磁性吸附材料CuFe2O4吸附砷的性能

根据Cu(Ⅱ)和Fe(Ⅲ)都对砷有较强的亲和性,制备了同时含有Cu(Ⅱ)和Fe(Ⅲ)的、可用磁分离方法进行分离回收的磁性吸附材料CuFe₂O₄,并对其进行了表征及吸附砷的性能研究.结果表明,该吸附剂对砷的吸附能力与溶液pH有关,在弱酸性及中性条件下,吸附砷的能力最强,而对As(V)的吸附能力比对As(Ⅲ)更强些,在平衡浓度为10μg/L时,其吸附容量可达10mg/g左右,可以很容易地将水中浓度为1～20mg/L的As(V)降到10μg/L以下.实验考察了几种无机阴离子对吸附砷的影响,表明较高浓度(砷浓度的20倍)的硫酸盐对As(Ⅲ)和As(V)的吸附均有一定影响,盐酸盐及磷酸盐则影响不明显;负载的As(V)可较容易地用0.1mol/L NaOH洗脱下来,使吸附剂再生,而As(Ⅲ)则难以洗脱,这与2种价态砷的吸附机理不同有关.     

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.     

Novel Fe/glass composite adsorbent for As(V) removal

An effective adsorbent for arsenic removal was synthesized by hydrothermal treatment of waste glass powder (GP), followed by loading Fe(Ⅲ) oxyhydroxide onto the surface of waste glass powder. The ≡Si-O-H group was formed on the surface of GP and the specific surface area of GP powder was slightly increased after hydrothermal treatment. FeOOH was loaded onto the surface of hydrothermally treated waste glass powder (HGP) by the hydrolysis of FeCl3. The formation conditions of FeOOH were also investigated. The...     

三种氧化铁吸附水环境中砷的试验研究

采用两种人工合成的氧化铁(针铁矿、水铁矿)和赤铁矿作为吸附剂,对含砷(三价砷及三价五价砷混合液)水进行了吸附试验。结果表明,在初始浓度为1200μg/L的As(Ⅲ)溶液中,水铁矿的吸附效果最好,针铁矿和赤铁矿吸附效果较差;在初始pH为7,As(Ⅲ)和As(Ⅴ)摩尔比为1:1的混合液中时,三种铁矿对总砷的吸附效果均随着As/Fe摩尔比的增大而减小;在A(sⅢ)和As(Ⅴ)摩尔比为1:1的混合液中,吸附总砷效果最好的是针铁矿,水铁矿次之,赤铁矿的吸附效果最差;A(sⅤ)的存在对除砷效果有一定的影响,三价砷和五价砷共存时,三种铁矿对其吸附具有一定的选择性。     

Effects of solution chemistry on arsenic(Ⅴ) removal by low-cost adsorbents

Natural and anthropogenic arsenic （As） contamination of water sources pose serious health concerns, especially for small communities in rural areas. This study assessed the applicability of three industrial byproducts （coal fly ash, lignite, and green waste compost） as the low-cost adsorbents for As（V） removal under various field-relevant conditions （dissolved oxygen, As（V）/Fe ratio, solution pH, and presence of competing species）. The physico-chemical properties of the adsorbents were characterized by XRD, XRF, FT-IR, and NMR analysis. Batch experiments demonstrated that coal fly ash could provide effective As（V） removal （82.1%-95%） because it contained high content of amorphous iron/aluminium hydroxides for As（V） adsorption and dissolvable calcium minerals for calcium arsenate precipitation. However, the addition of lignite and green waste compost was found unfavourable since they hindered the As（V） removal by 10%-42% possibly due to dissolution of organic matter and ternary arsenate-iron-organic matter complexes. On the other hand, higher concentrations of dissolved iron （comparing As（V）/Fe ratios of 1：1 and 1：10） and dissolved oxygen （comparing 0.2 and 6 mg/L） only marginally enhanced the As（V） removal at pH 6 and 8. Thus, addition of dissolved iron, water aeration, or pH adjustment became unnecessary because coal fly ash was able to provide effective As（V） removal under the natural range of geochemical conditions. Moreover, the presence of low levels of background competing （0.8 or 8 mg/L of humic acid, phosphate, and silicate） imposed little influence on As（V） removal, possibly because the high adsorption capacity of coal fly ash was far from exhaustion. These results suggested that coal fly ash was a potentially promising adsorbent that warranted further investigation.     

Novel Fe/glass composite adsorbent and its property for arsenic(V) removal

An effective adsorbent for arsenic removal was synthesized by hydrothermal treatment of waste glass powder (HGP), followed by loading iron(III) oxyhydorxide on the surface of waste glass powder (GP). The ?Si-O-H group was formed on the surface of GP and the specific surface area of GP powder was slightly increased after hydrothermal treatment. FeOOH was loaded on the surface of HGP by the hydrolysis of FeCl3. The formation conditions of FeOOH were also investigated. The ability of this new adsorbent for arsenic removal was tested. The results indicate that the highest arsenic removal efficiency is about 97% for 1 mg/L As(V) solution at pH 6 and keeping time 2h.     

Arsenic removal from groundwater by acclimated sludge under autohydrogenotrophic conditions

Arsenic in the environment is attracting increasing attention due to its chronic health effects. Although arsenite(As(III)) is generally more mobile and more toxic than arsenate(As(V)), reducing As(V) to As(III) may still be a means for decontamination, because As(III) can be removed from solution by precipitation with sulfide or by adsorption or complexation with other metal sulfides. The performance of As(V) bio-reduction under autohydrogenotrophic conditions was investigated with batch experiments. The results showed that As(V) reduction was a biochemical process while both acclimated sludge and hydrogen were essential. Most of the reduced arsenic remained in a soluble form, although 20% was removed with no addition of sulfate, while 82% was removed when sulfate was reduced to sulfide. The results demonstrated that the reduced arsenic was re-sequestered in the precipitates, probably as arsenic sulfides. Kinetic analysis showed that pseudo first-order kinetics described the bio-reduction process better than pseudo second-order. In particular, the influences of pH and temperature on As(V) reduction by acclimated sludge under autohydrogenotrophic conditions and total soluble As removal were examined. The reduction process was highly sensitive to both pH and temperature, with the optimum ranges of pH 6.5–7.0 and 30–40°C respectively. Furthermore, Arrhenius modeling results for the temperature effect indicated that the As(V) reduction trend was systematic. Total soluble As removal was consistent with the trend of As(V) reduction.     

Migration of manganese and iron during the adsorption-regeneration cycles for arsenic removal

Fe-Mn binary oxide incorporated into porous diatomite (FMBO-diatomite) was prepared in situ and regenerated in a fixed-bed column for arsenite [As(III)] and arsenate [As(V)] removal. Four consecutive adsorption cycles were operated under the following conditions: Initial arsenic concentration of 0.1 mg·L⁻¹, empty bed contact time of 5 min, and pH 7.0. About 3000, 3300, 3800, and 4500 bed volumes of eligible effluent (arsenic concentration ⩽ 0.01 mg·L⁻¹) were obtained in four As (III) adsorption cycles; while about 2000, 2300, 2500, and 3100 bed volumes of eligible effluent were obtained in four As(V) adsorption cycles. The dissection results of FMBO-diatomite fixed-bed exhibited that small amounts of manganese and iron were transferred from the top of the fixed-bed to the bottom of the fixed-bed during As(III) removal process. Compared to the extremely low concentration of iron (<0.01 mg·L⁻¹), the fluctuation concentration of Mn²⁺ in effluent of the As(III) removal column was in a range of 0.01–0.08 mg·L⁻¹. The release of manganese suggested that manganese oxides played an important role in As(III) oxidation. Determined with the US EPA toxicity characteristic leaching procedure (TCLP), the leaching risk of As(III) on exhausted FMBO-diatomite was lower than that of As(V).     

草酸盐介导下含As(V)黄钾铁矾的相转化过程与As(V)的再分配行为

黄钾铁矾能够通过吸附和共沉淀作用固定酸性矿山废水（AMD）中的重（类）金属（如砷）,降低其迁移性和生物可利用性.草酸盐广泛存在于天然水环境中,其具有的羧酸官能团能改变铁矿物的稳定性,进而影响吸持的重（类）金属的再分配行为.利用水热法合成含As（V）黄钾铁矾,探究其在不同草酸盐浓度与pH条件下的溶解、重结晶和共沉淀As（V）的行为.研究结果表明,草酸盐与含As（V）黄钾铁矾表面Fe（III）活性位点配位形成的可溶性强络合物是促进矿物溶解的第一步和关键;在pH 2.5时,含As（V）黄钾铁矾的溶解速率随草酸盐浓度增加而增加,伴随大量As（V）释放到溶液,反应过程中只有少量As（V）重新吸附到固相上,这是由于草酸盐与As（V）竞争矿物表面的同一活性位点;在pH 6.5条件下,草酸盐促进含As（V）黄钾铁矾的重结晶,经X射线衍射分析表明针铁矿和纤铁矿为主要产物,能有效地吸附释放的As（V）.研究结果有助于揭示在AMD环境下黄钾铁矾沉积物与含羧酸官能团有机酸共存时对As（V）的释放和固定机理,对AMD环境中As（V）污染控制有重要意义.     

Ligand effects on arsenite removal by zero-valent iron/O2: Dissolution, corrosion, oxidation and coprecipitation

Ligands may increase the yields of reactive oxygen species (ROS) in zero-valent iron (ZVI)/O₂ systems. To clarify the relationship between the properties of ligands and their effects on the oxidative removal of contaminants, five common ligands (formate, acetate, oxalate, ethylenediaminetetraacetic acid (EDTA), and phosphate) as well as acetylacetone (AA) were investigated with arsenite (As(III)) as the target contaminant at three initial pH values (3.0, 5.0, and 7.0). The addition of these ligands to the ZVI/O₂ system resulted in quite different effects on As(III) removal. EDTA enhanced the oxidation of As(III) to arsenate (As(V)) but inhibited the removal of As(V). Oxalate was the only ligand in this work that accelerated both the removal of As(III) and As(V). By analyzing the ligand effects from the four aspects: dissolution of surface iron (hydr)oxides, corrosion of ZVI, reaction with ROS, and interference with precipitation, the following properties of ligands were believed to be important: ability to provide dissociable protons, complexation ability with iron, and reactivity with ROS. The complexation ability is a double-edged sword. It could enhance the generation of ROS by reducing the reduction potential of the Fe(III)/Fe(II) redox couple, but also could inhibit the removal of arsenic by coprecipitation. The elucidated relationship between the key property parameters of ligands and their effects on the ZVI/O₂ system is helpful for the rational design of effective ZVI/ligand/O₂ systems.     

Bacterial reduction and release of adsorbed arsenate on Fe(Ⅲ)-, Al- and coprecipitated Fe(Ⅲ)/Al-hydroxides

Mobilization of arsenic under anaerobic conditions is of great concern in arsenic contaminated soils and sediments. Bacterial reduction of As(V) and Fe(Ⅲ) influences the cycling and partitioning of arsenic between solid and aqueous phase. We investigated the impact of bacterially mediated reductions of Fe(Ⅲ)/Al hydroxides-bound arsenic(V) and iron(Ⅲ) oxides on arsenic release. Our results suggested that As(V) reduction occurred prior to Fe(Ⅲ) reduction, and Fe(Ⅲ) reduction did not enhance the release of arsenic. Instead, Fe(Ⅲ) hydroxides retained their dissolved concentrations during the experimental process, even though the new iron mineral-magnetite formed. In contrast, the release of reduced As(Ⅲ) was promoted greatly when aluminum hydroxides was incorporated. Thus, the substitution of aluminum hydroxides may be responsible for the release of arsenic in the contaminated soils and sediments, since aluminum substitution of Fe(Ⅲ) hydroxides universally occurs under natural conditions.     

河口沉积物对砷的吸附性能及影响因素

对比分析了砷在辽东湾营口河口外侧近海域沉积物和河口内侧河流段沉积物上的含量和吸附行为,并探讨了主要影响因素.结果表明,海域沉积物和河流段沉积物中As含量分别为7.5和4.0 mg/kg,相对于As的效应临界浓度TEL值7.2 mg/kg,海域沉积物中有一定的As污染.河口外侧近海域沉积物由于铁锰铝等金属和有机质含量较高...     

纳米零价铁颗粒去除As(III)和As(V)的动力学过程及性能研究

本研究系统分析了不同初始砷浓度和不同nZVI投加量等条件下,nZVI去除As（III）和As（V）的动力学过程和除砷性能.结果表明,nZVI可快速有效地去除As（III）和As（V）,除砷过程均符合准二级动力学模型,且As（III）的去除速率明显快于As（V）.在砷浓度为5 mg·L^-1时,As（III）去除速率常数达最大值0.30 g·mg^-1·min^-1,为As（V）去除速率（0.034 g·mg^-1·min^-1）的8.8倍.Weber-Morris粒子内扩散模型拟合结果表明,nZVI除砷速率是由外扩散和颗粒内扩散共同控制的.分析反应平衡时砷浓度测定结果,发现不同砷浓度条件下nZVI对As（III）的去除量为As（V）的1.5~2.6倍,nZVI对砷的去除量随初始砷浓度增加而降低,随nZVI投加量增加而增加.砷浓度为50.0 mg·L^-1时,As（III）和As（V）去除量达到最高,分别为152.14 mg·g^-1和62.02 mg·g^-1,均高于传统（羟基）氧化铁对As（III）和As（V）的去除量.因此,nZVI可高效去除水中As（III）和As（V）,且用于修复以As（III）污染为主的地下水更具有优势.     

A laboratory scale study on arsenic（Ⅴ） removal from aqueous medium using calcined bauxite ore

The present work deals with the As（Ⅴ） removal from an aqueous medium by calcined refractory grade bauxite （CRB） as a function of solution pH, time, As（Ⅴ） concentration and temperature. The residual As（Ⅴ） was lowered from 2 mg/L to below 0.01 mg/L in the optimum pH range 4.0-7.0 using a 5 g/L CRB within 3 h contact time. The adsorption data fits well with Langmuir isotherm and yielded Langmuir monolayer capacity of 1.78 mg As（Ⅴ）/g of CRB at pH 7.0. Presence of anions such as silicate and phosphate decreased As（Ⅴ） adsorption efficiency. An increase temperature resulted a decrease in the amount of As（Ⅴ） adsorbed by 6%. The continuous fixed bed column study showed that at the adsorbent bed depth of 30 cm and residence time of 168 min, the CRB was capable of treating 340 bed volumes of As（V） spiked water （C0 = 2 mg/L） before breakthrough （Ce = 0.01 mg/L）. This solid adsorbent, although not reusable, can be considered for design of adsorption columns as an efficiency arsenic adsorption media.     

壳聚糖海藻酸钠铁锰泥吸附剂制备与除As(V)研究

将生物除铁除锰水厂反冲洗铁锰泥包埋在壳聚糖海藻酸钠水凝胶中,成功制备了一种具有高机械强度和稳定性的复合除砷吸附剂（CAFB）.表征结果显示,其表面粗糙,铁锰元素含量为69.31%,比表面积达117.20m²/g,且具有介孔结构.吸附动力学数据更符合准二级动力学模型（R²=0.963）.Langmuir等温吸附模型能更好地描述As （V）吸附过程（R²=0.969）,25℃时最大吸附容量为15.80mg/g.酸性条件有利于As （V）的吸附,在pH=3~7范围内As （V）去除率能达到80%以上.H²PO₄^-,SiO₃^2-离子对吸附过程抑制作用明显.用0.1mol/L的NaOH溶液再生4次后吸附量能达到初始值的70.68%,具有在工程上运用的前景.     

CTAC改性活性炭去除水中砷(V)的柱实验吸附和再生研究

为了开发一种能有效去除水中砷的吸附材料, 研究了十六烷基三甲基氯化铵(CTAC)改性活性炭后, 活性炭对水中五价砷As(V)的去除效果.研究中利用动态小柱实验(Rapid small-scale column test, RSSCT)探讨了CTAC改性后活性炭对砷的吸附能力、影响吸附能力的因素和活性炭再生方法.结果表明, CTAC改性能有效提高活性炭对As(V)的吸附.活性炭对As(V)的吸附受溶液pH、空床接触时间、进水中砷浓度及水中其他离子存在的影响.另外, 1 mol·L^-1的盐酸能有效对吸附穿透后的活性炭进行再生,再生后的活性炭可以重复使用.同时,柱实验中对出水CTAC的检测结果表明, CTAC和活性炭的结合非常稳定.     

铁屑内电解法处理EDTA溶液中络合铜离子

采用批式试验和现代仪器分析研究了铁屑内电解法处理EDTA溶液中络合铜离子,考察了溶液浓度、溶液pH、温度和铁屑粒径等因素对铜离子去除过程的影响.结果表明,铜离子去除过程符合表观一级动力学方程.在pH 2.0～11.0范围内,pH值越低越利于铜离子去除;在酸性条件下溶液pH随内电解进行升高,在碱性条件下溶液pH随内电解进...     

铁改性赤泥吸附剂的制备及其除砷性能研究

以氧化铝生产废渣--赤泥为原料,采用铁盐改性处理制备了新型羟基铁包覆型赤泥除砷吸附剂.研究考察了吸附剂吸附砷效能、投加量、吸附时间和pH值对吸附除砷效果的影响;采用扫描电镜(SEM)、红外光谱(IR)、比表面积(BET)等仪器对吸附剂进行了表征,并探讨了吸附机制.结果表明,铁盐改性赤泥吸附剂对As(V)具有显著吸附效能,在pH为7,初始砷浓度为1 mg·L-1,铁盐改性赤泥吸附剂饱和吸附容量为50.6mg·g-1时,除砷率高达99.9%,吸附后出水砷含量可达到0.01 mg·L-1以下,吸附规律符合Langmuir等温方程式;溶液pH值显著影响砷去除效果,吸附机制主要为羟基铁的表面吸附机制;吸附后的吸附剂可通过NaOH溶液再生,脱附率达到92.1%.     

载铁(β-FeOOH)球形棉纤维素吸附剂去除地下水As(Ⅴ)的研究

制备了一种载铁(β- FeOOH)球形棉纤维素吸附剂,球珠孔隙度大,强度好,活性成分铁的载入量可高达360mg/mL ,(质量分数达50%) ,活性好.研究表明,当铁含量为220mg/mL时,该吸附剂对As(V)的最大吸附量为15.6mg/mL(33.2mg/g) ,Langmuir和Freundlich方程能很好地描述吸附等温线.吸附速度较快,10h可达到吸附平衡,吸附动力学符合Lagergren二级方程.SiO₃^2- ,SO₄^2-,Cl^-干扰离子均不影响砷的去除.柱吸附实验表明,空床停留时间为5.9min ,进水As(V)浓度为500μg/L时,As(V)的穿透体积为5000BV .吸附剂可以用1.5mol·L^-1 NaOH再生,洗脱和再生效率可达90%以上.活性成分β-FeOOH形态稳定,柱操作和再生时铁无溶出.吸附剂制备方法简单,新颖,对地下水和饮用水砷去除具有较好的应用前景.     

Preparation and evaluation of Zr-β-FeOOH for efficient arsenic removal

A Zr-β-FeOOH adsorbent for both As(V) and As(III) removal was prepared by a chemical co-precipitation method.Compared with β-FeOOH,the addition of Zr enhanced the adsorption capacities for As(V) and As(III),especially As(III).The maximum adsorption capacities for As(III) and As(V) were 120 and 60mg/g respectively at pH 7.0,much higher than for many reported adsorbents.The adsorption data accorded with Freundlich isotherms.At neutral pH,for As(V),adsorption equilibrium was approached after 3 hr,while for As(III),adsorption equilibrium was approached after 5 hr.Kinetic data fitted well to the pseudo second-order reaction model.As(V) elimination was favored at acidic pH,whereas the adsorption of As(III) by Zr-β-FeOOH was found to be effective over a wide pH range of 4-10.Competitive anions hindered the adsorption according to the sequence:phosphate > silicate > bicarbonate > sulfate > nitrate,while Ca2+ and Mg2+ increased the removal of As(III) and As(V) slightly.The high adsorption capability and good performance in other aspects make Zr-β-FeOOH a potentially attractive adsorbent for the removal of both As(III) and As(V) from water.