative with quaternary ammonium and magnetic properties(QM-chitosan) was prepared and employed to remove chromium(VI) and phosphorus(V)(Cr(VI) and P(V)) from aqueous environments. The QM-chitosan was characterized by Fourier transform infrared spectrometry(FT-IR),thermogravimetric analysis(TGA), energy dispersive X-ray(SEM-EDX) and zeta potential.Batch experiments show that QM-chitosan can effectively remove Cr(VI) and P(V), and the main mechanism was believed to be electrostatic interaction. A pseudosecond-order model was fitted to describe the kinetic processes of Cr(VI) and P(V) removal. The adsorption isotherms of both Cr(VI) and P(V) on the QM-chitosan were well fitted by the Langmuir isotherm equation. The saturated adsorption capacity of P(V)(2.783 mmol/g) was found to be higher than that of Cr(VI)(2.323 mmol/g), resulting from the size of the H2PO-4ions being smaller than that of the HCr O-4ions. However, the theoretical calculation and experimental results showed that QM-chitosan had a stronger affinity for Cr(VI) than P(V). The adsorption–desorption of the QM-chitosan was evaluated, and high regeneration rates were demonstrated.  相似文献   

16.
霉菌吸附水体中Cr(Ⅵ)Cd(Ⅱ)离子研究   总被引:1,自引:5,他引:1  
采用从活性污泥中筛选的ZYL霉菌,进行吸附水体中Cr(Ⅵ)、Cd(Ⅱ)离子研究。研究结果表明:在Cr(Ⅵ)、Cd(Ⅱ)浓度分别为300mg/L时,菌种生长良好。吸附水体中[Cr(Ⅵ)、Cd(Ⅱ)]的最佳条件是pH=5.0,时间1h,温度为10℃。吸附规律符合Langm uir等温吸附模型,由回归方程得到Cr(Ⅵ)的表观最大吸附量为14m g/g;Cd(Ⅱ)的表观最大吸附量为52m g/g,说明该霉菌可以很好的去除低温水体(地下水)中Cr(Ⅵ)、Cd(Ⅱ)离子。  相似文献   

17.
Mg–Al–Cl layered double hydroxide (Cl-LDH) was prepared to simultaneously remove Cu(II) and Cr(VI) from aqueous solution. The coexisting Cu(II) (20 mg/L) and Cr(VI) (40 mg/L) were completely removed within 30 min by Cl-LDH in a dosage of 2.0 g/L; the removal rate of Cu(II) was accelerated in the presence of Cr(VI). Moreover, compared with the adsorption of single Cu(II) or Cr(VI), the adsorption capacities of Cl-LDH for Cu(II) and Cr(VI) can be improved by 81.05% and 49.56%, respectively, in the case of coexisting Cu(II) (200 mg/L) and Cr(VI) (400 mg/L). The affecting factors (such as solution initial pH, adsorbent dosage, and contact time) have been systematically investigated. Besides, the changes of pH values and the concentrations of Mg2+ and Al3+ in relevant solutions were monitored. To get the underlying mechanism, the Cl-LDH samples before and after adsorption were thoroughly characterized by X-ray powder diffraction, transmission electron microscopy, Fourier transform infrared spectroscopy, and X-ray photoelectron spectroscopy. On the basis of these analyses, a possible mechanism was proposed. The coadsorption process involves anion exchange of Cr(VI) with Cl in Cl-LDH interlayer, isomorphic substitution of Mg2+ with Cu2+, formation of Cu2Cl(OH)3 precipitation, and the adsorption of Cr(VI) by Cu2Cl(OH)3. This work provides a new insight into simultaneous removal of heavy metal cations and anions from wastewater by Cl-LDH.  相似文献   

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