Comparison of four supports for adsorption of reactive dyes by immobilized Aspergillus fumigatus beads

Four materials, sodium carboxymethylcellulose (Na-CMC), sodium alginate (SA), polyvinyl alcohol (PVA), and chitosan (CTS), were prepared as supports for entrapping fungus Aspergillus fumigatus. The adsorption of synthetic dyes. Reactive Brilliant Blue KN-R, and Reactive Brilliant Red K-2BP, by these immobilized gel beads and plain gel beads was evaluated. The adsorption efficiencies of Reactive Brilliant Red K-2BP and Reactive Brilliant Blue KN-R by CTS immobilized beads were 89.1% and 93.5% in 12 h, respectively. The adsorption efficiency by Na-CMC immobilized beads was slightly lower than that of mycelial pellets. But the dye culture mediums were almost completely decolorized in 48 h using the above-mentioned two immobilized beads (exceeding 95%). The adsorption efficiency by SA immobilized beads exceeded 92% in 48 h. PVA-SA immobilized beads showed the lowest adsorption efficiency, which was 79.8% for Reactive Brilliant Red K-2BP and 92.5% for Reactive Brilliant Blue KN-R in 48 h. Comparing the adsorption efficiency by plain gel beads, Na-CMC plain gel beads ranked next to CTS ones. SA and PVA-SA plain gel beads hardly had the ability of adsorbing dyes. Subsequently, the growth of mycelia in Na-CMC and SA immobilized beads were evaluated. The biomass increased continuously in 72 h. The adsorption capacity of Reactive Brilliant Red K-2BP and Reactive Brilliant Blue KN-R by Na-CMC immobilized beads was 78.0 and 86.7 mg/g, respectively. The SEM micrographs show that the surface structure of Na-CMC immobilized bead is loose and finely porous, which facilitates diffusion of the dyes.     

聚甲基丙烯酸-Fe3O4纳米吸附剂的吸附性能

以共沉淀法制备纳米Fe3O4,通过在颗粒表面接枝聚甲基丙烯酸(PMAA),制备了一种新型磁性纳米吸附剂.用透射电镜(TEM)、X-衍射分析(XRD)等对其进行了表征,并考察了它对酸性玫瑰红B(RB)的吸附性能.结果表明,制备的磁性微球平均粒径18nm.该吸附剂能有效去除RB,吸附速率很快,在5min内基本达到平衡.等温吸附数据符合Langmuir模型,饱和吸附容量为0.2mg/mg,吸附常数为7.2mL/mg.吸附为吸热过程,288～318K时,焓变为18kJ/mol.     

改性壳聚糖季铵盐的研制及其对高氯酸盐的吸附研究

通过将壳聚糖季铵盐改性以实现固定化,并用于水体中ClO 4-的吸附去除,研究了改性过程相关工艺参数对产物吸附能力的影响,考察了产物的吸附和再生性能.结果表明,戊二醛的交联性能优于甲醛和环氧氯丙烷的交联性能,戊二醛的最佳投加量为6.82%,最佳的反应温度为45℃,pH值在3～12之间交联反应均能很好地进行,从而实现壳聚糖...     

石棉摩擦材料废弃物制吸附剂对染料的吸附研究

以石棉摩擦材料加工废弃物为材料制得的吸附剂,在色度５０００倍溶液中对阳离子黄Ｘ－５ＧＬ的静态吸附量为１５９．６８ｍｇ／ｇ,在色度５００倍的溶液中对阳离子艳蓝ＲＬ的静态吸附量为７９．６８ｍｇ／ｇ;对毛纺厂腈纶染缸废水的处理量可达２８０ｍｌ／ｇ,对活性染料亦有较好的吸附效果,吸附饱和吸附剂可通过后处理实现资源化。     

水溶液中磷的吸附与预测模型

用红壤和水滑石作为吸附剂,进行了水溶液中磷的等温吸附试验,目的是研究吸附剂(W)0效应和起始吸附质浓度(C)0效应对经典方程参数变异的影响,分析经典Langmuir和Freundlich方程在液/固离子吸附体系中的适用性和验证新吸附模型的预测精确度。试验结果显示,红壤和水滑石在吸附磷的过程中存在明显的吸附剂和吸附质浓度效应,单一的经典方程仅适用于给定吸附剂或吸附质浓度的体系,因此,用其参数来表征不同吸附剂的吸附能力或描述不同吸附剂或吸附质浓度水平上的吸附规律具有一定的局限性。数据分析表明,单位吸附剂的平衡吸附量qe不唯一由初始浓度C0或液相平衡浓度Ce所决定,而是C0/W0或Ce/W0的函数,新吸附预测模型能较好的反映红壤和水滑石磷吸附的总体趋势。新的预测模型用来描述红壤和水滑石的磷吸附曲线时具有较高的精确度。在实践中,新模型可用来预测给定条件下磷的吸附量和所需吸附剂的用量。     

A novel aminated polymeric adsorbent for removing refractory dissolved organic matter from landfill leachate treatment plant

Refractory dissolved organic matter (DOM) from landfill leachate treatment plant was with high dissolved organic carbon (DOC) content. An aminated polymeric adsorbent NDA-8 with tertiary amino groups and sufficient mesopore was synthesized, which exhibited high adsorption capacity to the DOM (raw water after coagulation). Resin NDA-8 performed better in the uptake of the DOM than resin DAX-8 and A100. Electrostatic attraction was considered as the decisive interaction between the adsorbent and adsorbate. Special attention was paid to the correlation between porous structure and adsorption capacity. The mesopore of NDA-8 played a crucial role during uptake of the DOM. In general, resin in chloride form performed a higher removal rate of DOC. According to the column adsorption test, total adsorption capacity of NDA-8 was calculated to 52.28 mg DOC/mL wet resin. 0.2 mol/L sodium hydroxide solution could regenerate the adsorbent efficiently.     

Ion adsorption components in liquid/solid systems

Experiments on Zn^2＋ and Cd^2＋ adsorptions on vermiculite in aqueous solutions were conducted to investigate the widely observed adsorbent concentration effect on the traditionally defined adsorption isotherm in the adsorbate range 25--500 mg/L and adsorbent range 10--150 g/L. The results showed that the equilibrium ion adsorption density did not correspond to a unique equilibrium ion concentration in liquid phase. Three adsorbate/adsorbent ratios, the equilibrium adsorption density, the ratio of equilibrium adsorbate concentration in liquid phase to adsorbent concentration, and the ratio of initial adsorbate concentration to adsorbent concentration, were found to be related with unique values in the tested range. Based on the assumption that the equilibrium state of a liquid/solid adsorption system is determined by four mutually related components： adsorbate in liquid phase, adsorbate in solid phase, uncovered adsorption site and covered adsorption site, and that the equilibrium chemical potentials of these components should be equalized, a new model was presented for describing ion adsorption isotherm in liquid/solid systems. The proposed model fit well the experimental data obtained from the examined samples.     

桉树遗态Fe/C复合材料对水中Cr(Ⅵ)的动态吸附探讨

为研究桉树遗态Fe/C复合材料（PBGC-Fe/C）对水中Cr（Ⅵ）的净化能力及其动态吸附过程,以PBGC-Fe/C吸附剂为固定床,选择溶液初始pH、进水流速、溶液初始浓度、吸附剂投加量和环境温度为影响因素开展动态吸附试验分析.结果表明:在溶液初始pH为2,进水流速为5.14 mL/min,吸附剂投加量为2 g和环境温度为35℃的条件下,PBGC-Fe/C对水中Cr（Ⅵ）的最佳平衡吸附容量达到10.72 mg/g;提高溶液初始pH、进水流速和溶液初始质量浓度或降低吸附剂投加量均可缩短反应穿透时间和衰竭时间;Thomas和Yoon-Nelson模型均能较好地描述PBGC-Fe/C对水中Cr（Ⅵ）的动态吸附过程,说明该吸附过程中内部扩散和外部扩散均为非限速步骤,吸附速率常数（k_Th）随着进水流速的增大从1.3×10-3 mL/（min·mg）升至2.6×10-3 mL/（min·mg）,随着溶液初始质量浓度的增大从2.7×10-3 mL/（min·mg）降至1.4×10-3 mL/（min·mg）.研究显示,PBGC-Fe/C对水中Cr（Ⅵ）具有较好的动态吸附能力,具有较好的市场应用前景.      

介体厌氧催化活性艳红K-2BP脱色及构效特性研究

研究了筛选出的4种结构相似的醌类氧化还原介体对活性艳红K-2BP厌氧脱色的促进作用,并分析了介体促进效果与其化学结构活性相关性. 在35℃中温厌氧条件下,采用间歇批量实验法,测定不同体系中介体催化活性艳红K-2BP脱色效果.结果表明,①结构相似的醌类氧化还原介体蒽醌(AQ)、1,5-二氯蒽醌(1,5-AQ)、1,8-二氯蒽醌(1,8-AQ)和1,4,5,8-四氯蒽醌(1,4,5,8-AQ),均促进活性艳红K-2BP脱色,反应速率提高了1.4～3倍;②当醌类介体投加浓度为4 mmol·L^-1,活性艳红K-2BP染料浓度为300 mg·L^-1时,促进作用由大到小的顺序为:1,8-AQ>1,5-AQ>AQ>1,4,5,8-AQ;③ 当活性艳红K-2BP染料浓度为300 mg·L^-1时,1,8-AQ促进效果最佳且脱色速率常数随1,8-AQ浓度的增加而增加呈线性关系;④介体促进效果与介体取代基团数量、位置和电子共轭效应相关.本研究初步建立了氧化还原介体定性/定量构-效关系数学模型,探究和完善非水溶性氧化还原介体催化强化理论体系.     

改性硅藻土对三种有机染料的吸附作用研究

以天然硅藻土分别负载十六烷基三甲基溴化铵(CTMAB)、四甲基溴化铵(TMAB)和壳聚糖,制得一系列改性硅藻土,研究了改性硅藻土吸附水中的阴离子染料(活性红120)、阳离子染料(亚甲基蓝)、酸性染料(玫瑰红B)的适宜条件及吸附机理.结果表明,天然硅藻土对亚甲基蓝、四甲基溴化铵改性硅藻土对玫瑰红B和壳聚糖改性硅藻土对活性红120的饱和吸附量分别为51.15、49.56、56.64mg.L-1,效果良好,可被直接利用.延长吸附时间、增大吸附剂用量、控制溶液的pH值(<6)都能提高改性硅藻土吸附剂的吸附效果;3种染料在各自吸附剂上的平衡吸附量Qe与平衡浓度Ce之间的关系均符合Freundlich等温吸附方程,表明改性硅藻土吸附染料以分配作用、弱的溶质吸收为主.改性剂的引入可以改变硅藻土的表面电性,从而对不同类型染料的吸附能力产生不同影响.     

Brilliant red X-3B uptake by a novel polycyclodextrin-modified magnetic cationic hydrogel: Performance, kinetics and mechanism

A novel polycyclodextrin-modified magnetic cationic hydrogel (PCD-MCH) was developed and its performance, kinetics and mechanism for the removal of reactive brilliant red X-3B (X-3B) were studied. The results showed that the zeta-potential of PCD-MCH was 32.8 to 16.7 mV at pH 3.0–10.5. The maximum X-3B adsorption capacity of PCD-MCH was 2792.3 mg/g. The adsorption kinetics could be well-described by the Weber–Morris model and the homogeneous surface diffusion model (HSDM). Diffusion stages corresponding to surface or film diffusion, intra-particle or wide mesopore diffusion, and narrow mesopore/micropore diffusion occurred at 0–120, 120–480 and 480–1200 min, respectively. The latter two diffusion stages were rate-controlling for X-3B adsorption kinetics. At the initial X-3B concentration of 600 mg/L, the diffusion coefficient (D_s) and external mass transfer coefficient in the liquid phase (k_F) were 3 × 10^?11 cm²/min and 4.68 × 10^?6 cm/min, respectively. X-3B approaching the center of PCD-MCH particles could be observed at 360 min. At the end of the third diffusion stage, the C_p at q/q_e = 0 was 45.20 mg/L, which was close to the homogeneous C_p value of 46 mg/L along the radius of PCD-MCH particles. At pH 3.0–10.0, PCD-MCH showed stable X-3B adsorption capacities. After five regeneration-reuse cycles, the residual adsorption capacity of regenerated PCD-MCH was higher than 892.7 mg/g. The corresponding adsorption mechanism was identified as involving electrostatic interactions, cyclodextrin cavities and hydrogen bonds, of which cyclodextrin cavities showed prominent capture performance towards dye molecules through the formation of inclusion complexes.     

东方伊萨酵母YP-1对染料活性艳红K-2BP的脱色

利用含染料的选择性培养基从土壤中分离出一株对活性艳红K-2BP有明显脱色效果的酵母菌株YP-1,经鉴定为东方伊萨酵母Issatchenkia orientalis.结果表明,该酵母菌对￡400mg/L的活性艳红K-2BP有较好的脱色效果.对于活性艳红K-2BP起始浓度为100mg/L的培养基,该菌株可在12h达到99%以上的最大脱色率,其最佳接种量为10%(体积分数),最适pH值在3~9之间,氮源(NH4)2SO4的浓度30.02%,碳源葡萄糖的浓度30.2%.脱色机理研究结果表明,该酵母对活性艳红K-2BP的去除是先吸附后生物降解.此外,该菌株对初始浓度为200mg/L的偶氮染料活性黑KN-B的脱色率也可达99.5%.     

天然菱铁矿改性及强化除砷研究

我国高砷地下水分布广泛,经济、高效地饮用水除砷技术受到广泛关注.静态批实验采用资源丰富、价格便宜的天然菱铁矿为主要原材料,考虑灼烧温度、时间及添加黏合剂等因素确定最优改性条件使除砷效果达到最佳.结果表明,在加铝量为10 mg.g-1、350℃下恒温灼烧90 min后造粒达到强度要求并除砷效果较优.25℃、固液比为0.5 g∶50 mL、As(Ⅲ)和As(Ⅴ)初始浓度为5 mg.L-1时,吸附后溶液中残留As浓度均<10μg.L-1.静态吸附批实验结果表明,25℃时,接触反应时间为12 h可达到吸附平衡,吸附过程较好地符合Lagergren假二级吸附速率方程;最优改性天然菱铁矿对砷的吸附规律可用Langmuir和Freundlich等温吸附模型很好地描述,As(Ⅲ)、As(Ⅴ)饱和吸附容量分别可以达到1 039、1 026μg.g-1.结合XRD、SEM等研究方法和比表面及孔结构分析初步探讨天然菱铁矿改性以及除砷的主要机制.分析表明,改性后天然菱铁矿比表面积大幅度增大,孔径减小,且在表面活化生成一层圆球状的含Fe(Ⅱ)和Fe(Ⅲ)的化合物.改性天然菱铁矿是一种值得进一步研究并实际应用的除砷材料.     

磁性有序介孔碳的制备及其对水中双酚A的吸附

采用水热法成功制备了磁性有序介孔碳（Fe-OMC）,用于吸附水中双酚A （BPA）.采用高倍投射电镜、X射线衍射仪、傅里叶红外光谱仪、比表面积分析仪和振动样品磁强计对Fe-OMC进行表征.结果表明,该吸附剂具备较大的比表面积、独特的有序介孔孔道结构、丰富的含氧官能团以及较强的超顺磁性.Fe-OMC能够高效地吸附去除水中的BPA,平衡吸附量可达72.62mg/g,经过外加磁场分离回收后依旧具备较好的吸附性能.随着BPA浓度从1mg/L提高到20mg/L,其平衡吸附量由8.33mg/g增至91.78mg/g.随着pH值的升高呈现出先降低后升高再降低的趋势,最高吸附量出现在pH=8（75.34mg/g）.Fe-OMC对BPA的吸附过程可用准二级吸附动力学模型和Langmuir吸附等温模型进行描述.计算的热力学参数表明,Fe-OMC对BPA的吸附过程是自发进行的放热过程.     

磁性有序介孔碳的制备及其对水中双酚A的吸附

采用水热法成功制备了磁性有序介孔碳（Fe-OMC）,用于吸附水中双酚A （BPA）.采用高倍投射电镜、X射线衍射仪、傅里叶红外光谱仪、比表面积分析仪和振动样品磁强计对Fe-OMC进行表征.结果表明,该吸附剂具备较大的比表面积、独特的有序介孔孔道结构、丰富的含氧官能团以及较强的超顺磁性.Fe-OMC能够高效地吸附去除水中的BPA,平衡吸附量可达72.62mg/g,经过外加磁场分离回收后依旧具备较好的吸附性能.随着BPA浓度从1mg/L提高到20mg/L,其平衡吸附量由8.33mg/g增至91.78mg/g.随着pH值的升高呈现出先降低后升高再降低的趋势,最高吸附量出现在pH=8（75.34mg/g）.Fe-OMC对BPA的吸附过程可用准二级吸附动力学模型和Langmuir吸附等温模型进行描述.计算的热力学参数表明,Fe-OMC对BPA的吸附过程是自发进行的放热过程.     

活性炭纤维对活性染料的吸附动力学研究

研究了活性炭纤维从水溶液中吸附4种活性染料（活性艳红K-2BP、活性翠蓝KN-G、活性金黄K-3RP、活性黑KN-B）的吸附特性,从动力学角度探讨了吸附机理.结果表明,活性炭纤维对4种染料的平衡吸附量q_e均随着初始浓度和温度的增加而升高,相同条件下,q_e的大小顺序为：活性艳红＞活性金黄＞活性黑＞活性翠蓝.吸附过程符合伪二级吸附速率方程,染料分子的空间结构、大小和极性是影响初始吸附速率的主要因素.活性炭纤维对4种染料的吸附活化能都比较低,依次为16 .42、3 .56、5 .21和26 .38 kJ·mol^-1,说明吸附过程以物理吸附为主.     

β-环糊精/环氧氯丙烷聚合物的制备及其对双酚S的吸附特性

BPS（双酚S）用途广泛,但存在水环境污染问题,容易引起类似于双酚A的雌激素反应,因此需要寻求高效的吸附剂从水溶液中将其脱除.在NaOH水溶液中,以环氧氯丙烷为交联剂,合成了β-CDP（β-环糊精/环氧氯丙烷聚合物）,用于吸附水溶液中的BPS.基于此,考察了吸附时间、pH、初始ρ（BPS）、β-CDP用量对吸附性能的影响以及β-CDP的再生性能,探讨了吸附动力学、等温吸附模型和吸附机理.结果表明:①在温度为298 K、pH为5.4、β-CDP用量为0.05 g、初始ρ（BPS）为100 mg/L、BPS溶液体积为50 mL、吸附时间为60 min的条件下,BPS吸附量为69.7 mg/g,吸附率为69.7%;②吸附动力学符合准二级动力学模型,表明化学吸附为速率控制步骤;③Langmuir吸附等温模型的成功拟合表明,吸附BPS在β-CDP表面上形成了单分子层覆盖;④β-CDP吸附BPS为放热过程,低温有利于吸附的进行;⑤与初始吸附量（69.7 mg/g）相比,β-CDP连续再生6次,BPS吸附量仍可达68.1 mg/g;⑥吸附机理是通过BPS的羟基与β-CDP形成氢键作为推动力,并借助β-CD（β-环糊精）空腔内部的疏水作用,使得BPS进入空腔形成包结物.研究显示,β-CDP对水溶液中的BPS具有良好的吸附性能,再生循环使用稳定性高,具有较高的性价比.      

γ-Fe_2O_3/膨胀石墨复合材料吸附废水中六价铬的应用研究

介绍了采用溶胶凝胶法合成新型的复合材料-磁性的γ-Fe_2O_3膨胀石墨(MEG)复合材料。通过采用X-射线衍射(XRD)、扫描电子显微镜(SEM)、透射电子显微镜(TEM)以及X-光电子能谱仪(XPS)对该复合材料MEG进行了表征,结果表明MEG中γ一Fe_2O_3的粒径约为50nm,而且其中γ一Fe_2O_3和膨胀石墨通过C=O相互作用。复合材料MEG作为新型的六价铬吸附剂,通过吸附时间、初始溶液的pH值以及再生性对该吸附过程进行了考察。结果表明:在40 min内MEG吸附六价铬的过程基本达到平衡;在初始溶液的pH为3.5时,MEG对六价铬的最大吸附量可以达到16.4mg/g;而且该复合材料MEG重复使用3次后吸附效果基本没有下降。因此,复合材料MEG对于废水中六价铬的处理有选择性吸附作用,而且初始溶液的pH值对其吸附过程起着重要作用。     

磁性纳米复合吸附剂PFM对铜的吸附性能与吸附机理研究

制备了磁性纳米复合吸附剂PAM@Fe₃O₄/MnO₂(PFM),用于含铜废水的吸附实验研究,考察了吸附剂投加量、重金属溶液初始浓度、吸附时间等因素对吸附效果的影响。实验结果表明:磁性纳米复合吸附剂PFM可有效去除水中的铜离子,在Cu2+浓度为50 mg/L,pH为6.0,吸附剂量为1.6 g/L的条件下,在400 min达到吸附平衡,吸附容量可达到30.29 mg/g,Cu2+去除率可达到97%。吸附-再生循环实验证实PFM具有良好的再生性能,在去除Cu2+方面具有很好的实际应用前景。VSM分析表明:纳米PFM具备超顺磁性和铁磁性的优势;PFM的XRD图谱显示,PAM附着于纳米Fe₃O₄/MnO₂表面,增强了其与溶液中金属离子接触的表面积,有利于对金属离子的吸附;在纳米PFM吸附剂的FTIR中出现PAM中的酰胺键,印证了Fe₃O₄/MnO₂与PAM成功制备为磁性纳米复合吸附剂PFM。     

Sequestration of toxic Pb(Ⅱ) ions by chemically treated rubber(Hevea brasiliensis) leaf powder

Rubber leaf powder(an agricultural waste) was treated with potassium permanganate followed by sodium carbonate and its performance in the removal of Pb(Ⅱ) ions from aqueous solution was evaluated.The interactions between Pb(Ⅱ) ions and functional groups on the adsorbent surface were confirmed by Fourier transform infrared(FT-IR) spectroscopy,scanning electron microscopy(SEM) coupled with X-ray energy dispersive spectroscopy(EDX).The effects of several important parameters which can affect adsorption capacity such as pH,adsorbent dosage,initial lead concentration and contact time were studied.The optimum pH range for lead adsorption was 4-5.Even at very low adsorbent dosage of 0.02 g,almost 100% of Pb(Ⅱ) ions(23 mg/L) could be removed.The adsorption capacity was also dependent on lead concentration and contact time,and relatively a short period of time(60-90 min) was required to reach equilibrium.The equilibrium data were analyzed with Langmuir,Freundlich and Dubinin-Radushkevich isotherms.Based on Langmuir model,the maximum adsorption capacity of lead was 95.3 mg/g.Three kinetic models including pseudo first-order,pseudo second-order and Boyd were used to analyze the lead adsorption process,and the results showed that the pseudo second-order fitted well with correlation coefficients greater than 0.99.