磁性离子交换树脂对模拟水中四环素的吸附特性研究

采用静态实验研究了溶液中四环素在磁性离子交换树脂上的吸附行为,考察了反应物初始浓度,初始p H值等因素对吸附效果的影响,分析了吸附动力学、吸附等温线模型和吸附热力学,并阐明了吸附机制。结果表明:磁性离子交换树脂对四环素具有良好的吸附效果;准二级动力学模型能更好的描述磁性离子交换树脂对四环素的吸附过程;Freundlich模型更适合描述磁性离子交换树脂对四环素的吸附平衡过程,D-R模型说明吸附过程包含离子交换作用;中性和酸性条件下磁性离子交换树脂对四环素的吸附效果较好;磁性离子交换树脂吸附四环素是自发、吸热和熵增加的反应过程,升温有利于吸附。     

牛粪生物炭对水中磷的吸附特性及其影响因素研究

以牛粪生物炭为吸附剂,通过静态吸附实验研究牛粪生物炭对磷的吸附特性。研究了pH值、投加量等对牛粪生物炭吸附磷的影响。结果表明,牛粪生物炭吸附磷的最佳初始pH值为6.0;当投加量为0.1 g时,对磷的去除较为理想;通过对动力学数据进行分析,发现准二级动力学(R~2=0.999)比准一级动力学方程(R~2=0.5 886)和Elovich方程(R~2=0.927)能更好的拟合动力学数据,颗粒内扩散方程拟合结果发现牛粪生物炭对磷的吸附包括表面吸附和颗粒内扩散两个过程。吸附等温线拟合发现Langmuir吸附等温方程能很好拟合等温吸附数据,表明生物炭对磷的吸附以单分子层吸附模式为主。     

干旱区牛粪生物炭对水中磷的吸附特性研究

以牛粪生物炭为吸附剂,通过静态吸附实验研究生物炭对磷的吸附特性。通过对动力学数据进行分析,发现准二级动力学(R2=0.999)比准一级动力学方程(R2=0.5886)和Elovich方程(R2=0.927)能更好地拟合动力学数据,颗粒内扩散方程拟合结果发现牛粪生物炭对磷的吸附包括表面吸附和颗粒内扩散两个过程。吸附等温线拟合发现Langmuir吸附等温方程能很好拟合等温吸附数据,表明生物炭对磷的吸附以单分子层吸附模式为主。利用牛粪热解产生的生物炭吸附去除水中磷是可行的,不仅成本低廉并且能够达到干旱区农业废弃物资源化利用及废水除磷的目的。     

XDA-1型大孔吸附树脂对水中氯仿的吸附性能

研究了XDA-1型大孔吸附树脂对用自来水配制的低浓度溶液中氯仿的动态吸附能力,以及浓度、流速、温度和pH等因素对吸附过程的影响.结果显示,采用XDA-1大孔树脂吸附水中的氯仿,其吸附效率可达99%以上,泄漏点前的吸附量为160mg/ml.采用热空气热解吸方式回收氯仿,回收率达85%,为含氯仿工业废水的处理提出一种新的处理工艺.     

没食子药渣生物炭对苯酚的吸附

以没食子药渣为原料,采用限氧热解法制备了不同温度300℃、400℃、500℃、600℃下的药渣生物炭,考察pH、投加量、溶液温度、不同接触时间和溶液初始浓度对吸附苯酚的影响。实验结果表明,这几个因素均能影响生物炭对苯酚的吸附效果。4种不同热解温度制备的生物炭对苯酚的吸附能力为400℃500℃600℃300℃,300℃和400℃最佳pH为5.0,500℃～600℃的最佳pH为7.0,药渣生物炭吸附苯酚的最佳投加量为0.05 g。在25℃～45℃条件下,较高的温度有利于药渣生物炭对苯酚溶液的吸附。没食子药渣生物炭的吸附过程先快后慢,在10 h趋于平衡。利用Langmuir和Freundlich模型对4种生物炭进行拟合,发现不同热解温度的药渣生物炭基本符合Langmuir和Freundlich等温吸附模型。研究结果为预测药渣生物炭吸附重金属提供理论参考,从而为拓展药渣资源化利用提供有效途径。     

对氯苯酚在湿地土壤中的吸附特性研究

利用恒温振荡法对土壤对对氯苯酚的吸附情况进行实验,进行了对氯苯酚在湿地土壤中吸附特征的研究,结果表明:对氯苯酚在湿地土壤中的吸附行为较好的符合Langmuir等温式,吸附速率较慢,符合二级动力学规律,湿地土壤对对氯苯酚的吸附量随着离子强度的增大而减小。     

褐煤除去水溶液中六价铬离子的动力学实验研究

廉价的褐煤能够去除工业废水中的铬离子引起了人们的广泛兴趣。近年来国内外相继报导过这方面的应用研究,但有关褐煤除铬机理的研究报导甚为少见。本文在于通过实验找出褐煤除铬的吸附平衡及动力学规津。结果表明,褐煤吸附量与溶液中铬离子的平衡浓度之间呈对数直线关系;吸附速度遵从固膜扩散速度方程。在处理数据时,作者对简化了的固膜扩散方程作了推广。在实验温度范围内计算了反应表现活化能ED(58.2KJ/mol)。这对于提高反应速度,指导褐煤除铬实践具有一定的现实     

蒙脱石对溶液中镍和铜的吸附特性研究

采用镍和铜作为溶液中的吸附质,探讨了蒙脱石对这2种重金属的吸附性能。通过实验研究了p H值、吸附剂用量、反应时间、浓度等因素对吸附Ni2+和Cu2+的影响。根据实验结果可知,蒙脱石对金属离子的吸附效率随溶液p H值、吸附剂用量、反应时间的增加而增加,但随着金属离子浓度的增加而降低。吸附动力学研究表明,蒙脱石对Ni2+和Cu2+的吸附过程符合准2级动力学模型。     

磁性活性炭吸附苯酚的初步研究

本文研究了磁性活性炭对苯酚的吸附性能;探讨了Cd2＋对苯酚在磁性活性炭上吸附的影响。目的是对磁性活性炭进行研究,以及为在实际废水中吸附处理苯酚提供参考。结果表明,磁性活性炭对苯酚的吸附过程符合拟二级动力学模型,R2为0.9935;与Freundlich吸附模型相比,Langmuir吸附模型能更好地描述磁性活性炭对苯酚的吸附行为;在不影响去除率的情况下,Cd2＋的存在使苯酚吸附处理最佳浓度由30 mg/L增大至50 mg/L;同时,Cd2＋对磁性活性炭和活性炭吸附苯酚分别具有促进和抑制作用。针对苯酚的吸附去除率,当无Cd2＋时,磁性活性炭的比活性炭的低10.65%～20.2%;当有Cd2＋时,磁性活性炭的比活性炭的高0.3%～7.71%。     

两种有机污染物的吸附研究

本文研究了水中苯酚－间甲酚与苯酚－对氯酚在ＮＫＡ树脂上的竞争吸附,结果表明,ＩＡＳ及ＬＣＡ模型都能较好地反映这两个吸附系统的竞争吸附规律。     

苯酚,糖醇及甲醛的吸附与脱附的研究

本文研究了水中苯酚，糖醇及甲醛在ＮＫＡ树脂上的吸附平衡，发现了各组份之间的竞争吸附特点，以及苯酚脱附过程中受到其它二组份的影响情况。     

Removal of phenol from aqueous solutions by adsorption

Experiments have been conducted to examine the liquid-phase adsorption of phenol from water by silica gel, HiSiv 3000, activated alumina, activated carbon, Filtrasorb-400, and HiSiv 1000. Experiments were carried out for the analysis of adsorption equilibrium capacities and kinetics. The adsorption isotherm model of the Langmuir-Freundlich type was the best to describe adsorption equilibrium data for phenol for the adsorbents studied. Results of kinetic experiments indicated that HiSiv 1000 had the highest rate of adsorption among the adsorbents studied and therefore more detailed studies were carried out with this adsorbent. The influence of particle size, temperature, and thermal regeneration on adsorption of phenol by HiSiv 1000 was evaluated. From particle size experiments it appeared that adsorption capacity of HiSiv 1000 did not change by changing the particle size, but the rate of adsorption decreased considerably by increasing the particle size. The effect of temperature on adsorption was studied by determining equilibrium isotherms for HiSiv 1000 at 25, 40, and 55 degrees C. The results showed that adsorption capacity decreased with increasing temperature. Thermal regeneration of HiSiv 1000 was performed at 360 degrees C. It was observed that adsorption capacity of HiSiv 1000 did not change after 14 regeneration cycles. Equilibrium experiments showed that the adsorption capacities of activated carbon and Filtrasorb-400 were several times higher than that of HiSiv 1000.     

生物法处理含酚废水的研究

为了降低炼油厂污水处理场的酚负荷,对催化裂化汽提塔所排含酚废水的预处理进行了研究。进行了煤渣吸附实验,酚的生物降解动力学实验及酚在兼氧条件下的处理实验;采用４－氨基安替比林光度法测定酚浓度。实验结果表明采用煤渣填料－生物膜反应器,酚的去除率可达９０％,酚的生物降解符合一级反应动力学,酚类物质可在兼氧条件下降解     

石油类污染物在充填状灰岩裂隙中迁移规律研究

针对淄博市大武水源地的石油污染状况进行了动态模拟石油类污染物迁移特性的研究。内容包括用现场粘土充填灰岩石板缝测定弥散系数、吸附系数及其他有关参数，建立该系统在饱水条件下的迁移数学模型。研究表明静态吸附均遵循Ｌａｎｇｍｕｉｒ吸附模式，且吸附能力较小；静态吸附结果与动态参数比较吻合，可直接用于建立整体模型；水中的石油类污染物在地表以下迁移性很强，容易下渗进入潜水层。     

Application of a chemically modified green macro alga as a biosorbent for phenol removal

Phenol and substituted phenols are toxic organic pollutants present in tannery waste streams. Environmental legislation defines the maximum discharge limit to be 5–50 ppm of total phenols in sewers. Thus the efforts to develop new efficient methods to remove phenolic compounds from wastewater are of primary concern. The present work aims at the use of a modified green macro alga (Caulerpa scalpelliformis) as a biosorbent for the removal of phenolic compounds from the post-tanning sectional stream. The effects of initial phenol concentration, contact time, temperature and initial pH of the solution on the biosorption potential of macro algal biomass have been investigated. Biosorption of phenol by modified green macro algae is best described by the Langmuir adsorption isotherm model. Biosorption kinetics of phenol onto modified green macro algal biomass were best described by a pseudo second order model. The maximum uptake capacity was found to be 20 mg of phenol per gram of green macro algae. A Boyd plot confirmed the external mass transfer as the slowest step involved in the biosorption process. The average effective diffusion coefficient was found to be 1.44 × 10⁻⁹ cm²/s. Thermodynamic studies confirmed the biosorption process to be exothermic.     

Adsorption of phenol and its derivatives from water using synthetic resins and low-cost natural adsorbents: a review

In this article, the technical feasibility of the use of activated carbon, synthetic resins, and various low-cost natural adsorbents for the removal of phenol and its derivatives from contaminated water has been reviewed. Instead of using commercial activated carbon and synthetic resins, researchers have worked on inexpensive materials such as coal fly ash, sludge, biomass, zeolites, and other adsorbents, which have high adsorption capacity and are locally available. The comparison of their removal performance with that of activated carbon and synthetic resins is presented in this study. From our survey of about 100 papers, low-cost adsorbents have demonstrated outstanding removal capabilities for phenol and its derivatives compared to activated carbons. Adsorbents that stand out for high adsorption capacities are coal-reject, residual coal treated with H3PO4, dried activated sludge, red mud, and cetyltrimethylammonium bromide-modified montmorillonite. Of these synthetic resins, HiSiv 1000 and IRA-420 display high adsorption capacity of phenol and XAD-4 has good adsorption capability for 2-nitrophenol. These polymeric adsorbents are suitable for industrial effluents containing phenol and its derivatives as mentioned previously. It should be noted that the adsorption capacities of the adsorbents presented here vary significantly depending on the characteristics of the individual adsorbent, the extent of chemical modifications, and the concentrations of solutes.     

Removal of phenol from aqueous solution by adsorption onto OTMAC-modified attapulgite

The potential of octodecyl trimethyl ammonium chloride (OTMAC)-modified attapulgite (AT) for phenol adsorption from aqueous solutions was studied. The comparison of natural AT and modified AT showed that it is possible to utilize the sonication-modified OTMAC-AT in the treatment of phenol-contaminated wastewaters. Batch sorption studies were carried out to evaluate the effect of contact time, shaking frequency, temperature and the amount of AT. The results showed that in a lab-scale reactor, at room temperature, with an amount of the modified AT added (2.5 g), and a shaking frequency of 140 rev/min, the adsorption rate of phenol could be 60.4% for a duration of 60 min. The sorption kinetics were described by a pseudo-second-order model, and the values of k and q(e) were 1.367 mg/ig min and 0.7901 ig/mg, respectively. The analysis of equilibrium data showed that the Freundlich isotherms were found to be applicable for the adsorption equilibrium data. K and 1/n were estimated to be 14.53 and 0.8438, respectively.     

酸水汽提净化水中酚的治理技术研究

采用吸附法对酸水汽提净化水中的酚进行了处理。这种方法不仅可以满足对实验浓度酚的处理,同时可以回收酚。通过吸收过程及不同流速对比实验得出:树脂的吸附效果显著,吸附能力较强,吸附时间较长;净化水的流速与吸附效果具有一定的线性关系;不同流速吸附效果不同,对应树脂需要再生的时间也不同。应用结果表明:吸附法中较可行的方法为树脂吸附法。     

Phenol removal from aqueous environments by natural & chemically modified kaolin clay

Natural, acid and base modified kaolin clays were studied for the sake of phenol and 4-chlorophenol removal from aqueous environments and their application to real ground and industrial wastewater samples. Scanning electron microscope (SEM), infrared spectroscopy (IR), X-ray diffraction (XRD), Thermo Gravimetric Analysis (TGA), Differential Thermal Analysis (DTA), and Surface area analysis were employed for characterization of the adsorbents microstructure. Operating factors such as adsorbent dose, solution pH, initial phenol concentration, and contact time were studied. The experimental data displayed that the increase of the adsorbent dose, contact time, and pH value from 2 to 7 increases the efficiency of the removal process. Optimal conditions for phenolic removal were; contact time of 300 min, primary phenol solution of 25 mg/L, pH 7 and 2.5 g/L as an appropriate adsorbent dose using crude (natural), acid modified and base modified kaolin clays. The higher phenolic removal efficiencies were obtained at 5 mg/L as 90, 97, 96.2%, respectively, for the adsorbents in the previously mentioned order. The adsorption capacity in the removal of phenol and 4-chlorophenol were 7.481 and 4.195, 8.2942 and 3.211, and 8.05185 and 18.565 mg/g, respectively, for the adsorbents in the same mentioned order. The adsorption equilibrium data were fitted and analyzed with four isotherm models, namely, Langmuir, Freundlich, Temkin, and Dubinin–Radushkevich isotherm equations. The adsorption process of phenol on studied adsorbents was exothermic, spontaneous and thermodynamically favorable proved by the negative values of their thermodynamic parameters ΔH° and ΔG°. The correlation coefficient (R²) for all concentrations was higher than 0.94, which indicates that in the studied system, the data suitably fit the first-order kinetics. The % desorption capacity was amounted to 96%, 91.11%, and 87.06% of adsorbed phenol, respectively, for the adsorbents in the previous order using 0.1N NaOH and 10% V/V ethanol solutions as eluents at 25°C, indicating the reusability of the adsorbents. Kaolin and its modified forms can be introduced as eco-friendly and low-cost adsorbents in water remediation implementation.