孔径分布和溶液浓度对碳气凝胶电极电吸附除盐性能的影响分析

在不同进水浓度下,采用两种比表面积相似但是孔径分布不同的碳气凝胶作为电极进行了一系列电吸附除盐平衡试验.结果表明,随着溶液浓度的变化,不同的孔径分布对碳气凝胶除盐效果影响不一样.其机理为双电层的存在,使得碳气凝胶空隙内的双电层扩散层相互叠加;同时,根据德拜定律,碳气凝胶空隙内的双电层扩散层在不同浓度溶液中厚度不同,从而使得双电层扩散层相互叠加的情况也随浓度变化而变化.这两种作用共同导致了实验结果.当溶液浓度为 0.01 mol·L-1时,选择主要孔径不小于20hm的碳气凝胶电极;当溶液浓度为 0.1 mol·L-1时,应选用主要孔径不小于 10nm 的材料;当溶液浓度为几 mol·L-1时.则分散层几乎消失,孔径大小对电吸附性能影响几乎不考虑.     

富集甲基汞的树脂膜筛选及条件优化

树脂膜作为DGT技术的核心部分,是影响 DGT测定的关键因素。为确保树脂吸附和洗脱实验的准确性,筛选出醋酸-盐酸混合溶液作为甲基汞溶液的保存试剂。以标液中甲基汞的吸附率为指标,比较了4种吸附树脂的基本特征及在室内标液浓度为1μg/L的条件下对甲基汞的吸附效果,筛选出吸附效果最佳的树脂TCH-95,并对TCH-95树脂胶的不同洗脱试剂进行了研究。结果表明：24h TCH-95对甲基汞的吸附率高达98.9%。且在洗脱实验中,对硫脲-盐酸混合溶液添加冰醋酸有助于提高树脂胶中甲基汞的洗脱率,其2%硫脲-0.2mol/L HCl-4%HAc混合溶液的甲基汞洗脱率为84.5%,是目前TCH-95树脂的最佳洗脱剂。     

离子交换树脂静态吸附二甲胺的研究

通过静态吸附实验,研究了二甲胺在ZGSPC106型细颗粒树脂上的吸附行为,从热力学和动力学角度对吸附过程进行了分析,并用红外光谱的方法探讨了树脂吸附二甲胺的机理.结果表明,Langmuir等温方程能够很好的拟合吸附平衡数据,热力学参数表明该吸附可自发进行,且为熵增加的吸热过程,293K温度下树脂的静态饱和吸附容量为138.89mg/g(干树脂);吸附动力学符合准二级动力学模型,颗粒扩散是树脂吸附二甲胺速率的主要控制步骤.     

Adsorption mechanism of phenolic compounds from aqueous solution on hypercrosslinked polymeric adsorbent

The adsorption of two phenols, namely, phenol and salicylic acid(SA) onto a water-compatible hypercrosslinked polymeric resin (NJ-8) were studied in terms of pseudo-second-order and first order mechanisms for chemical sorption as well as an intraparticle diffusion mechanism process. Kinetic analysis showed that the intraparticle diffusion process was the essential rate-controlling step. The activation energies of sorption have also been evaluated with the pseudo-second-order and intraparticle diffusion constants, respectively. Adsorption equilibrium data were well fitted by the Langmuir, Freundlich and Redlich-Peterson isotherms. Adsorption was exothermic and basically of a type of transition between physical and chemical character. The sorption capacity was higher for SA due to its more hydrophobic. Phenol has a higher adsorption enthalpy since it could form stronger hydrogen bonding on NJ-8.     

胞外聚合物结合磷效能的研究

以实验SBR反应器的活性污泥为研究对象,探讨了超声波-树脂法提取EPS的方法与程序;以5种不同来源的活性污泥为研究对象,考察了EPS结合磷的效能.结果表明,超声波-树脂法分离EPS和细菌细胞的较优程序为：采用21kHz、40W超声波作用60mL污泥2min（VSS约为8000mg·L-1）;然后,投加80g·g-1（以...     

固相萃取-电感耦合等离子体质谱测定自然水体痕量钍和铀

自然水体中Th和U的浓度极低,尤其Th的浓度单位仅为ng/L,定量测试非常困难。该研究建立了一种NOBIAS PA1螯合树脂萃取结合电感耦合等离子体质谱(ICP-MS)同时测定自然水体中痕量Th和U的分析方法。该方法首先使用UV/H₂O₂法消解水样30 min,去除水体中的有机物,然后在pH=3.00±0.05条件下,将水样以2 mL/min流速通过树脂对Th和U进行富集,使用NH₄AC-HAC溶液去除树脂上吸附的盐类,最后用1 mol/L超纯硝酸对样品进行洗脱,用ICP-MS测试。分析结果显示：Th和U的流程空白值分别为0.47、0.22 ng/L,检出限分别为2.9、2.3 ng/L,测定下限分别为11.46、9.11 ng/L。将该方法应用于不同有机物浓度的咸水和淡水中,结果显示：Th和U的回收率分别为97%～104%和98%～103%,相对标准偏差分别为3%～6%和1%～3%。说明该方法具有较高的回收率、精密度和准确度,适用于自然界各种不同水体中Th和U的定量分析。     

可用于去除高盐废水中有机污染物的混凝-Fenton氧化联合工艺

以某环氧树脂生产厂产生的高盐有机废水为对象,对比研究了Fenton、Fenton-混凝、混凝-Fenton等工艺去除废水中有机污染物的效能。考察了Fenton反应中Fe2+、H2O2投加比、初始pH、反应时间以及混凝反应中混凝剂种类、投加量等参数对处理效果的影响。结果表明：Fenton工艺的最佳条件为亚铁和过氧化氢投加比1：20,投加量分别为25 mmol·L-1和500 mmol·L-1,初始pH 3,反应时间120 min,TOC去除率为62.50%;混凝工艺选择FeSO4混凝剂,投加量为300 mg·L-1,TOC去除率为23.78%;废水经过Fenton-无混凝剂混凝、Fenton-混凝剂混凝、混凝-一级Fenton氧化和混凝-二级Fenton氧化工艺处理,TOC去除率分别为68.32%、71.51%、80.69%和89.27%。     

混凝-生物强化联合处理环氧树脂高盐废水

环氧树脂高盐废水是目前较难处理的工业废水之一.采用混凝联合生物强化工艺:通过混凝过程进行预处理后,投加嗜盐菌进行生物强化考察盐度变化对系统降解有机物的影响以及污泥性状的变化情况.结果表明,当废水中氯离子浓度达到驯化目标10 g/L时,系统对COD的去除率仍稳定在85%左右;以没有投加嗜盐菌的反应器为对照组,在进水COD平均浓度为550 mg/L左右,氯离子浓度由12 g/L增至21 g/L时,对照组COD平均去除率由82%降至60%以下,而投加了嗜盐菌的反应器(投加组)则仍保持在85%以上;此外,盐度的变化同时影响污泥的活性及其沉降性能,随着盐度增大,两组中的污泥活性均有所降低,但投加组的污泥活性相对较高,其污泥的沉降时间和污泥体积指数(sludge volume index, SVI)值也较低.采用本工艺处理环氧树脂高盐废水,使得生物处理过程能够长期稳定运行,且能够保持较高的耐盐度和COD去除率.     

A miniature stainless steel net dumbbell-shaped stir-bar for the extraction of phthalate esters in instant noodle and rice soup samples

Abstract

This work reports the development of a very-simple-to-construct stir-bar extraction device so called “a dumbbell-shaped stainless steel stir-bar.” The extraction device was assembled from a rolled up stainless steel net filled with an XAD-2 sorbent and a metal rod to allow the use of a magnetic stirrer during extraction. The dumbbell-shaped stainless steel stir-bar was used to extract diethyl phthalate (DEP), dibutyl phthalate (DBP), and di(2-ethylhexyl) phthalate (DEHP) before analysis by a gas chromatograph equipped with an electron capture detector (GD-ECD). Under the optimal conditions, the developed method provided a good linearity from 10.0 to 1,000.0?ng mL^?1 for all three compounds. Limits of detection and limits of quantification were 9.37?±?0.29?ng mL^?1 and 31.22?±?0.95?ng mL^?1 for DEP, 5.73?±?0.31?ng mL^?1 and 19.1?±?1.0?ng mL^?1 for DBP and 3.30?±?0.06?ng mL^?1 and 11.0?±?0.19?ng mL^?1 for DEHP, respectively. Good recoveries in the range of 81.89?±?0.17 to 109.5?±?2.0% were achieved when the method was used to extract phthalate esters in five instant noodle and two rice soup samples.     

Nitrogen removal efficiencies and microbial communities in full-scale IFAS and MBBR municipal wastewater treatment plants at high COD:N ratio

• Two IFAS and two MBBR full-scale systems (high COD:N ratio 8:1) were characterized. • High specific surface area carriers grew and retained slow-growing nitrifiers. • High TN removal is related to high SRT and low DO concentration in anoxic tanks. The relative locations of AOB, NOB, and DNB were examined for three different kinds of carriers in two types of hybrid biofilm process configurations: integrated fixed-film activated sludge (IFAS) and moving bed biofilm reactor (MBBR) processes. IFAS water resource recovery facilities (WRRFs) used Anodkalness^TM K1 carriers (KC) at Broomfield, Colorado, USA and polypropylene resin carriers (RC) at Fukuoka, Japan, while MBBR WRRFs used KC carriers at South Adams County, Colorado, USA and sponge carriers (SC) at Saga, Japan. Influent COD to N ratios ranged from 8:1 to 15:1. The COD and BOD removal efficiencies were high (96%–98%); NH₄⁺-N and TN removal efficiencies were more varied at 72%–98% and 64%–77%, respectively. The extent of TN removal was higher at high SRT, high COD:N ratio and low DO concentration in the anoxic tank. In IFAS, RC with high specific surface area (SSA) maintained higher AOB population than KC. Sponge carriers with high SSA maintained higher overall bacteria population than KC in MBBR systems. However, the DNB were not more abundant in high SSA carriers. The diversity of AOB, NOB, and DNB was fairly similar in different carriers. Nitrosomonas sp. dominated over Nitrosospira sp. while denitrifying bacteria included Rhodobacter sp., Sulfuritalea sp., Rubrivivax sp., Paracoccus sp., and Pseudomonas sp. The results from this work suggest that high SRT, high COD:N ratio, low DO concentration in anoxic tanks, and carriers with greater surface area may be recommended for high COD, BOD and TN removal in WRRFs with IFAS and MBBR systems.