无机陶瓷纳滤膜分离高钠盐废水中的锶

本实验研究表明，仅用截留分子量为1000的无机陶瓷纳滤膜分离高钠盐模拟溶液中的锶，分离效果并不理想。为提高陶瓷纳滤膜对锶的选择分离效果，选择了分子量为3000的聚丙烯酸作为陶瓷纳滤膜分离的强化剂，重点探讨了溶液pH值、聚丙烯酸浓度、温度及离子强度对模拟溶液盐分离效果和膜通量的影响，并得到了适宜的锶钠分离条件。实验结果表明，在适宜条件下，通过聚丙烯酸强化和两级分离，陶瓷纳滤膜可大大提高模拟溶液中锶离子的选择分离效果，锶／钠的分离因子高达205。     

LVJ纳滤膜对磺胺二甲基嘧啶截留性能

用LVJ-NF102聚酰胺纳滤膜在LJ-2540ST卷式膜中试设备中进行纳滤截留水体中磺胺二甲基嘧啶实验,考察操作时间、操作压力、磺胺二甲基嘧啶浓度和离子强度等因素对纳滤膜截留磺胺二甲基嘧啶的影响.结果表明,LVJ纳滤膜对磺胺二甲基嘧啶的截留率100 min后基本稳定;随操作压力的增加,LVJ纳滤膜通量和对磺胺二甲基嘧啶的截留率都增大;随着溶液中磺胺二甲基嘧啶浓度的增加,LVJ纳滤膜通量下降,对磺胺二甲基嘧啶的截留率先增大后维持不变;随溶液中离子强度的增加,LVJ纳滤膜通量和对磺胺二甲基嘧啶的截留率都减小.在磺胺二甲基嘧啶浓度为28.2 mg/L、操作压力为0.4 MPa条件下,LVJ纳滤膜5 min可使溶液中磺胺二甲基嘧啶截留82.7％.     

苦咸水脱盐的纳滤技术的研究

着重考察纳滤装置对苦咸水中Cl-、Mg2+、Ca2+的去除作用以及影响纳滤膜工作的因素。结果表明:(1)0.60MPa为纳滤膜最佳的操作压力;(2)温度对产水通量和离子去除率有很大影响,宜控制在20℃;(3)纳滤膜运行周期为12h,影响纳滤膜产水通量的主要因素是苦咸水中的部分离子结垢;(4)纳滤膜对苦咸水中的Ca2+的去除率为90%,Mg2+的去除率为78%,Cl-的去除率为44%,可见纳滤膜对不同价态离子的去除效果不同,对二价和高价离子的去除率明显高于一价离子;(5)纳滤膜的酸洗效果远好于碱洗,同时酸洗可去除膜表面的无机盐离子且不会破坏纳滤膜的产水性能。     

双分离层复合纳滤膜的制备及其性能

以改性后的聚丙烯腈(PAN)超滤膜为基膜,依次采用层层自组装(LBL)和界面聚合的方法制备了具有双层分离层的复合纳滤膜。以间苯二胺(MPD)为水相单体,均苯三甲酰氯(TMC)为有机相单体,聚乙烯亚胺(PEI)为阳离子聚电解质,聚(4-苯乙烯磺酸钠)(PSS)为阴离子聚电解质,探索了LBL条件对双分离层复合纳滤膜性能的影响,考察了通过不同制备方法获得的纳滤膜对硫酸镁(MgSO_4)的分离性能,得到了最佳的LBL制备条件:PEI溶液的浓度为1.00 g·L~(-1),pH为7;PSS溶液的浓度为1.00 g·L~(-1),p H为10,支撑电解质氯化钠(NaCl)浓度为1.00 mol·L~(-1),单一聚电解质(PEI或PSS)的沉积时间为20 min。与仅通过界面聚合法制得的聚酰胺纳滤膜相比,在界面聚合反应之前,先通过LBL沉积1.5层的聚电解质层时得到的复合纳滤膜分离性能优异稳定,在0.80 MPa的压力下,过滤2.00 g·L~(-1)MgSO_4溶液时的通量为18.6 L·(m~2·h)~(-1),截留率达到99.07%。     

电镀废水膜分离法问世

电镀废水回用技术的开发成果，首次将纳滤及反渗透技术集成用来处理电镀废水，这一成果已经申请“电镀废水处理零排放的膜分离方法”发明专利。该成果开发创新了新型膜组件等硬件技术和膜工艺设计、优化、管理运行等方面的软件，采用纳滤膜除去废水中的一价盐，并对镍离子预浓缩，再通过二级反渗透进一步浓缩镍，使其浓缩100倍，     

RES/PIP混合聚酰胺纳滤膜的制备

以聚砜超滤膜为基膜,间苯二酚(RES)与哌嗪(PIP)混合作为水相溶液,均苯三甲酰氯(TMC)为有机相溶液,采用界面聚合法制备复合纳滤膜。探索了混合水相质量比RES/PIP、TMC浓度、界面聚合时间、热处理温度及热处理时间等界面聚合条件对复合膜分离性能的影响,考察了最佳条件所得复合膜对不同种类无机盐的分离性能,并使用原子力显微镜(AFM)对基膜及所得复合膜表面形貌进行了表征。结果表明最佳聚合条件为:RES质量分数0.5%,PIP质量分数1.5%,TMC质量分数0.15%,水相浸渍时间3 min,界面聚合反应时间60 s,热处理温度80℃,热处理时间3 min;在0.6 MPa下,所得复合膜对4种无机盐的截留顺序依次为Na_2SO_4MgSO_4≥MgCl_2NaCl,这表明静电排斥作用在纳滤膜分离过程中占主导地位;此外,由基膜和所得复合膜的表面形貌对比结果可得,通过界面聚合反应会在基膜表面形成一层粗糙度较大的聚酰胺功能层。     

酒石酸钾钠（PST）对纳滤处理重金属废水的强化效果

以酒石酸钾钠（PsT）为络合剂，分别选取cd、zn、As和Ph4种金属废水，探索络合纳滤工艺对金属离子去除率和膜通量的强化效果，测定纳滤膜表面接触角以表征膜通量变化规律，并研究了压力、金属浓度和溶液pH参数对络合纳滤过程的影响。结果表明，PsT对4种金属去除的强化效果存在相似规律，分别有一个最佳PsT添加浓度。随PsT浓度的增加，金属离子去除率先增大后减小，而膜通量一直增大。研究发现，纳滤膜表面接触角与膜通量呈稳定的反比例关系，与金属离子种类和PsT添加量无关。随着操作压力的增大，膜通量线性增加，去除率基本不变；金属离子浓度的增加对膜通量影响不大，金属去除率略有上升；pH在4～5之间变化时，As去除中膜通量和去除率均有所升高，而cd、zn和Ph3种溶液处理效果基本不受pH影响。     

混凝-纳滤集成工艺深度处理脱墨废水简

采用混凝-纳滤工艺对脱墨废水生化出水进行深度处理。实验结果表明，当聚合氯化铝的投加量为100 mg/L时，废水中污染物的综合去除性能最佳，其中浊度去除率达91%，色度去除率达74%。采用4种相同材质、不同切割分子量的纳滤膜进一步深度处理后，出水达到《再生水质标准（SL368-2006）》中锅炉用水控制指标的要求。     

混凝-纳滤集成工艺深度处理脱墨废水

采用混凝-纳滤工艺对脱墨废水生化出水进行深度处理。实验结果表明，当聚合氯化铝的投加量为100mg／L时，废水中污染物的综合去除性能最佳，其中浊度去除率达91％，色度去除率达74％。采用4种相同材质、不同切割分子量的纳滤膜进一步深度处理后，出水达到《再生水质标准（SL368—2006）》中锅炉用水控制指标的要求。     

啤酒酵母菌对溶液中锶离子的吸附行为

利用废弃啤酒酵母菌为生物吸附剂,考察了pH、啤酒酵母菌加入量、锶离子初始浓度、吸附时间等对锶离子吸附行为的影响,并通过红外光谱分析探讨了吸附机制.结果表明:(1)在吸附温度为25℃、pH为4.5、啤酒酵母菌加入量为2.0 g/L、锶离子初始质量浓度为10.0 mg/L、吸附60 min的条件下,啤酒酵母菌对锶离子的吸附基本达到平衡.(2)啤酒酵母菌对锶离子的吸附较好地符合Langmuir和Freundlich吸附等温式,且以Langmuir吸附等温式拟合效果更优.在吸附温度为25℃、pH为4.5、啤酒酵母菌加入量为2.0 g/L、吸附时间为180 min、锶离子初始质量浓度为5.0～250.0 mg/L的条件下,啤酒酵母菌对锶离子的理论饱和吸附量为29.67 mg/g.(3)啤酒酵母菌吸附锶离子前后的红外图谱显示.部分吸收峰发生了位移并且透过率改变.推断在啤酒酵母菌吸附锶离子的过程中,锶离子先与NH2和酰胺基团中的N原子进行配位络合,随后被络合了的锶作为成核位点再吸附更多的锶离子在表面.此外,蛋白质特征谱带--酰胺Ⅰ带和酰胺Ⅱ带吸收峰的透过率也发生变化,可能是啤酒酵母菌蛋白质上的官能团也结合了锶离子.     

制革废水中丙烯酸类鞣剂的膜分离特征

针对3种丙烯酸类鞣剂超滤(UF)、反渗透(RO)分离参数进行了实验研究,探索其在废水深度处理中膜去除的可行性,研究结果表明,3种鞣剂在分离参数:浓度为200 mg/L,超滤的操作压力(P UF)为0.11 MPa,反渗透的操作压力(P RO)为0.4 MPa的条件下UF-RO分离,效果最好。其次,丙烯酸类鞣剂对膜通量影响较大,导致产生的清液较少,所以用UF、RO处理含有这类物质的制革废水时,应尽可能对废水进行预处理。最后,丙烯酸类鞣剂分子中含有极性较强的基团时,粒径分离效果不同。     

Integrated nanofiltration and upflow anaerobic sludge blanket treatment of textile wastewater for in-plant reuse.

The filtration characteristics of simulated dyeing effluents containing Acid Orange 7, sodium sulfate, and a pH buffer made of acetic acid and sodium acetate is described using a commercially available nanofiltration membrane. The original membrane filtration properties were characterized with deionized water to provide a baseline of membrane performance. At high volumetric concentration of the test solutions, greater than 98% rejection of dye and sodium sulfate were obtained. Rejection of buffering chemicals was approximately 50% in all experiments, giving a permeate water not suitable for reuse in most dyeing operations. The final composite concentrate had a chemical oxygen demand (COD) value > 2000 mg/L. No problems were encountered with anaerobic treatment of the concentrate obtained from the dyeing wastewater. Adjusting the sulfate concentration to give COD-to-sulfate ratios to 2.9, 5.4, and 18.2 in the reactor feed had no significant alterations in the performance of the upflow anaerobic sludge blanket reactor.     

Reactive transport of 85Sr in a chernobyl sand column: static and dynamic experiments and modeling

The effects of nonlinear sorption and competition with major cations present in the soil solution on radioactive strontium transport in an eolian sand were examined. Three laboratory techniques were used to identify and quantify the chemical and hydrodynamic processes involved in strontium transport: batch experiments, stirred flow-through reactor experiments and saturated laboratory columns. The major goal was to compare the results obtained under static and dynamic conditions and to describe in a deterministic manner the predominant processes involved in radioactive strontium transport in such systems. Experiments under dynamic conditions, namely flow-through reactor and column experiments, were in very good agreement even though the solid/liquid ratio was very different. The experimental data obtained from the flow-through reactor study pointed to a nonlinear, instantaneous and reversible sorption process. Miscible displacement experiments were conducted to demonstrate the competition between stable and radioactive strontium and to quantify its effect on the 85Sr retardation factor. The results were modeled using the PHREEQC computer code. A suitable cation-exchange model was used to describe the solute/soil reaction. The model successfully described the results of the entire set of miscible displacement experiments using the same set of parameter values for the reaction calculations. The column study revealed that the stable Sr aqueous concentration was the most sensitive variable of the model, and that the initial state of the sand/solution system had also to be controlled to explain and describe the measured retardation factor of radioactive strontium. From these observations, propositions can be made to explain the discrepancies observed between some data obtained from static (batches) and dynamic (reactor and column) experiments. Desorbed antecedent species (stable Sr) are removed from the column or reactor in the flow system but continue to compete for sorption sites in the batch system. Batch experiments are simple and fast, and provide a very useful means of multiplying data. However, interpretation becomes difficult when different species compete for sorption sites in the soil/solution system. A combination of batches, flow-through reactor and column experiments, coupled with hydrogeochemical modeling, would seem to offer a very powerful tool for identifying and quantifying the predominant processes on a cubic decimeter scale (dm3) and for providing a range of radioactive strontium retardation factor as a function of the geochemistry of the soil/solution system.     

膨润土接枝丙烯酸高吸水性树脂的抑尘性能研究

在微波辐射下制备了膨润土接枝丙烯酸高吸水性树脂(SAP)(一种加入聚乙烯醇(PVA),另一种不加入PVA)。结果表明:(1)红外光谱图表明,PVA与聚合网络形成了半互穿网络结构;X射线衍射图表明,膨润土与PVA、丙烯酸形成了具有无定形结构的复合产物。(2)不论是沙土堆还是尘土堆,喷洒膨润土接枝丙烯酸SAP溶液的抑尘效果明显比喷洒自来水好;喷洒膨润土接枝丙烯酸SAP溶液的尘土堆的抑尘效果好于沙土堆。(3)在温度为15℃时,考虑到节约成本的问题,首选不加入PVA的膨润土接枝丙烯酸SAP做抑尘剂;在温度为45℃时,加入PVA的膨润土接枝丙烯酸SAP适合做抑尘剂。(4)膨润土接枝丙烯酸SAP浓度越高,其耐蒸发性越高。     

提高生物法分离制革污泥中铬分离效率的研究

在已确定污泥驯化最佳条件的基础上，通过改变滤材、液固分离条件，添加营养物质继续降低pH等方法，进行提高生物沥滤法分离制革污泥中铬的分离效率的研究。同时考察化学沥滤法（1∶1硫酸）在相同条件下的分离效率。试验结果表明：用相应pH值酸液（1∶1硫酸配制）淋洗，淋洗+闷洗和抽真空＋酸液淋洗等过滤方式可提高铬的分离效率。生物沥滤中当pH值下降至1.8时，分离效率即可达到94.65%，与直接用蒸馏水淋洗相比要高得多。化学沥滤中当pH值下降到1时，分离效果可达96.7%，沥滤污泥中剩余铬含量可达到制革污泥农用标准。     

MBR-NF截留液中腐植酸的纳滤分离浓缩特性

MBR-NF截留液是一类难处理的高浓度有机废水,其所含有机物几乎都是腐植酸,可考虑资源利用。实验室内采用纳滤对其所含腐植酸进行分离浓缩。引入分离因子来表征纳滤的分离效果。实验结果表明,分离因子(SF)与体积浓缩倍数(CF)有很好的线性关系,浓缩倍数为5时,截留液中有机碳浓度为9 413 mg/L,重金属浓度处于mg/L水平,分离因子达到2.76,表明纳滤可有效地将MBR-NF截留液中的腐植酸与无机盐分离,并进行浓缩。     

Water reclamation during drinking water treatments using polyamide nanofiltration membranes on a pilot scale

The aim of this study was to investigate the performances of polyamide nanofiltration membranes during water reclamation. The study was conducted using nanofiltration concentrates obtained from two different nanofiltration drinking water treatment plants placed in the northern part of Serbia (Kikinda and Zrenjanin). Used nanofiltration concentrates contained high concentrations of arsenic (45 and 451 μg/L) and natural organic matter (43.1 and 224.40 mgKMnO₄/L). Performances of polyamide nanofiltration membranes during water reclamation were investigated under various fluxes and transmembrane pressures in order to obtain drinking water from nanofiltration concentrates and, therefore, reduce the amount of produced concentrates and minimize the waste that has to be discharged in the environment. Applied polyamide nanofiltration membranes showed better removal efficiency during water reclamation when the concentrate with higher content of arsenic and natural organic matter was used while the obtained permeates were in accordance with European regulations. This study showed that total concentrate yield can be reduced to ~5 % of the optimum flux value, in both experiments. The obtained result for concentrate yield under the optimum flux presents considerable amount of reclaimed drinking water and valuable reduced quantity of produced wastewater.     

Denitrification using PBS as carbon source and biofilm support in a packed-bed bioreactor

Biodegradable polymer was used as carbon source and biofilm support for nitrate removal from aqueous solution as an attractive alternative for biological denitrification. The objective of this paper was to investigate the denitrification performance and microbial community of a packed-bed bioreactor using poly (butanediol succinate) (PBS), a biodegradable polymer, as carbon source and biofilm support. NO₃–N concentration was determined by UV spectrophotometer. NO₂–N concentration was assayed by hydrochloric acid naphthyl ethylenediamine spectrophotometry method. Total organic carbon (TOC) was measured using a TOC analyzer. The morphology of the samples was observed using an environmental scanning electron microscope (ESEM). The microbial community was analyzed by pyrosequencing method. The experimental results showed that an average removal efficiency of nitrate was 95 %. ESEM observation and FTIR analysis indicated the changes of PBS granules before and after microbial utilization. Pyrosequencing results showed that Betaproteobacteria predominated, and most of PBS-degrading denitrifying bacteria were assigned to the family Comamonadaceae. Denitrifying bacteria accounted for 13.02 % in total population. The PBS granules were suitable support and carbon source for denitrifying bacteria.     

Enhanced adsorption of hexavalent chromium by a biochar derived from ramie biomass (<Emphasis Type="Italic">Boehmeria nivea</Emphasis> (L.) Gaud.) modified with β-cyclodextrin/poly(L-glutamic acid)

This paper explored biochar modification to enhance biochar’s ability to adsorb hexavalent chromium from aqueous solution. The ramie stem biomass was pyrolyzed and then treated by β-cyclodextrin/poly(L-glutamic acid) which contained plentiful functional groups. The pristine and modified biochar were characterized by FTIR, X-ray photoelectron spectroscopy, specific surface area, and zeta potential measurement. Results indicated that the β-cyclodextrin/poly(L-glutamic acid) was successfully bound to the biochar surface. Batch experiments were conducted to investigate the kinetics, isotherm, thermodynamics, and adsorption/desorption of Cr(VI). Adsorption capacities of CGA-biochar were significantly higher than that of the untreated biochar, and its maximum adsorption capacity could reach up to 197.21 mg/g at pH 2.0. Results also illustrated that sorption performance depended on initial solution pH; in addition, acidic condition was beneficial to the Cr(VI) uptake. Furthermore, the Cr(VI) uptake was significantly affected by the ion strength and cation species. This study demonstrated that CGA-biochar could be a potential adsorbent for Cr(VI) pollution control.     

连续式离子分离系统(ISEP)在水杨酸生产废水处理中的应用

采用连续式离子分离系统 (ISEP)处理水杨酸生产废水 ,结果表明 ,该系统对水杨酸生产废水有良好的处理效果。当进水CODCr为 180 0 0— 2 0 0 0 0mg/L时 ,经一步吸附处理 ,出水CODCr可实现达标排放 ,苯酚、水杨酸去除率接近10 0 % ,脱附液中高浓度苯酚、水杨酸等资源可有效回收利用