共查询到18条相似文献，搜索用时 640 毫秒
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凹凸棒石铁/铝氢氧化物纳米复合材料对磷的吸附动力学研究 总被引：1，自引：0，他引：1
用铁/铝盐水解法制备了凹凸棒石/铝氢氧化物(PNCMⅠ)、凹凸棒石/铁氢氧化物(PNCMⅡ)和凹凸棒石/铁铝氢氧化物(PNCMⅢ)3种凹凸棒石纳米复合材料。对比了这3种纳米复合材料对水中磷的吸附净化能力,并利用吸附动力学实验探讨了3种材料对磷的吸附机理。结果发现:负载了铝/铁氢氧化物后凹凸棒石的晶体结构没有改变;温度对于3种吸附剂吸附磷的动力学参数影响不显著;3种吸附剂对磷的实际吸附量、理论吸附量和初始吸附速率均随着磷的初始浓度增大而增大。PNCMⅠ对磷的理论吸附量为18.18 mg/g,较其他2种吸附剂大。当磷的初始浓度从5 mg/L增加到50 mg/L,PNCM I对磷的初始吸附速率从0.125 mg/(g·min)增加到1.425 mg/(g·min)。3种凹凸棒石黏土纳米复合材料对磷的吸附符合准二级动力学方程,表明其吸附均为化学吸附。 相似文献
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氟铝交互作用对茶园土壤氟吸附动力学特征的影响 总被引：1，自引：0，他引：1
在氟的不同初始浓度及不同水土比情况下,茶园土壤对氟的吸附平衡时间均在25min左右,但对动力学方程拟合效果有一定差异,除了初始浓度为4.0mg/L(水土比10∶1)、20.0mg/L(水土比40∶1)、100.0mg/L(水土比40∶1和20∶1)处理氟的吸附动力学不能用一级动力学方程或二级动力学方程描述外,其余处理均可以用双常数方程、Elovich方程、一级动力学方程、二级动力学方程和抛物线方程这5个动力学方程描述。在铝存在下,不同氟铝比对氟的吸附动力学过程有明显影响,表现为吸附速率下降,吸附平衡时间延长,50min左右达吸附平衡。动力学方程拟合效果虽然有一定差异,但均可以用这5个动力学方程描述。在有无铝存在下,茶园土壤氟的吸附动力学特征用双常数方程和Elovich方程描述的效果更好。 相似文献
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通过动力学和等温吸附实验,研究了不同初始氨氮浓度下水溶铵、交换铵和固定铵在中砂上的吸附规律。结果表明,吸附平衡时各种形态铵含量随初始氨氮浓度增加而增大。3种形态铵吸附行为符合准二级动力学方程。吸附速率常数K大小顺序为：固定铵〉交换铵〉水溶铵,初始速率：固定铵〈交换铵〈水溶铵。随着初始氨氮浓度的增加,水溶铵占总铵的比重由40%上升到65%,其吸附的主要限制步骤为颗粒间扩散。交换铵对总铵的贡献率维持在25%左右,吸附饱和后有所降低,初始氨氮浓度为交换铵吸附的主要限制步骤。固定铵达到饱和时,吸附量只有26.18 mg/kg,对总铵的贡献率由33%下降到9%。 相似文献
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膨润土提纯后的尾矿主要含石英、斜绿泥石和白云母等矿物,以尾矿为主原料制备了复合陶瓷颗粒,采用XRD,IR和SEM探讨了烧结工艺对结构变化的影响,研究了复合陶瓷颗粒的组分变化、烧结温度、pH、初始浓度、吸附时间和温度对Cr(Ⅵ)离子吸附效果的影响,探讨了动力学和热力学变化。结果表明,烧结温度对吸附影响不大,烧结适宜温度为1000℃,陶瓷颗粒的主晶相为石英和硅灰石,表面为不均匀多孔结构。吸附的最佳吸附条件是pH值1、陶瓷颗粒用量1 g、吸附时间12 h及铬离子初始浓度100 mg/L,吸附率达96.33%。吸附行为符合准二级动力学方程,属于单分子层化学吸附;热力学数据说明,吸附反应为自发吸热反应。 相似文献
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针对我国东北某石油烃污染场地地下水中的萘污染,筛选出了Acinetobacter和Pseudomonas菌属的高效萘降解菌群。该菌群对萘的耐受性较高,且具有良好的乳化性,能够自动调节细胞表面疏水性和自聚集性。不同pH值、萘初始浓度、温度和菌接种量对萘降解效率的影响研究表明:最适菌群生长的pH范围为7.08.0;萘降解效率和速率在1.005.00 mg/L范围内与其初始浓度成正比;在1030 ℃温度范围内均表现出较高的萘降解效率。在此基础上,利用Guass、GuassAmp、LogNomal、Poisson和Pulse数学模型对萘的降解过程进行拟合,其降解速率更符合GuassAmp模型。通过将降解动力学模型中的常数与影响因素相关联,推导出了拟合度较高的多因素影响下的萘降解动力学方程。 相似文献
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苏打盐碱土对氮转化的影响 总被引：2，自引：0，他引：2
以苏打盐碱土中的主要成分NaHCO3作为主要影响因素,通过室内培养方法,研究不同苏打盐碱化条件对氮的吸附、矿化、硝化及反硝化作用的影响。结果表明,在不同NaHCO3质量浓度影响下：NH+4-N吸附符合Langmuir吸附等温式;矿化模型符合一阶动力学方程,随着NaHCO3质量浓度的增大,潜在矿化势(M0)和矿化速率常数(km)分别由358.48 mg/kg和0.088 d-1降低到337.08 mg/kg和0.059 d-1;硝化作用符合“S”形曲线模型,随着NaHCO3质量浓度的增大,最大速率（kmax）由22.56 mg/(kg·d)降低到16.68 mg/(kg·d);反硝化作用符合零阶动力学方程,但NaHCO3与Na2CO3混合质量浓度变化对反硝化速率常数(kd)影响不显著。随着NaHCO3质量浓度的增大,苏打盐碱土中NH+4-N吸附、有机氮矿化和硝化作用均受到抑制。 相似文献
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以坡缕石粘土为原料,通过溶胶-凝胶法制备坡缕石/氧化铝复合材料,通过静态吸附实验研究了复合材料吸附水中磷的动力学特征、吸附平衡和热力学参数,探讨了吸附机理。结果表明,复合材料对磷有较好的吸附作用,吸附过程能较好地符合准二级动力学方程,吸附速率常数随初始浓度的增大而减小,随温度的升高有所增大;吸附平衡能较好地符合Langmuir方程和D-R方程,吸附过程吸热,ΔG为-25~-21 kJ/mol,是物理吸附和化学吸附并存的过程。 相似文献
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采用壳聚糖对酸性蓝黑B模拟废水进行处理,研究了溶液的酸度、吸附时间、溶液的初始浓度和溶液温度等对吸附效率的影响。结果表明,壳聚糖对酸性蓝黑B具有优良的吸附效果,在溶液初始浓度小于400 mg/L,pH=3.5~6,温度约为30~40℃,吸附处理30~40 m in,COD去除率可达90%以上。 相似文献
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采用批实验方法,研究了北京平原典型沉积物对NH+4 N的吸附规律。结果表明颗粒越细的沉积物,达到吸附反应平衡所需的时间越长,对NH+4 N的吸附量也越大;NH+4 N初始浓度在0~50 mg/L范围内,Henry、Langmuir、Freundlich吸附等温模式均能较好地描述北京平原典型沉积物对NH+4 N的吸附特性。沉积物对NH+4 N的吸附量随初始浓度的增加而增加;沉积物的颗粒越细,Henry吸附系数K越大,单位质量沉积物的饱和吸附量也越大;沉积物中TOC含量对沉积物的NH+4 N吸附行为有一定的控制作用,永定河、潮白河沉积物TOC值与Henry吸附系数K的相关系数R2分别为050,076;沉积物对NH+4 N的饱和吸附量随着土水比的增加而减少,通过乘幂的方式拟合不同土水比下的饱和吸附量,得出了北京平原包气带沉积物对NH+4 N的饱和吸附量;相同岩性条件下,特别是细颗粒沉积物中,潮白河沉积物对NH+4 N的吸附能力较永定河沉积物强,而同一流域内,中、下游沉积物的吸附能力较上游强。 相似文献
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M. Taghdiri N. Zamani 《International Journal of Environmental Science and Technology》2013,10(1):19-26
The adsorption of hexamine onto powdered activated carbon from aqueous solutions was studied in a fixed bed system. Langmuir, Freundlich, Redlich–Peterson and Toth isotherm models were used to fit the experimental data and isotherm parameters were determined. The results revealed that the adsorption isotherm models fitted the data in the order of Langmuir > Toth > Redlich–Peterson > Freundlich. Lagergren pseudo-first order kinetic model was found to correlate well with the experimental data. The effects of solution pH, temperature, initial hexamine concentration and added salts concentration on the adsorption capacity and the rate of adsorption were studied. The results indicate that the rate of adsorption increases and then decreases as temperature of the hexamine solution increases, however, the adsorption capacity decreases. The addition of low concentration of salt significantly increases the adsorption capacity of activated carbon. The results showed that the activated carbon has potential for the adsorption of hexamine from industrial hexamine wastewater. 相似文献
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D. Li J. Yan Z. Liu Z. Liu 《International Journal of Environmental Science and Technology》2016,13(7):1815-1822
Sugar beet pulp is an abundant, renewable and low-cost precursor for production of activated carbon. In the present study, sugar beet pulp based activated carbon was prepared by using phosphoric acid as activating agent for adsorption of methylene blue. The conditions of preparation process had a significant influence on the adsorption of methylene blue, and the optimal preparation conditions were obtained as follows: liquid-to-solid ratio of 5, temperature of 450 °C and phosphoric acid concentration of 3 mol/L. The properties of sugar beet pulp based activated carbon were characterized by nitrogen adsorption isotherm. The adsorption increases as the increase of contact time, adsorption temperature and pH, and initial concentration of methylene blue. Batch kinetic studies showed that an equilibrium time of 100 min was needed for the adsorption, and the adsorbance of methylene blue is 244.76 mg/g at equilibration. Kinetic models, Weber’s pore diffusion model and Boyd’s equation were applied to the experimental data to study the mechanism of adsorption and the controlled step. The results showed that the adsorption kinetics followed the pseudo-second-order type kinetic model, intraparticle diffusion was not the rate-limiting mechanism and adsorption process was controlled by film diffusion. 相似文献
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F. Farzaneh Kondori K. Badii M. E. Masoumi G. Golkarnarenji 《International Journal of Environmental Science and Technology》2018,15(3):543-550
In the present work, a continuous catalytic wet peroxide oxidation fixed bed reactor was employed to treat a simulated wastewater sample with malachite green dye, as a contaminant. Natural perlite particle-supported nano-Fe3O4 catalyst was used as a fixed bed inside a reactor, and it was immobilized by a persistent magnetic field. The range of (perlite) particle sizes was from 100 to 1000 nm. The effects of various operating parameters, including temperature of the reactor, pH, initial hydrogen peroxide concentration and initial dye concentration, were investigated on the percentage removal of malachite green dye. Load of catalyst of 2 g and volumetric flow rate of 1 L/h were selected for all the tests. Maximum malachite green degradation was 99.5 ± 0.3%. This removal percentage was attained at temperature of 80 °C, pH = 6, initial dye concentration of 6 mg/L and initial hydrogen peroxide concentration of 100 mg/L. The process was isotherm, and the catalyst showed high catalytic activity in the steady-state condition. The loss of catalyst was less than 0.3%. 相似文献
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M. Nameni M.Sc. M. R. Alavi Moghadam M. Arami 《International Journal of Environmental Science and Technology》2008,5(2):161-168
In this research, adsorption of chromium (VI) ions on wheat bran has been studied through using batch adsorption techniques. The main objectives of this study are to 1) investigate the chromium adsorption from aqueous solution by wheat bran, 2) study the influence of contact time, pH, adsorbent dose and initial chromium concentration on adsorption process performance and 3) determine appropriate adsorption isotherm and kinetics parameters of chromium (VI) adsorption on wheat bran. The results of this study showed that adsorption of chromium by wheat bran reached to equilibrium after 60 min and after that a little change of chromium removal efficiency was observed. Higher chromium adsorption was observed at lower pHs, and maximum chromium removal (87.8 %) obtained at pH of 2. The adsorption of chromium by wheat bran decreased at the higher initial chromium concentration and lower adsorbent doses. The obtained results showed that the adsorption of chromium (VI) by wheat bran follows Langmuir isotherm equation with a correlation coefficient equal to 0.997. In addition, the kinetics of the adsorption process follows the pseudo second-order kinetics model with a rate constant value of 0.131 g/mg.min The results indicate that wheat bran can be employed as a low cost alternative to commercial adsorbents in the removal of chromium (VI) from water and wastewater. 相似文献
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铀污染地下水分布于世界多国,其危害备受关注。本文基于溶胶-凝胶法制备方解石负载羟基磷灰石复合材料(CLHC),通过静态与动态对比试验,探讨了PRB活性介质对水中铀离子的吸附机理和去除效果。试验结果表明,制备的CLHC表面被羟基磷灰石覆盖,对铀离子具有较强的吸附能力。当U的初浓度为5.0 mg/L、试验周期为2 h、溶液pH值为4、CLHC用量为0.5 g/L时,CLHC可以吸附水中所有的铀离子。CLHC对铀离子的吸附过程可以用Langmuir等温吸附模型、粒子内扩散吸附动力学模型和准二级吸附动力学模型较好地进行描述。石英砂负载羟基磷灰石与CLHC相比,后者具有更强的吸附能力,而且具有更长的使用寿命。CLHC在吸附铀的过程中没有价态变化,其对铀离子的吸附主要为离子交换的化学吸附。本研究的成果可为可渗透反应墙被应用于铀污染地下水修复提供试验依据。 相似文献