Fe(Ⅲ)对Anammox污泥脱氮效能长短期影响

通过接种厌氧氨氧化(Anammox)污泥,研究了Fe(Ⅲ)对Anammox污泥脱氮效能长短期影响.结果表明,适量提升Fe(Ⅲ)浓度可以提升Anammox菌的活性.当进水Fe(Ⅲ)浓度达到0.09mol/L时,反应器氮去除速率最高为0.238kg/(L·d),较对照组提升了14.2%.继续提高进水Fe(Ⅲ)浓度,氮去除速率逐步下降,当Fe(Ⅲ)浓度升至0.18mol/L时,氮去除速率降至0.215kg/(L·d),与最高氮去除速率相比下降10.75%.采用Haldane抑制动力学模型拟合得到Fe(Ⅲ)对Anammox半速率常数(KFe)为0.012mol/L,半抑制常数(KI)为0.449mol/L.长期结果表明,在0.09mol/L Fe(Ⅲ)浓度下,Anammox氮去除速率增幅最快,并且随着Fe(Ⅲ)浓度增加而逐步降低.由于Fe(Ⅲ)代替了NO_(2)^(-)-N作为电子受体发生厌氧铁氨氧化反应,在含有Fe(Ⅲ)的反应器中NO_(2)^(-)-N与NH_(4)^(+)-N的转化比在1.108~1.227之间波动,明显低于理论值1.32,并随Fe(Ⅲ)浓度的提升而降低.扫描电镜结果表明,添加Fe(Ⅲ)可使Anammox菌细胞结构更加稳定.

Fe(Ⅲ)-XG配合物选择性絮凝微细粒赤铁矿与石英及其机理研究

基于金属离子配位理论,将FeCl_(3)·6H_(2)O与黄原胶(XG)按一定比例混合制备Fe(Ⅲ)-XG配合物,用于改善微细粒赤铁矿难沉降、回收效果差的问题。采用沉降实验研究了不同条件下Fe(Ⅲ)-XG对微细粒赤铁矿和石英的选择性絮凝行为,结合动电位、红外光谱和显微镜分析,揭示Fe(Ⅲ)-XG对赤铁矿的絮凝作用机理。矿物絮凝沉降试验结果表明:以黄原胶和Fe(Ⅲ)为絮凝剂,无法实现赤铁矿与石英的选择性絮凝,而黄原胶与FeCl_(3)·6H_(2)O质量比为1︰9时生成的Fe(Ⅲ)-XG配位絮凝剂,对赤铁矿和石英表现出较强的选择性絮凝作用,pH值为6时两者沉降率差异最大,分别为91.50%和39.96%。显微镜观察结果证实,Fe(Ⅲ)-XG作用下,赤铁矿颗粒形成块状絮体,且絮体密实程度更大,而石英颗粒间未发生团聚作用,处于相对分散的状态。Zeta电位、溶液化学计算、吸附量实验与红外光谱分析结果表明:黄原胶主要通过羧酸基团的羰基C=O与Fe^(3+)发生配位作用形成Fe(Ⅲ)-XG配合物,Fe(Ⅲ)-XG在石英和赤铁矿表面吸附方式不同,因而在两种矿物表面吸附量不同。Fe(Ⅲ)-XG中的羟基氧和赤铁矿表面的铁元素发生化学键合特异性吸附在赤铁矿表面,而在石英表面只有微弱的氢键吸附。通过FeCl_(3)·6H_(2)O与黄原胶配位组装可显著提升微细粒赤铁矿选择性絮凝分离效果,为赤铁矿选择性絮凝分选提供新的策略和理论指导。

羟胺强化Fe(Ⅲ)-NTA络合物活化过二硫酸盐降解磺胺甲恶唑

针对Fe(Ⅱ)/过二硫酸盐(Peroxydisulfate,PDS)高级氧化技术存在的pH值应用范围窄、铁泥产量大等缺陷,研究构建Fe(Ⅲ)-氨三乙酸(Nitrilotriacetic Acid,NTA)/羟胺(Hydroxylamine,HAm)/PDS体系,以在中性条件下高效降解水中新污染物磺胺甲恶唑(Sulfamethoxazole,SMX)。研究结果显示,Fe(Ⅲ)-NTA/HAm/PDS体系在pH=7条件下对SMX的降解率可达91%,该体系降解SMX的主要活性物种为·SO_(4)^(-)和·OH。SMX在Fe(Ⅲ)-NTA/HAm/PDS体系中的降解效率随溶液pH值的升高而降低,且增加Fe(Ⅲ)、PDS的用量会加速SMX降解。NTA的引入可将Fe(Ⅱ)/PDS体系的pH值应用范围由酸性拓展至弱碱性,与此同时,向体系内加入HAm可有效减少铁泥的产量。根据检测到的降解产物,提出SMX在Fe(Ⅲ)-NTA/HAm/PDS体系中可能的降解途径包括断键反应、羟基化反应、氨基氧化反应。双酚AF、双氯芬酸、土霉素等其他新污染物也能在Fe(Ⅲ)-NTA/HAm/PDS体系中被高效去除,表明该体系在新污染物的降解领域有较大的应用潜力。

Fe(Ⅲ)/2,6-吡啶二羧酸活化高碘酸盐强化染料脱色的效能与机制

有色染料是环境中非常重要的污染源之一,严重威胁着水生生态环境和人类健康。由于其难以被天然降解,且传统的污水处理工艺亦无法实现其高效去除,因此急需开发绿色、高效的水处理工艺进行有色染料污染控制。发现Fe(Ⅲ)/2,6-吡啶二羧酸(2,6-PDA)可高效活化高碘酸盐(PI)实现亚甲基蓝(MB)这一典型染料的高效降解。实验结果表明,该体系在Fe(Ⅲ)浓度为10μmol/L、2,6-PDA浓度为10μmol/L和PI浓度为200μmol/L时,可在pH 3.0条件下使5 mg/L MB降解率在120 s内大于97%。该方法依托高级氧化原理和配位强化策略,利用PI对有色染料进行降解,为目前染料废水治理提供了新思路从而有效地修复了污染水体。

基于半胱氨酸-Fe(Ⅲ)-邻菲啰啉体系的共振光散射光谱法测定半胱氨酸的含量

半胱氨酸是一种含有巯基的非必需氨基酸,参与体内多种氧化还原反应,在人体生理过程中发挥着至关重要的作用,它在人体内的浓度水平与多种疾病相关[1-2]。半胱氨酸在食品、制药、化妆品中的应用十分广泛[3],因此建立省时、高效的检测半胱氨酸的方法对于相关产品的质量控制具有重要意义。

Investigation of Performances and Mechanism of Fluoride Removal by Fe(Ⅲ)-Loaded Ligand Exchange Cotton Cellulose Adsorbent

Novel adsorbent, Fe（Ⅲ）-loaded ligand exchange cotton cellulose adsorbent [Fe（Ⅲ） LECCA], was used to in vestigate the adsorption performances and mechanism of fluoride removal from aqueous solutions. The adsorbent was found to adsorb fluoride rapidly and effectively. The fluoride removal was influenced by pH. Adsorption mode followed first-order reaction at different temperature, theapparent adsorption activated energy Ea was 6.37 kJ·mol^-1, and adsorption enthalpy △H was 5.35 kJ·mol^-1. The adsorption enfluoride on adsorbent was 3.2 mmol·g^-1 （dry weight）. The maximal integer coordination ratio of fluoride with Fe（Ⅲ） LECCA was 3：1. The ligand exchange mechanism of adsorption was elucidated through chemical methods and IR spectral analysis.

Adsorptive removal of tetracycline from water using Fe(Ⅲ)-functionalized carbonized humic acid

Humic acid(HA)was carbonized at 300,400 and 500℃ and then functionalized with 1 wt%–12 wt%Fe(Ⅲ)respectively[CHA300/400/500-Fe(Ⅲ)].Adsorption of such Fe(III)-functionalized carbonized HA as adsorbents to aqueous tetracycline(TC:25 mg·L^-1)was studied.The adsorption equilibrium time for CHA400-Fe(Ⅲ)to TC was 6 h faster and the adsorption removal efficiency(Re)was two times higher than that of HA/CHA.The adsorption Reof CHA400-Fe(Ⅲ)loaded 10%iron[CHA400-(10%)Fe(Ⅲ)]to TC could reach 99.8%at 8 h and still kept80.6%after 8 cycles.The adsorption kinetics were well fitted to the pseudo-second-order equation and the adsorption isotherms could be well delineated via Langmuir equations(R^2N 0.99),indicating that the homogeneous chemical adsorption of TC occurred on the adsorbents.The main adsorption mechanisms of TC were complexation Fe(III)and hydrophobic distribution.Electropositive and electronegative repulsion between TC and CHA400-(10%)Fe(Ⅲ)at lowly p H(2)and highly p H(8–10)respectively,leaded to the relatively low adsorption capacity and more notable influence of ion concentration.When the p H was between 4 and 8,TC mainly existed in neutral molecules(TCH2),so the influence of ion concentration was not obvious.The dynamic adsorption results showed that the CHA400-(10%)Fe(Ⅲ)could continuously treat about 2.4 L TC(27 mg·L^-1)wastewater with the effluent concentration as low as 0.068 mg·L^-1.Our study suggested a broad application prospect of a new,effective,lowcost and environment-friendly adsorbent CHA400-(10%)Fe(Ⅲ)for treatment of low-concentration TC polluted wastewater.

基于三氰基铁(Ⅲ)酸盐的Fe^(Ⅲ)_(4)Ni^(Ⅱ)_(2)六核配合物的合成、结构及磁性

利用三氰基铁酸盐(Bu_(4)N)[FeⅢ(Tp)(CN)_(3)](Tp=氢化三(1-吡唑基)硼酸)与配体2,9-二吡唑基-1,10-菲咯啉(dpzpen)以及高氯酸镍反应合成了一例氰根桥联的Fe^(Ⅲ)_(4)Ni^(Ⅱ)_(2)六核配合物[Fe_(4)Ni_(2)(Tp)_(4)(CN)_(12)(dpzpen)_(2)]·12H_(2)O·3CH_(3)OH (1)。结构研究表明配合物1具有近似菱形的Fe^(Ⅲ)_(2)Ni^(Ⅱ)_(2)骨架结构,另外2个Fe则通过氰根延伸在菱形的外侧。磁性研究表明在配合物1中氰根桥联的Fe和Ni表现出铁磁相互作用。更为重要的是,基于配合物1的结构模型,对它的变温磁化率数据进行拟合得到了不同Fe-Ni之间的磁耦合常数,得到的最佳磁耦合常数J3d(15.73 cm^(-1))>J2d(3.53 cm^(-1))≈J1d(3.50 cm^(-1))与Ni-N键的键长以及Ni-N≡C键角的变化趋势有关(J3d:0.206 5 nm,169.8°;J2d:0.206 2 nm,163.1°;J1d:0.198 7 nm,161.6°)。以上结果表明Ni-N键长越短,Ni-N≡C键角越大,Fe与Ni之间的铁磁耦合越强。

基于Fe(Ⅲ)和邻苯二胺显色反应快速检测硫化物

比较了不同金属离子(Fe^(2+)、Fe^(3+)、Cu^(2+)、Zn^(2+)、Al^(3+)、Na^(+)、Ca^(2+)、Mg^(2+)、K^(+)、Ag^(+)、Cr^(3+))对邻苯二胺(OPD)的氧化能力,基于Fe^(3+)能直接氧化OPD产生黄色发荧光的产物而构建了Fe^(3+)-OPD显色体系。结合硫化物的还原性以及对金属离子较强的亲和性,开发了一种通过比色法选择性检测硫化物的方法。结果表明,在pH 4.0NaAc-HAc缓冲液中,Fe^(3+)-OPD显色体系的吸光度和荧光强度与NaHS的浓度分别在10~200μmol/L和5~150μmol/L范围内呈线性关系,荧光法的检出限可达0.1μmol/L,体系内其他还原性物质及硫醇对NaHS的检测无干扰。将Fe^(3+)-OPD显色体系结合纸芯片构建的纸基比色体系蓝色分析色道值(B值)与NaHS的浓度在20~150μmol/L范围内呈线性关系,检出限为2μmol/L,并可用于定量检测加标自来水和胎牛血清中的硫化物。

锌精矿氧压酸浸过程Fe(Ⅲ)助浸及水解沉淀行为

针对锌精矿氧压酸浸过程受多相传质影响导致氧化能力不足的问题,本文利用锌浸出渣中可溶性Fe(Ⅲ)的强氧化性促进锌精矿中低价硫化物的高效溶解,同时实现铁酸锌、金属硫化物的强化解离和铁的清洁分离。结果表明:锌浸出渣中铁酸锌溶解产生的Fe(Ⅲ)可以提高体系氧化还原电位,强化锌精矿浸出;以添加锌浸出渣形式向系统补充6.1g/L Fe(Ⅲ)后,锌浸出率由87.59%升高到98.82%;升高反应温度、提高氧分压将有助于提升Fe(Ⅲ)、Fe(Ⅱ)的氧化还原反应能力,同时促进锌的高效浸出和Fe(Ⅲ)的矿物化沉淀;提高酸度可以加快锌精矿的溶解速率,但酸度过高将抑制Fe(Ⅲ)矿物化水解沉淀。在初始Fe(Ⅲ)为6.1 g/L、初始酸度95 g/L、反应温度160℃、氧分压0.8 MPa、液固比6 mL∶1 g、搅拌转速800 r/min、反应时间120min的优化技术条件下,锌浸出率为98.82%,同时溶液中92.36%的铁以铁矾的形式沉淀入渣,浸出终渣含黄钾铁矾40.2%、铅铁矾14.6%;浸出液含铁低至1.04 g/L。

Fe(Ⅲ)表面印迹硅胶聚合物的制备及其吸附性能研究

选用硅胶为基质材料、乙烯基膦酸为功能单体、Fe^(3+)为模板离子、乙二醇双甲基丙烯酸酯为交联剂,通过表面印迹技术制备了一种新型膦酸功能化的Fe(Ⅲ)印迹硅胶聚合物。对印迹吸附材料的吸附条件、吸附选择性和重复利用率进行了研究。通过FT-IR、SEM、EDX、TG和N_(2)吸附/脱附分析对印迹材料进行了表征,分析了印迹吸附剂对Fe^(3+)的吸附机理。结果表明:印迹吸附剂在8 min可达吸附平衡,最大吸附量达16.12 mg/g,吸附行为符合准二级动力学方程和Langmuir吸附等温式,印迹吸附剂展现出较高的选择性识别能力,与Cr^(3+)、Mn^(2+)和Zn^(2+)相比,对Fe^(3+)的选择性系数k分别为8.9、10.75和12.37。经过6次吸附-解吸试验,印迹材料吸附Fe^(3+)的能力仅下降了5.9%,证明其具有很好的可重复使用性能。

基于TA-Fe^(Ⅲ)还原Ag离子构建木材疏水表面

本研究用一种简单、通用、快速的化学表面改性方法对木材进行疏水改性,制备的木材试件具有优异的疏水性能,具有拓展低值人工林木材应用范围的潜在能力。利用单宁酸(TA)与三价铁离子(FeⅢ)配位形成的TA-FeШ复合涂层的粘附性以及TA中游离邻苯二酚/邻苯三酚良好的还原能力,将金属Ag离子原位还原为Ag纳米颗粒,在木材表面构建良好的粗糙度;随后,在复合涂层上接枝疏水长链,从而制备出疏水型木材。结果表明,随着自组装次数的增加以及还原的Ag纳米颗粒在木材复合涂层的沉积,使得木材表面的粗糙结构得到了适度的发展。未改性木材表面的接触角为52.0°,随着接触时间延长,接触角迅速下降,水滴很快渗入到木材中;而经过改性处理的木材,随着自组装次数的增加,TA-Fe^(Ⅲ)/木材试件的接触角从138.2°增加至近143.7°;TA-Fe^(Ⅲ)/Ag/木材试件的接触角从142.3°增加到了146.7°,使木材具有了优异的疏水性能。在强酸、强碱、有机溶剂、超声波清洗和紫外线老化等恶劣条件下,疏水木材接触角均高于135.0°,制备出的疏水木材表现出了优异的环境稳定性和化学耐久性。

Fe(Ⅱ)对CANON工艺处理城镇污水脱氮性能的影响

全程自养脱氮(CANON)工艺,作为新型脱氮工艺应用于城镇污水深度脱氮过程中,有望降低污水处理的运行费用。考察了亚铁离子[Fe(Ⅱ)]对CANON工艺启动及稳定运行时脱氮性能的影响。结果表明:15~23℃条件下投加6.3 mg/L Fe(Ⅱ)时,可有效启动并稳定运行CANON工艺处理城镇污水,该工艺氮去除负荷(NRR)、总氮去除率(TNRE)和氨氮去除率(ARE)分别为(4.8±1.1)g-N/(L^(3)·d)、(97±1)%和(44.2±9.3)%;相关性分析表明,通过调控Fe(Ⅱ)投加量可有效抑制亚硝酸盐氧化菌(NOB)的活性;本次优化的Fe(Ⅱ)投加量为6.3 mg/L,其对CANON工艺脱氮性能的影响机制与CANON工艺中功能微生物活性的提高、Fe(Ⅱ)与进水氨氮及其他氮化合物的循环反应、铁型反硝化过程以及铁型厌氧氨氧化过程的耦合有关。

High Efficient Removal of Trace Molybdenum from Water by FeCl_3:Effects of p H and Affecting Factors in the Presence of Co-existing Background Constituents

The effect of FeCl_3 coagulation-filtration on the removal of trace Mo(Ⅵ) from water is investigated in the p H range of 4. 00 to 9. 00 and the effects of sulfate,silicate,phosphate and humic acid( HA) on the process were determined. Overall,the removal of Mo(Ⅵ) is determined by two factors: the content of Fe intercepted from water( Intercepted Fe) and the affinity between Mo(Ⅵ)( or co-existing background constituents) and adsorption sites. At low p H,where the agglomeration of the iron flocs is limited,the former factor is dominant,so the methods that can promote the agglomeration of the iron flocs,such as increasing the p H,adding co-existing constituents( sulfate,phosphate or HA),can increase the removal of Mo(Ⅵ). While at high p H,the second factor dominated. Increasing the p H weakens the affinity between Mo(Ⅵ) and the iron flocs,and co-existing background constituents( sulfate,phosphate,silicate or HA) compete with Mo(Ⅵ) for adsorption sites,both effects result in a decrease in Mo(Ⅵ) removal. The Mo(Ⅵ) removal efficiency of FeCl_3 in natural water decreases as the p H increases from 4. 00 to 9. 00,and it is better to operate the coagulation process at p H 5.00 in the practical water treatment engineering.

Improvement of a Mesh-Type Cu/Ni/γ-Al2O3/Al Catalyst for Steam Reforming of Dimethyl Ether by Metal (Fe, Zn or La) Addition for CO in Situ Removal

A mesh-type structured anodic alumina supported Cu/Ni bi-functional catalyst was developed for steam reforming of dimethyl ether (SRD). It was found that the Cu/Ni/γ-Al2O3/Al catalyst had remarkable catalytic activity and stability, but a high CO selectivity. Therefore, a multi-functional catalyst was proposed by metals (Fe, Zn, or La) addition to inhibit CO formation during the SRD process. The results show that promoter Fe can improve the Cu dispersion and decrease the reduction temperature of catalyst, and CO selectivity was minimized from 27% to around 3%. However, the addition of Zn and La only can decrease the CO selectivity to 12%. Furthermore, there was an excellent synergetic effect between Cu/Ni/γ-Al2O3 and Fe over the Cu/Ni/Fe/γ-Al2O3/Al catalyst by evaluating catalytic performance of catalysts with different packing structures. And the synergetic mechanism of the active components (γ-Al2O3, Cu or Cu2O, and Fe3O4) for SRD and CO in suit removal was proposed. Finally, a 400-h durability test was carried out and the results show that the Cu/Ni/Fe/γ-Al2O3/Al catalyst had an excellent stability with a 100% DME conversion and low CO selectivity.

Removal of Chromium(Ⅲ) from Monoammonium Phosphate Solutions by a Porous Adsorbent of Fluor(calcium silicate) Composites

The products of monoammonium phosphate containing Cr^3+resulted in disqualification,and further posed a serious threat to ecological environment and human beings.Herein,the porous adsorbent of fluor(calcium silicate)composites(FCSc)was prepared by hydrothermal method using diatomaceous earth,hydrated lime and additive(NaF)as raw materials,which was characterized and used for the removal of Cr^3+from monoammonium phosphate solutions.The effects of different parameters,such as solution pH,initial Cr^3+concentration,temperature and contact time on the adsorption of Cr^3+onto FCSc were investigated in details.The results indicated that the adsorption process was in agreement with the pseudo-second-order kinetic model and Freundlich isotherm.The spontaneous and endothermic nature of the adsorption process was obtained by analyzing various thermodynamic parameters(△G0,△H0,and△S0).In addition,computational monte carlo simulations between Cr3+ions and FCSc were conducted to elucidate the adsorption mechanism.Such kind of porous adsorbent provided a potential application in the removal of impurities from monoammonium phosphate industry.

Removal of Cr(Ⅲ) and Cr(Ⅵ) from aqueous solution by adsorption on sugarcane pulp residue

Sugarcane pulp residue (SPR), a waste from sugar-refinery, which possesses a large surface area, can be used for removing chromium (Cr(Ⅲ) and Cr(Ⅵ)) from wastewater. In this work, the kinetics, isotherms of Cr(Ⅲ) and Cr(Ⅵ) adsorption and their removal by SPR were investigated. The results show that the removal percentages of Cr(Ⅵ) and Cr(Ⅲ) increase with increasing SPR dosage and temperature and decrease with increasing SPR particle size and the initial concentration of chromium ions. However, the influence of pH value on the Cr( Ⅵ) removal differs from that of the Cr( Ⅲ) removal. The Cr(Ⅵ) removal percentage decreases with increasing pH values, while the Cr(Ⅲ) removal percentage increases with increasing pH value. The adsorption kinetics of Cr(Ⅵ) and Cr(Ⅲ) well fits with pseudo-second-order model. Langmuir adsorption isotherm can well describe the adsorption phenomena of chromium ions with the maximum adsorption capacity of 0.567 mg/g for Cr( Ⅵ) and 3.446 mg/g for Cr( Ⅲ) . Moreover, SPR reveals higher adsorption capacity for Cr(Ⅲ) than that for Cr(Ⅵ), which implies that SPR has more potential application for Cr(III)-containing wastewater treatment than that for Cr(Ⅵ)-containing wastewater treatment.

Integrated ozone–photo–Fenton process for the removal of pollutant from industrial wastewater

The use of hybrid advanced oxidation processes(AOPs) for the removal of pollutants from industrial effluents has been extensively studied in recent literature. The aim of this study is to compare the performance of the photo,Fenton, photo-Fenton and ozone–photo–Fenton processes in terms of color removal and chemical oxygen demand(COD) removal of distillery industrial effluent together with the associated electrical energy per order. It was observed from the experimental results that the O_3/UV/Fe^(2 +)/H_2O_2 process yielded a 100% color and95.50% COD removals with electrical energy per order of 0.015 k W·h·m^(-3) compared to all other combinations of the AOPs. The effects of various operating parameters such as H_2O_2 and Fe^(2+) concentration, effluent pH, COD concentration and UV power on the removal of color, COD and electrical energy per order for the ozone–photo–Fenton process was critically studied and reported. The color and COD removals were analyzed using a UV/Vis spectrometer and closed reflux method.

Cr(Ⅲ) removal from simulated solution using hydrous magnesium oxide coated fly ash： Optimization by response surface methodology (RSM)

Hydrous magnesium oxide coated fly ash(MFA) has environmental remediation potential by providing a substrate for the adsorption of aqueous Cr(Ⅲ). Aqueous Cr(Ⅲ) adsorption onto MFA was examined as a function of MFA dosage, p H and initial Cr(Ⅲ) concentration with the Box–Behnken approach used for experimental design and optimization using response surface methodology(RSM). p H and dosage(dosage and concentration) have significant interactive effects on Cr(Ⅲ) adsorption efficiency. Analysis of variance shows that the response surface quadratic model is highly significant and can effectively predict the experimental outcomes. Cr(Ⅲ) removal efficiency of 98% was obtained using optimized conditions of MFA dosage, p H and initial Cr(Ⅲ) concentration of 1.57 g·L^(-1), 4.11 and 126 mg·L^(-1), respectively. Cr(Ⅲ) adsorption onto MFA is mainly attributed to the interaction between Cr(Ⅲ) and the functional group \\OH of the hydrous magnesium oxide, in all probability caused by chemisorptions. The results of this study can conduce to reveal the interactions between Cr(Ⅲ) pollutant and MFA characteristics, posing important implications for the cost-effective alternative adsorption technology in the treatment of heavy metal containing wastewater.

基于六偏磷酸钠-Fe^(2+)的铁盐脱氮反应器运行性能及微生物学特征研究

以实验室高效反硝化反应器中的反硝化污泥作为接种污泥,启动自养型六偏磷酸钠-Fe^(2+)脱氮反应器,试验采用模拟废水通过88 d的不间断运行,研究了铁盐脱氮工艺的脱氮效能及其微生物学特性。结果表明,当反应器硝态氮容积负荷为0.42 kg/(m^(3)·d)时,最高稳定氮去除负荷为0.41 kg/(m^(3)·d);当Fe^(2+)容积负荷为4.92 kg/(m^(3)·d)时,最大铁去除负荷为2.77 kg/(m^(3)·d)。反应器稳定运行时硝态氮、Fe^(2+)的去除率分别达94.6%、52.6%,最佳效能可维持28 d。反应器运行到第82天时,颗粒污泥由黄色变为灰褐色,颗粒解体,污泥比活性逐渐升高,比反硝化活性由0.71 mg[N]/(g[VSS]·h)升高到2.3 mg[N]/(g[VSS]·h),同比上升224%;比铁氧化活性由7.3 mg[Fe]/(g[VSS]·h)升高到15 mg[Fe]/(g[VSS]·h),同比上升105%。六偏磷酸钠-Fe^(2+)脱氮作为一种新型自养反硝化技术,不仅增强了活细菌的生物活性和反硝化活性,还延长了铁盐脱氮污泥反硝化的高效期。