活性炭及活性炭纤维对CS2的吸附行为研究及其方法探讨

以活性炭纤维(ACF)对水中CS:的吸附处理作为研究对象,并与另外两种活性炭(颗粒活性炭GAC和粉末活性炭PAC)进行对比研究,展示了ACF对CS:的优异吸附性能与处理效果,即吸附容量大,吸附低浓度效果好.同时运用新的宽平衡浓度吸附试验方法,测试了ACF、GAC、PAC对CS2的吸附平衡曲线,并对几种常见的吸附等温方程...     

壳聚糖复合吸附剂去除水源水中天然有机物的试验

以壳聚糖为基质,制备出壳聚糖-活性炭复合吸附剂。并研究了其对水源水中天然有机物的吸附性能,以及吸附操作条件的影响。结果表明,壳聚糖复合吸附剂结合了二者的优势,对天然有机物具有较好的吸附效果,pH是影响吸附的主要因素。     

高锰酸钾改性活性炭的制备、表征及其吸附Pb2＋的特性

为提高活性炭对废水中Pb2＋的去除效率,采用不同浓度的KMnO4溶液对颗粒活性炭进行静置氧化/冷凝回流改性;利用BET测定了改性活性炭比表面积,并采用BET、SEM、FTIR和XRD等方法对其进行了表征;考察了吸附时间、投加量、pH值、温度对吸附Pb2＋的影响。结果表明,Pb2＋浓度为40 mg/L,在3 g/L的投加量下,0.01KMnO4-GAC和0.03KMnO4-GAC对Pb2＋的吸附去除率分别达到了92%和94%,是GAC对Pb2＋吸附去除率的1.84和1.88倍;在吸附剂3 g/L的投加量下,180 min基本达到吸附平衡;3种吸附剂对Pb2＋的吸附,随着pH值的降低而减少;而温度对吸附Pb2＋的影响相对较小。     

TiO2/活性炭催化剂对4-CP的吸附和光催化活性

采用常压金属有机物化学气相沉积技术在活性炭表面沉积构成纳米TiO2催化剂,XRD分析表明,沉积在活性炭表面的TiO2为锐钛矿晶型.TEM分析表明负载量为8%(wt)时,TiO2颗粒的粒径为10-20nm;载体负载前后BET面积仅改变了6%,表明负载TiO2后对活性炭的结构影响不大.利用Langmuir-Hinshelwood动力学模型探讨了TiO2/活性炭催化剂对4-CP的吸附行为和光催化活性之间的关系,求出4-CP降解反应速率常数Kr,在紫外光照条件下催化剂对4-CP的吸附明显增强.     

硅藻土和膨润土对重金属离子Zn~（2＋）、Pb~（2＋）及Cd~（2＋）的吸附特性

以硅藻土和膨润土作为吸附剂,考察微波加热与否条件下,不同吸附时间、不同吸附剂用量和不同pH值对硅藻土和膨润土分别吸附Zn2＋、Pb2＋、Cd2＋重金属离子的影响.实验结果表明,硅藻土和膨润土对3种重金属离子均有很好的吸附效果,吸附时间对去除率影响不大,数分钟即可达到吸附平衡,微波加热、增加吸附剂用量和提高pH值,都有利于提高3种重金属离子的去除率.     

互花米草活性炭对镉的吸附

进行了磷酸活化法不同浸渍比（0.5—3.0）及活化温度（400℃—700℃）条件下制备的互花米草活性炭对镉的吸附性能研究,采用静态吸附法,考察不同初始浓度条件下活性炭对镉的平衡吸附量,旨在探索吸附机理、影响因素、除镉吸附剂的最佳制备条件以及活性炭物化性质对镉吸附性能的影响.实验表明,浸渍比和活化温度是影响成品活性炭镉吸...     

活性炭纤维的表面结构及其吸附模式

迄今的吸附模式,Henry定律、Langmuir模型、BET模型、D-R方程、D-A方程都分别适用于不同的表面结构,对于活性炭纤维（Activated Corbon Fiber,ACF）这种特殊的炭吸附材料适用于哪种吸附模型,未见有文献专题论述。本论文在对ACF材料进行了大量表面结构研究的基础上,对ACF的表面结构与颗粒活性炭（GranularActivated Carbon,GAC）的表面进行了对比,并尝试性地对适用于ACF的吸附模式进行了计算和比较,得到了一些有价值的结论。     

大田条件下不同钝化剂对空心菜吸收镉的影响及机理

通过大田试验,研究4种钝化剂（赤泥、海泡石、钙镁磷肥和磷矿粉）对两茬空心菜（Ipomoea aquatica Forsk.）生长和镉吸收的影响。钝化剂施用量为：赤泥（0.5%和1.0%）、海泡石（0.3%和0.5%）、磷矿粉（450和900 kg.hm-2）、钙镁磷肥（450和900 kg.hm-2）。结果表明,各钝化剂均能显著降低土壤有效态镉质量分数,钝化能力大小表现为海泡石〉赤泥〉钙镁磷肥〉磷矿粉;钝化剂提高了空心菜地上部生物量,第1茬时（50 d）,施用高量赤泥、低量海泡石和高量钙镁磷肥处理生物量增加最为明显,地上部分别增加78.7%、75.2%和76.6%。第2茬（80 d）,高量赤泥与高量磷矿粉处理增加最高,地上部分别增加24.6%和34.5%。钝化剂对空心菜镉吸收影响不同,第1茬时对根系和地上部分别起促进和抑制作用,施用高量赤泥和高量海泡石最能抑制地上部镉累积,镉质量分数分别降低27.3%和23.2%。第2茬时,除海泡石外,钝化剂均显著抑制了根系和地上部的镉吸收,高量磷矿粉和赤泥效果最佳。总体来看,赤泥是保障农产品安全的最佳钝化材料,海泡石效果最差。     

驯化的活性污泥强化降解土壤中氯酚的研究

以接种驯化的活性污泥为生物强化手段,在小型生物泥浆反应器中,研究了受氯酚污染土壤的修复情况.考查了添加驯化活性污泥对土壤中氯酚降解的强化效果,并对土壤中邻氯苯酚(2-CP)、对氯苯酚(4-CP)和2,4-二氯酚(2,4-DCP)在单一污染体系中的降解情况进行了研究.结果表明,在生物泥浆反应器中添加用邻氯苯酚(2-CP)驯化的活性污泥可以明显地促进土壤泥浆中2-CP的降解,是一种有效的强化手段.该方法对土壤中的4-CP和2,4-DCP也有较好的降解效果,对三种氯酚的降解速率由大到小的顺序为2-CP,4-CP,2,4-DCP.反应结束时,泥浆体系中剩余的氯酚基本都残留在土壤中,固液分离后的水相可以直接排放或者在土壤修复过程中循环利用.     

锆负载量对锆镁改性膨润土吸附水中磷酸盐的影响

制备了锆氧化物(ZrO_2)含量分别为2.98%、7.81%、13.73%和33.70%的4种锆镁改性膨润土,并考察了锆负载量对锆镁改性膨润土吸附水中磷酸盐的影响.结果表明,较高的吸附剂投加量有利于水中磷酸盐被锆镁改性膨润土所吸附去除.锆镁改性膨润土吸附水中磷酸盐的动力学过程符合准二级动力学模型.锆镁改性膨润土对水中磷酸盐的吸附等温行为可以采用Langmuir、Freundlich和Dubinin-Redushckevich (D-R)等温吸附模型进行描述.增加溶液pH值不会导致锆镁改性膨润土对水中磷酸盐吸附能力的下降.锆镁改性膨润土对水中磷酸盐的吸附能力随其锆含量的增加而增加.但是,从总体上,锆镁改性膨润土中单位质量ZrO_2对水中磷酸盐的最大吸附量则随其锆含量的增加而降低.研究结果说明,锆镁改性膨润土适合作为一种吸附剂去除水中的磷酸盐,较高的锆负载量有利于增强锆镁改性膨润土吸附水中磷酸盐的能力,而较低的锆负载量则有利于提高锆镁改性膨润土中单位质量ZrO_2对水中磷酸盐的吸附能力.     

Removal of fluoride by thermally activated carbon prepared from neem (Azadirachta indica) and kikar (Acacia arabica) leaves

The present investigation deals with fluoride removal from aqueous solution by thermally activated neem (Azadirachta indica) leaves carbon (ANC) and thermally activated kikar (Acacia arabica) leaves carbon (AKC) adsorbents. In this study neem leaves carbon and kikar leaves carbon prepared by heating the leaves at 400 degrees C in electric furnace was found to be useful for the removal of fluoride. The adsorbents of 0.3 mm and 1.0 mm sizes of neem and kikar leaves carbon was prepared by standard sieve. Batch experiments done to see the fluoride removal properties from synthetic solution of 5 ppm to study the influence of pH, adsorbent dose and contact time on adsorption efficiency The optimum pH was found to be 6 for both adsorbents. The optimum dose was found to be 0.5g/100 ml forANC (activated neem leaves carbon) and 0.7g/100 ml forAKC (activated kikar leaves carbon). The optimum time was found to be one hour for both the adsorbent. It was also found that adsorbent size of 0.3 mm was more efficient than the 1.0 mm size. The adsorption process obeyed Freundlich adsorption isotherm. The straight line of log (qe-q) vs time at ambient temperature indicated the validity of langergren equation consequently first order nature of the process involved in the present study. Results indicate that besides intraparticle diffusion there maybe other processes controlling the rate which may be operating simultaneously. All optimized conditions were applied for removal of fluoride from four natural water samples.     

Recovery efficiency of the hydrofluorocarbon (HFC‐134a) by activated carbons of different physicochemical properties

The adsorption characteristics of 1,1,1,2‐tetrafluoroethane (HFC‐134a) on activated carbon were investigated to evaluate the recovery efficiency of HFC‐134a by six activated carbons (two granular activated carbons (GAC1 and GAC2), one high‐surface area activated carbon (HAC), and three activated carbon fibers (ACF10, ACF15, and ACF20)). HFC‐134a adsorption on the activated carbons increased with increase in the specific surface area and pore volume of the activated carbon. The differential heat of the HFC‐134a adsorption decreased with increase in the percentage of the micropore volume to the total pore volume. The adsorption model of HFC‐134a on the activated carbon could be based on the Langmuir model. The constant a of the Langmuir plot of HAC and ACF20 is smaller than GAC1 or GAC2 and ACF10 or ACF15, respectively. The constant W_s of HAC has the largest value. The constant a was correlated to the heat of adsorption. It is concluded that the largest amount of HFC‐134a was adsorbed on HAC, and the least amount of interaction occurred between HFC‐134a and the HAC. The amount of HFC‐134a adsorbed on the activated carbons over time was applied to the Sameshima equation. The adsorption rate constant of HFC‐134a on HAC was the largest. The HAC could be suitable for the recovery of HFC‐134a.     

海泡石黏土矿物对Cu2+的吸附动力学研究

研究分析了海泡石黏土矿物对铜离子的吸附性能和动力学特征,结果表明,海泡石黏土矿物对Cu~(2 )吸附的最佳pH值为6.0左右,随着pH值的增大,吸附作用减弱;在[Cu~(2 )]=100mg·l~(-1),溶液pH值为6,吸附时间为2h时,添加0.1 g海泡石,海泡石对Cu~(2 )的吸附去除率仅为39.5%,当海泡石用量提高至0.4 g时,其对Cu~(2 )的吸附去除率提高到94.8%;实验结果同样显示,18min内有90%的Cu~(2 )被海泡石吸附,随着吸附时间的增加,吸附作用趋于稳定,2h可达到吸附平衡。该吸附过程符合Langmuir和Freundlich等温吸附方程.同时,分别采用拟一级模型和拟二级模型考察了吸附动力学,并计算了这些动力学模型的速率常数.实验数据和拟二级模型计算结果之间有较好的相关性.     

硝酸改性活性炭对渗滤液中小分子有机物的吸附性能

以硝酸为改性剂,分别采用浸渍和浸渍-高温热处理方法对活性炭进行了改性.低温氮吸附结果表明,活性炭表面积和微孔体积在浸渍后都变小,再经过高温热处理后则都变大.酸碱滴定显示,改性后活性炭表面酸性都增大,其中浸渍的酸性最大.对填埋场渗滤液中小分子有机物进行了等温线和动力学吸附实验,结果发现改性后活性炭对有机物的吸附量增加;硝酸浸渍活性炭吸附速率降低,而浸渍-高温热处理则使吸附速率明显加快.针对渗滤液中小分子有机物,硝酸浸渍-高温热处理的活性炭吸附效果最好,吸附量最大,吸附速率最快.     

Adsorption selectivity of salicylic acid and 5-sulfosalicylic acid onto hypercrosslinked polymeric adsorbents

Both bottle-point and column-feeding experiments involving different solutes and sorbents were carried out to investigate the adsorption selectivity and separation performance of salicylic acid and 5-sulfosalicylic acid. Their adsorption isotherms onto such hypercrosslinked polymeric adsorbents as NDA-100 and NDA-99 could be well described by the Freundlich equations whose characteristics describe extrathermic and favorable adsorption processes. The adsorption towards NDA-100 mainly depended on the π-π interaction, while that towards NDA-99 was extremely influenced by the static-electric interaction. Additionally, the adsorptive capacity of salicylic acid on NDA-99 decreased while it increased on NDA-100 with the presence of 5-sulfosalicylic acid in the adsorptive environment as the competitive component. Comparatively, the adsorption capacity of 5-sulfosalicylic acid decreased on both resins with salicylic acid as the competitive component. In fact, the difference in the interaction between adsorbent and adsorbate resulted in the straight antagonism on the effective adsorption sites on the adsorbent. In conclusion, the adsorption selectivity of salicylic acid onto NDA-100 was obviously larger than that onto NDA-99 with the existence of 5-sulfosalicylic acid in the adsorptive environment. A satisfactory separation and recovery of tested solutes in aqueous phase could be foreseeably achieved by the sequencing adsorption technique involving NDA-100 as well as NDA-99.     

The influence of chlorinated aromatics' structure on their adsorption characteristics on activated carbon to tackle chemical spills in drinking water source

This study focused on evaluating the efficiency of powdered activated carbon (PAC) adsorption process and tackling chlorobenzenes and chlorophenols spill in drinking water source. The adsorption kinetics and PAC’s capacities for five chlorobenzenes and three chlorophenols at drinking water contamination levels were studied in order to determine the influence of different functional groups on the adsorption behavior. The results showed that PAC adsorption could be used as an effective emergency drinking water treatment process to remove these compounds. The adsorption kinetics took 30 min to achieve nearly equilibrium and could be described by both pseudo first-order and pseudo second-order models. A mathematic relationship was developed between the pseudo first-order adsorption rate constant, k₁, and the solutes’ properties including lgK_ow, polarizability and molecular weight. The Freundlich isotherm equation could well describe the adsorption equilibrium behaviors of chlorinated aromatics with r² from 0.920 to 0.999. The H-bond donor/acceptor group, hydrophobicity, solubility and molecular volume were identified as important solute properties that affect the PAC adsorption capacity. These results could assist water professionals in removing chlorinated aromatics during emergency drinking water treatment.     

Potential of rice husk ash in atrazine removal

An experimental study was carried out to explore the possibility of using a prepared microporous material, Rice Husk Ash (RHA) as an alternative to the commercial Powdered Activated Carbon (PAC), to remove atrazine (ATZ) pesticide from aqueous solution. The effects of contact time and pH on the adsorption were studied using the batch technique. Based on Hückel model calculations, the zwitterion behaviour of atrazine molecule was proved to be related to the pH of zero charge point of adsorbents (6.8 for RHA and 8.2 for PAC). The results showed that the Pseudo Second Order model is applicable to both adsorbents, suggesting that chemisorption is the rate-limiting step. The equilibrium data fitted well with the Langmuir model in the case of RHA, whereas the Freundlich model better fitted the equilibrium data in the PAC case, suggesting the existence of multi-layer adsorption of atrazine. The adsorption for RHA was found to be feasible and spontaneous, with a removal capacity of atrazine of more than 7?mg?g^?1. With regard to the BET surface, this removal capacity (50.5?µg_ATZ / m²_RHA) was 25% better than that PAC (37.75µg_ATZ / m²_PAC).     

Removal of phenol by powdered activated carbon adsorption

In this study, the adsorption performance of powdered activated carbon (PAC) on phenol was investigated in aqueous solutions. Batch adsorption studies were performed to evaluate the effects of various experimental parameters like PAC type, PAC dose, initial solution pH, temperature and pre-oxidation on the adsorption of phenol by PAC and establish the adsorption kinetics, thermodynamics and isothermal models. The results indicated that PAC adsorption is an effective method to remove phenol from water, and the effects of all the five factors on adsorption of phenol were significant. The adsorption rate of phenol by PAC was rapid, and more than 80% phenol could be absorbed by PAC within the initial 10 min. The adsorption process can be well described by pseudo-second-order adsorption kinetic model with rate constant amounted to 0.0313, 0.0305 and 0.0241 mg·μg ^-1·min ^-1 with coal, coconut shell and bamboo charcoal. The equilibrium data of phenol absorbed onto PAC were analyzed by Langmuir, Freundlich and Tempkin adsorption isotherms and Freundlich adsorption isotherm model gave the best correlation with the experimental data. Thermodynamic parameters such as the standard Gibbs free energy (?G^o), enthalpy (?H^o) and entropy (?S^o) obtained in this study indicated that the adsorption of phenol by PAC is spontaneous, exothermic and entropy decreasing.